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Process Equipment and Plant Design

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

Tall but empty
Thick walled tall
Small
Large horizontal cylindrical

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Process Equipment and Plant Design
For turbine agitator, the impeller diameter is about

0.3 to 0.5 d
0.65 to 0.85 d
0.95 d
0.1 to 0.2 d

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

30.5
45.5
5.5
12.5

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Process Equipment and Plant Design
In seive plate column, holes are drilled or punched in sizes ranging from 2.5 to 12 mm (5 mm being widely used). The hole pitch is normally __________ times the hole diameter to give the required hole area.

2.5 to 4.0
10 to 15
5 to 10
0.5 to 1.5

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Process Equipment and Plant Design
Vertical vessels are not supported by

Skirts
Columns
Brackets
Saddles

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Square pitch
Heat transfer rate is independent of tube arrangement
Diagonal square pitch
Triangular pitch

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