Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism
Epoxidized vegetable oils are great concern as they are obtained from sustainable, and renewable natural resources. The epoxidation of palm oil-derived oleic acid was carried out by using in situ generated performic acid to produce epoxidized palm oil-derived oleic acid. The maximum conversion of pa...
Published in: | Environmental Progress and Sustainable Energy |
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Language: | English |
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John Wiley and Sons Inc
2022
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Online Access: | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85116352643&doi=10.1002%2fep.13764&partnerID=40&md5=48a5695e5854e0a27cd7567129c3b989 |
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Jalil M.J.; Azmi I.S.; Hadi A. |
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Jalil M.J.; Azmi I.S.; Hadi A. 2-s2.0-85116352643 Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism 2022 Environmental Progress and Sustainable Energy 41 1 10.1002/ep.13764 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85116352643&doi=10.1002%2fep.13764&partnerID=40&md5=48a5695e5854e0a27cd7567129c3b989 Epoxidized vegetable oils are great concern as they are obtained from sustainable, and renewable natural resources. The epoxidation of palm oil-derived oleic acid was carried out by using in situ generated performic acid to produce epoxidized palm oil-derived oleic acid. The maximum conversion of palm oil-derived oleic acid into oxirane was 86% by applying the in situ peracid mechanism. Based on the Fourier-transform infrared spectrum, the hydroxyl group was observed within a wavenumber range of 1210–1320 cm−1. Last, a mathematical model was developed using Runge–Kutta method and after 100 iterations, the reaction rate parameters were obtained as follows: (Formula presented.) = 0.046 mol·L−1·min−1, (Formula presented.) = 39.058 mol·L−1·min−1, (Formula presented.) = 2.789 mol·L−1·min−1, and (Formula presented.) = 0.0235 mol·L−1·min−1 for of dihydroxystearic acid production. © 2021 American Institute of Chemical Engineers. John Wiley and Sons Inc 19447442 English Article |
author |
2-s2.0-85116352643 |
spellingShingle |
2-s2.0-85116352643 Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism |
author_facet |
2-s2.0-85116352643 |
author_sort |
2-s2.0-85116352643 |
title |
Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism |
title_short |
Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism |
title_full |
Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism |
title_fullStr |
Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism |
title_full_unstemmed |
Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism |
title_sort |
Highly production of dihydroxystrearic acid from catalytic epoxidation process by in situ peracid mechanism |
publishDate |
2022 |
container_title |
Environmental Progress and Sustainable Energy |
container_volume |
41 |
container_issue |
1 |
doi_str_mv |
10.1002/ep.13764 |
url |
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85116352643&doi=10.1002%2fep.13764&partnerID=40&md5=48a5695e5854e0a27cd7567129c3b989 |
description |
Epoxidized vegetable oils are great concern as they are obtained from sustainable, and renewable natural resources. The epoxidation of palm oil-derived oleic acid was carried out by using in situ generated performic acid to produce epoxidized palm oil-derived oleic acid. The maximum conversion of palm oil-derived oleic acid into oxirane was 86% by applying the in situ peracid mechanism. Based on the Fourier-transform infrared spectrum, the hydroxyl group was observed within a wavenumber range of 1210–1320 cm−1. Last, a mathematical model was developed using Runge–Kutta method and after 100 iterations, the reaction rate parameters were obtained as follows: (Formula presented.) = 0.046 mol·L−1·min−1, (Formula presented.) = 39.058 mol·L−1·min−1, (Formula presented.) = 2.789 mol·L−1·min−1, and (Formula presented.) = 0.0235 mol·L−1·min−1 for of dihydroxystearic acid production. © 2021 American Institute of Chemical Engineers. |
publisher |
John Wiley and Sons Inc |
issn |
19447442 |
language |
English |
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Article |
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scopus |
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Scopus |
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1828987868916219904 |