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Process Equipment and Plant Design

Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

D
0.75 d
2 d
0.5 d

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Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein
Same
Less
More

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Process Equipment and Plant Design
__________ heat exchanger is also known as 'hair pin type' exchanger,

Regenerative
Plate type
Finned
Double pipe

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Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A liquid phase catalytic reactor
A vapor phase reactor
Pot type reactor
A liquid phase reactor

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Process Equipment and Plant Design
In the allocated cap area, bubble caps are generally arranged on equilateral triangular pitch. Number of caps fixed on a plate is with a

Neither A nor B
Cap pitch of 1.3-2 times the cap diameter
Either A or B
Clearance of 25-75 mm

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

4 to 10
10 to 20
1 to 2
20 to 30

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