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Process Equipment and Plant Design

Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the shell side cross flow area does not depend upon

Clearance
Baffle spacing
Pitch
None of these

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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
None of these
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
The thickness of heat transfer plates used in the plate type heat exchanger ranges from __________ mm, pressed in a single piece provided with grooves & corrugations.

3.5 to 7.0
0.3 to 0.8
1.25 to 3.125
44055

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering run) would be around

350
60
5
200

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Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

5.5
12.5
45.5
30.5

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Process Equipment and Plant Design
An adequate clearance between the tray and the shell wall of a distillation column is provided to

None of these
Allow for thermal expansion and facilitate installation
Avoid back-trapping
Drain the liquid from the tray when the unit is not in operation

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