Heat Transfer MCQs with answers Page - 3

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Q. When vaporisation takes place through a blanketting film of gas, the phenomenon is termed as __________ boiling.

  • (A) Pool
  • (B) Nucleate
  • (C) Transition
  • (D) Film

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Q. Resistance to heat flow by conduction is proportional to (where, t & ρ are thickness & density of the material respectively and A = area normal to the direction of heat flow.)

  • (A) t
  • (B) 1/ρ
  • (C) 1/A
  • (D) All of the above

A

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Q. For the same heat transfer area and the terminal conditions, the ratio of the capacities of a single effect evaporator to a triple effect evaporator is

  • (A) 0.33
  • (B) 1
  • (C) 1.33
  • (D) 3

A

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Q. Evaporation of 1kg of water from a solution in a single effect evaporator requires about __________ kg of steam.

  • (A) 0.4 - 0.6
  • (B) 1 - 1.3
  • (C) 1.8 - 2
  • (D) 2 - 2.4

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Q. Stefan-Boltzman law which describes the radiation heat transfer states that, it is proportional to (where, t = temperature in °C T = absolute temperature in °K)

  • (A) t4
  • (B) T4
  • (C) 1/t4
  • (D) 1/T4

A

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Q. A single pass air heater is connected to a two pass unit. For the air flow rate and other conditions remaining the same, the film heat transfer co-efficient for air will vary in the ratio of

  • (A) 2
  • (B) 20.8
  • (C) 20.2
  • (D) 20.5

A

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Q. The film co-efficient between condensing vapour and metal wall increases with

  • (A) Increasing temperature of the vapour
  • (B) Increasing viscosity of the film of condensate
  • (C) Decreasing temperature of the vapour
  • (D) Increasing temperature drop

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Q. If all the conditions and dimensions are same, then the ratio of velocity through the tubes of a double pass heat exchanger to that through the single pass heat exchanger is

  • (A) 1/2
  • (B) 1
  • (C) 2
  • (D) 4

A

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Q. Temperature profile in steady state heat transfer is

  • (A) Asymptotic
  • (B) Hyperbolic
  • (C) Parabolic
  • (D) Linear

A

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Q. The inner wall of a furnace is at a temperature of 700°C. The composite wall is made of two substances, 10 and 20 cm thick with thermal conductivities of 0.05 and 0.1 W.m-1.°C-1 respectively. The ambient air is at 30°C and the heat transfer co-efficient between the outer surface of wall and air is 20 W.m-2.°C-1. The rate of heat loss from the outer surface in W.m-2 is

  • (A) 165.4
  • (B) 167.5
  • (C) 172.5
  • (D) 175

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