Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production

Ethylene glycol (EG) is a valuable commodity organic intermediate that is produced using the catalyzed gas-phase hydrogenation process of dimethyl oxalate (DMO) from syngas. The reactor process is challenging to control because of its nonlinearity and multivariable condition. Thus, this study propos...

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Published in:Chemical Product and Process Modeling
Main Author: Rohman F.S.; Wan Alwi S.R.; Muhammad D.; Azmi A.; Murat M.N.
Format: Article
Language:English
Published: Walter de Gruyter GmbH 2024
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85209382229&doi=10.1515%2fcppm-2024-0025&partnerID=40&md5=24bd0742816f74bd838173db47b928d1
id 2-s2.0-85209382229
spelling 2-s2.0-85209382229
Rohman F.S.; Wan Alwi S.R.; Muhammad D.; Azmi A.; Murat M.N.
Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
2024
Chemical Product and Process Modeling
19
5
10.1515/cppm-2024-0025
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85209382229&doi=10.1515%2fcppm-2024-0025&partnerID=40&md5=24bd0742816f74bd838173db47b928d1
Ethylene glycol (EG) is a valuable commodity organic intermediate that is produced using the catalyzed gas-phase hydrogenation process of dimethyl oxalate (DMO) from syngas. The reactor process is challenging to control because of its nonlinearity and multivariable condition. Thus, this study proposes the application of Neural Wiener model predictive control (NWMPC) for DMO hydrogenation reactor control. The application of empirical-based MPC, such as NWMPC, is still new in DMO hydrogenation reactor control. In order to simulate the process, the DMO hydrogenation reactor is modeled using Aspen Plus and Aspen Dynamic software. The Neural Wiener (NW) model is developed based on state space and neural network modeling using a Linear-Nonlinear (L-N) identification approach. A validation test is also performed to verify the accuracy of the NW model. Based on the test, the model accuracy is acceptable with the coefficient of determination (R2) of 0.965 for EG output mole fraction (first output) and R2 of 0.936 for product temperature (second output). The NWMPC capability is evaluated with a PID controller to handle a setpoint change in EG output mole fraction and reject disturbance in the feed stream flow rate. The control performance results have demonstrated the superior ability of the NWMPC to handle such scenarios better than PID in terms of controller action speed and profile. © 2024 Walter de Gruyter GmbH, Berlin/Boston.
Walter de Gruyter GmbH
19342659
English
Article

author Rohman F.S.; Wan Alwi S.R.; Muhammad D.; Azmi A.; Murat M.N.
spellingShingle Rohman F.S.; Wan Alwi S.R.; Muhammad D.; Azmi A.; Murat M.N.
Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
author_facet Rohman F.S.; Wan Alwi S.R.; Muhammad D.; Azmi A.; Murat M.N.
author_sort Rohman F.S.; Wan Alwi S.R.; Muhammad D.; Azmi A.; Murat M.N.
title Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
title_short Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
title_full Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
title_fullStr Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
title_full_unstemmed Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
title_sort Nonlinear model predictive controller of hydrogenation of dimethyl oxalate for ethylene glycol production
publishDate 2024
container_title Chemical Product and Process Modeling
container_volume 19
container_issue 5
doi_str_mv 10.1515/cppm-2024-0025
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85209382229&doi=10.1515%2fcppm-2024-0025&partnerID=40&md5=24bd0742816f74bd838173db47b928d1
description Ethylene glycol (EG) is a valuable commodity organic intermediate that is produced using the catalyzed gas-phase hydrogenation process of dimethyl oxalate (DMO) from syngas. The reactor process is challenging to control because of its nonlinearity and multivariable condition. Thus, this study proposes the application of Neural Wiener model predictive control (NWMPC) for DMO hydrogenation reactor control. The application of empirical-based MPC, such as NWMPC, is still new in DMO hydrogenation reactor control. In order to simulate the process, the DMO hydrogenation reactor is modeled using Aspen Plus and Aspen Dynamic software. The Neural Wiener (NW) model is developed based on state space and neural network modeling using a Linear-Nonlinear (L-N) identification approach. A validation test is also performed to verify the accuracy of the NW model. Based on the test, the model accuracy is acceptable with the coefficient of determination (R2) of 0.965 for EG output mole fraction (first output) and R2 of 0.936 for product temperature (second output). The NWMPC capability is evaluated with a PID controller to handle a setpoint change in EG output mole fraction and reject disturbance in the feed stream flow rate. The control performance results have demonstrated the superior ability of the NWMPC to handle such scenarios better than PID in terms of controller action speed and profile. © 2024 Walter de Gruyter GmbH, Berlin/Boston.
publisher Walter de Gruyter GmbH
issn 19342659
language English
format Article
accesstype
record_format scopus
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