1 . حطس یامد اب هایس مسج کی ار دیشروخ 10400
نودا م ی شبات یژرنا خرن .دیریگب رظن رد
Rجوم لوط هزاب رد ار حطس زا هدش لیسگ زمرق λ=0.76−100 μm
.دیروآ تسدب
Analysis T = 10400 R = 5778 K, the blackbody radiation functions corresponding to are determined from Table 11-2 to be
λ
1T =( 0.76 μm )( 5778 K ) =4391.3 μ mK ⃗ f
λ1
= 0.547370 λ
2T =( 100 μm )( 5778 K ) =577,800 μ mK ⃗ f
λ2
= 1.0
Then the fraction of radiation emitted between these two wavelengths becomes fλ
2−fλ
1=1.0−0 .547=0 . 453
(or 45.3%)
The total blackbody emissive power of the sun is determined from Stefan-Boltzman Law to be Eb=σT4=(0.1714×10−8 Btu/h .ft2.R4)(10,400 R)4=2.005×107 Btu/h .ft2
Then,
Einfrared=(0. 451)Eb=(0. 453)(2.005×107 Btu/h .ft2)=9.08×106 Btu/h.ft2
2 . جو م لو ط رد ی شبات یژر نا رثکاد ح ه ک تسا یتروص هب پملا کی یحارط λ=0.47 μm
جو م لو ط هزاب رد ار هدش عطاس یشبات یژنا تبسن و پملا نیا یامد .دوش یم عطاس یئرم λ=0.40−0.76 μm .دیروآ تسدب
Radiation emitted by a light source is maximum in the blue range. The temperature of this light source and the fraction of radiation it emits in the visible range are to be determined.
Assumptions The light source behaves as a black body.
Analysis The temperature of this light source is
( λT )
max power=2897 .8 μm ⋅K ⃗ T = 2897 .8 μm ⋅ K
0. 47 μm =6166 K
The visible range of the electromagnetic spectrum extends fromλ1=0. 40μm to λ2=0.76μm . Noting that
=6166 K, the blackbody radiation functions corresponding to are determined from Table 11-2 to be
λ
1T =( 0. 40 μm )( 6166 K ) =2466 μ mK ⃗ f
λ1
= 0.15444 λ
2T =( 0.76 μm )( 6166 K ) =4686 μ mK ⃗ f
λ2
= 0.59141
Then the fraction of radiation emitted between these two wavelengths becomes fλ
2−fλ
1=0.59141−0.15444≃0.437
(or 43.7%)
3 . هرجنپ کی یحارط 2
m*2 m
هک تسا یا هنوگ هب
90 جوم لوط هزاب رد یشبات یژرنا %
λ=0.3−3.0μm
مسج کی دننام هشیش اه جوم لوط ریاس یازاب و دنک یم روبع هشیش زا
SUN T = 10,400 R
یا مد ود رد هایس مسج کی دیشروخ رگا .دنک یم راتفر تام لاماک 5800
و
K1000
K.دیروآ تسدب ار هرجنپ زا یروبع یشبات یژرنا خرن ،دوش هتفرگ رظن رد
Analysis The surface area of the glass window is As=4 m2
(a) For a blackbody source at 5800 K, the total blackbody radiation emission is Eb(T)=σT4As=(5.67×10−8 kW/m2.K)4(5800 K)4(4 m2)=2.567×105 kW The fraction of radiation in the range of 0.3 to 3.0 m is
λ
1T =( 0.30 μm )( 5800 K ) =1740 μ mK ⃗ f
λ1
= 0.03345 λ
2T =( 3.0 μm )( 5800 K ) =17,400 μ mK ⃗ f
λ2
= 0.97875
Δf=fλ2−fλ
1=0 . 97875−0 .03345=0 . 9453
Noting that 90% of the total radiation is transmitted through the window,
E
transmit= 0.90 Δ fE
b( T )
¿(
0.90 )( 0.9453 )( 2.567 × 10
5kW )= 2. 184 × 10
5kW
(b) For a blackbody source at 1000 K, the total blackbody emissive power is Eb(T)=σT4As=(5.67×10−8 W/m2.K4)(1000 K)4(4 m2)=226 .8 kW The fraction of radiation in the visible range of 0.3 to 3.0 m is
λ
1T =( 0.30 μm )( 1000 K ) =300 μ mK ⃗ f
λ1
= 0.0000 λ
2T =( 3.0 μm )( 1000 K ) =3000 μ mK ⃗ f
λ2
= 0.273232
Δf=fλ2−fλ
1=0 .273232−0 and
Etransmit=0.90Δ fEb(T)=(0.90)(0.273232)(226.8 kW)=55.8 kW SUN
L = 2 m
Glass
= 0.9
4 . رتمک یاه جوم لوط یازاب سم تافلوس اب هدش هدیشوپ یموینیمولآ هحفص کی ساکعنا بیرض
زا
3μmربارب 0.35 و زا رتشیب یاه جوم لوط یازاب
3μmربارب 0.95 یا مد ود رد .تسا
5800 و
K300 ( حط س ط سوتم سا کعنا بیر ض
Kreflectivity
( لی سگ بیر ض ،)
emissivity
( بذج و )
absorptivity
.دیروآ تسدب ار )
Analysis The average reflectivity of this surface for solar radiation ( = 5800 K) is determined to be
Noting that this is an opaque surface,
At = 5800 K:
α + ρ = 1 ⃗ α = 1 − ρ = 1 − 0.362 = 0. 638
Repeating calculations for radiation coming from surfaces at = 300 K,
ρ( T )=( 0.35 )(0.0001685 )+(0.95 )( 1−0.0001685)=0. 95
At = 300 K:
α + ρ = 1⃗ α = 1 − ρ = 1 − 0.95 = 0. 05
and
The temperature of the aluminum plate is close to room temperature, and thus emissivity of the plate will be equal to its absorptivity at room temperature. That is,
5 .
؟دید یایاوز
0.95
3 , m
Assumptions The surfaces are diffuse emitters and reflectors.
Analysis From Figure:
L 3 W = 1
2 = 0.5 ¿ } ¿¿ F 31 = 0.24 ¿
and
L 3 W = 1
2 = 0.5 ¿ } ¿¿ F 3 →( 1 + 2 ) = 0.29 ¿
We note that A1 = A3. Then the reciprocity and superposition rules give
A
1F
13= A
3F
31⃗ F
13= F
31=0. 24
F
3→(1+2)= F
31+ F
32⃗ 0.29 = 0.24 + F
32⃗ F
32= 0.05
Finally,
6 . دید یایاوز F
12∧ F
21:)لیوط( تیاهن یب همین یاه تکاد یارب
(1) A2
A1 A3 (3) L3 = 1 m
L2 = 1 m (2) W = 2 m
Assumptions 1 The surfaces are diffuse emitters and reflectors. 2 End effects are neglected.
Analysis (a) Surface (1) is flat, and thus . summation rule: F11+F12=1→F12=1
reciprocity rule: A1F12=A2F21⃗F21=A1
A2F12= Ds
(
πD2)
s(1)=2 π=0 .64
(b) Noting that surfaces 2 and 3 are symmetrical and thus , the summation rule gives
F
11+ F
12+ F
13= 1 ⃗ 0 + F
12+ F
13= 1 ⃗ F
12= 0.5
Also by using the equation obtained in Example 12-4 (we solved it in our class),
reciprocity rule: A1F12=A2F21⃗F21=A1
A2F12=a
b
(
12)
=2baD (2)
(1)
a (3) (2)
(1)
L1 = a L2 = a
L3 = b L4 = b
(c) Applying the crossed-string method gives
7 .
؟دید یایاوز
From Fig.12-5,
L 2 D = 2
2 ¿ } ¿¿ F ( 2 + 4 )→( 1 + 3 ) = 0.20 ¿
andL D 2 = 2 2 ¿ } ¿¿ F 14 = 0.12 ¿
superposition rule: F
(2+4)→(1+3)= F
(2+4)→1+ F
(2+4)→3symmetry rule: F
(2+4)→1= F
(2+4)→3Substituting symmetry rule gives
reciprocity rule: A
1F
1→(2+4)= A
(2+4)F
(2+4)→1⃗( 2 ) F
1→(2+4)=( 4 )( 0.10 )⃗ F
1→(2+4)= 0.20 superposition rule : F
1→(2+4)= F
12+ F
14⃗ 0.20 = F
12+ 0.12 ⃗ F
12= 0.20 − 0.12 = 0.08
8 . یا ه ر طق ه ب ز کرم مه هر ک ود D
1=0.3 m∧ D
2=0.8 m
تبا ث یا هامد رد
T1=700K∧T2=400K
هر ک ود نیا لی سگ بیارض .دنا هدش هتشاد هگن
ε1=0.5∧ε2=0.7
ر گا نین چمه .د یروآ ت سدب ار هرک ود نایم یشبات صلاخ ترارح لاقتنا خرن .دنشاب یم فارطا طیحم یامد
30℃هر ک یجرا خ حطس رد ار ییاجباج ترارح لاقتنا بیرض دشاب
ربارب هرک یجراخ حطس لیسگ بیرض( .دیروآ تسدب اه 0.35
).دوش هتفرگ رظن رد
Two concentric spheres are maintained at uniform temperatures. The net rate of radiation heat transfer between the two spheres and the convection heat transfer coefficient at the outer surface are to be determined.
Assumptions 1 Steady operating conditions exist 2 The surfaces are opaque, diffuse, and gray.
Analysis The net rate of radiation heat transfer between the two spheres is
Radiation heat transfer rate from the outer sphere to the surrounding surfaces are Q˙rad=ε FA2σ(T
24−T
surr4)
=(0.35)(1)[π(0.8 m)2](5.67×10−8 W/m2⋅K4)[(400 K)4−(30+273 K)4]=685W
The convection heat transfer rate at the outer surface of the cylinder is determined from requirement that heat transferred from the inner sphere to the outer sphere must be equal to the heat transfer from the outer surface of the outer sphere to the environment by convection and radiation. That is,
Q ˙
conv= ˙ Q
12− ˙ Q
rad= 1669 − 685 = 984 W
Then the convection heat transfer coefficient becomes
˙
Qconv.=hA2
(
T2−T∞)
984 W=h
[
π(0.8 m)2]
(400 K-303 K)⃗h=5.04 W/m2⋅° C= 0.35
Tsurr = 30C
T = 30C D1 = 0.3 m T1 = 700 K D2 = 0.8 m
T2 = 400 K