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NASA Contractor Report 185129
Users Manual for the NASA LewisIce Accretion Prediction
Code (LEWICE)
Gary A. Ruff and Brian M. Berkowitz
Sverdrup Technology, Inc.Lewis Research Center Group
Brook Park, Ohio
May 1990
Prepared forLewis Research Center
Under Contract NAS3-25266
National Aeronautics andSpace Administration
( NA?;A-C"-'- ! _:_5.L2 _ )
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TABLE OF CONTENTS
LIST OF SYMBOLS
PAGE
V
SUMMARY viii
1.0 BACKGROUND
2.0 INTRODUCTION
I
3
3.0 DISCUSSION OF THE ICE ACCRETION PROCESS
3.1 Ice Accretion Characteristics
3.2 Description of the Physical Model
6
6
7
4.0 METHODOLOGY
4.1 Calculation of the Flow Field
4.2 Calculation of the Droplet Impingement Characteristics
4.3 Calculation of the Thermodynamic Characteristics
4.4 Calculation of the Iced Geometry
4.5 General Computational Procedure
11
11
12
22
25
27
5.0
6.0
LEWICE INPUT
5.1 Input Format
5.2 User's Guide to Input Format
5.3 Interactive Input
LEWICE OUTPUT
6.1 Printed Output
6.2 Graphical Output
38
38
46
54
62
62
68
7.0 EXAMPLE CASES 88
7.1 Example 1: Glaze Icing on a NACA 0012 Airfoil, a = 0.0 ° 88
7.2 Example 2: Glaze Icing on a NACA 0012 Airfoil, a = 4.0 o 91
7.3 Example 3: Glaze Icing on a NACA 0012 Airfoil, a = 0.0 ° 96
7.4Example 4: Specification of a Droplet Size Distribution
7.5 Example 5: Thermal Anti-icing
8.0 PROGRAMMING AIDS
8.1 Description of Subroutines
8.2 Diagnostic and Error Messages
8.3 Potential Flow Calculations
8.4 Particle Trajectory Calculations
8.5 Thermodynamic and Ice Accretion Calculations
8.6 COMMON Blocks and Work Files
8.7 Size of the Code
8.8 Execution Times
8.9 Getting LEWICE Operational
LIST OF REFERENCES
APPENDICES
A. Derivation of the Icing Energy Equation
B. Integral Boundary Layer Method on an Iced Surface
C. Flow Field Corrections
D. Complete Input to the Potential Flow Code ($24Y)
E. Calculation of the Local Edge Velocities
F. Empirical Relationship for the Equivalent Sand-Grain
Roughness Height
97
100
146
146
146
146
147
148
149
149
157
157
158
160
171
188
204
216
220
ii
ACKNOWLEDGEMENTS
The development of LEWICE leading to the publication of this user
manual has involved many researchers, each of whom made improvements
to the code and/or comparisons with experimental data. All of these efforts
contributed to the version of LEWICE described in this manual. Special
recognition should go to Dr. Robert J. Shaw of NASA Lewis Research
Center and Dr. James T. Riley of the Federal Aviation Administration
Technical Center for providing funding over the years, and for their constant
support of the project.
Below is the list of people who have contributed to the development
of the current version of LEWICE. My apologies to any who, through my
negligence and ignorance, have been excluded from the list.
University of Dayton Research Institute
Charles D. MacArthur
Patrick A. Haines
John L. Keller
Dr. William Hankey
NASA Lewis Research Center
James E. Newton
Nicola M. Juhaz
John M. Prather
Loretta A. Austin
Denise Deems
Sverdrup TechnologT_. Inc.
Susan Zeleznik
Angela Quealy
*****************************************************************
* By participating in the generation of the computer codes or other *
* test data reported herein, NASA makes no assurances that said *
* code or other data is complete, accurate, or sufficient for purposes *
* of assuring safety of operation of aircraft. ******************************************************************
iii
List Of Symbols
A
At
At
AB
C
Cd
cl
el
Cm
Cp
C!CVF
d_
d_
D
E=
f
FRL
gH
h,
i
L,k°
L
L!
L_
LWC
M
m
tT_H
r_
r_ u
rt i
Characteristic area
Accumulation parameter
Modified accumulation parameter
Mass transfer driving potential
Characteristic length
Drag coefficient
Skin friction coefficient
Lift coefficient
pitching moment coefficient
Pressure coefficient, also specific heat, J/kg
Cunningham correction factor
Control volume fraction
Ice thickness, m
Mass median droplet diameter,/zm
Drag force, N
Total collection efficiency
Freezing fraction
Flight reference line
Mass transfer coefficient, kg-K/J
Projected height, m
Convective heat transfer coefficient, W/m2/K
Enthalpy, J/kg
Moment of inertia relative to z axis
Equivalent sand-grain roughness, m
Lift force, N
Heat of fusion, J/kg
Heat of vaporization, J/kg
Liquid water content, g/m 3
Much number; moment of aerodynamic forces
Mass, kg
Mass per unit area, kg/m 2
Mass flow rate, kg/sec
Mass flux, kg/rn _ /sec
Mass fraction of liquid water for droplet diameter i
PRECEDING PAGE BLANK NOT FILMED
N
P
Pr
qc
qk
Tc
Re
Rek
Re_
S
Sc
St
Stk
T
t
At
V
v:vkX
y
/t0
V
P
E
6
Subscripts
a
&w
c
d
Number of droplet sizes defining a droplet distribution
Number of points describing geometry
Pressure, Pa
Prandtl number
Convective heat flux, W/rn _
Conductive heat flux, W/rn 2
Recovery factor
Freestream Reynolds number
Laminar/turbulent transition Reynolds number
Droplet Reynolds number based on V_
Surface length, m; surface length increment, m
Schmidt number
Stanton number
Roughness Stanton number
Temperature, °K
Icing time, sec
Icing time increment, sec
Velocity, m/8
Volume fraction of LWC
Velocity at y : ko, rn/s
x-coordinate
y-coordinate
Angle of attack, degrees
Local collection efficiency
Pitch angle, degrees; momenteum thickness, m
Viscosity, N s / rn 2
Density, g/m s
Shear stress, N/rn 2
Particle trajectory convergence criteria
Boundary layer thickness, m
Thermal conductivity of air, W/rn _o K
Air
Adiabatic wall
Critical; convection
Droplet
vi
e
i
(i)(i-I)1
L
Pr
Fin
7"ou t
S
sur
T
t
tr
U
t_
W
X
y
0
O0
G
Superscripts
Evaporation; condition at the edge of the boundary layer
Ice
Control volume
Preceding control volume
Lower surface; laminar
Local condition; condition at the edge of the boundary layer
Particle
Runback water
Runback into control volume
Runback out of control volume
Static condition
Surface condition
Total condition
Turbulent
Laminar to turbulent transition
Upper surface
Vapor
Liquid water
Magnitude of the vector in the x-direction
Magnitude of the vector in the y-direction
Initial
Freestream conditions
Shear
Vector quantity
Derivative with respect to time
Non-dimensionalized parameter
vii
SUMMARY
LEWICE is an iceaccretion prediction code that applies a time-stepping
procedure to calculate the shape of an ice accretion. The potential flow field
is calculated in LEWICE using the Douglas Hess-Smith 2-D panel code
($24Y). This potential flow field is then used to calculate the trajectories
of particles and the impingment points on the body. These calculations
are performed to determine the distribution of liquid water impinging on
the body, which then serves as input to the icing thermodynamic code.
The icing thermodynamic model is based on the work of Messinger, but
contains several major modifications and improvements. This model is
used to calculate the ice growth rate at each point on the surface of the
geometry. By specifying an icing time increment, the ice growth rate can
be interpreted as an ice thickness which is added to the body, resulting in
the generation of new coordinates. This procedure is repeated, beginning
with the potential flow calculations, until the desired icing time is reached.
The operation of LEWICE is illustrated through the use of five ex-
amples. These examples are representative of the types of applications
expected for LEWICE. All input and output is discussed, along with many
of the diagnostic messages contained in the code. Several error conditions
that may occur in the code for certain icing conditions are identified, and
a course of action is recommended.
LEWICE has been used to calculate a variety of ice shapes, but should
still be considered a research code. The code should be exercised further to
identify any shortcomings and inadequacies. Any modifications identified
as a result of these cases, or of additional experimental results, should be
incorporated into the model. Using it as a test bed for improvements to
the ice accretion model is one important application of LEWICE.
viii
Chapter 1
BACKGROUND
The evaluation of both commercial and military flight systems in icing
conditions has become important in the design and certification phases
of system development. These systems have been evaluated in flight in
natural icing, in a simulated cloud produced by a leading aircraft, and in
ground test facilities. All icing testing is relatively expensive, and each test
technique, i.e., flight or ground testing, has operational limitations which
limit the range of icing conditions that can be evaluated. It would benefit
the aircraft or flight system manufacturer to be able to analytically predict
the performance of the system for a range of icing conditions.
This first step in the prediction of the performance characteristics is
the determination of the location, size, and shape of the ice that will form.
An analytical ice accretion model would allow the evaluation of a wide
range of proposed test conditions to identify those that will be most critical
to the flight system. This could substantially reduce the amount of test
time required to adequately evaluate a system and increase the quality
and confidence level of the final evaluation. The analytically predicted
ice accretion could also serve as the input to an advanced aerodynamic or
system performance code to allow more complete evaluation in the design
phases of the system. For these reasons, several analytical ice accretion
prediction methods have been developed by various investigators.
The most well-known axe those of Ackley and Templeton 1, Lowzowski 2,
Hankey and Kirchner a, and Cansdale and Gent 4. All apply essentially the
same physical model of the ice accretion process but differ in the manner
that the surface properties, for example, the local collection efficiency and
convective heat transfer coefficient, are calculated and allowed to vary over
the surface. Also, several of these models were restricted to the simulation
of the icing of a cylinder. One of the major inadequacies of these moclels
is that they do not account for any of the time-dependent aspects of the
ice accretion process. In general, the ice accretion rate is calculated as
a function of position on the airfoil and projected at a constant rate to
approximate a finite growth over a prescribed period of time. Therefore,
1
any sensitivity of the ice accretion process to the changing iced airfoil shapeis not included.
The purpose of the current study was to develop a time-dependent, an-
alytical model of the ice accretion process that could be used to predict the
shape of the ice accretion that would form on an arbitrary two-dimensional
geometry when exposed to icing conditions. The development of the com-
puter code (LEWICE) was begun by the University of Dayton Research
Institute (UDRI) under contract to NASA Lewis Research Center. The
results of this study are described in Reference 5. Development of the code
was then continued at the NASA Lewis Research Center under NASA fund-
ing until October 1984 when funding by the Federal Aviation Administra-
tion (FAA) was begun. This document describes the results of the current
development effort and contains the information necessary to apply the ice
accretion prediction method to practical icing problems.
2
Chapter 2
INTRODUCTION
The computer code, LEWICE, embodies an analytical ice accretion model
that evaluates the thermodynamics of the freezing process that occurs when
supercooled droplets impinge on a body. The atmospheric parameters of
temperature, pressure, and velocity, and the meteorological parameters of
liquid water content (LWC), droplet diameter, and relative humidity are
specified and used to determine the shape of the ice accretion. The sur-
face of the clean (uniced) geometry is defined by segments joining a set
of discrete body coordinates (Fig. 2.1). The code consists of three major
modules. They are 1) the flow field calculation, 2) the particle trajectory
and impingement calculation, and 3) the thermodynamic and ice accretion
calculation. Each of these modules will be discussed in detail in following
sections.
LEWICE differs from other ice accretion prediction codes 1-4 because
it applies a time-stepping procedure to "grow" the ice accretion. Initially,
the flow field and droplet impingement characteristics are determined for
the clean geometry. The ice growth rate on each segment defining the
surface is then determined by applying the thermodynamic model. When
a time increment is specified, this growth rate can be interpreted as an ice
thickness and the body coordinates are adjusted to account for the accreted
ice. This procedure is repeated, beginning with the calculation of the flow
field about the iced geometry, then continued until the desired icing time
has been reached. The application of this time-stepping procedure to the
prediction of an ice accretion shape will be discussed in greater detail in
following chapters.
Ice accretion shapes for cylinders and several single-element airfoils have
been calculated using this computer code. The calculated results have been
compared to experimental ice accretion shapes obtained both in flight and
in the Icing Research Tunnel at NASA Lewis Research Center. In general,
the comparisons have been encouraging but inconsistent. Ice shapes for
some conditions are well predicted, while for others there is little similarity
between the predicted accretion and that obtained by experiment. Unfor-
3
tunately, the poorer predictions do not consistently occur in only one type
of icing condition such as glaze or rime icing, on a specific type of airfoil, or
in comparisons with results from a specific facility. There are many possible
explanations for this behavior including inaccurate modeling of the accre-
tion process, occasional errors in setting test conditions, and overextending
the computer code into conditions where the assumptions, such as potential
flow, do not apply. The known limitations will be addressed throughout
this user's manual.
The manual begins with a discussion of the ice accretion process to
identify the requirements of an ice accretion prediction methodology. The
major components of the code and the mathematical models applied in
each are then discussed. The input and output to the code are described,
followed by the presentation of several sample cases, which illustrate various
aspects of the code. The manual concludes with a summary of the current
resultsand shortcomings of the method.
Areas requiring additional development are identifiedand discussed in
the Appendices (A through F).
4
+y'
STAGNATIONPOINT
(S = 0.0)-_,..
NODES/ix.
// | \X\
I I \\I I \I I \
+X
Figure 2.1: Geometry defined by segments joining body coordinates
5
Chapter 3
DICUSSION OF THE ICE ACCRETION PROCESS
The model of the ice accretion process applied in LEWICE is presented in
this chapter, beginning with a discussion of some of the general character-
istics of ice accretion shapes, mad followed by a description of the physical
model of the ice accretion process from which a mathematical model must
be formulated.
3.1 Ice Accretion Characteristics
Before discussing the physical model of the ice accretion process, it is nec-
essary to define some of the terms used in such a discussion.
Ice may form on the forward facing surfaces of an aircraft flying through
clouds composed of supercooled water droplets. The type and shape of ice
that forms are functions of the atmospheric parameters of velocity, pres-
sure, and temperature, and the meteorological parameters of liquid water
content, droplet diameter, and icing time.
Ice shapes are generally classified as glaze, mixed, and rime accretions.
Rime ice is milky white and opaque, and will be denoted in the ice accretion
profiles in this report by shading as shown in Figure 3.1a. Glaze ice is
generally clear and is characterized by the presence of larger protuberances,
commonly known as glaze horns, as shown in Figure 3.1b. A mixed ice
accretion will have some of the characteristics of both glaze and rime ice
accretions. As shown in Figure 3.1c, the center portion of a mixed ice
accretion will have the characteristics of glaze ice accretion. This glaze
center will be surrounded by rime ice accretions, commonly called rime
feathers because of their thin, feather-like shape and delicate structure.
The type of ice that will be formed is dependent on the atmospheric
and meteorological conditions identified in the preceding paragraph. Pre-
dicting the type and shape of the ice accretion that will be formed for a
specified set of icing conditions is difficult because of the complex interac-
tions between the atmospheric and meteorological parameters. Typically,
rime ice is formed at lower temperatures, velocities, and LWC than glaze
6
ice. An example of the transition from glaze to rime ice as the total temper-ature is lowered is shown in Figure 3.2. At the warmest total temperature,
Tr - -2.0C, the accretion is composed exclusively of glaze ice. As the tem-
perature decreases, areas of rime ice begin to form near the impingement
limits. As the temperature decreases further, these rime portions increase
in size until the accretion is composed solely of rime ice. The extent of icing
and the locations at which ice forms on a surface are largely dictated by the
size of the droplets impinging on the surface. For a given icing condition,
and in the absence of ice shedding, the size of the accretion depends on
the length of time ice is allowed to accrete. The general effects of temper-
ature, droplet size, LWC, and angle of attack on ice shapes formed on a
NACA 0012 airfoil in the NASA Lewis Icing Research Tunnel (IRT) are
documented in Reference 6.
3.2 Description of the Physical Model
An understanding of the interactions between these parameters is required
to predict the shape of an ice accretion that will be formed at a specified
set of icing conditions. To develop this fundamental understanding, it is
necessary to examine the physical model of the ice accretion process.
A model of the ice accretion process was first presented by Tribus _ and
developed further by Messinger s. While many studies have been done to
understand various aspects of the ice accretion process, the original physical
model has been applied relatively unchanged. Recent close-up movies and
photographs of the ice accretion process made at the NASA Lewis Research
Center 9 have increased our understanding of the process and indicated that
modifications to the physical model may be necessary. Conclusions drawn
from the observations are included in the following discussion of the ice
accretion process, and differences from the previous model are highlighted.
The ice accretion process is characterized by the presence of supercooled
droplets entrained in the flow about a body. These droplets follow trajecto-
ries that will cause them to either be carried past or impinge upon a body.
Upon impact with a clean surface, the droplets coalesce into larger surface
drops under the effects of surface tension and flow along the surface as dic-
tated by the airflow along the surface of the body. These surface drops will
then either freeze on the surface or be shed from the surface because of the
7
aerodynamic forces on the drop. The ice accretions formed by this initial
freezing form a rough surface which enhances the convective heat transfer
and local collection efficiency of the surface, and therefore allows the ice
accretion process to continue.
The type of ice that will form for a given set of conditions is determined
primarily by the rate at which the freezing process occurs. For example, if
the conditions are such that the droplets freeze rapidly, there is essentially
no initial coalescing and flowing of the droplets. Instead, they freeze on
impact and form the characteristic rime ice a_:cretions. These accretions
are opaque and milky white in color because of the presence of air bubbles
that are trapped in the structure during the rapid freezing process. As the
rate of the freezing process decreases, the droplets begin to coalesce and
flow on the surface. Upon freezing, these larger surface droplets form sur-
face roughness elements which tend to enhance the convective heat transfer
and local collection efficiency characteristics, which, in turn, enhance the
continuing growth of the ice accretion in this region. These local areas
of enhanced ice growth are, therefore, the beginnings of the characteristic
horns found on mixed and glaze ice accretions. As the freezing rate de-
creases further, the drops flow further along the surface of the body before
freezing, thus moving the regions of enhanced ice growth away from the
stagnation point. This, in turn, causes the horns of the accretion to move
further apart and forms the familiar glaze ice accretions. As the rate of the
freezing process decreases, less air is trapped within the ice structure and
the ice gradually becomes clearer until it is essentially transparent, as in
glaze ice.
This description of the ice azcretion process has identified four basic
areas or processes that must be modeled in order to predict the shape of an
ice accretion that will form on a body for a specified set of icing conditions.
These areas are 1) the flow field about the body, 2) the droplet trajectory
and impingement characteristics on the body, 3) the thermodynamics of
the freezing process, and 4) the accumulation of ice on the surface of the
body. To analytically predict a_n ice accretion shape, a mathematical model
of each of these physical processes must be developed. Each of these areas
will be discussed in subsequent sections to identify the methods used in the
ice accretion prediction code, LEWICE.
ICING CONDITIONS
A __.8 C__CYLINDER DI_U_, IN. 1.0 2.0 1.0
PS" P$|A 1_.2 12.2 lq.2
Ts, OF -5.0 21.1 5Vo fps 200 367 qo0aM, p_ _ 20 22 15
LWC, g/_ O. G O. 35 O. 53
X, MZX 8.0 3;0.6 6.8
SHADEDPORTIONSDENOTERIMI" ICE\
\\
a. Rime ice accretion, f : 1.0
GLAZE HORNS
b. Glaze ice accretion, f = 0.15
RIME FEATHERS-._
c. Mixed ice accretion, f = 0.53
Figure 3.1: Examples of ice accretions formed at various atmospheric and
meteorological conditions
9
OR1GINA[ PAGE IS
OF POOR QUALITY
,f_ ALLGLAZE ICE
(A) TO(AL TEI'IP_RATUR_L,-2 °C (B) TOTAL Tt-/_°f.RATURE, -8 oc
(MAGNATION FREEZING FRACTION, 0.22). (STAGNATION FREEZING FRACTION, 0.32).
(C) TOTAL TEMPERATURE,-15 °C
(STAGNATION FRE£ZING FRACTION, O.SS).
STREAKS
(D) TOTAL TLPPERATURE, -18 °C
(STAGNATION FREEZING FRACTION, 0.55).
(E) TOTAL TIE/_RATURIE, -20 °C
(STAIglATIOR FREEZIII6 FRACTION,
WHITE RI/'_
ICE IS OPAQUE:BLACKMIEN
BACKLIGHTED
ALL
RIPE
(F) TOTAL TEMPE,RATURE, -26 °C
(STAGNATION FRE£Z|NG FRACTION, 0.9).
Figure 3.2: Effect of temperature on the ice accretion shape. Thin ice
samples removed from the airfoil and backlighted; Airspeed, 20gkm/hr;
LWC, 1.3g/mS; DVM, 20m; Time, 8rain; Airfoil, 0.53m chord 0012 airfoil
at 4 ° angle.
10
Chapter 4
METHODOLOGY
The phenomena that make up the ice accretion process have been identified
and now must be investigated in order to accurately predict the shape of
an ice accretion that will form on a body. These include the evaluation of
1) the flow field about the body,
2) the droplet trajectory and impingement characteristics,
3) the thermodynamics of the freezing process, and
4) the accumulation of the ice on the surface.
The computational methodology used to evaluate each of the above areas
is discussed in the following sections.
4.1 Calculation of the Flow Field
The application of a flow field calculation method to an ice accretion pre-
diction code requires that the method not only be able to calculate accurate
flow fields about clean geometries, but also around the irregular, convoluted
ice shapes that occur for many icing conditions. It is also desirable that the
computational time and memory requirements of the method be as small
as possible so that the use of the code is not limited to icing researchers
with large computer facilities.
The Douglas two-dimensional potential flow program developed by Hess
and Smith, described in Reference 10, meets these requirements, and is used
in the present study for calculating the flow field about the body. This pro-
gram uses a distribution of sources, sinks, and/or vortices along the body
surface to calculate the potential flow field. The body surface is represented
by an arbitrary number of straight line segments. In calculating the flow
field, contributions from all the sources, sinks, and/or vortices are summed.
The accuracy of this method was tested by comparing its predicted veloc-
ities and surface pressure coefficients with both analytical solutions and
11
experimental data 1°. Excellent agreement was found. Similar comparisons
were performed at NASA Lewis and compared with pressure coefficient
data found in Reference 11. These comparisons, shown in Figures 4.1a-j,
show that the surface pressure coefficient is well predicted by the poten-
tial flow method for angles of attack up to approximately 11.0 degrees and
Mach numbers up to 0.50. These flow field limitations must be considered
when predicting ice accretion shapes at high Mach numbers or high angles
of attack.
Only limited details of the methodology applied in the potential flow
program are provided in this manual since the purpose of this study was to
develop an analytical ice accretion prediction program. However, sufficient
description of the input as well as subroutines are supplied to allow the user
to become familiar with the primary aspects and limitations of the code.
4.2 Calculation of the Droplet Impingement Characteristics
The algorithm applied in the current ice accretion model to calculate the
droplet trajectory and impingement characteristics was originally developed
by Frost, Chang, Shieh, and Kimble of FWG Associates under contract to
NASA Lewis 12-13.
This code was developed to calculate the trajectories and impingement
characteristics of arbitrarily-shaped particles, and although water droplets
are of primary concern when evaluating the ice accretion process, the gen-
erality has been retained in LEWICE. While much of this code has been
applied in its original form in the current study, there are significant changes
in many areas and, therefore, the current version of the code is discussed
in detail in this report.
4.2.1 Definitions
The primary droplet impingement characteristics that must be evaluated
by an ice accretion prediction code are the regions of droplet impingement
and the distribution of the mass of liquid on the surface of the body within
this impingement region.
The equations of particle motion, to be discussed in the following sec-
tion, are used to calculate droplet trajectories from far upstream to impinge-
12
ment on the body and, if it occurs, the total and local collection efficiencies.
The total collection efficiency is defined as the ratio of the actual mass of
impinging water to the maximum value that would occur if the droplets
followed straight-line trajectories. Figure 4.2 illustrates that this definition
can be given in equation form as
E,,_ = I/o (1)H
where !t0 is the vertical distance between the droplet release points of the
upper and lower surface tangent trajectories. The local collection efficiency,
3, is also defined in Figure 4.2 and can be written in differential form as
dyo
(2)
It is related to the total collection efficiency by the equation
1 i s"= -- _ dsE,,, H
(3)
where s,, and sl are the upper and lower surface impingement limits, respec-
tively. The following sections will cover the methods applied to calculate
the variables discussed above.
4.2.2 Equations of Particle Motion
The motion of a particle is analyzed as a point mass particle that is acted
on by the potential flow field but which itself does not affect the flow.
The forces acting on the particle are considered to be those of lift, drag,
pitching moment, and gravity. Figure 4.3 shows the forces acting on the
particle and the velocity vectors relative to the motion of the particle.
The flight reference line (FRL) is not significant for a spherical particle;
however, for arbitrarily shaped particles, i.e., a snow flake, the FRL must
be defined relative to the lift, drag, and moment coefficient data available.
The equations of motion of an arbitrarily shaped particle are derived from
a force balance on a point mass, as shown in Figure 4.3, and are as follows:
rn_ = -D cos "_ - L sin 7 + rng sin a
mfl = -.D sin "1 + f_,cos "7 - mg cos a (4)
13
where
"_= ta"- 1 _,,- v, (5)_p - V,
In Figure 4.3, note that the coordinate system used in LEWICE is fixed to
the leading edge of the clean airfoil.
For an airfoil at an angle of attack a, the coordinate system is at an
angle to the gravitational coordinate system. Therefore, the effect of gravity
must be accounted for in the equations for both lift and drag.
The flow field velocity components in the x and y directions, i.e., V_
and V_, respectively, are obtained from the potential flow program. The
aerodynamic drag and lift forces are defined as
p, V 2
= Cd_ Ap,_ p.____'vA, (6)
where Ap is a characteristic area of the particle, p_ is the density of air at
the position of the particle, and V is the particle velocity relative to the
flow field and defined as
V = V'(_, - vz)' + (0,- v,)' (7)
For arbitrarily shaped particles, the pitch angle, 0p, is required to eval-
uate the angle of attack ap, using the following equation
,,,,,= o,,- ,_ (8)
This motion is governed by the following equation
MI. (o)
where Iu is the moment of inertia of mass relative to the z axis. The
moment of aerodynamic forces acting on the particle is
p, V _
M = c,,_---_ Apdj, (10)
14
where c,_ is the pitching moment coefficient which must also be specified
by the user.
The lift, drag, and pitching moment coefficients, cl, Cd, and c,_ respec-
tively, must be provided by the user for arbitrarily shaped particles. The
coefficient data is input to the program through subroutine COEFF and
should be functions of the particle angle of attack, as defined by Equation
8, and the particle Reynolds number based on the particle diameter, given
by the following equations:V dp
R,, - (11)/2
The diameter of the particle, d, and the kinematic viscosity of air, u, are
assumed constant along the trajectory of the particle.
Since water droplets are usually assumed to be rigid spheres in icing
studies, the only forces considered to be acting on the particle are those of
drag and gravity. The governing equations can therefore be simplified as
follows:
m_c = -D co8 "7 + rng sin a
= -5 si."7 - mg (12)
In this case, the drag force, D, is determined using a steady-state drag
coefficient for a sphere which is a function of the droplet Reynolds number,
Rep. Approximating droplets as rigid spheres is valid for drop radii less
than 500.0 microns 14. A valid drag law for spherical particles is built into
the computer program in subroutine COEFF.
For particles with diameters of less than 10 microns, the ratio of particlediameter to the mean distance between air molecules is small enough so that
molecular slip phenomena result in drag forces lower than those calculated
by the drag law used in LEWICE. The Cunningham correction factor, C/,
Reference 15, is therefore applied to correct the drag coefficient using the
following equation:Cd
cdJslip = -_I (13)
The values of C! are input by the user when necessary and are given in
Table 4.1. As shown in Table 4.1, this effect is small for particles with
diameters greater than 1.0 micron. Droplets this small would be included
15
Table 4.1: Cunningham Correction Factor for Standard Air
d(u) C d(u) C
0.001 221.600 0.1 2.911
0.002 111.100 0.2 1.890
0.003 74.250 0.3 1.574
0.004 55.830 0.4 1.424
0.005 44.780 0.5 1.337
0.006 37.410 0.6 1.280
0.007 32.150 0.7 1.240
0.008 28.200 0.8 1.210
0.009 25.140 0.9 1.186
0.010 22.680 1.0 1.168
0.020 11.650 2.0 1.084
0.030 7.978 3.0 1.056
0.040 6.151 4.0 1.042
0.050 5.060 5.0 1.034
0.060 4.337 6.0 1.028
0.070 3.823 7.0 1.024
0.080 3.441 8.0 1.021
0.090 3.145 9.0 1.019
10.0 1.017
in an ice accretion prediction only in exceptional circumstances, such as
testing the limiting capabilities of an ice accretion code.
4.2.3 Method of Integration
The equations governing the motion of arbitrarily-shaped particles are asfollows:
dx dy 0 0 (14a - c)= d-7 = d-7 = dgi
-- cosT--- sinT+gsinadt m m
16
- -- sin_+-- cos_-gcos adt m m
dO M
dt I_
(14d- f)
For spherical water droplets, Equations 14c and 14f are not applicable
and Equations 14d and 14e are simplified to result in the following four
equations:
dx
dt
dy
- cos "7 + g sindt m
-- = --- sin "7-g sindt m
(15)
These equations are integrated using the method of Gear developed for stiff
equations 16-17. The details of the subroutines that make up the integration
method, i.e., DIFSUB, DECOMP, SOLVE, and PEDERV, can be found in
Reference 16 and in COMMENT statements in the computer code. The
integration routine also requires that the equations to be integrated be
located in a subroutine named DIFFUN. This subroutine currently contains
Equations 14- 15.
4.2.4 Determination of Droplet Impingement
The calculation of the droplet trajectories is continued until the droplets
impinge upon the body or move out of range. This section describes the
procedure used to determine whether or not a droplet impacts the body
and, if so, the location of impingement. These calculations are controlled
by subroutine MODE.
17
As previously discussed, the geometry is defined by segments joining a
discrete set of body coordinates as shown in Figure 2.1. A droplet is con-
sidered to impact the body when its trajectory intersects one of these body
segments. The current model does not take account of grazing collisions
or droplets that may impact the body so that they are re-introduced into
the flow by bouncing, splashing, etc. The impact algorithm, found in sub-
routine INTRST, sequentially sums the angles between lines drawn from
the particle position to adjacent points describing the closed curve of the
geometry, as shown in Figure 4.4. The summation starts with the angle
between lines drawn to the first and second points, continuing with the
angle between the lines to the second and third points, and so on, all the
way to the angle between lines drawn to the next to last and last points.
If the particle is outside the body, the sum of these angles will always be
zero. If the particle has crossed one of the body segments and lies inside
the body, the sum of the angles is 21r. If the particle lies directly on one of
the body segments, the summed angle will equal It.
A particle trajectory is calculated until the summed angles total 7r or 27r,
which indicates that the particle has impinged upon the body, or until the
particle passes outside of the pre-specified boundaries. The impact point
results from the intersection of the particle trajectory and the line con-
necting the adjacent ice shape points through which the particle trajectory
passed (Figure 4.5). The particular line segment through which the particle
passed is determined by first calculating the intersection of the line joining
the present and previous particle positions and the line formed by each of
the adjacent points that describe the body geometry, as shown in Figure
4.5. If the particle passed through a particular segment, the distance from
the intersection (impingement) point to the endpoints of the segments will
be less than the length of either the trajectory or body segments. Once the
body segment through which the particle passed and the intersection (im-
pingement) point have been determined, the surface distance, s, from the
stagnation point to the impingement point is determined by interpolation.
4.2.5 Calculation of the Local Collection Efficiency
The particle trajectories and impingement points, calculated as previously
described, are used to establish the relations between the particle's initial
position (x0, Y0) and the position where it impinges on the body surface,
18
specified by the surface distance, s, which is the length along the bodysurface measuredfrom the stagnation point. The value of s is defined asnegative on the lower surfaceand positive on the upper surface.
The local collection efficiency is calculated by first calculating droplettrajectories and producing a plot of particle releasepoint, y0, vs. surface
impact distance, s, as shown in Figure 4.6. As was indicated by Equation
2, the local collection efficiency is a function of the surface distance and
can be determined by differentiating the curve shown in Figure 4.6 with
respect to s.
The derivative at the center of each body segment is calculated by first
determining the four y0 vs. s points whose s values are closest to the s
value of the body segment at which the local collection efficiency is desired,
as shown in Figure 4.6. These four points are then fit with a quadratic
polynomial using the method of least squares. The local collection efficiency
at the desired s location is determined by differentiating the polynomial.
The local collection efficiency is calculated in subroutine EFFICY, while
the curve fitting/differentiation procedure is found in subroutine TERP.
4.2.5.1 Local Collection Efficiency Calculation for Multidispersed
Particle Distributions
The previous section described how the local collection efficiency was calcu-
lated for a single droplet diameter. In icing applications, the mass median
droplet diameter of the droplet size distribution is used to characterize the
size of the droplets. A feature of the particle trajectory portion of the tra-
jectory program is that it allows the user to analyze the local collection
efficiency for a multidispersed particle distribution.
To perform this calculation, the user must input the droplet diameter
and the associated mass fraction and Cunningham correction factor for
each specified droplet size. A maximum of 10 droplet sizes can be used to
characterize a droplet distribution. For example, the required input for a
Langmuir D distribution with a mass median of 20.0 microns is shown in
Table 4.2.
The solution procedure is begun by calculating the local collection effi-
ciency distribution for each droplet size characterizing the distribution. The
19
Table 4.2: Langmuir D droplet size distribution with a mass median of 20
microns
Percentage Ratio of Droplet Cunningham
LWC Diameters Diameter (/_m) Correction Factor0.05 0.31 6.2 1.0272
0.10 0.52 10.4 1.00
0.20 0.71 14.2 1.00
0.30 1.00 20.0 1.00
0.20 1.37 27.4 1.00
0.I0 1.74 34.8 1.00
0.05 2.22 44.4 1.00
local collection efficiency for the distribution is determined by summing the
contributions of each of the droplet sizes using the following equation:
N
(s) -- _ n, 8/(s) (16)i----1
where n/ is the mass fraction of liquid water associated with droplet di-
ameter i and N is the number of droplet sizes used to characterize the
distribution. The local collection efficiency for a droplet size distribution is
also calculated in subroutine EFFICY.
4.2.6 Computational Procedure
The previous sections described various aspects of the calculation of the
particle impingement characteristics. The purpose of this section is to
describe how these calculations work together to yield the desired local
collection efficiency information.
After calculating the flow field about the body, the program enters the
particle trajectory main subroutine, TRAJ. First, the initial particle loca-
tion x0, Y0 and velocity Vz_, Vvp must be determined, either by the computer
program or from information input by the user. A particle should be re-
leased at a location upstream of the airfoil where the flowfield is essentially
2o
the same as the free stream conditions. The program will select an ini-
tial upstream x-coordinate, x0, by searching for a position where the local
velocity VL and the freestream velocity Voo satisfy the following inequality:
1 v,. ,,ol-.. (17)
where e (VEPS in the computer program) is specified by the user. Equation
(17) is tested over a specified range, Yo[,,_,, < Yo < Yo[,,_,_, where yolmin
and y0[,,_,z, illustrated in Figure 4.7, are also input by the user.
With the initial upstream x-coordinate known, the next step is to locate
two trajectories, one that passes above the body and one that passes below
the body. The vertical distances from which these particles are released,
y0[_ and yo],_in, respectively, are specified by the user. The calculation of
these particle trajectories is controlled by subroutine RANGE. Using these
upper and lower trajectories as boundaries, the upper and lower impinge-
ment limits, yo_, and yo_, are determined in subroutine IMPLIM (Figure
4.7b). This subroutine uses a Newton iteration scheme to determine the
release points for particles with trajectories that impinge upon the body
tangent to the surface. For example, when searching for the upper impinge-
ment limit, the trajectory of a particle released from Y011 = (v01_,_+vol-..) is2
computed. If the particle passes under or hits the body, the next trajectory
is computed from Y0]2 = (v0h+uol..s} If it passes over the body, the next2
trajectory is calculated from Y012 = (voh+vol.;.} Successive halving of the2
range Y01,,_, to Y0[,_z continues until the upper impingement limit is found.
Convergence of this iterative procedure is assumed when the difference be-
tween the Yo values of two trajectories, i.e., one that hit the body and one
that missed, is less than a small value specified by the user (YOLIM). This
procedure is then repeated for the lower surface to determine the lower
surface impingement limit. Any particle released between the upper and
lower impingement limits will strike the body and any particle released
from outside this range will miss the body.
With the limiting release points known, the program enters subroutine
COLLEC where the range of vertical position, y0_ to y0t, is divided into a
number (NPL) of equally-spaced increments prescribed by the user. The
trajectory of particles leaving each of these vertical positions is calculated,
21
and the impingement position of the particle on the body surface is deter-
mined using the method previously described. The Y0 vs. surface distance,
s, information obtained in this calculation is then differentiated in subrou-
tine EFFICY to determine the local collection efficiency at the midpoint of
each of the body segments.
4.3 Calculation of the Thermodynamic Characteristics
The thermodynamic analysis of an icing surface was first developed by
Tribus 7 from the physical model of the ice accretion process previously
discussed. This model was used to calculate the heating requirements for
icing protection and proposed LWC measurement systems. Messinger s de-
veloped the thermodynamic model further to include an analysis of the
temperature of an unheated surface in icing conditions for three surface
temperature regimes, i.e., less than 273.15 K, equal to 273.15 K, and above
273.15 K, and the concept of the freezing fraction, f, to be discussed later.
These early formulations have been used in various icing applications.
As discussed in Section 3.2, microscopic movies of the ice accretion pro-
cess made at NASA Lewis Research Center 9 indicate that the process may
be more accurately modeled by modifying the equations used in past icing
studies. The observations reveal that, after the initial flow of the coa-
lesced droplets on the surface, the liquid does not flow but is caught and
frozen in the grooves between the individual surface roughness elements.
Incorporating this observation into a mathematical model would proba-
bly require modeling the individual roughness elements and the freezing of
pools of water surrounded on all sides by ice. A microscopic and possibly
three-dimensional analysis of the icing surface would be required to math-
ematically apply this model to an ice accretion prediction method. The
mathematical model used in this and previous studies is more macroscopic
in nature because the roughness elements do not directly effect the freezing
process except to enhance the convective heat transfer coefficient.
The equations that model the thermodynamics of the freezing process
on a body undergoing icing are formulated by performing a First Law of
Thermodynamic mass and energy balance on a control volume located on
the surface. The control volume to be analyzed is located on the surface of
the body and extends from outside the boundary layer to the surface of the
22
body, asshownin Figure 4.8a. The lower boundary of the control volume is
initially on the surface of the clean geometry and moves outward with the
surface as the ice accretes. Therefore, the control volume is always situated
on either the clean or ice surface. Computationally, a control volume is
placed over each segment defining the body geometry, as shown in Figure
4.8b. The equations resulting from the mass and energy balance can be
expressed as follows:
Mass Balance:
rh,.o,., = (1.0 -/)(rh,, + m,...) - r'n,, (18)
Energy Balance:
?Jrh_[c_,.,,(T. - 273.15) + +
rhr,. [cz,u,.,ur(i-1)(T, ur(i+l } - 273.15)] + qkAs =
rh,[c_,,,,.,_,,.[(T,,,.- 273.15)+ L.]+
[(1 - f)(rhc + rh.,,.) - m,] e;,,,,.o,,,.(Tc,.,, - 273.15)+
frh,, - rh,.,. )[C_,o,,,.(T°_,,. - 273.15) - LI] +
ho[r..,-n2epa J A8
(19)
The complete derivation of Equations (18) and (10) is included in Appendix
A.
4.3.1 Definitions
Before discussing the method used to solve Equations (18) and (19), it is
necessary to discuss several of the terms that are important to the solution
procedure.
As discussed in Section 3.1, the atmospheric and meterological param-
eters determine the type of ice that will form for a given icing condition. It
has been found by various authors that the concept of a freezing fraction
23
can be used to determine the type of ice that will form. The freezing frac-
tion, f, was defined by Messinger as the fraction of impinging liquid that
freezes within the region of impingement. In this application, f is defined
as the fraction of the total liquid entering the control volume that freezes
within the control volume. It is given by the equation
f - (20)
For colder icing conditions, the droplets tend to freeze immediately on
impact, resulting in the formation of rime ice. Since all the water entering
the control volume freezes within the control volume, the freezing fraction
equals 1.0. Freezing fractions close to 0.0 characterize glaze or clear ice.
Freezing fractions between approximately 0.3 and 1.0 will normally indicate
that the ice has some combination of glaze and rime characteristics. As
shown in Figure 3.1, ice accretions are often composed of glaze, rime, and
intermediate regions. The local value of the freezing fraction therefore
varies along the surface, and can be calculated using the mass and energy
balances given by Equations (18) and (19).
4.3.2 Solution of the Energy Equation
The evaluation of Equation (19) is begun at the stagnation point because
there will be no runback into the control volumes located on each side of
the stagnation point, as shown in Figure 4.8b. Therefore,
,_.,nl.ta,=,%nl.,o,_, =0.0 (21)
It is first assumed that the equilibrium surface temperature, Tour, equals
273.15 K. The terms of Equation (19) are then evaluated at this tempera-
ture, and the resulting expression is solved to determine the freezing frac-
tion, f. This calculation is performed in subroutine COMPF. The value
of f will be either 1) less than 0.0, 2} between 0.0 and 1.0, inclusive, or 3)
greater than 1.0.
For 0.0 < f < 1.0, T,u,. = 273.15K, and the initial assumption was
correct. A value of f < 0.0 indicates that the surface temperature is greater
than 273.15 K. Therefore, the solution is obtained by setting f = 0.0 and
solving for T,u, in subroutine COMPT. Note that an iterative procedure
24
is required since many of the terms of Equation (19) are functions of To,r.
Similarly, f > 1.0 indicates that Tou, is less than 273.15K, and f should be
set equal to 1.0. Again, an iterative procedure must be applied to determine
TSUr "
When the thermodynamic characteristics of the control volume are
known, the mass balance given by Equation (18) is used to determine the
mass flow rate of runback water out of the control volume. Any water flow
out of the control volume will be away from the stagnation point and into
the next control volume.
The above procedure is then repeated for the adjacent downstream con-
trol volume and continued along the upper surface of the body. The entire
procedure is then repeated again, starting at the stagnation point and pro-
ceding along the lower surface of the body.
4.4 Calculation of the Iced Geometry
When the freezing fraction has been determined for each segment (con-
trol volume) on the body, Equation (20) is used to calculate the local ice
accumulation rate, rewritten below as
m, = f(_zc -1- m,.,.) (22)
This ice growth rate must be interpreted as an ice thickness to form an
ice accretion on the surface of the geometry. The thickness of the ice layer
grown on a particular segment is given by the equation
d_ = _' At + As (23)Pi
where Pi is the density of the ice, As is the length of the segment, and At
is a time increment specified by the user.
The density of the accreted ice is determined using the empirical expres-
sion developed by Macklin (Reference 18). This correlation was developed
from predominantly rime ice accretions at low temperatures and velocities
and is as follows:
25
i
p,= (24)
In this expression, d,,_ is the mass median droplet diameter in microns, Va
is the droplet impact velocity in m/sec, and T0ur is the surface temperature
in °C. In the calculation, the freestream velocity Voo is used for Va. The ice
density has the units of kg/m s. Equation (24) is used to determine the ice
density when the atmospheric and meteorological parameters are such that
see °C - 2 T,_,, - see°C
and T0_, < -5°C. When these conditions are not satified, it is assumed
that the ice has a density of 917kg/m 3. In general, the inequality will be
satisfied under conditions of small droplets, low velocities, and low surface
temperatures. For example, with a droplet diameter of 12 microns and
a velocity of 60 m/s, the surface temperature must be less than -20 °C, a
rather extreme rime condition. The density of the ice accretion is evaluated
for each surface segment to allow mixed ice accretions to form (mixed ice
accretions contain both rime and glaze ice). The calculation of the ice
density is performed in function RHOICE.
The new ice surface is formed by first adding the ice thickness, d_, per-
pendicular to each segment, as shown in Figure 4.9. The adjacent endpoints
of each of these new segments are then averaged to obtain the coordinates
describing the new ice surface. The new ice surface is calculated in subrou-
tine NWFOIL using this procedure.
When the new surface is formed, the length of a segment increases.
The segments are allowed to grow but, at some point, must be split to
maintain adequate definition of the surface. The segment length is allowed
to increase until it is SEGTOL times the length of the original segment.
The value of SEGTOL is input by the user. When a segment has grown
to SEGTOL times the initial segment length, it is divided in half to form
two new segments, and a new point is added to the set of coordinates.
These two new segments will be allowed to grow to SEGTOL times their
current length before being divided. Note that a value of SEGTOL < 2.0
will result in progressively shorter segments. Values greater than 2.0 will
26
result in progressively longer segments. The segment lengths are checked
and, if necessary, divided in subroutine NWPTS.
As the ice accretion grows, it is also possible for two lobes of the accre-
tion to grow together, causing some of the points to lie in the interior of
the body, as shown in Figure 4.10. These points must be removed in orderto continue the calculations.
The point removal procedure is begun by applying the same procedure
used to determine if two segments intersect, as shown in Figure 4. In this
case, each body segment is checked with every other segment, excluding the
two adjacent segments. As shown in Figure 10, if an intersection is found,
all segments between the two intersecting segments are removed, and the
set of coordinates is revised to reflect these changes. This procedure is
performed in subroutine SEGSEC.
4.5 General Computational Procedure
The previous sections discussed each of the individual phenomena of the
ice accretion process that are evaluated in LEWICE. The purpose of this
section is to describe how these individual calculations are implemented to
form a complete ice accretion.
As discussed in the Introduction, LEWICE applies a time-stepping pro-
cedure to grow an ice accretion. The flow field and droplet impingement
characteristics are initially determined for the clean geometry. The ice
growth rate on each segment defining the surface is determined by applying
the thermodynamic model. The new surface is then formed by specifying
an icing time and applying the procedure described in the previous section
to account for the accreted ice on the clean surface. After calculating this
initial ice layer, two options are available.
The most desirable option is to repeat the entire procedure, beginning
with the calculation of the flow field about the iced geometry, to obtain
revised local collection efficiency and thermodynamic data. Unfortunately,
since the majority of the computational time is spent calculating droplet
trajectories, this option also increases the computational time required to
accrete a layer of ice. Therefore, a second option was made available.
27
If the amount of ice accreted during the time step is small or no new
protuberances, such as glaze horns, were formed, it is possible to accrete
another layer of ice using the same local collection efficiency curve calcu-
lated from the previous time step. This option, of course, does not produce
results that are as accurate as those in the first option, especially for glaze
ice accretions. The advantage is that the computational time required is
significantly reduced.
Each of these options will require that another time increment be spec-
ified. The above procedure is repeated by specifying discrete time incre-
ments until the desired icing time is reached. Guidelines for choosing an
appropriate time increment are also given in Section 5.3.1.
Ice accretions can have many geometrical shapes ranging from the
smooth, aerodynamically-shaped rime accretions to rough glaze accretions
with deep center grooves. LEWICE is therefore required to calculate suf-
ficiently accurate flow fields and particle trajectories about what can be
very irregular geometries where viscous effects such as boundary layer sep-
aration and reattachment are important. This can, at times, exceed the
capabilities of the potential flow code and produce non-physical results.
Much work has been done to identify and correct inaccuracies in the flow
field calculations. The techniques that have been implemented in the code
to overcome these flow field inadequacies will be discussed in many of the
following sections.
28
Cp
-5.0
-4.0
-8.0
-2.0
-1.0
1.0
_.0 0
L!-I__ _-i--
I
LI
_I I I, I I !
.2 .4 .8 .8 1.0
x/ca. m=0.300; c.=-0.018;
I Ii
-_- Experimental
o Predicted
Ir_ I liL.
I
f _ i iI t tlI [I [ ]
0 .2 .4 .6 .8
x/c
b. m--0.300; c,,--0.577;
a=-O.14 a--5.88
1.0
\ " " i
E_[I IIi,:_
wl I
0
_! ii!iiFl!i
C°
.2 .4 .B .8 1.0
x/c¢)m=0.299; e,_= 1.0,,6;
a=10.86
-.1.3 ......
-3.0
-2.0
l
Cp .l.0
.6 .8 1.0
x/c
d. m=0.499; cn=-0.014;
Experimental
o Predicted
i
\(:I-1
O,A- _
v, ,J u"0.o 3
LJ
0 .2 .4 .6 .8 1.0 0
x/c
e. m=0.500; cn=0.626; f.
a=-O.14 a=5.86 a=10.86
I
.2 .4 .6 .8 1.0
x/c
m=0.500; c,:0.966;
Figure 4.1 Comparison to experiment of pressure coefficient over a NACA
0012 airfoil calculated by the Douglas 2-dimensional flo@ code.
29
•2.0
-1.$
-1.2
Cp -.4
.4
.8
1.2
go
J
.2 .4 .6 .8 1.0
x/c
m=0.698; e,=-O.O18;
_=-0.14
-_ Experimental
o Predicted
m_-E]
A L--
0
h.
.2 .4 .6 .8 1.0
x/c
m--0.697; cn--0.716;
a=5.86
L
2=r'-
i ....
___.---...
.2 .4
..............r]I
..... i ............. ,
_r_ :-_" ..........
_ ......
---I ....... __+ ..... ;--- --,
......... ] .....
.6 .8 1.0
x/c
m=0.801; e,,=O.021;
a=O.14
-0- Experimental
o Predicted-1.2
Cp o_- --I-h
,b.8_1!
1._ 0 ._ .4 .6 .8 1.0
x/a
m=0.798; c,,=0.367;jl
a=2,86
Figure 4.1: Continued.
3o
tH
Js= = Upper - Surface Impingement Limit
st = Lower - Surface Impingement Limit
H = Forward Projection of the Airfoil Height
Total Collection Efficiency
YO
Em -H
E._ - H Ids
Local Collection Efficiency
Figure 4.2: Definition of total and local collection efficiency
Figure 4.3: Forces acting on an arbitrarily-shaped particle
31
r SINGLE ELEJ_NT,/ CLOSED G£O_TRY/
//.-- PARTICLE /
1, N
i+I i
N
OT ----Z Oi,1
N = number of points describing the geometry (point 1 is the same as
poing N).
If xp, yp lies outside the body, Or = 0. If xp, yp lies on the body, Or = 7r. If
Xp, yp lies inside the body, Or = 2r
Figure 4.4: Illustration of the method to determine particle impact
r'-" PARTICLE POSITION
I AT PREVIOUS
I TIRESTEP F- CURRENT
I PARTICLE I-POINT OFI tI I POSITION _ INTERSECTIONI I
.....
I. Particle does not pass through
the segment being evaluated.
,........ ,.,.. _ --,- "" _ '" ''0 P1
II. Particle passes through the
segment being evaluated.
The particle passed through the segment being evaluated if all of the fol-
lowing criteria are satisfied:
IPI < PoPx
IN,+1 < N, N,+I
IPo < PoP_
INi < Ni Ni+l
Figure 4.5: Illustration of the method to determine the location of particle
impingement
32
-.t_O
-.152
-.ISq
-.166
-.I§O
-,160
-.162
-.164
-.t6&
-.lk8
-.lTg
m
w
m
D
m
J|
POINTS FIT WITH A
gUADRAT IC POLYNORIAL ._,_
/ \\_/ \ \." \ o
//// _"
o
o
o
o
-._, .._, .._,, .._, ,.._, -._, -._, _o._,o o._,
S (M)
o.Ioz
Figure 4.6: Particle release position, Yo, vs. surface impace distances, s,
points used to determine the polynomial
33
X - Xi, 1
X - Xi+ 2
q:
YO) MAX"_',,%,
q
- X i
*Y
+X
• ;I/1- 'U'---Y-_'_',,ol,,,,,,-<_
a. Criteria to determine the particle release location.
X z X 0 -_
Yt
v._ z-4, -_ -
l
SU = UPPER SURFACE II_INGEIIENT LIMIT
SL = LONER SURFACE II_INGEI, IENT LIIIII
\t- UPPER fANGENI S
,/' IRAJE£TORY y
/v, (I "
Y
,- C_OR[IR IC
'S / CIiORO LINE
b. Particle release locations for the upper and lower surface tangent trajectories
Figure 4.7: Definition of terms used to determine the Local Collection Efficiency.
34
CONTROl VOLU_ --\
0
ROIINI)ARY LAYER --\\
\\
IIII
/APPROACH | NG /
WATER 0,_,/0
DROPLETS -_\ _/
0 _,,\ 0\\\\ / 0 \
\ / ",\ 0 \\
b// o/ o
o / o/
\o /o\ /
\_ o
o //_\o/
/
/- WAll R FIlM/
//
/
AIRFOI[
a. Single control volume on the icing surface.
+y'/ i
/ I/
ST T,. p0,., /r Z/
n_DvMc /," .......-.-:".4COIITROL VOUffiES -.-_-"
.4r, NODES
i I I _'_,
J
÷X
b. Thermodynamic control volumes over each segment defining the body geometry
Figure 4.8: Identification of the control volume used to formulate the ther-
modynamic equations
35
ice s_#f "I'ilE. t+At
f#
l_.'"'f ""-,-,=_o_-i
/i,&
Figure 4.9:Illustration of the method to calculate the iced geometry
36
®
® ®
® ®
a. Geometry with intersecting segments(_)and(_
(8)
/
/
b. Revised geometry with the intersecting segments removed. (The original
segment numbers from a. are in parenthesis)
Figure 4.10: Illustration of the method to remove points from the body
geometry
37
Chapter 5
LEWICE INPUTS
This chapter presents the input format for a LEWICE input card deck.
Section 5.1 contains the documentation that is needed to set up, execute,
and make changes to the data deck. When more explanation is required,
the user should consult Section 5.2 which includes additional information
concerning input definitions and program options. Examples of the input
files are shown in Section 7.0. The interactive input requested by the pro-
gram is discussed in Section 5.3.
5.1 Input Format
The purpose of this section is to provide a quick reference to the input
parameters used in LEWICE. Additional information can be found in Sec-
tion 5.2 and in various sections throughout the text. Where applicable,
the sections that contain additional information about the parameters are
identified.
5.1.1 Potential Flow Input
CARD 01 Run Identification Card (8A4)
IDR
CARD 02 Potential Flow Code Control Parameters (NAMELIST $24Y)
Variable Description
ILIFT Lift Control Flag
= 0 This is not a lifting body
= 1 This is a lifting body
38
IPARA
IFIRST
ISECND
IPVOR
INCLT
CLT
ICHORD
CCL
Element Geometry Flag
-- 0 Linear Elements
-- 1 Parabolic Elements
First-order Terms Flag
= 0 No first-order terms
= 1 First derivative term
= 2 Curvature term
= 3 Both first-order terms
Second-order terms flag
= 0 No second- order terms
= i Second derivative term
= 2 Curvature squared term
= 3 Both second- order terms
Vorticity Distribution Flag
= 0 Use constant vorticity between
body elements
= 1 Use variable vorticity
distribution
c_, a Flag
= 0 Angle of attack, a, is input
= 1 Total lift coefficient, cz, is input
Value of angle of attack (degrees)
or lift coefficient depending on the
value of INCLT
Reference Length Flag
- 0 The reference length used in
calculating c_ is to be set -- 1.0
= 1 The reference length used in
calculating c_ will be input as CCL
The value for the reference length
(chord) used in calculating ci
39
IND
ISOL
IPRINT
IFILL
Individual Solution Flag
$24Y iscapable of calculatingthe
potential flow about up to 6 bodies
and then superimpose the resultsof
each. The possible values of IND are
as follows:
-- 0 Edge velocitiesare not calculated
for each body
- 1 Edge velocitiesare calculated
for each body
In LEWICE, only one body isinput and the
edge velocitiesare always required.
Therefore, IND - 1
Matrix Solution Method Control Flag
= 0 Use routine SOLVIT for the matrix
solution (used when a very large number
of geometry points have been input)
-- 1 Use routine QUASI for the matrix
solution
= 2 Use routine MIS1 for the matrix
solution. Maximum number of geometry
points is 101. Ifthe number of
points isgreater than 101, the program
willautomatically use SOLVIT.
Print/Punch Flag
= 0 Normal output
= 2 Print the individual matrices
= 7 Punch the output on cards
IPRINT should be set equal to 0 to
reduce the amount of printed output
Parabolic Integration Flag
$24Y calculatesthe forcesand moments
acting on the body using both trapezoidal
and parabolic integrationof the calculated
pressure coefficient.The resultsof the
trapezoidal calculationsare always output.
4O
ICOMB
The value of IFILL determines whether the
parabolic results are printed.
= 0 Results of the parabolic integration are
not printed
= 1 Results of the parabolic integrations are
printed
Combination Solution Flag
= 0 No combination solution calculated
= 1 Combination solution calculated
CARD 03 x-Coordinates (6F12.7,2X,I1,1X,I1,1X,I1)
Column Variable Description
01-12 X(1)13-24 X(2)25-36 X(3)37-48 X(4)4_60 X(5)61-72 X(6)
75 INO
77 ISTAT
79 ITYPE
x-coordinate of the geometry. Up to
six coordinates may be input on each
card depending on how the INO flag is
set.
Number of data points per card. If
there are 6 values per card, INO may
be left blank.
Last Card Flag
=0 This is not the last
x-coordinate card. More cards
will follow.
=1 This is the last x-coordinate card.
x-Coordinate Flag
--3
41
CARD 04 y-Coordinates (6FI2.7,2X,I1,1X,I1,1X,I1)
Column Variable Description
01-12 YO)13-24 Y(2)25-36 Y(3)37-48 Y(4)49-60 Y(5)61-72 Y(6)
y-coordinate of the geometry. Up
to six points may be input on each
card depending upon how the INO flag
isset.
75 INO
77 ISTAT
79 ITYPE
Number of data points per card. If
there are six values per card, INO
may be left blank.
Last Card Flag
= 0 This is not the last y-coordinate
card. More cards will follow.
= 1 This is the last y-coordinate
card.
y-Coordinate Flag
-4
5.1.2 Trajectory Code Input
CARD 05 Tajectory Input I (NAMELIST TRAJ1)
Variable Description
GEPS
VEPS
Convergence criterion for the integration
method of Gear
Accuracy criterion for the case when
LXOR = I (Section 4.2.6)
42
DSHIFT
LCMB
LCMP
LEQM
LSYM
LYOR
LXOR
x-distance to shift coordinates after
the potential flow calculation to avoiddiscretization errors
Combination Correction Flag
= 0 Calculates the combination solution
using the method of $24Y
= 1 Calculates the combination solution
using the method of COMBIN-2D
Compressiblity Correction Flag
- 0 No correction for compressibility
- 1 Correct velocity values to account
for compressibility
Particle Initial Condition Flag
= 0 The initial x- and y-components of
the particle velocity will be input
: 1 The initial particle velocity is
equal to the flow at the initial
particle location (in equilibrium
with the flow)
Symmetric Flow Field Flag
- 0 Unsymmetric flow field (general case)
: 1 Symmetric flow field (only half plane
is computed)
y-Coordinate Particle Release Flag
= 0 Particle is released from the position
specified by YORC
- 1 Program determines the vertical particle
release position using YOMAX and YOMIN as
the initial guesses
x-Coordinate Particle Release Flag
- 0 Particle is released from the position
specified by XORC
: 1 Particle release position is determined
the criteria i[1- vo I,< VEPSusing
43
NEQ
NPL
NSEAR
NSI
TIMSTP
Number of equations to be solved to
determine the particle trajectories
-- 4 Spherical, non-lifting particle
= 6 Lifting, rotating particle
Number of particle trajectories to be
computed to define the Y0 vs. s curve.
If NPL is set equal to 1, a single
trajectory isto be calculated.
Maximum number of trajectoriesallowed
to be calculated in the search for the
upper and lower impingement limits
Number of droplet sizesused to
characterize the cloud droplet
distribution (maximum of 10)
Initialvalue of the time step used in
the integrationof the particle
trajectoryequation (Gear's integration
method)
CARD 06 Trajectory Input II (NAMELIST TRAJ2)
Variable Description
CHORD
G
PIT
PRATK
XORC
YORC
Airfoilchord (m)
Acceleration of gravity (m/s 2)
Initialangle of the particleflight
reference line (Figure 4.3) (degrees)
Initialvalue of the particle angle
of attack (Figure 4.3) (degrees)
x-coordinate position of particle
release(Xo/chord). XORC need not
be input ifLXOR = 1.
y-coordinate position of particle
release (y0/chord). YORC need not be
input ifLYOR -- 1.
44
XSTOP
YOLIM
YOMAX
YOMIN
VXPIN,
VYPIN
Maximum downstream distance, normalized
by the chord of the airfoil, for which
particle trajectories are calculated
Accuracy criterion for computing the
surface impingement limits
(Section 4.2.6)
Initial guess for the y-coordinate of
the upper surface tangent trajectory
release point (y0/chord)
(Section 4.2.6)
Initial guess for the y-coordinate of
the lower surface tangent trajectory
release point (y0/chord)
(Section 4.2.6)
x- and y-components of the particle
release velocity. They are input only
when LEQM = 0.
CARD O7 Droplet Distribution Characterization Card
(NAMELIST DIST)
Variable Description
DPD
FLWC
CFP
Droplet sizes in the distribution
(maximum of 10) (microns)
Fraction of LWC for each droplet size
specified in the distribution
Cunningham correction factor
(Section 4.2.2, Table 4.2)
5.1.3 Ice Accretion Input
CARD 08 Ice Accretion Data (NAMELIST ICE)
45
Variable Description
VINF
TAMB
PAMB
LWC
DPMM
RH
XKINIT
SEGTOL
Free-stream velocity (m/s)
Static temperature (K)
Static pressure (Pa)
Liquid water content (g/m a)
Mass median droplet diameter of the
specified droplet distribution (microns)
Percent relative humidity
Initial value of the equivalent sand-
grain roughness of the icing surface
(Chapter 4.3, Appendix F)
Maximum amount any segment may grow
before it is divided in two
(Chapter 4.4)
5.2 User's Guide to Input Format
5.2.1 Potential Flow Input
As discussed in Section 4.1, the flow field used in LEWICE is calculated
using the Douglas potential flow method ($24Y). This code was developed
to calculate the flow field about a wide variety of geometries. Using this
code in an ice accretion prediction method decreases the generality required
by the potential flow code, and many of the input parameters and program
options are not necessary for this application. The input to the potential
flow code required by LEWICE users was simplified to include only the
applicable parameters. However, the potential flow computer code was
not modified and remains in its original form in LEWICE. Therefore, the
original input format to the potential flow code is still used and all input
parameters are required. The input parameters not found in NAMELIST
$24Y are set to default values in subroutine SETUP. In this subroutine,
the input file to the potential flow code is set up and written to unit 45. A
description of the complete input to the potential flow code written to unit
45 is given in Appendix C. Further details concerning the input parameters
can be found in Reference C-1 and C-2.
46
5.2.2 Trajectory Code Input
This section provides the userwith additional information about many of
the input parameters to the particle trajectory code. Suggested values of
the parameters are also given.
5.2.2.1 Trajectory Input 1 (NAMELIST TRAJ1)
GEPS
This variable is the error test constant used in the integration method
of Gear. Single step error estimates made in the integration algorithm must
be less than GEPS in the Euclidean norm. The step size and/or order is
adjusted so that this criteria is met. See References 16 and 17 for additional
information on the parameter and the integration scheme in general.
Parametric studies were made to evaluate the effect of changing the
value of GEPS from 0.001 to 0.00001. Increasing the value of GEPS was
found to reduce the cpu time required to calculate each trajectory by allow-
ing larger integration step sizes to be used. Figure 5.1 shows how increasing
GEPS decreases the computational time per trajectory.
Unfortunately, larger values of GEPS also allow larger computational
errors which are reflected in the calculated particle impingement locations.
Computationally, GEPS should approach 0.0, but the required compu-
tational time would be excessive, as shown in Figure 5.1. A value of
GEPS=0.00005 was therefore used for all calculations.
VEPS
This parameter is used when the program is to locate the proper x
location at which to release the particles. The particles will be released
from an x location where, between YOMIN and YOMAX,
I1 I<_ VEPS
Increasing the value of VEPS will allow particles to be released closer to
the body and thereby decrease the number of integration timesteps required
for the particle to strike the body. The computational time will therefore
be decreased.
47
No studies have beenmade to show the effect of releasingthe particlescloser to the body. The particles must be released in essentially free stream
conditions for physically accurate trajectories to be calculated. For this
reason, a VEPS value of 1.0 x 10 -s has been used for all calculations.
DSHIFT
The potential flow computer program has a relatively large discretiza-
tion error very close to the body. Figure 5.2, taken from Reference 12,
shows the longitudinal and vertical velocities around the leading edge of a
Joukowski airfoil. The velocity is computed for different constant values
of separation distance (DSHIFT) from the body, as illustrated in the in-
sert. Note the large oscillations in the flow field velocity near the surface.
These oscillations can cause erratic particle trajectories close to the body,
especially for small particles that are effected by small flow field perturba-
tions, and can cause fatal program errors to occur, thereby terminating the
program.
To overcome the effect of the discretization error near the body, an ar-
tificial impingement surface is generated by the computer program. This
surface is defined by displacing each point of the body by a small incre-
ment DSHIFT in the upstream z direction. This displacement essentially
increases the size of the body to include the region where discretization
errors are present. DSHIFT values of approximately .2 to .6 percent of the
chord length are commonly used. If irregularties in the impingement curves
or droplet trajectory calculations persist for a specific case, the DSHIFT
value should be increased. Additional information concerning this flowfield
correction can be found in Appendix C.
The artificial impingement surface is generated in the computer program
after the potential flow calculation. Thus, the flow field is not influenced
by the creation of the pseudo-surface. Also, this surface is discarded after
the collection efficiency has been calculated, and is not used when a new
ice surface is formed.
LEQM
This parameter is the flag to specify the initial velocity of the particle.
In cases where an ice accretion is to be formed, the particles should be
released in equilibrium with the flow, i.e., LEQM = 1. The option exists
to specify the x- and y- components of the initial particle velocity when
48
LEQM = 0. This option could be used along with the options to specify
the particle release position to simulate a droplet being ejected from a spray
nozzle.
LSYM
If a body and flow field are symmetrical, the local collection efficiency
distribution will also be symmetrical. Therefore, particle trajectory and
impingement locations need to be calculated only for either the upper or
lower surface. The local collection efficiency distribution is then assumed
to be identical for the opposite surface. When LSYM = 1, the droplet im-
pingement characteristics will be calculated only on the upper surface, and
the local collection efficiency distribution is specified to be identical on the
lower surface. When LSYM = 0, the droplet impingement characteristics
are calculated for both the upper and lower surfaces.
While some clean geometries are exactly symmetrical, the ice shapes
rarely have exactly symmetrical surface coordinates. Forcing symmetrical
collection efficiency distributions onto these surfaces has caused inaccurate
ice shapes to form. Therefore, it is suggested that, unless three or fewer
time-steps are to be performed, LSYM be set equal to 0 even for symmet-
rical bodies at zero angle of attack. Of course, the computational time will
be longer, but, in general, fewer problems will be encountered.
LYOR, LXOR
These are the x- and y-coordinate particle release flags used to indicate
whether the particle release position will be specified by the user or de-
termined in the computer program using the criteria discussed in Section
4.2.6. When using the code to predict ice accretions, it is better to let the
code determine the particle release positions. The positions that might be
specified by the user for the clean geometry may be unsatisfactory as an
ice accretion grows. These options have been included so that the code can
also be used to calculate individual trajectories of particles released from a
specific person.
49
NPL
This parameter is used to specify the number of particle trajectories
calculated in subroutine COLLEC to define the Yo vs. s curve. The curve
will be better defined when more trajectories and impingement locations
are calculated. This, of course, is done at the expense of computational
time. While a maximum of 50 trajectories can be calculated, NPL = 15 is
normally specified.
If NPL is set equal to 1, the impingement limits will not be calculated
and the program will calculate the trajectory of only one particle. The
particle will be released from a position specified by XORC, YORC.
NSEAR
The criteria to identify an impingement limit are specified by the pa-
rameter YOLIM. If this specified parameter is specified too small, an exces-
sive number of trajectories could be calculated. This parameter limits the
number of trajectories that can be calculated while searching for the im-
pingement limits; a value of NSEAR = 50 is normally input. Calculations
of excessive numbers of trajectories can also be caused by erroneous input
values and coordinates defining the body geometry.
TIMSTP
As mentioned in the description of the GEPS parameter, the integra-
tion step size is determined in the program so that the single step error
estimate is less than GEPS. Since the program automatically determines
the step size during the integration, the value of the initial step size is not
critical. A value of TIMSTP = 0.0005 has been used consistently for all
calculations. This value is then decreased or increased as required in the
computer program.
NSI
This parameter specifies the number of droplet size increments used to
characterize the cloud droplet size distribution. If a monodispersed cloud
is to be input, NSI = 1. The effect of using a multidispersed droplet
distribution as opposed to a monodispersed distribution to determine an
ice accretion shape is discussed in Section 7.4.
5o
5.2.2.2 Trajectory Input II (NAMELIST TRAJ2)
CHORD
The chord of the airfoil(or diameter for a cylindricalbody) is used
as the reference length for the coordinate release inputs discussed in this
section. The chord isinput in meters.
G
The acceleration of gravity is input in m/s 2. If it is input as zero,
the effectof gravity on the particle trajectoriesis neglected. The effect
of gravity on the trajectoriesof droplets lessthan 50.0 microns isusually
negligible,and is therefore omitted in most icing studies19. The effectof
gravity was omitted for allof the sample cases in thisreport except for the
ones using a multidispersed droplet distributioncontaining droplets larger
than 50.0 microns.
PIT, PRATK
PIT is the initial particle pitch angle, which is defined as the angle be-
tween the axis oriented parallel to the airfoil x- axis and the flight reference
line (See Figure 4.3 and Section 4.2.2). For spherical, non-rotating particles
(such as water droplets) PIT = 0.0. PRATK is the initial particle angle of
attack and should also be set equal to 0.0 for spherical particles.
When LEWICE is used to calculate ice accretion shapes, PIT and
PRATK should both equal 0.0. The option to calculate the trajectories
for non-spherical, rotating particles has been included so that the particle
trajectory calculation may be useful for alternate applications, however,
appropriate equations for the lift, drag, and moment coefficients must be
supplied by the user and placed in subroutine COEFF. The subroutine was
developed so that the coefficients are functions of the Reynolds number and
the particle angle of attack.
XORC, YORC
These parameters are used to specify the particle release location when
LXOR = 0 and LYOR = 0. XORC and YORC should be input normalized
with respect to the airfoil chord length.
XSTOP
51
This parameter isthe maximum downstream value of x/chord for which
particle trajectoriesare calculated. If a particlereaches a location where
x > XSTOP, it isconsidered to have missed the body and moved out of
range. This rear boundary of the computational box should extend at least
past the location of maximum thickness, and often further, depending on
the geometry and angle of attack. Ifthe value of XSTOP isgreater than the
maximum x-coordinate defining the body (XREAR), XSTOP isset equal
to XREAR.
YOMAX, YOMIN
These are the initial guesses for the y-coordinate of the upper and lower
surface tangent trajectory release points, normalized with respect to the
chord.
YOLIM
YOLIM is the accuracy criteria to be used in determining when an im-
pingement limit has been reached. As discussed in Section 4.2.6, when the
release points of two trajectories (one that hit the body and one that missed
the body) are within YOLIM, the trajectory that hit the body is identified
as either the upper or lower surface tangent trajectory. The smaller the
value of YOLIM, the greater the number of trajectories that will have to be
calculated to identify the tangent trajectory. A practical value for YOLIM
is 0.0001; this value is used for all sample calculations.
VXPIN, VYPIN
These values are the x- and y-components of the initialparticlevelocity
in m/s. These values need to be input only when LEQM = 0.
5.2.2.3 Droplet Distribution Input (NAMELIST DIST)
DPD
This array is used to specify the droplet sizes characterizing the distri-
bution. The droplet sizes should be input in microns.
52
FLWC
FLWC is the fraction of the total liquid water content contained in eachdroplet size increment.
CFP
This parameter is the Cunningham correction factor (Reference 15).Small particles, i.e., those lessthan 10.0microns, have a drag slightly lessthan that given by the equation for spheres in cross-flow. The Cunning-
ham correction factor is used to correct the drag coefficient given by the
equations in subroutine COEFF. The correction factors are found in Table
4.2.
5.2.3 Ice Accretion Input (NAMELIST ICE)
VINF, TAMB, PAMB, LWC, DPMM, RH
These variables are used to specify the icing condition. The pressure and
temperature inputs are static conditions. The variable DPMM is the mass
median droplet diameter of the specified droplet distribution in microns.
If a monodispersed cloud is specified (NSI = 1), DPMM is equal to the
droplet size specified as DPD. When a multidispersed cloud is specified
(NSI = 1), DPMM should still be input because it is used as a label on the
parameter plots.
XKINIT
This parameter is the initial value of the equivalent sand-grain rough-
ness of the icing surface. The integral boundary layer method applied to
calculate the convective heat transfer coefficient uses this variable to ac-
count for the effect of surface roughness. The value of XKINIT is input
by the user and obtained using a relationship that expresses XKINIT as a
function of static temperature, velocity, and LWC. The value of XKINIT
is constant throughout the icing encounter. A discussion of the procedure
used to determine this relationship is given in Appendix F.
SEGTOL
To maintain adequate definition of the body geometry, it is necessary
to divide segments as they grow. This variable is the maximum fractional
amount by which a segment may increase in length before being divided in
53
two. A value of SEGTOL < 2.0 will result in progressively shorter segments.
Values greater than 2.0 will allow the segments to grow progressively longer.
A value of SEGTOL = 1.5 has been found to work well in most icing
predictions.
QCOND
This variable is used to input heat flow either to or from the body
surface. The values of QCOND are input in W/m 2 as a function of surface
distance. It can be used to simulate thermal anti-icing systems, but is not
applicable to de-icing systems since the thermodynamics of the ice-to-liquid
phase change at the surface of the body are not modeled. The results can
only be assumed to be correct for the first timestep because, the effect
of conduction through an ice layer formed during the first timestep is not
modeled.
5.3 Interactive Input
The timestepping feature of LEWICE ca;n, at times, cause conditions to
exist that require the user's interaction. This section describes the pri-
mary interactive prompts and responses required in the computer code.
Several interactive prompts are also made to indicate an unusual condition
requiring analysis by the user. These will be discussed as they occur in the
examples in Section 7.0.
After the primary input file (unit 35) has been read and the potential
flow and particle trajectory files have been set up, the program will prompt
the user to enter the desired icing time (in seconds). The icing time is
considered to be the total length of time that the accretion is to be grown.
The prompt will read as follows:
TIME = 0
ENTER DESIRED ICING TIME (SEC), (F10.0)
Upon entering the icing time, the program will then prompt the user to
enter the desired time increment for the first timestep with the following
statement:
ENTER DESIRED TIME INCREMENT (SEC), (F10.0)
54
A general guideline for selecting an icing time increment for a given icing
condition is discussed in Section 5.3.1.
The user will then be asked to select the desired plot options. The
prompt will be as follows:
AVAILABLE PLOT OPTIONS
0- NO PLOTS
1- PARAMETER PLOTS ONLY
2- TRAJECTORY PLOTS ONLY
3- PARAMETER AND TRAJECTORY PLOTS
ENTER PLOT OPTION ()
If plot option 2 or 3 is chosen, the trajectories will be plotted immediately
after each is calculated. The trajectory points axe not saved and, therefore,
are lost when subsequent trajectories axe calculated. Plot options 1 and 3
will send the program into a plotting routine after the completion of the
timestep so that the significant parameters can be plotted. The plotting
routine uses a menu from which the following plots can be selected:
01 - Iced airfoil
02 - Particle release point (Y0) vs. Surface impact distance(s)
03- Local collection efficieny (/_) vs. Surface distance(s)
04- Edge velocity (Ve) vs. Surface distance(s)
05- Edge temperature (W,) vs. Surface distance(s)
06- Edge pressure (P,) vs. Surface distance(s)
07- Surface temperature (T,u,) vs. Surface distance(s)
08 - Convective heat transfer coefficient (h,) vs. Surface distance(s)
0g - Equivalent sand-grain roughness height (k,) vs. Surface distance(s)
10 - Ice density (p,) vs. surface distance(s)
11 - Freezing fraction (f) vs. surface distance(s)
Examples of these plots axe given in Section 6.0, LEWICE Output.
5.3.1 Selection of an Icing Time Increment
The timestepping procedure makes LEWICE unique among ice accretion
prediction methods because it allows the physics of the ice accretion to
55
be more accurately modeled. Unfortunately, the procedure also adds com-
plexity to the model because a proper time increment must be selected by
the user. Also, the timestep will influence the ice accretion shape for a
specific icing condition; the shape is not uniquely determined by the icing
conditions. For example, Figure 5.3 shows three glaze ice accretion shapes
calculated for the same icing condition, but with different timesteps. In
Figure 5.3a, the accretion was formed in a single timestep. This shape
has the basic shape of the experimental ice accretion but lacks much of
the detail. Figures 5.3b and c show the same accretion formed at shorter
timesteps. Note that, as the timestep is decreased, the predicted accretion
takes on more of the characteristics of the experimental ice shape. Similar
results for a rime ice accretion are shown in Figure 5.4. These results indi-
cate that there is some maximum amount of ice that should be deposited
during a single timestep. On the other hand, when a short timestep is se-
lected, more steps are required to form the final ice shape, which increases
the computational time required for each icing condition.
Many ice accretion shapes have been calculated during the development
of LEWICE, and a criterion has been developed to help the user select an
appropriate timestep. Various authors have developed a term known as the
accumulation parameter, which is given by the following equation:
A° = _1,,,,,, V_ LWC ,',t (25)cpi
where c is the chord length of the body geometry (Some authors omit the
factor fll,,_z in the definition of A,_9.} The accumulation parameter is rep-resentative of the non-dimensional maximum thickness of the ice accreted
during time At. Therefore, a limiting value of A, could be used to de-
termine the length of a timestep. However, it was found that when ice
shapes were formed on an airfoil at an angle of attack, better results were
obtained using timesteps shorter than those used when the airfoil was at
0.0. Equation (25) was modified as follows:
_, = _l,,,_t V¢_ (LWC) At (1 + _) (26)c Pi
where a is in degrees. When comparisons with experimental ice accretions,
the modified accumulation parameter was generally less than. 1. Therefore,
the following equation can be used to calculate the time step:
56
at < (.i) (9.17× i05_) c (27)- _i._z vooLwC (I + _)
Suppose that an ice accretion is to he formed on an airfoil with a chord
of 0.3 m at the following icing condition:
Velocity = 80.0 m/s
LWC = 1.2 g/m s
Angle of attack = 4.0
Icing time = 5.0 min
If the value of _[._.z, the maximum value of the local collection efficiency,
is known, it should be used to evaluate Equation (27). If not, a value of
0.80 is a reasonable upper limit and can be substituted into Equation (27).
The equation is evaluated as follows:
At < (.1) (9.17 × lOSg/rn s) (.3m)
- o.8o(8o,_I_)(1.2glrns) (1+ _0)
< 29.85seconds ,,, 30.0seconds
This indicates that the initial timesteps should be no greater than 30.0
seconds. Since Equation (27) was developed only to provide guidance in
selecting a timestep, it is always appropriate to round the calculated time
to a whole number.
Depending on the icing condition and size of the geometry, a time in-
crement may be calculated that is greater than the total icing time. In this
case, it is recommended that the total icing time be divided into at least
two, and perhaps three, timesteps even though Equation (27) indicated the
ice could be accreted in one step. If a single step were used, none of the
time dependent features of the accretion would be calculated by LEWICE.
It was found that more realistic ice accretions are predicted if at least two
timesteps are used.
There is one additional note concerning the selection of a timestep.
Depending on the icing condition, the predicted shape can become very
convoluted and irregular after several time.steps and computational inac-
curacies, such as multiple calculated stagnation points, may occur. If the
57
multiple effects of these approximations cause the abnormal termination
of the code or the formation of a non-physical ice accretion, increase the
timestep and re-run the condition. By doing so, the user can get an idea
of the general size and shape of the accretion. By comparing this result
to the accretion obtained using the shorter timesteps, the accuracy of the
prediction can be evaluated.
58
150
11o
Figure 5.1:
9Oo 5 10
GEPS
• I I I15 20 25x10 -q
Computational time as a function of GEPS
8
_J
1.20
.8_
• q% --
,08 --
-. JO- .08
I I I I I-.05 -.03 0 .03 .05
SURFACEDISTANCE, slJ_c
.O8
Figure 5.2: Discretization error in the flow field near the nose of a Joukowskiairfoil.
59
EXPERIMENTAL (REF. 20) (a) At = 120.0 SEC.
(b) 4,t = 60.0 SEC. (c) &t = 40.0 SEC.
VELOCITY (M/S) 129.00
TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75
Hm,aDITY oo.ooLWC (G/M s) 1.00
DROP DIAM (MICRONS) 20.00
TIME (SEC) 120.00
Figure 5.3: Effect of icing time increment on a calcualted glaze ice accretion.
6O
At = 120 SEC
At = 60 SEC
At = qO SEC
TOTAL ICING TIME = 120 SEC
VELOCITY (H/S) 60.00
TEHPERATUR[ (C) -26.I5
PRESSURE (KPA) 98.80
HUHIOITY (X) 100.00
LWC (G/H--3) 1.00
OROP OIAM (HICRONS) EO.O0
TIHE ($ZC) 120.00
Figure 5.4: Effect of icing time increment on a calculated rime ice accretion
61
Chapter 6
LEWICE Output
The standard output from LEWICE consists of both printed and plot-
ted output. The printed output is made available primarily for diagnostic
purposes and examination of the calculated values. Most comparisons of
calculated variables and ice shapes are made with the graphics routines
provided in the code. The output discussed in this section is the output for
the sample case presented in Section 7.1.
6.1 Printed Output
Printed output is produced by the potential flow, particle trajectory, and
ice accretion portions of the computer code. All output is printed on unit
56. The following sections describe the printed output from each of these
portions.
6.1.1 Printed Output from the Potential Flow Code ($24Y)
All write statements contained in the original version of $24Y are included
in LEWICE, however, many of these write statments have been commented
out to reduce the amount of printed output.
The initial output from the potential flow code is a listing of the input
geometry coordinates, as shown in Figure 6.1a. Following the coordinate
listing are the calculated non-dimensional surface velocities and the body
pressure coefficients, as shown in Figure 6.lb. A description of each of the
parameters printed on this output page is as follows:
62
ALPHA
ALPHA O
CL
CHORD
NO. OF ELEMENTS,
TOTAL ELEMENTS
I, J
X, Y
S
VT
Angle of attack (degress) specified by the user
Calculated angle of zero lift (degrees)
Calculated lift coefficient. The reference length
is that specified by CHORD
Chord length (meters) specified by the user to
use as the reference length in the calculation
of CL
Number of segments specified to define
the body geometry
Segment number
x,y coordinates of the midpoint of each
segment
Surface distance to the midpoint of each
segment
s = 0.0 corresponds to the trailing edge of the
body (point number 1)
Non-dimensional surface velocity given by the
following equation:
CP
VT=--
Surface pressure coefficient, cp calculated
from VT using the following equation:
CP = 1.0 - VT 2
The force coefficients (lift, moment, normal, axial, and pressure drag)
are calculated from the pressure coefficient data and printed after the data
described above. These variables are calculated using two methods from
the same set of pressure coefficient data. The first method integrates the
pressure coefficient curve using the trapezoidal rule while the second uses
Simpson's rule.
63
6.1.2 Printed Output from the Particle Trajectory Code
The first output from the particle trajectory code will be a statement iden-
tifying the x location from which the particles were released, X0. This
output, shown in Figure 6.2, is a result of the calculations performed insubroutine RELEAS.
The next output consists of the identification of some of the geometry
characteristics. All of the values are dimensional with standard units in the
MKS system. Recall that the geometry coordinates have been adjusted to
avoid the discretization errors in the flow field calculation (Appendix C).
The values of the leading edge, trailing edge, and thickness are determined
from these modified values and not from the original input coordinates.
This computational correction is removed before the collection efficiency
calculation and the calculation of the new ice surface.
The particle trajectory data begin after the geometry characteristics are
printed. The first output is a statement identifying how the particles were
released. If the particles are released in equilibrium with the air (LEQM =
1), the following message will be printed:
The particles are released in equilibrium with the air.
If LEQbf = 0, no message is printed, and the particle release velocities
are specified by the user. In this case, the initial particle velocities are
printed in the line of data shown in Figure 6.2.
Note that when LEQM = 1, the initial particle velocities are shown to
be 0.0 m/s. This indicates that the user did not specify the input velocity.
The initial velocity of each particle is determined by the program and will
depend on the particle release location.
The next statement will indicate the percent mass of each particle cor-
responding to the droplet diameter specified. Following this statement, the
results of the integration of the particle trajectory equations are printed.
This output indicates whether a particle released from a point X0, Y0 im-
pinges on the body. The column headings used in this section of the output
are defined as follows:
64
XO
YO
XP
YP
S
DT
B
I
NSTP =
x-location of particle release
y-location of particle release
x-location where particle either impinged
upon the body or moved out of range
y-location where the particle either impinged
upon the body or moved out of range
surface distance from the stagnation point
to the particle impingement point (lower surface
is negative)
size of the integration timestep when the particle
either hit the body or moved out of range
number of integration timesteps required for the
particle to either impinge upon the body or move out
of range
As discussed in Section 4.2.6, particle trajectories are first calculated
to determine the impingement limits in subroutine IMPLIM. The release
points for the upper and lower surface tangent trajectories are defined as
the particle release positions. A particle released between these points
will strike the body, and one released outside of these points will miss the
body. When the impingement limits are found, they will be printed as
shown in Figure 6.2. The remaining particle trajectory calculations, for
particles released between the upper and lower surface tangent trajectory
release points, are made in COLLEC. All of these particles should strike
the body, and are used to determine the local collection efficiency. When
a droplet distribution has been specified, the output shown in Figure 6.2
will be repeated for each droplet size before continuing with the collection
efficiency calculation.
After completing the calculation of the impingement limits for each
droplet size, the program enters subroutine EFFICY, where the local col-
65
lectionefficiencyiscalculated. The output consistsof the calculated _/ovs.
s points that form the curve that isdifferentiatedto determine the local
collectionefficiency,as shown in Figure 6.3a. This isfollowed by the surface
distance and calculated local collectionefficiencyfor each body segment.
An example of thisoutput isshown in Figure 6.4b. Ifa droplet distribution
has been specified,the output shown in Figure 6.3a and b is printed for
each droplet size.
When a droplet distributionhas been specified,the localcollectioneffi-
cienciesfor each droplet sizein the distributionmust be combined to form
a cumulative local collectionefficiencydistribution. The local collection
efficiencyfor each body segment corresponding to a specificdroplet size
is weighted using the fraction of the total mass specifiedon input. This
weighting procedure isdescribed in Section 4.2.5.1.These cumulative val-
ues are used in the thermodynamic and ice accretion portions of the code.
6.1.3 Printed Output from the Ice Accretion Code
The first page of output from the thermodynamic and ice accretion por-
tions is shown in Figure 6.4a. This output contains the run identification
specified by the user on input, and the current icing time in seconds. The
free stream icing conditions are then printed, followed by general informa-
tion concerning the thermodynamic and ice accretion calculations. This
information contains the body segment numbers corresponding to the stag-
nation point, the upper and lower surface boundary layer transition points
(transition from laminar to turbulent flow), and the upper and lower sur-
face icing limits. The total number of points used in the calculation of
this timestep is given, followed by the number of segments added to the
geometry generated by the previous timestep.
Following this page are three pages containing the detailed output of the
most significant aerodynamic, thermodynamic, and ice accretion parame-
ters. All of these parameters are functions of the surface distance, s, and
are shown in Figure 6.4b. The column headings in the computer output
are defined as follows:
Page 1
I - Body segment number
X - x-coordinate of the iced surface corresponding
66
y
S
VE
TE
PE
RA
SEGLENGTH -
to segment I (m)y-coordinate of the iced surface corresponding
to segment I (m)
Surface distance, s, to the midpoint of segment I (m)
Velocity at the outer edge of the boundary
layer,Ve, (m/s)
Static temperature at the outer edge of the
boundary layer,Te, (K)
Static pressure at the outer edge of the
boundary layer, P., (Pa)
Density of the air at the outer edge of the
boundary layer,po, (kg/m s)
Length of the body segment, s, (m)
Page 2
HTC
XK
BETA
FFRAC
RI
TSURF
DICE
- Convective heat transfer coefficient, he,
(WIm'IK)
- Equivalent sand-grain roughness height,
k., (m)
- Local collectionefficiency,/_
- Freezing fraction,f
- Density of the ice, pi, (kg/m s)
- Equilibrium surface temperature, Tour, (K)
- Thickness of the ice accreted in the current
timestep, d_, (m)
Page 3
QCOND
MDOTC
MDOTRI
MDOTE
- Conductive heat flux from the body surface,
qo,(wire')- Mass flux of liquid impinging in segment I,
rhc (kg/s)
- Mass flux of liquid water running along the
surface into the control volume, the.,
of segment I
- Mass flux of water vapor evaporating from
67
MDOTTI
MDOTT
the control volume, rh,,of
segment I (kg/s)
- Total mass fluxof water entering control
volume, rhT_, of segment I (kg/s)
- Total mass flux of water in to control volume
rhr, of segment I (kg/s)
This concludes the descriptionof the printed output from LEWICE. All
of the output described above isrepeated for each time step.
6.2 Graphical Output
While the printed output isusefulto verifywhether the code isperforming
as expected, much of the output from LEWICE isdisplayed graphically to
aid in the evaluation of the results.
The plotting commands used in LEWICE are unique to NASA Lewis
Research Center and, therefore,are not likelyto be directly applicable to
another facility.GRAPH2D/GRAPH3D commands are used.
All plots discussed in this section have the same border, which contains
title and icing condition information.
6.2.1 Droplet Trajectory Plots
As discussed in Section 5.3.1, when plot option 2 or 3 is selected, the particle
trajectories will be plotted. An example of five such plots are shown in
Figure 6.5. The axes limits (in meters) are determined by the program
so that the entire body geometry is plotted. When a particle impinges
upon the body, the y-coordinate of the release point, y0, and the surface
impingement distance, s, are displayed on the plot. If the particle misses
the body, this information is omitted.
The plotting commands are located in subroutine PLTRAJ, which is
called from subroutine INTIG after the calculation of the trajectory is com-
pleted. Each trajectory is plotted immediately after it is calculated and,
once the calculation of a new trajectory is begun, the previous trajectorycoordinates are erased.
68
6.2.2 Ice Accretion Data
Much of the ice accretion data (Section 6.1.3) can also be plotted to as-
sist the user in interpreting the results. If plot option 1 or 2 has been
selected, the program will enter the plotting routine (subroutine PLOTD)
after completing the ice accretion calculations. The following plot menu
will be displayed upon entering the plot routine:
AVAILABLE PLOT OPTIONS
0 NO PLOTS
1 ICED GEOMETRY
2 ZVSS
3 - BETA VS S
4 - VE VS S
5 - TE VS S
6 - PE VS S
7 - TSURFVSS
8 - HTC VS S
9 - XK VS S
10 - ICE DENSITY VS S
11 - FFRAC VS S
ENTER OPTION NUMBER (I2)
The user then inputs the two-digit identifier for the desired plot.
When plot 01 is selected the iced geometry, with all preceding timesteps,
will be plotted. Before plotting the geometry, the user will be asked to
specify the percent of the geometry to be plotted with the following prompt:
ENTER PERCENT OF GEOMETRY TO BE PLOTTED (F10.0)
Since the size of the plot is fixed, the larger the portion of the airfoil to
be plotted, the smaller the geometry will appear on the plot. For example,
Figures 6.6a, b, and c show geometries plotted with the specified percent
equal to 100, 50., and 25., respectively. After the geometry is plotted, the
program will return to the plot menu.
Plots 02 to 11 are all parameters that are functions of the surface dis-
tance, s. The format for all of these plots is similar and is described below.
69
After selectingthe desired plot, the minimum and maximum values on
the ordinate and abcissa willbe displayed. After each maximum and min-
imum isdisplayed, the user willbe asked to specify the desired axis limit.
After the desired limitsare input, the program willask ifexperimental data
isto be plotted, i.e.,
ENTER 1 IF EXPERIMENTAL DATA IS TO BE PLOTTED IF NOT,
ENTER O
Ifexperimental data are to be plotted, the program will firstask for the
number of data points, and then ask the user to manually input the data.
After the lastexperimental data point is input, the plot will be displayed,
and the experimental data willbe represented as circles.
After viewing the plot, the user willbe given the chance to change the
axes limitswith the following prompt:
IF YOU WOULD LIKE A DIFFERENT SCALE, ENTER 1. IF NOT,
ENTER O.
If this is desired, the maximum and minimum ordinate and abcissa values
will be displayed again, and the above procedure is repeated. If new axes
limits are not desired, the plot menu will be returned to the screen.
As previously stated, plots 02 to 11 all use the operating format de-
scribed above with the occasional exception of plot 02, yo vs. s. When a
droplet distribution is specified, the Y0 vs. s curve corresponding to each
droplet size will be plotted. The correct droplet size for each plot will be
printed in the parameter box in the upper left-hand corner of the plot. The
user will be asked to input the maximum and minimum axes limits for the
plot of each droplet size.
Examples of each of the parameter plots (02-11) are shown in Figures
6.7a-k.
70
<,56709
I0II
13I<,1515
1819202122232<,2526272829303132333<,3536373839<,0<,I<,243<,4<,5<,6q748<,950
UNTRANSFORMED
I X(II1 1 0000000Z 0 98999993 0 9800000
0 97000000 9500000
0 92500000 90000000.87500000.85000000.82500000.80000000.77500000.75000000.72500000.70000000.67500003.65000000.62500000.6000000
0.57500000 5500000
0 52500000 5000000
0 47500000 45000000 4250000
0 40000000 37500000 33000000 52500000.30000000.27500000.25000000.22500000.20000000.17500000.15000000.12500000.10000000.09000000.08000000.07000000.06000000.05000000.04500000.04000000.03500000.03000000.02500000.0200000
COO_DItIATE DATA FOR BODY ID =
Y(I) I0.0000000 51
-0.0018740 52-0.0036110 55-0.0032390, 54-0.0082510 55-0.0117000 56-0.0149080 57-0.0179550 58-0.0208880 59-0.0237390 60-0,0265150 61-0.0292210 62-0.0318550 63-0.0344110 64
-0.0368870 65-0.0392810 66-0.0415850 67-0.0437950 68-0.0<,590<,0 69-0.0479060 70-0.0497930 71-0.0315600 72-0.0531980 75-0.0546980 74-0.0560510 75-0.0572430 76-0.0582620 77-0.0590900 78-0.0597070 79-0.06009q0 80-0.0602260 81-0.0600760 82-0.0596120 83-0.0587940 84
-0.0575700 85-0.0558790 86-0.0536360 87-0.0507320 88-0.0470040 89-0.0452280 90-0.0432520 91-0.0410380 92-0.0385350 93-0.0356740 9_-0.0340820 95-0.0323620 96-0.0304960 97-0.0284620 98-0.0262300 99-0.0237260 100
1, HACA 0012
X(I)0.0150000 -00.0100000 -00.0075000 -00.00500000.00375000.00250000.00225000.00200000.00175000.00150000.00125000.00100000.00087500.00075000.00062500.00050000.00037500.00025000.00012500.00000000.00012500,00025000.00037500.00050000.00062500.00075000.00087500.00100000.00125000.00150000.0O175000.00200000.00225000.00250000.00575000.00500000.00750000.01000000.01500000.02000000.02500000.03000000.03500000.0400000O.OqSO0000.05000000.06000000.07000000.08000000.0900000
: EXAMPLE 1
Y(I)020797001724800150780
-0 0123860-0 O1O699O-0 0086200-0 0081360-0 0076230-0.0070750-0.0064850-0.0058470-0 005146O-0 00_7660-0 0043630-0 0039310-0 0034620-0 0029450-0 0023560-0 0016320
0 00000000 00163200 00235600 00294500 00346200 00393100 00436300 00476600 00514600 0058_700 00648500.00707500.00762300.00813600 00862000 01069900 01238600 01507800 0172q800 02079700 02372600 02623000.028q6200.030_9600.03236200.03408200.03567400.03853500.04103800.04325200.0q52280
a. Geomentry coordinates input.
DOUGLA_
COHBINED FLCU
ALPHA : 0.000000
CL : -0.000001
BODY ID : 1
I ×I 0 99500302 0 98500223 0 9750018<, 0 96000<,55 0 93750q<,6 0 91250307 0.88750188 0.86250119 0.8375007
10 0.8125005II 0.7875000
12 0.762500813 0.7375007l<, 0.717500615 0.6875005
16 0.6_2500917 0.6375008
18 0.612500819 0.5875007_0 0.562500621 0.5375010_ 0.512500923 0.<,8750102<, 0.4625010
25 0.437500926 0.412500927 0.387500828 0.3625006
AIRCRAFT CONPANY T_O-DI_IEHSIOHAL POTENTIAL
NACA 0012 : EXAMPLE 1
ALPHA O = -0.000010
CHORD =/ 1.000000
NACA 0012 : EXAMPLE 1
Y-0.0009536-0.0027575-0.0044365-0.0067700-0.0100112-0.0133284-0.0164470-0.0194323-0.0223233-0.0251359-0.0278768-0.0305473-0.0331<,27-0.0356590
-0 0380946-00qO4q<,4
-0 0<,27021-0 0448624-0 0_69188-0 0_88641-0 0506920-0 0523956-0 0539657-0.0553936-0.0566678-O.0577752-0,0587010-0.0594260
FLGM PROGRAM
NO. OF BODIES 1
TOTAL ELEMENTS 138
NO. OF ELEMENTS 138
S VT CP J0.0024939 -0.8268576 0.3163066 10.0074755 -0.8886778 0.2102517 20.0124468 -0.9189486 0.1555335 30.0198878 -0.9_51062 0.1067743 40.0310313 -0.9680851 0.0628113 50.0433954 -0.9839670 0.0318090 60.0557466 -0.9951780 0.0096207 70.0680897 -1,0043_50 -0.0087891 80.0804271 -1.0128355 -0.0258350 90.0927601 -1.0208483 -0.0421305 100.1050892 -1.0285645 -0.0579443 110.1174146 -1.0361195 -0.0735426 120.1297361 -1.0_3<,093 -0.0887022 130.1420537 -1.0504131 -0.1033669 1<,
0.15_3674 -1.0573263 -0.1179380 150.1666770 -1.0641356 -0.1323843 16
0.1789825 -1.0707989 -0.1466093 170,1912838 -1.0773840 -0.1607561 18
0.2035809 -1.0838785 -0.1747923 190.2158735 -1.0902719 -0.1886921 200.2281619 -1.0966110 -0.2025557 210.2404459 -1.1029654 -0.2165318 220,2527257 -1.1092901 -0.2305241 230.2650014 -1.1156693 -0.2447176 2_0.2772729 -1.1220798 -0.2590628 250.2895406 -1.1285248 -0.2735682 260.3018047 -1.1350374 -0.2883091 270.3140656 -1.1414566 -0.3029222 28
I
101102
I03104
105106
107108
109110
Ill112
113114
115116
117118
119120121
122123
124125
126127
128129
130131
152133
13q135
136137138
139
X(I) Y(I}
0.I000000 0.04700400.1250000 0.0507320
0.1500000 0.05363600.1750000 0.0558790
0.2000000 0.05757000.2250000 0.05879400.2500000 0.05961200.2750000 0.0600760
0 3000000 0.06022600 3250000 0.06009400 3500000 0.0597070
0 3750000 0.0590900
0 4000000 0.05826200 <,250000 0.0572<,30
0 <,500000 0.05605100 4750000 0.05<,69500 5000000 0.05319800 5250000 0.0515600
0 5500000 0.04979300 5750000 0.0<,790600 6000000 0.0<,590_00 6250000 0.0<,379500 6500000 0.0q15850
0.6750000 0.0_928100.7000000 0.0368870
0.7250000 0.0344110
0.7500000 0.03185500.7750000 0,02922100.8000000 0.02651500.8250000 0.02373900.8500000 0.02088800.8750000 0.01795300.9000000 0.01_9080
0.9250000 0.01170000.9500000 0.00825100.9700000 0.00523900.9800000 0.00361100.9899999 0.00187401.0000000 0.0000000
ORIGINAL PAGE IS
OF POOR Q_JALITY
SIGMA VN-0,0131<,Z 0.000003
-0.013130 0.00000<,-0.012671 0.000004-0.012001 0.00000<,-0.011208 0.00000<,-0.010560 0.000003
-0.010141 0.000003-0.009908 0.000002-0.009761 0.000001-0.009632 0.000001-0.009518 0.000001
-0,009385 0.000001-0.009215 0.000001
-0.009038 0.000001-0.008855 0.000001-0.008629 0.000001
-0.008389 0.000001-0.008116 0.000001
-0.007818 0.000001-0.007483 0.000001-0.007134 0.000001-0.0067<,5 0.000001-0.006321 0.000000
-0.005863 0.000000-0.0053<,0 0.000000-0.004772 0.000000-0.004120 0.000000-0.003377 0.000000
Figure 6.1:
b. Surface flow characteristics
Printed output for the potential flow calculations in Example
71
I
303132
33343536
3738
39qO
qLto2
;5
_8
5051
52
535455
57
5859
606I
6263
6463
6667
686970
7172
737q
757677
78
8c81
_2
8586
870889909l
9293
9q95
9691
9899
100101
102103
104105
106107
lO_s109110
IllI12
113
115116
117118
11912012l
I72123
12q125
126127128
129130131
132
133
X0.33750040.31250010.28749970.262¢9920.23749840.212_9730.18749560.16249320.137089_0.11248320.09499600.08499480.0749931
0.06499050.05_9870
3.0G71957
_.03/_9360 032_920
0.02;_920.022_8320.017_724
0.01245260.0087273
0.00620750.0043571
0.00309790.00237360.002123_0.0018732
0.00162300.0013727O.0O112220.0009367
0.00081160.00068640.00056120.00043590.00031010.00018300.00003370.00003370.0001830
0,00031010.0000359
0.00056120.00068640.00081160.00093670.00112220.0013727
0.00162300.0018732
0,002123_0.0023736
0,00309/90.00_3571
0.00620750.008/2730.012452b
0.017_72#0.0224832
0.027_8920.03249200.03749_60.0_249070.047_9570.05498700.06499050.07499310.08499480.09499600.11248320.1374894
0.16249320.18709560.212_9730.237498_0.262_992
0.2_749970.31250010.337500_0.36250060.38750080.41250090.43750090.4625010
0.48750100.5125009
0.53750100.56250060.58;50070.61250080.63750080.66250090&875005).7125006
0.73750070.76250380.78750080.81250050.83750070.86250110.88750180.9125030
Y-0.0599308-0.0601935-0.0601882-0.0598856-0.0592503-0.0582363-0.0567876
-0.0548323-0.05227_9-0.0089800-0.0461379-0.0442662-0.0421762-0.01982_3
-0.0371499-0.0348913
-0.0332373-0.0314462-0.0_94985
-0.0273701
-0.0250116-0.0223086-0.0190892-0.0161891-0.0137715-0.0115558-0.0096758
-0,0083787-0,0078803-0.0073_98-0.0067808-0.0061669-0.005_975-0.0049363-0.00456_8-0.0041473-0.0036968-0.0032039-0.0026510-0.0019948-0.0008182
0.00081820.00199_80.00265100.0032039
0.00369680.0041473
0.00456480.000956]0.0054975
0.00616690.00678080.0073_90O.0O788030.00837870.00967580.0115558
0.01377150.0161891
0.0190892O.0223O86
0.02501160.02737010.02949850.031_4620.0332373
0.03489130.03714990.03982430.0421762
0.04_26620.0461379
0.04898000.05227490.05_83230.0567876
0.05823630.05925030.05988560.06018820.06019350.05993080.059_2600.05870100.05777520.0566678
0.05539360.05396570.05239560.05069200.04886410.0469188
0.04486200,0q270210.040444q0.03809_60.0356590
0.03314270.0305_73
0.02787680,0251359
O.O2232330.0194323
0.01644700.0133284
S0.32632390.538580q0.35083630.36309320,37535330.38761970.39989690._1219140.42431320.43687840.4455638
0.45055190.45556100.4605983
0.46567_80.4695106
0._7209280,47069700,47732820.47999350.48270650.48549800.48842220.49073740.q9245010,49386590.49497550.49570390.49597720.49626470.49656940.49689440.49724470._9752510._9772660.49794020.¢98169_0.49861870.69869660._9902430._9960580.30040880.50099040.50131800.30159600.50184530.50207450.5022881o.5o248960.50277000.50312030.50344530.50375000.50_03740.50_31080.50503920.50614880.50756450.50927720.51159240.51451670.51730820.5200211
0.52268640.52531770.52792190.53050410,53433990.53941630.54445370.5_946280.554_5090.56313630.5755014
0.38782330.6001178
0.61239500.62466140.63692130.64917830.661¢3420.67369070.68594900.6982099O.71O47400.72274170.73501330.74728890.75956880.77185280.78414110.79643380.80873080.82103220.83333770.84564730.85796090.87027850.88260010.89492540.9072545
0.91958700.9319250
0.94426800.9566193
VT-L.1477957-1.1540527
-I.16014q8-1.1660824
-1.1718359-1.1771927-1.1819983-1.1859293-1.1885757-1.1891918-1.1883059-1.1872902-i.1851130-I.1808882-1.1729183-1.1636887-1.1553183-I.I443930
-1.1306782-I.i155020
-1.0984278-1.0677700-1.0151653-0.9530601
-0.8769044-0.7800953-0.6789735-0.6001744-0.5699795-0.5368442-0.4998890-0.4601299-0.4157784-0.3790950-0.3526587-0.3240126-0.2925072-0.2_76460-0.2174368-0.1691881
-0.07223460.07223470.16918730.21743520.25764440.29250530.32401070.35265560.37909350.41577710.46012900.49988730.53684320.56997890.60017290.6789733
0.78009530.87690520.95306001.01516531.06777101.098_2781.11550241.1306782
1.14439201.15531831.16368871.17291831.1808882
1.18511301.1872892
1.18830391.18918991.18857481.18592831.18199831.17719271.17183591.16608141.16014391.15405271.14779571.1414566
1.13503741.12852481.12208081.11566931.10929011.10296541.09661101.09027191.08387851.0773830
1.07079891.06413561 0573254I 05041311 04340931 03611951 02856451 0208483I 01283451 00438500 99517760 9839664
CP-0.31743h3-0.3318377-0.3459358
-0.3597479-0.3731985-0.3857822-0.3971195-0.4064274-0.4127121-0.41_1769-0.4120703-0.q096575-0.4044924-0.3944960-O.3757372-0.3541708-0.3347597
-0.3096352-0.278_328
-0.2443447-0.2065_30
-0.1401320-0.0305605
0.09167650.23103860.3914513
0.53899500.63979080.6751234
0.7117984
0.75011100.78828050.82712840.85628710.87563190.89501590.91463960.9336185
0.95272130.971375_0.99478220.99478210.97137570.95272200.93361940.9144407O.89501710.87563400.85628820.82712940.78828140.75011270.71179940.67512410.63979250.53899530.39145140.23103730.0916766
-0.0305605
-0.1401348-0.2065430-0,2443447-0.2784328-0.3096323-0.3347597-0.3541708-0.3757372-0.394496O-0.4044924-0.4096556-0.4120655-0.4141722-0.4127092-0.4064255
-0.3971195-0.3857822-0.3731985-0.3597450-O.345933O-0.3318377-0.3174343-0.3029222-0.2883091-O.2735682-O.2590647-0.2447176-O.23O5241-0.2163318-0.2025557-0.1886921-0.1747923-0.1607542-0.1466093-0.1323843-0.1179361-0.1033669-0.0887022-O.0735426-0.0579443-O.O4213O5-0.0258331-0.0087891
0.00962160.0318101
J9
3o31
3233
3536373839
4O
_2
434_
¢.6
_7_8
5O
515253
5455
565758
596O
6162
6364
6566
6768
697O71
727374
7576777879
8O
8182
8384
858687
8889
9O91
9293
9495
969798
99I00
i01102
I03104
105I06
I07I08
109110
Ill112113
114I15
116i17
118I19
120121122
123
125
126127128
129130
131
132133
_IGMA0 002b',8
-0 oo167_-0 000_8_0 000589
0 0019310 0030970 0053O4
0 0074570.0100150.0131700.0158020.017660
0.0198880.0225930.0259120.028774O.030983
O.O333880,035952
0.038617O.042161
0.0479860.055116
0.0624050,0707700,0791970.0860450.0902400.0914790.0927910.O941720.095317
0.0963940.0971540.0975120.0977820.0980000.0980230.0977670.0970090.0960000.0960000.0970080 0977670 O98O230 098000
0 0977820 0975120 0971540 096394o 0953170 0941720 092791.
0 0910790 0902_0
0 0860450 0791970 0707700 O624040 0551160 0079860.0_21610.0386170.0359510.0333880.0309820.02577_0.025912
0.O225930.0198880.0176600.0158020.013169
O.0100150.0074570.0053040.0034970.0019310.000589
-0.000585-0.001628
-0.002558-0.003377-O.0O412O-0.004772-O.OO5340-0.005863
-0.006321-0.006746-0.007134
-0.007483-0.007818-0.008116-0.008389-0.008629-0.008855-0.009038
-O.OO9215-0.009385-0.009518
-0.009632-0.009761
-0.009908-0.O1O141
-0.010560
VH0.000000o.o0o0oo
o.0000000.00000o
0.0000000.000000
-0.000002-0.000002
-0.00000q-0.000003
-0.000003-0.000002
-0.000002-0.000002-0.000002
-0.000001-0.000001-O.O00001
-0.000000-O.O00001
-0.000000-0.000000
0.0000000.000001
0.000001O.O00001O.O00001
O.OOOO020.000002O.0OOOO20.0000020 0000020 000002
0 0000020 0000020 0000020 0000020 000003
-0 000003-0 000009-0 000026-0 000027-0 000013-0 0000030 O0OOO1
0 0000020 0000020 O000010 0000010 0000020.0000010.000001
O.OOOO020.000001
0,000001
0.0000020 000001
0 000000-0 000000-0 000001
-0 000002-0 000002
-0 000003-0 000003
-0 000003-0 000003-0 000003-0 000003-0 000003-0 000004-0 000003-0 000004-0 000003
-0,000002-0.000002-0.000002
0.0000000.0000000.0000000.0000000.000000
0.0000000.0000000.0000000,000000
0.0000000.0000000.O00OOOO.O00001O.OOOO01
0.000001O.O000010.000001
0.000001
0.000001O.O000010.0000010.000001
O.0OOOO10.000001
0.0000010.000001
0.0000010.000001
0.000001
Surface flow characteristics (continued)
Figure 6.1: continuedORIGINAL PAGE _S
OF POOR QUALITY
72
L3_ 0 _37504_ 0.0100112[_5 0 05000_5 0.00677801_6 0q75UUt8 0.004436513/ 0.9850022 0.0027575130 0.9950050 0.0009536
INTEGRATED VALUES
CY = 0.00000 CX = 0.00010
(:L = 0.00000 CD = 0.00010
PARABOLIC IHTEGRATION
INTEGRATED VALUES
CY : 0.00000 CX : 0.0001%
CL = 0.00000 CD = 0.0001_
TOTAL CM = 0.00000
TOTAL CM : -0.00000 (PARABOLIC)
S0.96898320.98012670.98756760.99253880.997520_
CM = 0.00000
CM : -0.00000
VT0.96808460.94510600.9189_850.88867680.8268565
CP0.06281230.10577470.15553370.21025370.316_08_
J SIGMA VN13_ -0.01120_ 0.000004135 -0,0IZ001 0.000004136 -0.01267l 0.00000_137 -0.013130 0.000005
138 -0,0131qZ 0.00000q
ORIGINAL PACi_ 19
OF POOR QUALITY
Surface flow characteristics (continued)
Figure 6.1: Concluded
THE PARTICLES ARE RELEASED FROM X = -1.26000E 00WHICH IS OBTAINED AT TilE I LOOP OF 50 LOOPS
GEOMETRY CHARACTERISTICS:
LEADING EDGE (X,Y) -2.0000E-033.0200E-01
TRAILING EDGE (X,Y) / _.0136E-02TIIICKNESSCHORD 5.0000E-01ANGLE OF ATTACK 0.0000
U?PE_ BOUNDARY 2.2075E-02LCWER BOUNDARY -2.2075E-02
PARTICLE TRAJECTORY DATA:
0.00000.0000
THE PARTICLES ARE RELEASED IN EQUILIBRIUM WITH THE AIR
PARTICLE INITIAL INITIAL PARTICLE PITCII PIT GRAVT ERROR
DIAMETER VX VY AOA ANGLE DOT CONST CRITERIA(MICRONS) (M/S) (M/S) (DEGREES) (DEGREES) (DEG/SEC) (M/S_W2)
20.00 0.00 0.00 0.00 0.00 0.00 0.00 5.00E-05
THE PARTICLES OF SIZE 20.00COHTAIN 1.0000 OF THE TOTAL MASS
X0 Y0 XP YP S DT NSTP-1.2599993 0.0150000 OUT OF RANGE 0.0471370 0.022q023 3.6qq0E-05 58-1.2599993 -0.0150000 OUT OF RANGE 0,0_73017 -0.022q552 3.5855E-05 67
YOMAX= 1.5000E-02 YOMIN= -1.5000E-02
-1.2599993 0.0000000 HIT BODY AT -0.0019999 0.0000010 0.0000011 5.9902E-06 _6-1.2599993 0.0075000 NIT BODY AT 0.01252q9 0.0100_23 0.0197897 1.1801E-05 67
-1.2599993 0.0112500 OUT OF RAH_E 0.0732779 0.0228669 q.9098E-05 7q
-1.2599993 0.0093750 OUT OF RANGE 0.08q6801 0.0229987 6.0772E-05 83-1.2599993 0,008q375 HIT BODY AT 0.022720q 0.0127862 0.030566q 1.7692E-05 65-1.2599993 0.0089062 OUT OF RANGE 0.0793677 0.0221173 5.7872E-05 0_-1.2599993 0.0086719 OUT OF RANGE 0.0863379 0.0227919 5.558_E-05 83
-1.2599993 0.00855_7 OUT OF RANGE 0.0862296 0.0227190 5.9_60E-05 99-1.2599993 0,008q961 NIT BODY AT 0.0258700 0.013_200 0.0337822 2._208E-05 69-1.2599993 -0.0032520 HIT BODY AT 0.0000620 -0.0037906 -0.0055256 5.B16qE-06 59-1.2599993 -0.0091260 OUT OF RANGE 0.0826181 -0.022627_ 5.8351E-05 83-1.2599993 -0.0061890 HIT BODY AT 0.00636_5 -0.0077377 -0.0133298 9.1509E-06 61
-1.2599993 -0.0076575 HIT BODY AT 0.0133570 -0.010373q -0.0208795 1.1755E-05 65
-1.2599993 -0.0083917 HIT BODY AT 0.0216_31 -0.0125515 -0,029_638 1.9979E-05 69-1.2599993 -0.0087588 OUT OF RANGE 0.0826917 -0.022_2_2 _.8719E-05 87-1.2599993 -0.0085753 OUT OF RANGE 0.0875171 -0.0228_87 7.0857E-05 86-1.2599993 -0.008q855 HIT BODY AT 0.0237963 -0.0150158 -0.0316695 1.7371E-05 74
UPPER SURFACE LIMIT LOWER SURFACE LIMIT
YOU SU Y0L SL
0.Bq96E-02 0.3378E-01 -0.8%83E-02 -0.3167E-01
-1.2599993 0.0076_71 HIT BODY AT 0.0132636 0.0103qq8 0.0207819 1.1751E-05 69
Figure 6.2: Printed output for the individual particle trajectory calculations
in Example 1.
"73
×0 Y0
-1.2599973 0.0065556 HIT BODy AT-1.2599993 0.0054640 HIT BODY AT-1.2599993 0.00_3725 HIT BODY AT-1.2599993 0.0032809 HIT BODY AT
-1,2599995 0.0021896 HIT BODY AT-|.2599993 0.0010978 HIT BODY _T-1.2599993 0.0000063 HIT BODY _T
-1.2599993 -0.0010852 flIT BODY AT
-1.2599993 -0.0021768 HIT BODY AT
-1.2599993 -0.0032683 HIT BODY AT
-1.2599993 -0.0063599 HIT BODY AT-1.2599993 -0.005651_ NIT BODY AT
-i,2599993 -0.0065q30 HIT BODY AT
-i 2599993 -0.00763q5 HIT BODY AT
XP
0 0077701
0 0042313
0 00182710 0000979
-0 001039_
-0 00171O8
-0 001999q
-0 0017167-0.0010524
0.00007760.00179590.00_1859
0.0077176
0.01320q7
YP
0.00836890.00667970.00520050.00382380.00251880.00125620.0000057
-0.0012406-0.00250_9-0.00380_9-0.0051801-0.0066553
-0.0083265-0.0103267
S
0 01_8929
0 0109037
0 00800550 00557q5
0 0035691
0 00179990.0000057
-0.0017832-0.0035500-0.0055467-0.0079682-0.0108521
-0.01_8358-0.0207203
Figure 6.2: Concluded
DT
8.683OE-06
7 9091E-06
6 0560E-066 136_E-06
5 9198E-06
6 98_3E-06
5 9947E-067 I0_3E-06
6 17qqE-06
6._569E-06
7.3536E-06
9.0981E-068.6736E-06
1.73_6E-05
NSTP57
_652
5_
6O
_647
43
46
_9
61
5?
57
Y0 VS S DATA FOR DROPLET DIAMETER =
17 POINTS HAVE BEEN CALCULATED
I S
1 0.0537822 0.0207823 0.016893
0.0109065 0.0080056 0.0055757 0.0055698 0.001B009 0 000006
10 -0 00178311 -0 503550
12 -0 00556713 -0 00796814 -0 010852!5 -0 016836
16 -0 020720i7 -0 031670
Y0
0,008¢960.0076470.0065560,005¢640.0043720 0032810 0021890 0010980 000006
-0 001085
-0 002177
-0 003268-0 00_360-0 005_51-0 006543
-0 007655-0 008683
20.00000 MICRONS
a. Calculate Yo vs s points
ORIGINAL PAGE IS
OF POOR QUALITY
CALCULATED
SEG
I -02 -0
5 -0
4
56
7
89
!0
11
12
13
1516
!7
19
20
2122
23
2q
25
LOCAL COLLECTION EFFICIENCY FOR DROPLET DIAMETER s
S309069306890301823
-0 2972q5-0 290605-0 282821-0 275269-0 _67686-0 260129-0.252576-0.245025-0.237_77-0.229931-0.222386-0.21484;-0,20730_-0 199766-0 192231
-0 186697-0 177165-0 169635-0 162108
-0 156582-0 167058-0 139536
_ETA SEG S0.000000 26 -0.1320140.000000 27 -0.1244940.000000 28 -0.1169740.000000 29 -0.109_540.000000 30 -0.1019330.000000 31 -0.09_4100.000000 32 -0.0868840.000000 33 -0.0793530.000000 34 -0.0718140.000000 35 -0.06426_0.000000 36 -0.056696
0.000000 37 -0.0691020.000000 38 -0.0_14820.000000 39 -0.0361130.000000 40 -0,035010
0.000000 61 -0.0298990.000000 _2 -0.026761
0.000000 _3 -0.0235970.000000 4_ -0.0211920.000000 65 -0.0195560.000000 46 -0.0179110.000000 67 -0.0162;20.000000 48 -0,0145600.000000 _9 -0.0127860.000000 50 -0.010945
20.00000 MICRONS
BETA SEG0.000000 51
0.000000 52
0.000000 53
0.000000 540.000000 55
0.000000 56
0.000000 570.000000 580.000000 590.000000 60
0.000000 610.000000 620.000000 630.000000 660.000000 65
0.023592 660.067630 670.11202_ 680.1%5775 69
0 168733 700 191828 710 215251 72
0 251020 730 28907_ 760 528992 75
S-0.009002-0.007390-0.006131-0.005052-0.00ql9q-0.003623
-0.005371-0.00316_
-0.002904-0.002669
-0.002381-0.002162-0.001995-0.001826
-0.001663
-0.001_2
-0.001212-0 000895-0 000351
0 000351
0 0008950 001212
0 001_2
0 0016q_
0 001826
b. Local collection efficiency for each body segment.
Figure 6.3: Summary of the particle trajectory and local collection efficiency
calculations in Example 1.
BETA0.3876320._%08360.q_3091
0.5225690.5578310.581160
0.5813000.5854090.5897590.59_386
0.5992250,6032080.6062200.60928_0.6139150,613387
0.612782
0.6119500.610521
0.61045_
0.6116820.6120320.612518
0,612899
0.608128
74
SEG767778798O8182838_85868788
909192939495969793
:O2!03
105106107
S0.0019950.0021620.0023310.0026090.0029040.0031440.0033710.0036280.004194
0.0050520.0061310.0073900.00900200109_50.0127860.0145400 0162_20 0179110 0195560 021192
0 0235970 026761
0 029399
0 033010
0 C36113
0 0_I_820 0_9102
0.0_66960.06_2640.07131_
0.0793530.08638_
BETA0.6050380.6020000.5979820.5931020.5884350.5840470.5799040.5804440.5571250.5218460.4820570.440096
0.3872850.328975
0.289_06
0.2516B3
0 2158060 1928100 170136
0 I07597
0 I14_61
0 0708770 0276420 0000000 0000000 0000000.0000000.0000000.0000000.0000000.0000000.000000
SEG108
109
II0Iii
112
113
114
115
116117
118119
120
121
122123
124
125
126
127128
129
130
131
132133
134
135
136
137138
S0.0944100.1019530.109#5_0.1169740.12_4940.132014
0.139536
0.1670580 1565820 162108
0 1696350 177165
0 184697
0 192231
0 199766
0.207306
0.2168440,222386
0.229931
0.237_77
0.2650250.2525760.2601290.2676860.2752_90.2828210.290005
0.297205
0.501823
0.3048900.509069
BETA0.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000 0000000 0000000 0000000 0000000 0000000 0000000 000000
0 0000000 0000000 0000000 0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000.000000
b. Local collectionefficiencyfor each body segment
Figure 6.3: Concluded
OR/GINAE PAGE IS
OF POOR QUALITY
(continued).
SEG SI -0.30721E 002 -0.30016E 003 -0.30112E 00
-0.29656E 005 -0.28970E O06 -0.282|8_ O07 -0.27q62E O08 -0.26707E O0
9 -0.25952E 00
I0 -0 25197E O0
Ii -0 2_2E 0012 -0 23638E 0013 -0 2293_E 00I_ -0 221_0E 00
15 -0 21_27E 00
16 -0 20673E 00
17 -0 19920E 0018 -0 19168E 00
19 -0,18615E 0020 -0.17665E 0021 -0.16911E 0022 -0.16159E 00
23 -0.15608E 0024 -0.1_656E 0025 -0.13905E 0026 -0.13155E 0027 -0.12404E O028 -0.I1656E 0029 -0.10904E 0030 -0.10156E 0031 -0.9_037E-0152 -0 86537E-0133 -0 79034E-0136 -0 71528E-0135 -0 66015E-0136 -0 56691E-0137 -0 _8951E-0138 -0 q138qE-01
39 -0 36069E-01_0 -0 35011E-01ql -0.29968E-01_2 -0.26853E-0143 -0.23729E-016_ -0.21363E-01
05 "-0.19763E-01
QCOND
0.000000.000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
0 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.00000O.O00OO0.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
MDOTC MDOTRI0.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.00000
J 0.00000 0.00000
0.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.00000
0.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0,000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.00000
0.00000 0.00000
0.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.000000.00000 0.00000
0.46756E-05 0.000000.13490E-04 0.00000
0.22546E-04 0.000000.1q801E-04 0.000000.17264E-04 0.00000
HDOTE
0.00000
0.000000.000000.00000
0.00000
0.000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000 000000 000000 00000
0 000000 000000 000000.000000.000000.000000.000000.000000.00000
0.93270E-050.30625E-050.35536£-050.19768E-050.21182E-05
HDOTTI0.000000.000000.000000.000000.000000,000000,000000.000000,000000,000000.000000.000000,00000
0 000000 000000 000000 00000
0 000000 000000 000000 000000 000000 000000 00000
0 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
0._6756E-050.13690E-060.225_6E-000.16801E-060.1726_E-06
HDOTT
0.00000
0.000000 00000
0 00000
0 00000
0 000000 0000O
0 000000 000000 000000.000000.000000.00000
0.000000.00000
0.00OOO
0.00OOO
0.000000.0OO000.000000.000000.000000.00000
0.000000.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 00000
0 00000
0 OO0OO0 000000 000000 000000 00000
0.10_28E-0_0.18993E-000.12827E-040.15106E-0_
a. Icing condition and summary of ice accretion data
Figure 6.4: Printed output from the ice accretion calculations in Example
1. 75
5EG_6¢7
48¢9SO515253
55's6575859
6061625364SS_66768697071":2737,q75;67"7879808182838¢8586878889909192939_9S96979899
].00101102103
105106107108109110111112113
11611711811912012112212312c+125126J271281291.5013113213313c+135136137138
S-0.181_6E-01-0.16506E-01-0.1_833E-01-0.13110E-01-0.11302E-01-0.93693E-02-0.77677E-02-0.6_879E-02-0.53333E-02-0._3923E-02-0.37712E-02-0.36932£-02-0.32617£-02-0.29800Eo02
-0.270_8£-02-0.26173£-02-0.21866£-02-0.20]37E-02-0,183)3E-02-0.16529E-02-0.16501_-02-0.12199E-02
-0.91868E-03-0.37066E-03
3 3706_E-030 91867E-030 12199E-020 1_500E-020 16528E-020 18392E-02
0 20136E-02
0 21865E-02
0.2_171E-02
0.27047E-020.29798E-020.3ZqlSE-020.3_930£-020.37710£-020.63922E-020.53337E-02O.64871£-020.77652£-020.93666E-020.11299E-010.13107£-010.16830E-010.16§03E-010.18143E-010 19759£-010 21360£-010 23726E-010 26851E-010 299q6E-010 33015E-010 36067E-010 _1382E-010 489_9E-01
0 56489E-01
0.6;013[-01
0.7152GE-010.79032E-010.86535E-010.96035E-010.1015_£ 000.1090_E 000.11656E 000.12_0_E 000.13155£ O00.13905E O00.16656E O00.15_07E O00.16159E 000.16911E 000.17663E 000.18_15E 000.19167E 000.19920E O00,20673E 00
0.21627E 000.22185£ 000.22936E 000.23688E 000.2_6_2E 00
O.25197£ 000,25951E 000.26706£ 000.27_62E 000.28218£ 000.2897;E 000.29656E 000.30112E 000.30_16E 000.30721E 00
QCOND0.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.00000
0.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000600.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
_DOTC0.19810E-040.22683E-0fi0.26596E-060.31279E-060.36889E-060._5990E-0_0.28238E-0_0.3_3_2E-0q0.21231E-0_0.26185E-0_0.61258E-050.6q190E-050.68230E-050.73125£-050.78811E-050.86295£-050.46692E-050._9695E-050.53020E-050.57658E-050.63131E-05
0.71395E-050.86999E-050.19336E-0_0.1933_E-060.86932£-050.71313E-050.63062E-050.57563E-050.52920E-050 69399E-050 _6598E-050 86117E-050 78641E-050 72961E-050 68071E-05
0 6q036E-050 61185E-050.26151E-040.21202E-0q0.3q268E-0q0.28191E-04O._§9q9E-0_0.36&87E-0q0.31315E-0q0.26666E-0_0.225_1E-0_0.19911E-0_0.17k07E-0_0.1_986E-040.23037E-0_0.1q138E-0_0.Sq782E-05
0.000000.000000.000000.000000.000000.00000O.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
MDOTRI
0.000000.000000.000000.000000.000000.000000.000000.00000
0.18_32E-050.85131£-050 93358E-050 992_6E-050 10286E-0_0 10377£-0_0 10151E-0_0 95637E-050 910_8E-050.85090E-050.777O8£-050.68596E-050.58027E-050.q5832E-050.31_32E-05
0.000000.00000
0.31_13E-05
0._5755E-050.57880E-050.68372E-050.77_01E-050.86697E-05
0.90572E-050.95080E-050.10080E-0q0.10292E-0_0.10186E-0_0.98116E-050.92095E-050.83806E-050.16818E-0§
0.000000.000000.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000,000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
_DOTE
0.22692E-050.24326E-050.26663E-050.29390E-050.32710E-050.3773_E-050.21648E-050.2_859£-050.15_91E-050.20664E-050._3172E-060._3325£-060.q_l�SE-060._5292E-06
0 _6528E-060 _8563E-060 25283£-060 26031E-060 27181E-060 28796E-060 31115E-06
0 35022E-06
0.63012E-060.95677E-060.95677E-060._3012£-060.35022E-060.31115E-060.28796E-060.27181E-060.26031E-060.25283E-060.qSS63E-060._6528E-060._5292E-060._191£-060.q3325E-060.q3172E-060.2066_E-050 15393E-050 2_826E-050 21627E-050 37718E-050 32709£-050 29_05E-050 26693E-050 2_350E-050 22734E-050.212_2£-050.19825E-050.35737£-050.30885E-050.9327_E-05
0 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.000000,000000.000000.00000
0.00000
_DOTTI0.19&IOE-040.22_83E-0_0.26596E-040.31279E-0q0.36889E-0_0._5990E-060 28238E-0_0 3q362E-0_
0 2307_E-0q0 3q698E-0_0 15662E-0_0 1634qE-0_0 17109E-0_0 17690E-0_0.18032_-0_0 18193E-0_
0 1377_£-040 13459E-0_0 13073E-0_0 12625E-06
0 12116E-06
0 I1723E-0_
0 118G3E-060 19336E-060 19336E-06
0 I1835E-04
0 11707E-0_0 12092E-0_
0 12593E-Oq0 13032£-0_0 13_IOE-06
0.13717_-06
0.18120E-0_
0.179_q£-060.17588£-0_0.16993E-060.16215£-0_0.15328£-040.36532E-0_0.22883E-040.3_268E-0_0.28191E-0_0._5969E-0_0.36887E-0_0.31315E-0_0.26666E-060.22541E-0_0.19911£-0_
0.17_07E-0_
0.1_986E-040.23037E-0_0.1_138E-0_0.56782E-05
O.000OO0.000000.000000.000000.000000.000000.000000 00O0O0 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.00000
0.000000 000000 000000 00000
0 000000 00000
0 000000 000000 000000 000000.000000.000000.000000.000000.000000.000000.00000
0.00000
0.00000
_DOTT
0.17560E-060.20050E-0q0.23930E-060.283_0E-0_0.33618E-0q0.42217E-0_0.2607_£-0_0.31856E-0_0.21525E-0q0.32631E-0_0.15030E-0_0.15910E-0_0.16667E-060.17237E-0_0.17567E-0_
0 17708E-0_
0 13521E-0q
0 13198E°0_0 12801E-0_
0 12337E-OG
0 I1805E-0_
0 11372E-06
0 11613E-060 18379E-06
0 18377£-06
0 II_04E-0_
0 I1357E-0G
0 I1781E-06
0 12305E-O_0 12760_-06
0 131_9E-0_
0 13_6_E-0_
0 1763_£-0_
0 17679£-0_
0 17135E-0_0 16551E-0_
0.15782E-0_
0.I_896_-0q0.32665E-0_0.2136_E-0_
0,31786£-06
0.26028E-0q
0,62177E-060.33616E-0_0.2837_E-0_0.23997E-0_0,20106E-0_0.17638E-060.15283E-040.1300_E-0q0,19q63E-0q
0.11069E-060.000000.000000.000000.000000.000000.00000
0.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
0.000000.000000.000000.000000.000000.000000.00000
0.00000
0.000000 00000
0 OOO0O
0 00000
0 000000 00000
0 00000
0 000000 000000 000000.000000.000000.000000.000000.000000.00000
b. Calculated surface ch_acteristics (continued)
Figure 6.4: continued
76
ORIGINAL PAGE IS
OF POOR QUALITY
HACA 0012 : EXAMPLE 1
ICING CONDITIOH:
STATIC TEMPERATURE (C)STATIC PRESSURE (PA)VELOCITY (M/S)LWC (GIM"_3)DROPLET D_AMETER (_ICROHS)
: T_E = 60.000 SEC
260.5590748.00
129.000.50
20.00
ICE ACCRETION DATA:
STAGNATIOH POINTTRAt4SITIOt4 POINTS (LOWER,UPPER)ICIHG LIMITS (LOWER,UPPER)HUMBER OF POINTSNUMBER OF SEGMENTS ADDED
7O6842
1390
7197
OmCfNALPAGE ;sOFPOORQUAL;TY
SEG X Y1 0.30000E 00 0.000002 0.29700E 00 -0.56220E-033 0.29400E 00 -0.10833E-02
0.29100E 00 -0.15717E-025 0.28500E 00 -0.24753E-026 0.27750E 00 -0.35100E-027 0.27000E 00 -0.q_72_E-028 0.26250E 00 -0.53859E-029 0.25500E 00 -0.6266_E-02
10 0.24750E 00 -0.71217E-0211 0.24000E 00 -0.795_5E-0212 0.23250E 00 -0.87663E-0213 0.22500E 00 -0.9§565E-0214 0.21750E 00 -0.10323E-0115 0.21000E 00 -0.11066E-0116 0.20250E 00 -0.1178_E-0117 0.19500E 00 -0.12475E-0118 0.18750E 00 -0.13138E-0119 0.18000E 00 -0.13771E-0120 0.17250E 00 -0.1_372E-0121 0.16500E 00 -0.1_938E-0122 0.15750E 00 -0.15468E-0123 0.15000E 00 -0.15959E-0124 0.14250E 00 -0.16409E-0125 0.13500E 00 -0.16815E-0126 0.12750E 00 -0.17173E-0127 0.12000E 00 -0.17479E-0128 0.11250E 00 -0.17727E-0129 0.10500E 00 -0.17912E-0130 0.97500E-01 -0.18028E-0131 0.900_0E-01 -0.18068E-0132 0.82500E-01 -0.18023E-0133 0.75000E-01 -0.1788_E-0134 0.67500E-01 -0.17638E-0135 0.60000E-01 -0.17271E-0136 0.52500E-01 -0.16764E-0137 0.45000E-01 -0.16091E-0138 0.37500E-01 -0.15220E-0139 0.30000E-Of -0.14101E-0140 0.27000E-01 -0.13568E-0141 0.2_000E-01 -0.12976E-0142 0.20965E-01 -0.124§0E-0143 0.1790_E-01 -0.11926E-0144 0.1_8_2E-01 -0.11223E-01_5 0.13291E-01 -0.1085_E-0146 0.11743E-01 -0.10_25E-0147 0.10187E-01 -0.97488E-0248 0.86129E-02 -0.9_430E-02_9 0.70109E-02 -0.88981E-0250 0.53760E-02 -0.82622E-0251 0.36757E-02 -0.75051E-0252 0.19168E-02 -0.65439E-02$3 0.89327E-03 -0.59196E-025_ -0.20987E-03 -0.51230E-0255 -0.10241E-02 -0.46363E-0256 -0.15952E-02 -0.38979E-0257 -0.16134E-02 -0.35899E-0258 -0.16399E-02 -0.33_39E-0259 -0.167qBE-OZ -0.30707E-OZ60 -0.17045E-02 -0.28245E-0261 -0.17332E-02 -0.25435E-0262 -0.17677E-02 -0.22528E-0263 -0.17728E-02 -0.20803E-026_ -0.17852E-02 -0.19116E-0265 -0.18036E-02 -0.17328E-02
s-0.30721E 00-0.30416E 00-0.30112E 00-0.29656E 00-0.28974E 00-0.28218E 00-0.27_62E 00-0.26707E 00-0.25952E 00-0.25197E 00-0.24_42E 00-0.23688E 00-0.2293_E 00-0.22180E 00-0.21_27E 00-0.20673E 00-0.19920E 00-0.19168E 00-0.18415E 00-0.17663E 00-0.16911E 00-0.16159E 00-0.15_08E 00-0.14656E 00-0.13905E 00-0.13155E 00-0.1240_E 00-0.11654E 00-0.1090;E 00-0.10154E 00-0.94037E-01-0.86537E-01-0.79034E-01-0.71528E-01-0.6_015E-01-0.56;91E-01-0._8951E-01-0.413&_E-01-0.36069E-01-0.33017E-01-0.29948E-01-0.26853E-01-0.23729E-01-0.21363E-01-0.19763E-01-0.18146E-01-0.16506E-01-0.1_833E-01-0.13110E-01-0.11302E-01-0.93693E-02-0.77677E-02-0.64879E-02-0.53333E-02-0,43923E-02-0.37712E-02-0.3_932E-02-0.32;17E-02-0.2_lgQE-g2-0.27048E-02-0.24173E-02-0.21846E-02-0.20137E-02-0.18393E-02-0;.16S29E-02
VE0.10282E0.113q7E0.11731E0.12094E0.12_23E0.12655E0.12819E0.12954E0.13075E0.13189E0.13298E0.13q0;E0.13507E0.13607E0.13704E0 13801E0 13895E0 13989E0 lq081E0 14171E0 14262E0 14352E0 1_442Eo 1_533E0 14624E0 14715E0 1_806E0.1_896E0.1_985E0.15072E0.15157E0.15237E0.15314E0.1§383E0.15_IE0.15483E0.15500E0.15;78E0.15_26E0.15380E0 15308E0 15196E0 15022E0 1_830E0 1_666E0 l_60E0 1_207E0 13891E0 13_73E0 12866EO 1195_E0 10892E0 98295E0.87_17E0.77850E0,71259E0.682_8E0.6559_E0.62800E0.59880E0.56913E0.54569E0.52861E0.51209E0.49522E
TE03 0.26357E 0303 0.26242E 0303 0.26198E 0303 0.26155E 0303 0.26115E 0303 0.26086E 0303 0.26065E 0303 0.260_8E 0303 0.26032E 0303 0.26017E 0303 0.26003E 0303 0.25989E 0303 0.25975E 0303 0.2§962E 0303 0.25949E 0303 0.2§93§E 0303 0.25922E 0303 0.25909E 0303 0.25896E 0303 0.25884E 0303 0.25871E 0303 0.25858E 0303 0.2§845E 0303 0.25832E 0303 0.25819E 0303 0.25806E 0303 0.25792E 0303 0.25779E 0303 0.25766E 0303 0.257_3E 0303 0.257_0E 0303 0.25728E 0303 0.25716E 0303 0.25706E 0303 0.25697E 0303 0.25690E 0303 0.25688E 0303 0.25691E 0303 0.25699E 0303 0.25706E 0303 0.25717E 0303 0.25734E 0303 0.25760E 0303 0.25789E 0303 0.25813E 0303 0.25843E 0303 0.25879E 0303 0.25923E 0303 0.25980E 0303 0.26059E 0303 0.26172E 0303 0.26293E 0302 0.26_02E 0302 0.26503E 0302 0.26_81E 0302 0.26630E 0302 0.26651E 0302 0.26669E 0302 0.26687E 0302 0.26704E 0302 0.26722E 0302 0.2673_E 0302 0.26744E 0302 0.26752E 030Z 0.26761E 03
PRESS0.94482E 050.93052E 050.92506E 050.91976E 050.91482E 050.91129E 050.90874E 050.90664E 0S0.90673E 050.90292E O50.90117E 050.89946E 050.89779E 050.89617E 050.89_57E 050.89298E 050.89141E 050.88985E 050._8831E 050.88677E 050.8852_E 050.88371E 050.88216E 050.88061E 050.87903E 050.87745E 050.87585E 0S0.87426E 050.87270E 050.87115E 050.86966E 050.86821E 050.86684E 050.86559E O50.86_54E 050.86379E 050.86348E 050.86388E 050.86482E 050t86565E 05
0.8669_E 050.86895E 050.87205E 050.87543E 050.87833E 050.88186E 050.88618E 0S0.891_8E 050.89835E 050 90801E 050 92182E 050 93678E 05o 95052E 050 9632_E 050 97328E 05o 97956E 050 98226E 050 98_54E 050 98685E 050 98915E 050 99139E 050 99308E O50 99427E 050 99538E O50 99648E 05
b. Calculated surface characteristics (continued)
Figure 6.4: continued
RA0 12469E 010 12334E 010 12282E 010 12231E 010 12185E 010 12151E 010 12127E 010 12107E 01o 12088E Olo 12071E 010 12054E 01o 12038E Olo 12022E 010 12007E 010 11991E 010 11976E 010 11961E 010 11946E 010 11931E 010 11917E 010 11902E 010 I1887E 010 I1872E 010 I1857E 010 I1842E 010 I1827E 010 IISIIE 010 I1796E 010 I1781E 010 I1766E 010 11752E 01o I1738E Ol0 I1725E 010 I1713E 010 I1702E 010 I1695E 010 I1692E 010 I1696E 01o 11705E 010 I1713E 010 11726E 010 117_5E 010 11775E 010 11807E 010 11835E 010 11869E 010 I1911E 010 I1962E 010 12027E 010 12120E 010.12251E 010.12393E 010.12522E 010.12642E 010.12736E 010.1279_E 010.12820E 010.12841E 010.12862E 010.12884E Ol0.12905E 010.12920E 010.12931E 010.129_2E 010.12952E 01
SEGLEHGTH0 30523E-020 30449E-020 30395E-020 60676E-020 75710E-020 75615E-020 75554E-020 75515E-020 75486E-020 75461E-020 75438E-02o 75ql_E-020 75391E-02o 75367E-02o 75343E-02o 7531_E-02o 75292E-020 752C6E'320 75240E-020 75214E-020 75187E-020 75160E-020 75135E-020 75110E-020 75085E-020 75062E-020 75041E-020 75023E-020 75009E-020 75002E-020 75001E-020 75012E-020 75041E-020 75089E-020 75171E-020 75301E-0Z0 75504E-020 75829E-020 30_69E-020 30580K-OZ0.30799E-020.3109_g-020.31386E-020.15939E-020.16068E-020.16265E-020.16§36E-020.1692].E-020.17543E-020.18612E-020.2004_E-020.11989E-020.13607E-020.94852E-030.93358E-030.30853E-030.24737E-030.25563E-030.26787E-030.28247E-030.29266E-030.17260E-030.16919E-030.17971_E-030.1931]E-03
77
5EG
66676869707172737c_757677";8
8O8182838_8586878859909Z92939K,9596979899
10010110210310qI05106107108109110111112113
116117113
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0.00000
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0.00000
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0.00000
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SEG
L
2
3
5
57
8
9
I0
ii
1213
It
1516
17
18
19
2O
S-0 30721E 00-0 30_16E 00-0 30112E 00-0 Z9656E 00-0 2897qE 00-0 28Z18E 00-0 27_62E 00-0 26707E 00-0 25952E 00-0 25197E 00-0 2_2E 00-0 Z3588E 00-0 2293_E 00-0 22180E 00-0.21_27E 00-0.20673E 00
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6. Calculated surface characteristics (continued)
Figure 6.4: continued
TSURF DICE
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ORIQINAL PAOg I_
OF POOR QUALITY
78
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3O313233343536373839_0
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FFRAC0 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 0l0 10000E 01o 10000E 010 10000E 010 10000E 010 10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 0l0.88732E O00.42148E O00.40227E 000.39408E 000.39295E O00.39869E 000.61536E 000.28732E oo0.30615E 000.32831E 000.36170E 000.q0815E 000.47513E O00.57669E 000.78796E 000.78804E 000 57703E oo0 q7567E 000 60883E 000 36252E 000 32923E 000 30516E 0o0.28861E 000.q1691E 000.40052E 000.39510E 000.39660E 000.60533E OO0.62509E 000.89146E 000.10000E 010.10000E 010ol0000E 01O.10000E 010.10000E 010.10000E O10.10000E 010.10000E 010.10000E 010.10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 0l0 10000E 010 10000E 0l0.10000E 010.10000E 010.I0000E 010.10000E 010.I0000E 010.10000E 010.10000E 010.10000E 010.10000E 010.10000E 010.I0000E 010.10000E 01
0.10000E 010,10000E 010.10000E 010,10000E 010.10000E 01
0.35791E0.35791E0.35791E0.35791E0.35791E0.35791E0,35791E0.35791E0.35791E0.35791E0.35791E0.35791E0.35791E0.35791E 030.35791E 050 35791E O30 35791E 030 35791E 030 35791E 030 35791E 030 35791E 03o 91700E 030 91700E 030 91700E O3o 91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 050,91700E 030.91700E 030.91700E 050.91700E 030.91700E 030.91700E 030.91700E 030.91700E 050.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.9170QE 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030.91700E O30.91700E 030.91700E 030.9£700E 030.91700E 030 91700E 030 91700E 030 91700E 030 91700E 030 91700E O30 91700E 030 91700E 030 91700E 030 91700E 050 91700E O30.91700E O30.91700E 050.91700E 030.91700E 030.91700E 030.91700E 030.91700E 030,35791E 030.35791E 030.35791E 030.35791E O30.35791E 030.35791E 030.35791E 030.35791E O30.35791E 030.35791E 030.35791E 030.35791E 050.35791E 030.35791E 030.35791E 050.35791E 030 35791E 03o 3579IE O30 35791E 030 35791E 030 35791E 030 35791E 03
TSURF03 0 0000003 0 0000003 0 0000003 0 0000003 0 00000O3 o o0ooo03 0 ooooo03 0 0000003 0 00000O3 0 0oooo03 0 0000003 0 0000003 0 00000
0 000000 000000 000000 000000 000000 000000 00000o ooooo
0.26639E O30.26684E 030.26716E 030 26737E 030 26757E 030 26777E 030 26807E 030 26838E 03o 26872E O30 26924E 030.26982E 030.27040E 030.27150E 030.27315E O30.27315E 050.27315E 030.27315E 030.27315E 030.27315E 030.27315E 030,27315E 030.27315E 030.27315E O30 27315E 03o 27315E 030 27315E 03o 27315E 030 27315E 030 Z7315E 030 27315E 030 27315E 030 27315E 05o 27315E O30 27315E O30 27315E 030.27315E 030.27315E 030.27315E 030.27315E 030.27315E 030.27313E 030.27315E 030.27315E 030.271_6E O30.27039E 030.Z6981E 030.26924E 030.26872E O30.26838E 030.26807E 030.Z6778E 030.26758E O30.26738E 050.26718E 030.26687E 030.26643E 03
0.000000.000000.000000.000000.000000.000000.000000.00000
• 0.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.000000.00000
b. Calculated surface characteristics
Figure 6,4: continued
(continued)
ORIGINAL PAGE iS
OF POOR QUALITY
DICE0.000000.000000.000000.000000.000000.000000 000000 000000 000000 000000 000000 ooooo0.000000 000000 000000 000000 000000 000000 0013000 000000 00000
0.Z8542E'-030.47277E'-030.6X_21E'-030.7121QE'-030.80957E'-030.90842E'-030.10594E"020,1Z200E'-020.1388_E--020 16359E--020 18605E'-020 20388E"02o 23969E--020 27681E--02o 26091E--020 25127E--020 2_413E-'020 23660E"02o 2Z883E-O_
.221_5E-02.21577E-02.21159E-0_
0.20815E-020.20520E-020.20277E-020.20175E-020.20275E-020.20302E-020,20302E-020.20272E'-020.20171E-020.20272E.-020.20515E-020.20808E"020 21152E"020 21570E"020 22138E"020 22875E"020 23652E'-020 24403E-'020 25119E"020 26087E"020 27677E"OZo 23770E--020.203_4E-020 18573E-'020 16344E-'020 1388_E-'020 1221_E--020 10622E"020 91076E"030.81371E-.030.71802E-.030.62290E-'030.q8306E-'030.29912E-.03
0 000000 000000 000000 000000 00Q000 000000 000000 000000 000000 000000 000000 00000o oooooo ooooo0.000000.000000.000000.000000.000000.000000.000000.00000
79
SEG12012i122J23
125126127128
13113223313_135136137138
s0.I8415E 00
0.19167E 000.19920E 000.20673E 0o0.21q27E 000.22180E O00.2293qE O00.2_688E oo0.2_4_2E 000.25197E O00.25951E 000,26706E 000.27q62E 000.28218E O00.2897_E O00.29656E 000.30112E 000.30_16E 000.30721E 00
HTC0.56370E0.55383E0.54_2_E0.53492E0.52580E0.S1689E0.5081qE0._99_4E0._9077E0.q8216E0.473_9E0.46¢60E0.45518E0.q_42_E0_2981E0._1048E0.39015E0.36936E0,31_66E
XK03 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0j_35000E-0303 0'.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-0303 0.35000E-03
BETA0.000000.000000.000000.00000o oooooo ooooo0 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.000000.00000
FFRAC0 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010 10000E 010.10000E 010.10000E 010.10000E 0l0.10000E 0I0.10000E 010.10000E 010.10000E 010.I0000E 010.10000E 010.10000E 010.10000E 010.10000E 01
RZ0 3579iE0 35791E0 35791E0 35791E0 35791Eo 35791E0 35791Eo 35791E0 35791E0 35791E0.35791E0.35791E0.35791E0.35791E0.35791E0.35791E0.35791E0.35791E0.35791E
03030303030303030303
b. Calculated surface characteristics (continued)
Figure 6.4: Concluded
0303030,30303030303
TSURF0.000000,000000.000000.000000.000000.000000.000000 000000 000000 00000o oo0ooo oo0ooo oooooo.oooooo.oooooo.oooooo.oo0oo0.000000.00000
DICE0.00O000.000000,000000.000000 000000 000000 000000 000000 000000 000000 000000 000000 000000.000000.000000.000000.00000O.000000.00000
ORIGINAl/PAGE IS
OF POOR QUALITY
8o
0._
Y O,O
-.2
_(LC_ITY (N'$) 129.00
T_MP(R_TUR[ (C) -[2.60
P_ESSU_ (KPA) 90.76
L_C fG/H--3) 0.50
_P Dl_H (_CRONS) 20.G0
TIME ($EC) 0.00
a°
O
X
Trajectory of particle released from YOMAX
J
Q.Z
0.0
-.2
#ELC31TY (H,'S_ 127.00
TEmPERaTURE (C> -t2.60
_U_IDITY (_) I00.00
_ _3,:_q-3) 0.50
_3P OI_M (MICRONS) 20.$0
TIM[ (S_C) 0.00
o
x
b. Trajectory of particle released from YOMIN
Figure 6.5: Examples of droplet trajectory plots from Example 1.
81
4').C
_:ELCglTf <N,'S_
TE_F_TU_E (C)
5_EP Ol_H f_ICRON$)
129.00
-12.60
90._5
lO0.OO
0.50
20.00
0.00
YO= 0o00000
S = 0.00000
I
C°
o
x
Trajectory released from YOMAX'I'YOMIN2
0.2
0.0
-°_ .
MELC_ITY (.M/S) 129.00
TEHPER_TUQ[ (C) -12o60
F_!.SSUq_ (KPA) 90.75
HUHIDITY (_) I00.O0
LXZ (_/H..3) O.SO
C_CP 0[_M (MICRONS) 20.GO
TIME (SEC) 0.00
IIt[
j ......
ttJ
0 v
d. Trajectory calculated while searching for the upper impingement limit.
Figure 6.5: continued
82
ORIGINAL PAGE' IS
OF POOR QUALITY
#EL:;|TY CM/S) ]29.0Q
TEMPER_TUQ[ (C) -12.60
-C_I3]TY (_) 100.00
_P DIeM (MICRONS) 20.GO
":HI (SEC) O,CO
D.2
010 ""
IW= 2
YO= 0,00_50
S - 0,0Z979
II
J ,
I
I
_______-I j
IfJ
e. Trajectory calculated while searching for the upper impingement limit.
Figure 6.5: Concluded
83
NACA 0012 : EXAMPLE 1
VELOCITY (N/S) 129._6
TENPERATURE (C) -12.60
PRESSURE (KPA) 90.75
HUMIOITY (X) IO0.O0
LWC <G/M=-3) O.SO
OROP OIaM (MICRONS) 20.00
TIME (SZC) bO.O0 ORIGWAL PAGE IS
POOR QUALITy
a. Percent plotted = 100%
NACA 0012 : EXAMPLE 1
VELOCITY (H/S) IZg.q6
IEHPERAIU_E (C) -IE.60
PRESSUnE (KPA) 90.75
HUMIDITY (X) IO0.O0
LWC (G/H=-3) O.SO
DROP O/AN (N|_RONS) 20.00
TIME (SEC) 60.00
b. Percent plotted = 50%
Figure 6.6: Size of the plotted geometry as a function of the percent plotted.
84
NACA 0012 : EXAMPLE I
VELOCITY (H/S) 129.96
IEHPERATURE (C) -12.60
PRESSURE (KPA) 90.75
HUNIDITY (X) |00.00
L_C (G/H--3) 0,50
DROP O|A_ (NICRON$) 20.00
lIME (SEC) 60.00
c. Percent plotted = 25%
Figure 6.6: Concluded
85
a. Iced airfoil geometry
VELOCITY (M/S)
TEMPERATURE (C)PRESSURE (KPA)HUMIOITY (%)
LHC (G/M--3)DROP OIAM (MICROTIME (SEC)
129._6-12.&O
90.75!00.00
0.50N)20.O0
60.00
ORIGINAL PAGE IS
POOR QUALITY
20C -
L150 [-
I6Q _-
1_0 L
=_loo I
I60 F
.o,k
'°i_.35 -°'28 -o=21 -,li_ -o'07 -.;OO 0°;07 0o;!_ 0721 O*:2B O. '_=;
S (M;
d. Edge velocity vs. su_ace location
O.OIC_
0.008
O.OOe
0.00 _
_c 0.002
0.000
o-.00;
-o00'
S (M)
b. Particle release position vs. surfaceimpact distance
ioo m l
i \
"-:2 1
-!8 _
i ......
"2_,'_5 -,28 -.'2; .oT -.io0 0.0; 0.I ° 0,21 O.'2B 3.'35
S (WI
e. Edge temperature vs. surface location
I.O ff I13 _"/ i
°' i ;°'F0.6 :3" ;'"
0.7 . ;3; ,-
t
Lp
0.,, f qe _"
== 0._ 'P2
0.3 e9
0.2 I 6c
o., I e-_-e;.l_ s ' , , , , ,0. O. 0,_ 0 ! 1 0. i_ ._,0 -._'6 -.21 -.1_ ..T? ..tO0 0 .:_. 7 0 • : '_" _..Z: 0._5 _.._5
S (M) S (_')
c. Local collection efficiency vs. surface f. Edge pressure vs. surface location
location
Figure 6.7 Icing parameter plots for the first timestep of Example i.
86
ORIGINAL PAGE IS
OF POOR QUALITY,VELOCITY (M/S) 129._6TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75HUMIDITY (%) 100.00LWC (G/M--3) 0.50OROP OlAM (MICRON)20.O0TIME (SEC) 60.00
ni
.:.L
.=_61r
-7 _-
.;_.%_ I ' I ' ' '-.E_ °?El -.'1_' -.'? -.CO O.O7 C..l_" C._ C,._8 C.'35
S (H)
g. Equilibrium surface temperature vs.surface location
ORIGINAE PAGE IS
OF POOR QUALITY
1000 E90C ,
800 r
?00 ]-I
z bO= ,_
_ 50G L
300
IOC :-
j*
J
i , , 1 • .C.'3_ -.2e - .2_ -.]', -.37 .130 C.J; o.J'* 0._1 0.Te "_.3 _.
S (M)
Ice density vs. surface location
1500
;200
]050
900
75G
z600
300
150
O°
h.
j,J
! ,i ' '
5 12_ -.f2; ._:_ -.POT -.OC O.r07 0.I _" O,'ZJ 0.2_ G,13S
S (P)
Convective heat transfercoefficient
vs. surface location
.00050
.000_5
.000_0
.00035
.00030
w. OOO2S
.00020
.00015
.00010
.00005
.oooqo
i°
-.126 -.!21 ..114 ..107 ..100 O.]OF 0._1_ 0.121 O,!ZB 0.135
$ (M)
Equivalent sand-grain roughness
height vs. surface location
I0 kC.9
C'7 F
O.a._-
I0.5 P"
: I
c.2r-
IC,; _
I
C t
k°
-.C;24 - .OG6 0.=C6 G.G2- 0.0_0
S (M)
Freezing fraction vs. surface location
Figure 6.7: Concluded.
87
Chapter 7
EXAMPLE CASES
In this section, the capabilities of LEWICE are illustrated through the
presentation of five example cases. These examples include the input data
sets and the printed and plotted output data; however, printed output is
included for example 1 only.
7.1 Example 1: Glaze Icing on a NACA 0012 Airfoil, a -- 0.0 °
In this example, a 2-minute glaze ice accretion will be formed on a NACA
0012 airfoil at an angle of attack of 0.0 degree. The accretion will be formed
in two l-rain timesteps. The icing conditions are shown below:
Velocity
Static Temperature
Static Pressure
LWC
Droplet Diameter
Roughness Height
= 129.46 m/s
= 260.55 K
= 90748.0 Pa
= 0.50 g/m s
= 20.0 microns (monodispersed cloud)
= 0.00035 m
The input file and the interactive input for the first timestep in Example
1 are shown in Figures 7.1a and b, respectively. Plot option 3 was selected
in the interactive input, therefore, the particle trajectories and icing pa-
rameters were plotted. Figures 6.5a-e show the first five particle trajectory
plots from this example case. Figures 6.5a and b show the trajectories of
particles released from YOMAX and YOMIN. As discussed in Chapter 5,
these trajectories are calculated to identify the release point of a particle
that passes above the body and one that passes below the body. These
calculations are performed in subroutine RANGE.
After locating an upper and lower boundary trajectory, the search for
the upper and lower impingement limit is begun by releasing a particle
from a position halfway between the release points of the two trajectories
identified in Figures 6.5a and b. When a particle impinges on the body,
88
the particle number (IW), particle release ordinate (Y0), and the surface
impact distance (S) are displayed, as shown in Figure 6.5c. Using the
Newton iteration scheme described in Chapter 4.2.6, the search for the
upper impingement limit is continued, as shown in Figures 6.5d and e.
These calculations are performed in subroutine IMPLIM. When plot option
3 is selected, all of the trajectories will be plotted. Only the first five have
been shown in this example.
After calculating the particle trajectories, the program will prompt the
user to preview the Y0 vs. s data or to continue with the collection emciency
calculation with the following statement.
ENTER 1 TO PREVIEW Y0 VS S DATA
ENTER 0 TO CONTINUE WITH THE COLLECTION EFFICIENCY
CALCULATION (II)
Ifoption 1 isselected and the axes limitsare specifiedas follows:
smin = -0.04 smax = 0.04
y0min = -0.01 yomax = 0.01
the Yo vs. s points calculated in subroutine COLLEC will be plotted as
shown in Figure 7.2. Upon producing the plot, the following statement will
be printed on the screen:
THE CALCULATED SURFACE IMPACT DISTANCES iS) AND
RELEASE POINTS (Y0) ARE AS FOLLOWS
I Y0 S I Y0 S
1 0.00850 0.03378 10 -0.00109 -0.00178
2 0.00765 0.02078 11 -0.00218 -0.00355
3 0.00656 0.01489 12 -0.00327 -0.00555
4 0.00546 0.01090 13 -0.00436 -0.00797
5 0.00437 0.00801 14 -0.00545 -0.01085
6 0.00328 0.00557 15 -0.00654 -0.01484
7 0.00219 0.00357 16 -0.00763 -0.02072
8 0.00110 0.00180 17 -0.00848 -0.03167
9 0.00001 0.00001 18 0.00000 0.00000
HOW MANY TRAJECTORIES ARE TO BE DELETED BEFORE
THE COLLECTION EFFICIENCY CALCULATION? (12)
89
At this time, Y0 vs. s points can be removed, if necessary. Non-
physical impact locations can occur when inaccurate flow fields are cal-
culated around the horns of glaze ice accretions. In this example, it is not
necessary to remove any points, so option 0 was selected.
The title of the run, icing condition parameters, ice accretion data, and
parameter plot menu are then printed on the screen as follows:
NACA 0012 : EXAMPLE 1
ICING CONDITION:
STATIC TEMPERATURE (C)
STATIC PRESSURE (PA)
VELOCITY (M/S)
LWC (G/M s)
DROPLET DIAMETER (MICRONS)
ICE ACCRETION DATA
STAGNATION POINT
TRANSITION POINTS (LOWER,UPPER)
ICING LIMITS (LOWER,UPPER)
NUMBER OF POINTS
NUMBER OF SEGMENTS ADDED
AVAILABLE PLOT OPTIONS
0 - NO PLOTS
1 - ICED GEOMETRY
2 - ZVSS
3 - BETA VS S
4 - VE VS S
5 - TE VS S
6 PE VS S
7 - TSURF VS S
8 HTC VS S
9 - XK VS S
10 - ICE DENSITY VS S
11 - FFRAC VS S
ENTER OPTIONS NUMBER (12)
: TIME = 60.000 SEC
260.55
9O748.OO
129.00
0.50
20.00
70
68 71
42 97
139
0
9O
All of the parameter plots for the first time-step are shown in Figures
6.7a-k. When the option for no plots is selected, the computer will respond
with the following message:
TIME STEP COMPLETE: TIME - 60.0
ICING TIME INPUT HAS BEEN REACHED
PROGRAMS OPTIONS
1 - CONTINUE ICING, USE PREVIOUS FLOW FIELD
2 - CONTINUE ICING, CALCULATE NEW FLOW FIELD
3 - TERMINATE PROGRAM
Since a second 1-min timestep with a new flow field calculation is desired,
option 2 is selected.
The second timestep proceeds in a manner similar to the first. The
plots, computer prompts, and responses are shown in the order of their
occurrence in Figure 7.3. The printed output from the first timestep in
this example is shown in Figures 6.1-6.4. The icing parameter plots for the
second timestep are shown in Figure 7.4a-k. The printed output for the
second timestep is shown in Figure 7.5.
The overall accuracy of LEWICE is checked by comparing calculated
and experimental ice accretion shapes. The experimental ice accretion for
the condition was obtained by Gent (Reference 20), and is compared to the
calculated shape in Figure 7.6.
7.2 Example 2: Glaze Icing on a NACA 0012 Airfoil, a : 4.0 °
This example is identical to Example 1 except that the airfoil is now at a
4.0 angle of attack. The icing time for this condition is also 2-minute and
the accretion is formed in two 1-minute timesteps. The input file is shown
in Figure 7.7. Note that the value of CLT in namelist $24Y is now equal
to 4.0.
Figures 7.8 show the particle trajectories calculated in subroutine
RANGE, where the program searches for a trajectory that passes above
91
and below the body. More accurate selections of YOMIN and YOMAX
would have resulted in fewer trajectoriesbeing calculated while the code
searches for the two boundary trajectories.The firstthree trajectoriescal-
culated in subroutine IMPLIM are shown in Figures 7.9. These trajectories
are calculated while the program was searching for the upper surface im-
pingement limit.No additional trajectorieswillbe shown for thisexample,
but alltrajectorieswillbe plotted when plot option 3 is selected. The Y0
vs. s points calculated in subroutine COLLEC are shown in Figure 7.10.
After the plot iscompleted, the following prompts are printed to the screen
to allow the user to remove any incorrect points"
THE CALCULATED SURFACE IMPACT DISTANCES (S) AND
RELEASE POINTS (Y0) ARE AS FOLLOWS
I Y0 S I Y0 S
1 -0.11162 0.01610 10 -0.12296 -0.00836
2 -0.11263 0.01042 11 -0.12425 -0.01156
3 -0.11392 0.00727 12 -0.12554 -0.01528
4 -0.11521 0.00473 13 -0.12683 -0.01979
5 -0.11650 0.00276 14 -0.12812 -0.02534
6 -0.11779 0.00081 15 -0.12942 -0.03270
7 -0.11908 -0.00103 16 -0.13071 -0.04386
8 -0.12037 -0.00315 17 -0.13171 -0.06252
9 -0.12167 -0.00561 18 0.00000 0.00000
HOW MANY TRAJECTORIES ARE TO BE DELETED BEFORE
THE COLLECTION EFFICIENCY CALCULATION? (12)
As in Example 1, option 0 was selected because it was not necessary to
remove any points. The program then entered displays the plot menu to
the screen, and the plots shown in Figures 7.11a-i were obtained. The
results of the first timestep are similar to those obtained in Example 1.
After plot option 0 was selected,the prompts for the program option
were printed, and, as in Example 1, option 2 was selected.The plot option
was not changed from the firsttimestep and the calculationof the potential
flow fieldwas begun. When the program entered subroutine STAG, itwas
found that two "stagnation points_ had been calculated. This is indicated
by the following message and prompt:
92
2 STAGNATION POINTS HAVE BEEN CALCULATED. ENTER 1
TO SHOW THE LOCATIONS OF THE CALCULATED STAGNATION
POINTS. ENTER 0 TO DISPLAY OPTIONS.
When this situation occurs, it may be necessary to form a pseudo-surface
over the region where the multiple stagnation points exist. The procedure
to form the pseudo-surface is described in the following section. Appendix C
discusses additional causes for the calculation of multiple stagnation points.
T.2.1 Application of the Pseudo-Surface
In normal operation, select option 1 to display the locations of the stagna-
tion points. The locations of the stagnation points are indicated by X's, as
shown in Figure 7.12. After displaying the plot, the x, y, and s locations
of the stagnation points will be displayed, and the user will be asked either
to select one of the points for use as the stagnation point in the remaining
calculations, or to form the pseudo-surface.
THE FOLLOWING MULTIPLE STAGNATION POINTS HAVE
BEEN CALCULATED
I X Y S
57 - 0.00089 - 0.00336 0.00123
59 - 0.00111 - 0.00309 0.00172
AVAILABLE OPTIONS
0 - CONTINUE CALCULATIONS WITH MANUALLY-SELECTED
STAGNATION POINT
1 - RECOMPUTE FLOW FIELD USING A PSEUDO-SURFACE
In this example, option 1 was selected.
In Figure 7.12, the axes scales were such that it was difficult to identify
the locations of the stagnation points. Therefore, the user will be asked if
the plotting scales should be changed to enlarge the region of interest. In
this example, the axes limits were changed as shown below:
z._ffi= y,_, = 0.02
z_. = y._. = -0.02
93
The locations of the stagnation points will then be re-plotted using the new
axes limits, as shown in Figure 7.13.
The circular arc that will be placed over the multiple stagnation points
is defined by specifying two points on the arc and the radius. The two
points on the arc are the locations where the pseudo-surface intersects theactual ice surface. The best results are obtained when the ends of the
pseudo-surface arc intersect on a tangent to the ice surface. Figure 7.13
shows that this may be possible near y values near -0.006 and -0.001. These
values are input by the user as shown below:
ENTER THE Y COORDINATE OF THE DESIRED LOWER
LIMIT OF THE PSEUDO-SURFACE (F10.0)
-.006
ENTER THE Y COORDINATE OF THE DESIRED UPPER
LIMIT OF THE PSEUDO-SURFACE (FI0.0)
-.001
The computer willrespond with the two body coordinates closestto the
desired upper and lower limitsas shown below:
THE POINTS CLOSEST TO THE LOWER LIMIT ARE
X= 0.0019641 Y=-0.0065025 I= 52
X= 0.0012161 Y= -0.0055978 I= 53
THE POINTS CLOSEST TO THE UPPER LIMIT ARE
X= -0.0028274 Y= -0.0010464 I-- 74
X= -0.0029714 Y= -0.0008570 I= 75
The user is then prompted to enter the segment number of the desired upper
and lower limits. In this example, segments 52 and 75 were selected as the
lower and upper limits of the pseudo-surface, respectively. The program
will then request that a radius be input. In this example the radius is 0.03.
The input of these values is shown below.
ENTER THE I VALUE OF THE DESIRED LOWER AND UPPER
LIMITS (213) 52 75
ENTER THE DESIRED RADIUS (F10.0) .03
Because the selectionof an appropriate radius isa manual iteration,there
are no general criteriafor selecting a radius. If an arc with the desired
94
radius cannot be formed between the two points specified, the program will
respond by asking for another radius. The iced airfoil with the pseudo-
surface will then be plotted, as shown in Figure 7.14. After the plot is
completed, the following menu is displayed:
THE FOLLOWING OPTIONS ARE NOW AVAILABLE (11)
0 - SPECIFY NEW UPPER AND LOWER LIMITS
1 - SPECIFY A NEW RADIUS
2 PSEUDO-SURFACE SATISFACTORY, CONTINUE
CALCULATIONS
3 PSEUDO-SURFACE UNSATISFACTORY, CONTINUE
CALCULATIONS
WITH THE ACTUAL ICE SURFACE
At this time, new upper and lower limits or a new radius can be selected,
and the above procedure will be repeated. Option 2 will cause the pro-
gram to re-calculate the flow field using the pseudo-surface. Option 3 is
selected when a satifactory pseudo-surface cannot be formed and any errors
in the flow field must be accepted. In this example, the pseudo-surface was
satisfactory, therefore, option 2 was selected.
While it did not occur in this example, multiple stagnation points may
still be calculated after the pseudo-surface has been formed. Unless a
smoother pseudo-surface can be formed, it is usually best to select one
of the points and continue with the calculations. Select the point that is
closest to the stagnation point calculated in the previous timestep. This
point can be identified by the value of surface distance, s. (Recall that s =
0.0 denotes the stagnation point.)
In this example, a single stagnation point was calculated when the
pseudo-surface was placed on the iced surface, and the second timestep
proceeded in a manner similar to the first. It was not necessary to remove
any Y0 vs. s points from the plot shown in Figure 7.15 when the following
prompt was displayed:
HOW MANY TRAJECTORIES ARE TO BE DELETED BEFORE
THE COLLECTION EFFICIENCY CALCULATION? (12)
The plots obtained from the plot menu for the second timestep are
shown in Figures 7.16a-i. The calculated airfoil shape is compared to the
95
experimental ice accretion shape, obtained from Reference 20, in Figure
7.17.
7.3 Example 3: Rime Icing on an NACA 0012 Airfoil, a = 0.0 °
In this example, ice will be accreted on an NACA 0012 airfoil at an angle
of attack of 0.0 for 2 min. As in Examples 1 and 2, the accretion will
be formed in two l-rain time steps. The icing conditions, which should
produce a rime ice accretion, are as follows:
Velocity
Static Temperature
Static Pressure
LWC
Droplet Diameter
Roughness Height
= 64.73 m/s-- 260.55 K
- 90748.0 Pa
= 0.50 g/m s
= 20.0 microns (monodispersed cloud)
= 0.00025 m
The input file for this example is shown in Figure 7.18.
The program executes in a manner similar to Example 1. The parameter
plots for the first and second timesteps are shown in Figures 7.19a-i and
7.20a-i, respectively. The predicted ice accretion shape is compared to the
experimental shape (Reference 20) in Figure 7.21.
As discussed in Section 4.3.1, the difference between rime and glaze ice
is determined by the calculated value of the freezing fraction, f (FFRAC in
LEWICE). Figure 7.19k shows that the freezing fraction was equal to 1.0
over the entire surface for the first timestep. This would be indicative of a
solid rime ice accretion. On the second timestep, the freezing fraction was
slightly less than 1.0 near the stagnation point, as shown in Figure 7.20k.
This indicates that the accretion is starting to take on some glaze ice accre-
tion characteristics in that region, and would therefore constitute a mixed
ice accretion. Glaze characteristics become more evident as the freezing
fraction approaches 0.0. Experimentally, these initial glaze characteristics
would probably not be observed until the ice accretion grew larger and the
size of the glaze portion increased.
96
7.4 Example 4: Specification of a Droplet Size Distribution
The atmospheric conditions in this example are identical to those in Ex-
ample 1. However, in this example, a droplet size distribution was used to
characterize the icing cloud instead of a single droplet size. The icing time
for this case is 60.0 sec, and the ice will be accreted in a single timestep.
The droplet size distribution was specified to have a normal volume
(mass) distribution with a mean of 20 microns and a = 5, as shown in Figure
7.22. As discussed in Section 4.2.5.1, the droplet size distribution is input
into the code by specifying the mass fraction corresponding to a discrete
droplet diameter. The procedure for quantifying a known distribution for
input into LEWICE is discussed below.
The volume fraction (fraction LWC) corresponding to each droplet size
used to produce Figure 7.22 is shown in Table 7.1. The cumulative volume
fraction (CVF) is calculated for each droplet size, d_, using the equation
CVF_ = CVF(__I) + VI: (29)VVS,
The resulting plot of CVF vs. d is shown in Figure 7.23. For input
into LEWICE, the droplet size range must be divided into a number of
discrete droplet size bins of a constant width. The size of the bin width is
arbitrary, but no more than 10 bins can be input to the code. Using more
bins will increase the accuracy of the calculations but will also increase
computational time. Five bins with a width of 8.0 microns were used in
this example. The droplet diameter corresponding to the middle and the
right-hand side of each bin is shown in Table 7.2.
97
Table 7.1 Volume Fraction for a Normal Mass Distribution of
Droplet Size with a Mean of 20mm and a -- 5
d (microns) Volume Fraction
0 0.0000
2 0.0002
4 0.0010
6 0.0032
8 0.0090
10 0.0216
12 0.0444
14 0.0776
16 0.1158
18 0.147"4
20 0.1596
22 0.1474
24 0.1158
26 0.0776
28 0.0444
30 0.0216
32 0.0090
34 0.0032
36 0.0010
38 0.0002
40 0.0000
The cumulative volume fraction at the right-hand side of each bin must
be determined using the data in Table 7.1 and Figure 7.23 using the fol-
lowing equation:
vs, = CVF, - CV F _I (30)
This volume fraction is assigned to the droplet size at the middle of the bin
and assumes a uniform distribution of droplets inside the bin. The values
of V/, for each droplet size bin are shown in Table 7.2. This data is input
into LEWICE using namelist DIST, as shown in Figure 7.24.
98
Table 7.2 Volume Fraction for Each Droplet Size Bin Specified in
Example 4
Bin Droplet Diameter Cumulative Volume
Middle Right-Hand Volume Fraction
Endpoint Fraction
1 4 8 0.0082 0.0082
2 12 16 0.2119 0.2037
3 20 24 0.7881 0.5762
4 28 32 0.9918 0.2037
5 36 40 1.0000 0.0082
When a droplet size distribution is input, the execution of the program
is similar to when a single droplet size is specified. The difference is that
the particle trajectory calculations must be performed for each droplet size
specified. Since five discrete droplet sizes were specified in this example,
the impingement limits and Y0 vs. s data were calculated for each of the
droplet sizes. This will require significantly more computational time.
This example will require user interaction when asked to preview the Y0
vs. s data. This question will be asked for each droplet diameter, and the
user will have the opportunity to remove points from each set of y0 vs. s
data. The procedure for removing the points was discussed in Example 1.
Figures 7.25a-o show the plotted output created from the plot menu.
Note that Figures 7.25b-f show the Y0 vs. s curves for each of the droplet
diameters specified. These plots are made from a single selection of plot
option 2. The user will be requested to input the axes limit for each set of
y0 vs. s data. The total local collection efficiency curve (Figure 7.25g) is
calculated by summing the contributions from each of the droplet diame-
ters, as described in Section 4.2.5.1. The local collection efficiency for each
droplet size is not stored by the program.
Recall that in Example 1, an ice accretion was formed for this same icing
condition except that a single droplet diameter of 20 microns was specified.
A comparison of the local collection efficiency from the first timestep of
99
Examples 1 and 4 is shown in Figure 7.26. The local collection efficiency
curves are similar near the stagnation point (s = 0.0). However, the region
over which droplets impinge is much greater when a droplet distribution
is specified because of the presence of the larger droplets. This result is
similar to that concluded by previous investigators (Chang, Reference 13).
The increased region of droplet impingement is also noticeable in com-
parisons among the predicted ice accretion shapes. However, because of the
small amount of mass present at the impingement limits, the effect on the
total ice accretion shape is small. These results axe not sufficient for deter-
mining the total effect of using a multidispersed droplet size distribution
to characterize an icing cloud as opposed to a monodispersed distribution.
The effect of wider distributions with similar mass median droplet diam-
eters must be evaluated. The effects must also be determined for various
types of icing conditions and ice accretions.
7.5 Example 5: Thermal Anti-lclng
The formulation of the thermodynamic equations in LEWICE allows the
surface of the body to be a heat source or sink. However, since conduction
through an existing ice layer is not modeled, the equations are valid only
on the first timestep when ice is accreted on the clean airfoil. Also, since
the melting of previously deposited ice from the surface of the body is
not modeled, the equations are not applicable to a de-icing system. They
are applicable, however, to the evaluation of a thermal anti-icing system.
This example demonstrates the capability of LEWICE to determine the
minimum thermal anti-icing heating requirements for maintaining an ice-
free surface for a specified set of icing conditions. A discussion of the
applicability of the thermodynamic model is presented in Appendix A.
The NACA 0012 airfoil evaluated in this example has an electro-thermal
anti-icing heater covering the first 20 percent of the airfoil, as shown in
Figure 7.27. A uniform heat flux of 6000.0 W/m _ was specified over the
entire surface. Lewice is to be applied to determine whether this heat flux
is sufficient to maintain an ice-free surface at the following icing condition:
Angle of attack
Velocity
= 6.0
= 128.41 m/sec
lO0
Static Temperature
Static Pressure
LWC
Droplet Diameter
Roughness Height
= 265.0 K
= 90748.0 Pa
= 0.50 g/m s= 20.0 microns
= 0.0002 m
The input file is shown in Figure 7.28. The heat flux from the surface (into
the thermodynamic control volume) is input in namelist ICE through the
variable QCOND.
The icing time for this case was arbitrarily specified to be 120.0 sec so
that any ice that did form would be easily visible on the plots. No user
interaction, except the standard responses discussed in Examples 1 and 3,
was required. As shown in Figure 7.29a, the heat input was not sufficient
to maintain an ice-free surface. The ice accretion on the lower surface was
formed as liquid water flowed off the heater and onto the colder airfoil
surface. This result indicates that it is possible for ice to form aft of the
heater but, since the shedding of water droplets from the surface are not
modeled, the amount of ice may be over-predicted. The ice accretion on
the upper surface was formed on the heater itself because the increased
velocity (Figure 7.29d) over the upper surface caused a large decrease in
the local static temperature (Figure 7.29e). It is also interesting to note
the calculated surface temperature and convective heat transfer coefficient
profiles over the surface (Figures 7.29g and h, respectively). The convective
heat transfer was at a maximum on the upper surface which, when com-
bined with the decreased local static temperature, contributed to the ice
growth. The surface temperature profile shows that the temperature was
greater than 0.0 ° C over a large portion of the heater, but was less than 0.0
over a small portion of the upper surface.
These results indicate that the heat flux should be increased in this
region to maintain an ice-free surface. The actual minimum icing require-
ment could be determined by incrementally increasing the heat input and
re-calculating the ice accretion shape. Unfortunately, there was no exper-
imental data to verify these calculations. This example was presented to
demonstrate the capability of the thermal model. It is expected that this
capability be further exercised to evaluate its accuracy.
lOl
HACA 0012 : EXAMPLE 1
_$24YILIFT= 1IPARA= 1IFIRST= 3ISECND= 3IPVOR= IIHCLT = 0CLT= 0.0/CHORD= 0CCL= 0.0IND = IISOL= 0IPRINT = 0_FLLL = I&END
1.00C0000 0.9899999 0.9800000 0.9700000 0.9500000 0.92500000.9000000 0.8750000 0.8500000 0.8250000 0.8000000 0.77500000.7500000 0.7_50000 0.7000000 0.6750000 0.6500000 0.62500000.6000000 0,5750000 0.5500000 0.5250000 0.5000000 0.47500000.4500000 0.6250000 0.4000000 0.3750000 0.3500000 0.52500000.3000000 0.2750000 0.2500000 0.2250000 0.2000000 0.17500000.1500000 0.1250000 0.1000000 0.0900000 0.0800000 0.07000000.0600000 0.0500000 0.0450000 0.0400000 0.0350000 0.03000000.0?50000 0.0200000 0,0150000 0.0100000 0.0075000 0.00500000.0037500 0.0025000 0.0022500 0.0020000 0.0017500 0.00150000.0012500 0.0010000 0,0008750 0.0007500 0.0006250 0.00050000,0003750 0.0002500 0,0001250 0,0000000 0.0001250 0.00025000.0003750 0.0005000 0.0006250 0.0007500 0.0008750 0.00100000.0012500 0,0015000 0,0017500 0.0020000 0.0022500 0.00250000.0057500 0.0050000 0.0075000 0.0100000 0.0150000 0.02000000.0250000 0.0300000 0,0350000 0.0400000 0.0450000 0.05000000,0600000 0.0700000 0.0800000 0.0900000 0,I000000 0.12500000.1500000 0,1750000 0.2000000 0.2250000 0.2500000 0.27500000.3000000 0.3250000 0.3500000 0.3750000 0.4000000 0.42500000.4500000 0._750000 0.5000000 0.5250000 0.5500000 0.5750000
0.6000000, 0.6250000 0.6500000 0,6750000 0.7000000 0.72500000.7500000 0.7750000 0.8000000 0.8250000 0.8500000 0.87500000.9000000 0.9250000 0.9500000 0.9700000 0.9800000 0.98999991.0000000 0.0000000 0.0000000 0.0000000 0.0000000 0.00000000.0000000 -0.0018740 -0.0036110 -0,0052390 -0.0082510 -0.0117000
-0.0149080 -0.0179530 -0.0208880 -0.0237590 -0.0265150 -0.0292210-0.0318550 -0.0344110 -0.0368870 -0.0392810 -0.0_15850 -0.0437950-0.0459040 -0.0479060 -0.0497930 -0.0515600 -0.0531980 -0.0546980-0.0560510 -0.0572430 -0.0582620 -0.0590900 -0,0597070 -0.0600940-0.0602260 -0.0600760 -0.0596120 -0.0587940 -0.0575700 -0.0558790-0.0536360 -0.0507320 -0.0470040 -0.0452280 -0.0432520 -0.0410380-0.0385350 -0.0356740 -0.0340820 -0.0323620 -0.0304960 -0.0284620-0.0262300 -0.0237260 -0.0207970 -0.0172480 -0.0150780 -0.0123860-0.0106990 -0.0086200 -0.00813&0 -0.0076230 -0.0070750 -0.0064850-0.0058470 -0.0051460 -0.0047660 -0.0043630 -0.0039310 -0.0034620-0.0029_50 -0.0023560 -0.0016320 0.0000000 0.0016320 0.00255600.0029_50 0.0034620 0.0039310 0.0063630 0.0047660 0.0051_600,0058470 0.0064850 0.0070750 0.0076230 0.0081360 0.00862000.0106990 0,0123860 0.0150780 0.0172480 0.0207970 0.02372600.0262300 0.0284620 0.0306960 0.0323620 0.0340820 0.03567_00.0385350 0.0410380 0.0¢32520 0.0652280 0.0670040 0.05073200.0536360 0.0558790 0.0575700 0.05879_0 0.0596120 0.06007600.0602260 0.06009¢0 0.0597070 0.0590900 0.0582620 0.05724300.0560510 0.0546980 0.0531980 0.0515600 0.0_97930 0.04790600.0459040 0.0437950 0.0415850 0.0392810 0.0368870 0.03441100,0318550 0.0292210 0.0265150 0.0237390 0.0208880 0.01795500.0149080 0.0117000 0.0082510 0.0052390 0.0036110 0.00187400.0000000 0.0000000 0.0000000 0.0000000 0.0000000 0,0000000
ETRA¢IGEPS= 0.4999999E-04DSHIFT= 0.20E-02VEPS = 0.9999999E-03LC_B= 0LC_P= 0LEQM = 1LSYM = 0L_OR= IL:<O_ = INBDY = INEQ= 4NPL = 15HSEAR = 50HSI= ITI_STP= 0.9999999E-03££ND&T_AJ2CHORD = 0.30G= 0.0PIT= 0.0PITDOT = 0.0PRATK = 0.0XORC= -4.0XSTOP= 0.50YOLIM = 0.9999999E-04YOMAX: 0.50E-01YOMXH = -0.50E-01YORC= 0.9999996E-01_EHDEDIST
FLtOC= 1.0, 9_0.0DPD= 20.0, 9w0.0CFP= 1.0, 9_0.0_£NO£ICEVIHF= ]29.460LWC= 0.50TAMB= 260.5_98PAMB= 90748.0RH= 100.0DPI'IM= 20.0XF:IHIT= 0.00035EEGTOL= 1.50
a. Input data file
Figure 7.1: Input data for Example 1
102
6036036 036O36036036 03603603603603603603603603b 0 ,36 0 36 0 3603603603603603!136 0 46 0 46 0 q
6046 0 46 0 q6046 0 c+6 0 t+6 06 0 46046 0 _6 0 4
604604604604604
6046046 0 4604I I 4
ORIGINAL PAGE IS
O_ POOR QUALITY
TIH_ = B.
ENTE_ DESIRED iCING TIME (SEC), (_le.O)
ENTER DESIRED TIME INCREMENT (SEC), (FIB.el6B.
ARE NEW PLOT OPTIONS DESIRED? (Y/N)
AVAILABLE PLOT OPTIONSe - NO PLOTSI - PARAItETER PLOTS ONLY2 - TRAJECTORY PLOTS ONLY3 - PARAHETER AND TRAJECTORY PLOTS
E_TER PLOT OPTION (II)3
THE POTENTIAL FLOW FIELD IS NOW BEING CALCULATED
b. Interactive input
Figure 7.1: Concluded
103
_:EL::ITY (.M/S_ 129.00
T[MoE_TU_E <C) -12.68
F_SS_E (KP_) g0.75
-C_I_ITY (_) 100o00
TIME (SEC) S.O0
ORIGINAL PAGE IS
OF POOR QUALITY
0.010
0.008
0.006
O.CO_
0._C2
v O. 000
_- -.002
-.00'_
-.006
-.OOg
-. 0 l_
m
l
l
l
q'O
o
o
o
o
o
o
o
o
o
o
o
o
S (M)
Figure 7.2: Yo vs s points calculated in subroutine COLLEC for Example 1
THE CALCULATED SURF_E |HPACT DISTANCES (S) ANDARE _S FOLLOVS
; (0 S
O.Q07gS g.e27152 O.OO?;8 e. QIB443 O,oOSt3 O.Ot3O24 O.OO_tl 0.009645 0.6_49B 9,98694G 0.@0305 0.08370i' B.B@2e3 0.00240e 0.00100 0.B_154g -0.00003 -0.00003
RELEASE POINTS (YO|
l YO S
-0.00106 -O.OO_6O1 -O.@02eB -O.OO25G2 -_.B0311 -O.BB3BS3 -0.B0414 -O.OB7344 -O.OOSI7 -e.oog83S -O.OO619 -0.0132GG -O.BB722 -O.OlOB_7 -B.BBBB2 -0.03702
tO O.OOOOO 0.00000
hO_ _AN_ TRAJE_SOR!ES ARE TO BE DELETED BEFORE*h_l _0_LECTICN EFFICIENCY CALCULATION? (!2_
_ACA 8812 : EXANPLE 1 : TIME- 120.000 SEC
ICING CONDITIONSTAT;C TEHPERATURE (C) 2G0.SSSTATIC PRESSURE (PAD 9B748.B0VELOCITY tH/S) 129.00LVC (G/M_*3) B.SO
DROPLET DIAMETER (MICRONS) 20.00
ICE ACCRETION DATASTAGNAT:GN POINT 74TRANS;TION POINTS (LOWER,UPPER) 72ICING LIMITS (LOWER,UPPER) 43NUMBER OF POINTS 147NUMBER OF SEGMENTS ADDED B
AVAILABLE PLOT OPTIONSB NO PLOTSI ICED GEOMETRY
2 Z VS S3 BETA V$ S4 - VE VS SS - TE vs SG - PE VS S7 TSURF VS SB - HTC VS Sg - XK VS S10 - ICE DENSITY VS SII - FFRAC VS S
ENTER OPTION NUMBER (12)
75103
Figure 7.3: Interactive input and output for the second time step of Example 1.
ORIGINAL PAGE IS
OF POOR QUALITY
a. Iced airfoil geometry
VELOCITY (M/S) 129,_6TEMPERATURE (C) -12,60PRESSURE (KPA) 90,75HUMIDITY (X) 100,00LNC (G/MN-3) O.SODROP DIAM (MICRON)20.O0TIME (SEC) I2O.OO
2o0FlBO
if_ _2oi ,'"f_IDC [-
2: F_.'35 -.2e -o12: ..T!_ -.'G7 -°IOC 0°'0; C_.:;_ 0.I_I C-_2' 0-135
S (41
d. Edge velocity vs. surface location
C.OIC
C.OO,
C.OOo
C.O0*
_C.O02
-0.000
_-.ooz
-.00.
-.OOe
-.OOg
-.o)_
b.
/./-
o-._3,-._,_-._,.._o6-._oco._o,o._o_.b-_.h_o._oS (M)
Particle release position vs. surface
impact distance
o F-_[-
"2_.!_5 -.'_ -.21 -.:!_ -.'07 -JOO C.I_ : 0.!_ 0,?:I G.:2_ G.'35
S (M)
e. Edge temperature vs. surface location
0.6 F
C.7 L-
_O.S
0"3 F \,
D.2 __0,: F
_'-%O_G 02 OOB 0 03, 0 G2 O.O_O
S (M;
c. Local collection efficiency vs..urf_:elocation
lid
]G7
ICl
98
q5
_2
8q
.o
B3 L
8_'.13_ -.'_E -.'2; -.:I = -.TOt -.[00 OJO; O.I'.* G.121 G.'_' 0.'35
c _m)
f. Edge pressure vs. surface location
Figure 7.4: Icing parameter plots for the second timestep of Example 1.
105
:F": I-
i-2[-
-9 L
g°
VELOCITY (M/S) 129.1+6TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75HUMIDITY (X) lO0.OOLWC (G/M,, w3) 0.50DROP DIAM (MICRON) 20.00
TIME (SEC) 120.00
1o00 F
900
800
700 i-
z bOO i
F-- _OO F
300
200
]OO _-
-:-3.}5 -.2g -.2: -.:_ -._; -?00 C.'C/ O.:w ?.2: C.26 C.25
S (M)
Equilibrium surface temperature vs.
surface location
j°
_._5 -.26 -.21 -.I'_ -.07 -.'DO 0.'07 0.]_ 0.'21 0.28 0.35
S (_I!
Ice density vs. surface location
leOO F
Ib20 L
iIw_O F
12bO
IOBO
Iz
720 I
360 L
18C
h,
n_.'35 -.28 -.2_ -.],r -.07 -.00 0.07 0.i,_ 0._i C.26 C.35
S (M)
Convective heat transfer coefficient
vs. surface location
.00050
.000_5
.OO0*C
.0003!
.0003_
.00025
.OO0_O
.00015
.C0010
.0300'
"O00Q_:_5 -.2e -._I -.1_ -._07 -.00 O?Ol c._l_ C.2l C.'ZB G.35
S (M)
i. Equivalent sand-grain roughness
height vs. surface location
;.Of-
O'_ F
O.e.t
C.7 _
O.o L
I:'0.5
: F
o._-G.2 L
!O.] -
!o.o.o,, c
Figure 7.4: Concluded
-.3_- - .OO6 G.3C8 0.02 _ G-O*O
S (M)
k. Freezing fraction vs. surface location
106
9
10
ii12L$
Z5
1718
192O
21;2
232 (,
2525
2?2829
3O31
32333;
35
3?
3_39_,0
4142(,3
(.4('5(,6(.7
48
495O
U_(TRA;_SFORMED COORDINATE DATA FOR BODY ID =
X(1)
1 00000000 98799970 9799998
0 96999970 9_99997
0 92('99980,8999999
0.87('99990.8('999980.82('9999
0.79999970.7749997
0.75000000.72('99980.69999970.67('99980.64999990.62(.99990.5999998
0.57('99990.5('99997
0.52('99970.5000000
0.47('99980.('(.99997
0.('2499980.39999990.37999990.3('999980.32('99990.2999997
0.27499970.25000000.22('99980.19999990.17499993.14999990.12500000.0999598
0.08999990.07999990.06988('50.05956770.0('947220.0('_0280.03919210.03395770.02870980.02336980.0179198
Y(I)0.0000000
-O.OOIB7qO
-0.0036110-0.0052390-0.0082510-0.0117000
-0.01490B0-0.0179530-0.0208880-0.0237390-0.0265150
-0.0292210-0.0318550-0.0344110-0.0368870-0.0392810-0.0415850-0.0437950-0.0459040-0.0479060-0.0497930-0.0515600
-0.0531980-0.05_6980-0.0560510
-0.0572430-0 05B2620-0 0590900-0 0597070-0 0600940-0 0602260
-0 06O076O-0 0596120-0 05879('0-0 0575700-0.055B790-0.0536360-0.0507320
-0.0470040-0.0452280-0.043252O-0.0('14994-0.0397540-0.0374086-0.0361813-0.034748('-0.0331625
-0.031('767-0.0296603-0.0275407
I, HACA 0012
I X(I)51 0.012252252 0.0063893
53 0.002977654 -0.000699655 -0.002056556 -0.003413557 -0.0053174
58 -0.005347859 -0.005378260 -0.005466561 -0.005582762 -0.005681763 -0.005777364 -0.005892465 -0.005909266 -0.0059506
67 -0.006012268 -0.006089669 -0.006199170 -0.006369171 -0.006473972 -0.006578773 -0.006663274 -0.006747675 -0.0066629
76 -0.006578277 -0.006473178 -0.006368079 -0.006197680 -0.006087881 -0,006010182 -0.005948583 -0.00590708_ -0.005890285 -0.005775086 -0.005679487 -0.005580088 -0.0054638
89 -0.005376490 -0.005346391 -0.005316292 -0.003386493 -0.002027094 -0.0006677
95 0.002986396 0.006394197 0.012253798 0.017918999 0.0233668
100 0.028706¢
: EXAMPLE 1
Y(1)
-0.0250171-0.0218130-0.0197319
-0.0170765-0.0162655-0.0154545-0.0129929-0.0124796-0.0119662-0.0111464-0.0103023
-0.0094149-0.0084782-0.0075095-0.00693('4-0.0063720-0.0057760-0.0051370-0.0044373-0.0036290-0.0030471-0.0024653-0.0012327
0.00000000.00123260.00246520.0030_700.00362870.00_43690.00513660.00577550.00637130.00693370.00750870.00847740.00941390.01030110.01114510.0119654
0.01247880.01299220.01543450 01624320 01705190 01972310 02180710 02501500 0275427,0 02966670.031¢846
ORIGINAL PAGE IS
OF POOR QUALITY
II01
102103
lOqI05106
I0/lO&
1o)L15
Ill112
113114
i15116I17
I18119
120121
122123
12('125126
127128
129130131
132133
134135
136137
138139
140141
I('2143I('4
lq5le,6147
X(1)0 0339538
0 03913650 0442957
0 04946360 059_575
0 06987890 0799999
0 08999990 09999980 1250000
0 14999900 17_9999
0 19999990 22(.9998
0 25000000 27499970 2999997
0 3299999
0 3_999980 37499990 3999999
0.('2_99980.4499997
0._7499980.50000000.52499970.54999970.5749999
0.59999980.6249999
0,64999990.67499980.69999970.72499980.75000000.77499970.79999970.82('99990.8('999980.87499990.8999999
0.92('99980.9('999970.9699997
0,97999980.9899997
1.0000000
Y(I)
o 0331726o 03(.76G20 0362028
0 03743720 0397926
0 04152160 0_32520
0 04522800 09700_00 0507320
0 0536360
0 05587900 05757000 05879_0
0.05961200.0600760
0.06022600.0600940
0.05970700.05909000.0552620
0.0572430
0.05605100.05469800.05319800.0515600
0.04979300.0('790600.0('59040
0.04379500.0415850
0.03928100.03688700.03441100.0318550
0.02922100.02651500.02373900.02088800.01795300.01990800.0117000
0.00825100.00525900.0036110
0.00187('00.0000000
DOUGLAS
COrlBIHED FLO{.i
ALPHA = 0.000000
CL = 0.000002
BODY IO = i
T 7
I 0.99500,'?.52 0 .9850022
3 0.975001.3(' 0. 96000('5
5 0.9_750(.qs 0.91250257 0.8875015•_ 0.8625011
9 0.B375007!O 0 .8125005'.1 0.7875003
12 0.752500813 0 73}5007
I(. 3.712500515 0 .637500_16 0,562500417 0 657900_15 0.6125008
19 0.587500/20 0.56."5006
21 0.537500522 0. 512500921 0.qB750092(' 0.462500825 0.4375007
26 0.412500727 0. 387500628 0. 362500529 0.337500330 0. 312('999
31 0.287('99('32 0.262q990
33 0.23749833t+ 0.2124971
35 0. 187495636 0. 16;.t. 73137 0.137489338 O. 112483139 0.0949959(.0 0.08q999941 0.0749(.38
A[FC_AFT COHPAHY TWO-DIHENSIONAL POTENTIAL
HAC_ 0012 : EXAMPLE I
ALPHA O = 0.000013
CHORD : 1.000000
HACA 0012 : EXAMPLE 1
Y
-0,0009536-0.0027573-0.00('4365-0,0067780-0.0100112-0.013328('-0.016_(.70-0.019_323-3.0223233-0.0251359-0.0278?68-0 0305473-0 0331427
-0 0356590-9 03B0946
-00qO('(.q4-0 0('27021-0 044862('
-0 0469188-0 0('88641
-0 0506920-0 0523956-0 0539657-0 0553936-0 0366678-0.0577752-0.0587010-0.0594260-o.o5993o8-0.0601935-0.0601882-0.0598856-0.0592503-0.0582363-0.0567876-00548323-0.0522749
-0.0489800-0.0461379
-0.0442400-0,0423663
S0.002_7150.00740850.01233520.019709;0.03075280.04300580.0552('620.06747840.07970510.09192750.1041459
0.11636050.1285714
0.1('0778('0.15298150.16518060.17737560.IB95665
0.20175310.21393560.22611370.23828740.250_5690.262622_0.27478380.286941_0.29909540 31124620 32339_40 33554100 34768690 35983370 3719836
0 38414000.39630690.40849100.42070220.43295640.4915639
0.44650720._514770
FLOW PROGRAM
NO. OF BODIES
TOTAL ELEMENTS
NO. OF ELEMEHTS
VT-0.8268182-0.8886436-0.9189040-0.9450629-0.9680377-0.9839131-0.9951214-1.0043230-1.0127668-1.0207739-1.0284805-1.0360298-1.0433102-1.0503035-1.0572052-1.0640011-1.0706520-1.0772190-1.0836945-1.0900660-1.0963779
-1,1027031-1.1089926-1.1153297-1.1216908-1.1280737-1.1345110-1.1408377-1.1470585-1.1531639-1.1590567-1.1697253-1.1701040-I 1749191-I 1788921
-I 1814556-1 1815958-1 1766272-1 1659_98-1 1386347
-1 128655_
1
146
I96
CP
0.31637160.21031250.15561540.10685620 06290310 03191500 0097334
-0 0086641
-0 025695_-0 0419789-0 0577717-0 0733576-0 0884953-0 1031370-0 1176825I 0 1320982-0.1462955-O.16O4OO4-0.1743937-0.1882429-0.2020_26-0.2159538-0.2298641-0.2_39604-0.2581892-0.2725496-0.2871151-0.3015099-0.3157_25-0.3297863-0.3434114
-0.3565845-0.3691('25-0.3804390-0.3897858m0.3958368--0.3961678"0.38_4509--0.3594389--0.296488B--0,2738628
JI
23
456789
l0]112131(.15161718192O2122232('252627282930313233343536373B39('0ql
SIGtIA-0.013141
-0.013129-0.012670-0.012000-0.011207-0.010559-O.OlOlqO-0.009907-0.009760
-0,009630-0.009516
-0.00938('-O.O09213-0.009036
-0,008853-0.008626-0.008386-0.008112-0.007813-0.007('77-0.007127-0.006738-0.0O6311-0.005851
-0,005326-0.004755-0.00('099-0.003351-0.002524-0.001583-0.000526
0.0006710.0020470.0036660 0055580 0078530 0106530 0142430 017('080 0199400 014238
VN0.000004
0.00000('0.00000('
O.0O00O4
O.OO00040.00000(.0.0000030.000002
0.0000010.0000010.000001
0.0000010.000001
0.0000010.000001
0.000001O.O000010.000001
0.0000010.0000010.000001
0.0000010.000000
0.000000o.080o000.O0OOOO0.0000000.0000000.000000
0.0000000.000000
-0,000000-0.0000000.000000
-0 000002-0 000002-0 00000('-0 0OOO04
-0 O0000q-0 000003
-0 000003
Figure 7.5: Printed output for the second time step of Example 1
107
88
89
9O9192
0394
9596
9798
99leoIOl
102103
10't
105106107
108109
110Ill
If2113ll4
i15
I16I17If8
119120
121122
123
DOUGLAS A _.CRiFT
CCMBZrtE_ FLC_
ALFtlA : 0.000000
CL = 0.000002
BODY ID = I
I X42 0.06_7761q3 0.05_5632
_5 0.0417_68_6 0.0365461_7 0.031330548 0.026033749 0.020632_50 0.015066_
51 0.009292_52 0.00_670253 0.00113905q -0.001377955 -_.07_735056 -0.00_589257 -0 005332758 -0 005363059 -0 005_181
60 -0 00551q661 -0 0056339
6? -0 005729563 -0.00583q86q -0.005900865 -0.005_37_66 -0.0059797
67 -0.0_0_8968 -0.0061q07
69 -0,006_8qI:0 -0.006q21571 -0.006526372 -0.006621573 -0.0067059
7q -0.006705275 -0.0066205
76 -0.006525877 -0.006&Z0678 -0.006_82879 -0.006139080 -0.0060_7081 -0.005977682 -0.005925383 -0.005_q_6
8q -0.005832685 -0.005727286 -0,005631q87 -0.0055219
-0.005qi58-0.0053613
-0.0053312-0.00q5729-0 0027067-0 0013_72
0 0011593
0 00q67650 009295q0 0150667
0 0206308
0 026030_0 03132690.0365_1_0.0q171050.0q687750.05q553_0.06q76810 0749q080 08q99990 09q99590 1124831
0 137#8930 162_931
0 187_9560.212_9710.237_9830.262_9900.287_99q0.31249990.33750030.36250050.3875006
0.q1250070._3750070.4623008
COrIpA?(Y
HACA 0012 : E:,:A_PLE
ALPHA 0 =
CHORD =
NACA 0012 : EXAMPLE
-0.0q06267-0,0386106
-0.0368035-0.035_850-0.0339678-0.0323297-0.0305865-0.0286313-0.0263229-0.0234670-0.02079_2-0.01840_2-0,0166708
-0.0150600-0.01q3968-0.0127363
-0.0122229-0.0115558-0.01072_3
-0.0098588-0.0089465-0.0079938-0.0072219-0.0066530-0.0060738-0.0054563-0.0047866
-0.0040331-0.0033380-0.0027562-0.0018490-0.000616_
0.00061630.0018489
0,00275610.00333790.00_03280.00_78620.005_5580.00607320.00663230.0072212
0.00799300.0089456
0.00985770.01072310.01155_8
0.01222210.01273550.01_388_0.01583880.0166q730.01838750 02078750 023_6310 0263228
0 02863560 03059370 032338_0 033980_
0 03550360.03682880.0386_570.0_065710.0_237820,0_2_000.0_613790.0_898000.05227_90.05483230.05678760.05823630.05925030.05988560.06018820,06019330.05993080.059_2600.05870100.05777520.03666780.0353936
THO-DI_EHSIOH_L POTEHTIkL
i
0.000013
1.000000
I
FLON PROGR_{1
S0.456q88q0.4615475
0,46537950.q6797110.q7058920.q732_500.6759541
0.47874q70.4816726
O.q8q80310._8739730.48946990._9095570.49172360._9288010._9377750.49402730.49_352_0.69_75960._95183_0._9362900.q9609_60.696_712
0._967_790._97030_0.49733220.69766060,_9803320.q98377q0.69866_60.q9910830.q9970850.50030880.50090900.30135270.50163980.50198_10.50235670.30268310.50298690.50326960.5035_610.50392270.50_38830.50_83380.30525750.50566490.30599010.50623990.50713750.50829_0.50906280.S105q6q
0.51261630.51520970.51833990,52126750.52q05820.52676730.529_2_20.5320q130.33q63290.538_6500,5_352_70.5_853700.35350730.558_5030.56705800.37931220.591523_0.60370760.61587_50.62803080.6_018080.65232750.66_735
0.67662000.68876820,70091900.71307300.7252306
0.7373920
HO. OF BODIES
TOTAL ELEHENTS
HO. OF ELEHERTS
VT
-I.166576_-I.1738958-1.1783762
-1.181_q80-I.1633625
-I.lq959q3-I.152104q
-1.1499968-1.1401501
-1.0972996-1.0662109-0.9627361-0.9737q62-i. I0183_3
-1.2881260-0.8853139-0.710_751-0.627910q-0.5720q86-0.5080939-0._1_389-0._16525_-0.3197q75-0.3052155-0.2738528-0.2_70832-0.216q860-0.2118799-0 17q696_-0 1783613-0 09359q3
-0 06071500 06029200 09q_7910 17925080 17503110.2121_6_0.2167311
0,2_7q2530.27603070.30561210.32005_70._1699080.6619_790.308887_0.5723_7_0.62878070.71305770.88910311.29076291.09589960.96887770.958_5631.0659027
1.09725671.16003751.15017601.1523075I.I_926821.16315081.18176861.17917731.17607_01.1687_981.12822821.13737_91.1656160
1.176_8511.18153191.181q2031.1788692
1.17_90391.17009331.16_71671.13906901.1531582
1 1_703371 I_083391 13_50811 12807081 12168881 1133278
1
146
I_6
CP-0.3608999-0.3780308-0.3885698
-0.3958187-0.353_I17
-0.3215666-0.3273439-0.322_916-0.2999_20-0.2040663
-0.1325_50.07313930.051818_
-0.21q0379-0.65926840.216219_0.49522510.60572860.672760q0.7_184060.80513180.82650670.89776160.9068_350.92390530.93896990.95313390.95510690.969_8120.96818730.9912_010.9963138
0.99636q90.9910737
0.96786920.96936_20.95_99_00.933O2770.93878070.92380710.90660130.89756510.82611870.80_68210.7_I03370.67218950.60463_90._9156880.209_958
-0.6660681-0.200995_
0.06127610.0813615
-0.1361_85-0.2039719-0.2996855-0.32190q6-0.3278122-0.3208170-0.3529196-0.3963292-0.390_391-0.3831501-0.365975_-0.2728987-0.2936211-0.3386607-0,38_1162-0.3960171-0.3957539-0.389732_-0.3803988-0.3691187-0.33656_5-0.3_339_3-0.3297729-0.3137320-0.3013013-0.287108q-0.2725q30-0.258185_-0.2_39356
Figure 7.5: continued
d
434q_+5_6q748_95051525354555657585960616263646566676869707I72737q7576777879808182838_8586878889909192939q9596979899
lO0101102103lOq105106107108109110111112113
115116117118119120121122123
SIGMA
0.0115_20.019G2_
0.0105030.0235590.026692
0.0271_60.0272q80.03124q0 03_985
0 0_29640 0q3626
0 0_90180 02358_0 009558
0 0q33060 1260q3
0 1289690 1282950 123520
0 12q8370 127661
0 1256300 1316_5
0 1364770 1352100 13_6700 133_900 12_528
0 1198060 114872
0 1180390 I1603q0 1162090 I181_30 114737
0 1197280 12_920 133_580.13q6600.1352130.136_30.1316150.125575
0.1275890.12q7220,123q680.1283030.128798
0.1257870.0q1929
0.0097220.0237460.0501_20,0_37910.04310_0.0351320.0313950.0273000.0272250.0269010.0237530.0187360.0195680.011189
0.0138230.0199_20.0174050.01_238
0.0106_90.0078_80.00555_0,0036620.00204_0.000669
-0.000528-0.00158_-0.002526-0.003353-0.00_101-0.006757-0.005328-0.005852
ORIGINAL PA_E IS
OF POOR QUALITy
VH
-0.000002-O,000002-0,000002
-0.000001-O.000002
-O,OOO002-0.000001
-O,OO0O01-0.000001
-0.000000-0.0000000,000000
0.0000020.000003
0.000004-O.OOO032-0.000030-0 000026-0 000018
-0 000024-0 000025-0 OOOO24
-0 000032-0 000023-0 OOO023-0 000022-0 000015-0 000002
-0.000010-0.000008
-0.000025-0.000027-0.000026-0.000027-0 000007-0 OOOO08-0 000003-0 000015
-0 000021
-0 000023-0 000026-0.000026
-0.000019-0.000023-0.000021-0.000018-0.000026-0.000025
-O.O0002qO.O0000qO.OO0O01
-O.O00001-O.O00001
-O.OOOO02-O.OO0OO2
-0.000002-0.000003
-0.000003-0.000003-0.000003-0.000003-0.00000_-0.00000_-0.000003-0.00000_-0.000003-0.00000_-0.000003-0.000002-0.000002-O.O0000Z
0.0000000.0000000.0000000.0000000.000000
0.0000000.0000000.0000000.0000000.0000000.000000
108
_OUGLAS ATPCRAFT COMPANY T_O-DIHENSIONAL POTENTIAL
CO,DINED fl.O_ NACA 0012 ; EXAMPLE I
A!,PtlA = 0.000000 ALPHA O = 0.000013
CL : 0.000002 CHORD = 1.000000
BODY ID = I NACA 0012 : EXAMPLE 1
I X Y S
i2q 0.48?5009 0.0539657 0.7495575125 0.5125009 0.0523956 0.7617270
126 0.5375005 0.0506920 0.7739007I27 0.5625006 0.0488641 0.7860789
(28 0.5875007 0.0469188 0.7982613129 0.6125008 0.0648624 0.8104479130 0.6375008 0.0427021 0.822638813I 0.6625004 0.0404444 0.8348338132 0.6875005 0.0380946 0.8470329
133 0.7125006 0.0356590 0.8592360134 0.7375007 0.0331427 0.8714_30135 0.762500B 0.0305473 0.8836539136 0.7875003 0.0278768 0.8958685137 0.8125005 0.0251359 0.9080870138 0.8375007 0.0223233 0.9203093139 0.8625011 0.0194323 0.9325360140 0.8875018 0.0164470 0.9447682141 0.9125025 0.0133284 0.9570085142 0.9375044 0.0100112 0.9692615143 0.9500045 0.0067780 0.9803048144 0.9750013 0.0044365 0.9876790145 0.9850022 0.0027573 0.9926056
146 0.9950025 0.0009536 0.9975426
INTEGRATED VALUES
CY = 0.00003 CX = -0.00106
CL = 0.00003 CD = -0.00106
PARABOLIC INTEGRATION
IHTEGRATED VALUES
CY _ 0.00002 CX = -0.00030
CL = 0.00002 CD = -0.00030
TOTAL CM = 0.00000
CM : 0.00000
CM = 0.00000
FLOW PROGRAH
NO. OF BODIES 1
TOTAL ELEMENTS I_6
NO. OF ELEHEHTS 146
VT CP1.1089916 -0.22986221.1027021 -0.21595191.0963764 -0.20204071.0900640 -0.1882391
0836935 -0,1743908I 0772171 -0.1603966i 0706501 -0.1462908I 0640001 -0.1320953i 0572042 -0 11768051 0503025 -0 10313511 0433102 -0 0884953I 0360289 -0 07335571 0284805 -0 0577717
• 0207729 -0 0419769.0127659 -0 0256939
• 0043221 -0.0086622• 9951208 0.0097346
0.9839124 0.03191640.9680369 0.06290460.9450626 0.10685680.9189037 0.15561600.8886423 0.21031500.8268158 0.3163756
TOTAL CH = 0.00000 (PARABOLIC)
ORIGINAL PAGE IS
OF POOR QUALITY
J124
125126127
125129
130131
132133
134135
136137
138139
140141142143
144145
146
SIGHA-0.006312
-0.006739-0.007128
-0.007478-0.007814-0.008112-0.008386-0.008627
-0.008853-0.009036
-0.009214-0 009384
-0 009517-0 009631-0 0O9760-0 009907-0 010141-0 010560-0 011207-0 012000-0 012670-0 013129
-0 013141
VN
0.0000000.000001
0.0000010.0000010.000001
0.0000010 000001
0 0000010 000001
0 0000010 000001
0 0000010.0000010.000001
0.0000010.000001
0.0000010.0000010.000004
0.0000050.000004
0,0000050.000004
T'IE PARTICLES
WHICH IS OBTAINED AT TIIE
GEOHETRY CHARACTERISTICS:
LEADItIG EDGE (X,Y)T_,ILIt(G EDGE IX,Y}THICH,_ESS
CHOPDA;4GLE CF ATTACK
UI'FER BCUt{DAPYLO'_EB BOUNDARY
PARTICLE TRAJECTCRY DATA:
ARE RELEASED FROM Z = -1.26000E 00
I LOOP OF 50 LOOPS
-4.0243E-03
3.0200E-014.0136E-02
3.0000E-010.0000
2.2075E-02-2.2075E-02
2.0715E-070.0000
THE PARTICLES ARE RELEASED I_I EQUILIBRIUM HIT}I THE AIR
PARTICLE IHITIAL I?IITIAL PARTICLE PITCH PIT GRAVT ERRGR_IA:_ER VX VY AOA ANGLE DOT CONST CRITERIA(HICROHS} (M/S} (M/S} (DEGREES} (DEGREES) (DEG/SEC) (M/SW_2)
20.00 0.00 0.00 0.00 0.00 0.00 0.00 5.00E-05
Tile PARTICLES OF SIZE 20.00CONTAIN 1.0000 OF TIIE TOTAL HASS
X0 Y0 XP YP
-1.2599993 0.0090961 OUT OF RANGE 0.0831582 0.0226937-1.2599993 -0.0090835 OUT OF RMIGE 0.0828083 -0.0226548
YOHAX = 9.09_1E-03 YOMIN = -9.0835E-03
DT4.6785E-055.2456E-05
-1.2599993 0.0000063 NIT BODY AT -0.00_0239 0.0000050 0.0000050 8.1206E-06-1.2599993 0.0045512 NIT BODY AT -0.0009029 0.0054289 0.0082736 2.8464E-06-1.2599993 0.0068236 HIT BODY AT 0.0061579 0.0088386 0.0162043 9.2295E-06-I.2599993 0.0079599 NIT BODY AT 0.0166598 0.0117465 0.0271505 6.7323E-06-1.2599993 0.0085280 OUT OF RANGE 0.0813009 0.0221908 4.7782E-05-1.2599993 0.0082439 OUT OF RAtIGE 0.0829488 0.0222186 4.7512E-05-1.2599993 0.0081019 OUT OF RANGE 0.0871353 0.0226163 6.1404E-05-1.2599993 0.0080309 OUT OF RANGE 0.0854309 0.0225082 4.4515E-05-1.2599993 -0.0005618 HIT BODY AT *0.0039709 -0.0006448 -0.0007154 6.9591E-06-1.2599993 -0.0048227 HIT BODY AT -0.0003887 -0.0057987 -0.0089134 3.1107E-06-1.2599993 -0.0069531 HIT BODY AT 0.0069689 -0.0091094 -0.0170804 1.i02BE-05-1.2599993 -0.0080183 HIT BODY AT 0.0263552 -0.0135138 -0.0370157 9.9582E-06-I.2599993 -0.0085509 OUT OF RANGE 0.0868925 -0.0228065 4.9236E-05
-1.2599993 -0.0082846 OUT OF RANGE 0.0823606 -0.0221761 4.0522E-05-1.2599993 -0.0081514 OUT OF RANGE 0.0851743 -0.0224173 5.1358E-05-1.2599993 -0.0080849 OUT OF RANGE 0.0836582 -0.0222142 4.8017E-05
0.01844340.0130234
UPPER SURFACE LIIIIT LOWER SURFACE LIMIT
YOU SU Y0L SL0.7960E-02 0.2715E-01 -0.8018E-02 -0.3702E-01
-1.2599993 0.0071610 flIT BODY AT 0.0082593 0.0095326-1.2599993 0.0061338 HIT BODY AT 0.0032192 0.0076855
9.5929E-067.8691E-06
HSTP101
97
4168
65Bo95
111116119
455658
9187
108iii
92
7168
Figure 7.5: continued
109
-i.2599993 0.0051065 HIT BODY AT-1.2599993 0.0040795 fliT BODY AT
-1.25q9993 0.0030523 HIT BODY AT-!.2599993 0.0020251 ?lIT BODY AT-1.2599993 0.0009980 HIT BODY AT
-L.2579993 -0.0000292 HIT BODY AT-1.2599993 -0.0010564 fliT BODY AT
-1.2599993 -0.0020835 HIT BODY AT-1.2599973 -0.0031107 HIT _ODY AT-1.2599793 -0.0041379 HIT BODY AT
-|.2599993 -0.0051650 flit BODY AT-L.2599993 -0.0061922 HIT BODY AT
-1.2599993 -0.0072194 HIT BODY AT
0 0002541-0 0018151
-0 0036111-0 0037484-0 0038598
-0 0040216-0 0036480-0 0087397-0 0036065-0 0016187
0 00041490 003435B0.00865_1
0.0061759
0.00481640.0035133
0.00233660.0011532
-0.0000330-0.0012178-0.0024063-0.0035786-0.0048994-0.0062647-0.0077756-0.0096553
0 00963_20 0069433
0 00378470 00249180 0015363
-0 0000332-0 0016015
-0 0025623-0 0038509-0 0073419-0 0098281-0 0132625
-0 0188647
4.0084E-062._937E-066.9544E-06
1.0324E-05_.0499E-068.1260E-06
8.0255E-066.3720E-06
4.9189E-062.7035E-064.3314E-069.5905E-067.5941E-06
'(0 VS S _AT,'. FCR DROPLET DIAIIETER _17 POINTS I!AVE BEEN CALCULATED
i
L23
5
? 08 09 -0
10 -011 -0
12 -013 -0i', -015 -0
16 -017 -0
S YO
0 027150 3.0079600.0184_3 0 007161
0 013023 0.006134049538 0005107
0 0069G3 0,004079003785 0 003052002492 0.002025
001536 0.0009980000_3 -0.00002900L602 -0.001056
002562 -0.002084303851 -0.0051110073_2 -0.004138009828 -0.005165013263 -0.006192018_65 -0.007219
037016 -0.0080LB
20.00000 MICRONS
CALCULATED
S_G SI -0.311805
2 -0.3076263 -0304559
4 -0.2999815 -02931416 -0.2855577 -0.2779858 -0.270_22
9 -0.252865
11 -] 2_7761IZ -0.2%0213
l_ -0.232S67i_ -0.225122
15 -0.21756016 -0.210040
17 -0.20250212 -,2+194966
19 -0.18745320 -0.17990121 -0.172371
22 -0.1648_423 -0.157318
24 -0.14979_25 -0.142272
26 -0.13475027 -0.12723028 -0.I19710
29 -0.11219030 -0.10466931 -0.0971q632 -0.089620
33 -0.0B208934 -0.074550
35 -0.06700036 -0.05943237 -0.051B3838 -0.04421839 -0.03684940 -0.03577041 -0.03271642 -0.02960743 -0.02642544 -0.024004
45 -0.022348
46 -0,02068047 -0.01900_08 -0.017286
49 -0.01548650 -0.013567
LOCAL COLLECTION EFF_CIEHCY FOR DROPLET DIAMETER =
BETA SEG S
0 0008000 000000
0 0000000 000000
0 0000000 0000000 0000000 0000000 000000
0 0000000 0000000.000000
0.0000000.000000
0.0000000.000000
0.0000000.0000000.0000000.000000
0.0000000.0000000.080000
0.0000000.0800000.0000000.0000000.0000000.0800000.0000000.000000O.0000O00.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0000000.0190780.0624260.0954000.117956
0.1406850.163511
0.1869250.2114370.237579
20.00000 MICRONS
BETA
-- 51 -0.011512 0.31260052 -0.009782 0.334206
53 -0.008418 0.33286654 -0,007550 0.33201555 -0.006894 0.37361856 -0.005735 0.40860357 -0.001q76 0,q_668558 -0.0038',2 0.67219759 -0.003704 0.702001
60 -0.003688 0.7t+890561 -0.003210 0.8090_962 -0.002921 0.871553
63 -0.002613 0.93836264 -0.002321 0.85002465 -0.0G2153 0.83777766 -0.002940 0.82947967 -0.001904 0.819519
68 -0.001772 0.80990269 -0.001598 0+857995
70 -0,001381 0.83318471 -0.001112 0._0257472 -0.000728 0.758828
73 -0.000254 0.70_71674 0.000254 0.71287q75 0.000729 0.76748176 0.001113 0.81165377 0.001381 0.842557
7B 0.001599 0.B0246779 0.001773 0.81502680 0.001904 0.62453081 0.002040 0.83436382 0.002153 0.84255083 0.002321 0.85_658a4 0.002612 0.924965
85 0.002921 0.85738486 0.003210 0.79416087 0.003487 0.73354088 0.003702 0.68637089 0.003840 0.50082590 0.004483 0.47375291 0,005731 0.42041592 0.006902 0.37200593 0.007548 0.3¢075794 0.00840B 0.33722695 0.009775 0.34323396 0.011507 0.29858297 0.013561 0.24213298 0.015481 0.20992699 0.017280 0.179721
100 0.018999 0.150880
HICA 0012 : EZAHPLE 1
ICIHG CO:(DITIO_(:
%TATIC TE;1PER_TURE (C)STATIC P_ESSURE (PAl
VELOCITY (M/S)LWC (G,'_'_3)DROPLET DIAMETER (MICRONS)
: TIME= 120.000 SEC
260,5590748.00
129.000.50
20.00
ICE ACCBETION DATA;
STAGNATION POINTTRANSITION POINTS (LO_ER,UPPER)
ICING LIMITS (LOWER,UPPER)PIUM_ER OF POII(_S
NU_BER OF SEGME?(TS ADDED
7472 7543 103147
8
Figure 7.5: continued
"t-In
SEG
10110210310410510610710B109110
112113114115116117lIB119120121122123124125126127128129130131132133134135136137138139140141142143144145146
54
525256
503946
5661
5960
6355
ORIGINAL PAGE IS
OF POOR QUALITY
S BETA0.020674 0.122772
0.022342 0.0947800.023998 0.0659910.026420 0.0263420.029605 0.0000000.032716 0.0000000.035768 0.0000000 038847 0.0000000 044215 0 000000
0 051835 0 0000000 059429 0 000000
0 066997 0 8000000 074547 0 000000
8 082086 0 0000000 089618 0 0000000 0971_3 0 0000000 104666 0 000000
0 1121B7 0 0000000 119707 0 000000
0 127227 0 0300000 134748 0 0000000 42269 0 000000
0 149791 0 000000
0 157315 0 0000000 164841 0.0000000 172369 0.000000
0 179898 0 0000000 187430 0.0000000 94964 0.0000000 202500 0.000000
0 210038 0.0000000 217578 0.0000000 225120 0.0000000 232664 0.000000
0.240210 0.0000000.247759 0.0000000.255309 0.0000000.262863 0.000000
0.270419 0.0000000.277982 0.000000
0.285554 0.0000000.293138 0.0000000.299979 0.0000000.304556 0.000000
0.307624 0.0000000.311802 0.000000
_KGi2}(,56;
9
10II12
13%4
1516
17
I?
2021
2223
?_25_621
2829
303132
333(,
3536
3738
39q0
(,243
4__5
_6_7(18
4950
5157.53
5__5
5657
98}96O61
(,263
656667
6869
7071
72737_75
7677
?879
8081
828}8_
8586
a708899O
9192
939(t95
9697
989910'?.
IGI
102I03
IQqI05
I06I07I08
109110
X
0.30000E 000.29700E 000.29_0oE 00
0.29100E 000.2_500E 000.2775]F O00.27000E 000.26250E 000,25900E 000.2_7_0E 00
0.2_009E 000.2_250E 00
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Y0.00000
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0.10870E-010.11191E-010.11369E-010.11938E-010.12_56E-010.12976E-010.13568E-010.1_I01E-010.15220E-01
S-0,31233E 00-0.30929E 00-0.3062_E 00-0.30169E 00-0.27487E 00-0.28730E 00
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0.2_;87E-030.72q_6E-03
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0.13_05E-020.15567E-020.17365E-020.18766E-020.20190E-020.21_3qE-020.23311E-020.26616E-020.30079E-020.3320_E-020.361_6E-020.38182E-020._0096E-020._7420E-020.66297E-020.8_734E-020.06778E-020.11072E-010.12_76E-010.1_167E-010.16183E-010.18055E-010.19815E-010.21510E-010.2316_E-010.2;796E-010.26_1_E-010.28792E-010.31917E-010.3501_E-010.38083E-010._1156E-010._6_51E-010.}_017E-01
VE
0.I0281E0.113_/E
0.I1730E0.12093E0.12;22E
0.1265_E0.12819E0.12953E0.1307_E0.13188E0.13297E0.13_03E0.13506E0.13605E0.13703E
0.13799E0.13893E
0.13986E0.I_078E
0.14169E0.1_258E0.1_3_8E0 lq438E0 lq528E0 1_618E0 1_708E0 I_798E0 I_887E0 1_97_E0 1_059E0 151_lE0 15218E0 1_289E0 153§0E0 15396E0.15_18E0.1§398E0.15298E0.15113E0.1_809E0.I_822E0.15026E0.1_09_E0.150_7E0.1_985E0.1_8_8E0.1t692E0.1q5q_E0.1_339E0.13771E0.13396E0.12711E0.12068E0.11609E0.111_�E0.10001E0.82295E0.72197E0.7001_E0.665_2E0.62158E0.57735E0.53236E0._9196E0._6975E0._5561E
0.42505E0.q0822E0.38966E0.57010E0.3_789E0.33281E0.33289E0.3_796E0.37031E0.38993E0._08_7E0._2529E0._3970E0._5589E0._6997E0._7222E0.53260£0.57761E0.62191E0.66557E0.70002E0.72190E0.82_29E0.10016E0.111*7E0.11596E0.12052E0.12702E0.13392E0.13989E0.1_339E0.145_5E0.1_693E0.1_850E0.1_990E0.15057E0.15113E0.150_3E0.1_822E0.1_891E0.15108E0.15296E0.15307E
TE
03 0.26357E 0303 0.262_2E 03
03 0.26198E 0303 0.26155E 0503 0.26115E 0305 0.26086E 05
03 0.26065E 0303 0.260_8E 0303 0.26032E 03
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02 0.2663_£ 0302 0,26663E 0302 0.26691E 0302 0.26717E 0302 0.26742E 0302 0.26762E 03
02 0.26773E 0302 0.26780E 03
02 0.26787E 0302 0.26793E 0302 0.26800E 0502 0.26807E 0302 0.26815£ 03
02 0.26823E 0302 0.26828E 0302 0.26828E 0302 .0.26823E 0302 0.26815E 0302 0.26807E 0302 0.26800E 0302 0.26793E 0302 0.26787E 0302 0.26779E 0302 0.Z6773E 0302 0.26762E 0302 0.267_2E 0302 0.26717E 0302 0.26690E 0302 0.26662E 0302 0.26639E 0302 0.2662_E 0302 0.265_5E 0303 0.2638_E 0303 0.26265E 0303 0.2621_E 0303 0.26160E 0303 0.26080E 0303 0.25991E 0303 0.2_909E 0303 0.23860E 0303 0.23830E 0303 0.25809E 0303 0.25786E 0303 0.25765E 0303 0.25755E 0305 0.257_6E 03
03 0.25757E 0303 0.25790E 03
03 0.25780E 0303 0.257_7E 0303 0.2_719E 0303 0.25703E 03
Figure 7.5: continued
111
PRE_S
0.9q_83E O50.93053E O5
0.92507E 050.91977E 050.91_83E 050.91130E 050.90875E 050.90665E 050.9047_E 050.90294E 05
0.90119E 050.899_8E 050.89701E O5
0.89620E 050.89_60E 05
0.89301E 050.8914qE 050._8989E 050.88835E 050.88682E 050.88530E 05
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I36 0.2q9_9E 00 0.00000 0.00000 0.0O000 0.00000 0.00000 0.00000]37 0.2570_E 00 0.00000 0.00000 0,00000 0.00O00 0.00000 0.00000
]38 0.26q58E 00 0.00000 0.00000 0.O0000 0.0000O 0.00000 0.00000139 0.27213E O0 0.00000 0.00000 0.00000 0.00000 0.00000 0.000001_0 0.27969E O0 0.00000 0.00000 0.00000 0.00000 0.00000 0.000001_| 0.2872qE 00 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000]_2 0.29_81E 00 0,00000 0.00000 0.00000 0.00000 0.00000 0.000001_3 0.30163E 00 0.00000 0.00000 0.00000 0.00000 0.00000 0,00000I_ 0.30613E 00 0,00000 0.00000 0.00000 0.00000 0.00000 0.00000
lq5 0.30923E 00 O.00000 0.00000 0.00000 0.00000 0.00000 0.000001_6 0.31227E O0 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
Figure 7.5: Concluded
ORIGrNAL-PAGE IS
OF POOR QUALITY
115
EXPERIMENTAL
THEORETICAL
VELOCITY (M/S) 129.00TEMPERATURE (C) -12.60
PRESSURE .(KPA) 90.75HUMIDITY (%) I00.00LWC (G/M s) 1.00DROP DIAM (MICRONS) 20.00
TIME (SEC) 120,00
Figure 7.6: Comparison of the experimental and calculated ice shapes for
Example 1.
116
HACA 0012 : EXAMPLE 2&$24¥I£IFT- IIPkRA- lIFIRST- 3ZSEC_D# 3IPVOR z 1IHCLTs 0CLT= 4.0ICItORD = 0CCL= 0.0I)_D = 1ISOL= 0IPRIHT = 0IFLLL- 1_LND
1.0000000 0.98999990.9000000 0.87500000.7500000 0,72500000.6000000 0.57500000.4500000 0.42500000.3000000 0.27500000.15_0000 0.12500000.0600000 0.05000000.0250000 0.02000000.0037500 0.00250000.0012500 0.00100000.0003750 0.00025000.0003750 0.00050000.0012500 0,00150000.0037500 0.00500000.0250000 0.03000000.0600000 0.07000000.1500000 0.17500000.3000000 0.32500000._500000 0.47500000.6000000 0.62500000.7500000 0.77500000.9000000 0.92500001.0000000 0.00000000.0000000 -0.0018740
-0.0149080 -0.0179530-0.0318550 -0.0344110-0.0459040 -0.0479060-0.0560510 -0.0572430
-0.0602260 -0.0600760-0.0536360 -0.0507320-0.0385350 -0.0356740-0.0262300 -0.0237260-0.0106990 -0.0086200-0.0058470 -0.0051400-0.0029450 -0.0023560
0.0029450 0.00346200.0058470 0.0064850
0.0106990 0.01238600.0262300 0.02846200.0385350 0.04103800.0336360 0.05587900.0602260 0.06009400.0560510 0.05469800.0459040 0,04379500.0318550 0,02922100.0149080 0.01170000.0000000 0.0000000
CTRAJ1GEPS= 0.4999999E-04DS_iIFT = 0.20E-02VEPS= 0.9999999E-03LC_B = 0L=HP= 0LE'_ = ILSY(I= 0LYOR= 1LXOR = 1HDDY= 1HEQ = qHPL = 15HSEAR = 50NSI= 1TI_STp= 0.9999999E-0__ENDCTRAJ2CHORD= 0.30G= 0.0PIT = 0.0PITDOT = 0.0PRATK = 0.0XORC # -4.0XSTOP_ 0.50YOLZM= 0,9999999E-04¥0MAXu 0.50E-01¥OMZH_ -0.50E-01YORC # 0.9999996E-01CEHD£DISTFLWC" 1.0, 9NO.ODPD# 20.0, 9_0.0CFP = 1.0, 9_0.0&END£1CEVIr(F z 129.460LWC- 0.50TAHB m 260,5498PArlBz 90748.0_Ha _00.0DPIIMz 20.0XI:IIIIT= 0.00035SEGTOL= 1.50&END
0.98000000.85000000.70000000.55000000.40000000.25000000.10000000.04500000.01500000.00225000.00087500.00012500.00062500.00175000.00750000,03500000.08000000.20000000.35000000.50_00000.65000000.80000000.95000000.0000000
-_.0036110-0.0208880-0.0368870-0.0497930-0.0582620-0.0596120-0.0470040-0.0340820-0.0207970-0.0081360-0.0047660-0.0016320
0.00393100.00707500.01507800.03049600.04325200,05757000.05970700.05319800.04158500.02651500.00825100.0000000
0.9700000 0.95000000.8250000 0.80000000.6750000 0.65000000.5250000 0.50000000.3750000 0.35000000.2250000 0.20000000.0900000 0.08000000.0400000 0.03500000.0100000 0.00750000.0020000 0.00175000.0007500 0.00062500.0000000 0.00012500.0007500 0.00087500.0020000 0.00225000.0100000 0.01500000.0400000 0.04500000.0900000 0.10000000.2250000 0.25000000,3750000 0.40000000.5250000 0.55000000.6750000 0.70000000,8250000 0.85000000.9700000 0.98000000+0000000 0.0000000
-0.0052390 -0.0082510-0.0237390 -0.0265150-0.0392810 -0.0415850-0.0515600 -0.0531980-0.0590900 -0.0597070-0.0587940 -0.0575700-0.0452280 -0.0432520-0.0323620 -0.0304960-0.0172480 -0.0150780-0.0076230 -0.0070750-0.0043630 -0.0039310
0.0000000 0.00163200.0043630 0.00476600.0076230 0.0081360
0.0172480 0.02079700.0323620 0.03408200.0452280 0.04700400.0587940 0.05961200.0500900 0.05826200.0515600 0.04979300.0392810 0.03688700.0237390 0.02088800.0052390 0.00361100.0000000 0.0000000
0.92500000.77500000.62500000.47500000.32500000.17500000.07000000.03000000.00500000.00150000.00050000.00025000.00100000.00250000.02000000.05000000.12500000.27500000.42500000.57500000.72500000.87500000.98999990.0000000
-0.0117000-0.0292210-0.0437950-0.0546980-0.0600940-0.0558790-0.0410380-0.0284620-0.0123860-0.0064850-0.0034620
0.00235600.00514600.0086200
0.02372600.03567400.05073200.06007600.05724300.04790600.03441100.01795300.00187400.0000000
60360360360360360360360360360360360360360360360360360360360360360360 SI I ,,$6046046O460460460460460 _.60 q60460460460460 q
60460460460460460460460 q004114
ORIGINAL PAGE !$
OF. POOR QUALITY
Figure 7.7: Input data file for Example 2
117
V(LCCITY ¢M/$}
T[HPEEATUR[ (C)
F_[_SUq[ (KPA)
-UMI31TY (_)
L_ (3/H--3)
_R_P OI4M (MICRONS)
rIME (SIC)
129,00
-t2.&O
90.75
I00.00
0.50
20.C0
0.00
Y 0.0
-.2
ft
I
I
b
III!
f_
f
O,D
X
VEL331TY (M'5) 129.00
TEHPER_TUQ[ (C) -[2.&0
P_[_SUQ[ (KPA) 90.75
-UMI_JTy (I) 100o00
_ (S"M-,3) 0.50
5R_P OlAM (M!CRONS) 20.09
TIME (SEC) 0.00
ORIGINAL PA(_E rS
OF. POOR QUALITY
0.2
Y 0.I3
-._ D 0
Figure 7.8: Plots of the particle trajectories calculated in subroutine
RANGE. i18
VELOCITY (M/S) 129,00
T[HPE_TUQE (C) -L2.60
P_LSSUqE (KP_) 90._5
_U_I3ITY (_) lO0.OO
L_C (_./H--3) 0.50
_P Ol_M (MICRONS) 20.00
TIME (SEC) O.OO
C."
O.D
-. ='._
..... --v
III
I
o!o
VELOCITY (.M./5) 129,00
TEMPEEATUQE (C) -L2,60
P_[SSUq[ (KPA) 90o_5
-U_IDITY (_) 100.00
_A_ (_-'M--3) 0.50
_CP OIAM (MICRONS) 2O.Gg
_IME (SEC) O,O0
ORIGINAL:PAG- iS
OF POOR QUALITY
0.0
-°,_
I _.T.:-T._5____ ...........
Figure 7.8: Concluded
119
0.5
0.0
-.2
_:ELCC1TY CM/$)
T_MPER_TURE (C)
P_LSSdR_ (KP_)
_U_I31TY (X)
L;_ (_./H--3)
CROP O[&M (MICRONS)
TIME (S_C)
129.00
-I2.60
90.75
IO0.OO
0.50
20.GO
0.00
ORIGINAL PAGE IS
OF POOR QUALITY
ix_= t IYO= -0.12000
S = -0,0_Z53
I
/
I
S
J °VELCCITY (.M/S) 129.00
T_MPER4/UR[ (C) -I2.&O
PRESSUR_ (KPA) 90.75
-_RI31TY (_) I00.00
LA_ (_/H--3) O.SO
C_P GI4M (H|C_ONS) 20.GO
TIM[ (S_C) D.O0
Y O.0
YO= -0.I1250 I
5 = O.01G:B !
I
iI f
I
Figure 7.9: Sample of the plots of the particle trajectories calculated in
subroutine IMPLIM.
120
V[LCCITY (.N/S)
T_HPERATURE (C)
PRL_SUR£ (KPA)
_U_IDITY (_)
L_C f_,/H-=3)
C_2P GI4H (HICRON$)
129.00
-12.60
90.75
100.00
0.50
20.00
0.00
ORIGINAE PAGE iS
OF POOR QUALITY
0.2
T 0.0
-.2
!
!
J
l
J
l
0 +
Figure 7.9: Concluded
•I00 _-
-, 13_"
-.100 --
.II_ -
-.116
rv -.120 --
-. IZq" --
-.128 -
-. 13,_ --
-*136
- • I '_0._ 3B
o
0
o
o
o
o
o
o
o
o
o
o
o
S (H)
Figure 7.10:Y0 vs. s data calculated in subroutine COLLEC for Example 2
121
ORIGINAl.. PAGE IS
POOR QUALIT _'VELOCITY (M/S) 129.9-6TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75HUMIDITY (X) I00.00
LWC (G/M,, ,, 3) O.SOOROP OIAM (MICRON) 20.00TIME (SEC) 80.00
a. Iced airfoil geometry
220 F
198 i
176
°°[I
22 _
do
-,lOt
..IO_ f-
-.135
I
_-..:_- [-
;
b. Particle release position vs. surface
impact distance
!.O r
o, Q L
_.8, L
I
:::E
c. Local collection efficiency vs. surfacelocation
o¢o_
o¢°_
^.::._ - ,_ . /
-27,e -
//
i •
c .?
e. Edge temperature vs. surface location
f,
_8
90
86
$2
78
7'+
;.Q _-._'_--:ca-._-._, -.'a; .%o _,"_;-_:.:_* :._, o."._o._-_-
$ cH_
Edge pressure vs. surface location
Figure 7.11: Icing parameter plots for the first timestep of Example 2.
122
0
°:
-2
-3
G
-7
-8
-9
-_
g,
VELOCITY (M/S) 129.LF6
TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75HUMIDITY (%) IOO,OOLWC (G/M-- 3) 0.50DROP DIAM (MICRON) 20.00
TIME (SEC) 60,00
I" _,f
f
5 -oLd8 -.!21 -._;_ -._07 -.'00 0.107 0.';_ 0.!21 C.128 0.J35
S (H)
Equilibrium surface temperature vs.surface location
zOO0
900
800
700
600o
5OO
-- '_00
300
200
]OC
, 5 - ?28 - ,Iz [ - .11
ORI(_IIVA[ PA(_E IS
OF POOR QUALITY
j,
4 -.!o7 -.Jog oJo? O.PI_ o.121 C.'28 O.J3._
s (M)
Ice density vs. surface location
2C00
:EO0
:tO0
:200
zFbC
_C.C
Z:Z
h.
,OOCEO
•COC'_!
.000_!
.COO3!
.0003C
.OOOE5x
•GC_,20
,CC_: =.
.CCC;_
i,
•._--:.: -.'c; -Joo o.o7 o.i]'_ o.121 o.l_'e oJ35
S _M)
Convective heat transfer coefficient
vs. surface location
5 -.CE - -.i_ . i . IOO O :07 2.; _ O,?I G.2_ 0.'35
S (M)
Equivalent saad-grain roughness
height vs. surface ]ocatlon
1.0
0.8
0,7
O.o
0.5
0,_
D,3 !
0,2
0,1
0 _ B -.107 -,lOb -,105 -olOq" -o103 -oI(32 -.101 0o100 O,iOl 0.102
S (M)
k. Freezing fraction vs. surface location
Figure 7.11: Concluded
123
: ! I ! f !-.IO -.OB -,06
0.10
0.08
0.06
O.Oq-
O.Og
I I f _.../
- • O'_" -sO,?. _''/_
/CALCULATED /STAGNATION POINTS--"
-,02
-.Dee
-.06
-.06
-.LO
n
p
m
w
f
• l I00 0.02.
i I l I I f ( fo.o_ 0.06 o.o6 o. I o
Figure 7.12: Locations of the multiple stagnation points in the second time
step of Example 2
124
0.00Q
. .008
.,,OZO
Figure 7.13: Locations of the multiple stagnation points in Example 2 after
speciryingl new axes limits
).25
0.020
O°Ot6
0.0_2
O.OOO
Y-.OOO -.OON" "_'-".1
- .009
-.OL2
-.016
I I 1 ItOO O.OOq O.0OB
//_I
,_ / ! ! I0.0[2 0.016 0.020
-.OZQ --
Figure 7.14: Iced airfoil with the pseudo-surface
126
ORIGINAL PAGE I_
OF POOR QUALITY
_EL_ITY (.N/S) 127,00
T[MPER_TURE (C) -12,60
P_E55_ (KPA) 90.75
-C_I_ITY (X) lO0oOO
O_SP GlUM (MICRONS) 20.09
TIME (SEC) O.OO
-.100
-.tO_
-.tO0
-.112
-,I!6
v -,t20
0-.t2_
-.t28
-,t32
-.t36
-.I_Q,
F
ow
• ' •0
@
0
o
o
o
o
0
o
0
o
o
o
_._, .._, _._,, .._, .._,, _._,, -.in, o.£o o.fo, oJo,
S (M)
Figure 7.15:Y0 vs. s data calculated in subrouting COLLEC for the second
time step of Example 2
127
a. Iced airfoil geometry
VELOCITY (M/S) 12g._6
TEMPERATURE (C> -12.60
PRESSURE (KPA) 90.75
HUMIDITY (%) I00.00
LWC (G/M--3) 0.50DROP OIAM (MICRON)20.O0
TIME (SEC) 120.00
196 I
]5_ F
Ello
86
66 _
"t2_
_.35
d,
OF POOR QUAU_Y
-.12B -.JZI -,lI'+ -.'07 ".lOG 0,_07 Ool]_ 0._21 0,128 O 135.
$ _M)
Edge velocity vs. surface location
-.lO0
-.I0_
-.IG8
-.112
--.1I¢
-.12Q
-.198
-.]32 I-.13¢
"'I_'_.zOB -,;O; -.'0¢ -.FOE -.;0_ -.lO3 -.;0_ -._31 0.100 O.'Oi O.102
S (M)
b. Particle release position vs. surface
impact distance
1.0
0,q
o. 8 //_
00:'-o/ /\
c._._o ._s _o3 -)c2 -.'_: c._oo o._o_ ; _.ro_"
S <M;
c. Local collection efficiency vs. surfacelocation
-2.0
-6.8
-9.2
-11.6
-16._=
-_: ._
-23,=
/
//
'c//
-2¢'_.".=E -.128 -,_21 -.ll_ -.'07 -.'CO 0.'C? O,l _" 0.'2: C.2E 0.I)5
S (H_
e. Edge temperature vs. surface location
]06
]02
q,,,
m. 86
82
f,
_. (M)
Edge pressure vs. surface location
Figure 7.16: Icing parameter plots for the second timestep of Example 2.
128
oF sPOOR QUALITy
0
-1
-2
-3
3
on
-,_.9 p,
I
/
129._&-12.6090.75
IO0.OO0.50
(MICRON)20.OO120.00
10o0
9o0
Boo
7oo
z bOO
50C
-- _00 1
3O0
20C
]CO
0.35 -.I_6 -._l ..I -.=C7 -.CO C.'O_--C-.!:_ O.;_i 0°;28 0_35
E ,M_
j. Ice density vs. surface location
VELOCITY (M/S)TEMPERATURE (C)
PRESSURE (KPA)HUMIDITY (X)
LWC (G/M''3)DROP DIAMTIME (SEC)
JI
fJ
"]1_.135 -.'2_ -.J2! ".ll't ".107 -.100 0.107 0.!I _' C._21 072B 0.i35
5 (M)
g. Equilibrium surface temperature vs.surface location
_500
_OCO
:750
1500
_25o_:000
5OO
ho
LL
E
0.155 :-._28 -.'21 . I + -.'C; -.lO0 OJO7 0._:_ 0.'21 OJ2B--O'_J. 35
S (M)
Convective heat transfer coefficientvs. surface location
•O00SO F
.000_5_
.000_0_
• 00035 F
•00030 F
.COOISL
.00C05-
:.Z .... '
S (y)
i. Equivalent sand-grain roughness
height vs. surface location
k,
"°F 1O.e {'-
0.7
0°_
3°2 E
I
0._.'_6
Figure 7.16: Concluded
-.L37 -.,Co -.!05 -.C_ -JC3 -.'_- -.IcI 0.'0_ 0.101 O.J02
S IM)
Freezing fraction vs. surface location
129
..... EXPERIMENTAL
THEORETICAL
VELOCITY (M/S) 129.00TEMPERATURE (C) -12.60
PRESSURE (KPA) 90.75
_ITY (_) mo.ooLWC (G/M s) 1.00DROP DIAM (MICRONS) 20.00
TIME (SEC) 120.00
Figure 7.17: Comparison of experimental and calculated
shapes for Example 2.
ice accretion
130
NACA 0012 : EXAMPLE 3CS2q¥ILIFTs 1IPARA • 11FInSTa )ISECI;D, $IFVORe tI)ICLT" 0CLT = 0.0ICHORD z 0CCL= 0.0I_{D= IISOL _ 0IPRINT = 0YFLLL= I_EHD
1.0000000 0.98999990.9000000 0.87500000.7500000 0.7250000
.0.6000000 0.57500000.4500000 0.42500000.3000000 0.27500000.1500000 0.12000000.0600000 0.05000000.0250000 0.02000000.0037500 0.00250000.0012500 0.00100000.0003750 0.00025000.0003750 0.00050000.0012500 0.00150000.0037500 0.00500000.0250000 0.03000000.0000000 0.07000000.1500000 0.17500000.3000000 0.32500000.4500000 0.47500000.6000000 0.62500000.7500000 0.77500000.9000000 0.92500001.0000000 0.00000000.0000000 -0.0018740
-0.0149000 -0.0179530-0.0310550 -0.0344110-0.0459040 -0.0479060-0.0560510 -0.0572430-0.0602260 -0.0600760-0.0536360 -0.0507320-0.0385350 -0.0356740-0.0262300 -0.0237200-0.0106990 -0.0086200-0.0058470 -0.0051q60-0.0029450 -0.00235600.0029450 0.00346200.0058470 0.00648500.0100990 0.01238600.0262300 0.02846200.0385350 0.04103800.0536360 0.05587900.0602260 0.06009400.0560510 0.05469800.0459040 0.04379500.0318550 0.02922100.0149000 0.01170000.0000000 0.0000000
CTRAJIGEPS = 0.4999999E-04DSHIFT= 0.20£-02VEPS z 0.9999999E-03LCM8= 0LCrlP= 0LEOH = 1LSYM= 0LYOR= 1LXOR" 1PiBDY- 1HEQ= 4HPL = 15tlSEAR= 50HSI= IT_[ISTPs 0.9999999E-03C£_(DCTRAJ2CIIORD = 0.30G: 0.0PIT= 0.0PITDOT = 0.0pRAT_= 0.0XORC = -4.0×_T_P = 0.50YOLIrl = 0.9999999[-04YOtlAX= 0.50/-01¥0MXN= -0.50E-01YORC z 0.9999996E-01EErZD_DISTFLWC= 1.0, 9*0.0DPD = 20.0, 9wO.OCFP= 1.0, 9w0.0CE?ID&ICEVIHF= 64.72_LWC= 0.500TAMB= 200.55PAIIB= 90748.0RI{= 100.0DPM;1 = 20.0XKIPIIT= 0.25E-03SEGTOL= 1.50CEND
0.9800000 0.9700000 0.9500000 0.92500000.8500000 0.8250000 0.8000000 0.77500000.7000000 0.6750000 0.6500000 0.02500000.5500000 0.5250000 0.5000000 0.47500000.4000000 0.3750000 0.3500000 0.32500000.2500000 0.2250000 0.2000000 0.17500000.1000000 0.0900000 0.0800000 0.07000000.0qS0000 0.0400000 0.0350000 0,03000000.0150000 0.0100000 0.0075000 0.00500000.0022500 0.0020000 0.0017500 0.00150000.0008750 0.0007500 0.0006250 0.00050000.0001250 0.0000000 0.0001250 0.00025000/0006250 0.0007500 0.0008750 0.00100000.0017500 0.0020000 0.0022500 0.00250000.0075000 0.0100000 0.0150000 0.02000000.0350000 0.0400000 0.0450000 0.05000000.0800000 0.0900000 0.1000000 0.12500000.2000000 0.2250000 0.2500000 0.27500000.3500000 0.3750000 0.4000000 0.42500000.5000009 0.5250000 0.5500000 0.57500000.6500009 0.6750000 0.7000000 0.72500000.8000000 0.8250000 0.8500000 0.87500000.9500000 0.9700000 0.9800000 0.98999990.0000000 0.0000000 0.0000000 0.0000000
-0.0036110 -0.0052390 -0.0082510 -0.0117000-0.0208880 -0.0237390 -0.0265150 -0.0292210-0.0368870 -0.0392810 -0.0q15850 -0.0437950-0.0497930 -0.0515600 -0.0531980 -0.0546980-0.0582620 -0.0590900 -0.0597070 -0.0600940-0.0596120 -0.0587940 -0.0575700 -0.0558790-0.0470040 -0.0452280 -0.0432520 -0.0410380-0.0340820 -0,0323620 -0.0304960 -0.028_620-0.0207970 -0.0172400 -0.0150780 -0.0123860-0.0081360 -0.0076230 -0.0070750 -0.006_850-0.0047660 -0.0043630 -0.0039310 -0.003_620-0.0016320 0.0000000 0.0016320 0.0023560
0.0039310 0.0043630 0.0047660 0.00514600.0070750 0.0076230 0.0081360 0.00862000.0150780 0.0172480 0.0207970 0.02372600.0304960 0.0323620 0.0340820 0.03567400.0432520 0.0452280 0.0470040 0.05073200,0575700 0.0587940 0.0596120 0.06007600.0597070 0.0590900 0.0582620 0.05724300.0531980 0.0515600 0.0_97930 0.04790600.0415830 0,0392810 0.0368870 0.034_1100.0265150 0.0237390 0.0208880 0.017_5300.0082510 0.0052390 0.0036110 0.00187400.0000000 0.0000000 0.00000o0 0.0000000
ORIGINAl/PAGE IS
OF POOR QUALITY
0 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 30 3I 30 40 40 40 40 400 40 40 40 40 40 40 40 40 40 40 40 40 40 40 40 40 41 4
Figure 7.18: Input data file for Example 3.
131
OF. POOR QUALIfy
a. Iced airfoil geometry
VELOCITY (M/S) 6q.73TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75
HUMIDITY (X) IOO.O0LNC (G/M,, ,,3) O.SODROP DIAM (MICRON)20.ODTIME (SEC) 60.00
:oc F,_0 L
BC "
zc_- ,/;'°" f Ii
i V_ so
"> _'0 _-
2G -I
:o,_ i£ -.26 -.)i -.i- -._; -._,C C.'C 7 C.I" C,.21 C.2E £.._
S t_:
d. Edge velocity vs. surface location
O,OICq
0.006 _-
C.OO6
!
O.O0 W _-
__.o_FO.OOO r
_-.ooa L!
-.00_ i-
-.00_
ff
J
-oOCB i
b. Particle release position vs. surface
impact distance
-10.=. -
-;].C _-
i_::.c r-
. . , . ,
^-:2.C _-
_.:2.= -i
_'- _ :-. C -
-:-.C -
'i
J
r I i'
? (_,,
e. Edge temperature vs. surface location
_.0
G._
O.e
0.7
0.6
,LO.5
h"
0.3
0.]
_.C
C°
I /
F /I3;_ -_ . _ -.005 0.o05 C.o]5 o. _,_=.
S (_
Local co1|ectionefficiencyvs. surface
location
IO0
I
Qe L
- 90
" ia $8
f,
82 r"
B_.35 ._E -,21 -.I- -.G7 -.00 _.C: C.:- .:._: _._6 C,.:._
S (*_,
Edge pressure vs. surface location
Figure 7.19: Icing parameter plots for the first timestep of Example 3.
132
ORIGINALPACE |SOF POOR QUALITY
VELOCITY (M/S) 6°r. 73TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75HUMIDITY (X) I00o00
LHC (G/M" N3) 0o50DROP OlAM (MICRON) 20oOOTIME (SEC) 60.00
0.0 -
-3,0 !"- I
_-7.5
--9.0 -
I
-12.C i
-X3,5 L-I
-: .Co'_ -.'2_ -._.i -o:,t .;07 -.o_
Equilibrium surface temperature vs.
surface location
g.
IOOG E90C
8CG 1-
I
;'05 _-
_oo_LSOD
-- _.00 _-
300 t
20C E_00
j.
I' ' I ' ' ' '
_ b -.2E -.21 -.i- o.'O; -._ rz.'_7 G.':'. 0.'2_ :..2E G.3E
S (M_
Ice density vs. surface location
e
hQ
80O 7
?20
_'_0
_OO _ /
- .o _
eC - f
_.'_5 "o2_ -o2i _ I:,+ -.O? -oGG O.C_ C.I- C.21 Co29 Oo._E
Convective heat transfer coe_icient
vs. surface location
Io0
0,?
0.8
0.5
C.'+
0.3
°.I
O.C
ko
, KM)
Freezing fraction vs. surface location
.CO0"5_
oCCO_G_
.CO0_O
oC°015_
• CCC:O r
.CCCC_ I-.=_ -._= -°'_: -.':- -.i_7 -.'OC C.'C: C _.'_:
i.
-.;Z_. C.=E
Equivalent sand-grain roughness
"height vs. surface location
Figure 7.19: Concluded.
133
a. Iced airfoil geometry
VELOCITY (M/S) 6ur.73TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75HUMIDITY (X) 100.00LWC (G/M,,,,3) 0.50DROP DIAM (MICRON) 20.00TIME (SEO) 120.00
O0
72
&_
56
_, _e
_ 32
16
$
Q,
d*
ORIGINAL PAGE IS
oF POORQUALITY.
5 -.t28 -.r21 -.IN -707 -._0 C.':17 0.l_ C,.2I 0.128 0,'_5
5 (e)
Edge velocity vs. surface location
0"01C F
oi0o_!
_.00_
O,OOC
_-.oo2
-.OON
m'O0 _
-.00£
-,olq
b,
S (M)
Particle release position vs. surface
impact distance
"°I0.9
0.8-
O,l
0.6
_o.5
_o._
0.3
0,2
0.]
o.o
C°
'5 0.025
$ (M)
Local collection efficiency vs. surfacelocation
-I0,0
-10.5
-II.5
"' .]3. r
-13.£
- I ",. C
-]_.£
"15"-_,!35 -.!2@ -.:?i -.ll" -.!07 -.loc G.'G7 O.'l _ 0.'_1 0.F28 0.1_5
S (M)
e. Edge temperature vs. surface location
]00
96
9_
90
c_ 88
06
11'4
f,
82
80" 5 -- "12 _ I *'_ i I " ] _ " " 0 ? m " 00 &.'Of 0.!I'_ 0.2] O.12B 0.135
S (H;
Edge pressure vs. surface location
Figure 7.20: Icing parameter plots for the second timestep of Example 3.
134
VELOCITY (M/S) 6°r. 73TEMPERATURE (C) -12.60PRESSURE (KPA) 90.75HUMIDITY (X) lO0.O0LNC (G/M"" 3) 0.50DROP OIAM (MICRON) 20.00TIME (SEC) 120.00
-0.0 I°I ,2
-2.'+ F"
-3,a _-
I
_ob.O
-10.8 L
":2"_.'3_ -.'28 -.'_'; -.I1_ -._07 -.100 0._0t O._l ", 0°'2; 0.'_5 0._35
S (M)
g. Equilihxium surface temperature vs.surface location
1000
900
800
700
z 600
_ 500¢J- _00
300
2OO
100
jo
PAGEisOF POOR QUALITY
5 -o:28 -.'21 -o'_V -o07 -.100 O.fO/ 0.'1_ 0.12| 0.25 0ol35
5 (M)
Ice density vs. surface location
600
5_C
_,80
_20
360
3oo=
2_c
180
_20
bo
h,
.00050
.0004
.ODOr,
.0003!
.00030
.00025
w.00020
,00015
.00010
.00005
.O000C-,:
L
!I ////
FJ' !-. '26 " i ...._-135 -,_ -,':* -,'_; -,'0C 0,'07 0,1_ 0°'21 3°28 0,'3_
¢. {M)
Convective heat transfer coe_cientvs. surface location
1,0
0,9
0.5
0,?
0,b
0,5
0,3
0,'2
0,!
0,.Cl
ko
°,"_'E -,l_l °,]1_ -,'07 -,'00 0°IOF o,i;_ G,'_I Oo;2B 0.135
$ (M)
Equivalent sand-grain roughnessheight vs. surface location
Figure 7.20: Concluded
W
5 -.o,s -._05 0._05 0.6_5 0._5S (M)
Freezing fraction vs. surface location
135
EXPERIRENTAL
THEORETICAL
VFLDC|TY (H/S) 6_.73
T[HPERATUR[ (C) -|2.60
PRESSURE (KPA) 90.76
HUMIDITY (_) 100.00
LHC (G/N--3) 0.60
DROP D[AH (HiCRONS) 20.00
TINE (SEC) 120.00
Figure 7.21: Comparison of experimental and calculated ice accretion shape
for example 3.
136
F
b-
0,10 --u..
10 20 30DROPLETDIAMETER,d, pM
Iqo
Figure 7.22: Droplet distribution specified for Example 4.
1,0(} m
.80--
.qo
.20
10 20 30 qo
DROPLETDIAMETER,d, MM
Figure 7.23: Cumulative volume fraction vs. droplet diameter for the
droplet distribution specified in Example 4.
137
HACA 0012 : EXAMPLE 6
E324¥ILIFT = 1
IPARA= 1
ZFZRSTS 3
ISECHDs 3
IPVOR" 1
IfICLTs OCLT z 0.0
ZCHORD = 0
CCL a 0.0ItlD = 1
ISOL" 0
ZPRZHTz 0IFLLL • 1
CEND
1.0000000 0,98999990.9000000 0.8750000
0.7500000 0.7250000
0.6000000 0.5730000
0.4500000 0.42500000.3000000 0.2750000
0.1300000 0.1250000
0.0600000 0.0500000
0.0250000 0.02000000.0037500 0.0025000
0.0012500 0.0010000
0.0003750 0.00023000.0003730 0.9005000
0.0012500 0.0015000
0.0037500 0.00500000.0250000 0.0_00000
0.0600000 0.07000000.1500000 0.1750000
0.3000000 0.3250000
0.4500000 0,6750000
0,6000000 0.62500000.7500000 0.7750000
0.9000000 0.9250000
1.0000000 0.0000000
0.0000000 -0.0018740
-0.0140080 -0.0179530
-0.0318550 -0.0344110
-0.0459040 -0.0479060
-0.0560510 -0.0572430-0.0602260 -0.0600760
-0.0S36360 -0,0507320
-0.0385350 -0.0356740
-0.0262300 -0.0237260
-0.0106990 -0.0086200-0.0058470 -0.0051460
-0.0029450 -0.0023S60
0.0029450 0.0034620
0.0058470 0.0064850
0.0100990 0.01238600.0262300 0.0284020
0.0385350 0.0410380
0.0536360 0.0558790
0.0602260 0.0600940
0.0560510 0.0566980
0,0459040 0,04379500.0318550 0.0292210
0.0149080 0.0117000
0.0000000 0.0000000
CTRAJ1
GEPS_ 0.4999999E-04DSHIFTz 0.20£-02
VEPS" 0.9999999E'03
LCM8= 0LCMP" 0
LEQM= 1
LSYM = 0
LYOR" 1LXOR= I
tlBDY= I
/lEO= 4
- HPL- 15HSEAR" 50
NSI- 5
TIMSTPm 0.9999999E-03
CEHD
CTRAJ2
CHORD- 0.30
O = 0.0PZT= O.0
PITDOT- 0.0
PRATK z 0.0
XORC= -4.0
XSTOP- 0.50
¥0LIM- 0.9999999E-04YOMAX _ 0.50E-Ol
YOMZH- -0.$0E-01
¥ORC- 0.9999996E-0I
CEND
CDZST
CFPw 1.042, 4_1.0, 5N0.0
0.9800000 0.9700000 0.9500000
0.8500000 0.8250000 0.8000000
0.7000000 0.6750000 0.6500000
0+5500000 0.5250000 0.50000000.4000000 0,3750000 0.3500000
0,2500000 0.2250000 0.2000000
0.1000000 0.0900000 0.0800000
0.0450000 0.0400000 0.03500000.01_0000 0.0100000 0.0075000
0.0022500 0.0020000 0.0017500
0.0008750 0.0007500 0.00062500.0001250 0.0000000 0.0001250
0,0006250 0.0007500 0.0008750
0.0017500 0.0020000 0.00225000.0075000 0.0100000 0,0150000
0.0350000 0.0400000 0.04500000.0800000 0.0900000 0.1000000
0.2000000 0.2250000 0.2500000
0.3500000 0.3790000 0.40000000.5000000 0.5250000 0.5500000
0.6500000 0.5750000 0.7000000
0.8000000 0.8250000 0.8500000
0.9500000 0.9700000 0.9800000
0.0000000 0.0000000 +0.0000000
-0.0036110 -0.0052390 -0.0082510
-0.0208880 -0.0237390 -0.0255150
-0.0368870 -0.0392810 -0.0415850
-0.0497930 -0.0515500 -0.0531980-0.0582620 -0.0590900 -0.0597070
-0.0596120 -0.0587940 -0.0575700
-0.0470040 -0.0452280 -0.0432520
-0.0360820 -0.0323620 -0.0304960
-0.0207970 -0.0172480 -0.0150780
-0.0081360 -0.0076230 -0.0070750-0.0067640 -0.0063630 -0.0039310
-0.0016320 0.0000000 0.00103200.0039310 0.0043530 0.0047660
0.0070750 0.0076230 0.0081360
0.0150780 0.0172480 0.02079700.0304960 0.0323520 0.0340820
0.0432520 0.0452280 0.0470040
0.0575700 0.0587940 0.0596120
0.0597070 0.0590900 0.0582620
0.0531980 0.0515600 0.0497930
0.0415850 0.0392810 0.0368870
0.0255150 0.0237390 0.02088800.0082510 0.0052390 0.0036110
0.0000000 0.0000000 0.0000000
DPD- 4.0, 12.0o 20.0, 28.0, 36.0, 5"0.0
FLWC = 0.0082, 0.2037, 0.5762, 0.2037, 0.0082, 5_0.0
_ENO
CICEv2ttr= 129,460
L_C- 0.750
TArIB_ 260.5498
PAM8= 90748.0
RH = I00.0
DPMM" 20,0
XKIHIT: 0.00035SEGTOL s 1.50
CEHD
0.9250000
0.7750000
0.62500000,4750000
0.3250000
0.1750000
0.07000000.0300000
0.0050000
0.0015000
0.00050000.0002500
0.00100000,0025000
0,0200000
0.05000000.1250000
0.2750000
0.42500000.5750000
0.7250000
0.8750000
0.9899999
0.0000000
-0.0117000
-O.0292210
-0.0437950
-0.0546980-0.0600940
-0.0558790
-0.0410380
-0.0286620
-0.0123860
-0,0054850-0.0034620
0,00235600.0051660
0.0086200
0,02372600.0356740
0.0507320
0.0600760
0.0572430
0.0479060
0.0344110
0.01795500.0018740
0.0000000
603
603
603603
603
603
603603
603
603
603603
603603
603
603603
603
603
0 0 3603
603
603
1 I 3
604
604
604604
604
604
604
604
604
6 0 q604
604604
6 0 ¢t,
604604
604
0 0 4
604
0 0 4
604
604604
11 4
Figure 7.24: Input data file for Example 4.
138
ORIGINAL PAGE IS
OF POOR QUALITY
a. Iced airfoil geometry
VELOCITY (M/S) 129.'_6TEMPERATURE (C) -12,60PRESSURE (KPA) 90.75
HUMIDITY (X) IO0.OOLWC (G/M w" 3) 0.75DROP DIAM (MICRON)20.O0TIME (SEC) 60,00
0,01. _
0,0]_
0.00_
0.00
_o.oo
0.00(o
-.00_
-.OOd
-. 00'_
-,Of;
o:,
de
,0-._'+S-._36 -.{_Z4 -._lZ'-.O00 0.(_12 0._2'+ 0._3_ O._e 0.-'_60
$ (M)
Particle release position vs. surface
impact distance, d,_ = 20 microns
°.°'i_0.9)
0.009
O,O0o
_-o.oc3
o 0"000 j
-.003
-.OOb
. .000
" "O121_"_-:? o -._--.(_, -._, -._,_ -.,%oo._ o._2, o.(_, o._, o._,o$ (M}
b. Particle release position vs. surfaceimpact distance, d,_ = 4 microns
0.0;_
C.O_2E
O'OCc !
O.O0_'
0.000
_-.003
-,00_
"'°°qi!-.0;2
S (M)
e. Particle release p_osition vs. surfaceimpact distance, d,_ = 28 microns
O.OI5_ O.OIS
0,0121 O.OIE
0.009 1 0.009
O.OOb 0.006
_0.003 _0.003
0,000 i _0"000>o.003 _-.003
-.O0oL -.006
-.0091 -.009
.O_Ef6 -.012
.o:so-._5-._.-.;_, -._ -.;ooo.;:_o.o__.;_. o.;,_o._,o -.o_,S (M)
c. Particle release p_osition vs. surface f.impact distance, d,_ = 12 microns
J
_,6 _6 _2. _2 .6ooo.6_o._,o._,o.6,o.66oS (M)
Particle release p_osition vs. surfaceimpact distance, d,. = 36 microns
Figure 7.25: Icing parameter plots for the first timestep of Example 4.
139
:.z --
i.: .-
,3 ,
/i
//
//
/
VELOCITY (M/S)TEMPERATURE (C)
PRESSURE (KPA)
HUMIOITY (X)
LWC (G/MwN3)
OROP OIAM
TIME (SEC)
0.060
g°
\
\
,,\
ORIGINAl: PAaE_is12 9. _ 6 OF POOR QUALITY-12.60
90.75
I00.000.75
(MICRON) 20.00
60.00
!:0 i
107
(
j. Edge pressure vs. surface locationLocal collection efficiency vs. surface
location
h,
hfi
i
I
' ," i .-, " .'C -T -': .7_ 3 -C .-J __.._=_1_ ; --O .'2 i 0 .I_8 O.135
3
Edge velocity vs. surface location
o
-1
-2
-3
u_-6
-I
-8
-q
-I0
k.
'35 -.z28 -.'21 -.If'," -.;OT'_-.-_,'_.-JC_ - OJl_ 0._21 0_\___=-
S c,')
Equilibrium surface temperature vs.surface location
2
"'.-L . ÷ -., . " ._" *.3'- C._, u.: W _.2; G._g8 0J35
Edge temperature vs. surface location
1500
1350
1200
1050
_0O
_sobOO
_50
3O0
150
g.
l,
' "- J_e - ._ ! - .zl ',' - JOT---; _;%--c ._'t', _- C,.; .:" o T2 : -i', J, L_, ,
S ,H:
Convective heat transfer coefficient
vs. surface location
Figure 7.25: Continued.
140
ORIGINAt PAGE IS
OF POOR QUALITY
VELOCITY (M/S) 129._6TEMPERATURE (C) '12.60PRESSURE (KPA) 90.75HUMIDITY (%) I00.00LHC (G/M"" 3) 0.75DROP DIAM (MICRON) 20.00TIME (SEC) 60.00
• OOOSO F
.O00_SL
.OOC_O
.00035
.00030
.00025
*00020
.000i5
.000)0
.00005
.ODD00
m,
5 -.I2B -.'2l -.Ii_ -.!Of -[00 O.TG; O.::_ O.i_I 0J26 C
S (M)
Equivalent sand-grain roughness
height vs. surface location
10oo
_00
BOO
700
z _00
SO0
-- _OG
30O
200
_00
0[35 -.i26 -J2i _.I_
n°
-.IO; -,I00 O.'O? O.'_ 0721 Oo!_B 0.1)5
S _M)
Ice density vs. surface location
1.0
0.9
0,8
0,7
0.6
0.5
0.3
0.2
0.1
O.&
O,
o ' -.6_, ' -.6,_ ' o.6,2 ' o._, ' o.AoS (M)
Freezing fractionvs. surface location
Figure 7.25: Concluded.
141
l--
t_JIx]
i.O
0,9
0.II
0.#
0.6
O.S
O,,e-
O.3
0.,?
0.I
o.o
NACA0012 AIRFOIL
NORMALDISTRIBUTION
140NODISPERSED
DISTRIBUTION
/ \
-.°3, -._, _,_ .ho o._,, o.'_+, o._,o
S (M)
Figure 7.26: Comparison of the calculated local collection efficiency vs.
surface distance for a normal and monodispersed droplet distributions with
mass median diameters of 20.0 microns.
f- ELECTROTH_R/_d.HEATER/
//
,Ill'Figure 7.27:
Example 5.
Electrothermal heater on a NACA 0012 airfoil modeled in
142
HACA 0012 : THERMAL A/!CS2qYILIFT = |ZPARA m 1IFIRST" 3ISECNns 3ZPVOR- 1INCLT s 0CLT= 6.0ZCHORD= 0CCL = 0.0I)¢Dz IISOL= 0IPRIHT" 0IFLLL= I&EHD
1.0000000 0,98999990.9000000 0.87500000,7500000 0.72500000.6000000 0.57500000.6500000 0.62500000.3000000 0.27500000.1500000 0.12500000.0600000 0.05000000.0250000 0.02000000.0037500 0.00250000.0012500 0.00100000.0003750 0,00025000.0003750 0.00050000.0012500 0.00150000,0037500 0.00500000.0250000 0.03000000.0600000 0.07000000.1500000 0.17500000.3000000 0.32500000,6500000 0.¢750000O.buO050O 0.62500000.7500000 0.77500000.9000000 0.92500001.0000000 0.00000000,0000000 -0.0018760
-0,0169000 "0.0179530-0,0318550 -0.0366110-0.0_590_0 -0.0679060-0.0560510 -0.0572630-0.0602260 -0.0600760-0.0536360 -0.0507320-0.0385350 -0.0356760-0.0262300 -0.0237260-0.0106990 -0.0086200-0.0058670 -0.0051660-0.002?450 -0.0023560
0,0029_50 0.00366200.0058470 0.00668500.0106990 0.01238600.0262300 0.02866200.0385350 0.06103800.0536360 0.05587000.0602260 0.06009¢00.0560510 0:05669800.0659060 0.06379500.0318550 0.02922100.01_9080 0.01170000.0000000 0.0000000
&TRAJI
0.0800000 0.9700000 0.95000000.8500000 0.8250000 0.80000000.7000000 0.6730000 0.65000000.5500000 0.5250000 0.50000000.q000000 0.3750000 0.35000000.2500000 0.2250000 0.20000000.1000000 0.0900000 0.08000000.0¢50000 0.0_00000 0.03500000.0150000 0.0100000 0.00750000.0022500 0.0020000 0.00175000.0008750 0.0007500 0.00062500.0001250 0.0000000 0.00012500.0006250 0.0007500 0.00087500.0017500 0.0020000 0.00225000.0075000 0.0100000 0.01500000.0350000 0.0¢00000 0.06500000.0800000 0,0900000 0.10000000.2000000 0.2250000 0.25000000.5500000 0.3750000 0.60000000.5000000 0.5250000 0.55000000.6500000 0.6750000 0.70000000.8000000 0.8250000 0.85000000.9500000 0.9700000 0.58000000.0000000 0.0000000 , 0.0000000
-0.0036110 -0.0052390 -0.0082510-0.0208880 -0.0237390 -0.0265150-0.0368870 -0.0392810 -0.0615850-0.0697930 -0,0515600 -0.0531980-0.0582620 -0.0590900 -0.0597070-0.0596120 -0.0587060 -0.0575700-0.0670060 -0.0652280 -0,0632520-0.0360820 -0.0325620 -0.030_960-0.0207970 -0.0172680 -0.0150780-0.0081360 -0.0076230 -0.0070750-0.0067660 -0.0063630 -0.0039310-0.0016320 0.0000000 0.0016320
0.0039330 0.0063650 0.00676600.0070730 0.0076230 0.00813600.0150780 0.0172680 0.02079700.0304960 0.0323620 0.03608200.0632520 0.0652280 0.06700600.0575700 0.0587940 0.05061200.0397070 0.0590?00 0.05826200.0531980 0,0515500 0.06979300.0615850 0.0392610 0.03588700.0265150 0.0237390 0,02088800.0082510 0.0052390 0.00361100.0000000 0.0000000 0.0000000
GEPS = 0.6999909E-06DSHZFT = 0.20E-02VEP5= 0.0990099E-03LCMB= 0LCrlP _ 0LEQM = ILSYM: 0LYOR= 1LXOR # I);BDY= 3HEO: 6HPL= 15IISEAR= 50HSZ= 3TZI1STP = 0.0909999E-03CEIIDCTRAJ2CIIORD = 0.30G- 0.0PIT= 0.0PITDOT- 0.0PRATK • 0.0XORC 2 -4.0XSTOP= 0.50YOLIM= 0.9999999E-0_¥OMAX = 0.50E-01YOM171= -0.50E-01¥ORC = 0.9999996E-01_E.D&DISTCFP=I.0, 9_0.0DPD=20.0, ?_0.0FLt4C=I.00, 9e0.0CEr<D£ICEVIHF= 128,608LHC= 0.500TAMB: 265.00PAMS= 90768.0RH= 100.0DPMM= 20.0XKIHIT: 0.20E-03SEGTOL= 1.50QCOHD=Sq"0.0,71N6000.,]95N0.0_EHD
0.92500000.77500000.62500000,47500000.32500000.17500000.07000000.03000000.00500000.00150000.00050000.00025000.00100000.00250000.02000000.05000000.12500000.27500000,62500000.57500000.72500000.87500000.98999990,0000000
-0.0117000-0.0202210-0.0437950-0.0566980-0.0600960-0.0558790-0,0610380-0.028_620-0.0123860-0.0066850-0.0036620
0.00235600.00516600.00862000.02372600.03567600.05073200.06007600.0572_300.0¢790600.03661100.01795300.00187_00.0o0o0oo
ORIGINAL PAGE IS
OF POOR QUALITY
603603603603603603603603603603603603603603603603603603603603603603603I [ 36 0 66066066 0 _,6 0 c,6066066066066066066066066066 0 ¢6066066065 0 66066 0 q60¢606I I ¢
Figure 7.28: Input data file for Example 5.
143
I-ICE ACCRETIOfl
/ ON THE HEATER
I
/
I
_--ICE ACCRETION
AFT 0F THE HEATER
a. Iced airfoil geometry
ORIGINAL F_E'_ _S
OF POOR QUALITY
VELOCITY (M/S)TEMPERATURE (C)PRESSURE (KPA)HUMIDITY (X)
LWO (G/M.N3)DROP DIAM (MICRTIME (SEC)
128.@1-8.1590.75
IO0oO00.50
ON)20.O060.00
\
S
2_F'Q.'35 -.128 -.;21 -.;1'+ -.107 -.;OC
S _M)
d.
25O
225
200
175
150
125
log
75
50
c.'o__FT:__:'_
Edge velocity vs. surface location
-.:oC .
-.:0- L.
L-.;72 F
_:..: 7_ L
-.;_C L
b°
S/
_:: :_., _-. _-.-T_;.:,_._2_;_.._o-o._oeo._ao
Particle release position vs. surface
impact distance
- i
2,? -
5.1 "-
S :=)
c. Local collection efficiency vs. surfacelocation
o
-3
-6
-9
-IE
-15
._
-El
-El
-30
e.
I]0
105
tOO
_. _0
1S
70
f.
bS
/._f /
;, *.L_8 -.l_l -,ll'f -?07 -.106 0.[07 C,ll_ 0.12; 0.128 0.13_
S (M)
Edge pressure vs. surface location
Figure 7.29: Icing parameter plots for the first time.step of Example 5.
144
ORIOINAE PAGE |S
OF POOR QUALITY
5
3
2
I
0
-2
-3
go
VELOCITY (M/S) 128._I
TEMPERATURE (C) -8.15PRESSURE (KPA) 90.75HUMIDITY (%) IOO.O0LWC <G/M,*3) 0.50DROP DIAM (MICRON)20.OOTIME (SEC) 60.00
Jf
f
-.'2, -.'2, -.',_ -.'o, -.'oo o.'_, o.'_* o.'_, o_8 °/35S (#4)
Equilibrium surface temperature vs.
surface location
I000 I
QO0
• 70G
_°°° I50C
)OC -
200 l
)OC [-
J,
I ,iJ
f_.'35 - .'_'8 - .;2 i --.11 _' - .PO7 - .IO0 0.:07 G ,11'_ 0.I_ ] 0.'28 0.J35
Ice density vs. surface location
_800 II_20
]2bO
1080 _
120
]80 _-
_.l .. fi . I t . .I _ - .10_ -._(lO 0.107 0.11 • 0.:_ l O.'E8 0.f35
$ (M)
h. Convective heat transfer coefficientvs. surface location
],0
0.9
0,8
0.7
0.6
0o_
0.3
0°2
0ol
o..o
k,
' -.b_ "_"_-.&_ _ -.(_8 _ -._o_ _o0 .
$ (M)
Freezing fraction vs. surface location
o00050 c
•000'_5_-
.O00EO_
.OOOlS_
:Oo:Oo::F.C_O_0%_ -.:2e -.:,?.t -._;_ -.TO;' -.roo o.lo_ o._t,_ e._t 0._,?,8 o._,s
S (M)
i. Equivalent sand-grain roughness
height vs. surface location
Figure 7.29: Concluded.
145
Chapter 8
PROGRAMMING AIDS
This section contains information regarding the coding of LEWICE to aid
users who require a more advanced understanding of the program. Descrip-
tions of the subroutines, common blocks, and work files are included, along
with flow charts of various sections of the program.
8.1 Descriptions of Subroutines
The subroutines will not be discussed individually in this user's manual.
Instead, a description can be found in the program listing in COMMENT
statements preceding most subroutines. These descriptions include the pur-
pose of the subroutine, the input and output variables, and additional notes
describing special features of the subroutine.
8.2 Diagnostic and Error Messages
In a program as complex as LEWICE, the programmer must provide mes-
sages informing the user of any abnormalities in the calculations. The most
common error messages are discussed in this section. They are grouped by
the program module in which they will occur, i.e., potential flow calcula-
tion, particle trajectory calculation, or thermodynamic and ice accretion
calculation.
When an error message or unusual situation occurs, the first step should
be to check the description of the input parameters found in Section 5.0.
The following descriptions of the error messages will assume that this step
has already been completed, and will concentrate on how the error may
relate to certain aspects of the icing condition or geometry being evaluated.
8.3 Potential Flow Calculations
All of the lines of data input to the potential flow code are identified by
a card type number found in the most right-hand column in each line of
146
data. When the data line is read, this value is checked against the value
of the card type that was anticipated. If these numbers do not match, an
error message is printed and the program terminated. This error condition
is usually caused by having input values in the wrong columns on a line of
data.
Another error occurs occasionally when stagnation points are calculated
behind (downstream) of the large horns of a glaze ice accretion. The error
will usually be characterized by _division by zero" messages. The situation
cannot be corrected by forming a pseudo-surface as described in Section 7.2
and Appendix C. However, the case should be re-run with a larger timestep
which will make the predicted glaze ice accretion somewhat smoother and
may allow the calculations to continues.
Another error condition can occur when multiple stagnation points are
calculated which cannot be removed by the formation of a pseudo-surface,
and a stagnation point has been manually selected. In this case, there will
be at least two locations where the local velocity is 0.0 m/s. When the
compressible, dimensional surface velocity is calculated from the incom-
pressible, non-dimensional values (subroutine VEDGE), division by zero
errors can again occur. It is best to force the calculations to continue
through this error, if possible, because the locations of the error may be
downstream of the impingement region and, therefore, will not affect the
ice accretion shape. If the calculations cannot be continued, re-run the case
with a larger timestep.
8.4 Particle Trajectory Calculations
Most of the errors that occur in the particle tr_ectory calculations result
from inaccuracies in the flow field or errors in input data. Errors caused
by improper input parameters will generally be accompained by diagnostic
messages, which will be discussed below.
Subroutine RANGE will allow a total of 30 trajectories to be calculated
while searching for a trajectory that passes above and below the body.
If two such trajectories are not identified, the following message will be
printed and the program stopped:
30 Trajectories are calculated in RANGE. Run aborted.
147
The most probable cause of the error is that the values of YOMAX and
YOMIN have been input incorrectly. If the values are correct, review the
body coordinates that are being used by the program.
A run can be terminated in a similar manner in subroutine IMPLIM. In
this case, if the number of trajectories required to identify the upper and
lower impingement limits exceed NSEAR, the run is terminated. The value
of NSEAR is input by the user through namellst TRAJ1 and is normally
set equal to 50. If the limiting value of NSEAR is reached, the value of
YOLIM may be unnecessarily small or there may be a problem with the
way the program has read or interpreted the body coordinates.
In subroutine COLLEC, the program will be terminated if the value of
NPL is greater than 100. The value of NPL is input by the user through
namelist TRAJ1, and typical values are between 10 and 20. If this error
occurs, verify that the value of NPL is in the proper column in the input
file.
Occasionally, errors occur in the flow field near the surface of the body,
especially for convoluted glaze ice accretions. In these cases, very large
local velocities are calculated which cause exponent overflows or negative
arguments in subroutine ABFORM. If these errors occur, try to force the
calculations to continue through this error because, if a bad impingement
point is calculated as a result of the error, it can removed before calcu-
lating the local collection efficiency. Unfortunately, once this error has
been encountered in one timestep, it will probably occur in all subsequent
timesteps.
8.5 Thermodynamic and Ice Accretion Calculations
if the program completes the flow field and particle trajectory calculations
with no errors, there generally will be no additional errors in the ther-
modynamic calculations. There are temperature limits in the subroutines
used to calculate the pressure of water vapor over liquid water and over
ice. These calculations are performed in subroutines PVW and PVI, re-
spectively. The temperature ranges, shown below, are sufficient for any
anticipated application of the code.
Vapor Pressure over Liquid Water: 223.15 K < T < 323.15 K
148
Vapor Pressure over Ice : 213.15 K < T < 273.15 K
8.6 COMMON Blocks and Work Files
In a program of this size,much of the information must be transfered
between subroutines through COMMON statements. Table 8.1 listseach
COMMON block in the program, the general purpose of the variables in
the COMMON block, and the subroutines in which each block is found.
No open COMMON statements are used in LEWICE.
In addition to COMMON blocks, much information ispassed between
subroutines through temporary work files.The work filesand the purpose
of each are shown in Table 8.2. Many of these filesare used in the potential
flow calculations (subroutine $24Y), and will not be described in detail
because littlework was done to modify the potential flow calculations.
8.7 Size of the Code
Because LEWICE combines three complex computer codes into a single
computational algorithm, the code requires a substantial amount of com-
puter memory for both the source code and operation. On the IBM 370
computer used at NASA Lewis, the source code itself requires approxi-
mately 1400 K of memory. The input file requires only 4 K, but 500 K
should be allowed for the output file, especially if a droplet distribution has
been specified. Also, a restart file is generated by the program which will
be the same size as the input file. The work files used in the code require
approximately 150 K of memory. They are erased at the termination of the
run and, therefore, could be placed in a temporary work area.
149
Table 8.1 Common Blocks Used in LEWICE
COMMON Block
LABELS Contents:
Variables:
Subroutines:
CNTL Contents:
Variable:
Subroutine:
PSEUDO Contents:
Variables:
Subroutines:
ICECOM Contents:
Variables:
Subroutines:
Description
Parameters to be placed on plots
IDR, VINF, LWCKG, TAMB, PAMB, RH,
MAIN, BORDER
Control parameters used in the plotting
and particle trajectory routines
LOPT, LEQM, IPLOT, LCMB, LCMP
MAIN, TRAJ, IMPLIM, COLLEC, INTIG,
RANGE, MODE, READIN, VELCTY, COMB2I)
x-coordinates of the pseudo surface that havc
been generated
IPSURF, XPS
MAIN, STAG, VEDGE, PSURF, NEW45,
MODE, READIN
Variables used in the thermodynamic and
ice accretion subroutines
X, Y, SEGLEN, SEGLIN, VE, TE, PE,
RA, XK, BETA, TSURF, FFRAC, HTC, RI
QCOND, MDOTC, MDOTE, MDOTRI, MDOTTI,
MDOTT, DICE, VINF, TAMB, PAMB, RH,
DPMM, LWCKG, CPA, CPI, LV, LF, VISC,
PI, NPTS, NTHI, NTLOW, ISTAG
CNSTS, STAG, PSURF, NWPTS, SEGSEC,
ICE, CDYLYR, EBAL, COMPF, COMPT,
NWFOIL, OUTPUT, PLOTD
150
Table 8.1 Continued
COMMON Block Description
DROP Contents:
Variables:
Subroutines:
Droplet distribution data
NSI, FLWC, IRS, DPD, EPT
PLOTD, TRAJ, EFFICY
BFLAG Contents:
Variables:
Subroutines:
Potential flow data
IDB, INL, IFL, NL, LIFT, IBMF, ISAV1,
ISAV2, ISAV3, BTITLE, IBT, IBST,
IBTOT, NELTOT, ITRB, INMB, CHORDB,
IBD, LIFTOT, IPRB, IFST, ISEC,
FTITLE, IPVR
$24Y, MAIN1, MAIN3, ASSEMB, ELFORM,
FLOWS, MAFORM, PRNTEL, VXYOFF
COMBO Contents:
Variables:
Subroutines:
Potential flow data
CCL, INCLT, CLT, ALPHA, SUMDS, TLU,
IND, ALPHAO, CNU, SMDSWF, MIO
$24Y, MAIN1, MAIN3, ASSEMB, COMBO,
FLOWS, MAFORM, OFFBOD, VXYOFF
FILEID Contents:
Variables:
Subroutines:
Potential flow data
IFILE1, IFILE2, IFILE3, IFILE4,
IFILE5, IFILE6, IFILE7, IFILE8,
IFILE9, IFILIO, IFILll, IFIL12,
IFIL13, IFIL14, IFIL15, IFIL16,
IFIL17, IFIL18, IFIL19, IFIL20
$24Y, REWYND, FILRS, MAIN1, MAIN3,
SOLVE, ASSEMB, COMBO, ELFORM, FLOWS,
MAFORM, VPROFF, VXYOFF
MDATA Contents:
Variables:
Subroutines:
Potential flow data
ISOL, IOFF, NONU, MBNU, IPRINT, MORE, M
$24Y, MAIN1M MAIN3, ASSEMB
151
Table 8.1 Continued
COMMON Block
ROTAT Contents:
Variables:
Subroutines:
ELDATA Contents:
Variables:
Subroutines:
GCOEFS Contents:
Variables:
Subroutines:
COM Contents:
Variables:
Subroutines:
SPACER Contents:
Variables:
Subroutines:
SIGMAS Contents:
Variables:
Subroutines:
GEOMD Contents:
Variables:
Subroutines:
GCFF Contents:
Variables:
Subroutines:
Description
Potential flow data
NROT, ROTRAD
$24Y, ASSEMB, FLOWS, MAFORM
Potential flow data
XO, YO, DS, SA, CA, CURV, DL
MAIN1, ASSEMB, ELFORM, MAFORM
Potential flow data
CD, CF, CG, CI, WF
MAIN1, ASSEMB, ELFORM, MAFORM
Potential flow data
IFILL
MAIN1, MAIN3, FLOWS, VPROFF, VXYOFF
Potential flow data
WKAREA
SOLVE
Potential flow data
CSIG, CK
COMBO, FLOWS, VXOFF
Potential flow data
X, Y, XSAVE, YSAVE
ELFORM, FLOWS, BTITLE
Potential flow data
CD, CF, CG, CI, WF
FLOWS, VXYOFF
152
Table 8.1 Continued
COMMON Block Description
ELDD Contents:
Variables:
Subroutines:
Potential flow data
X, Y, DS, SA, CA, CURV, DL
FLOWS, VXYOFF, READIN, VELCTY
OVER Contents:
Variables:
Subroutines:
Potential flow data
V1Y, V2Y, V3Y, V4Y, V5Y, V6Y, V3X,
V4X, VSX, V6XVPROFF
BODY Contents:
Variables:
Subroutines:
Coordinates describing the body
geometry
NPTS, XSH, YSH, X, Y
TRAJ, MODE, READIN, PLTRAJ
BOUND Contents:
Variables:
Subroutines:
Coordinates of the most forward and
aft points of the body geometry and
boundaries for the particle trajectory
calculations
XFRNT, YFRNT, XREAR, YREAR, XSTOP,
YLO, YUP
TRAJ, RELEAS, IMPLIM, INTIG, RANGE,
MODE, READIN
IMP Contents:
Variables:
Subroutines:
Particle impingment data for use in
the collection efficiency calculation
S, SW, YO, IS
TRAJ, IMPLIM, COLLEC, ORDER, INTIG,
RANGE, MODE, READIN
INIT Contents:
Variables:
Initial conditions for particle
release
XIN, YIN, DPM, RL, PITDOT, PIT,
VINF, VXP, VYP, AOAR
153
Table 8.1 Continued
COMMON Block Description
Subroutines: TRAJ, RELEAS, IMPLIM, COLLEC, INTIG,
RANGE, DIFFUN, MODE, COMB2D
DIFF Contents:
Variables:
Subroutines:
Variables used in the particle
trajectory equations
Q, AMASS, G, YYI, VISC, CF
TRAJ, DIFFUN
STEP Contents:
Variables:
Subroutines:
Time step and error criteria used
in the integration of the particle
trajectory equations
TIMSTP, EPS
TRAJ, IMPLIM, COLLEC, RANGE
TP15 Contents:
Variables:
Subroutines:
Variables used to calculate the
combination solution of velocity
ABCD, ATOTAL, VC15, RSORTC, NX15
READIN, COMB2D
NUM Contents:
Variables:
Subroutines:
Variables used to calculate the
flow field velocities
N, M, IND, IBTOT, LIFTOT
READIN, VELCTY
GCF Contents:
Variables:
Subroutines:
Parameters used to calculate the
flow field velocities
CD, CF, CG, CI, WF, CSIG, CK, SIG
READIN, VELCTY
FLG Contents:
Subroutines:
Parameters used to calculate the flow
field velocities
READIN, VELCTY
154
COMMON Block
VEX Contents:
Subroutines:
Table 8.1 Continued
Description
x- and y-components of the flow
field velocity
VELCTY, COMB2D
Table 8.2 Output and Work Files Used in LEWICE
i 3
File
Number
1,2,4,
7-18,
21
5,6
2O
22
Type Description
Binary
Character
Character
Character
These are work files used in the potential
flow calculations. Since no modifications
were made to $24Y, the contents of these files
have not been examined in detail.
Unit 3 contains the y0 vs. s points for each
droplet diameter. This file is read in
subroutines EFFICY and PLOTD.
These are the read/write defaults to displayinformation on the screen.
This file contains the airfoil coordinates for
all timesteps. The file is read in subroutine
PLOTD to plot the airfoil.
Unit 22 contains the airfoil segment distances
used in the collection efficiency
calculations.
155
Table 8.2 Continued
File
Number
24
3O
35
36
45
56
Type
Character
Binary
Character
Character
Character
Character
Description
This is an internal input file for subroutine
TRAJ. It is created from the input on
unit 35. There is no updating of unit 24 for
the second or subsequent timesteps.
This is the main working file for the
program. It contains the current values of
the body coordinates, surface distances,
edge velocities, pressures, etc. for each
segment.
This is the primary input file prepared by
the user. It is used to set up all of the
other internal input files.
This is the restart input file produced by
the program after each timestep. It is
identical to the input file on unit 35,
except that the body coordinates are of the
current ice shape. The icing time
corresponding to the ice shape coordinates
is also included in namelist ICE.
This is the internal input file for the
potential flow code ($24Y). It is formed from
the data input on unit 35.
This is the primary output file for LEWICE.
It contains the printed output from all
portions of the code.
156
8.8 Execution Times
When an ice shape is predicted, the largest portion of the execution time is
spent on the particle trajectory calculations. The CPU time required to run
the example cases found in Section 7.0 on the IBM 370 computer are given
in Table 8.3. Also indicated are the total number of particle trajectories
calculated in each, and the average CPU time per trajectory.
Table 8.3 CPU Time for Examples 1-5
Number of
Example CPU Time Trajectories CPU-sec
Number (see) Calculated Trajectory
1 362.52 67 5.41
2 350.80 71 4.90
3 395.01 68 5.81
4 719.30 205 3.51
5 185.50 44 4.22
With these results, the computational time required for a specific icing
condition can be estimated if the speed of another type of computer is
known compared to an IBM 370.
8.9 Getting LEWICE Operational
When LEWICE is transferred to a system other than that at NASA Lewis,
it must first be compiled. A FORTRAN 77 compiler has been used to
compile the version used at NASA Lewis. The graphics commands used
in LEWICE are from a system that is unique to NASA Lewis and will
not be directly applicable to any other system. The name of this graphics
package is GRAPH3D, but most of the commands in LEWICE are from
GRAPH2D, the predecessor of GRAPH3D. Calls to the graphics package
are located in subroutines STAG, PSURF, PLOTD, BORDER, INTIG,
PLTRAJ, and EFFICY. The graphics in LEWICE use only the simplest
commands, and, therefore, modification of the commands should not be
difficult; unfortunately, it will probably be time-consuming.
157
I_|st of References
.
.
Ackley, S.F. and Templeton, M.K. UComputer Modeling of Atmo-
spheric Ice Accretion." Cold Regions Research and Engineering Lab-
oratory Report 79-4, 1979.
Lozowski, E.P., Stallabrass, J.R., and Hearty, P.F. _The Icing of an
Unheated Non-Rotating Cylinder in Liquid Water Droplet-Ice Crystal
Clouds." National Research Council of Canada Report LTR-LT-96,
1979.
3. Hankey, W.L. and Kirchner, R. "Ice Accretion of Wing Leading
Edges." AFFDL-TM-85-FXM, 1979.
.
,
.
.
.
.
10.
Cansdale, J.T. and Gent, R.W. UIce Accretion on Aerofoils in Two-
Dimensional Compressible Flow - A Theoretical Model." Royal Air-
craft Establishment Technical Report 82128, 1983.
MacArthur, C.D., Keller,J.L.,and Leurs, J.K. "Mathematical Mod-
eling of Ice Accretion on Aerofoils."AIAA-82-0284, 1982.
Olsen, W., Shaw, R., and Newton, J. "Ice Shapes and the Resulting
Drag Increase for an NACA 0012 Airfoil." NASA Technical Memo-
randum 83556, 1984.
Tribus, M.V., et al. "Analysis of Heat Transfer Over a Small Cylinder
in Icing Conditions on Mount Washington." American Society of
Mechanical Engineers Transactions, Vol. 70, 1949, pp. 871-876.
Messinger, B.L. _Equilibrium Temperature of an Unheated Icing Sur-
face as a Function of Airspeed." Journal of the Aeronautical Sciences,
Vol. 20, No. 1, 1953, pp. 29-42.
Olsen, W. "Close-up Movies of the Icing Process on the Leading Edge
of an Airfoil." NASA Lewis Research Center Movie C-313, 1985.
Hess, J.L. and Smith, A.M.O. "Calculation of Potential Flow About
Arbitrary Bodies." Progress in Aeronautical Sciences, 8:1-138, (D.
Kuchemann, editor). Elmsford, New York, Pergmon Press, 1967.
158
11.
12.
13.
14.
15.
16.
17.
18.
19.
20.
Harris, C.D. "Two-Dimensional Aerodynamic Characteristics of the
NACA 0012 Airfoil in the Langley 8-Foot Transonic Pressure Tunnel."
NASA TM 81927, April 1981.
Frost, W., Chang, H., Shieh, C., and Kimble, K. "Two- Dimensional
Particle Trajectory Computer Program." Interim Report for Contract
NAS3-22448, 1982.
Chang, H., Frost, W., and Shaw, R.J. "Influence of Multidroplet Size
Distribution on Icing Collection Efficiency." AIAA-83-0110, 1983.
Hobbs, P.V. Ice Physics. Oxford University Press, Ely House, Lon-
don, 1974.
Carlson, D.J. and Haglund, R.F. "Particle Drag and Heat Transfer in
Rocket Nozzles." AIAA Journal, Vol. 2, No. 11, 1964, pp. 1980-1984.
Gear, C.W. "The Automatic Integration of Ordinary Differential
Equations." Comm. ACM 14, 1971, pp. 176-179.
Gear, C.W. "DIFSUB for Solutions of Ordinary Differential Equa-
tions." Comm. ACM 14, 1971, pp. 185-190.
Macklin, W.C. "The Density and Structure of Ice Formed by Accre-
tion." Quarterly Journal of the Royal Meteorological Society, Vol.
88, 1962, pp. 30-50.
Bragg, M.B., Gregorek, G.M., and Shaw, R.J. _An Analytical Ap-
proach to Airfoil Icing." AIAA-81-0403, 1981.
Gent, R.W., Markiewicz, R.H., and Cansdale, J.T. "Further Studies
of Helicopter Rotor Ice Accretion and Protection." Paper No. 54,
Eleventh European Rotorcraft Forum, September 1985.
159
Appendix A
DERIVATION OF THE ICING ENERGY EQUATION
In this appendix, the thermodynamic processes that take place during
the formation of an ice accretion are identified and expressed mathemati-
cally to form the icing energy equation. This derivation is similar to that
presented in Reference A-l, except that the equation is applicable to an
arbitrary control volume instead of a control volume situated on the stag-
nation line.
A.1 Definition of the Control Volume
The control volume to be analyzed is located on the surface of the body
and extends from outside the boundary layer to the surface of the body,
as shown in Figure A-1. It encloses a distance along the external surface,
and, for dimensional completeness, extends one unit length in the spanwlse
direction (into the page). The lower boundary of the control volume is
initially on the surface of the clean geometry, and moves outward with the
surface as the ice accretes. Therefore, the control volume is always situated
on either the clean or iced surface, and any accumulated ice is considered
to leave the control volume through the lower boundary. This definition is
important in conduction heat transfer, discussed later in this appendix.
A.2 Mass Balance on an Icing Surface
An evaluation of all mass entering and leaving the control volume is
shown in Figure A-2. A mass balance equation can be formed from these
terms as shown below.
rh, + rhr_. - rh, - rhro., = rh_ (A - 1)
At the stagnation point, there will be no water inflow along the surface
so therefore, m_n = 0.0.
Since the freezing fraction is defined as the proportion of the total mass
of liquid entering the control volume that freezes in the control volume, it
can be expressed by the following equation:
f - m' (A - 2)
160
Substituting Equation {A-l) into Equation {Ao2), the water flow out of
the control volume can be expressed as
m,_, = {1- l){m, + m,,.}- m, (A-3)
A.3 Energy Balance on an Icing Surface
The same control volume concept is used to formulate the energy bal-
ance on the icing surface. The First Law of Thermodynamics for a control
volume can be expressed as: energy inflow rate -- energy outflow rate +
energy storage rate.
The modes of energy transfer, illustrated in Figure A-3, are as follows:
Mode of Energy Transfer
1. Impinging Water
2. Water Flow Into Control Volume
3. Evaporation4. Water Flow Out of Control Volume
5. Ice Accumulation Within Control Volume
6. Convection
7. Conduction through the Skin
Energy Flow Rate
rhciw,T
#nr,. iw,.,,.( _- , )
¢n.io,.,,.
rh...,i.,._,.{O
qcAs
qkA8
Using the convention that energy flow into the control volume is positive,
the terms can be summed to yield the general form of the energy equation:
rh, {w.T + mr,. {w,°u.(,-l) -" the i,_,.u. -t- rh.o., iw,.u.
+ rh_ it°,,. + q. As + qk As (A-4)
The evaluation of the terms of the energy equation has been made by
various authors, most notably by Sogin {Reference A-2), Lowzowski {Refer-
ence A-3), and Cansdale and Gent {Reference A-4). The following sections
will evaluate each of the terms of Equation (A-4).
161
A.4 Impinging Water
Since droplets are essentially brought to rest when they strike an object,
it is appropriate to use the stagnation enthalpy defined as
v2i.,T = c,.,. (r. - 273.15)+ ®
2(A - 5)
The arbitrary reference for zero enthalpy used in this study is water at
273.15 K. Substituting Equation (A-5), the energy flow rate of the imping-
ing water becomes
r_c iw,T = Trtc Cp,,o
where
m,"" = LWC(Voo)_ (A- 7)
A.5 Water Flow Into the Control Volume
The water flowing into the control volume will be at the surface tem-
perature of the preceding control volume. The enthalpy can therefore be
expressed as
i.,...(__,)= % ....,(,_,) (Tw(,-,) - 273.15)
where (i-l) denotes that the specific heat and temperature are evaluated at
the conditions of the proceding control volume. The runback water energy
flow rate into the control volume can therefore he expressed as
rh,,. {.,,.,(;-1)= m,;. c_ ..... (,_,) (T,,,,(__,)- 273.15) (A-9)
162
A.6 Evaporation
The rate of energy transfer from the surface because of evaporation is
given by
• .[ ]rh, su.,u, -- m, c_,,.o..(T_,r - 273.15) -}- L, As (A - 10)
where rne"" is the evaporative mass transfer flux and L, is the latent heat of
vaporization.
The mass transfer rate is analogous to the convective heat transfer rate
and can be written as
.H
m e =gAB (A-11)
where g is the mass transfer coeffcient and AB is the evaporative driving
potential. The mass transfer coefficient, g, can be evaluated using the
analogy to heat transfer given by the following equation found in ReferenceA-5:
hc ( Pr _ "_7g = cp--_ \So/
(A- 12)
In Equation (A-12), Pr is the Prandtl number and Sc is the Schmidt num-
ber.
The mass transfer driving potential is analogous to the temperature
difference in the convective heat transfer equation. In the case of evapora-
tion, the driving potential is a vapor concentration difference instead of a
temperature difference. The equation used in this study is similar to that
derived by Sogin (Reference A-2), and given as
AB = (A- 13)
(1/.622)P,/T, - P,.,,,,/T,_,,
163
This term accounts for compressibility effects, as does the term derived
by Cansdale in Reference A-4.
When the water droplets freeze on impact (f = 1.0), there is no liquid
water on the surface to be evaporated; however, water vapor can still leave
the surface through sublimation. In this case, Equations (A-10), (A-11),
(A-12), and (A-13) are still used to determine the rate of energy transfer
from the surface, except that the latent heat of sublimation, L,, is used in
Equation (A-10) instead of the latent heat of vaporization, Lu.
A.7 Water Flow Out of the Control Volume
The water flowing out of the control volume will be at the surface tem-
perature of the control volume, allowing the enthalpy to be expressed as
i_,°ur(i) -: c_ ..... (0 -- (T"ffir¢d) -- 273.15) (A -- 14)
where (i) denotes that the specific heat is to be evaluated at the surface
temperature of the control volume being analyzed. Using Equation CA-3),
the runback water energy flow rate can be expressed as
rh, o,,, i,,,,°,,,(,)- [(1-f)(rh,+rh,,,,)-_h.] cj,,,,,.,,,,o (T.,,,(,)-273.15) (A- 15)
A.8 Ice Accumulation Leaving the Control Volume
As previously discussed, the control volume remains on the surface of the
geometry as the ice accumulates within the control volume.
From the definition of the freezing fraction, Equation (A-2), the freezing
rate is
The enthalpy of ice referenced to water at 273.15 K is
(A-16)
ii,°., : cp, .... (Tw - 273.15) - L! (A- 17)
164
Combining Equations (A-16) and (A-17), the rate of energy leaving the
control volume in the accumulated ice can be expressed as
fn, i,.°u, = f (The + Th,,.) [%, .... (T_, - 273.15) - LI] (A- 18)
A.9 Net Convective Heat Flux
The local value of the aerodynamically induced heat flow to or from
the outer boundary of the control volume is determined by the convective
cooling and kinetic heating of the surface. The net convective heat flow
can therefore be defined by the following equation:
qo/_ = ho(T.., - To.) A_ (A - 19)
In this equation, T0_, is the surface temperature and 2",, is the adiabatic
wall temperature. The adiabatic wall temperature is given by
v:(A- 20)
To_ = T_ + r_ 2 %.
where T, and V, are the temperature and velocity at the edge of the bound-
ary layer, respectively, and rc is the recovery factor. The local temperature
is calculated from the pressure coefficients calculated by the potential flow
code using the isentropic relationships. Substituting Equation (A-20) into
Equation (A-19), the expression for the convective heat flow rate becomes
qcas= ho(T..,-T.r_ V,_.
c-_) As (A - 21)
The heat transfer coefficient is calculated using the integral boundary
method described in Appendix B.
A.10 Conduction From the Airfoil Surface
When the cloud is first encountered, a temperature difference will exist
between the wetted surface and the inner structure of the airfoil. Prior to
165
entering the cloud, this inner structure is assumed to be at an equilibrium
temperature. The evaluation of the resulting conductive heat flow rate is
dependent on knowing the thermal conductivity and detailed geometry of
the inner structure of the airfoil.
After a layer of ice forms on an unheated surface, the temperature of
the skin should again reach an equilibrium temperature. Since ice is an
insulator, any heat transfer through the skin will not affect the growth of
the ice accretion at the air/ice interface.
In a thermal deicing system, an ice layer is allowed to form and heat is
then applied at the ice/skin interface. The effect of this heat is to melt the
ice attached directly to the surface, thereby allowing the ice to shed due
to the aerodynamic forces acting on the ice accretion. Currently, LEWICE
is not capable of analyzing this deicing phenomenon because a thermal
analysis would be required not only at the air/ice interface but also at the
ice/surface interface. A complete description of the current capability to
model a thermal deicing system is given in Reference A-6.
A thermal anti-icing system differs from a deicing system in that suffi-
cient heat is applied to prevent any ice from forming. The formulation of
the icing energy equation in LEWICE should be applied to thermal anti-
icing systems only to determine the minimum heating requirements to keep
ice from forming on the surface. The heat flux from the skin is specified as
a function of s and is assumed to be from the inner control volume bound-
ary. On the first timestep, this boundary is the uniced surface. If the heat
input is not sufficient to keep ice from forming, the heat input on the second
timestep would be assumed to come from the iced surface and incorrectly
neglects the thermal conductivity of ice and the effect of the varying ice
thickness on the surface. An example of the application of the code to a
thermal anti-icing system is discussed in Section ?.5.
166
The energy terms can now be summed to form the complete energy
balance for an icing surface used in LEWICE. This equation is as follows:
[(I - f)Crh, + Th,,,,) -- rh,] c,,.,,., (T_, - 273.15)4-
)'(rhc- )'h,.,) [c)),,,., (T). - 273.18) - L/]+
h, [T,_, - T, 2cp. J
The solution of Equation (A=22) is presented in Section 4.3.2.
(A - 22)
167
List of References
1. Ruff, G.A. "Analysis and Verification of the king Scaling Equations."
AEDC-TR-85-30 Vol. 1 (Revised), 1985.
2. Sogin, H.H. "A Design Manual for Thermal Anti-Icing Systems."
Wright Air Development Center (WADC) Technical Report 54-313,
1954.
3. Lozowski, E.P., Stallabrass, J.R., and Hearty, P.F. _The Icing of an
Unheated Non-Rotating Cylinder in Liquid Water Droplet-Ice Crystal
Clouds." National Research Council of Canada (NRC) Report LTR-
LT-96, 1979.
4. Cansdale, J.T. and Gent, R.W. "Ice Accretion on Aerofoils in Two-
Dimensional Compressible Flow - A Theoretical Model." Royal Air-
craft Establishment Technical Report 82128, 1983.
5. Kreith, F. Principles of Heat Transfer. Harper & Row, Publishers,
Inc., New York, 1973.
6. Leffel, K.L. "A Numerical and Experimental Investigation of Elec-
trothermal Aircraft Deicing." NASA CR 175024, 1986.
168
0
/
o//°
_/ o
/0\/ \
o
o
CLEAN AIRFOIl./
ICE SURFACE
Figure A-l: Identification of a control volume.
2.
\\ 3.
\ S.
\
IFIPINGING WATER Mc
EVAPORATION _e
WATERFLOW OUT OF CV MrOUT
WATER FLOW INTO CV t_rl x
ICE ACCUMULATION _iLEAVING THE CV
Figure A-2: Mass balance for a control volume.
169
i //'_%
I.
/// 3.
q.
5,
6,
7.
II_INGING WATER _Iciw,T
£YAPO_TIO_ _eiv,suR
_/Aff.RFLO_OUTOF ¢V _rouTiW,su_
k_TEaFLOWIMTOCV _rxNiw,suR
ICE ACCUPLATION _i i i ,SURLEAVINGTHECV
CONVECTION qc As
CONI_I"I ON qK As
_C:iw,T + " . +qKAS " . + ' . +_i i +qcSsturin IWoSUR = Helv,stm 14rOUTIM,SUm I,SUR
Figure A-3: Energy balance for a control volume.
170
APPENDIX B
INTEGRAL BOUNDARY LAYER METHOD ON AN ICED
SURFACE
As described in the text, the evaluation of the boundary layer character-
istics using a complete Navier-Stokes solver would be too time-consuming
to be practical in an interactive program such as LEWICE. An integral
boundary layer solution was therefore developed to account for surface
roughness and variable velocity in the calculation of the convective heat
transfer coefficient. The original algorithm was developed by UDRI, but
was modified in the current version of LEWICE.
B.1 Characterization of the Ice Surface Roughness
The integral boundary layer method to be applied in LEWICE is re-
quired not only to determine the convective heat transfer coefficient on the
iced surface in the laminar and turbulent regions, but also to determine the
location of the transition from laminar to turbulent flow (transition point).
The transition to turbulent flow is caused primarily by the surface rough-
ness of the iced surface which acts to trip the boundary layer from laminar
to turbulent flow. Also, once turbulent, the surface roughness elements
enhance the convective heat transfer coefficient by 1) increasing the skin
friction coefficient and 2) increasing the effective surface area from which
heat transfer takes place.
A representative surface of an actual ice accretion is shown in profile in
Figure B-1. The size and shape of the surface roughness elements found on
typical ice accretions are functions of the atmospheric and meteorological
conditions at which the ice is formed. Unfortunately, there is insufficient
data to characterize the size and shape of the surface roughness as a func-
tion of those conditions. Also, the complex roughness patterns found on
typical glaze ice accretions are beyond the analysis capability of an integral
boundary layer method. Therefore, an alternate method to characterize
the surface roughness is required.
Analysis of rough surfaces has been performed by numerous investiga-
tors, one of the earliest and most well-known being Nikuradse (Reference
B-l). These experiments dealt primarily with turbulent flow in pipes that
171
were artificially roughened with uniform grains of sand. Schlichting (Ref-
erence B-2) introduced the concept of equivalent sand-grain roughness as
a means of characterizing other types of roughness elements by referring
to the equivalent net effect produced by Nikuradse's experiments. In this
application, the irregular roughnes8 elements of an iced surface are repre-
sented by a value of equivalent sand-grain roughness height, k0, as shown
in Figure B-2. This value is specified by the user and is constant during the
calculation of a given icing condition. The value of ko should be changed as
a function of the atmospheric and meteorological parameters of the icing
condition using the guidelines discussed in the text.
B.2 Calculation of the Boundary Layer Characteristics
Determination of the Transition Location
The evaluation of the boundary layer is begun at the stagnation point
(s = 0.0). The calculations are initiated by determining the location of the
transition for laminar to turbulent flow, i.e., the transition point. The crite-
ria for transition, developed by Von Doenhoff (Reference B-3), assumes that
the flow will become turbulent when the local roughness Reynolds number
is greater than 600. The empirical criteria, based on data obtained using
sand-grain type roughness elements, are therefore given by the following
equation
R,, = k. > 600 (B - )V
where k0 is the equivalent sand-grain roughness height representing the
actual ice surface roughness. The velocity at y -- k,, designated V_, (Figure
B-2) must be determined to evaluate the local roughness Reynolds number.
The following is the method used to determine Irk, found in Equation (B-l).
Assume that the laminar velocity profile can be represented by a 4th
order polynomial of the form
172
where 6 is the boundary layer thickness, and V, and y are defined in Figure
B-2. This assumption is known as the Pohlhausen approximation (Refer-
ence B-4, pp. 310-311). By applying the following boundary conditions at
y=O:
a=V 1 ap dV. (B-3a)ay, ; _ -v"i:
lira --a"V = 0 n = 1, 2, 3, ... (B- 3b)v-.oo ay"
it can be shown that the expression for V/V, resulting from Equation (B-2)
is
V(y)- [2(y/6) - 2(y/6)' + 2(y/6)'] + 1/6 A (y/,_) C1 - y16) 3 (B 4)
v,
where
A= 62/u dVe (B - 5)
If we let y = ko in Equation (B-4), the velocity at y = ko can be written
as follows:
Vk =[2(k,/6) - 2(k,/6)' + (k./6)'] + 1/6 A (k./6)(1 - k./6)' (B-6)v,
To apply this equation, the boundary layer thickness, 6, must be evaluated.
The laminar momentum thickness, St, is defined in Reference B-4, p.
244, as
8,=fo '_V" (1 -- FY--_)dyf. (B- 7)
173
Substituting Equation (B-4) into Equation (B-7) and integrating from
y = 0 to y = 6, it can be shown that 6 is related to the laminar momentum
thickness by the following approximation:
6 = s.s 0_ (B - 8)
From the integral momentum equation, the laminar momentum thick-
ness can be evaluated using Thwaites formula (Reference B-4, p. 315) which
is given by the following equation:
.45u fo° V6d °
If it is assumed that the velocity at the edge of the boundary layer, V,,
is the surface velocity calculated by the potential flow equations, Equation
(B-9) can be numerically evaluated to determine 0t for each segment on
the body. Equations (B-6) and (B-8) can then be applied to determine Vk
as a function of s, and, therefore, Equation (B-l) can be evaluated along
the surface to determine whether the flow has transitioned from laminar to
turbulent flow.
Laminar Convective Heat Transfer Coefficient
If the boundary layer is found to be laminar at a surface distance, s,
the convective heat transfer coefficient for flow over a constant temperature
body of arbitrary shape is calculated using an equation developed by Smith
and Spaulding and described in Reference B-4, pp. 327-329. This equation
is given as
t_,(_)= .2o6_ v,-'." v,'."d_ (B-IO)
where _ is the thermal conductivity of air.
Turbulent Convective Heat Transfer Coefficient
174
If, upon evaluating Equation (B-l), it is found that the boundary layer
is turbulent, Equations (B-7)-(B-10) are not applicable, and an alternatemethod to determine the convective heat transfer coefficient must be de-
veloped. Using a technique outlined in Reference B-5, an overall Stanton
number can be developed using the thermal and momentum laws of the
wall for fully rough flow. This equation is given in Reference 13-5, p. 132
as
st = I/2 (B- 11)P,,+ O/st.)
The terms of this equation that must be evaluated are the skin friction
coefficient, c/, and the roughness Stanton number, Stk. The experimental
data for air (Reference B-6) suggest that the turbulent Prandtl number,
Pn, is approximately constant and equal to 0.9.
Assuming for now that the values of c! and Stk are known, the turbu-
lent heat transfer coefficient is calculated using Equation (B-11) and the
definition of the Stanton number. Therefore,
h, Cs) = S'tpV,cj, = [ c!/2 ]Pr, + V/_(1/,S'tk) 1 .af/',cp
(B- 12)
The expressions for the skin friction coefficient and the roughness Stan-
ton number are now developed.
Skin Friction Coefficient
If the boundary layer has been found to be turbulent, i.e., the roughness
Reynolds number is greater than 600.0, the surface can be considered to
be fully rough (Reference B-5, p. 186). A basic characteristic of the fully
rough surface is that the skin friction coefficient, el, is independent of the
Reynolds number. In this region, the pressure drag on individual roughness
elements dominates and viscosity is no longer a significant variable. With
this assumption, an expression for the skin friction coefficient can be devel-
oped from the momentum law of the wall for fully rough flow (Reference
B-5, pp. 186-188) as follows
175
c! .41 ] _-- __ l,,( se4.00 , J2 ."'_ k, +2.568)
(B- 13)
where 0t is the turbulent momentum thickness and ko is the equivalent sand-
grain roughness height. (This equation was derived in a manner similar
to Equation 10-45 in Reference B-5 except that Equation 10-43 was not
simplified.)
The turbulent momentum thickness is evaluated using the momentum
integral equation in a manner similar to that for the laminar momentum
thickness. The equation for 0t is given in Reference B-5, p. 175 as
[.0156 Vf "s6 ] .s= Lv,.. /o" d. (B- 14)
Since the turbulent boundary layer is proceeded by a laminar boundary
layer, the numerical integration of Equation (]3- 14) is begun at 8 =str
instead of s = 0.0. The laminar momentum thickness already existing at
s : .st, must then be added. Equation (B-14) can therefore be written as
01 0/; ]-0tea)= _ ,. V_'Sed8 + O,(n..)(B-15)
where 0_ is evaluated using Equation (B-O) and Ve is the surface velocity
calculated by the potential flow code.
Roughness Stanton Number
The roughness Stanton number is developed from the thermal law of
the wall for fully rough flow, and is given in Reference B-5, p. 231 by an
equation of the form
Sit : C Pr -'44 (B - 16)
176
where V, is the shear velocity. In Equation (]3-16), C is a constant that
must be determined from experimental data and is a function of the type
of roughness. Data for a rough surface composed of closely-packed spheres
yields a value of C = 1.0 (Reference ]3-6). Setting the Prandtl number,
Pr, equal to 0.72 and substituting the values for C and Pr into Equation
(B-16), the expression for Stk becomes
(B- 17)
The shear velocity, u,, is evaluated using the equation from Reference B-5,
p. 187.
v,= Vf_-I/2 (B- 18)v,
In this equation, c! is determined from Equation (B-13).
B.3 Method of Solution
To correctly apply the equations previously discussed, the integration
procedure should be identified. As discussed in the text, the geometry is
represented by a set of Cartesian coordinates (nodes) connected by straight
line segments, as shown in Figure B-3. The stagnation point is designated
s = 0.0, and will always fall on a nodel 1 point. The s values used in the
integration correspond to the midpoint of each of the body segments. The
calculation of the boundary layer characteristics is begun by evaluating
Equations (B-6), (B-8), and (B-9) for s = 0.0 to s = 81. The transition
criteria, Equation (B-l), is then applied, and, if the flow is found to be
turbulent at this point, it is assumed to be turbulent at each segment
downstream. Equations (B-13), (B-15), (B-l?), (B-18), (B-11), and (B-12)
are applied to calculate h_ if the boundary layer is turbulent. If the flow is
laminar, Equation B-10 is used to calculate hc and the turbulence criteria
is checked at the next segment. This procedure is then repeated for the
lower surface.
177
B.4 Comparison with Experimental Data
The results of the integral boundary layer method described in the pre-
vious sections have been compared to experimental convective heat transfer
data collected by Achenbach (Reference ]3-7). The current method was also
compared to an integral boundary layer method developed by Makkonen
(Reference B-S).
An excellent discussion of the analytical method developed by Makko-
nen and the comparisons to experimental data can be found in Reference
B-8. The work by Makkonen also includes a discussion about the applica-
bility of an integral boundary layer method to the calculation of convective
heat transfer characteristics over an ice accretion shape. Therefore, a de-
scription of the experimental data and detailed analysis of the results will
not be presented in this appendix. Instead, the results of the integral
boundary layer method described in this appendix will only be compared
to the results in Reference B-8 and the general trends identified.
The experimental measurements were made on a 15-cm diameter cylin-
der roughened with grains of sand at various Reynolds numbers. The rough-
ness element height, k, is 0.9 mm and the equivalent sand grain roughness
height, k°, is 1.35 ram. The method developed by Makkonen uses both
the maximum probable roughness height and the equivalent sand grain
roughness height. The method described in this appendix uses only the
equivalent sand grain roughness. Figure B-4 shows a comparison of the
analytical results of LEWICE (with ko = 1.35 mm) and Makkonen to the
experimental results. At a Reynolds number of 4.8 x 104, the method of
LEWICE shows a transition at an angle of approximately 50 °, while no
transition is predicted by Makkonen's results or in the experimental data.
Similar transition locations and location of the maximum heat transfer co-
efficient are predicted by both analytical methods for Reynold's numbers
of 2.8 x 10 s and 8.8 x 10 s. However, the magnitude of the maximum heat
transfer coefficient is over-predicted by the method used in LEWICE.
Since the current method uses only a single roughness parameter, there
is some question whether the maximum probable roughness or the equiva-
lent sand grain roughness height should be used in comparisons with exper-
imental data. A comparison of the analytical and experimental results with
k0 = 0.9 mm in LEWICE is shown in Figure B-5. These results compare
178
more favorably with the method of Makkonen and with experimental data
than those in Figure B-4, but still over-predict the maximum value of the
convective heat transfer coefficient.
Measurements of convective heat transfer have also been made on simu-
lated wooden ice accretion shapes roughened with grains of sand (Reference
B-9). Figures B-6a, b, c, and d show the comparisons of the values cal-
culated by LEWICE with experimental data for 2, 5, and 15 rain glaze
ice accretions. In these cases, the maximum probable roughness height of
0.00033 m was used in the calculations. These results show that the pre-
dicted values of hc generally compare well with experiment in the leading
edge region where much of the accretion process will take place.
179
Appendix B
List of References
1. Nikuradse, J., Forsh. Arb. Ing.-Wes. No. 361, 1933.
2. Schlichting, H., Ing. Arch.. Vol. 7, 1936, pp. 1-34.
3. Von Doenhoff, A.E. and Horton, E.A. _Low-Speed Experimental
Investigation of the Effect of Sandpaper Type of Roughness on
Boundary-Layer Transition." NACA TN 3858, 1956.
4. White, F.M., Viscous Fluid Flow. McGraw-Hill, Inc, 1974.
5. Kays, W.M. and Crawford, M.E., Convective Heat and Mass Trans-
fer.2nd Edition, MacGraw-HUl Book Company, New York, 1980.
6. Pimenta, M.M., Moffat, R.J., and Kays, W.M. Report No. HMT-
21, Department ofMechanical Engineering, Stanford University,May
1975.
7. Achenbach, E. "The Effectof Surface Roughness on the Heat Transfer
from a Circular Cylinder to the Cross Flow of Air." "International
Journal of Heat and Mass Transfer.",Vol. 20, 1977, pp. 359-369.
8. Makkonen, L. "Heat Transfer and Icing of a Rough Cylinder." "Cold
Regions Science and Technology." Vol. 10, 1985, pp. 105-116.
9. Van Fossen, G.J., Simnoneau, R.J., Olsen, W.A., and Shaw, R.J.
"Heat Transfer Distributions Around Nominal Ice Accretion Shapes
Formed on a Cylinder in the NASA Lewis Icing Research Tunnel."
NASA TM 83557, January 1984.
180
y_6//
BOUNDARYLAYER--\ //
\ /1 S.\\ //r SURFACE k
\ / I ROUGHNESS
/" [
•,y // d./_"
I'/,,./., - ',,/ /---...__ X--ICE
Figure B-1" Identification of the boundary layer terms usedin the integral boundary layer method.
//
//
//
/!
Figure B-2: Identification of the computational surface beingevaluated by the integral boundary layer method.
181
+y
STAGNATIONPOINT
(S " 0.0) -'-....
NODES/1%
I/ _ %,,/ I "
LS 1
+X
Figure B-3: Analytical representation of a typical geometry.
10 I I I
-- LEWICE, xs = 0.00135 M
------ RAKKONEN(REF. B-8)
0 EXPERIRENT (REF. B-7)
I I I I I
RE
8.8 x 105
Q-
0 //
o //
//
/
/
/
/
/
/
/
/
/ o/
2.8 x 105
o 0 o
oo
o
q,8 x 10q o
oo
I I I I
0 10 20 _0 qO
0 0 "" "_ _
0 0 0I l I I
50 60 70 80 90
AN6LE, PEG
FigureB-4: Comparison of caluclated and experimental corrective
heat transfer characteristics,LEWICE k, -- 0.00135m.
182
10 l l I
LEgICE, Ks = O.O00S M
I_KKONEN (REF. B-8)
EXPER]FENT (REF. B-7)
I i ! i I
RE
8.8 x 105
z
q 0 /
0
//
//
o/
/
o o o o
2.8 x 105
0 00
t I l I I I
0
q.8 x 10q
o o
0 10 20 30 qO 50 60 70
ANGLE, DEG
o o o
80 90
Figure B-5: Comparison of calculated and experimental corrective
heat transfer characteristics, LEWICE k, = O.000gm.
183
8
1500
i350
1200
1050
I00
75O
600
45O
300
150
g
0 EXPERIMENT (REF. B-9)
-- r3LCULATED
I
0 •
/I l ,, I I I I_.
SURFACE DISTANCE. M
1D. IO
a. Two minute glaze ice shape.
Figure B-6: Comparison of calcuiated and experimental heat--
transfer coefficients on simulated glaze and rime ice shapes.
184
i500 --
1360
_, 1200
a_
= 1050
w
900 -
750 --
bOO --
450 _
3OO
150
-°2:1o -1,60 -1.26 -0o6_
EXPERIMENT(REF. B-9)CALCULATED
I I I I-O.q2 0,00 O,q'2 O,Oq- 1,2& 1.68 2.10
s/c
b. Five min glaze ice shape.
Figure B-6: continued
185
1600
1350
O0 °
I I I-O.&_ 0.00 0.6_
s/c
0 EXPERIRENT(REF B-91
CALCULATED
0
D
0 0
I JL.2B 1.92 2,5& 3.20
c. Fifteen rain glaze ice shape.
Figure B-6: continued
186
z
u
wm_
M
EXPERIME.NT (REF. B-9')
CALCULATED
I I I
0
-0.80 -0._ 0,00
0
0
0
IO,q'_ 0,88 1,32 1.76 2.20
sic
d. Fifteen min rime ice shape.
Figure B-6: Concluded
187
APPENDIX C
FLOW FIELD CORRECTIONS
As discussed in the text, there are two types of flow field corrections
that are applied in LEWICE to allow more accurate particle trajectory
calculations. The first correction is made to avoid errors that occur in the
flow field close to the surface because the geometry is represented by discrete
points connected by line segments instead of a smooth curve. These are
called discretization errors. The second correction is made to avoid errors
caused by convoluted ice shapes. Both of these corrections are performed by
producing an imaginary or pseudo-surface which is used in the calculations
instead of the actual ice surface. The corrections are described in the
following sections.
C.1 Correction for Discretization Errors Near the Body
The potential flow computer program used in this study has a relatively
large discretization error very close to the body. As shown in Figure Col,
taken from Reference C-1, the longitudinal and vertical velocities around
the leading edge of the Joukowski airfoil are very irregular close to the airfoil
but become smoother as A_ is increased. (In Figure C-l, A_ is equivalent to
the DSHIFT parameter in LEWICE). The velocity is computed for different
constant values of separation distance from the body, as illustrated in the
insert. Note the large peaks or oscillations in the flow field velocity near
the surface.
Figure C-2 illustrates the trajectories of three different particles released
at very small separation distances, Y0, upstream of the body. Note that
the upper particle turns near the nose and flows backward, reverses direc-
tion again, and flows around the body. The initial intermediate positioned
particle trajectory crosses the lower particle trajectory near the body. It
approaches very close to the surface somewhat downstream of the nose,
and then departs off into the free-stream without impinging on the body.
Finally, the lower particle trajectory impinges on the body. These erratic
trajectories are caused by the strong perturbations in the flow field near
the body.
To overcome the effect of the discretization error near the body, an
artificial impingement surface is generated by the computer program. This
188
surface is achieved by displacing the surface of the body a small increment
DSHIFT in the upstream x direction. To generate the pseudo-impingement
surface, the x-coordinates are increased by the quantity DSHIFT times
the cosine of the segment angle while the y-coordinates remain constant.
The resulting pseudo-impingement surface is displaced outward into the
freestream as shown in Figure C-3. The value of DSHIFT is input by the
user in namelist TRAJ1. Commonly used values between .2 to .6 percent
of the chord length encompass the major area of uncertainty in the flow
field.
The pseudo-impingement surface is used only for particle impingement
calculations and does not influence the potential flow calculations. The
pseudo-impingement surface is discarded once the particle trajectory calcu-
lations are completed and is not present when a new ice surface is formed.
C.2 Correction for Multiple Calculated Stagnation Points
Glaze ice accretions are often characterized by the formation of two
horns, as shown in Figure C-4a. The calculation of the flow field around
these typical glaze ice shapes produces undesirable results such as multiple
calculated stagnation points (surface velocity = 0.0). An example of such a
calculation is shown in Figure C-4b. When more than one stagnation point
is calculated, errors occur in the particle trajectory and thermodynamic
portions of the code, causing an abnormal termination. Since the Douglas
potential flow solution is the most feasible method for use in this code, a
method to obtain a sufficiently accurate flow field solution is required when
this situation occurs.
Before the development of computer codes capable of applying the
Navier-Stokes equations to the calculation of flow characteristics in recir-
culation zones, the potential flow codes available had a problem similar to
that in this application. One solution was to replace the boundary of the
separation/reattachment zone with a pseudo-surface, as shown in Figure
C-5. A similar approach is used in this application to smooth the groove
found at the stagnation point of many ice accretions.
Determination of the Locations of Stagnation Points
The location of the stagnation point(s) is determined in subroutine
STAG by checking the non-dimensional edge velocities calculated by $24Y
189
(VT) for a change in sign. These velocities will be negative on the lower
surface and positive on the upper surface. The velocity on each segment is
checked, and the number of each segment at which the sign of VT changes
is stored as a stagnation point. If more thaa one sign reversal is found,
it is assumed that the flow field is inaccurate, and the user will be given
the option of selecting one of the calculated stagnation points to use in
the remaining calculations, or to form a pseudo-eurface over the calculated
stagnation points.
The algorithm to form the pseudo-surface is located in subroutine
PSURF. The computer prompts and responses used to form the surface
can be found in Example 2 of Chapter 7. The purpose of the remainder of
this appendix is to demonstrate the accuracy of this method by comparing
experimental data to surface velocity profiles calculated using a pseudo-
surface. The geometries used for these comparisons are simulated 2- and
5-min glaze ice accretions and a 15-min rime ice accretion. These ice shapes
are made of wood and simulate actual ice accretions formed on a cylinder.
The surface velocity measurements were obtained from surface pressure
data for each of the geometries.
Recall that Figure C-4a shows a 5-rain glaze ice accretion for which two
stagnation points were calculated. The corresponding calculated surface
velocity profile is shown in Figure C-4b. A pseudo-surface, shown in Fig-
ure C-6a, was placed over the glaze accretion, and the resulting calculated
surface velocity compared to experimental data. Note that the calculated
velocity profile now has only one stagnation point, and that the calculated
and experimental velocities compare very well near the stagnation point.
Additional applications of the pseudo-surface technique are shown in Fig-
ures C-6b and c. In all cases, the presence of the pseudo-surface produced
smoother velocity profiles which more closely matched experimental results.
This method, while capable of improving the accuracy of the flow field
solution, is an approximation to the true solution and must be treated as
such. For example, Figures C-Ta and b show a 15-min glaze ice accretion
and the corresponding calculated surface velocity. In this case, ten stag-
nation points were calculated. A pseudo-surface, shown in Figure C-Sa,
was placed over the glaze ice accretion, and the calculations were repeated.
As shown in Figure C-8b, the calculated velocity profile is much smoother
than that for the actual ice shape, and the velocity in the groove is slightly
190
over-predicted. While this solution would allow the calculation of the iceaccretion to continue, it illustrates that the pseudo-surface technique can
produce a very rough approximation to the actual flow field.
191
Appendix C
List of References
1. Frost, W., Chong, H., Shieh, C., and Kimble, K. "Two-Dimensional
Particle Trajectory Computer Program." Interim Report for Contract
NAS3-2244B, 1982.
192
ORIGINAL PAGE IS
OF POOR QUALITY
8
>-
8
>:
1.20
.83
.45
,O8
I I I I I
A_" = CONSTANTSEPARATION
DISTMCE FROMTHE BODY/'-/
//
/
-.3o I I I I I-.08 -.05 -.03 0 .03 .05 .08
SURFACE DISTANCE, s/_ c
C-1: Discretizationerror in the flow fieldnear the nose of the Joukowski airfoil•
193
.53
.so,
w-
_ .i17
/
/
• 115 I-.21 -. 16
/-PARTICLE TRAJECTORIES/ / / _-osos5
/ _ "5050
PSEUDO-IRPINGERENTSURFACE_./ _. _..,,_
I I I I _-. 10 -.05 .01 .07 .12
SURFACEDISTANCE, s/J_c x 10-1
C-2: Discretization error in the flow field near the nose of the upper body
of a two-dimensional inlet.
PSEUDO-IRP l NGERENTSURFACE"j
C-3: Illustration of the pseudo-impingement surface.
194
_-- GROOVE AT THESTAGNATION POINT
\\
\\
\
(a) FIVE RINUTE GLAZE ICE ACCRETION WITH GLAZE HORNS.
250
22S
200
175
tSO
125
lO0
F5
50
0-.15
I-.IZ
I I-.09
i II
-.06 -.03 0.00 0.03
-- CALCULATED STAGNATION
POINTS
SURFACE D[STANCEo M
IO,LZ
i0,15
(b) MULTIPLE CALCULATED STAGNATION POINTS FOR A 5 RINUTE GLAZE ICE SHAPE
C-4: Simulated fiverain glaze ice accretion on a cylinder and the corresponding
calculated surface velocity profile.
195
FLOW RE-ATTACHRENT
_\_\.__.__ SEPARATED FLOW ZONE
\_'.._GLAZE ICE ACCRETION
PSEUDO-SURFACE_
\
C-5: Example of the application of the pseudo-surface technique on a recirculation zone.
196
PSEUIX)-SURFACE ---_
\
't\'(
250 --
225 --
200 --
[75 --
t50 --
t2S --
tOO --
75 --
50 --
25 --
o I-.15 -.12
Oo
I-.07 -.06 -.03 0.00 0.03
SURFACE DISTANCE, M
o EXPERIRENT
CALCULATED
I IO.t2 0.15
a. Simulated five min glaze ice shape
C-6: Comparison of experimental surface velocities on simulated ice shapes
to those callculated for the ice shape with pseudo-surface.
197
PSEUDO-SURFACE
\
\\\
2°°I180
t60
1 ',t-O
|20 --
I00 --
_ 80-
6O
'tO
2O
0-o10 -.08 -.Oh -.0_
0
0 0
o 0
-.02 O.OO 0.02
SURFACE DISTANCE, e_
0 EXPER[I'ENT
CALCULATED
0 • O"l- O.O& 0.0e
I0,I0
b. Simulated two min glaze ice shape
C-6: continued
198
PSEUDO-SURFACE -- D
m
>_
150 --
135 --
120 --
LOS --
90 --
?S --
60 --
q'5 --
30 --
15 --
0-o|5
I-.IZ
o EXPERINENT
CALCULATED
I I I ] I I-o07 -,06 -,03 0,00 0,03 0,06 0.09
SURFACE DISTANCE. H
I IO,L2 0,15
c. Simulated fifteen min rime ice shape
C-6: Concluded
199
ORIGINAL PAGE IS
OF POOR QUALITY
f IO.Ol
a. Locations of the multiple calculated stagnation points
C-7: Simulated fifteen min glaze ice accretion on a cylinder.
200
ORIGINAL PAGE |S
OF. POOR QUALITY
3OO
270
2_FO
2)0
180
150
120
90 --
60 --
30 --
D-.2(I
I-.16 -.12 - . ()El -oOq- 0.0() I],0_ 0.08 0.)2 0.16
SURFACE DISTANCE, M
IO._'N
b. Calculated surface velocity over the ice shapeC-7: Concluded.
201
ORIGINAL PAGE L_
OF. POOR QUALI'[_r
O.O&O fOoO'HI
PSEUDO-SURFACE
I f I ....
-.O6O -.Oq I -,Q3& -_ -.012 o. --
/ / '°
-.01-11 --
-.O&O
I fO.Od
C-8a: Application of the pseudo-surface technique on a simulated
fifteen min glaze ice accretion.
202
ORI(_INAE PAGE IS
OF POOR QUALITY
>-
,....,>
350 --
315 -
2_-5 --
_?) (| --
I/5 --
ILtO --
I O5 --
?0-
35 ,--
0-.ZO
O EXPER IREttT
CALCULATED
OOO O00 O )0 000 000
J-.16 -.12 -,OH -.O_t - 0.00 O.Oq" O,(18 0.12 0.16
IO,2Q
SURFACE DISTANCE° M
C-8b: Calculated surface velocity over ice shape with pseudo-surface.
203
APPENDIX D
COMPLETE INPUT TO THE POTENTIAL FLOW CODE
($24Y)
As noted in Section 5.1, the input to the potential flow code was simpli-
fied for use in LEWICE. Many of the generalities in S24Y are not applicable
to LEWICE, and, therefore, are set to default values in the program (SUB-
ROUTINE SETUP). SUBROUTINE SETUP reads the simplified input
from unit 35, and, after assigning the default values, writes to unit 45 in
the proper $24Y input format. Since the original input to the code is still
used, it is necessary to define all of variables used in this input file. The
following is the description of the S24Y input file written to unit 45.
D.I Potential Flow Code Input Cards
Card 01 Program Control Card
(3(I1,2X), lX, 7A4, 5X, 9(n, 2X), 1X, 11)
Column Code
01 ID
04 ISV
07 ILIFT
11-38 TTITLE
Format Description
Body Number
Flag to control the saving of the
geometry for future use by the 2-D
program- 0 Do not save data
- 1 Save the input geometry data for
future use
Lift Control Flag
= 0 This is not a lifting body
= 1 This is a lifting body
Body Description
204
44
47
5O
53
56
IPARA
IFIRST
ISECND
ITR
INORM
Element Geometry Flag
= 0 Linear Elements
= 1 Parabolic Elements
First-order Terms Flag
-- 0 No first-orderterms
- 1 First derivative term
- 2 Curvature term
- 3 Both first-orderterms
Second-order terms flag
-- 0 No second-order terms
- 1 Second derivative term
- 2 Curvature squared term
- 3 Both second-order terms
Geometry transformation card
= 0 Transformation card will not
be input
- 1 Geometry transformation card
will be input
Ellipse generation. Ellipse
generation card will be input.
Transformation card will not
be input.
Ellipse generation. Ellipse
generation card will be input.
Transformation card willbe input.
=2
=3
Geometry Normalization Card
= 0 Geometry will not be normalized
- 1 All of the geometry data
(x and y) will be divided by
the chord length before use by
the potential flow program
205
59 IBOD Body Disposition Flag
This flag together with the IDOLD
parameter controls the sequence of
the potential flow analysis part of
the program. With the use of these
two flags and the ISV parameter, it
is possible to perform a variety of
multi-element problems with a
minimum of input data. For normal
useage when all of the geometry data
are input, only the IBOD -- 1 and = 2
are used.
= 1 New geometry is being used.
The storage of geometry data
for the potential flow solution
will start with this body.
= 2 New geometry is being input, but
this is not the first body.
This body will be added to the
sequence of body data already input.
= 3 New geometry is being input, but
it is to be added to an old
sequence of data.
All previously saved geometry will
be used
The geometry for this body will
be selected from the previously
saved data (body IDOLD will be
selected). This selected body
will be added to the current string
of bodies.
Previously saved geometry data
will be used with the body
number indicated by the IDOLD
parameter removed from the solution
=4
-5
---6
206
62 IDOLD
65 IPVOR
Old Body ID Number
This parameter is used in
conjunction with the IBOD parameter
in selecting which previously saved
shape is to be retrieved as the
present body
Vorticity Distribution Flag
= 0 Use constant vortlcity between
the body elements
- 1 Use a variable vorticity distribution
68 LAST Last Body Flag
= 0 This is not the last body.
After this body is input, the
program will return to read another
Body Title and Control Card for the
next body.
= 1 This is the last body.
72 ITYPE Card Type Flag
=I
X-Coordinate Cards (6F12.7, 2X, I1, lX, I1, lX, I1)
Column Code Format Description
1-12 X(1)13-24 X(2)25-36 X(3)37-48 X(4)49-60 X(5)61-72 X(6)
6F12.7 x-coordinates of the body geometry.
Up to six points may be on each card
depending upon how the INO flag is set.
75 INO I1 Number of data points on the card
207
77 ISTAT I1
(Maximum of six)
Last Card Flag
= 0 This is not the last
x-coordinate card. More cards will follow.
= 1 This is the last x-coordinate card.
79 ITYPE I1 Card Type Flag
--3
Y-Coordinate Cards (6F12.7, 2X, I1, lX, I1, lX, I1)
Column Code Format Description
1-12 y(1)13-24 v(2)25-36 Y(3)
37-48 Y(4)
49-60 Y(5)
61-72 v(6)
6F12.7 y-coordinates of the body geometry.
Up to six points may be input on
each card depending upon how the
INO flag is set.
75 INO I1 Number of data points on the card
(Maximum of six)
77 ISTAT Ii Last Card Flag
-- 0 This isnot the last
y-coordinate card. More cards
willfollow.
-1 This isthe lasty-coordinate
card
79 ITYPE I1 Card Type Flag
=4
208
Flow Title Card (15A4, llX, I1)
Column Code Format Description
1-60 FTITLE 15A4 Title
72 ITYPE I1 Card Type Flag
=8
Flow Control Card
(I1,4X,F 10.5,2X,I1,2X,F 10.5,5(4X.I1),9X,I1,3X,II,I2,I1)
Column Code Format
1 INCLT I1
6-15 CLT F10.5
18 ICHORD I1
21-30 CCL F10.5
Description
c_, a Flag
= 0 Airfoil angle of attack, a, is
input.
=1 Total lift coefficient, C,, is
Value of the angle of attack or lift
coefficient depending on how the
INCLT flag was set
Reference Length Flag
= 0 The reference length used to
calculate C, is set = 1.0
= 1 The reference length used to
calculate C, will be input as CCL
The input value for the reference
length used in calculating Ce
(generally the airfoil chord)
35 IND I1 Individual Solution Flag
$24Y is capable of calculating the
potential flow about up to 6 bodies
209
and then superimpose the results of
each. The possible values of IND are
as follows:
= 0 Edge velocities are not calculated
for each body
= 1 Edge velocities are calculated for
each body
In LEWICE, only one body is input and the
edge velocities are always required.
Therefore, IND = 1.
4O ISOL II Matrix Solution Method Control Flag
= 0 Use routine SOLVIT for the
matrix solution (used when a very
large number of points have been input)
= 1 Use routine QUASI for the matrix
solution
= 2 Use routine MIS1 for the matrix
solution. The maximum number
of geometry points = 101. If
the number of points is greater
than 101, the program will
automatically shift to use SOLVIT.
45 IOFF I1 Off-body Calculation Flag
= 0 Off-body points will not be
calculated
= 1 Off-body points will be calculated
50 NONU Ii Non-uniform Flow Flag
= 0 Non-uniform flow is not input
= 0 Non-uniform flow will be input.
The number of flows input = NONU
(maximum of six). When this option
is used, the program sets ISOL = 1.
210
55 NBNU II
65 IPRINT I1
The number of bodies for which
the non-uniform flows are input
Print/punch Flag
= 0 Normal output
= 2 Print the individual matrices
= 7 Punch the output on cards
70 MORE I1 Last Case Flag
= 0 This is the last case
= 1 This is not the last case
Another set of Flow Title and
Flow Control cards (and any
non-uniform or off-body cards)
will be expected after this case
is completed
70-71 IFILL 12 Parabolic Integration Flag
$24Y calculates the forces and
moments acting on the body using
both a trapezoidal and parabolic
integration of the calculated
coefficient. The results of
the trapezoidal calculations
are always output. The valueof IFILL determines whether the
parabolic results are printed.
72 ITYPE I1 Card Type Flag
--9
Off-Body Title and Control Card
(11, 9X, 7A4, 12X, 2(2X, I1), 2(5X, I1), 2X, I2)
211
Column
1
11-38
53
56
62
68
Code
ID
TITLE
ITR
INORM
IDOLD
LAST
Format
I1
7A4
Ii
II
II
II
Description
Identification number for this
group of off-body points. Off-body
points are read in groups of up to
100. There is no limit on the number
of groups.
Title or description for this
group of off-body points
Coordinate Transformation Flag
See the ITR parameter on the Body Titleand Control Card
Coordinate Normalization Flag
= 0 Off-body coordinates will not
be normalized
= 1 Normalize the coordinates by
the input chord or by the chord
for the body with ID = IDOLD
Body Selection Flag for Normalizing
Off-body Points
- 0 Use the input chord to normalize
the off-body points
= 0 Use the chord for body withID = IDOLD to normalize the
off-body points
Off-body Group Termination Flag
= 0 Another group of off-body
points will follow this group
= 1 This is the last group of off-
body points
212
71-72 ITYPE I2 Card Type Flag
= 21
Off-Body X-Coordinate Cards (6F12.7, 2X, I1, IX, II, IX, I1)
Column Code Format Description
,-,2 X(l)13-24 x(2)2s-36 x(3)37-48 x(4)61-72 x(6)
6F12.7 x-coordinates of the off-body
points. Up to six points may be
input on each card depending upon
how the INO flag is set.
75 INO 11 Number of data points on the card
77 ISTAT I1 Last Card Flag
= 0 This is not the last
x-coordinate card. More cards
will follow.
= 1 This is the last x-coordinate
card
79 ITYPE I1 Card Type Flag
--3
Off Body Y-Coordinate Cards (6F12.7, 2X, I1, lX, I1, 1X, I1)
Column Code Format Description
1-12 Y(1)
13-24 Y(2)
25-36 Y(3)
37-48 Y(4)
49-60 Y(5)
61-72 Y(6)
6F12.7 y-coordinates of the off-body
points. Up to six points may be
input on each card depending upon
how the INO flag is set.
75 INO I1 Number of data points on the card
213
77 ISTAT I1
(Maximum of six)
Last Card Flag
= 0 This is not the last y-coordinate
card. More cards will follow.
= 1 This is the last y-coordinate
card
79 ITYPE II Card Type Flag
=4
D.2 Sample Input
The input to the $24Y code using the formats described in the previous
section is written to unit 45 in subroutine SETUP. An example of the
$24Y input file on unit 45 is shown in Figure D-1. For normal operation of
LEWICE, this file should not have to be examined or modified.
214
ORIGINAL PAGE iS
OF POOR QUALITY
! 0 1 NACA1.00000000.90000000.75000000.60000000.45000000.30000000.15000000.06000000.02500000.00575000.00125000.00037500.00057500.00125000.00375000.02500000.06000000.15000000.30000000.45000000.60000000.75000000.90000001.0000000
00120.98999990.07500000.72500000.57500000.42500000,27500000.12500000.05000000.02000000.00250000.00100000.00025000.00050000.00150000.00500000.05000000.07000000.17500000.52500000.47500000.62500000.77500000.92500000.0000000
-0.0310550-0.0459040-0.0560510-0.0602260-0.0556560-0.0385350-0.0262500-0.0106990-0.0058470-0.0029450
0,00294500.00584700.01069900.02623000.03053500.05365600.06022600.0560510"0.04590400.05105500.01490000.0000000
NACA 0012
0.98000000.05000000.70000000.55000000.40000000.25000000.1000000O.OqSO0000.01500000.00225000.00007500.00012500.00062500.00175000.00750000.03500000.08000000.20000000.35000000.50000000.65000000.00000000.95000000.0000000
1 3 3 0 0 10.9700000 0.95000000.0250000 0.00000000.6750000 0.65000000.5250000 0.50000000.3750000 0.55000000.2250000 0.20000000.0900000 0.00000000.0400000 0.05500000.0100000 0.00750000.0020000 0.00175000.0007500 0.00062500.0000000 0.00012500.0007500 0.00087500.0020000 0.00225000.0100000 0.01500000.0400000 0.04500000.0900000 0.10000000.2250000 0.25000000.5750000 0.40000000.5250000 0.55000000.6750000 0.70000000.8250000 0.05000000.9700000 0.98000000.0000000 0.0000000
0,0000000 -0,0018740 -0.0036110 -0.0052590 -0.0082510-0.0149000 -0.0179550 -0.0200880 -0.0257590 -0.0265150
-0.0544110 -0.0560870 -0.0592810 -0.0415850-0.0479060 -0.0497950 -0.0515600 -0.0531980-0.0572430 -0.0582620 -0.0590900 -0.0597070-0,0600760 -0.0596120 -0.0587940 -0.0575700-0.0507520 -0.0470040 -0.0452200 -0.0432520-0.0356740 -0.0340020 -0.0325620 -0.0304960-0.0237260 -0.0207970 -0.0172400 -0.0150780-0.0086200 -0.0081360 -0.0076230 -0.0070750-0.0051460 -0.0047660 -0.0043630 -0.0039310-0.0023560 -0.0016320 0.0000000 0.0016320
0.0054620 0.0039310 0.0043650 0.00476600.0064050 0.0070750 0.0076250 0.00015600.0123060 0.0150780 0.0172480 0.02079700.0284620 0.0304960 0.0323620 0.03408200.0410300 0.0432520 0.0452280 0.04700400.0558790 0.0575700 0.0587940 0.05961200,0600940 0.0597070 0.0590900 0.05826200.0546980 0.0551980 0.0515600 0.04979500.0437950 0.0415850 0.0392810 0.03688700.0292210 0.0265150 0.0237590 0.02088800.0117000 0.0082510 0.0052590 0.00361100.0000000 0.0000000 0.0000000 0.0000000
4.00000 0 0.00000 1 0 1 0 0NACA 0012 0 0
-0.0200000 -0.0200000 0.0000000 0.0000000 0.00000001.0000000 0.5000000 0.0000000 0.0000000 0.0000000
0 1 1 10.92500000.77500000.62500000.4750000O. 32500000. 17500000.07000000.0500000O. 00500000.00150000.00050000.00025000.00100000.00250000.02000000.05000000.12500000.27500000.42500000.57500000.72500000.87500000.90999990.0000000
-0.0117000-0.0292210-0.0437950-0.0546980-0.0600940-0.0550790-0.0410380-0.0284620-0.012,3060-0.0064050-0.0054620
0. 0023560O. 00514600,00862000. 025726O0.03567400.05075200.06007600.05724300.04790600.03441100.01795300.00187400.0000000
80 0 19
1 10.00000000.0000000
6 0 36 0 36 0 3
6056 0 36 0 36036056 0 56056036 0 56036 0 36 0 36 0 36 0 36036 0 56 0 36 0 36 0 36 O 31 13
604604604604604604604604604604604604604604604604604604604604604604604114
21 3214
D-l: Input to $24y written to unit 45.
215
APPENDIX E
CALCULATION OF THE LOCAL EDGE VELOCITIES
Another pseudo-surface, related to the one created for particle impinge-
ment calculations, is created to determine non=dimensional edge velocities.
This pseudo-surface is formed by moving each point on the body a dis-
tance DSHIFT along the outward normal to the surface. The resulting
pseudo-surface is shown in Figure E-1. The non=dhnensional edge velocities
that were originally computed in subroutine FLOWS on the "true" surface
are recalculated in subroutine READIN on the pseudo-surface. (This re-
calculation step can be omitted with only a small change to subroutine
READIN.) The purpose of creating a pseudo-surface is to shift the surface
outward into a region where the velocity profile is smoother, thus avoiding
numerical problems that may occur when velocities must be computed on
an irregular ice surface. This method will produce higher stagnation ve-
locities but will affect the ice shape only in a relatively small region of the
airfoil unless a value of DSHIFT larger than recommended in this manual
is used.
The non-dimensional edge velocities that are recalculated on the pseudo-
surface are the ones used in the evaluation of the thermodynamic charac-
teristics of the ice surface. These non-dhmensional velocities, V_, are given
by the equation
v;= v" (E-X)Voo
The values of V_ are initially written to unit 30 in subroutine READIN
and then read in subroutine VEDGE, where they are used to calculate the
dimensional local edge velocities. The boundary layer edge velocities, IF,,
temperature, T,, and pressure, P,, are calculated from V_ using the isen-
tropic equations with the Karman-Tsien compressibility correction. These
parametes are assigned the following variable names in the computer code:
Local static pressure, (P,)
Local static temperature, (7",)
PE(I)
TE(I)
216
Local dimensional velocity, (V,)
Local non-dimensional velocity, (V_)
VE(I) (compressible)
VT(I) (incompressible)
Each of the parameters are arrays with (I) denoting the segment number.
This appendix describes the equations used to calculate these flow proper-
ties.
The free stream roach number, total temperature, and total pressure
are first calculated using the following isentropic equations:
Voo (E-2)Moo - 20.05V_
M_TT --"T,(I +-"_-)
2
PT = Po(1+ M£p.55 "
(E-3)
(E-4)
An incompressible pressure coefficient is calculated from the non-
dimensional edge velocities using the following equation:
%,., = 1 - (V:) 2
This incompressible pressure distribution around the body is then corrected
for compressibility using the Karman-Tsien compressibility correction given
by the following equation:
]_,.= (_- M_)'/"+ _.+ (i :-Moo)'/' (E-6)
The local pressure is calculated using this corrected pressure coefficient and
the following equation:
217
? ') (E 7)t",=t', 1 + _ e,. M_.
where Po is the free stream static pressure. If a local static pressure is
calculated to be greater than the total pressure, the local static pressure is
set equal to the total pressure.
The local mach number is calculated using the following isentropic re-
lationship between the local static and total pressures:
. 00]'"The local static temperature is determined using the following isentropic
relation:
(Te=TT 1+ (E-9)
The dimensional local edge velocity is then calculated using the isentropic
equation for the speed of sound in air and the local Mach number, e.g.,
v.=u.(2o.osv .) (E- 10)
The values of VE, TE, and PE for each body segment are then written to
unit 30.
218
10
r6EOllrTRY FOItJIE])BY LINESI JOININ6 BODYCOORDINATES
II
'_OUI"WARD NORMALTO POINT S
15
2
>
E-l: Illustration of the pseudo-surface.
219
APPENDIX F
EMPIRICAL RELATIONSHIP FOR
SAND GRAIN ROUGHNESS HEIGHT
THE EQUIVALENT
As discussed in Section 5.2, the size, shape, and type of ice accretion
that is formed is dependent upon the convective heat transfer rate from the
ice surface. The integral boundary layer method, described in Appendix B,
requires that a surface roughness height be specified to identify transition
to turbulent flow and evaluate the convective heat transfer characteristics
of the rough surface.
Increasing the size of the roughness elements will increase the calculated
convective heat transfer coefficient. Therefore, a calculated ice shape can
change quite drastically when various values of roughness element height are
specified. Figure F-1 shows the effect of varying the input value of the sand
grain roughness height, ko, on the calculated ice accretion shape. When
the value of k° is smaller, the amount of heat removed from the surface by
convection is reduced. Therefore, the surface temperature is not lowered
sufficiently to allow all of the ice to freeze on impact and a glaze accretion is
formed. Incrementally increasing k, increases the convective heat transfer,
thereby increasing the fraction of impinging water that freezes on contact.
As a result, the accretions begin to take on more characteristics of rime
ice. At some value of ko, sufficient heat will be removed to freeze all of the
water on impact, and a complete rime ice accretion is formed.
Empirical correlations that can be used to evaluate the effect of rough-
ness exist in the literature (Reference F-1 and F-2). Unfortunately, these
correlations are usually applicable only for a specific, well-defined type of
roughness element. None of these correlations are directly applicable to the
irregular surface roughness elements found on typical ice accretions. Fur-
thermore, the size and shape of the roughness elements on an ice surface are
dependent on the conditions at which the ice was formed. They can vary
with the icing condition, surface location, and, since the ice shape changes
with time, the icing time. While the effect of each of these parameters on
the formation of the surface roughness elements is very complex, all analyt-
ical ice accretion prediction methods must address the problem because of
the strong influence on the calculated ice accretion shape shown in FigureF-1.
220
It has become standard practice in current ice accretion prediction
methods to develop an empirical correlation for either the surface element
roughness height (Reference F-3) or the convective heat transfer coefficient
(Reference F-4). These correlations are developed by first predicting the ice
shapes for a set of experimental ice shapes by changing the convective heat
transfer coefficient (or roughness element height) to determine the value
that yields the best agreement with experiment. Unfortunately, the corre-
lation will depend on the computational algorithm and may not be directly
applicable to any other analytical ice accretion prediction method. Since
the timestepping procedure applied in LEWICE is unique among analyti-
cal ice accretion prediction methods, an empirical correlation relating the
surface roughness height to the icing condition had to be developed.
The experimental data used to develop this correlation was obtained
by Gent (Reference F-5). This data set, shown in Figures F-2, -3, and -4,
show the effect of velocity, LWC, and static temperature on the shape of
the ice accretion formed. Also shown in the figures are the ice accretion
shapes, calculated by LEWICE, that best compare with the experimental
shape and the corresponding value of k,. The accretion shown in Figure F-
3a for LWC =0.Sg/m s was used as a baseline condition for the correlation.
Therefore, all values of k° were divided by the value of k, for this case and
plotted as a function of either velocity, LWC, or static temperature. The
resulting data points, normalized by the airfoil chord of 0.3m are shown in
Figures F-5,-6, and -7, respectively.
A correlation relating the sand grain roughness height to the icing pa-
rameter was formed by fitting the data on each of these plots with a least
squares linear or quadratic curve fit. The curve calculated from each cor-
relation is also shown in Figures F-5, -6, and -7. The equations are as
follows:
Velocity
k,/c = 0.4286 + 0.0044139(V0o) (F - 1)
Liquid Water Content
k°/c-0.5714 + 0.2457(LWC) + 1.2571(LWC) 2 (F- 2)
221
Static Temperature
k°/c IT.\
\1000 /(F-3)
In all of these equations, k°/c)6o°°, the baseline value, is 0.00117. The ve-
locity, LWC, and static temperature are input into the equations in m/sec,
g/m s, and K, respectively. By relating them to a baseline value, the corre-
lations calculate a multiplying factor accounting for the effect of velocity,
LWC, and static temperature. The value of sand-grain roughness height to
be input is calculated using the following equation:
r ./o r ./o r 1k° = Lk0/c)bo°,vooLk°lc)b,°,LwcLk,/d_°,,JT. k,ld_,,,
(F-4)
The use of these equations is best illustrated by a numerical example.
Suppose that the ice shape for the following icing condition is to be deter-
mined.
Airfoil Chord = 0.3m
Velocity = 75.0 m/s
Static Temperature = 255.0 Ks
LWC = 0.5 g/m
The multiplying factors calculated from Equations (F-l), (F-2), and (F-
3) are 0.7596, 1.0085, and 0.7401, respectively. Substituting these values
into Equation (F-4), the final factor to be multiplied by the baseline value
and the airfoil chord is 0.5670. Therefore, for a baseline value of 0.00117
and chord of 0.3 m, the sand-grain roughness to be input into the code is
0.000199 m.
222
As previously noted, these three correlations were developed to account
for the effect of velocity, LWC, and static temperature on the surface rough-
ness elements formed on an ice accretion. These three icing parameters were
selected because of their obvious influence on the type of ice formed, and
because a complete and consistent set of experimental data existed from
which to form a correlation. The effects of droplet diameter, body geometry,
static pressure, etc. have not been included. Also inherent in the baseline
value of sand-grain roughness height are any characteristics unique to the
facility in which the experimental ice accretion shapes were formed. These
can include levels of free-stream turbulence, LWC and droplet diameter cal-
ibrations, and possibly even the droplet size distribution produced by the
spray nozzle. Comparisons with experimental ice accretion shapes have in-
dicated that the baseline value of k,/c)b,, = 0.00117 yields good results for
the facility of Reference F-1 and the NASA Lewis Icing Research Tunnel
(IRT) but would not be expected to be appropriate for all icing facilities
and applications. A value for flight test data has not been determined but
is expected to be less than 0.00117, primarily because of the lower level of
free-stream turbulence encountered in flight.
The surface roughness, while known to be a function of icing time and
surface location, is currently specified to be constant for the entire icing
time. Sufficient experimental data does not exist to produce meaningful
correlations relating these parameters to the roughness element height.
223
APPENDIX F
List of References
I. Kays, W.M. and Crawford, M.E. Convective Heat and Mass Trans-
fe__£r.2nd Edition, MacGraw-Hill Book Company, New York, 1980.
2. White, F.M. Viscous Fluid Flow. MacGraw-Hill Book Company,
New York, 1974.
3. Kirchner, R.D. "Aircraft Icing Roughness Features and Its Effect on
the Icing Process." AIAA-83-0111, January 1983.
4. Cansdale, J.T. and Gent, R.W. "Ice Accretion on Aerofoils in Two-
Dimensional Compressible Flow - A Theoretical Model." Royal Air-
craft Establishment Technical Report 82128, January 1983.
5. Gent, R.W., Markiewicz, R.H., and Cansdale, J.T. _Further Studies
of Helicopter Rotor Ice Accretion and Protection." Paper No. 54,
Eleventh European Rotorcraft Forum, September 1985.
224
RIME FEATHERS
EXPERIMENT (IRT) Ks = 0.001 M
Ks = 00005 M
C--__Ks = o00q M
Ks = 0.002 M
VELOCITY (M/S) 93,88
TEMPERATURE (C) -1#.37
PRESSURE (KPA} 93.61
HUMIDITY (X) IOO.OO
LMC (G/M--3) 0.96
DROP DIAM (MICRONS) 37.50
TIME (SEC) 225.00
F-l: Effect of varying the equivalent sand-grain roughness
on the ice accretion calculated for a mixed icing condition
on a NACA 0012 airfoil section at 0.0 deg angle of attack.
225
_,, O._
_., O._
\
\
\
\
\
\
,(
,..- .ju_¢._e,_o_t,_'?e'
-2" ._ec_, o_ "ve_'°c'_"/o__.ce
,_6
EXPERIMENTAL
LWC - 0.25 gll,_
TI-IEORET! CAL
LWC= O,.50g/_ 3
LWC= 0.75 g/_
LWC= 1.00g/M 3
VEI. I)GI lY (It/S) 129.UII
l E I'IPFR,_|UR[ (C) -IZ.60
PRKSSURE (KI)A) 90.76
IItJM I OI lrY (X) IUU,O0
OROP OIAM (MICRONS) 20°00
TIHE (SEC) 120.00
a. Angle of attack = 0.0°
F-3: Effectof LWC on ice accretion shape.
227
EXPER| RENTAL
LgC = 0.25 g/M 3
THEORETICAL
LWC ffi 0.50 g/M 3
LgC = 1.00 g/t43
UELOCIIY (14/S) 129.00
1EHI'ERfiTURE (C) -12,bO
PRF, SSUgE (KI)h) ?fJ, 16
IIUtlIDI IY (x) 10o.00
IJROP UIAfl (HICRDNS) 20°00
TitlE (SEC) 120.00
b. Angle of attack = 4.0°
F-3: Concluded.
228
EXPERIRENTAL
r,. -8.oc ......
Ts = -/2.6 C
Ts = -22.9 C
V[LOCITy (N/S) 131,00
PR/SSUR[ (KP_) 90,75HUNIDJIy ¢X)
LHC (O/H--3) IO0,gO0.50
DROP DIAN'¢M|CRONS) 24,00f|H[ ISLE) •
IEo,o0
F-4: Effect of static temperature on ice accretion shape.
229
1.5
1.0
.5
I I I I50 100 150 200
VELOCITY, _v's
F-5: Emperical relationship for equivalent sand-grain roughness
as a function of velocity.
2.5
2.0
_1.5
t_
.5
-- 0 0_0 (FIG. F-3A) 0
I I I I I.2 .q .6 .8 1.0
LIQUID WATER CONTENT, glM3
F-6: Emperical relationship for equivalent sand-grain roughness
as a function of LWC.
230
1.0
o5 m
I I I 1-250 260 270 280
STAT[CTER°ERATURE,K
F-7: Emperical relationship for equivalent sand-grain roughness
as a function of static temperature.
231
Report Documentation PageNat*oriel Aeronauhcs and
SDace Admlnistrallon
I. ReportNo. 2. GovernmentAccessionNo. 3. Recipient'sCatalog No.
NASA CR- 185129
4. Titleand Subtitle
Users Manual for the NASA Lewis Ice Accretion
Prediction Code (LEWICE)
7. Author(s)
Gary A. Ruff and Brian M. Bcrkowitz
g. PerformingOrganizationName and Address
Sverdrup Technology, Inc.
Lewis Research Center Group
2001 Aerospace ParkwayBrook Park. Ohio 44142
12 SponsoringAgencyName and Address
National Aeronautics and Space Administration
i Lewis Research CenterCleveland, Ohio 44135-3191
5. ReportDate
May 1990
6. PerformingOrganization Code
8. PerformingOrganizationReportNo
None
10. WorkUnit No.
505-68-11
11. ContractorGrantNo.
NAS3-25266
13. Type of Reportand Period Covered
Contractor ReportFinal
14. SponsoringAgencyCode
i15. Supplementary Notes
Project Manager, J.J. Reinmann, Propulsion Systems Division, NASA Lewis Research Center.
i' 16. Abstract
LEWlCE is an ice accretion prediction code that applies a time-stepping procedure to calculate the shape of an
ice accretion. The potential flow field is calculated in LEWlCE using the Douglas Hess-Smith 2-D panel code
($24Y). This potential flow field is then used to calculate the trajectories of particles and the impingement points
on the body. These calculations are performed to determine the distribution of liquid water impinging on the
body, which then serves as input to the icing thermodynamic code. The icing thermodynamic model is based on
the work of Messinger, but contains several major modifications and improvements. This model is used to
calculate the ice growth rate at each point on the surface of the geometry. By specifying an icing time increment.
the ice growth rate can be interpreted as an ice thickness which is added to the body, resulting in the generation
of new coordinates. This procedure is repeated, beginning with the potential flow calculations, until the desired
icing time is reached. The operation of LEWlCE is illustrated through the use of five examples. These examples
are representative of the types of applications expected for LEWlCE. All input and output is discussed, along
with many of the diagnostic messages contained in the code. Several error conditions that may occur in the code
for certain icing conditions are identified, and a course of action is recommended. LEWICE has been used to
calculate a variety of ice shapes, but should still be considered a research code. The code should be exercised
further to identify any shortcomings and inadequacies. Any modifications identified as a result of these cases, or
of additional experimental results, should be incorporated into the model. Using it as a test bed for improvements
to the ice accretion model is one important application of LEWICE.
17. Key Words(SuggestedbyAuthor(s)) 18. DistributionStatement
Aircraft icing Unclassified-Unlimited
Ice accretion modeling Subject Category 01Heat transfer
19. SecurityClassif. (ofthisreport) 20. SecurityCliisllif.(of thispage) 21. No.of pages 22. Price*
Unclassified Unclassified 233 A 10
"For sale by the National Technical Information Service, Springfield, Virginia 22161
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