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Process Equipment and Plant Design

Process Equipment and Plant Design
The diameter of a propeller agitator used in agitation tank ranges from __________ percent of the tank diameter and its peripherial speed is normally 300 to 500 metres/minute.

5 to 10
40 to 50
15 to 30
55 to 75

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Process Equipment and Plant Design
Rate of filtrate delivery is inversely proportional to the

Cake & filter medium resistance
Viscosity of filtrate
Filtering area & the pressure difference driving force
Both A & B

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

Packed
Bubble cap plate
None of these
Sieve plate

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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

0.99
0.55
0.8
0.95

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Process Equipment and Plant Design
Lug support is

All of these
The most suitable for thick vertical vessel
Same as bracket support
Provided usually for vessels of much smaller height than skirt supported vessels

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Process Equipment and Plant Design
In a distillation column, minimum clearance to be maintained betweeen the overflow weir and the last row of the bubble caps is __________ cms.

7.5
2.5
15
20

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