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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as

Δp = G2
Δp = G0.5
Δp = 1/G0.6
Δp = G

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Process Equipment and Plant Design
An underdesigned steam trap will

None of these
Back up condensate and cause water hammer in steam line
Waste steam
Destroy itself of acceleration wear due to rapid recycling

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

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

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Process Equipment and Plant Design
What is the slope of the operating line in the stripping section of a distillation column?

< 1
?
> 1

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

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Process Equipment and Plant Design
Value of Peclet number = ∞, is the representative of

Laminar flow
Eddy diffusivity = 0
Complete back mixing
Plug flow

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