Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor
Multi-objective optimization (MOO) of low-density polyethylene (LDPE) production in a tubular reactor is performed for three problems with three different objectives. For the first problem, the objective is maximization of productivity and minimization of cost of initiators. For the second problem,...
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my.utm.1065162024-07-09T06:25:40Z http://eprints.utm.my/106516/ Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor Rohman, Fakhrony Sholahudin Idris, Iylia Muhammad, Dinie Wan Alwi, Sharifah Rafidah Zahan, Khairul Azly Murat, Muhamad Nazri Azmi, Ashraf Q Science (General) TP Chemical technology Multi-objective optimization (MOO) of low-density polyethylene (LDPE) production in a tubular reactor is performed for three problems with three different objectives. For the first problem, the objective is maximization of productivity and minimization of cost of initiators. For the second problem, the objective is maximization of conversion and minimization of cost of initiators. While for the third problem, the objective is maximization of productivity, minimization of cost of initiators, and maximization of conversion. An inequality constraint on reactor temperature is also enforced to prevent the tubular reactor from a runaway condition. The non-dominated sorting–based strategies are utilized to tackle the optimization problem with Aspen simulator as model-based optimization for LDPE production in a tubular reactor. The strategies are non-dominated sorting genetic algorithm II (NSGA-II), non-dominated sorting grey wolf optimizer (NSGWO), and non-dominated sorting whale optimization algorithm (NSWOA). The inputs for MOO decision variables are mass flowrates of tert-butyl peroxypivalate (TBPPI), tert-butyl peroxyacetate (TBPA), tert-butyl 3,5,5 trimethyl-peroxyhexaonate (TBPIN), and tert-amyl peroxyacetate (TAPA). Performance matrices like hypervolume, spacing, and pure variability are examined to choose the most effective MOO approach. Findings showed that the NSGWO is the most effective MOO approach due to the discovered solution set providing the most precise, diverse, and appropriate in the homogeneity allocation points along the Pareto front (PF). The highest productivity, lowest cost of initiators, and highest conversion obtained by NSGWO are 549.369 Mil. RM/year, 7.5589 Mil. RM/year, and 31.685%, respectively. Springer Nature 2023-11 Article PeerReviewed Rohman, Fakhrony Sholahudin and Idris, Iylia and Muhammad, Dinie and Wan Alwi, Sharifah Rafidah and Zahan, Khairul Azly and Murat, Muhamad Nazri and Azmi, Ashraf (2023) Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor. Process Integration and Optimization for Sustainability, 7 (5). pp. 1131-1148. ISSN 2509-4238 http://dx.doi.org/10.1007/s41660-023-00332-z DOI:10.1007/s41660-023-00332-z |
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Q Science (General) TP Chemical technology Rohman, Fakhrony Sholahudin Idris, Iylia Muhammad, Dinie Wan Alwi, Sharifah Rafidah Zahan, Khairul Azly Murat, Muhamad Nazri Azmi, Ashraf Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor |
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Multi-objective optimization (MOO) of low-density polyethylene (LDPE) production in a tubular reactor is performed for three problems with three different objectives. For the first problem, the objective is maximization of productivity and minimization of cost of initiators. For the second problem, the objective is maximization of conversion and minimization of cost of initiators. While for the third problem, the objective is maximization of productivity, minimization of cost of initiators, and maximization of conversion. An inequality constraint on reactor temperature is also enforced to prevent the tubular reactor from a runaway condition. The non-dominated sorting–based strategies are utilized to tackle the optimization problem with Aspen simulator as model-based optimization for LDPE production in a tubular reactor. The strategies are non-dominated sorting genetic algorithm II (NSGA-II), non-dominated sorting grey wolf optimizer (NSGWO), and non-dominated sorting whale optimization algorithm (NSWOA). The inputs for MOO decision variables are mass flowrates of tert-butyl peroxypivalate (TBPPI), tert-butyl peroxyacetate (TBPA), tert-butyl 3,5,5 trimethyl-peroxyhexaonate (TBPIN), and tert-amyl peroxyacetate (TAPA). Performance matrices like hypervolume, spacing, and pure variability are examined to choose the most effective MOO approach. Findings showed that the NSGWO is the most effective MOO approach due to the discovered solution set providing the most precise, diverse, and appropriate in the homogeneity allocation points along the Pareto front (PF). The highest productivity, lowest cost of initiators, and highest conversion obtained by NSGWO are 549.369 Mil. RM/year, 7.5589 Mil. RM/year, and 31.685%, respectively. |
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Article |
author |
Rohman, Fakhrony Sholahudin Idris, Iylia Muhammad, Dinie Wan Alwi, Sharifah Rafidah Zahan, Khairul Azly Murat, Muhamad Nazri Azmi, Ashraf |
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Rohman, Fakhrony Sholahudin Idris, Iylia Muhammad, Dinie Wan Alwi, Sharifah Rafidah Zahan, Khairul Azly Murat, Muhamad Nazri Azmi, Ashraf |
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Rohman, Fakhrony Sholahudin |
title |
Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor |
title_short |
Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor |
title_full |
Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor |
title_fullStr |
Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor |
title_full_unstemmed |
Non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor |
title_sort |
non-dominated sorting-based strategy for optimizing the mixture of initiators in polyethylene reactor |
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Springer Nature |
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2023 |
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http://eprints.utm.my/106516/ http://dx.doi.org/10.1007/s41660-023-00332-z |
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