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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

15000
7500
1250
2500

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Process Equipment and Plant Design
__________ is the determining factor for the number of bubble caps to be used per tray.

Vapor load
Permissible slot velocity
Tray diameter
Liquid load

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Process Equipment and Plant Design
The normal range of velocity of water in pipes is __________ m/sec.

15-30
1-2
0.1-0.5
10-50

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Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.5 to 0.6 d
0.02 to 0.05 d
0.08 to 0.12 d
0.2 to 0.5 d

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

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

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Process Equipment and Plant Design
What is the slope of the operating line in the stripping section of a distillation column?

?
< 1
> 1

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