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Process Equipment and Plant Design

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

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

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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
Angled baffles are preferred in the agitation tank to control the swirling action; if the viscosity of the liquid to be mixed is about 200 poise. However, the baffle may be completely eliminated for mixing liquids having viscoisty above __________ poise.

1500
1000
600
300

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Tall vertical
Large horizontal
Thick walled
Small horizontal

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

0.8
0.55
0.99
0.95

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

10000
3000
5000
1000

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