Heat Transfer
Bulk of the convective heat transfer resistance from a hot tube surface to the fluid flowing in it, is

None of these
Uniformly distributed throughout the fluid
Mainly confined to a thin film of fluid near the surface
In the central core of the fluid

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Heat Transfer
Baffle spacing

Should be less than one fifth the diameter of the shell
None of these
Should be less than the inside diameter of the shell
Is not the same as baffle pitch

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Heat Transfer
Nusselt number is the ratio of the

Heat flux at the wall to that across the entire pipe
Temperature difference to the temperature gradient at the wall
Temperature gradient of the wall to that across the entire pipe
None of these

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