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Previous year question hub

Plant Design and Economics - Chemical Engineering Previous Year Questions

Practice Plant Design and Economics - Chemical Engineering previous year questions organised from real papers, with year-wise coverage and clear topic navigation.

18Papers
18Years
42Questions
1Topics

Plant Design and Economics question pattern

Every graph below is calculated only from this selection.

Questions by year

Year-wise coverage for Plant Design and Economics. Each bar uses a separate theme-derived color.

Difficulty distribution

How the classified questions are distributed by difficulty.

Easy 28 66.7%
Medium 14 33.3%

Question type distribution

MCQ, numerical, multiple-select and other formats found in these papers.

MCQ 24 57.1%
Numerical Answer Type (NAT) 15 35.7%
Fill in the blanks 2 4.8%
MSQ 1 2.4%

Subject weightage

Top subjects by unique question coverage.

Chemical Engineering
42 Qs

Most asked topics

Top topics across the included previous year papers.

Plant Design and Economics
42 Qs

Subtopic coverage

Top subtopics inside this exact selection.

Process Economics and Cost Estimation
37 Qs
Equipment Design and Optimization
5 Qs

Paper coverage

Question coverage for the most populated papers. Every active PYP paper remains listed below.

Chemical Engineering (CH) 2026
2 Qs
Chemical Engineering (CH) 2025
2 Qs
Chemical Engineering (CH) 2024
1 Qs
Chemical Engineering (CH) 2023
2 Qs
Chemical Engineering (CH) 2022
3 Qs
Chemical Engineering (CH) 2021
4 Qs
Chemical Engineering (CH) 2020
1 Qs
Chemical Engineering (CH) 2019
2 Qs
Chemical Engineering (CH) 2018
3 Qs
Chemical Engineering (CH) 2017
2 Qs
Chemical Engineering (CH) 2014
2 Qs
Chemical Engineering (CH) 2013
2 Qs
Chemical Engineering (CH) 2012
3 Qs
Chemical Engineering (CH) 2011
4 Qs
Chemical Engineering (CH) 2010
4 Qs
Chemical Engineering (CH) 2009
2 Qs
Chemical Engineering (CH) 2008
2 Qs
Chemical Engineering (CH) 2007
1 Qs

Browse by subtopics

Open a focused page built from the same verified paper data.

Included previous year papers

Newest papers appear first. Sort by year, question coverage or name.

PaperYear / sessionQuestions in this viewOpen
Chemical Engineering (CH) 202620262View paper
Chemical Engineering (CH) 202520252View paper
Chemical Engineering (CH) 202420241View paper
Chemical Engineering (CH) 202320232View paper
Chemical Engineering (CH) 202220223View paper
Chemical Engineering (CH) 202120214View paper
Chemical Engineering (CH) 202020201View paper
Chemical Engineering (CH) 201920192View paper
Chemical Engineering (CH) 201820183View paper
Chemical Engineering (CH) 201720172View paper
Chemical Engineering (CH) 201420142View paper
Chemical Engineering (CH) 201320132View paper
Chemical Engineering (CH) 201220123View paper
Chemical Engineering (CH) 201120114View paper
Chemical Engineering (CH) 201020104View paper
Chemical Engineering (CH) 200920092View paper
Chemical Engineering (CH) 200820082View paper
Chemical Engineering (CH) 200720071View paper

Sample previous year questions

A varied preview from the papers represented in this selection, with every available option.

1
2007 · Chemical Engineering · Plant Design and Economics · Equipment Design and Optimization
Chemical Engineering (CH) 2007

A cylindrical storage tank can have a self supported conical roof,

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2
2008 · Chemical Engineering · Plant Design and Economics · Process Economics and Cost Estimation
Chemical Engineering (CH) 2008

For the case of single lump-sum capital expenditure of Rs. 10 crores which generates a constant annual cash flow of Rs. 2 crores in each subsequent year, the payback period (in years), if the scrap value of the capital outlay is zero is

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3
2009 · Chemical Engineering · Plant Design and Economics · Process Economics and Cost Estimation
Chemical Engineering (CH) 2009

The total fixed cost of a chemical plant is Rs. 10.0 lakhs; the internal rate of return is 15%, and the annual operating cost is Rs. 2.0 lakhs. The annualized cost of the plant (in lakhs of Rs.) is

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4
2010 · Chemical Engineering · Plant Design and Economics · Equipment Design and Optimization
Chemical Engineering (CH) 2010

The term, knuckle radius, is associated with

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5
2011 · Chemical Engineering · Plant Design and Economics · Equipment Design and Optimization
Chemical Engineering (CH) 2011
Minimum input required to calculate the ‘blank diameter’ for a torispherical head is
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6
2012 · Chemical Engineering · Plant Design and Economics · Process Economics and Cost Estimation
Chemical Engineering (CH) 2012
A batch reactor produces \(1 \times 10^7\) kg of a product per year. The total batch time (in hours) of the reactor is \(k \sqrt{P_B}\), where \(P_B\) is the product per batch in kg and \(k = 1.0\) h/\(\sqrt{kg}\). The operating cost of the reactor is Rs. 200/h. The total annual fixed charges are Rs. \(340 \times P_B\) and the annual raw material cost is Rs. \(2 \times 10^6\). The optimum size (in kg) of each batch (adjusted to the nearest integer) is
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