Heat Transfer
In a shell and tube heat exchanger, square pitch compared to triangular pitch

Gives a lower shell side pressure drop
None of these
Can pack more surface area into a shell of given diameter
Gives a higher shell side pressure drop

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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

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

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