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Process Equipment and Plant Design

Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

2.5 to 3.5
1 to 1.5
6 to 8
4 to 5

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Process Equipment and Plant Design
An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

All of these
An increase in relatived volatility for rectification columns
Decrease in gas solubility for absorbers
An increase in liquid viscosity

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Thick walled tall
Small
Large horizontal cylindrical
Tall but empty

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Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same

Inside diameter
Outside diameter
None of these
Wall thickness

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Process Equipment and Plant Design
Shortest distance between two tubes is

Called tube pitch
None of these
More in case of triangular pitch as compared to square pitch of tube layout
Called tube clearance

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Process Equipment and Plant Design
Thickness of the frame of a plate and frame filter as compared to that of plates is

Less
More
Either A or B
Same

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