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Process Equipment and Plant Design

Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.95
0.75
0.55
0.85

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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.

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

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

12.5 to 18.5
3 to 12.5
4 to 8
L to 3

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering branch) would be

Both B and C
Around 90
Less than that for Tee (used as elbow, entering run)
More than that for Tee (used as elbow, entering run)

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Neither A nor B
Floating head tube sheet
U-bend
Either A or B

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Process Equipment and Plant Design
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

(p² - πd²/4)/πd
(4p² - πd²/4)/πd
4(0.86p² - πd²/4)/πd
4(0.86p² - πd²)/πd

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