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Process Equipment and Plant Design

Process Equipment and Plant Design
Longitundinal stress induced in a thin walled cylindrical storage vessel is

PD/4t
PD/3t
PD/6t
PD/2t

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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
Speed of industrial paddle agitator ranges from __________ rpm.

1 to 5
1000 to 2000
500 to 750
20 to 100

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Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

1
>1
< 1
Equal to the order of reaction

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Process Equipment and Plant Design
Baffle spacing is generally __________ the I.D. of the shell.

Both B and C
More than
Not less than one fifth of
Not greater than

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Process Equipment and Plant Design
Hold up of material in a operating rotary drier is in the range of

0.05 to 0.15
0.25 to 0.50
0.5 to 0.8
0.8 to 0.9

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