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Process Equipment and Plant Design

Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.5-0.65
0.15-030
0.60-0.90
0.75-0.85

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

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

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Process Equipment and Plant Design
Compensation against openings in process vessels for giving inlet and outlet connections, for providing sight glasses and manholes etc. is provided for strength and rigidity. The most efficient type of compensation is of __________ type.

Nozzle or rim
Flared out
Fluid in
Ring plate

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Process Equipment and Plant Design
Vertical vessels are not supported by

Saddles
Brackets
Columns
Skirts

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Process Equipment and Plant Design
In case of saddle packing (e.g., berl and intralox saddles), the maximum size of the packing should not exceed __________ of the column diameter.

l/30th
l/50th
l/15th
l/5th

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Process Equipment and Plant Design
A high vapour velocity is required for high plate efficiency in a seive plate coloumn. The satisfactory value of operating vapor velocity for design purpose in seive plate column is about __________ percent of the flooding velocity.

80
60
95
45

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