Novel in Situ Batch Reactor with a Facile Catalyst Separation Device for Biodiesel Production
文献类型：期刊论文
| 作者 | Jiang, Yanjun1,2; Gu, Hanqi1; Zhou, Liya1; Cui, Cuicui1; Gao, Jing1 |
| 刊名 | INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
 |
| 出版日期 | 2012-11-21 |
| 卷号 | 51期号:46页码:14935-14940 |
| 关键词 | JATROPHA-CURCAS L ENZYMATIC TRANSESTERIFICATION EXTRACTION OIL LIPASE OPTIMIZATION OILSEEDS SEED |
| ISSN号 | 0888-5885 |
| 通讯作者 | Gao, J |
| 英文摘要 | In an effort to reduce the production cost of biodiesel and realize the lipase recovery of the in situ transesterification technology, a reactor with facile catalyst separation device was developed in this study. Compared with conventional method of biodiesel production, this improved reactive extraction. technology can realize not only the biodiesel synthesis in a single step, but also the separation of immobilized lipases from the oilseed residues easily. This technology may present a sustainable, economically attractive process for biodiesel production. J. curcas L. seed, methanol, Lipozyme TL IM, and cosolvent n-hexane were used in this study. The effect of various process parameters on the yield of fatty acid methyl esters (FAMEs) was investigated. The highest FAMEs yield of 90.6% could be achieved under the optimum conditions: n-hexane/seed ratio of 3.5:1 inL/g, methanol/oil molar ratio of 6:1, 15% (w/w) of Lipozyme TL IM, reaction temperature of 45 degrees C, water content of 1.0%, and reaction time of 12 h. The lipase could maintain more than 40% of its initial activity after 13 batches operation under optimal reaction conditions This simple in situ transesterification technology with facile catalyst separation device can be a potential route for biodiesel production, which may greatly reduce the processing steps and costs. |
| WOS标题词 | Science & Technology ; Technology |
| 类目[WOS] | Engineering, Chemical |
| 研究领域[WOS] | Engineering |
| 关键词[WOS] | JATROPHA-CURCAS L. ; ENZYMATIC TRANSESTERIFICATION ; EXTRACTION ; OIL ; LIPASE ; OPTIMIZATION ; OILSEEDS ; SEED |
| 收录类别 | SCI |
| 语种 | 英语 |
| WOS记录号 | WOS:000311325200001 |
| 公开日期 | 2013-10-11 |
| 版本 | 出版稿 |
| 源URL | [http://ir.ipe.ac.cn/handle/122111/3149]  |
| 专题 | 过程工程研究所_生化工程国家重点实验室 |
| 作者单位 | 1.Hebei Univ Technol, Sch Chem Engn & Technol, Tianjin 300130, Peoples R China 2.Chinese Acad Sci, Natl Key Lab Biochem Engn, Inst Proc Engn, Beijing 100190, Peoples R China |
| 推荐引用方式 GB/T 7714 | Jiang, Yanjun,Gu, Hanqi,Zhou, Liya,et al. Novel in Situ Batch Reactor with a Facile Catalyst Separation Device for Biodiesel Production[J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH,2012,51(46):14935-14940. |
| APA | Jiang, Yanjun,Gu, Hanqi,Zhou, Liya,Cui, Cuicui,&Gao, Jing.(2012).Novel in Situ Batch Reactor with a Facile Catalyst Separation Device for Biodiesel Production.INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH,51(46),14935-14940. |
| MLA | Jiang, Yanjun,et al."Novel in Situ Batch Reactor with a Facile Catalyst Separation Device for Biodiesel Production".INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH 51.46(2012):14935-14940. |
入库方式： OAI收割
来源：过程工程研究所
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