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Process Equipment and Plant Design

Process Equipment and Plant Design
Rivets are generally specified by the

Shank diameter
None of these
Head diameter
Overall length

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

5
60
350
200

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Independent of the type of
Segmental
Disk and ring
Orifice

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Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

20-40
100-150
1000-1500
43835

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Process Equipment and Plant Design
The slope of the feed line in distillation opeartion is given by (where, q = fraction of the feed stream that is liquid.)

None of these
-q
-q/(1-q)
-q/(q-1)

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Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

4 to 5
1 to 1.5
2.5 to 3.5
6 to 8

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