Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism

Recent research has concentrated on more sustainable approaches to producing epoxides, specifically focusing on utilizing vegetable oils. This paper presents research on the mechanism of in situ peracids’ epoxidation of palm stearin using zeolite ZSM-5 as a catalyst. The Taguchi technique is used to...

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Published in:Biomass Conversion and Biorefinery
Main Author: Rahim N.H.; Rasib I.M.; Azmi I.S.; Jalil M.J.
Format: Article
Language:English
Published: Springer Science and Business Media Deutschland GmbH 2024
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85208810651&doi=10.1007%2fs13399-024-06312-8&partnerID=40&md5=25ced2ce543248b4d4067445d837e2c9
id 2-s2.0-85208810651
spelling 2-s2.0-85208810651
Rahim N.H.; Rasib I.M.; Azmi I.S.; Jalil M.J.
Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
2024
Biomass Conversion and Biorefinery


10.1007/s13399-024-06312-8
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85208810651&doi=10.1007%2fs13399-024-06312-8&partnerID=40&md5=25ced2ce543248b4d4067445d837e2c9
Recent research has concentrated on more sustainable approaches to producing epoxides, specifically focusing on utilizing vegetable oils. This paper presents research on the mechanism of in situ peracids’ epoxidation of palm stearin using zeolite ZSM-5 as a catalyst. The Taguchi technique is used to discover the optimal level of each process parameter involved in the epoxidation of palm stearin. The results show the most optimum levels for each process parameter: (A) reaction temperature, 70 °C (level 2); (B) stirrer speed, 200 rpm (level 1); (C) catalyst loading, 0.8 w/t % (level 4); (D) acetic acid/palm stearin molar ratio, 1:1 (level 2); and (E) hydrogen peroxide/palm stearin molar ratio, 0.5:1 (level 1). The relative conversion to oxirane (RCO) was achieved at 43% under optimum conditions. The numerical integration method, the 4th-order Runge–Kutta technique, was employed to develop a mathematical model. The results demonstrated a high level of agreement between the simulation and the experimental data, affirming the model’s validity. © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2024.
Springer Science and Business Media Deutschland GmbH
21906815
English
Article

author Rahim N.H.; Rasib I.M.; Azmi I.S.; Jalil M.J.
spellingShingle Rahim N.H.; Rasib I.M.; Azmi I.S.; Jalil M.J.
Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
author_facet Rahim N.H.; Rasib I.M.; Azmi I.S.; Jalil M.J.
author_sort Rahim N.H.; Rasib I.M.; Azmi I.S.; Jalil M.J.
title Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
title_short Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
title_full Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
title_fullStr Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
title_full_unstemmed Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
title_sort Synergistic catalytic epoxidation of palm stearin applied by in situ peracid mechanism
publishDate 2024
container_title Biomass Conversion and Biorefinery
container_volume
container_issue
doi_str_mv 10.1007/s13399-024-06312-8
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85208810651&doi=10.1007%2fs13399-024-06312-8&partnerID=40&md5=25ced2ce543248b4d4067445d837e2c9
description Recent research has concentrated on more sustainable approaches to producing epoxides, specifically focusing on utilizing vegetable oils. This paper presents research on the mechanism of in situ peracids’ epoxidation of palm stearin using zeolite ZSM-5 as a catalyst. The Taguchi technique is used to discover the optimal level of each process parameter involved in the epoxidation of palm stearin. The results show the most optimum levels for each process parameter: (A) reaction temperature, 70 °C (level 2); (B) stirrer speed, 200 rpm (level 1); (C) catalyst loading, 0.8 w/t % (level 4); (D) acetic acid/palm stearin molar ratio, 1:1 (level 2); and (E) hydrogen peroxide/palm stearin molar ratio, 0.5:1 (level 1). The relative conversion to oxirane (RCO) was achieved at 43% under optimum conditions. The numerical integration method, the 4th-order Runge–Kutta technique, was employed to develop a mathematical model. The results demonstrated a high level of agreement between the simulation and the experimental data, affirming the model’s validity. © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2024.
publisher Springer Science and Business Media Deutschland GmbH
issn 21906815
language English
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