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Heat Transfer

Heat Transfer
In a liquid-liquid heat exchanger, for the same process temperature, the ratio of the LMTD in parallel flow to the LMTD in counter flow is always

< 1
> 1
∞
1

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Heat Transfer
Boiling point elevation of a solution of NaOH

Both B and C
Increases rapidly with temperature rise
Is almost independent of temperature
Is almost independent of pressure

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Heat Transfer
The purpose of providing a 'catchall' in the vapor line of an evaporator is to

Create vacuum
Arrest the entrained liquid
Vent the non-condensible gases
Regulate the vapor flow

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Heat Transfer
Harmonic mean temperature difference is given by

2.(ΔT₁ . ΔT₂)/(ΔT₁ + ΔT₂)
√(ΔT₁ . ΔT₂)
(ΔT₁ - ΔT₂)/(ΔT₁ . ΔT₂)
2.(ΔT₁ . ΔT₂)(ΔT₁ - ΔT₂)

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Heat Transfer
Fouling factor for a heat exchanger is given by (where, U₁ = heat transfer co-efficient of dirty surface U₂ = heat transfer co-efficient of clean surface)

U₂ - U₁
1/U₁ - 1/U₂
U₁ - U₂
1/U₂ - 1/U₁

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Heat Transfer
For a liquid in laminar flow through a very long tube, when the exit fluid temperature approaches the wall temperature, the equation to be used is

Nu = 0.023 Re0.8 . Pr0.4
Nu = 2Gz0.5
Nu = Gz
Nu = Gz

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