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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure drop per tray in the atmospheric distillation column is about __________ psi.

0.07 - 0.12
0.01 - 0.5
0.5 - 1.0
43833

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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.

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

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Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

10-12.5
15-20
5-7.5
2.5-3.0

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Process Equipment and Plant Design
With increase in the number of shell passes, the value of FT

Increases
Decreases
Remains same, only if the number of tube passes does not change
Remains same

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the overall heat transfer co-efficient is proportional to the tube side (volumetric flow rate)0.8. This is valid, only when the ratio of the tube side film resistance to the total resistance is almost equal to

20.8
∞
1
2

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Process Equipment and Plant Design
The distance between the centre of a rivet hole to the nearest edge of the plate is called

None of these
Margin
Back pitch
Pitch

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