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Process Equipment and Plant Design

Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Large horizontal
Small horizontal
Tall vertical
Thick walled

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Process Equipment and Plant Design
In distillation columns, bubble caps are held in place over trays by

Rivets
Both B and C
A hold down bar
Bolts

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Process Equipment and Plant Design
To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

(1.2)3/2
(1.2)3/5
(1.2)2/3
(1.2)5/3

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

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

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

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

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