Chemical Engineering
GATE CH Mass Transfer PYQs
Build your understanding with focused practice from past exam papers.
Questions 71–77 of 77. Imported answers require independent review unless marked reviewed.
Question 14
Open questionCHMCQ1 markNeeds review
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
Your answerChoose one option.
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Open questionCHNAT1 markNeeds review
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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Open questionCHMCQ1 markNeeds review
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
Your answerChoose one option.
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You can attempt this question now. Sign in to view the answer key, explanations and discussion.Log in to check answerQuestion 42
Open questionCHNAT2 marksNeeds review
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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Open questionCHMCQ2 marksNeeds review
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, isYour answerChoose one option.
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Open questionCHNAT2 marksNeeds review
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.

The MINIMUM flowrate of pure steam for this process, rounded to 1 decimal place, is ______ mol/s.
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You can attempt this question now. Sign in to view the answer key, explanations and discussion.Log in to check answerQuestion 45
Open questionCHNAT2 marksNeeds review
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.Log in to check the answer
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