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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.

2500
7500
1250
15000

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Orifice
Independent of the type of
Segmental
Disk and ring

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Process Equipment and Plant Design
What is the slope of the operating line in the stripping section of a distillation column?

?
< 1
> 1

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Process Equipment and Plant Design
Generally, no corrosion allowance in wall thickness of a part is required, if the thickness is more than __________ mm.

5
10
30
20

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Process Equipment and Plant Design
Which of the following packing materials provides for maximum mass transfer?

All of these
Raschig rings
Cross-partition rings
Lessig rings

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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.

Nozzle or rim
Fluid in
Ring plate
Flared out

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