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Process Equipment and Plant Design

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.

30
20
35
10

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Process Equipment and Plant Design
The maximum liquid gradient over a tray must not exceed

5"
0.5" -1.25"
2"-3.5"
Half the tray spacing

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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

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

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Thick walled tall
Small
Tall but empty
Large horizontal cylindrical

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thin shperical (e.g. Horton sphere)
Thick walled vertical
None of these
Horizontal

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Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

1
3.5
3
2

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