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Sheet 1 and Solution

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Higher Future Institute of Engineering and Technology
Second year mechanical engineering
Sheet 1
INTRODUCTION AND BASIC CONCEPTS
1– Air enters a 12-m-long, 7-cm-diameter pipe at 50°C at a rate of 0.06 kg/s. The
air is cooled at an average rate of 400 W per m2 surface area of the pipe. The air
temperature at the exit of the pipe is:
(a) 4.3°C (b) 17.5°C (c) 32.5°C
(d) 43.4°C
(e) 45.8°C
Answer (c) 32.5ºC
Solution:
From air table at
Tf = =
T1 +T1
2
≈ 60o C get: Air cp = 1007 J/kg. K
L = 12 m , D = 0.07 m, T1 = 50o C , ṁair = 0.06 kg/s
q′′ = 400 W/ m2
As = π. D. L
Since: Q = q′′ . As = mΜ‡air . cp. (T1 − T2 )
q′′ =
Q
mΜ‡air . cp. (T1 − T2 )
=
As
As
400 =
Q
0.06 x 1007 (50 − T2 )
=
As
π x 0.07 x 12
T2 = 32.5o C
1
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
2
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
2– Heat is lost steadily through a 0.5-cm thick 2 m x 3 m window glass whose
thermal conductivity is 0.7 W/m.K. The inner and outer surface temperatures of the
glass are measured to be 12°C to 9°C. The rate of heat loss by conduction through
the glass is:
(a) 420 W
(b) 5040 W
(c) 17,600 W
(d) 1256 W
(e) 2520 W
Answer (e) 2520 W
Solution: 0.5 cm
𝐴 = 3π‘₯2 = 6 π‘š2, βˆ†x = L = 0.005 m, T1 = 12o C , T2 = 9o C , π‘˜ = 0.7 π‘Š/π‘š. 𝐾
Since:
𝑄 = π‘˜. 𝐴.
(T1 −T2 )
βˆ†x
= 0.7 π‘₯ 6
(12−9)
0.005
= 2520 π‘Š
3
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
3– Steady heat conduction occurs through a 0.3-m-thick 9 m x 3 m composite wall
at a rate of 1.2 kW. If the inner and outer surface temperatures of the wall are 15°C
and 7°C, the effective thermal conductivity of the wall is:
(a) 0.61 W/m.K (b) 0.83 W/m.K (c) 1.7 W/m.K (d) 2.2 W/m.K (e) 5.1 W/m.K
Answer (c) 1.7 W/m⋅°C
Solution:
𝐴 = 9π‘₯3 = 27 π‘š2, βˆ†x = L = 0.3 m, T1 = 15o C , T2 = 7o C , 𝑄 = 1200 π‘Š
π‘˜ = 0.7 π‘Š/π‘š. 𝐾
Since:
𝑄 = π‘˜. 𝐴.
(T1 −T2 )
βˆ†x
= π‘˜ π‘₯ 27
(15−7)
0.3
= 1200 π‘Š
π‘˜ = 1.7 π‘Š/π‘š. 𝐾
4– Heat is lost through a brick wall (k = 0.72 W/m.K), which is 4 m long, 3 m
wide, and 25 cm thick at a rate of 500 W. If the inner surface of the wall is at 22°C,
the temperature at the midplane of the wall is:
(a) 0°C
(b) 7.5°C (c) 11.0°C (d) 14.8°C (e) 22°C
Answer (d) 14.8ºC
Solution :
𝐴 = 3π‘₯4 = 12 π‘š2, βˆ†x = L = 0.25 m, Ti = 22o C,
Tc = ? ,
To =? ,
𝑄 = 500 π‘Š , π‘˜ = 0.72 π‘Š/π‘š. 𝐾
Since:
𝑄 = π‘˜. 𝐴.
(Ti −To )
βˆ†x
= π‘˜. 𝐴.
(Ti −Tc )
βˆ†x
2
( )
4
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
500 = 0.72 π‘₯ 12
(22 − To )
(22 − Tc )
= 0.72 π‘₯ 12
0.25
0.25
)
(
2
To = 7.4o C
Tc = 14.8o C
5– A 10-cm-high and 20-cm-wide circuit board houses on its surface 100 closely
spaced chips, each generating heat at a rate of 0.12 W and transferring it by
convection and radiation to the surrounding medium at 40°C. Heat transfer from
the back surface of the board is negligible. If the combined convection and
radiation heat transfer coefficient on the surface of the board is 22 W/m2.K, the
average surface temperature of the chips is:
(a) 41°C
(b) 54°C
(c) 67°C
(d) 76°C
(e) 82°C
Solution:
As = 0.1 x 0.2 = 0.02 π‘š2 , β„Ž = 22 π‘Š/π‘š 2 . 𝐾
Air, 𝑇∞ = 40π‘œ 𝐢
𝑄 = 100 π‘₯ 0.12 = 12 π‘Š
𝑄 = β„Ž. As . (𝑇𝑠 − 𝑇∞ )
𝑇𝑠 = 𝑇∞ +
𝑄
12
= 40 +
= 67.2π‘œ 𝐢
β„Ž. As
22 π‘₯ 0.02
5
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6– While driving down a highway early in the evening, the air flow over an
automobile establishes an overall heat transfer coefficient of 18 W/m2.K. The
passenger cabin of this automobile exposes 9 m2 of surface to the moving ambient
air. On a day when the ambient temperature is 33°C, how much cooling must the
air conditioning system supply to maintain a temperature of 20°C in the passenger
cabin?
(a) 670 W
(b) 1284 W (c) 2106 W
(d) 2565 W
Answer (c) 2.6 MW
Solution :
As = 9 π‘š 2 , β„Ž = 18 π‘Š/π‘š 2 . 𝐾
Air, 𝑇∞ = 33π‘œ 𝐢
𝑇𝑠 = 20π‘œ 𝐢
𝑄 = β„Ž. As . (𝑇𝑠 − 𝑇∞ ) = 18 π‘₯ 9 π‘₯(33 − 20) = 2106 π‘Š
6
(e) 3210 W
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
7– A 25-cm-diameter black ball at 130°C is suspended in air, and is losing heat to
the surrounding air at 25°C by convection with a heat transfer coefficient of 12
W/m2.K, and by radiation to the surrounding surfaces at 15°C. The total rate of
heat transfer from the black ball is:
(a) 217 W
(b) 247 W
(c) 251 W
(d) 465 W (e) 2365 W
Solution:
Black Ball: πœ€ = 1
𝐷 = 0.25 π‘š
As = 4π. 𝑅2 = π. 𝑑 2 = π. (0.25)2 = 0.1963 π‘š 2
Air, 𝑇∞ = 25π‘œ 𝐢 = 25 + 273 = 298 𝐾
β„Ž = 12 π‘Š/π‘š 2 . 𝐾
𝑇𝑠 = 130π‘œ 𝐢 = 130 + 273 = 403 𝐾
π‘‡π‘ π‘’π‘Ÿ = 15π‘œ 𝐢 = 15 + 273 = 288 𝐾
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = π‘„π‘π‘œπ‘›π‘£ + π‘„π‘…π‘Žπ‘‘
π‘„π‘π‘œπ‘›π‘£ = β„Ž. As . (𝑇𝑠 − 𝑇∞ ) = 12 π‘₯ π. (0.25)2 π‘₯(130 − 25) = 247.4 π‘Š
4 ]
π‘„π‘…π‘Žπ‘‘ = πœ€. 𝜎. As . [ 𝑇𝑠4 − π‘‡π‘ π‘’π‘Ÿ
π‘„π‘…π‘Žπ‘‘ = 1 π‘₯ 5.67π‘₯10−8 π‘₯ π. (0.25)2 π‘₯ [ (403)4 − (288)4 ] = 217 π‘Š
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = 247.4 + 217 = 464.4 π‘Š
7
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8– A 3-m2 black surface at 140°C is losing heat to the surrounding air at 35°C by
convection with a heat transfer coefficient of 16 W/m 2.K, and by radiation to the
surrounding surfaces at 15°C. The total rate of heat loss from the surface is:
(a) 5105 W
(b) 2940 W
(c) 3779 W
(d) 8819 W
(e) 5040 W
Black Ball: πœ€ = 1
A s = 3 π‘š2
Air, 𝑇∞ = 35π‘œ 𝐢 = 35 + 273 = 308 𝐾
β„Ž = 16 π‘Š/π‘š 2 . 𝐾
𝑇𝑠 = 140π‘œ 𝐢 = 140 + 273 = 413 𝐾
π‘‡π‘ π‘’π‘Ÿ = 15π‘œ 𝐢 = 15 + 273 = 288 𝐾
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = π‘„π‘π‘œπ‘›π‘£ + π‘„π‘…π‘Žπ‘‘
π‘„π‘π‘œπ‘›π‘£ = β„Ž. As . (𝑇𝑠 − 𝑇∞ ) = 16 π‘₯ 3 π‘₯(413 − 308) = 5040 π‘Š
4 ]
π‘„π‘…π‘Žπ‘‘ = πœ€. 𝜎. As . [ 𝑇𝑠4 − π‘‡π‘ π‘’π‘Ÿ
π‘„π‘…π‘Žπ‘‘ = 1 π‘₯ 5.67π‘₯10−8 π‘₯ 3 π‘₯ [ (413)4 − (288)4 ] = 3778 π‘Š
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = 5040 + 3778 = 8818 π‘Š
8
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9– A person’s head can be approximated as a 25-cm diameter sphere at 35°C with
an emissivity of 0.95. Heat is lost from the head to the surrounding air at 25°C by
convection with a heat transfer coefficient of 11 W/m2.K, and by radiation to the
surrounding surfaces at 10°C. Disregarding the neck, determine the total rate of
heat loss from the head.
(a) 22 W
(b) 27 W
(c) 49 W
(d) 172 W (e) 249 W
Solution:
sphere: πœ€ = 0.95
𝐷 = 0.25 π‘š
As = 4π. 𝑅2 = π. 𝑑 2 = π. (0.25)2 = 0.1963 π‘š 2
Air, 𝑇∞ = 25π‘œ 𝐢 = 25 + 273 = 298 𝐾
β„Ž = 11 π‘Š/π‘š 2. 𝐾
𝑇𝑠 = 35π‘œ 𝐢 = 35 + 273 = 308 𝐾
π‘‡π‘ π‘’π‘Ÿ = 10π‘œ 𝐢 = 10 + 273 = 283 𝐾
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = π‘„π‘π‘œπ‘›π‘£ + π‘„π‘…π‘Žπ‘‘
π‘„π‘π‘œπ‘›π‘£ = β„Ž. As . (𝑇𝑠 − 𝑇∞ ) = 11 π‘₯ π. (0.25)2 π‘₯(308 − 298) = 21.6 π‘Š
4 ]
π‘„π‘…π‘Žπ‘‘ = πœ€. 𝜎. 𝐴𝑠 . [ 𝑇𝑠4 − π‘‡π‘ π‘’π‘Ÿ
π‘„π‘…π‘Žπ‘‘ = 0.95 π‘₯ 5.67π‘₯10−8 π‘₯ π. (0.25)2 π‘₯ [ (308)4 − (283)4 ] = 28.77 π‘Š
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = 21.6 + 27.4 = 49 π‘Š
9
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Second year mechanical engineering
10– A room is heated by a 1.2 kW electric resistance heater whose wires have a
diameter of 4 mm and a total length of 3.4 m. The air in the room is at 23°C and
the interior surfaces of the room are at 17°C. The convection heat transfer
coefficient on the surface of the wires is 8 W/m2.K. If the rates of heat transfer
from the wires to the room by convection and by radiation are equal, the surface
temperature of the wire is:
(a) 3534°C
(b) 1778°C
(c) 1772°C
(d) 98°C
(e) 25°C
Answer (b) 1778ºC
Solution:
Cylinder:
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = 1.2 π‘˜π‘Š = 1200 π‘Š
𝐷 = 0.004 π‘š
𝐿 = 3.4 π‘š
As = π. d. L = π x 0.004 x 3.4 = 0.0427 π‘š 2
Air, 𝑇∞ = 23π‘œ 𝐢
β„Ž = 8 π‘Š/π‘š 2 . 𝐾
𝑇𝑠 = ? ? 𝐾
π‘‡π‘ π‘’π‘Ÿ = 17π‘œ 𝐢
𝑆𝑖𝑛𝑐𝑒: π‘„π‘π‘œπ‘›π‘£ = π‘„π‘…π‘Žπ‘‘
π‘Žπ‘›π‘‘: π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = π‘„π‘π‘œπ‘›π‘£ + π‘„π‘…π‘Žπ‘‘ = 1200 π‘Š
π‘„π‘π‘œπ‘›π‘£ = 1200/2 = 600 π‘Š
π‘„π‘π‘œπ‘›π‘£ = β„Ž. As . (𝑇𝑠 − 𝑇∞ ) = 8 π‘₯ π x 0.004 x 3.4 π‘₯(𝑇𝑠 − 23) = 600 π‘Š
𝑇𝑠 = 1778π‘œ 𝐢
10
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
11– A person standing in a room loses heat to the air in the room by convection
and to the surrounding surfaces by radiation. Both the air in the room and the
surrounding surfaces are at 20°C. The exposed surface of the person is 1.5 m2 and
has an average temperature of 32°C, and an emissivity of 0.90. If the rates of heat
transfer from the person by convection and by radiation are equal, the combined
heat transfer coefficient is:
(a) 0.008W/m2.K (b) 3.0W/m2.K (c) 5.5W/m2.K (d) 8.3 W/m2.K (e) 10.9 W/m2.K
Solution:
Find the combined heat transfer coefficient is β„Žπ‘π‘œπ‘šπ‘ :
π‘„π‘π‘œπ‘›π‘£ = π‘„π‘…π‘Žπ‘‘
πœ€ = 0.90
As = 1.5 π‘š 2
Air, 𝑇∞ = 20π‘œ 𝐢 = 20 + 273 = 293 𝐾
β„Žπ‘π‘œπ‘›π‘£ = ? ? π‘Š/π‘š 2 . 𝐾
𝑇𝑠 = 32π‘œ 𝐢 = 32 + 273 = 305 𝐾
π‘‡π‘ π‘’π‘Ÿ = 20π‘œ 𝐢 = 20 + 273 = 293 𝐾
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = π‘„π‘π‘œπ‘›π‘£ + π‘„π‘…π‘Žπ‘‘
π‘„π‘π‘œπ‘›π‘£ = β„Žπ‘π‘œπ‘›π‘£ . As . (𝑇𝑠 − 𝑇∞ ) = β„Žπ‘π‘œπ‘›π‘£ π‘₯ 1.5 π‘₯(32 − 20)
4 ]
π‘„π‘…π‘Žπ‘‘ = πœ€. 𝜎. 𝐴𝑠 . [ 𝑇𝑠4 − π‘‡π‘ π‘’π‘Ÿ
π‘„π‘…π‘Žπ‘‘ = 0.90 π‘₯ 5.67π‘₯10−8 π‘₯ 1.5π‘₯ [ (305)4 − (293)4 ] = 98.25 π‘Š
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = 2 π‘₯ 98.25 = 196.5 π‘Š = β„Žπ‘π‘œπ‘šπ‘ . As . (𝑇𝑠 − 𝑇∞ ) = β„Žπ‘π‘œπ‘šπ‘ π‘₯1.5π‘₯(32 − 20)
β„Žπ‘π‘œπ‘šπ‘ = 10.91 π‘Š/π‘š 2 . 𝐾
11
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Second year mechanical engineering
12– The inner and outer surfaces of a 4-m x 7-m brick wall of
thickness 30 cm and thermal conductivity 0.69 W/m.K are
maintained at temperatures of 26°C and 8°C, respectively.
Determine the rate of heat transfer through the wall, in W.
Solution :
𝐴 = 4π‘₯7 = 28 π‘š2, βˆ†x = L = 0.30 m, Ti = 26o C, To = 8o C ,
𝑄 = ? ? π‘Š , π‘˜ = 0.69 π‘Š/π‘š. 𝐾
Since:
𝑄 = π‘˜. 𝐴.
(Ti −To )
βˆ†x
= 0.69 π‘₯ 28
(26−8)
0.30
𝑄 = 1159 π‘Š
12
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
13– In a power plant, pipes transporting superheated vapor are very common.
Superheated vapor is flowing at a rate of 0.3 kg/s inside a pipe with 5 cm in
diameter and 10 m in length. The pipe is located in
a power plant at 20°C, and has a uniform pipe
surface temperature of 100°C. If the temperature
drop between the inlet and exit of the pipe is 30°C,
and the specific heat of the vapor is 2190 J/kg.K,
Determine:
1-Tthe heat transfer coefficient of convection between the pipe surface and the
surrounding.
Steam: π‘šΜ‡π‘ π‘‘ = 0.3 π‘˜π‘”/𝑠
𝑐𝑃𝑠𝑑 = 2190 𝐽/π‘˜π‘”. 𝐾
βˆ†π‘‡π‘ π‘‘ = 30π‘œ 𝐢
𝐷 = 0.05 π‘š
𝐿 = 10 π‘š
As = π. d. L = π x 0.05 x 10 = 1.57 π‘š2
Air, 𝑇∞ = 20π‘œ 𝐢
β„Žπ‘π‘œπ‘›π‘£ = ? ? π‘Š/π‘š 2 . 𝐾
𝑇𝑠 = 100π‘œ 𝐢
π‘„πΏπ‘œπ‘ π‘  = π‘šΜ‡π‘ π‘‘ . 𝑐𝑃𝑠𝑑 . βˆ†π‘‡π‘ π‘‘ = β„Žπ‘π‘œπ‘›π‘£ . As . (𝑇𝑠 − 𝑇∞ )
π‘„πΏπ‘œπ‘ π‘  = 0.3 π‘₯ 2190 π‘₯ 30 = β„Žπ‘π‘œπ‘›π‘£ π‘₯ 1.57π‘₯(100 − 20) = 19710 π‘Š
β„Žπ‘π‘œπ‘›π‘£ =
19710
1.57π‘₯(100−20)
= 157 π‘Š/π‘š 2. 𝐾
13
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Second year mechanical engineering
14– A transistors with a height of 0.4 cm and a diameter of 0.6 cm
is mounted on a circuit board. The transistor is cooled by air
flowing over it with an average heat transfer coefficient of 30
W/m2.K. If the air temperature is 55°C and the transistor case
temperature is not to exceed 70°C.
Determine:
1-The amount of power this transistor can dissipate safely.
Disregard any heat transfer from the transistor base.
Solution:
𝐷 = 0.6 π‘π‘š = 0.006 π‘š
𝐿 = 0.4 π‘π‘š = 0.004 π‘š
As = π. D. L = π x 0.006 x 0.004 = 7.54π‘₯10−5 π‘š2
Air, 𝑇∞ = 55π‘œ 𝐢
β„Žπ‘π‘œπ‘›π‘£ = 30 π‘Š/π‘š 2 . 𝐾
𝑇𝑠 = 70π‘œ 𝐢
π‘„π‘π‘œπ‘›π‘£ = 30 π‘₯ 7.54 π‘₯ 10−5 π‘₯(70 − 55) = 0.04 π‘Š
14
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15– Consider a person whose exposed surface area is 1.7 m2, emissivity is 0.5, and
surface temperature is 32°C.
Determine The rate of heat loss from that person by radiation in a large room
having walls at a temperature of (a) 300 K and (b) 280 K.
Answers: (a) 26.7 W, (b) 121 W
πœ€ = 0.5
As = 1.7 π‘š2
𝑇𝑠 = 32π‘œ 𝐢 = 32 + 273 = 305 𝐾
𝑇𝑠 = 305 𝐾
π‘‡π‘ π‘’π‘Ÿ = 300 𝐾
4 ]
π‘„π‘…π‘Žπ‘‘ = πœ€. 𝜎. 𝐴𝑠 . [ 𝑇𝑠4 − π‘‡π‘ π‘’π‘Ÿ
π‘„π‘…π‘Žπ‘‘−1 = 0.5 π‘₯ 5.67π‘₯10−8 π‘₯ 1.7π‘₯ [ (305)4 − (300)4] = 26.8 π‘Š
π‘„π‘…π‘Žπ‘‘−2 = 0.5 π‘₯ 5.67π‘₯10−8 π‘₯ 1.7π‘₯ [ (305)4 − (280)4] = 120.8 π‘Š
15
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16– A solid plate, with a thickness of 15 cm and a thermal conductivity of 80
W/m.K, is being cooled at the upper surface by
air. The air temperature is 10°C, while the
temperatures at the upper and lower surfaces of
the plate are 50 and 60°C, respectively.
Determine:
1-The convection heat transfer coefficient of air at the upper surface.
Solution:
Plate: βˆ†x = L = 0.15 m, Ts2 = 60o C, Ts1 = 50o C,
Air: 𝑇∞ = 10π‘œ 𝐢
β„Žπ‘π‘œπ‘›π‘£ = ? ? π‘Š/π‘š 2 . 𝐾
Since:
𝑄 = π‘˜. 𝐴.
(Ts2 −Ts1 )
π‘ž′′ = 80 π‘₯
βˆ†x
= β„Žπ‘π‘œπ‘›π‘£ . As . (𝑇𝑠1 − 𝑇∞ )
(60−50)
0.15
= β„Žπ‘π‘œπ‘›π‘£ π‘₯ (50 − 10)
β„Žπ‘π‘œπ‘›π‘£ = 133.33 π‘Š/π‘š 2 . 𝐾
16
π‘˜ = 80 π‘Š/π‘š. 𝐾
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
17– Air at 20oC with a convection heat transfer
coefficient of 25 W/m2.K blows over a horizontal steel
hot plate (k = 43 W/m.K). The surface area of the plate
is 0.38 m2 with a thickness of 2 cm. The plate surface is
maintained at a constant temperature of 𝑇𝑠 = 250 °C
and the plate loses 300 W from its surface by radiation.
Calculate the inside plate temperature 𝑇𝑖 .
Solution:
Plate: βˆ†x = L = 0.02 m, π‘˜ = 43 π‘Š/π‘š. 𝐾, As = 0.38π‘š2 , Ts = 250o C,
Air: 𝑇∞ = 20π‘œ 𝐢
β„Žπ‘π‘œπ‘›π‘£ = 25 π‘Š/π‘š 2 . 𝐾
π‘„π‘…π‘Žπ‘‘ = 300 π‘Š
Since:
π‘„πΆπ‘œπ‘›π‘‘ = π‘„π‘π‘œπ‘›π‘£ + π‘„π‘…π‘Žπ‘‘
π‘„πΆπ‘œπ‘›π‘‘ = π‘˜. 𝐴.
(Ti − Ts )
= β„Žπ‘π‘œπ‘›π‘£ . As . (𝑇𝑠 − 𝑇∞ ) + π‘„π‘…π‘Žπ‘‘
βˆ†x
𝑄 = 43 π‘₯ 0.38
(Ti −250)
0.02
= 25 π‘₯ 0.38 (250 − 20) + 300
Ti = 253π‘œ 𝐢
17
Higher Future Institute of Engineering and Technology
Second year mechanical engineering
18– Consider a person standing in a room at 20°C. Determine the total rate of heat
transfer from this person if the exposed surface area and the skin temperature of
the person are 1.7 m2 and 32°C, respectively, and the convection heat transfer
coefficient is 5 W/m2.K. Take the emissivity of the skin and the clothes to be 0.9,
and assume the temperature of the inner surfaces of the room to be the same as the
air temperature.
Solution:
πœ€ = 0.90
As = 1.7 π‘š2
Air, 𝑇∞ = 20π‘œ 𝐢 = 20 + 273 = 293 𝐾
β„Žπ‘π‘œπ‘›π‘£ = 5 π‘Š/π‘š 2 . 𝐾
𝑇𝑠 = 32π‘œ 𝐢 = 32 + 273 = 305 𝐾
𝑇𝑠 = 305 𝐾
π‘‡π‘ π‘’π‘Ÿ = 293 𝐾
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = π‘„π‘π‘œπ‘›π‘£ + π‘„π‘…π‘Žπ‘‘
π‘„π‘π‘œπ‘›π‘£ = β„Žπ‘π‘œπ‘›π‘£ . As . (𝑇𝑠 − 𝑇∞ ) = 5 π‘₯ 1.7 π‘₯ (32 − 20) = 102 π‘Š
4 ]
π‘„π‘…π‘Žπ‘‘ = πœ€. 𝜎. 𝐴𝑠 . [ 𝑇𝑠4 − π‘‡π‘ π‘’π‘Ÿ
π‘„π‘…π‘Žπ‘‘ = 0.90 π‘₯ 5.67π‘₯10−8 π‘₯ 1.7π‘₯ [ (305)4 − (293)4 ] = 111 π‘Š
π‘„π‘‘π‘œπ‘‘π‘Žπ‘™ = 102 + 111 = 213 π‘Š
18
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