Difficulty distribution
How the classified questions are distributed by difficulty.
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Practice Instrumentation and Process Control - Chemical Engineering previous year questions organised from real papers, with year-wise coverage and clear topic navigation.
Every graph below is calculated only from this selection.
Compare question counts across years.
How the classified questions are distributed by difficulty.
MCQ, numerical, multiple-select and other formats found in these papers.
Top subjects by unique question coverage.
Top topics across the included previous year papers.
Top subtopics inside this exact selection.
Question coverage for the most populated papers. Every active PYP paper remains listed below.
Open a focused page built from the same verified paper data.
Explore previous-paper coverage, trends and focused practice for Process Modelling and Dynamic Response.
Explore previous-paper coverage, trends and focused practice for Feedback Control and Stability.
Explore previous-paper coverage, trends and focused practice for Process Measurements and Instrumentation.
Explore previous-paper coverage, trends and focused practice for Controller Tuning and Advanced Control.
Newest papers appear first. Search these papers or sort by year and name.
| Paper name | Year | Attempt | |
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Chemical Engineering (CH) 20262026 | 2026 |
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Chemical Engineering (CH) 20252025 | 2025 | |
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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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A varied preview from the papers represented in this selection, with every available option.
An operator was told to control the temperature of a reactor at 60 °C. The operator set the set-point of the temperature controller at 60. The scale actually indicated 0 to 100% of a temperature range of 0 to 200 °C. This caused a runaway reaction by over-pressurizing the vessel, which resulted in injury to the operator. The actual set-point temperature was
| GROUP I | GROUP II |
|---|---|
| P. Flame temperature Q. Composition of LPG R. Liquid air temperature | I. Thermocouple II. Radiation pyrometer III. Gas chromatograph |