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Process Equipment and Plant Design

Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

√(2πd)
√d
D
√(2d)

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Process Equipment and Plant Design
Vertical storage vessels are never supported by __________ support.

Skirt
Saddle
Bracket
Lug

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Process Equipment and Plant Design
For a given design of bubble cap, the number of bubble caps to be used per tray is set by the

Diameter of the column
All of these
Allowable gas velocity through the slots
Plate spacing

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Process Equipment and Plant Design
Optimum reflux ratio in a continuous distillation column is determined by the

Maximum permissible vapour velocity
Total cost consideration (fixed cost of the column plus the cooling water & steam cost)
None of these
Flooding limit of the column

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Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

4(P² - πd²/4)/πd
Πd/4P²
(P² - πd²/4)/πd
4P²/πd

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Process Equipment and Plant Design
For identical operating conditions, the pressure drop over __________ tray is the highest out of the following.

Counterflow
Valve
Bubble cap
Sieve

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