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Mass Transfer

Mass Transfer
Tea percolation employs

Absorption
Leaching
Liquid-liquid extraction
None of these

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Mass Transfer
Small dia distillation column can be a

Sieve tray
Packed column
Any of these
Bubble cap

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Mass Transfer
In distillation where q is defined as the moles of liquid flow in the stripping section per mole of feed introduced, for saturated liquid feed

q = 1
q > 1
q < 1
q = 0

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Mass Transfer
Acetone is to be removed from air in an isothermal dilute absorber using pure water as solvent. The incoming air contains 5 mole% of acetone (yin = 0.05). The design equation to be used for obtaining the number of trays (N) of the absorber is, N+2 = 6 log (yin/yout).For 98% recovery of acetone, the number of trays required is/are

1
9
8
10

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Mass Transfer
On moving the feed line (q-line) from saturated liquid feed (vertical position) to saturated vapor feed (horizontal feed), if the slope of both the operating lines are to be increased, then it will result in

Increased reboiler load
Increased reflux ratio
Greater degree of separation with a fixed number of trays
None of these

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Mass Transfer
In stripping section of continuous distillation column, the

Liquid is stripped of high boiler
None of these
Vapour is stripped of low boiler
Liquid is enriched with high boiler

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