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Process Equipment and Plant Design

Process Equipment and Plant Design
for couplings and unions would be

350
200
60
Negligible

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the minimum shell thickness for carbon steel (inclusive of corrosion allowance) depends on shell diameter and is in the range of __________ mm.

43962
44183
43895
44058

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Process Equipment and Plant Design
With increase in pressure drop (for a given particle size), the dust collection efficiency of a cyclone separator will

Remain unaffected
Increase
Increase or decrease depending on the nature of the dust
Decrease

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the

Shortest distance between two adj acent tube holes
O.D. of the tube for square pitch
None of these
Shortest centre to centre distance between adjacent tubes

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be designed without wind load considerations
Be supported very easily
Withstand higher pressure for a given metallic shell thickness
Be fabricated very easily

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for

Creating turbulence
Reducing scale deposition
Increasing pressure drop
Fixing the tubes

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