Chemical Engineering
GATE CH format:mcq PYQs
Build your understanding with focused practice from past exam papers.
Questions 321–330 of 378. Imported answers require independent review unless marked reviewed.
Question 8
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Segmental baffles in a 2-4 shell and tube heat exchanger
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In connection with petroleum refining, identify the incorrect statement among the following options.
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Polyvinyl chloride is produced by
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The molecular formula of the predominant chemical compound in commercial sugar is
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Two packed towers are designed for the same mass velocity of the gas. The first has liquid and gas flow rates of 30 kg/s and 1.2 kg/s, respectively, while the corresponding flow rates in the second tower are 67.5 kg/s and 1.8 kg/s. The ratio of the design diameter of the wider tower to that of the narrower tower is
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The Annual Fixed Charges (AFC) and Annual Utilities Costs (AUC) of a distillation column being designed are expressed in terms of the reflux ratio (R) as
The reflux ratio (
) for optimizing the total cost of the distillation column may be found by solvingYour answerChoose one option.
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Consider the following properties:
(P) temperature
(Q) specific gravity
(R) chemical potential
(S) volume
The option which lists ALL the intensive properties is
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Liquid phase isomerization of o-xylene to p-xylene using a zeolite catalyst was carried out in a CSTR. Three sets of kinetic data at different temperatures and stirring speeds were obtained as shown below.
| set A | | | set B | | | set C | | |
|---|---|---|---|---|---|---|---|---|---|
temperature (K) | 500 | 500 | 500 | 600 | 600 | 600 | 700 | 700 | 700 |
stirring speed (rpm) | 1000 | 2000 | 3000 | 1000 | 2000 | 3000 | 1000 | 2000 | 3000 |
reaction rate (mol L⁻¹ s⁻¹) | 0.020 | 0.025 | 0.025 | 0.037 | 0.047 | 0.047 | 0.069 | 0.078 | 0.086 |
The operating condition at which the reaction rate is not controlled by external mass transfer resistance is
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Choose the correct statement
In viscose rayon manufacturing process,
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The reactant (M) is converted into product (N) in the presence of catalyst in a fixed bed reactor. All the flow rates (F, G, H, P and R) in mol/s, and mole fraction of reactant (M) in these streams (x_F, x_G, x_H, x_P and x_R) are shown in the diagram.

The overall fractional conversion is
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