wl373e-v0.3
TRANSCRIPT
-
7/29/2019 WL373e-V0.3
1/26
Experiment Instructions
WL 373 Heat Conduction in Gases
and Liquids
-
7/29/2019 WL373e-V0.3
2/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
i
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
Experiment Instructions
This manual must be kept by the unit.
Before operating the unit:
- Read this manual.
- All participants must be instructed on
handling of the unit and, where appropriate,
on the necessary safety precautions.
Version 0.3 Subject to technical alterations
Gases and Fluids
Thermal Conductivity of
und FlssigkeitenWrmeleitung von Gasen
WL 373
Leistung / PowerHeizer/ Heater
Ein/ On
Aus / Off
Leistung / Power Watt
Temperatur 2/ Temperature 2 CTemperatur 1/ Temperature 1 C
123.4 C 123.4 C
123
-
7/29/2019 WL373e-V0.3
3/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
ii
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
Table of Contents
1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1
1.1 Intended Use . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1
2 Safety. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2
2.1 Structure of the Safety Instructions . . . . . . . . . . . . . . . . . . . . . . . . . . . 2
2.2 Safety Instructions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3
3 Unit Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4
3.1 Unit Construction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4
3.2 Function. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5
3.3 Operating the Measurement and Control Unit. . . . . . . . . . . . . . . . . . . 6
3.4 Connecting the Heat Exchanger . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7
4 Principles . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
5 Experiments. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 9
5.1 Calibrating the Heat Exchanger. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 9
5.1.1 Preparing for the Experiment . . . . . . . . . . . . . . . . . . . . . . . . 10
5.1.2 Performing the Experiment. . . . . . . . . . . . . . . . . . . . . . . . . . 10
5.1.3 Evaluating the Experiment: Calibration Curve . . . . . . . . . . . 11
5.2 Determination of Coefficients of Thermal Conduction. . . . . . . . . . . . 14
5.2.1 Preparing for the Experiment . . . . . . . . . . . . . . . . . . . . . . . . 14
5.2.2 Performing the Experiment. . . . . . . . . . . . . . . . . . . . . . . . . . 155.2.3 Evaluating the Experiment . . . . . . . . . . . . . . . . . . . . . . . . . . 15
6 Appendix . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 17
6.1 Working Sheet: . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 17
6.2 Symbols and Units. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19
6.3 Table with Coefficients of Thermal Conduction. . . . . . . . . . . . . . . . . 20
-
7/29/2019 WL373e-V0.3
4/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
iii
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
6.4 Technical Data. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 216.5 Index . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 22
-
7/29/2019 WL373e-V0.3
5/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
1 Introduction 1
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
1 Introduction
Using the WL 373 Heat Conduction of Gases
and Liquids unit, basic aspects of steady state
thermal conduction in liquid and gaseous materi-
als can be investigated.
The unit is particularly suited to the determination
of the coefficients of thermal conduction of liquid
and gaseous materials.
The unit comprises a double walled cylinder withan integrated heater acting as the heat source,
and the surrounding cylinder acting as the heat
sink. The medium to be investigated is placed in
between in a measurement slot.
The temperatures of the heat source and sink are
measured using thermocouples and transmitted
to a measurement and control unit where the elec-
trical power consumption of the heater is also dis-
played.
The unit is very easy to set up and operate, it is
thus also suitable for student use.
Working sheets included in the appendix to these
instructions ease the evaluation of experiments.
The following topics are covered by the unit:
Steady-state thermal conduction in gases and
liquids
Determination of coefficients of thermal con-
duction
1.1 Intended Use
The unit is to be used only for teaching purposes.
-
7/29/2019 WL373e-V0.3
6/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
2 Safety 2
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
2 Safety
2.1 Structure of the Safety Instructions
The signal words DANGER, WARNING or CAU-
TION indicate the probability and potential sever-
ity of injury.
An additional symbol indicates the nature of the
hazard or a required action.
Signal word Explanation
Indicates a situation which, if not avoided, will result in deathor serious injury.
Indicates a situation which, if not avoided, may result in deathor serious injury.
Indicates a situation which, if not avoided, may result in minoror moderately serious injury.
NOTICE Indicates a situation which may result in damage to equip-ment, or provides instructions on operation of the equipment.
DANGER
WARNING
CAUTION
Symbol Explanation
Electrical Voltage
Hot Surfaces
Notice
-
7/29/2019 WL373e-V0.3
7/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
2 Safety 3
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
2.2 Safety Instructions
WARNING
Reaching into the open measurement andcontrol unit can result in electric shocks.
Disconnect from the mains supply before open-ing.
Work should only be performed by qualifiedelectricians.
Protect the measurement and control unitagainst moisture.
WARNING
Risk of burns.
The knurled bolt and the heat exchanger are veryhot.
Leave the unit cool down.
-
7/29/2019 WL373e-V0.3
8/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
3 Unit Description 4
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
3 Unit Description
3.1 Unit Construction
Fig. 3.1 Unit Construction
Gases and Fluids
Thermal Conductivity of
und FlssigkeitenWrmeleitung von Gasen
WL 373
Leistung / PowerHeizer / Heater
Ein / On
Aus / Off
Leistung / Power Watt
Temperatur 2/ Temperature 2 CTemperatur 1/ Temperature 1 C
123.4 C 123.4 C
123
1 Heat exchanger (1) with internal heater and cooling facility
2 Base
3 Shut-off valves for the cooling flow and the medium to beinvestigated
4 Measurement and control unit with temperature and heaterpower displays
Mains cable (not shown)
1 2 3 4
-
7/29/2019 WL373e-V0.3
9/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
3 Unit Description 5
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
3.2 Function
The heat exchanger contains an electrical heater
that acts as the heat source (1), and an annular
cooling slot through which cooling water flows,
this acts as the heat sink (2). This construction
results in the flow of heat from the inside to the
outside.
Between the heat source and the heat sink is an
annular measurement slot (3) of constant width,
the medium to be investigated is contained here.
The medium is inserted in the slot via a connector(see arrow).
The temperature of the heat source is measured
using a thermocouple (4), the temperature of the
cooling water is measured (viewed in the direction
of the flow of heat) immediately behind the mea-
surement slot, also using a thermocouple, and fed
to the measurement and control unit.
Fig. 3.2 Section through the heat exchanger
Cooling water
connection
Cooling waterconnection
2 4 1 3
-
7/29/2019 WL373e-V0.3
10/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
3 Unit Description 6
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
To make it easier to clean the slot, the inner cylin-
der can be removed together with the heater. To
do this undo the knurled bolt (5), remove the lid
(6) and the sealing ring, and take out the cylinder
(7). Refit in the reverse order of removal.
NOTICE
Ensure that the sealing ring is correctly seated!
3.3 Operating the Measurement and Control Unit
The displays for the temperature of the heat
source (1) and the heat sink (2), and the heater
power (power consumption) display (3) are fitted
to the front of the measurement and control unit.
The heater power can be regulated up to
max. 140...150W using the potentiator (4).
The heater can be switched on and off using the
power switch (5).
NOTICE
In order to avoid the heater burning out, itswitches off automatically above a temperature of
95C.
The two thermocouples fitted to the heat
exchanger and the cable for the heater are con-
nected to the rear of the measurement and control
unit. The main switch is also to be found here.
Fig. 3.3 Dismantling theHeat exchanger
77 6 5
Fig. 3.4 Front of the measurement and
control unit
Gases and Fluids
Thermal Conductivity of
und FlssigkeitenWrmeleitung von GasenWL 373
Leistung / PowerHeizer / Heater
Ein / On
Aus / Off
Leistung / Power Watt
Temperatur 2/ Temperature 2 CTemperatur 1/ Temperature 1 C
123.4 C 123.4 C
123
1 2
5 4 3
-
7/29/2019 WL373e-V0.3
11/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
3 Unit Description 7
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
3.4 Connecting the Heat Exchanger
Connect the heat exchanger to the shut off
valves in accordance with Fig. 3.5
The hoses are fitted with rapid action hose cou-
plings, to release simply pull back the sleeve.
Make the electrical connections in accordance
with Fig. 3.5
NOTICE
Do not reverse the cables for the thermocouples!
Fig. 3.5 Connection of the heat
exchanger on the base andmeasurement and control unit
A/B Unions for the medium to be investi-
gated
Hose size: 6mm
C Cooling water inlet union
Hose size: 13mm
D Cooling water outlet union
Hose size: 6mm
E To the thermocouple/ heater
connector
F To the test unit input
G To the thermocouple/ cooler
connector
A B C D G
F
E
-
7/29/2019 WL373e-V0.3
12/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
4 Principles 8
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
4 Principles
The medium to be investigated fills the cylindrical
slot completely. The slot is narrow enough to per-
vent the occurrence of convection, the transfer of
heat in the slot is therefore more or less com-
pletely due to thermal conduction.
Due to the constant width of the slot, thermal con-
duction occurs as in a plane wall. Here the
Fourier law is applicable for the amount of heattransferred Q:
(4.1)
This yields the relationship for the heat flow :
(4.2)
with
Head flow through the wall under
investigation
A Wall surface area
T Temperature gradient in the wall
Wall thickness
Coefficient of the thermal conduction
is temperature dependant; in general the meantemperature in the wall is used.
(in W/Km) can be thought of as the energy that
is conducted every second through a 1m thick
wall over an area of 1m2when there is a temper-
ature difference of 1K between the opposite sides
of the wall.
Fig. 4.1 Thermal conduction in a plane
wall
T T1 T2=
Q
Q
T2
T1 Q A
-----------=
Q
Q A T
------------------------=
Q
-
7/29/2019 WL373e-V0.3
13/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
5 Experiments 9
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
5 Experiments
The selection of experiments makes no claims of
completeness but is intended to be used as a
stimulus for your own experiments.
The results shown are intended as a guide only.
Depending on the construction of the individual
components, experimental skills and environmen-
tal conditions, deviations may occur in the experi-
ments. Nevertheless, the laws can be clearly
demonstrated.
5.1 Calibrating the Heat Exchanger
In order to determine the heat losses in the unit,
calibration is necessary.
Air is used as the medium to be investigated
during the calibration process; air is used
because its coefficients of thermal conduction are
well documented (values are given in the Appen-
dix).
-
7/29/2019 WL373e-V0.3
14/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
5 Experiments 10
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
5.1.1 Preparing for the Experiment
Clean the measurement slot to remove any
water or remnants of other media from the slot
(refer to Fig. 3.3, Page 6).
Connect the heat exchanger to the measure-
ment and control unit in accordance with
Fig. 3.1, Page 4 and Fig. 3.5, Page 7 and
switch on the unit.
Open the shut off valves (1) and (2) for themeasurement slot
Make the cooling water connections and set
the flow rate for example to 1ltr/min at shut off
valve (3)
The flow rate for cooling water to be deter-
mined by the help of a stop watch and a meas-
uring tank in accordance to the following
equation (5.1)
(5.1)
V Capacity water [ltr]
t Time [s]
5.1.2 Performing the Experiment
Set the heat power P= 100W
Wait until the temperature values are constant Read and record the temperatures for heater
T1und cooling water T2, as well as the actual
heater power P
Repeat the experiment with heater powers of
P= 80W, 60W, 40W, 20W, 10W
Fig. 5.1 Shut off valves
V
1
2
3
V
V V
t----=
-
7/29/2019 WL373e-V0.3
15/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
5 Experiments 11
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
5.1.3 Evaluating the Experiment: Calibration Curve
If the slot is viewed as a wall, then the Fourier for-
mula can be applied.
With an average slot diameter of dm= 39,6mm
and an effective slot length of l= 126mm, the
heat exchanger surface area A is
(5.2)
The slot width is = 0,4mm.
With the aid of equation Formula (4.1), Page 8 the
heat loss can be determined and the calibration
curve drawn (refer to Fig. 5.2, Page 13):
The coefficient of thermal conduction of air is tem-
perature dependant and is found to be
Calibration values are marked with .
(5.3)
where
T- Mean air temperature in C
(5.4)
T1 Temperature heater
T2 Temperature cooling water
A 0,0396m 0,126m 0,0157m2
= =
0,0242 1 0,003 T+=
TT1 T2+
2
-------------------=
-
7/29/2019 WL373e-V0.3
16/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
5 Experiments 12
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
For the actual heat flow transferred the equationis:
(5.5)
where
Temperature difference
(5.6)
The heat flow loss can be calculated:
(5.7)
Q
A
A T
-------------------------=
T T1 T2=
Q
B P Q
A=
P
in W
T1in C
T2in C
T
inCAir
in W/Km
B
in W
100 90,9 24,4 66,5 0,0284 74,09
90 84,4 23,9 60,5 0,0281 66,8
80 76,1 23,2 52,9 0,0278 57,73
70 69,7 22,8 46,9 0,0276 50,73
60 55,7 21,8 33,9 0,0270 35,94
50 47,5 21,1 26,4 0,0267 27,66
40 40,4 20,4 20,0 0,0264 20,73
30 33,8 19,8 14,0 0,0261 14,37
20 28,2 19,7 8,5 0,0259 8,65
10 22,6 19,3 3,3 0,0257 3,33
0 19,5 19,1 0,4 0,0256 0,40
Tab. 5.1 Calibrating the heat exchanger
Q
-
7/29/2019 WL373e-V0.3
17/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
5 Experiments 13
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
The values measured in this experiment are to be
used only for this special unit.
Every unit has its own calibration values.
Fig. 5.2 Calibration curve
0
10
20
30
40
50
60
70
0 10 20 30 40 50 60 70
Tin C
Bin WQ
-
7/29/2019 WL373e-V0.3
18/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
5 Experiments 14
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
5.2 Determination of Coefficients of Thermal Conduction
The experimental sequence is the same as for the
experiment to record the calibration curve, how-
ever water or oil is now used as the medium to be
investigated.
5.2.1 Preparing for the Experiment
It is very important that the measurement slot is
perfectly clean since even small quantities ofimpurities can seriously affect the results. The
measurement slot must therefore be well
cleansed (refer to Fig. 3.3, Page 6)
Connect the heat exchanger to the measure-
ment and control unit in accordance with
Fig. 3.1, Page 4 and Fig. 3.5, Page 7 and
switch on the unit
Make the cooling water connections and set
the flow rate for example to 1ltr/min at shut offvalve (3) (refer to Formula (5.1), Page 10)
Open the shut off valves (1) and (2) for the
measurement slot
Inject the medium to be investigated for exam-
ple with a syringe into socket A until the
medium runs out of socket B and until no air
bubbles to be seen inside transparent connec-
tion hoses
Close the shut off valves (1) and (2)
Lift up the heat exchanger and rotate it to
remove possible air bubbles out of heat
exchanger into transparent connection hoses,
if necessary bleed the system again by open-
ing the shut off valves (1, 2) and refill the sys-
tem with the medium to be investigated
Fig. 5.3 Shut off valves und sockets
V
1
2
3
A B
-
7/29/2019 WL373e-V0.3
19/26
-
7/29/2019 WL373e-V0.3
20/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
5 Experiments 16
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
The cause of the variations is predominantly small
remnants of air and other measured media in themeasurement slot.
P
in WT1
in CT2
in CT
in CB
in WA
in WAir
in W/KmLiterature
in W/KmVar.in %
100 45,8 24,5 21,3 22,78 77,22 0,092 0,13 29
70 38,4 24,0 14,4 15,04 54,96 0,097 0,13 25
Tab. 5.3 Example measurement results when using oil as the measured medium
Q
Q
-
7/29/2019 WL373e-V0.3
21/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
6 Appendix 17
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
6 Appendix
6.1 Working Sheet:
Calibration Curve/ Coefficient of Thermal Conduction
ExperimentNo.:
Date:
Medium: Flow rate cooling water in ltr/min:
Remarks:
P
in WT1
in CT2
in CT
in CB
in WA
in WMedium
in W/KmLiterature
in W/Km
Experiment
No.:
Date:
Medium: Flow rate cooling water in ltr/min:
Remarks:
P
in WT1
in CT2
in CT
in CB
in WA
in WMedium
in W/KmLiterature
in W/Km
Q
Q
Q
Q
-
7/29/2019 WL373e-V0.3
22/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
6 Appendix 18
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
Fig. 6.1 Calibration curve
0
10
20
30
40
50
60
70
0 10 20 30 40 50 60 70
Bin WQ
T in C
-
7/29/2019 WL373e-V0.3
23/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
6 Appendix 19
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
6.2 Symbols and Units
A Heat transfer surface area m2
dm Mean effective diameterof the heat exchanger mm
P Heater power consumption W
Q Heat transferred W
Heat transfer flow rate W/s
B
Heat flow loss W/s
A Actual heat flow transferred W/s
T Mean air temperature C
T2 Temperature cooling water C
T1 Temperature Heater C
T Temperature difference betweenheat source and heat sink C
Flow rate ltr/min
Slot width mm
Coefficient of thermal
conduction W/Km
Q
Q
Q
V
-
7/29/2019 WL373e-V0.3
24/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
6 Appendix 20
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
6.3 Table with Coefficients of Thermal Conduction
Substance Temperature in C in
Water 0 0,555
Water 20 0,598
Water 60 0,651
Water 100 0,681
Oil 40 0,123
Oil 80 0,120
Tab. 6.1 Coefficients of Thermal Conduction for Some Liquids
W
Km----------
Substance Temperature in C in
Air T 0,0242(1+0,003T)
Carbon dioxide CO2 0 0,0178
Oxygen O2 20 0,026
Steam 100 0,0242
Steam 200 0,0328
Steam 400 0,0551
Tab. 6.2 Coefficients of Thermal Conduction for Some Gases
W
Km----------
-
7/29/2019 WL373e-V0.3
25/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
6 Appendix 21
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
6.4 Technical Data
Dimensions:
Base plate:
(L x W x H) 250 x 400 x 150 mm
Measurement amplifier:
(W x H x D) 350 x 130 x 250 mm
Power Supply: 230VAC 50 Hz
Alternatives optional, see type plate
Weight: approx. 8 kg
Heat exchanger:
Effec. transfer area 0,0157 m2
Mean Effec. Diameter 39,6 mm
Slot width 0,4 mm
Heater
Max. Power Consumption 160 W
Thermocouples 2 x Type K
Measurement and control unit
Shut down of the heater supply T=95 C
-
7/29/2019 WL373e-V0.3
26/26
02/2012
WL 373 HEAT CONDUCTION IN GASES AND LIQUIDS
22
Allrig
htsreserve
d,
G.U.N.T.
Ger
tebau,
Bars
btte
l,Germany
02/2012
6.5 Index
C
Calibration curve . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11Coefficient of thermal conduction . . . . . . . . . . . . . . . . . . . . . . . 1, 8, 9, 20Convection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8Cooling water . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5
F
Fourier law . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
H
Heat sink . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5Heat source . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5Heater power . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6
I
Impurities . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14
M
Measurement and control unit . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6
P
Plane wall . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8Power consumption, heater . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6
R
Rapid action hose coupling . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7
SSymbols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19
T
Technical data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 21Thermal conduction in a plane wall . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8Thermocouple . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5Topics . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1