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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

4 to 8
3 to 5
6 to 12
2 to 3

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

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Process Equipment and Plant Design
The thickness of heat transfer plates used in the plate type heat exchanger ranges from __________ mm, pressed in a single piece provided with grooves & corrugations.

3.5 to 7.0
0.3 to 0.8
44055
1.25 to 3.125

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

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

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Process Equipment and Plant Design
Overall mass transfer co-efficient in case of absorption of __________ in water is based on the gas film co-efficient only, as the mass transfer process is gas film (phase) controlling.

None of these
SO₂
NH₃
CO₂

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

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

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