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Process Equipment and Plant Design

Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Skirts
Saddles
Columns

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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.

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

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Process Equipment and Plant Design
Width and depth of grooves in the tube sheet holes normally are __________ inch respectively.

1/2 and 8
1/2 and 5
1/64 and 1/8
1/8 and 1/64

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Process Equipment and Plant Design
Bubble cap diameter used for the distillation column having diameter ranging from 1.5 to 4.5 metres is about __________ mm.

10
150
50
100

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Process Equipment and Plant Design
In case of a continuous distillation column, increase in reflux ratio may result in the

Greater cost for the condenser coolant
Lower fixed charges for the column
Greater cost for the reboiler heat supply
All of these

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Process Equipment and Plant Design
In actual operation of a bubble cap distillation tower, the __________ at the bottom of the tower is more than that at the top of the tower.

Pressure and temperature
Molal flow rate of vapour
All of these
Vapour molecular weight

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