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Heat Transfer

Heat Transfer
The characteristic dimensionless groups for heat transfer to a fluid flowing through a pipe in laminar flow are

Nu, Pr
Nu, Pr, Re
Re.Gz
Nu, Gz

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Heat Transfer
In a shell and tube heat exchanger, floating head is used for

Less corrosion of tubes
High heat transfer co-efficient
Large temperature differentials
Low pressure drop

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Heat Transfer
In Fourier's law, the proportionality constant is called the

Stefan-Boltzman constant
Thermal conductivity
Thermal diffusivity
Heat transfer co-efficient

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Heat Transfer
The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe, where the wall heat flux is constant, is

120.36
4.36
Dependent on NRe only
2.36

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Heat Transfer
Steady state one dimensional heat flow by conduction as given by Fourier's low does not assume that

Material is anisotropic
Boundary surfaces are isothermal
There is no internal heat generation
Constant temperature gradient exists

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Heat Transfer
The average heat transfer co-efficient for laminar film condensation on vertical surface is inversely proportional to (where, ΔT = Temperature drop across condensate film )

ΔT
None of the listed here
(ΔT)2
(ΔT)1/4

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