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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

1250
7500
2500
15000

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

Elliptical
Hemispherical
None of these
Torispherical

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Process Equipment and Plant Design
The slope of the feed line in distillation opeartion is given by (where, q = fraction of the feed stream that is liquid.)

-q/(1-q)
-q
None of these
-q/(q-1)

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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.

Flared out
Ring plate
Fluid in
Nozzle or rim

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Process Equipment and Plant Design
Fresh water carrying pipelines in chemical industries are coloured with __________ color.

Brown
Yellow
Red
Sea green

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Process Equipment and Plant Design
Needle valves are generally not used for

High pressure throttling service
Very accurate flow control
Very large diameter pipes
Smaller sizes of pipe

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