Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model

Epoxidized vegetable oils can produce a natural-based polymer product as chemical reaction intermediates, plasticisers, and stabilizers in polyvinyl chloride. This study aims to identify the effects of using different concentrations of hydrogen peroxide and the effect of different molar ratios of hy...

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Published in:Environmental Progress and Sustainable Energy
Main Author: Azmi I.S.; Azlee N.A.M.; Jalil M.J.
Format: Article
Language:English
Published: John Wiley and Sons Inc 2024
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85164456459&doi=10.1002%2fep.14236&partnerID=40&md5=139238c42d66d622e345a36aa4221b5c
id 2-s2.0-85164456459
spelling 2-s2.0-85164456459
Azmi I.S.; Azlee N.A.M.; Jalil M.J.
Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
2024
Environmental Progress and Sustainable Energy
43
1
10.1002/ep.14236
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85164456459&doi=10.1002%2fep.14236&partnerID=40&md5=139238c42d66d622e345a36aa4221b5c
Epoxidized vegetable oils can produce a natural-based polymer product as chemical reaction intermediates, plasticisers, and stabilizers in polyvinyl chloride. This study aims to identify the effects of using different concentrations of hydrogen peroxide and the effect of different molar ratios of hydrogen peroxide on relative conversion to oxirane. Epoxidized palm oil was produced in situ using performic acid as epoxidation agents and titanium dioxide as a catalyst. The results indicated that a higher concentration of hydrogen peroxide at 50% concentration and the ratio of 2:1 of hydrogen peroxide to palm oil used in the in situ epoxidation of had provided a higher relative conversion to oxirane (50%) in reaction time (70 min). Fourier transformation infrared spectroscopy revealed the presence of an oxirane group at 1200 cm−1. Numerical kinetic modeling was developed with applied genetic algorithm optimization to find the process model that fit experimental data. Then, the kinetic rate, k parameters obtained k11 = 0.031 mol L−1 min−1, k12 = 3.159 mol L−1 min−1, k2 = 2.620 mol L−1 min−1 for epoxidation palm oil, and k3 = 1.19 × 10−5 mol L−1 min−1 in degradation process. © 2023 American Institute of Chemical Engineers.
John Wiley and Sons Inc
19447442
English
Article

author Azmi I.S.; Azlee N.A.M.; Jalil M.J.
spellingShingle Azmi I.S.; Azlee N.A.M.; Jalil M.J.
Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
author_facet Azmi I.S.; Azlee N.A.M.; Jalil M.J.
author_sort Azmi I.S.; Azlee N.A.M.; Jalil M.J.
title Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
title_short Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
title_full Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
title_fullStr Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
title_full_unstemmed Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
title_sort Catalytic epoxidation of palm oleic acid by heterogeneous catalysts: Optimization and kinetic model
publishDate 2024
container_title Environmental Progress and Sustainable Energy
container_volume 43
container_issue 1
doi_str_mv 10.1002/ep.14236
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85164456459&doi=10.1002%2fep.14236&partnerID=40&md5=139238c42d66d622e345a36aa4221b5c
description Epoxidized vegetable oils can produce a natural-based polymer product as chemical reaction intermediates, plasticisers, and stabilizers in polyvinyl chloride. This study aims to identify the effects of using different concentrations of hydrogen peroxide and the effect of different molar ratios of hydrogen peroxide on relative conversion to oxirane. Epoxidized palm oil was produced in situ using performic acid as epoxidation agents and titanium dioxide as a catalyst. The results indicated that a higher concentration of hydrogen peroxide at 50% concentration and the ratio of 2:1 of hydrogen peroxide to palm oil used in the in situ epoxidation of had provided a higher relative conversion to oxirane (50%) in reaction time (70 min). Fourier transformation infrared spectroscopy revealed the presence of an oxirane group at 1200 cm−1. Numerical kinetic modeling was developed with applied genetic algorithm optimization to find the process model that fit experimental data. Then, the kinetic rate, k parameters obtained k11 = 0.031 mol L−1 min−1, k12 = 3.159 mol L−1 min−1, k2 = 2.620 mol L−1 min−1 for epoxidation palm oil, and k3 = 1.19 × 10−5 mol L−1 min−1 in degradation process. © 2023 American Institute of Chemical Engineers.
publisher John Wiley and Sons Inc
issn 19447442
language English
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