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Marpaung, Benaya Matius
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Chemical Engineering, Chemistry & Bioengineering Energy Engineering Materials Science & Nanotechnology

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Journal : Journal of Chemical Engineering Research Progress

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Improving Net Energy of Cumene Hydroperoxide Production using Cumene Oxidation Process Through Removing Cooler on the Recycle System to Achieve Energy Efficiency and Reduce Production Cost Marpaung, Benaya Matius; Setyanto, Henricus Jovan; Aliyah, St Nur; Haryono, Lim Christoval Evandy
Journal of Chemical Engineering Research Progress 2024: JCERP, Volume 1 Issue 2 Year 2024 (December 2024)
Publisher : UPT Laboratorium Terpadu, Universitas Diponegoro

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.9767/jcerp.20276

Abstract

This study investigates a modification to the cumene hydroperoxide (CHP) production process by removing the cooler between the reactor and separator, aiming to improve energy efficiency. The simulation results show that the modified process requires 245,259,223.09 kJ/h, compared to 265,992,099.05 kJ/h for the basic process, representing a significant energy reduction of 20,732,875.95 kJ/h. The removal of the cooler also leads to lower capital and operating costs, with annual savings of $111,900 in operating costs and $103,580 in utilities. This modification enhances the overall energy efficiency and cost-effectiveness of the CHP production process while maintaining product selectivity and operational performance. Copyright © 2024 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).
Optimizing Energy Efficiency in Acetone Production via Isopropyl Alcohol Dehydrogenation through Feed-Effluent Heat Integration Aditasya, Regina; Taslim, Melisa; Azzahra, Sri Fatimah; Narendro, Bagas Bumi; Prantindoe, Indira Avila; Seng, Kevin Setiadi; Marpaung, Benaya Matius
Journal of Chemical Engineering Research Progress 2025: JCERP, Volume 2 Issue 2 Year 2025 (December)
Publisher : UPT Laboratorium Terpadu, Universitas Diponegoro

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.9767/jcerp.20591

Abstract

Acetone production via isopropyl alcohol (IPA) dehydrogenation is an energy‑intensive process due to the endothermic nature of the reaction. This study aims to minimize net energy consumption by simulating a modified process design that incorporates a Feed‑Effluent Heat Exchanger (FEHE) strategy. The simulation results demonstrate that the modified configuration successfully recovers heat from the reactor effluent to preheat the feed stream to 178 °C, thereby reducing the total energy consumption from 4,695.8 kW to 4,532.0 kW. This energy saving of 163.8 kW confirms that the proposed heat integration is technically feasible and significantly enhances the thermodynamic efficiency of the acetone production process. 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).
Co-Authors Aditasya, Regina Aliyah, St Nur Azzahra, Sri Fatimah Haryono, Lim Christoval Evandy Narendro, Bagas Bumi Prantindoe, Indira Avila Seng, Kevin Setiadi Setyanto, Henricus Jovan Taslim, Melisa