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Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
[HEAT TRANSFER Laboratory II]
University of Baghdad
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
TABLE OF CONTENTS
MIN..................................................................................I
THEORY............................................................................II
Calculations and results...................................................V
DISCUSSION ...................................................................VI
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
Conduction Heat Transfer
Saif Al-din Ali -A-
1. MIN
Measuring the thermal conductivity K for a cylindrical specimen made from
iron and has certain dimensions and specifications
*Types of Heat Transfer are:
1. Conduction
2. Convection
3. Radiation
2. THEORY
1. The Apparatus used:
Draw a schematic shape for the apparatus demonstrating its parts clearly
2. The Experiment Procedure:
The specimen is heated by using an electrical heater located specimen. As a result.
the temperature of the specimen rises and three different locations on the
specimen surface is indicated to measure their temperature values by using
thermocouple wires attached to a selector and then to a digital thermometer The
heat is transferred from the specimen to the water contained in a reservoir ted and
in order to achieve a heat transfer by construction only the specimen is insula
completely so that neither convection nor nor radiation heat transfer take place.
The reservoir is supplied with water from a continuous source until reaching steady
state at which temperature values for the three points and the inlet and outlet
water temperature is recorded and this happens after approximately two hours.
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
3. Calculations and results
After the heat is transferred from the specimen to the water. The
following heat balance is written:
Heat transfer from specimen = heat added to water
βˆ’π‘˜π΄
𝑑𝑇
𝑑π‘₯
= π‘š`
𝑐 π‘π‘€βˆ†π‘‡
Where:
K Thermal conductivity for specimen (w/m.c`)
A Cross - sectional area (m^2)
𝑑𝑇
𝑑π‘₯
Temperature gradient (c`/m)
m`(w) Water mass flow rate (kg/sec)
p(w) Water density 1000 kg / m^3 (k / sec)
𝑐 𝑝𝑀 = 4.136 Specific heat at constant pressure (Kj/KG.C`)
** The average temperature of the specimen surface temperatures is
calculated which result in calculating three values for the thermal
conductivity k1. K2. K3 and then take the average for these three values,
** When the steady state condition is reached you must make the
following table for the data obtained during this experiment as shown
below:
TIME (min) 𝑇 𝑀𝐼𝑁 𝑇 π‘€π‘‚π‘ˆπ‘‡ 𝑇1 𝑇2 𝑇3
0 24 29 109.8 92 69.3
5 24 29 109.1 91.4 69.2
10 24 29 109.1 91.4 69.2
15 24 29 109.1 91.4 69.2
AV
7.5 24 29 109.25 91.5 69.25
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
Calculations
𝑨 =
𝝅
πŸ’
𝒅 𝟐
𝐴 =
πœ‹
4
(0.024)2
𝐴 = 4.52 Γ— 10βˆ’4
π‘š2
π’Ž^
= 𝝆
𝑽
𝒕
π‘š^
= 1000
29 Γ— 10βˆ’6
300
= 9.66 Γ— 10βˆ’5
π‘˜π‘”/𝑠𝑒𝑐
𝑸 π’˜ = π’Ž` 𝒄 π’‘π’˜βˆ†π‘»
𝑄 𝑀 = 9.66 Γ— 10βˆ’5
βˆ— 4.136 βˆ— 103
βˆ— (29 βˆ’ 24) = 1.997688 𝑀
βˆ†π‘‡
βˆ†π‘₯
= 𝑇1 βˆ’ 𝑇2 βˆ†π‘ΏπŸβ„
1- (1 βˆ’ 2)
βˆ†π‘‡
βˆ†π‘₯
= 109.25 βˆ’ 91.5 32⁄ Γ— 10βˆ’3
= 547.65625 𝑐 π‘šβ„
2- (1 βˆ’ 3)
βˆ†π‘‡
βˆ†π‘₯
= 109.25 βˆ’ 69.25 71⁄ Γ— 10βˆ’3
= 560.21 𝑐 π‘šβ„
2- (2 βˆ’ 3)
βˆ†π‘‡
βˆ†π‘₯
= 91.5 βˆ’ 69.25 39⁄ Γ— 10βˆ’3
= 570.512 𝑐 π‘šβ„
𝐐 𝐰 = 𝐀𝐀
𝐝𝐓
𝐝𝐱
𝐀 =
𝐐 𝐰
𝐀
𝐝𝐓
𝐝𝐱
1-k =
1.997688
4.52Γ—10βˆ’4βˆ—234.15
= 8 𝑀 π‘š. 𝑐`⁄
2-k =
1.997688
4.52Γ—10βˆ’4βˆ—560.21
= 7.88929 𝑀 π‘š. 𝑐`⁄
3-k =
1.997688
4.52Γ—10βˆ’4βˆ—570.512
= 7.746837 𝑀 π‘š. 𝑐`⁄
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
π‘˜ = π‘˜1 + π‘˜2 + π‘˜3 3⁄
π‘˜ = 8 + 7.88929 + 7.746837 3⁄
π‘˜ = 7.878709 𝑀 π‘š. 𝑐`⁄
4. DISCUSSION
1. After calculating the experimental value of (K) for iron compare the
calculated results with the theoretical value of (K) from tables for iron,
then determine the percentage error between the two values and
discuss the reason of the difference between the two values and find the
type of iron used.
Error=|
ktheβˆ’kex
kthe
|*100
1. |
80.2βˆ’7.878
80.2
| βˆ— 100 =91.77%
kthe = 80.2
kex = 7.878
We observe a high line rate and this depends on the process of taking
the readings from the device and the process of continuous calibration
of the device and the time period to take readings and the accuracy of
conversion of the signal type in the thermocouple device
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
2. Find the top surface temperature and bottom surface temperature for
the Specimen algorithmically and find them also from the plot. Then
compare between the two results obtained from the two methods.
𝐐 𝐰 = 𝐀𝐀
𝐝𝐓
𝐝𝐱
1 βˆ’ 1.997688 = 7.89 βˆ— (4.52 Γ— 10βˆ’4
)
𝑇𝑆 βˆ’ 109.025
15 Γ— 10βˆ’3
TS=117.427 C`
2 βˆ’ 1.997688 = 7.89 βˆ— (4.52 Γ— 10βˆ’4
)
117.427 βˆ’ 𝑇𝐡
100 Γ— 10βˆ’3
Tb=61.4057 C`
Note that the inverse relationship between heat and distance from the
heat generating site as we move away from the heat source is less
valuable
0
20
40
60
80
100
120
140
0 0.02 0.04 0.06 0.08 0.1 0.12
Y-TC`
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
3. Can you calculate (K) for two different materials at the same time?
Why?
It can not be calculated because the different materials have different k
and different stability condition can not reach the fixed state of the
metal Mean at the same time and heat.
The device used is specially designed to measure as a unit material,
depending on its shape
4. Define the steady state condition. Was the experiment at this condition
or not
Steady-state
Designating or of a system, operation, mixture, rate, etc. that does not
change with time or that contains a state of relative equilibrium even
after undergoing fluctuations or transformations, Yes it has been
adopted
Department of Mechanical Engineering/ College of Engineering/ University of Baghdad
5. State number of applications for this experiment
1. Burning of wood on coal
2. Melting of iron in blast furnace
3. Fission reactions in nuclear fuel rods of nuclear reactors
4. Cooking of food in metal utensils
6. What are the main results that you have given from this experiment?
1. Calculate the value of K and practically compare it with the
theoretical and knowledge of the metal class through it
2. Calculation of error ratio between theoretical and practical

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Measuring Thermal Conductivity of Cylindrical Iron Specimen

  • 1. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad [HEAT TRANSFER Laboratory II] University of Baghdad
  • 2. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad TABLE OF CONTENTS MIN..................................................................................I THEORY............................................................................II Calculations and results...................................................V DISCUSSION ...................................................................VI
  • 3. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad Conduction Heat Transfer Saif Al-din Ali -A- 1. MIN Measuring the thermal conductivity K for a cylindrical specimen made from iron and has certain dimensions and specifications *Types of Heat Transfer are: 1. Conduction 2. Convection 3. Radiation 2. THEORY 1. The Apparatus used: Draw a schematic shape for the apparatus demonstrating its parts clearly 2. The Experiment Procedure: The specimen is heated by using an electrical heater located specimen. As a result. the temperature of the specimen rises and three different locations on the specimen surface is indicated to measure their temperature values by using thermocouple wires attached to a selector and then to a digital thermometer The heat is transferred from the specimen to the water contained in a reservoir ted and in order to achieve a heat transfer by construction only the specimen is insula completely so that neither convection nor nor radiation heat transfer take place. The reservoir is supplied with water from a continuous source until reaching steady state at which temperature values for the three points and the inlet and outlet water temperature is recorded and this happens after approximately two hours.
  • 4. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad 3. Calculations and results After the heat is transferred from the specimen to the water. The following heat balance is written: Heat transfer from specimen = heat added to water βˆ’π‘˜π΄ 𝑑𝑇 𝑑π‘₯ = π‘š` 𝑐 π‘π‘€βˆ†π‘‡ Where: K Thermal conductivity for specimen (w/m.c`) A Cross - sectional area (m^2) 𝑑𝑇 𝑑π‘₯ Temperature gradient (c`/m) m`(w) Water mass flow rate (kg/sec) p(w) Water density 1000 kg / m^3 (k / sec) 𝑐 𝑝𝑀 = 4.136 Specific heat at constant pressure (Kj/KG.C`) ** The average temperature of the specimen surface temperatures is calculated which result in calculating three values for the thermal conductivity k1. K2. K3 and then take the average for these three values, ** When the steady state condition is reached you must make the following table for the data obtained during this experiment as shown below: TIME (min) 𝑇 𝑀𝐼𝑁 𝑇 π‘€π‘‚π‘ˆπ‘‡ 𝑇1 𝑇2 𝑇3 0 24 29 109.8 92 69.3 5 24 29 109.1 91.4 69.2 10 24 29 109.1 91.4 69.2 15 24 29 109.1 91.4 69.2 AV 7.5 24 29 109.25 91.5 69.25
  • 5. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad Calculations 𝑨 = 𝝅 πŸ’ 𝒅 𝟐 𝐴 = πœ‹ 4 (0.024)2 𝐴 = 4.52 Γ— 10βˆ’4 π‘š2 π’Ž^ = 𝝆 𝑽 𝒕 π‘š^ = 1000 29 Γ— 10βˆ’6 300 = 9.66 Γ— 10βˆ’5 π‘˜π‘”/𝑠𝑒𝑐 𝑸 π’˜ = π’Ž` 𝒄 π’‘π’˜βˆ†π‘» 𝑄 𝑀 = 9.66 Γ— 10βˆ’5 βˆ— 4.136 βˆ— 103 βˆ— (29 βˆ’ 24) = 1.997688 𝑀 βˆ†π‘‡ βˆ†π‘₯ = 𝑇1 βˆ’ 𝑇2 βˆ†π‘ΏπŸβ„ 1- (1 βˆ’ 2) βˆ†π‘‡ βˆ†π‘₯ = 109.25 βˆ’ 91.5 32⁄ Γ— 10βˆ’3 = 547.65625 𝑐 π‘šβ„ 2- (1 βˆ’ 3) βˆ†π‘‡ βˆ†π‘₯ = 109.25 βˆ’ 69.25 71⁄ Γ— 10βˆ’3 = 560.21 𝑐 π‘šβ„ 2- (2 βˆ’ 3) βˆ†π‘‡ βˆ†π‘₯ = 91.5 βˆ’ 69.25 39⁄ Γ— 10βˆ’3 = 570.512 𝑐 π‘šβ„ 𝐐 𝐰 = 𝐀𝐀 𝐝𝐓 𝐝𝐱 𝐀 = 𝐐 𝐰 𝐀 𝐝𝐓 𝐝𝐱 1-k = 1.997688 4.52Γ—10βˆ’4βˆ—234.15 = 8 𝑀 π‘š. 𝑐`⁄ 2-k = 1.997688 4.52Γ—10βˆ’4βˆ—560.21 = 7.88929 𝑀 π‘š. 𝑐`⁄ 3-k = 1.997688 4.52Γ—10βˆ’4βˆ—570.512 = 7.746837 𝑀 π‘š. 𝑐`⁄
  • 6. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad π‘˜ = π‘˜1 + π‘˜2 + π‘˜3 3⁄ π‘˜ = 8 + 7.88929 + 7.746837 3⁄ π‘˜ = 7.878709 𝑀 π‘š. 𝑐`⁄ 4. DISCUSSION 1. After calculating the experimental value of (K) for iron compare the calculated results with the theoretical value of (K) from tables for iron, then determine the percentage error between the two values and discuss the reason of the difference between the two values and find the type of iron used. Error=| ktheβˆ’kex kthe |*100 1. | 80.2βˆ’7.878 80.2 | βˆ— 100 =91.77% kthe = 80.2 kex = 7.878 We observe a high line rate and this depends on the process of taking the readings from the device and the process of continuous calibration of the device and the time period to take readings and the accuracy of conversion of the signal type in the thermocouple device
  • 7. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad 2. Find the top surface temperature and bottom surface temperature for the Specimen algorithmically and find them also from the plot. Then compare between the two results obtained from the two methods. 𝐐 𝐰 = 𝐀𝐀 𝐝𝐓 𝐝𝐱 1 βˆ’ 1.997688 = 7.89 βˆ— (4.52 Γ— 10βˆ’4 ) 𝑇𝑆 βˆ’ 109.025 15 Γ— 10βˆ’3 TS=117.427 C` 2 βˆ’ 1.997688 = 7.89 βˆ— (4.52 Γ— 10βˆ’4 ) 117.427 βˆ’ 𝑇𝐡 100 Γ— 10βˆ’3 Tb=61.4057 C` Note that the inverse relationship between heat and distance from the heat generating site as we move away from the heat source is less valuable 0 20 40 60 80 100 120 140 0 0.02 0.04 0.06 0.08 0.1 0.12 Y-TC`
  • 8. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad 3. Can you calculate (K) for two different materials at the same time? Why? It can not be calculated because the different materials have different k and different stability condition can not reach the fixed state of the metal Mean at the same time and heat. The device used is specially designed to measure as a unit material, depending on its shape 4. Define the steady state condition. Was the experiment at this condition or not Steady-state Designating or of a system, operation, mixture, rate, etc. that does not change with time or that contains a state of relative equilibrium even after undergoing fluctuations or transformations, Yes it has been adopted
  • 9. Department of Mechanical Engineering/ College of Engineering/ University of Baghdad 5. State number of applications for this experiment 1. Burning of wood on coal 2. Melting of iron in blast furnace 3. Fission reactions in nuclear fuel rods of nuclear reactors 4. Cooking of food in metal utensils 6. What are the main results that you have given from this experiment? 1. Calculate the value of K and practically compare it with the theoretical and knowledge of the metal class through it 2. Calculation of error ratio between theoretical and practical