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Mass Transfer

Mass Transfer
Leaching of coarse solid lumps is also termed as

Decoction
Agitation and settling
Dissolution
Percolation

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Mass Transfer
H₂S is being absorbed in a gas absorber unit. The height of the transfer unit based on the overall mass transfer coefficient on the gas side is 0.4 m. The equilibrium data is given by, y = 1.5 x. The bulk concentration of H₂S has to be reduced from 0.05 to 0.001 mole fraction in the gas side. The height of the tower (in metres) corresponding to an operating line given by, y = 5x + 0.001 is

2
1.56
0.56
1

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Mass Transfer
If G = insoluble gas in gas stream and L = non-volatile solvent in liquid stream, then the slope of the operating line for the absorber is

Always < 1
G/L
None of these
L/G

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Mass Transfer
The binary diffusivity in gases and liquids vary respectively as

T3/2 and √T
T and T3/2
√T and T3/2
T3/2 and T

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Mass Transfer
The operating cost of a distillation column at minimum reflux ratio is

Infinite
Zero
Maximum
Minimum

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Mass Transfer
Lewis number (Le) is

St x Sh
Sh x Pr
Pr x St
Sc x Pr

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