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Process Equipment and Plant Design

Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

1/D⁵
1/D
1/D²
D²

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Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

More than geometric mean value
Both B & C
More than arithmetic mean value
Less than arithmetic mean value

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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
Equal to the order of reaction
1

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Process Equipment and Plant Design
In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)

Z.H.ρ/L
L/Z.H.ρ
H.ρ/L
Z.H/L.ρ

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Process Equipment and Plant Design
Power required for agitation depends upon the

Size of agitator & the tank
Agitator type & speed of agitation
All of these
Height & properties of the liquid

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Process Equipment and Plant Design
Vertical vessels are not supported by

Columns
Skirts
Saddles
Brackets

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