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Process Equipment and Plant Design

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

Laminar flow
Complete back mixing
Plug flow
Eddy diffusivity = 0

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Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

15000
7500
2500
1250

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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.

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

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Process Equipment and Plant Design
Of the pressure vessels, with same thickness but different diameters, which one withstands higher pressure?

Strength of the vessel is same irrespective of the diameter
Smaller dia vessel
Larger dia long vessel
Larger dia vessel

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Process Equipment and Plant Design
For a given design of bubble cap, the number of bubble caps to be used per tray is set by the

Plate spacing
All of these
Diameter of the column
Allowable gas velocity through the slots

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Inadequate equipment design
Failure of equipments
Faulty operating procedures
Improper layout of the equipments

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