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Process Equipment and Plant Design

Process Equipment and Plant Design
A shell may by termed as thin if its thickness to diameter ratio is less than 0.1. The factor which can be neglected in the calculation of membrane stresses is

Bending
Elongation
Shear
Deformation

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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

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

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Process Equipment and Plant Design
Apex angle of conical heads used in the bottom heads of chemical process equipments is usually

45°
75°
60°
30°

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Process Equipment and Plant Design
Maximum size of the raschig rings used in a packed tower is about __________ of the coloumn diameter.

1/30th
1/50th
1/10th
1/20th

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Process Equipment and Plant Design
Value of Peclet number = 0, is the representative of

Complete back mixing
Laminar flow
Eddy diffusivity = 0
Plug flow

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Cross
Reverse
Cascade
Split

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