Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel Production
Two different methods of production of bio-hydrogenated diesel (BHD), simply called green diesel from rice bran oil (RBO), were performed. In the first route, a direct hydrotreating reaction of RBO to BHD catalysed by Pd/Al<sub>2</sub>O<sub>3</sub> was performed in a high-pre...
| 出版年: | Energies |
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| 主要な著者: | , , , , |
| フォーマット: | 論文 |
| 言語: | 英語 |
| 出版事項: |
MDPI AG
2023-01-01
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| オンライン・アクセス: | https://www.mdpi.com/1996-1073/16/3/1347 |
| _version_ | 1850262743440949248 |
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| author | Praepilas Dujjanutat Nithinun Srihanun Papasanee Muanruksa James Winterburn Pakawadee Kaewkannetra |
| author_facet | Praepilas Dujjanutat Nithinun Srihanun Papasanee Muanruksa James Winterburn Pakawadee Kaewkannetra |
| author_sort | Praepilas Dujjanutat |
| collection | DOAJ |
| container_title | Energies |
| description | Two different methods of production of bio-hydrogenated diesel (BHD), simply called green diesel from rice bran oil (RBO), were performed. In the first route, a direct hydrotreating reaction of RBO to BHD catalysed by Pd/Al<sub>2</sub>O<sub>3</sub> was performed in a high-pressure batch reactor. Operating conditions were investigated as follows: catalyst loading (0.5 to 1.5% wt.), temperature (325 to 400 °C), initial hydrogen (H<sub>2</sub>) pressure (40 to 60 bar) and reaction time (30 to 90 min). The optimal condition was obtained at 1% wt catalyst loading, 350 °C, 40 bar H<sub>2</sub> pressure and 60 min. Yields of crude/refined biofuels and BHD achieved were approximately 98%, 81.71% and 73.71%, respectively. In another route, transesterification together with hydrotreating reactions of rice bran methyl ester (RBME) to BHD was performed using the optimal conditions obtained from the first route. The amount of 98% crude biofuel was obtained and was equivalent to production yields of refined biofuel (85.71%) and BHD (68.51%). Furthermore, physical and chemical properties of both RBO/RBME green diesel were also considered following ASTM standard methods. In summary, both catalytic reactions were achieved in the range of a low-speed industrial diesel and were further recommended for BHD or green diesel production from RBO. |
| format | Article |
| id | doaj-art-e5433f4c54de40ebb407a4fe7d4a8a83 |
| institution | Directory of Open Access Journals |
| issn | 1996-1073 |
| language | English |
| publishDate | 2023-01-01 |
| publisher | MDPI AG |
| record_format | Article |
| spelling | doaj-art-e5433f4c54de40ebb407a4fe7d4a8a832025-08-19T23:46:12ZengMDPI AGEnergies1996-10732023-01-01163134710.3390/en16031347Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel ProductionPraepilas Dujjanutat0Nithinun Srihanun1Papasanee Muanruksa2James Winterburn3Pakawadee Kaewkannetra4Postdoctoral Training of Department of Biotechnology, Khon Kaen University, Khon Kaen 40002, ThailandGraduate School Khon Kaen University, Khon Kaen University, Khon Kaen 40002, ThailandPostdoctoral Training of Department of Biotechnology, Khon Kaen University, Khon Kaen 40002, ThailandDepartment of Chemical Engineering and Analytical Science (CEAS), The University of Manchester, Manchester M13 9PL, UKCentre for Alternative Energy Research and Development (AERD), Faculty of Engineering, Khon Kaen University, Khon Kaen 40002, ThailandTwo different methods of production of bio-hydrogenated diesel (BHD), simply called green diesel from rice bran oil (RBO), were performed. In the first route, a direct hydrotreating reaction of RBO to BHD catalysed by Pd/Al<sub>2</sub>O<sub>3</sub> was performed in a high-pressure batch reactor. Operating conditions were investigated as follows: catalyst loading (0.5 to 1.5% wt.), temperature (325 to 400 °C), initial hydrogen (H<sub>2</sub>) pressure (40 to 60 bar) and reaction time (30 to 90 min). The optimal condition was obtained at 1% wt catalyst loading, 350 °C, 40 bar H<sub>2</sub> pressure and 60 min. Yields of crude/refined biofuels and BHD achieved were approximately 98%, 81.71% and 73.71%, respectively. In another route, transesterification together with hydrotreating reactions of rice bran methyl ester (RBME) to BHD was performed using the optimal conditions obtained from the first route. The amount of 98% crude biofuel was obtained and was equivalent to production yields of refined biofuel (85.71%) and BHD (68.51%). Furthermore, physical and chemical properties of both RBO/RBME green diesel were also considered following ASTM standard methods. In summary, both catalytic reactions were achieved in the range of a low-speed industrial diesel and were further recommended for BHD or green diesel production from RBO.https://www.mdpi.com/1996-1073/16/3/1347rice bran oil (RBO)transesterificationhydrotreatingbio-hydrogenated diesel (BHD)rice bran methyl ester (RBME)green diesel |
| spellingShingle | Praepilas Dujjanutat Nithinun Srihanun Papasanee Muanruksa James Winterburn Pakawadee Kaewkannetra Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel Production rice bran oil (RBO) transesterification hydrotreating bio-hydrogenated diesel (BHD) rice bran methyl ester (RBME) green diesel |
| title | Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel Production |
| title_full | Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel Production |
| title_fullStr | Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel Production |
| title_full_unstemmed | Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel Production |
| title_short | Transesterification and Hydrotreating Reactions of Rice Bran Oil for Bio-Hydrogenated Diesel Production |
| title_sort | transesterification and hydrotreating reactions of rice bran oil for bio hydrogenated diesel production |
| topic | rice bran oil (RBO) transesterification hydrotreating bio-hydrogenated diesel (BHD) rice bran methyl ester (RBME) green diesel |
| url | https://www.mdpi.com/1996-1073/16/3/1347 |
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