Heat Transfer Miscellaneous
- A solid cylinder (surface 2) is located at the centre of a hollow sphere (surface 1). The diameter of the sphere is 1 m, while the cylinder has a diameter and length of 0.5 m each.'The radiation configuration factor F11 is
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Diameter of sphere = 1 m
Diameter of aylinder = 0.5 m
F21 + F22 = 1 (∵ F22 = 0)
F22 = 1
we know that
A1 F12 = A2 F21F12 = A2 A1 ∴ F11 = 1 - F12 = 1 - A2 A1 ∴ F11 = 1 - A2 A1 F11 = 1 - [(π × 0.5 × 0.5) + ( 2 × π/4 × 0.5 × 0.5)] = 0.625 4π × 0.5 × 0.5 Correct Option: B
Diameter of sphere = 1 m
Diameter of aylinder = 0.5 m
F21 + F22 = 1 (∵ F22 = 0)
F22 = 1
we know that
A1 F12 = A2 F21F12 = A2 A1 ∴ F11 = 1 - F12 = 1 - A2 A1 ∴ F11 = 1 - A2 A1 F11 = 1 - [(π × 0.5 × 0.5) + ( 2 × π/4 × 0.5 × 0.5)] = 0.625 4π × 0.5 × 0.5
- A hollow enclosure is formed between two inf initely long concentric cylinders of radii 1 m and 2 m, respectively. Radiative heat exchange takes place between the inner surface of the larger cylinder (surface-2) and the outer surface of the smaller cylinder (surface-1). The radiating surface are diffuse and the medium in the enclosure is non- participating. The fraction of the thermal radiation leaving the larger surface and striking itself is
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F11 + F12 = 1
F21 + F22 = 1
F11 = 0 due to concave surface
F12 = 1 Now
A1 F12 = A2 F21
⇒ F21 = F12 A1/A2
⇒ F12 = 1∴ F21 = A1 2πr1l r1 1 A2 2πr2l r2 2
F21 = 0.5
F22 = 1 – F21 = 0.5Correct Option: B
F11 + F12 = 1
F21 + F22 = 1
F11 = 0 due to concave surface
F12 = 1 Now
A1 F12 = A2 F21
⇒ F21 = F12 A1/A2
⇒ F12 = 1∴ F21 = A1 2πr1l r1 1 A2 2πr2l r2 2
F21 = 0.5
F22 = 1 – F21 = 0.5
- Consider two infinitely long thin concentric tubes of circular cross section as shown in figure. If D1 and D2 are the diameters of the inner and outer tubes respectively, then the view factor F22 is given by
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F22 = 1 - F21 =
= 1 - A1 = 1 - D1 A2 D2 Correct Option: D
F22 = 1 - F21 =
= 1 - A1 = 1 - D1 A2 D2
- For the same inlet and exit temperatures of the hot and cold fluids, the log mean temperature difference (LMTD) is
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NA
Correct Option: B
NA
- In a condenser of a power plant, the steam condenses at a temperature of 60°C. The cooling water enters at 30°C and leaves at 45°C. The Logarithmic Mean Temperature Difference (LMTD) of the condenser is
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Flow configuration in condenser as shown below.
ΔT1 = 30°C (Q1)
ΔT2 = 15°C (Q2)LMTD = ΔT1 - ΔT2 = 30 - 15 In ΔT1 In 30 ΔT2 15
= 21.6°CCorrect Option: B
Flow configuration in condenser as shown below.
ΔT1 = 30°C (Q1)
ΔT2 = 15°C (Q2)LMTD = ΔT1 - ΔT2 = 30 - 15 In ΔT1 In 30 ΔT2 15
= 21.6°C