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Process Equipment and Plant Design

Process Equipment and Plant Design
The diameter of a propeller agitator used in agitation tank ranges from __________ percent of the tank diameter and its peripherial speed is normally 300 to 500 metres/minute.

5 to 10
40 to 50
15 to 30
55 to 75

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Process Equipment and Plant Design
In case of bubble cap distillation column of diameter greater than 1.2 metres, the cap diameter is roughly about __________ cms.

35
20
30
10

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

1.25
2.5
3.5
1.75

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

Making the joint leak proof
Preventing the local overstressing of the shell around the opening
None of these
Reduction of discontinuity in shape at the junction

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Around 7
Both B and C
Much less (say 2% than that for fully open globe valves)
Much more than that for fully open globe valves

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

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

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