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Process Equipment and Plant Design

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.

44183
44058
43962
43895

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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.

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

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Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

More than geometric mean value
Both B & C
Less than arithmetic mean value
More than arithmetic mean value

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Process Equipment and Plant Design
A perforated plate has holes of diameter dh arranged in a pitch ph. Each hole has a tube of I.D. dt passing through it. The ligament efficiency is given by

(ph - dt)/ph
(ph - dh)/dh
(ph - dh . dt/2)/ph
(ph - dh)/ph

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Around 7
Both B and C
Much more than that for fully open globe valves
Much less (say 2% than that for fully open globe valves)

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Process Equipment and Plant Design
The wall thickness for a large high pressure pipeline is determined by the consideration of the

Forces exerted by static and dynamic action at bends
Axial tensile stress in the pipe
Circumferential pipewall tension
Temperature stresses

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