Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in Distillation
Methanol is a chemical product that is widely applied in the chemical industry. The methanol production process from carbon dioxide and hydrogen uses a hydrogenation process with a continuous stirred tank reactor (CSTR) under controlled thermodynamic and kinetic conditions. The process was modified...
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Universitas Diponegoro
2025-06-01
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| Series: | Journal of Chemical Engineering Research Progress |
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| Online Access: | https://journal.bcrec.id/index.php/jcerp/article/view/20305 |
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| author | Chindaga Widya Verisna Munna Lissa'adah Nursatitah Nursatitah Zulfa Aulia |
| author_facet | Chindaga Widya Verisna Munna Lissa'adah Nursatitah Nursatitah Zulfa Aulia |
| author_sort | Chindaga Widya Verisna |
| collection | DOAJ |
| description | Methanol is a chemical product that is widely applied in the chemical industry. The methanol production process from carbon dioxide and hydrogen uses a hydrogenation process with a continuous stirred tank reactor (CSTR) under controlled thermodynamic and kinetic conditions. The process was modified by replacing the Gibbs reactor with a Continuous Stirred Tank Reactor (CSTR), adding temperature and pressure regulation, and a compressor. This study aims to increase the product yield obtained from the modification results and mass efficiency. Based on the experimental results, it can be concluded that the modified design is quite effective compared to before modification, because it increases the methanol product yield from 44.54% to 99.78%. Copyright © 2025 by Authors, Published by Universitas Diponegoro and BCREC Publishing Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0). |
| format | Article |
| id | doaj-art-566bb541e9bc487da0790dd5cb5cd127 |
| institution | Kabale University |
| issn | 3032-7059 |
| language | English |
| publishDate | 2025-06-01 |
| publisher | Universitas Diponegoro |
| record_format | Article |
| series | Journal of Chemical Engineering Research Progress |
| spelling | doaj-art-566bb541e9bc487da0790dd5cb5cd1272025-08-20T03:30:08ZengUniversitas DiponegoroJournal of Chemical Engineering Research Progress3032-70592025-06-0121869110.9767/jcerp.203058513Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in DistillationChindaga Widya Verisna0Munna Lissa'adah1Nursatitah Nursatitah2Zulfa Aulia3Departement of Chemical Engineering, Faculty of Engineering, Universitas Diponegoro, Jl. Prof. Sudarto, SH, Tembalang, Semarang, 50275, IndonesiaDepartement of Chemical Engineering, Faculty of Engineering, Universitas Diponegoro, Jl. Prof. Sudarto, SH, Tembalang, Semarang, 50275, IndonesiaDepartement of Chemical Engineering, Faculty of Engineering, Universitas Diponegoro, Jl. Prof. Sudarto, SH, Tembalang, Semarang, 50275, IndonesiaDepartement of Chemical Engineering, Faculty of Engineering, Universitas Diponegoro, Jl. Prof. Sudarto, SH, Tembalang, Semarang, 50275, IndonesiaMethanol is a chemical product that is widely applied in the chemical industry. The methanol production process from carbon dioxide and hydrogen uses a hydrogenation process with a continuous stirred tank reactor (CSTR) under controlled thermodynamic and kinetic conditions. The process was modified by replacing the Gibbs reactor with a Continuous Stirred Tank Reactor (CSTR), adding temperature and pressure regulation, and a compressor. This study aims to increase the product yield obtained from the modification results and mass efficiency. Based on the experimental results, it can be concluded that the modified design is quite effective compared to before modification, because it increases the methanol product yield from 44.54% to 99.78%. Copyright © 2025 by Authors, Published by Universitas Diponegoro and BCREC Publishing Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).https://journal.bcrec.id/index.php/jcerp/article/view/20305methanolcarbon dioxidehydrogenationhysys simulationyield optimization |
| spellingShingle | Chindaga Widya Verisna Munna Lissa'adah Nursatitah Nursatitah Zulfa Aulia Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in Distillation Journal of Chemical Engineering Research Progress methanol carbon dioxide hydrogenation hysys simulation yield optimization |
| title | Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in Distillation |
| title_full | Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in Distillation |
| title_fullStr | Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in Distillation |
| title_full_unstemmed | Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in Distillation |
| title_short | Optimizing Methanol Production Yield through Carbon Dioxide Hydrogenation Process with Continuous Stirred Tank Reactor and Transition from Partial to Total Condenser in Distillation |
| title_sort | optimizing methanol production yield through carbon dioxide hydrogenation process with continuous stirred tank reactor and transition from partial to total condenser in distillation |
| topic | methanol carbon dioxide hydrogenation hysys simulation yield optimization |
| url | https://journal.bcrec.id/index.php/jcerp/article/view/20305 |
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