Questions 71–77 of 77. Imported answers require independent review unless marked reviewed.

Topic practice 77 questionsPage 8 of 8

Question 14

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Which of the following conditions are valid at the plat point? P) Density difference between the extract and raffinate phases is zero Q) Interfacial tension between the extract and raffinate phases is zero R) Composition difference between the extract and raffinate phases is zero
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Question 15

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The composition of vapour entering a tray in a distillation column is 0.47. The average composition of the vapour leaving the tray is 0.53. The equilibrium composition of the vapour corresponding to the liquid leaving this tray is 0.52. All the compositions are expressed in mole fraction of the more volatile component.
The Murphree efficiency based on the vapour phase, rounded to the nearest integer, is ______ %.

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Question 16

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Consider steady state mass transfer of a solute A from a gas phase to a liquid phase. The gas phase bulk and interface mole fractions are

and

, respectively. The liquid phase bulk and interface mole fractions are

and

, respectively. The ratio

is very close to zero.
This implies that mass transfer resistance is
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Question 42

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The vapor phase composition and relative volatilities (with respect to n-propane) on an ideal tray of a distillation column are
Component
Methane
Ethane
n-Propane
Mole fraction in vapor
0.12
0.28
0.60
Relative volatility
10
4
1
The mole fraction of n-propane in the liquid phase, rounded to 2 decimal places, is ____________.

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Question 43

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The Sherwood number (

) correlation for laminar flow over a flat plate of length

is given by

where

and

represent Reynolds number and Schmidt number, respectively. This correlation, expressed in the form of Chilton-Colburn

factor, is
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Question 44

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In a countercurrent stripping operation using pure steam, the mole ratio of a solute in the liquid stream is reduced from 0.25 to 0.05. The liquid feed flowrate, on a solute-free basis, is 3 mol/s. The equilibrium line for the system is given in the figure below.
Diagram for Chemical Engineering question 44

The MINIMUM flowrate of pure steam for this process, rounded to 1 decimal place, is ______ mol/s.

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Question 45

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In a batch adsorption process, 5 g of fresh adsorbent is used to treat 1 liter of an aqueous phenol solution. The initial phenol concentration is 100 mg/liter. The equilibrium relation is given by

where

is the amount of phenol adsorbed in mg of phenol per gram of adsorbent, and

is the concentration of phenol in mg/liter in the aqueous solution. When equilibrium is attained between the adsorbent and the solution, the concentration of phenol in the solution, rounded to 1 decimal place, is __________ mg/liter.

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