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Previous year question hub

Particle Size Reduction and Classification - Fluid Mechanics and Mechanical Operations - Chemical Engineering Previous Year Questions

Practice Particle Size Reduction and Classification - Fluid Mechanics and Mechanical Operations - Chemical Engineering previous year questions organised from real papers, with year-wise coverage and clear topic navigation.

10Papers
10Years
16Questions
1Topics

Particle Size Reduction and Classification question pattern

Every graph below is calculated only from this selection.

Questions by year

Year-wise coverage for Particle Size Reduction and Classification. Each bar uses a separate theme-derived color.

Difficulty distribution

How the classified questions are distributed by difficulty.

Easy 12 75%
Medium 4 25%

Question type distribution

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

MCQ 14 87.5%
Fill in the blanks 1 6.3%
Numerical Answer Type (NAT) 1 6.3%

Subject weightage

Top subjects by unique question coverage.

Chemical Engineering
16 Qs

Most asked topics

Top topics across the included previous year papers.

Fluid Mechanics and Mechanical Operations
16 Qs

Subtopic coverage

Top subtopics inside this exact selection.

Particle Size Reduction and Classification
16 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
1 Qs
Chemical Engineering (CH) 2019
1 Qs
Chemical Engineering (CH) 2018
2 Qs
Chemical Engineering (CH) 2017
2 Qs
Chemical Engineering (CH) 2014
1 Qs
Chemical Engineering (CH) 2013
2 Qs
Chemical Engineering (CH) 2010
1 Qs
Chemical Engineering (CH) 2008
1 Qs
Chemical Engineering (CH) 2007
3 Qs

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) 202520251View paper
Chemical Engineering (CH) 201920191View paper
Chemical Engineering (CH) 201820182View paper
Chemical Engineering (CH) 201720172View paper
Chemical Engineering (CH) 201420141View paper
Chemical Engineering (CH) 201320132View paper
Chemical Engineering (CH) 201020101View paper
Chemical Engineering (CH) 200820081View paper
Chemical Engineering (CH) 200720073View paper

All Particle Size Reduction and Classification previous year questions

Practice every matching question in batches of 20, with every available option.

1
2007 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2007

In Tyler series, the ratio of the aperture size of a screen to that of the next smaller screen is

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2
2007 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2007

Size reduction of coarse hard solids using a crusher is accomplished by

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3
2007 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2007

Sticky materials are transported by

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4
2008 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2008
Q.14 The power required for size reduction in crushing is
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5
2010 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2010
The critical speed (revolutions per unit time) of a ball mill of radius R, which uses balls of radius r, is
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6
2013 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2013

In the Tyler standard screen scale series, when the mesh number increases from 3 mesh to 10 mesh, then

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7
2013 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2013
100 ton/h of a rock feed, of which 80% passed through a mesh size of 2.54 mm, were reduced in size such that 80% of the crushed product passed through a mesh size of 1.27 mm. The power consumption was 100 kW. If 100 ton/h of the same material is similarly crushed from a mesh size of 5.08 mm to a mesh size of 2.54 mm, the power consumption (in kW, to the nearest integer) using Bond's law, is ______
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8
2014 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2014
In order to produce fine solid particles between 5 and 10 \(\mu m\), the appropriate size reducing equipment is
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9
2017 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2017
Which of the following is the correct sequence of equipment for size reduction of solids?
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10
2017 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2017
Size analysis was carried out on a sample of gravel. The data for mass fraction (\( x_i \)) and average particle diameter (\( D_{pi} \)) of the fraction is given in the table below:
\( x_i \)\( D_{pi} \) (mm)
0.25
0.410
0.420

The mass mean diameter of the sample, to the nearest integer, is ______ mm.
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11
2018 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2018

Critical speed of a ball mill depends on

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12
2018 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2018
Match the equipment in Column A with the corresponding process in Column B

Question diagram

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13
2019 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2019
Consider a cylinder (diameter \( D \) and length \( D \)), a sphere (diameter \( D \)) and a cube (side length \( D \)). Which of the following statements concerning the sphericity (\( \Phi \)) of the above objects is true:
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14
2025 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2025
A catalyst particle is modeled as a symmetrical double cone solid as shown in the figure. For each conical sub-part, the radius of the base is \( r \) and the height is \( h \). The sphericity of the particle is given by

Question diagram

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15
2026 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2026

Which one of the following is NOT a type of chain conveyor?

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16
2026 · Chemical Engineering · Fluid Mechanics and Mechanical Operations · Particle Size Reduction and Classification
Chemical Engineering (CH) 2026
The gross energy requirement, to reduce a very large feed of coal to such a size that 80% of the product passes through a 100 μm screen, is 13 kWh per ton of feed. In a process, 250 tons \( h^{-1} \) of coal is crushed. The range of feed sizes is such that 80% of the feed passes through an opening of 100 mm. The product size range is to be such that 80% of the product passes through an opening of 25 mm. According to the Bond’s law, which one of the following is the power consumption (in kW)?
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