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International Journal of Mechanical Engineering and Technology (IJMET)
Volume 9, Issue 9, September 2018, pp. 945–967, Article ID: IJMET_09_09_104
Available online at http://www.iaeme.com/ijmet/issues.asp?JType=IJMET&VType=9&IType=9
ISSN Print: 0976-6340 and ISSN Online: 0976-6359
© IAEME Publication Scopus Indexed
HEAT TRANSFER IMPROVEMENT IN A SOLAR
AIR HEATER BY USING DIFFERENT TYPES OF
ARTIFICIAL ROUGHNESS: A REVIEW
J L Bhagoria
Professor, Department of Mechanical Engineering,
Maulana Azad National Institute of Technology, Bhopal, India
Yogesh Agrawal
Research Scholar, Department of Mechanical Engineering,
Maulana Azad National Institute of Technology, Bhopal, India
ABSTRACT
Heat transfer in the field of thermal engineering plays an important role. Artificial
roughness can be applied in many types of roughness geometry element which can be
two and three dimensional ribs, sand grain, combination of rib and groove rib,
grooves, compounding ribs, wire fixation, transverse or inclined type of ribs, dimple /
protrusion formation type of geometry and expanded wire mesh fixation. An
artificially roughened surface of roughness plate is believed an efficient for the
increment of heat transfer. For the last thirty years, the use of artificial roughness
elements in air heater had been a good topic for research. Multiple investigators have
carried out so many numerical and observational works. Various roughnesses
geometric in literature have been reported by investigators to study the high
temperature transfer and friction characteristics of an artificially roughened duct of
solar air heaters. For increasing the heat transfer among a heat transfer technique,
artificial roughness is one of the most valuable techniques. Many investigators found
about the application of artificial roughness in the form of ribs. The literature of the
roughened heat transfer system by using different kinds of artificial roughness is
covered by this paper. To review the performance of various rib geometry employed
for developing artificial roughness, this attempt is formed. Based on correlations
observed by different researchers for friction factor, and heat transfer coefficient,
Improvement of heat transfer coefficient and reduction of friction factor is considered.
It has also reviewed and presented the thermo-hydraulic performance of different
geometry on its absorber surface of solar air heater duct has been compared.
Keywords: Artificial roughness, Heat Transfer, Pressure drop, solar air heater, solar
energy.
Heat Transfer Improvement in a Solar Air Heater by Using Different Types of Artificial
Roughness: A Review
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Cite this Article: J L Bhagoria and Yogesh Agrawal, Heat Transfer Improvement in a
Solar Air Heater by Using Different Types of Artificial Roughness: A Review,
International Journal of Mechanical Engineering and Technology, 9(9), 2018, pp.
945–967.
http://www.iaeme.com/IJMET/issues.asp?JType=IJMET&VType=9&IType=9
NOMENCLATURE Physical Parameters
Ac surface area of absorber plate, mm2
B half length of V-rib element, mm
Cp specific heat of air, J/kg K
Dh equivalent or hydraulic diameter of duct, mm
D diameter of dimple or protrusion, mm
E roughness height, mm
G groove position, mm
H height/depth of duct , mm
h heat transfer coefficient, W/m2K
I intensity of solar radiation, W/m2
K thermal conductivity of air, W/mK
L length of test section of duct, mm
L longway length of mesh, mm
M mass flow rate, kg/s
P pitch, mm
Qu useful heat gain,W
qu useful heat flux, W/m2
S shortway length of mesh, mm
Tpm mean plate temperature, K
Tam mean air temperature, K
Ti fluid inlet temperature, K
Ta ambient temperature, K
To fluid outlet temperature, K
UL overall heat loss coefficient, W/m2K
V velocity of air in the duct, m/s
W width of duct, mm
W width of rib, mm
∆p pressure drop, Pa
Geometrical dimensionless parameters
B/s relative roughness length
d/D relative print diameter
DD relative discrete distance
d/w relative gap position
d/α relative gap distance
e/Dhh relative roughness height
FR collector heat removal factor
fr friction factor for rough surface
Gd/Lv relative gap distance
g/e relative gap width
g/p relative groove position
HD/HD relative baffle height
l/e relative long way length of mesh
l/s relative length of metal grid
Ng number of gaps
Nu Nusselt number
PB/HB relative baffle pitch
p/e relative roughness pitch
J L Bhagoria and Yogesh Agrawal
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p’/p relative staggered rib pitch
Pr prandtl number
Re Reynold number
s/e relative short way length of mesh
s’/s relative roughness segment ratio
W/H duct aspect ratio
WD/HD channel aspect ratio
WD/WB relative baffle width
W/w relative roughness width
w/e staggered rib length to rib height ratio
α/90 relative angle of attack
Greek Symbols
(τα)e Effective transmittance absorptance
product
ɸ wedge angle/chamfer angle, degree
Α angle of attack, degree
Δ transition sublayer thickness, mm
ƞth thermal efficiency
Ρ density of air, kg/m3
Acronym
CFD Computational Fluid Dynamics
THPP Thermo-Hydraulic Performance Parameter
1. INTRODUCTION
Energy in various structures has assumed a decisive part in Globally for Economic advance
and industrialization. The Non-renewable energy resources are fixed (in the historic period of
energy shortage). Therefore, more consideration must be paid to upgrade and use the
sustainable power source assets. Sun is a definitive wellspring of vitality. All the patterns of
energy in the universe as we know it are solar in origin. The best points of interest of sun
based energy as contrasted and different strains of energy are that it is spotless and can be
provided without ecological contamination. [1] It is an effective process of enhancing thermal
efficieny of conventional solar air heaters is by implementing roughness on the bottom of an
absorber in terms of ribs, grooves, baffles, winglets, twisted tapes etc. To enhance the
performance of solar air heater in terms of thermo hydraulic can be improved by a passive
technique of heat transfer that is called artificial roughness. The device, which absorbs
incoming solar radiations and converts it into thermal energy, is called a solar air heater at the
absorbing surface. Many practices have been prepared by multiple investigators in their
research work for gaining the heat transfer increment through these solar air heaters by
applying various roughness elements on the surface of the absorber plate. Many researchers
developed friction factor correlation and heat transfer coefficient for roughened duct of solar
air heater have been studied in this paper. This paper summarizes all these efforts of attempt
and to achieve the conclusion about past experimentation works. This is a chance for
investigators to create the new parameters with materials and methods to get the satisfied
result of improvement of heat transfer with the decrement of the friction power provision. [2].
2. THEORY
2.1. SOLAR ENERGY CLASSIFICATION
Solar Energy is the best effectively accessible wellsprings of progression. This is one of the
non-conventional sources of energy because it is pollution free, hence aids in lessening the
greenhouse impact.
The sun's energy can be classified in two forms:
Heat Transfer Improvement in a Solar Air Heater by Using Different Types of Artificial
Roughness: A Review
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2.1.1. Heat or Thermal Energy (ii) Light Energy
Solar thermal methodology application the solar heat energy to heat substances like air or
water for use like pool heating, space heating and water heating for residencies and
commercial. The solar heat can be helpful for generating electricity on a big scale by
transforming the solar energy into mechanical energy.
2.2. SOLAR THERMAL COLLECTORS AND ITS TYPES
A device, which is used to collect solar radiation and displaces the energy to a fluid flowing in
contact with it is called solar thermal collector. The use of solar energy needs solar collectors.
Solar collectors can be either focusing or non-concentrating. In the non – concentrating form,
the area that intercepts the solar radiation that is collector area is the same as the area
absorbing the radiation that is absorber area. In this method, light is absorbed by the whole
solar panel. Concentrating collectors are having a larger interceptor rather than absorber as
shown in Fig.1 [3]. Multiple forms of solar thermal collectors are:
2.2.1. FLAT PLATE TYPE OF SOLAR COLLECTOR (NON CONCENTRATING TYPE)
As shown in the Fig. 2 for space, heating, drying and similar industrial application demanding
heated air at low to moderate temperature by applied flat plate solar air heaters. A function of
many designs and operating parameters are used to calculate the thermal efficiency of a solar
air heater (collector) .The Convective heat transfer coefficient is one of the key parameters
between the absorber plate and air flowing through the collector duct. They include of (1) a
transparent cover that decreases heat losses, (2) a heat insulating backing, (3) A heat transport
fluid it (air, antifreeze or water) to reduce heat from the absorber, and (4) A dark flat plate
observer. It can be found directly or by using a heat exchange as per shown in Fig.3.
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2.2.2. CONCENTRATING (FOCUSING) TYPE SOLAR COLLECTOR
As shown in Fig.4 Focusing or Concentrating Collectors intercept direct radiation over a huge
area and concentrate it onto a small absorber area. To get more efficient high temperature than
flat plate collector can be provided by these collectors because the absorption surface area is
much smaller. Hence diffused sky radiation cannot be concentrated onto the absorber. To
constantly orient the collectors towards the sun and to keep the absorber at the point of focus
mechanical equipment is required by the most concentrating collectors as shown in Fig.5 & 6.
Heat Transfer Improvement in a Solar Air Heater by Using Different Types of Artificial
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2.3. THE PERFORMANCE IMPROVEMENT OF SOLAR AIR HEATER
a. Increment of Intensity of solar radiations occurrence upon the solar collector
b. Decrement of thermal losses by;
i. Application of multiple glass covers
ii. Application of substitute medium or Vacuum in space;
c. Selective coating on the absorber plate by:
i. Application of two pass system
d. Enhancement of heat transfer from absorber plate to the air by;
i. Application Enlarged surfaces
ii. Packed bed solar heaters
iii. (iii)Application of artificial roughness on absorber plate
2.4. BASICS OF ARTIFICIAL ROUGHNESS
To improve thermo hydraulic performance of solar air heater a passive heat transfer
improvement technique is developed which is called artificial roughness is developed to
improve forced convective heat transfer, which needs flow at the heat-transferring surface to
be turbulent. Hence, Turbulence has to come from the fan or blower for creating energy and
to flow air through the duct, excessive power is needed. Therefore, it is mandatory that the
turbulence must be developed only in the area very near to the heat-transferring surface, to be
lessened power requirement. It can be done by making the height of the roughness element to
be short as compared with the duct dimension. To significantly improve the heat transfer
coefficient with minimum pressure loss penalty, artificial roughness on heat transferring
surface of a symmetrically high aspect ratio rectangular duct modeled as solar air heater ducts
has been shown.
Karwa et al. [13] Examined Experimentally and studied of develop heat transfer and
friction in the transverse, inclined, V-continuous and V-discrete pattern by utilizing two
identical parallel ducts, one with the roughened absorber plate and the other with the smooth
one in a symmetrically heated rectangular duct with ribs on the heated wall. The roughened
elements had the rib chamfer angle was fixed at 150 while a relative roughness pitch (p/e) of
4.58 and 7.09.This study demonstrated a significant enhancement in the Nusselt number (50-
120%) due to the enhancement in thermal efficiency (10-40%) over solar air heaters with
smooth absorber plates.
Bopche et al. [23] Examined the heat transfer coefficient and friction factor on the
absorber surface of an air heater duct for specially prepared inverted U-shaped turbulators.
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The roughened wall was uniformly heated and the remaining three walls were insulated. The
experiments surrounded the Reynolds number range from 3800 to 18,000, e/Dh varied from
0.0186 to 0.03986 and p/e varied from 6.67 to 57.14, the angle of attack of the flow on
turbulators α=900 kept constant during the whole experimentation. As compared to the
smooth duct, the turbulator roughened duct enhances the heat transfer and friction factor of
2.82 and 3.72 times respectively.
Kumar et al. [24] researched the thermo-physical performance of solar air heaters with
discrete W-shaped ribs and the parameters W/H=8;e/Dh=0.0168-0.0338;p/e=10;Re=3000-
15,000;α=30-750 on the absorber plate .Also developed the correlations for a Nusselt number
and friction factor using the range of parameters selected. They found that the increase in
Nusselt is 2.16 and friction factor is 2.75 at e/Dh=0.0338 and α=600 as compared to smooth
solar air heater.
Lanjewar et al.[29] examined experimental investigation with W-shaped ribs arranged at
an inclination with respect to flow direction on its underside on one broad wall for heat
transfer and friction factor characteristics of rectangular duct roughened. Range of parameters
was used are W/H=8, p/e=10, e/Dh=0.018-0.03375, Re=14000 and α=30-750. Max.
Enhancement of a Nuselt number and friction factor was found to be respectively 2.36 and
2.01 times that of the smooth duct as a result of providing artificial roughness for an angle of
attack of 600.
Gawande et al. [36] researched methodologies of numerical modeling and simulations for
thermal achievement optimization with 200 angled ribs were imitated used an algorithm
created in MATLAB to assume the most favorable set of design and performing set of
parameters. The simulation is done using correlations developed using second order
polynomial. The effect of heat flux, velocity, variation in the width of the duct, mass flow rate
and the no. of glass covers, on thermal & effective efficiencies of roughened solar air heater
are described in the form of plots.
2.5. HEAT TRANSFER IMPROVEMENT THROUGH ARTIFICIAL
ROUGHNESS IN SOLAR AIR HEATER
Most extreme heat transfer coefficient is utilized as a part of sunlight based air radiators using
the artificial roughness up to laminar sub-layer .The nearness of rib may upgrade heat transfer
in view of intrusion of the viscous sub-layer, which yields streamed turbulence, partition, and
reattachment prompting a higher heat transfer coefficient. The ribs are given just on the
heated divider. The other three dividers are smooth (without ribs) and shield. It is along these
lines alluring that the turbulence must be made just in the area near the heat exchanging
surface, i.e., In the laminar sub-layer just where the heat trade happens and the stream ought
not be unduly exasperates to stay away from over the top grinding misfortunes. In spite of the
fact that there are a few parameters that describe the course of action and state of the
harshness, the roughness element height (e) and pitch (p) are the most critical parameters.
These parameters are typically determined as far as dimensionless parameters, to be specific,
relative roughness height (e/Dh) and the relative roughness pitch (p/e).
2.6. PERFORMANCE ANALYSIS OF SOLAR AIR HEATER
It is required to analyze thermal and hydraulic performance; the design of solar air heater
should be efficient. It deals with a heat transfer process within the collector and hydraulic
performance deals with pressure drop in the duct. Both are given below:
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2.6.1. THERMAL PERFORMANCE
The useful energy gain (Qu) across the test section was calculated from the temperature to gain
across the test section and air mass flow rate (m) by using equation (1)
Qu=mCp(To-Ti) (1)
The convection heat transfer coefficient (h) from the absorber plate to air was measured
from mean temperature of the plate (Tpm) and air (Tam) using equation (2). It can be enhanced
by implementing artificial roughness on the surface of the absorber plate.
Qu =hAc (Tpm-Tam) (2)
It can be described in non-dimensional forms by using the following relationship of the
Nusselt number (Nu) given by a numerical form using equation (3)
Nu=hL/k (3)
Further, thermal efficiency (ƞth) of solar air heater can be explained by using the equation
(4)
ƞth= qu/I=FR[I(τα)e-UL((Ti-To)/I] (4)
2.6.2. HYDRAULIC PERFORMANCE
It meets with the pressure drop (∆P) in the duct and accounts for energy consumption by a fan
to propel air through the duct. The non - dimensional form express it by using the equation (5)
Friction factor (f) = (∆P)Dh/2ρLV2
(5)
2.6.3. THERMO HYDRAULIC PERFORMANCE
The design of solar collector should be required for highest heat Energy transfer to the passing
fluid with the lowest consumption of fan energy, the design of solar collector should be
desirable and hence can be applies hydraulic and thermal characteristics of the collector
simultaneously. [4]
2.7. FACTORS AFFECTING THE FLOW PATTERNS ON RIB GEOMETRY
The characterization of roughness can be described by using the key dimensions geometrical
parameters are:
i. Rib Height (e): It generates the following effect on the roughness element
If e<δ There will be no roughness impact
If e>δ There will be more roughness impact of fluid pressure as compared to heat
transfer
If e>δ There will improve in heat transfer and moderate fluid pressure could be
served
ii. Rib Pitch (p): The flow on downstream side of the roughness element is divided
based on height and to maintain the pitch properly the reattachment of the flow
should be occurring. If the pitch ratio is less than 8 then the reattachment of the
shear layer does not occur and it which shows in poor heat transfer from the
surface.
iii. Rib Alignment and Inclination(α): The achievement of the soalr air heater in the
surface the friction factor goes down rapidly as the angle of attack fall down from
900 to 15
0.
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iv. Duct Aspect Ratio (W/H): This factor plays a very important role in identifying
thermo hydraulic performance, which is the ratio of duct width to duct height.
v. Duct height (h): The air velocity can be increased by decreasing of duct height.
The higher efficiency of solar heater can be calculated by decreasing duct height.
By decreasing the depth solar air heater, efficiency can be increased. It is the ratio
of the distance between two consecutive ribs and height of the rib.
vi. Relative roughness height (e/Dh): It is defined as the ratio of rib height to
equivalent diameter of the air passage. The friction factor and Nusselt Number can
be increased by raising the relative roughness height.
vii. Angle of attack (α): It can be defined as the inclination of rib with direction of air
flow in the duct. The angling of the rib as per flow develop counter rotating
secondary flow along the span that reasons span wise variation of heat transfer
coefficient.
viii. The Shape of roughness element: The roughness elements can be written as two-
dimensional ribs or three-dimensional discrete elements, transverse or inclined ribs
or V-shaped continuous or broken ribs with or without a gap. It can be arc-shaped
wire, dimple, cavity, or compound rib-grooved. To investigate thermo hydraulic
performance the different shapes like circular, semi-circular and chamfered but the
most common shape of the ribs is square have been applied .
ix. Effect of rib chamfering: By deflecting the flow, the reattachment length can be
felt down and to reattach it closer to the rib. By decreasing the reattachment, the
length allows to organize ribs more nearly. Chamfering of the rib also enhances
the shedding of vortices developed at the rib top that show in raise turbulence.
Based on thermodynamic performance the optimum-chamfering angle has been
answered equal to 15-180.
3. TYPES OF ARTIFICIAL ROUGHNESS
3.1. Transverse continuous ribs
Prasad and Saini [5] experimentally researched, with small-diameter protrusion wire on
absorber plate, heat transfer coefficient and the friction factor of the fully developed turbulent
flow in a solar air heater duct. The type and position of the geometry are shown in Fig.7.
It recognized that the average Nusselt number and average friction factor in the roughened
duct were at 2.10, 2.24, 2.38 and 3.08, 3.67, 4.25 times that of the smooth duct for relative
roughness height (e/Dh) of 0.020, 0.027 and 0.033 respectively. The greatest improvement of
heat transfer coefficient and friction factor were at 2.38 and 4.25 times than that of smooth
duct respectively.
Heat Transfer Improvement in a Solar Air Heater by Using Different Types of Artificial
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3.2. Transverse broken ribs
Sahu and Bhagoria [14] studied the effect with 90⁰ broken transverse rib on the absorber plate
on the heat transfer coefficient and thermal Efficiency of solar air heater. Integral Rib
Roughened absorber plate was made by fixing wire of 1.5mm diameter over one side of the
absorber plate as depicted in Fig.8. With the roughness geometry having pitch (p) range from
10-30 mm, Reynolds number (Re) of 3000-12000, height of the rib (e) of 1.5mm, and a duct
aspect ratio (W/H) was 8. The greatest improvement of heat transfer coefficient occurs at a
pitch (p) of about 20mm while on another side of this pitch, the Nusselt Number decreases.
Varun et al. [22] research and reviewed the thermal aperture of solar air heater having a
roughness element as a combination of inclined as well as transverse rib with the relative
roughness pitch (p/e) of 3-8, Reynolds number (Re) ranges from 2000-14000, and relative
roughness height (e/Dh) of 0.030. It was analyzed that the most favorable thermal
performance occurs having the value of relative roughness pitch (p/e) of 8.
3.3. Inclined ribs
Kumar et al. [26] experimentally studied have been carried out with artificial roughness in the
form 600 discrete the inclined ribs for the improvement of heat transfer coefficient of a solar
air heater having roughened air duct provided. Marked improvement in heat transfer
coefficient has been reached with such roughness element. The investigated geometry has
been depicted in Fig.9.
Aharwal et al. [18] research and reviewed the effect of artificial roughness by inclined
split rib arrangement in a rectangular duct in solar air heater depicted in Fig.10. Considering
the gap of width ratio (g/e) and a gap of position ratio (d/w). The gain in Nusselt number and
the friction factor were in the range of 1.48-2.59 times and 2.26- 2.9 times of smooth duct
respectively.
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Gupta et al. [6] research and reviewed on fluid flow and heat transfer characteristics of
artificially roughened solar air heater ducts with inclined wires. They found that the greatest
heat transfer coefficient appeared for an angle of attack (α) of 600 whereas the friction factor
greatest for an angle of attack of 700.
3.4. Wire Mesh
3.4.1. Expanded Wire Mesh Fixation
Saini and Saini [7] experiments carried out by providing the expanded metal mesh geometry
on the absorber plate in solar air heater, the effect of heat transfer coefficient and friction
factor as depicted in Fig.11. For fully matured turbulent flow in a rectangular duct with a
large aspect ratio (W/H) of 11.1 has been found greatest Nusselt number and friction factor
corresponding to the relatively long way length of mesh (l/e) and the relatively short way
length of mesh (s/e) was 46.87, 71.87 and 25, 15 respectively. The greatest improvement in
Nusselt number and friction factor values were reported of the order of 4 and 5 times to that
of the smooth absorber plate respectively.
3.4.2. Discredited metal wire mesh
Karmare and Tikekar [17] Examined experimentally with metal mesh grit roughness as shown
in Fig.12. The range of the parameter was the Reynolds number as 4000-17000, (e/Dh) as
0.035-0.044, (p/e) as 12.5-36 and (l/s) as 1.72-01. They displayed that plate with Roughness
parameter (l/s) as 1.72, (p/e) as 17.5 had optimum performance.
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3.5. Chamfered ribs
Karwa et al.[10] Examined experimentally for repeated integral chamfered rib roughness on
the absorber plate as depicted in Fig. 13. its effect with rib chamfered angle of 15⁰ to 18⁰
having an aspect ratio (W/H) of 4.8 to 12, Reynolds number (Re) of 3000 to 20000 relative
roughness pitch (p/e) of 4.5 to 8.5, and a relative roughness height (e/Dh) of 0.0141 to 0.0328.
The greatest improvement was found in the air heater with the highest relative roughness
height.
3.6. Wedge shaped ribs
Bhagoria [12] Examined Experimentally with wedge shaped transverse integral ribs, the
effect of relative roughness pitch (p/e) relative roughness height (e/Dh) and wedge angle (ɸ)
on the heat transfer coefficient and the friction factor in solar air heater rectangular duct
roughened depicted in Fig.14. The greatest improvement of heat transfer at wedge angle of
about 10⁰. The researcher recorded an enhanced in Nusselt number up to 2.4 times while the
friction factor increases up to 5.3 times as compared to a smooth duct.
3.7. W-shaped rib
3.7.1. Continuous W-ribs
Lanjewar et al.[27] Researched Experimentally with W-shaped rib by utilizing the concept of
increasing number of a secondary cell. The Range of the parameter was the relative roughness
height (e/Dh) as 0.018-0.03375, angle of attack (α) 30-750 and relative roughness pitch (p/e)
10. They noted a W-down arrangement with the angle of attack 600 given a most favorable
thermo-hydraulic performance. The greatest improvement of Nusselt number and friction
factor was 2.36 and 2.01 times that of the smooth plate for an angle of attack 600. Roughness
geometry is depicted in Fig.15.
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3.7.2. Discrete W-ribs
Kumar et al. [20] investigated experimentally with discrete W-shaped ribs to find the heat
transfer distributions in solar air heater having its absorber plate roughened. The experiment
encircle Reynolds number (Re) range from 3000 to 15,000, rib height (e) values of 0.75 mm
and 1 mm, angle of attack (α) 450 relative roughness height (e/Dh) 0.0168 and 0.0225 and
relative roughness pitch (p/e) of 10.Thermal performance of the roughened solar air collector
was compared with that of smooth one under similar flow conditions and it was recorded that
the thermal performance of the roughened channel was1.2–1.8 times the smooth channel for a
range of parameters investigated & depicted in Fig.16.
4. ROUGHNESS ELEMENT COMBINATION
4.1. Transverse and inclined rib combination
Varun et al. [22] examined by applying the concept of combination roughness of transverse
and inclined ribs. They noted Reynolds number from 2000-14,000, relative roughness height
(e/Dh) as 0.030, relative roughness pitch (p/e) 3-8, they also reported that roughened collector
having roughness pitch (p) of 8 gave the best performance. Roughness geometry is depicted in
Fig.17.
Heat Transfer Improvement in a Solar Air Heater by Using Different Types of Artificial
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4.2. Transverse rib groove combination
Jaurker et al. [15] researched experimenting with performance of transverse rib roughness for
enhanced efficiency. The greatest heat transfer was achieved for relative roughness pitch (p/e)
of 6. The most favorable heat transfer was recorded in groove position to pitch ratio of 0.4.
Roughness geometry is depicted in Fig.18.
4.3. Chamfered rib groove combination
Layek et al. [16] examined with chamfered rib roughness. Experimental study was carried out
for Reynolds number from 2000-21,000, relative roughness pitch (p/e) 4.5-10, chamfer angle
(α) as 5-300, relative groove position (g/p) as 0.3-0.6, and relative roughness height as (e/Dh)
0.019-0.043.They recorded the Nusselt number and friction factor increased by 3.24-0.78
times, respectively, as compared to a smooth duct. The greatest improvement of Nusselt
number and friction factor were achieved for the relative groove position (g/p) of 0.4.
Roughness geometry is depicted in Fig.19.
4.4. Arc shaped ribs
Saini and Saini [19] researched and Reviewed with providing the bow- shaped parallel wire
on the absorber plate in solar air heater,the effect of heat transfer coefficient and friction
factor of relative roughness height (e/Dh) and angle of attack (α/90) as depicted in Fig. 20.
With Reynolds, number (Re) ranges of 2000-17000, angle of attack (α/90) of 0.3333-0.6666
and relative roughness height (e/Dh) of 0.0213-0.0422 for a fixed relative roughness pitch
(p/e) of 10. The greatest improvement in Nusselt number was achieved as 3.80 times
corresponding to the relative angle of attack (α/90) of 0.3333 at the relative roughness height
(e/Dh) of 0.0422.
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4.5. Dimple surface
4.5.1. Transverse dimple roughness
Saini et. al [21] used the latest concept of dimple shaped artificial roughness. Experimentally
enclosed range of parameters are: Reynolds number (Re) from 2000-12,000, relative
roughness height (e/Dh) as 0.018-0.037 and relative roughness pitch (p/e) 8-12. They found
the greatest value of relative roughness height of 0.0379 and relative roughness pitch of 10.
The least value of friction factor corresponding to the relative roughness height as 0.0289,
relative roughness pitch of 10. Roughness geometry is depicted in Fig. 21
4.5.2. Staggered dimple roughness
Bhushan et al. [28] studied with staggered dimple roughness in place of transverse dimple
roughness. Range of parameter reviewed were relative short way length (s/e) as 18.75-37.50,
relative long way length (l/e) as 25.00-37.50, Reynolds number (Re) from 4000-20,000,
relative print diameter (d/D) as 0.147-0.367, relative roughness height (e/Dh) as 0.03, an an
aspect ratio (W/H) as 10. Greater improvement in heat transfer coefficient was recorded for
relative short way length (s/e) of 31.25, relative long wavelength (l/e) of 31.25 and relative
print diameter (d/D) of 0.294 & depicted in Fig. 22.
4.5.3. Arc shaped dimple roughness 1
Yadav et al. [42] reviewed with arc shaped dimple roughness. Investigated parameter was
Reynolds number range from 3600-18,000, arc angle of protrusion arrangement as 45-750
(p/e) as 12 to 24, and (e/Dh) as 0.015-0.03 .The greatest improvement of Nusselt number and
friction factor was found to be 2.89 and 2.93 times, respectively of smooth duct for a range of
Heat Transfer Improvement in a Solar Air Heater by Using Different Types of Artificial
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parameter examined. The greatest improvement of the high heat transfer and friction factor
occurred in relative roughness height (e/Dh) of 0.03, relative roughness pitch (p/e) of 12 and
for arc angle value of 600. Roughness geometry is shown in Fig. 23.
4.5.4. Arc shaped dimple roughness 2
Sethi et al. [30] examined dimple shaped roughness. The range of parameters was investigated
and covered by duct aspect ratio (W/H) 11, relative angle of attack 47-750, Reynolds number
(Re) from 3600-18,000, relative roughness height (e/Dh) as 0.021-0.036,. They recorded
greatest value of the Nusselt number corresponding to the relative roughness height (e/Dh) of
0.036, relative roughness pitch (p/e) of 10 and arc angle 600 as depicted in Fig. 24.
Singh et al. [33] experimentally reviewed enclose the Reynolds number (Re) in the range
of 2200–22,000, relative roughness width (W/w) ranges from 1 to 7, relative roughness pitch
(p/e) the range of 4–16 relative roughness height (e/Dh) values of 0.018–0.045, and arc angle
(α) range of 30–750. By investigation and accumulated data correlations for the Nusselt
number and friction factor were matured as shown in Fig.25.
Pandey et al. [35] conducted analytically with multiple arcs with gaps.The range of
parameters were recorded are Reynolds number (Re) 2100-21000, relative roughness height
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(e/Dh) =0.016 to 0.044, angle of attack (α) =30-750 Relative width (W/w) =1-7, relative gap
distance (d/α) =0.25-0.85, relative roughness pitch (p/e) =4-16,.The greatest increase in new
and off was5. 85 and 4.96 times in comparison to the smooth duct are shown in Fig. 26.
4.6. V-Shaped ribs
4.6.1. Continuous type
Momin et al. [11] examined with inclined rib resulted in improve performance than transverse
ribs due to the increase of secondary vortices. The number of secondary vortices was
increased. They reviewed with V-shape rib roughness as depicted in Fig. 27. And also
examined the thermo hydraulic performance of solar air heater for Reynolds number (Re) as
2500-18,000, relative roughness height (e/Dh) as 0.02-0.034, an angle of attack (α) as 30-90
for fixed relative roughness pitch (p/e) of 10. Nussselt number and friction factor were
recorded as 2.30 and 2.83 times of smooth duct plate for the angle of attack 600 for greatest
improvement.
4.6.2. Discrete Type
Muluwork et al. [8] investigated and compared the thermal performance of V-shaped rib with
the staggered discrete V-apex up and V-down the ribs with corresponding staggered discrete
ribs. The roughness geometry is depicted in fig.28. They determined a Stanton number for V-
down discrete ribs greater than corresponding V-up and transverse discrete ribs. Stanton
number recorded improvement as 1.32-2.47 in the range of parameters examined.
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Sahu et al. [34] examined experimentally with Discrete arc-shaped rib roughness, heat
transfer and friction factor in solar Air heater duct on absorber plate, the roughened wall being
heated while the remaining three walls are insulated. It observed that the Nusselt number
increases as increases the Reynolds number attains a maximum for pitch (p) of 15 mm. For
improving the efficiency of solar air heater height of the rib in the range of 1-2mm, duct
aspect ratio (W/H) =8, relative roughness pitch (p/e) =10, an angle of arc 300, relative angle of
attack (α/90)0.3333, was utilized as depicted in Fig. 29.
Karwa et al. [13] experimental reviewed by V-discontinuous and V- discrete ribs. The
range of the parameter was relative roughness pitch (p/e) as 10.62, relative roughness length
(B/S) as 3 and 6, angle of attack as 450 and 600 and a Reynolds number as 2850-15,500.
They determined that discrete ribs perform greater than discontinuous ribs and 600 rib
perform better than 450 ribs. Roughness geometry is depicted in Fig. 30 & 31.
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4.7. Multiple V-ribs
4.7.1. Multiple continuous V-ribs
Hans et al. [25] examined with multiple continuous V- ribs and using a concept of increasing
number of secondary flow cells. The experiment encircled with Reynolds number (Re) from
2000-20,000, angle of attack 30-750, relative roughness height as (e/Dh) 0.019-0.043, relative
roughness pitch (p/e) 6-12, and relative roughness width (W/w) range as 1-10. Greatest heat
transfer occurred for relative roughness width (W/w) of 6 while friction factor attained
greatest value for relative roughness width (W/w) of 10. Both Nusselt number and friction
factor 6 and 5 times respectively in comparison to a smooth duct of parameter investigated.
Roughness geometry is depicted in Fig.32.
4.7.2. Multiple V-ribs with gap
Kumar et al. [31] utilized and examined the method of turbulence and acceleration of flow by
providing gap. Range of parameter encircled are Reynolds number (Re) from 2000-20,000,
relative width ratio as 6, angle of attack (α) 600, the relative gap distance ratio (Gd/Lv) as
0.24-0.8, relative gap width (g/e) as 0.5-1.5, relative roughness height (e/Dh) as 0.043. They
recorded the greatest improvement in Nusselt number and friction factor as 6.32 and 6.12
times of a smooth plate respectively as depicted in Fig. 33.
Maithani et al. [38] Researched experimentally have been carried out for improvement of
heat transfer coefficient with V-ribs and symmetrical gaps as turbulence promoter was used.
The investigated encircled Reynolds number (Re) 4000-18000, angle of attack (α) =30-750,
gap width to rib height (g/e) =1-5, relative roughness height (e/Dh) =0.043, relative
roughness pitch (p/e) =6-12, Number of gaps (Ng) =1-5.The greatest improvement of the
order of 3.6 times that of the smooth duct has been achieved, similarly, friction factor(ff ) also
increase by 3.67 times of that of smooth duct achieved as described in Fig. 34.
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Kumar et al. [39] Experimentally and numerically analyzed of heat transfer improvement
with broken multiple V-type baffle encircled parameters of channel aspect ratio (WD/HD)
=10, Reyonlds No. (Re) =3000-8000, relative discrete distance (DD) 0.67, relative baffle
width (WD/WB) 1-6, relative baffle height (HB/HD) = 0.5, relative baffle pitch (PB/HB) =
10, relative gap width (g/e) =1 with 600 angled broken multiple V-type baffles. The obtained
experimental results showed that greatest overall thermal performance occurred at a relatively
baffle width of 5, as depicted in Fig. 35
Kumar et al.[40] Researched and Examined with ‘S’ shape ribs for heat transfer and
friction factor and their correlations development for solar air heater duct artificially
roughened with aspect ratio(W/H)=12, , arc angle (α) =30-750,relative roughness width
(W/w) =1-4, relative roughness pitch(p/e)=4-16,relative roughness height(e/Dh)=0.022-0.054
and Reynolds number (Re) =2400-20000. Experimental results showed that the greatest
improvement in Nusselt number (Nu) and friction factor (f) have been found in relative
roughness width (W/w) =3, relative roughness pitch (p/e) =8, relative roughness height (e/Dh)
=0.043, arc angle (α) =600 as depicted in Fig.36
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6. CONCLUSION
In this paper, an endeavor has been made to report the heat transfer coefficient and friction
factor characteristics of artificially roughened duct in solar air heater utilizing of an alternate
type of rib geometry. Tentatively Investigations completed for utilization of manufactured of
artificial roughness of different shapes, size and orientation by various researchers in order to
improve the heat transfer.
In light of the writing audit the accompanying Conclusion is drawn:-
1. Artificial roughness utilized as a part of solar air heater are a powerful method to
improve heat transfer to the liquid streaming having in the pipe and it announced
the greatest heat transfer contrasted with the smooth surface under a similar
parameter/working conditions. Distinctive sorts of roughness geometry utilized as
a part of solar air heater are inferring that it relies on shapes, size, orientation and
arrangement of the roughness component on the absorber plate.
2. There is a positive increment in heat transfer in solar air heater with an expansion
in erosion to the stream when its surface is roughened. In any case, the diverse
specialists locate an alternate estimation of the addition in heat transfer and
rubbing factor for each kind of rib geometry utilized.
3. Many sorts of parameter that recognized the roughness elements, but most
repeated roughness geometry for solar air heater is repeated ribbing type which is
described by the dimensionless parameter .i e. Relative roughness pitch (P/e),
relative roughness height (e/Dh) angle of attack (α), channel aspect ratio (W/H).
High perspective, proportion esteems have better heat transfer effectiveness while
low viewpoint proportion esteems have a superior heat transfer execution in solar
air heater and pipes.
4. In transverse rib component, the vast majority of the examinations directed give
the outcome that the execution of the V-shaped, W-shaped ribs is ideal at how the
attack angle of 600, though for transverse inclined ribs the ideal execution edge of
slant is 450. Use of multi V-formed rib roughness with gap has the most elevated
Nu when contrasted with different roughness geometries for the explored scope of
parameters.
5. It was discovered that utilization of the arc shaped formed rib geometry and metal
grit ribs have the most astounding thermo-hydraulic performance parameters when
contrasted with regularly roughness geometry for the investigated scope of
parameters. The utilization of broken arc ribs has the greatest Nu contrasted with
the basic arc based molded rib roughness for the examined range of parameters.
6. The utilization of V-sort showed demonstrated that highest overall thermal
performance execution happened in a moderately perplex width contrasted with
circular segment molded with various design and V type discrete formed.
7. In the outline of solar air heater, Computational fluid dynamics approach has been
applied as a decent approach as of late and it is to improve the plan procedure
arrangements with the heat transfer and fluid flow.
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