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Process Equipment and Plant Design

Process Equipment and Plant Design
What is the minimum recommended ligament for square pitch arrangement in case of heat exchangers?

6.5 cms
6.5 mm
Equal to tube I.D
Equal to tube O.D

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Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

1
3
3.5
2

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Process Equipment and Plant Design
In a multiple effect evaporator system having 'n' effects, the amount of water evaporated per unit surface area in approximately equal to __________ times that in a single effect.

1.5 nth
nth
(1/n)th
0.5 nth

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Process Equipment and Plant Design
Compensation against openings in process vessels for giving inlet and outlet connections, for providing sight glasses and manholes etc. is provided for strength and rigidity. The most efficient type of compensation is of __________ type.

Fluid in
Nozzle or rim
Flared out
Ring plate

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Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.99
0.55
0.95
0.8

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Process Equipment and Plant Design
The minimum baffle height should be

Twice the tank diameter
Twice the impeller diameter
3/4 of the tank height
Equal to the impeller diameter

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