My Cart
Your Cart 0

    Your cart is empty.

  • Total (Amount) ₹0.00
Previous year question hub

Equipment Design and Optimization - Plant Design and Economics - Chemical Engineering Previous Year Questions

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

6Papers
6Years
6Questions
1Topics

Equipment Design and Optimization question pattern

Every graph below is calculated only from this selection.

Questions by year

Compare question counts across years.

Difficulty distribution

How the classified questions are distributed by difficulty.

Easy 4 66.7%
Medium 2 33.3%

Question type distribution

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

MCQ 4 66.7%
Numerical Answer Type (NAT) 2 33.3%

Subject weightage

Top subjects by unique question coverage.

Chemical Engineering
6 Qs

Most asked topics

Top topics across the included previous year papers.

Plant Design and Economics
6 Qs

Subtopic coverage

Top subtopics inside this exact selection.

Equipment Design and Optimization
6 Qs

Paper coverage

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

Chemical Engineering (CH) 2021
1 Qs
Chemical Engineering (CH) 2017
1 Qs
Chemical Engineering (CH) 2016
1 Qs
Chemical Engineering (CH) 2011
1 Qs
Chemical Engineering (CH) 2010
1 Qs
Chemical Engineering (CH) 2007
1 Qs

Included previous year papers

Newest papers appear first. Search these papers or sort by year and name.

Paper nameYearPDFAttempt
Chemical Engineering (CH) 20212021
1 questions in this view
2021
Chemical Engineering (CH) 20172017
1 questions in this view
2017
Chemical Engineering (CH) 20162016
1 questions in this view
2016
Chemical Engineering (CH) 20112011
1 questions in this view
2011
Chemical Engineering (CH) 20102010
1 questions in this view
2010
Chemical Engineering (CH) 20072007
1 questions in this view
2007

All Equipment Design and Optimization previous year questions

Practice every matching question in batches of 20, 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,

Open complete paper
2
2010 · Chemical Engineering · Plant Design and Economics · Equipment Design and Optimization
Chemical Engineering (CH) 2010

The term, knuckle radius, is associated with

Open complete paper
3
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
Open complete paper
4
2016 · Chemical Engineering · Plant Design and Economics · Equipment Design and Optimization
Chemical Engineering (CH) 2016
A vertical cylindrical tank with a flat roof and bottom is to be constructed for storing 150 m³ of ethylene glycol. The cost of material and fabrication for the tank wall is Rs 6000 per m² and the same for the roof and the tank bottom are Rs 2000 and Rs 4000 per m², respectively. The cost of accessories, piping and instruments can be taken as 10% of the cost of the wall. 10% of the volume of the tank needs to be kept free as vapour space above the liquid storage. What is the optimum diameter (in m) for the tank?
Open complete paper
5
2017 · Chemical Engineering · Plant Design and Economics · Equipment Design and Optimization
Chemical Engineering (CH) 2017
The total cost (C_T) of an equipment in terms of the operating variables x and y is
\[ C_T = 2x + \frac{12000}{xy} + y + 5 \]
The optimal value of C_T, rounded to 1 decimal place, is ______.
Open complete paper
6
2021 · Chemical Engineering · Plant Design and Economics · Equipment Design and Optimization
Chemical Engineering (CH) 2021
A viscous liquid is pumped through a pipe network in a chemical plant.
The annual pumping cost per unit length of pipe is given by
C_pump = 48.13 q² μ / D⁴
The annual cost of the installed piping system per unit length of pipe is given by
C_piping = 45.92D
Here, D is the inner diameter of the pipe in meter, q is the volumetric flowrate of the liquid in m³ s⁻¹ and μ is the viscosity of the liquid in Pa.s.
If the viscosity of the liquid is 20 × 10⁻³ Pa.s and the volumetric flow rate of the liquid is 10⁻³ m³ s⁻¹, the economic inner diameter of the pipe is _______ meter (round off to 3 decimal places).
Open complete paper