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Process Equipment and Plant Design

Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

0.5 d
D
0.75 d
2 d

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Process Equipment and Plant Design
A perforated plate has holes of diameter dh arranged in a pitch ph. Each hole has a tube of I.D. dt passing through it. The ligament efficiency is given by

(ph - dh . dt/2)/ph
(ph - dh)/ph
(ph - dt)/ph
(ph - dh)/dh

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Tall vertical
Small horizontal
Thick walled
Large horizontal

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

3 to 12.5
L to 3
4 to 8
12.5 to 18.5

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Process Equipment and Plant Design
The value of fouling factor depends upon the

All of these
Characteristic of process fluid
Velocity of process fluid containing suspended solids
Suspended solids in the fluid

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Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

4 to 8
6 to 12
3 to 5
2 to 3

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