Production of renewable 1,3-pentadiene from xylitol via formic acid-mediated deoxydehydration and palladium-catalyzed deoxygenation reactions
文献类型：期刊论文
| 作者 | Zheng, Mingyuan2; Sun, Ruiyan1,2; Li, Xinsheng1,2; Pang, Jifeng2; Wang, Aiqin2; Wang, Xiaodong2; Zhang, Tao2 |
| 刊名 | GREEN CHEMISTRY
 |
| 出版日期 | 2017 |
| 卷号 | 19期号:3页码:638-642 |
| ISSN号 | 1463-9262 |
| DOI | 10.1039/c6gc02868c |
| 文献子类 | Article |
| 英文摘要 | A two-step synthetic approach for the production of renewable 1,3-pentadiene was reported: xylitol deoxydehydration (DODH) by formic acid to 2,4-pentadien-1-ol, 1-formate (2E), followed by deoxygenation to 1,3-pentadiene over Pd/C. The overall carbon yield of 1,3-pentadiene reached 51.8% under the optimized conditions. |
| WOS关键词 | ETHYLENE-GLYCOL ; BIOMASS ; CONVERSION ; OLEFINS ; DEHYDRATION ; CHEMICALS ; DECARBONYLATION ; ALCOHOLS ; PENTITOLS ; REAGENT |
| WOS研究方向 | Chemistry |
| 语种 | 英语 |
| WOS记录号 | WOS:000395630000008 |
| 出版者 | ROYAL SOC CHEMISTRY |
| 源URL | [http://cas-ir.dicp.ac.cn/handle/321008/169486]  |
| 专题 | 大连化学物理研究所_中国科学院大连化学物理研究所 |
| 通讯作者 | Zheng, Mingyuan; Zhang, Tao |
| 作者单位 | 1.Univ Chinese Acad Sci, Beijing 100049, Peoples R China 2.Chinese Acad Sci, Dalian Inst Chem Phys, State Key Lab Catalysis, Dalian 116023, Peoples R China |
| 推荐引用方式 GB/T 7714 | Zheng, Mingyuan,Sun, Ruiyan,Li, Xinsheng,et al. Production of renewable 1,3-pentadiene from xylitol via formic acid-mediated deoxydehydration and palladium-catalyzed deoxygenation reactions[J]. GREEN CHEMISTRY,2017,19(3):638-642. |
| APA | Zheng, Mingyuan.,Sun, Ruiyan.,Li, Xinsheng.,Pang, Jifeng.,Wang, Aiqin.,...&Zhang, Tao.(2017).Production of renewable 1,3-pentadiene from xylitol via formic acid-mediated deoxydehydration and palladium-catalyzed deoxygenation reactions.GREEN CHEMISTRY,19(3),638-642. |
| MLA | Zheng, Mingyuan,et al."Production of renewable 1,3-pentadiene from xylitol via formic acid-mediated deoxydehydration and palladium-catalyzed deoxygenation reactions".GREEN CHEMISTRY 19.3(2017):638-642. |
入库方式： OAI收割
来源：大连化学物理研究所
浏览0
下载0
收藏0
其他版本
除非特别说明，本系统中所有内容都受版权保护，并保留所有权利。