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Process Equipment and Plant Design

Process Equipment and Plant Design
Vertical vessels are not supported by

Skirts
Brackets
Columns
Saddles

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Hole diameter of the seive tray
Lower limit of vapour velocity
Height of the plate spacing
Upper limit of the vapour velocity

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Process Equipment and Plant Design
For identical situation, condensing film coefficient in case of a horizontal condenser is almost __________ the value expected in case of vertical condenser.

Thrice
Five times
Twice
Half

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Process Equipment and Plant Design
If 'D' is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

D/2 or minimum 2" to 5D
D/5 or minimum 2" to 5D
D/5 or minimum 2" to D
None of these

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Orifice
Segmental
Disk and ring
Independent of the type of

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Process Equipment and Plant Design
Cylinderical shell thickness of rotary drier is generally __________ mm.

43864
18-22
43990
44180

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