Heat Transfer
In a heat exchanger, floating head is provided to

relieve stresses caused by thermal expansion
increase the heat transfer area
facilitate cleaning of the exchanger
increase log mean temperature gradient

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Heat Transfer
In a shell and tube heat exchanger,

The relationship is not generalised
There is no relationship between temperature drop and resistance
The temperature drop is inversely proportional to the resistance across which the drop occurs
The temperature drops in the two fluids and the wall are proportional to individual resistances

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Heat Transfer
A process stream of dilute aqueous solution flowing at the rate of10 Kg.s⁻¹ is to be heated. Steam condensate at 95°C is available for heating purpose, also at a rate of 10 Kg.s⁻¹. A 1 - 1 shell and tube heat exchanger is available. The best arrangement is

Counter flow with process stream on shell side
Parallel flow with process stream on tube side
Counter flow with process stream on tube side
Parallel flow with process stream on shell side

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Heat Transfer
Nusselt number is the ratio of the

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

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