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Process Equipment and Plant Design

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.

60
80
95
45

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Process Equipment and Plant Design
Rivets are generally specified by the

None of these
Shank diameter
Overall length
Head diameter

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Process Equipment and Plant Design
Which of the following lengths of heat exchanger tubes are normally not used in practice?

0.5 metre
6 metres
10 metres
2.5 metres

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Process Equipment and Plant Design
Which of the following factors affect the pressure drop in a co-current gas-liquid absorption packed tower?

All of these
Fluid flow rates
Density and viscosity of fluids
Size, shape, orientation and surface of the packing particles

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.1-0.2
1.2-1.5
0.2-0.5
0.4-0.9

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Process Equipment and Plant Design
In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Pressure drop is proportional to the square
Heat transfer co-efficient is proportional to 0.8th power
Both A & B
Neither A nor B

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