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Process Equipment and Plant Design

Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.55
0.8
0.99
0.95

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Process Equipment and Plant Design
__________ shapedroof is the most commonly used roof for cylinderical storage tanks.

Conical
Flat
Umbrella
Dome

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Upper limit of the vapour velocity
Lower limit of vapour velocity
Height of the plate spacing
Hole diameter of the seive tray

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large reflux ratio
Low gas velocity
Resistance offered to flow of liquids by caps & risers and the flow of gas
Large plate spacing

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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?

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

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Process Equipment and Plant Design
With increase in the reflux ratio for a fixed production from a continuous binary distillation column, the __________ decreases.

Running cost of steam for reboiler
Fixed charges initially
Vapour & liquid load both
Running cost of cooling water for condenser

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