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Heat Transfer

Heat Transfer
Steam consumption in kg/hr in case of an evaporator is given by (where, C & E are capacity the economy of the evaporator respectively)

E/C
CE
C/E
1/CE

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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)

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

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Heat Transfer
Which of the following is unimportant in forced convection ?

none of the listed here
Reynolds number
Prandtl number
Grashhoff number

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Heat Transfer
The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe whose surface temperature remains constant is

Dependent on NRe only
88.66
3.66
1.66

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Heat Transfer
The main purpose of providing fins on heat transfer surface is to increase the

Temperature gradient
Mechanical strength of the equipment
Heat transfer co-efficient
Heat transfer area

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Heat Transfer
Double pipe heat exchangers are preferably useful, when

A corrosive liquid is to be heated
Overall heat transfer co-efficient is very high
Requirement of heat transfer area is low
High viscosity liquid is to be cooled

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