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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.

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

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
Both B & C
4 : 1 to 8 : 1 for liquid-liquid exchanger
< 4 : 1 for gas-gas exchangers

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Process Equipment and Plant Design
Friction factor for turbulent flow in a new pipe is given by

f = 16/NRe
f = 25/NRe
f = 0.22 NRe0.05
f = 0.04/NRe0.16

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Process Equipment and Plant Design
Correct use of 'factor of safety' is very important in equipment design. It is defined as the ratio of the

Ultimate stress to working stress
Working stress to ultimate stress
Ultimate stress to breaking stress
None of these

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Process Equipment and Plant Design
In a pressure vessel containing multiple openings of various dimensions at different parts, stress concentration at the edges of the opening is maximum which becomes negligibly small beyond the area covered by __________ times the hole diameter.

Two
Twenty
Ten
Five

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Process Equipment and Plant Design
__________ shaped roof is most commonly used for cylindrical tanks.

Dome
Flat
Umbrella
Cone

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