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Practice Distillation and Absorption - Mass Transfer - Chemical Engineering previous year questions organised from real papers, with year-wise coverage and clear topic navigation.
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| Paper name | Year | Attempt | |
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Chemical Engineering (CH) 20262026 | 2026 |
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Chemical Engineering (CH) 20242024 | 2024 | |
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Chemical Engineering (CH) 20232023 | 2023 | |
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Chemical Engineering (CH) 20222022 | 2022 | |
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Chemical Engineering (CH) 20212021 | 2021 | |
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Chemical Engineering (CH) 20202020 | 2020 | |
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Chemical Engineering (CH) 20192019 | 2019 | |
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Chemical Engineering (CH) 20182018 | 2018 | |
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Chemical Engineering (CH) 20172017 | 2017 | |
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Chemical Engineering (CH) 20162016 | 2016 | |
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Chemical Engineering (CH) 20142014 | 2014 | |
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Chemical Engineering (CH) 20132013 | 2013 | |
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Chemical Engineering (CH) 20122012 | 2012 | |
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Chemical Engineering (CH) 20112011 | 2011 | |
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Chemical Engineering (CH) 20102010 | 2010 | |
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Chemical Engineering (CH) 20092009 | 2009 | |
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Chemical Engineering (CH) 20082008 | 2008 | |
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Chemical Engineering (CH) 20072007 | 2007 | |
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Practice every matching question in batches of 20, with every available option.

In a binary mixture containing components A and B, the relative volatility of A with respect to B is 2.5 when mole fractions are used. The molecular weights of A and B are 78 and 92 respectively. If the compositions are however expressed in mass fractions the relative volatility will then be
An ideal flash vaporization is carried out with a binary mixture at constant temperature and pressure. A process upset leads to an increase in the mole fraction of the heavy component in the feed. The flash vessel continues to operate at the previous temperature and pressure and still produces liquid and vapor. After steady state is re-established,
A batch distillation operation is carried out to separate a feed containing 100 moles of a binary mixture of A and B. The mole fraction of A in the feed is 0.7. The distillation progresses until the mole fraction of A in the residue decreases to 0.6. The equilibrium curve in this composition range may be linearized to y* = 0.7353 x + 0.3088. Here x and y are the mole fractions of the more volatile component A in the liquid and vapor phases respectively. The number of moles of residue is
The feed to a binary distillation column has 40 mol % vapor and 60 mol % liquid. Then, the slope of the q-line in the McCabe-Thiele plot is
| Component | \(K_i\) |
|---|---|
| 1 | 6 |
| 2 | 3 |
| 3 | 2.5 |
| 4 | 1.1 |

The flooding velocity in a plate column, operating at 1 atm pressure, is 3 m/s. If the column is operated at 2 atm pressure, under otherwise identical conditions, the flooding velocity will be
An equimolar mixture of A and B (A being more volatile) is flash distilled continuously at a feed rate of 100 kmol/h, such that the liquid product contains 40 mol % of A. If the relative volatility is 6, then the vapor product, in kmol/h, is
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