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Process Equipment and Plant Design

Process Equipment and Plant Design
Frame thickness in the plate and frame filter press is normally in the range of __________ inches.

0.25 to 8
1 to 5
0.25 to 4
1 to 12

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Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

10-12.5
5-7.5
15-20
2.5-3.0

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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
Horizontal
None of these

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Containing suspended solids flows at low velocity
Is highly viscous
Containing suspended solids flows at high velocity
Is of high specific gravity

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Process Equipment and Plant Design
The minimum baffle height should be

Twice the tank diameter
Equal to the impeller diameter
Twice the impeller diameter
3/4 of the tank height

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Process Equipment and Plant Design
Rivets are generally specified by the

None of these
Shank diameter
Overall length
Head diameter

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