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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum plate spacing in most of the pertroleum refinery distillation columns (of dia > 3 ft) is normally __________ inches.

12
6
18
34

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Process Equipment and Plant Design
For identical operating conditions, the pressure drop over __________ tray is the highest out of the following.

Bubble cap
Counterflow
Valve
Sieve

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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

Elongation
Shear
Bending
Deformation

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Around 7
Much more than that for fully open globe valves
Much less (say 2% than that for fully open globe valves)
Both B and C

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

6 metres
2.5 metres
10 metres
0.5 metre

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Fouling fluids
Double pipe heat exchanger
Counter flow of hot and cold fluids
Multipass shell and tube heat exchanger

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