Heat Transfer
Baffle spacing

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

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Heat Transfer
Condensing film co-efficient for steam on horizontal tubes ranges from 5000 to 15000 Kcal/hr.m² .°C. Condensation of vapor is carried out inside the tube in a shell and tube heat exchanger, when the

Higher condensing film co-efficient is desired
Lower pressure drop through the exchanger is desired
Temperature of the incoming vapor is very high
Condensate is corrosive in nature

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Heat Transfer
Steam trap is used to

Remove water resulting from partial condensation of steam
None of these
Stop the supply of steam
Condense the steam flowing in the pipeline

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