Temperature control of a non-isothermal CSTR at the unstable region using PID mode

This study aim isto test the control of a continuous stirred-tank reactor (CSTR) using PID mode of control with suppressed over-shooting feature at the unstable region of the multiple steady-state behavior exhibited by the test reactants, sodium thiosulfate and hydrogen peroxide. The experimentation...

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Main Authors: Go, Jonathan, Gobaco, Mario, Ha, Christopher
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Language:English
Published: Animo Repository 1995
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Online Access:https://animorepository.dlsu.edu.ph/etd_bachelors/9284
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Institution: De La Salle University
Language: English
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spelling oai:animorepository.dlsu.edu.ph:etd_bachelors-99292021-09-02T02:01:09Z Temperature control of a non-isothermal CSTR at the unstable region using PID mode Go, Jonathan Gobaco, Mario Ha, Christopher This study aim isto test the control of a continuous stirred-tank reactor (CSTR) using PID mode of control with suppressed over-shooting feature at the unstable region of the multiple steady-state behavior exhibited by the test reactants, sodium thiosulfate and hydrogen peroxide. The experimentation includes the verification, by actual testing, the multiple steady-state behavior exhibited by the laboratory-scale CSTR.Experimental data were obtained by taking samples from the CSTR at every steady-state operating point or controlled region in order to determine the conversion at that point. Temperature readings at important spots such as the inlet and outlet were also taken. These values were then plotted to determine the regions of steady and unsteady-state. Control of the reactor at the unsteady-state temperature was effected by admitting cooling water into the jacket surrounding the CSTR to remove any excess heat of reaction that will cause a rise in reaction temperature. The flow rate of the cooling water was varied with the use of a proportional valve which is driven by an electronic actuator. This actuator was regulated by the PID controller to which it was connected.The action of the controller was such that the reactor temperature will not exceed the set point but will approach it from time to time. Results showed that an S-shaped curve could be obtained when data for temperature rise is plotted against residence time. The unsteady-state temperature was taken from the sum of the midpoint of that S-curve and the average inlet temperature. The PID controller was able to control the temperature with +2 and -3 centigrade deviations from the set point. It was also able to control the temperature at the set point for a maximum of 18 minutes and 16.93 seconds. 1995-01-01T08:00:00Z text https://animorepository.dlsu.edu.ph/etd_bachelors/9284 Bachelor's Theses English Animo Repository Temperature control Tanks Chemical processes Chemical reactions Chemical Engineering
institution De La Salle University
building De La Salle University Library
continent Asia
country Philippines
Philippines
content_provider De La Salle University Library
collection DLSU Institutional Repository
language English
topic Temperature control
Tanks
Chemical processes
Chemical reactions
Chemical Engineering
spellingShingle Temperature control
Tanks
Chemical processes
Chemical reactions
Chemical Engineering
Go, Jonathan
Gobaco, Mario
Ha, Christopher
Temperature control of a non-isothermal CSTR at the unstable region using PID mode
description This study aim isto test the control of a continuous stirred-tank reactor (CSTR) using PID mode of control with suppressed over-shooting feature at the unstable region of the multiple steady-state behavior exhibited by the test reactants, sodium thiosulfate and hydrogen peroxide. The experimentation includes the verification, by actual testing, the multiple steady-state behavior exhibited by the laboratory-scale CSTR.Experimental data were obtained by taking samples from the CSTR at every steady-state operating point or controlled region in order to determine the conversion at that point. Temperature readings at important spots such as the inlet and outlet were also taken. These values were then plotted to determine the regions of steady and unsteady-state. Control of the reactor at the unsteady-state temperature was effected by admitting cooling water into the jacket surrounding the CSTR to remove any excess heat of reaction that will cause a rise in reaction temperature. The flow rate of the cooling water was varied with the use of a proportional valve which is driven by an electronic actuator. This actuator was regulated by the PID controller to which it was connected.The action of the controller was such that the reactor temperature will not exceed the set point but will approach it from time to time. Results showed that an S-shaped curve could be obtained when data for temperature rise is plotted against residence time. The unsteady-state temperature was taken from the sum of the midpoint of that S-curve and the average inlet temperature. The PID controller was able to control the temperature with +2 and -3 centigrade deviations from the set point. It was also able to control the temperature at the set point for a maximum of 18 minutes and 16.93 seconds.
format text
author Go, Jonathan
Gobaco, Mario
Ha, Christopher
author_facet Go, Jonathan
Gobaco, Mario
Ha, Christopher
author_sort Go, Jonathan
title Temperature control of a non-isothermal CSTR at the unstable region using PID mode
title_short Temperature control of a non-isothermal CSTR at the unstable region using PID mode
title_full Temperature control of a non-isothermal CSTR at the unstable region using PID mode
title_fullStr Temperature control of a non-isothermal CSTR at the unstable region using PID mode
title_full_unstemmed Temperature control of a non-isothermal CSTR at the unstable region using PID mode
title_sort temperature control of a non-isothermal cstr at the unstable region using pid mode
publisher Animo Repository
publishDate 1995
url https://animorepository.dlsu.edu.ph/etd_bachelors/9284
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