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...
Published in: | Environmental Progress and Sustainable Energy |
---|---|
Main Author: | |
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 |
format |
Article |
accesstype |
|
record_format |
scopus |
collection |
Scopus |
_version_ |
1809677577048031232 |