-SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism

Raw coal without carbonization was treated with sulfuric acid at different concentrations (70% to 95%) as a controlled sulfonation process to produce a simple and effective acidic catalyst. The synthetic catalyst (S.Coal) at the best H2SO4 concentration (95%) showed the best acid density (8.4 mmol/g...

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Autores principales: Sherouk M. Ibrahim, Ahmed M. El-Sherbeeny, Jae-Jin Shim, Ali A. AlHammadi, Mostafa R. Abukhadra
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Lenguaje:EN
Publicado: Elsevier 2021
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Acceso en línea:https://doaj.org/article/60b15647faee49c48cf8ed33e0ecdf1b
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spelling oai:doaj.org-article:60b15647faee49c48cf8ed33e0ecdf1b2021-11-28T04:34:29Z-SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism2352-484710.1016/j.egyr.2021.11.139https://doaj.org/article/60b15647faee49c48cf8ed33e0ecdf1b2021-11-01T00:00:00Zhttp://www.sciencedirect.com/science/article/pii/S2352484721012865https://doaj.org/toc/2352-4847Raw coal without carbonization was treated with sulfuric acid at different concentrations (70% to 95%) as a controlled sulfonation process to produce a simple and effective acidic catalyst. The synthetic catalyst (S.Coal) at the best H2SO4 concentration (95%) showed the best acid density (8.4 mmol/g), the best surface area (26.4 m2/g), and the best catalytic activity during the transesterification of the waste sunflower oil. The best yield (98.8%) at low-temperature conditions (40 °C) was achieved after 60 min using 3 g of the catalyst and at a methanol/oil ratio of 20:1. At high-temperature conditions (120 °C), the yield was enhanced to 99.5% after 30 min only considering the catalyst quantity and the methanol content as the same values. The S.Coal as a catalyst is of remarkable reusability for five transesterification runs either at low-temperature conditions (40 °C) or at high-temperature conditions (120 °C). Additionally, the catalyst is of higher catalytic performances than several basic and acidic catalysts demonstrate the efficiency of the sulfonation process on the raw coal without carbonization. The kinetic properties of the occurred transesterification reactions over S.coal followed the Pseudo-First order behavior and of low activation energy.Sherouk M. IbrahimAhmed M. El-SherbeenyJae-Jin ShimAli A. AlHammadiMostafa R. AbukhadraElsevierarticleCoalSulfonationAcidic catalystTransesterificationWaste sunflower oilKineticsElectrical engineering. Electronics. Nuclear engineeringTK1-9971ENEnergy Reports, Vol 7, Iss , Pp 8699-8710 (2021)
institution DOAJ
collection DOAJ
language EN
topic Coal
Sulfonation
Acidic catalyst
Transesterification
Waste sunflower oil
Kinetics
Electrical engineering. Electronics. Nuclear engineering
TK1-9971
spellingShingle Coal
Sulfonation
Acidic catalyst
Transesterification
Waste sunflower oil
Kinetics
Electrical engineering. Electronics. Nuclear engineering
TK1-9971
Sherouk M. Ibrahim
Ahmed M. El-Sherbeeny
Jae-Jin Shim
Ali A. AlHammadi
Mostafa R. Abukhadra
-SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism
description Raw coal without carbonization was treated with sulfuric acid at different concentrations (70% to 95%) as a controlled sulfonation process to produce a simple and effective acidic catalyst. The synthetic catalyst (S.Coal) at the best H2SO4 concentration (95%) showed the best acid density (8.4 mmol/g), the best surface area (26.4 m2/g), and the best catalytic activity during the transesterification of the waste sunflower oil. The best yield (98.8%) at low-temperature conditions (40 °C) was achieved after 60 min using 3 g of the catalyst and at a methanol/oil ratio of 20:1. At high-temperature conditions (120 °C), the yield was enhanced to 99.5% after 30 min only considering the catalyst quantity and the methanol content as the same values. The S.Coal as a catalyst is of remarkable reusability for five transesterification runs either at low-temperature conditions (40 °C) or at high-temperature conditions (120 °C). Additionally, the catalyst is of higher catalytic performances than several basic and acidic catalysts demonstrate the efficiency of the sulfonation process on the raw coal without carbonization. The kinetic properties of the occurred transesterification reactions over S.coal followed the Pseudo-First order behavior and of low activation energy.
format article
author Sherouk M. Ibrahim
Ahmed M. El-Sherbeeny
Jae-Jin Shim
Ali A. AlHammadi
Mostafa R. Abukhadra
author_facet Sherouk M. Ibrahim
Ahmed M. El-Sherbeeny
Jae-Jin Shim
Ali A. AlHammadi
Mostafa R. Abukhadra
author_sort Sherouk M. Ibrahim
title -SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism
title_short -SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism
title_full -SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism
title_fullStr -SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism
title_full_unstemmed -SO3H-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism
title_sort -so3h-functionalization of sub-bituminous coal as a highly active acidic catalyst during the transesterification of spent sunflower oil; characterization, application, and mechanism
publisher Elsevier
publishDate 2021
url https://doaj.org/article/60b15647faee49c48cf8ed33e0ecdf1b
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