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Process Equipment and Plant Design

Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

D
√d
√(2πd)
√(2d)

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

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

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Process Equipment and Plant Design
Heat transfer co-efficient, hG(Kcal/hr.m² .°C) and mass velocity of air, G (kg/hr.m² ) for air flow parallel to the surface in case of constant drying rate in batch drying is related as hG = 0.0176G0.8. But when the flow of air perpendicular to the surface is encountered, this equation changes to

HG = 0.0176G0.37
1.004G0.8
0.0176G1.37
HG = 1.004G0.37

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Process Equipment and Plant Design
Diameter of bubble caps used in high pressure columns is __________ as compared to that used in identical vacuum columns.

More
Either A or B; no generalisation can be made
Same
Less

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Reverse
Cross
Split
Cascade

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Process Equipment and Plant Design
__________ shaped roof is most commonly used for cylindrical tanks.

Flat
Cone
Dome
Umbrella

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