Knowledge Management System Of Guangzhou Institute of Energy Conversion, CAS
| Steam reforming of biomass raw fuel gas over NiO-MgO solid solution cordierite monolith catalyst | |
Wang, Chenguang1,2; Wang, Tiejun1 ; Ma, Longlong1; Gao, Yan1,2; Wu, Chuangzhi1
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| 2010-03-01 | |
| 发表期刊 | ENERGY CONVERSION AND MANAGEMENT
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| ISSN | 0196-8904 |
| 卷号 | 51期号:3页码:446-451 |
| 产权排序 | [Wang, Chenguang; Wang, Tiejun; Ma, Longlong; Gao, Yan; Wu, Chuangzhi] Chinese Acad Sci, Guangzhou Inst Energy Convers, Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Peoples R China; [Wang, Chenguang; Gao, Yan] Chinese Acad Sci, Grad Univ, Beijing 100039, Peoples R China |
| 通讯作者 | wangtj@ms.giec.ac.cn |
| 摘要 | The NiO-MgO solid solution cordierite monolith catalyst was prepared by impregnation. 60 h steam reforming tests were carried out at 1023 K TC was used to analyze the carbon deposition on the catalyst. GC and GC-MS were used to analyze the component of biomass fuel gas and tar. The results show that steam reforming can effectively improve the quality of fuel gas, H(2)/CO ratio can be adjusted by steam reforming, The addition of steam can also increase the activity and stability of the catalyst dramatically. The CH(4) conversion reached 94%. TG shows that the addition of steam can decrease the carbon deposition on the catalyst. GC-MS result shows that most of the tar was converted to H(2), CO and trace lighter component. Steam reforming can eliminate the biomass tar species more deeply than dry reforming. (C) 2009 Elsevier Ltd. All rights reserved. |
| 文章类型 | Article |
| 其他摘要 | The NiO-MgO solid solution cordierite monolith catalyst was prepared by impregnation. 60 h steam reforming tests were carried out at 1023 K TC was used to analyze the carbon deposition on the catalyst. GC and GC-MS were used to analyze the component of biomass fuel gas and tar. The results show that steam reforming can effectively improve the quality of fuel gas, H(2)/CO ratio can be adjusted by steam reforming, The addition of steam can also increase the activity and stability of the catalyst dramatically. The CH(4) conversion reached 94%. TG shows that the addition of steam can decrease the carbon deposition on the catalyst. GC-MS result shows that most of the tar was converted to H(2), CO and trace lighter component. Steam reforming can eliminate the biomass tar species more deeply than dry reforming. (C) 2009 Elsevier Ltd. All rights reserved. |
| 关键词 | Biomass Fuel Gas Steam Reforming Nio-mgo Solid Solution Cordierite Monolith Catalyst Tar Elimination |
| 学科领域 | Thermodynamics ; Energy & Fuels ; Mechanics ; Physics |
| WOS标题词 | Science & Technology ; Physical Sciences ; Technology |
| DOI | 10.1016/j.enconman.2009.10.006 |
| 研究领域[WOS] | Thermodynamics ; Energy & Fuels ; Mechanics ; Physics |
| URL | 查看原文 |
| 关键词[WOS] | SUPPORTED-RH CATALYSTS ; FLUIDIZED-BED ; TAR ELIMINATION ; GASIFICATION ; METHANE ; AIR ; PERFORMANCE ; OXIDATION ; PHENOL ; CO2 |
| 收录类别 | SCI |
| 语种 | 英语 |
| 项目资助者 | National High Technology Research and Development Program(863) of China [2007AA05Z416] |
| WOS类目 | Thermodynamics ; Energy & Fuels ; Mechanics ; Physics, Nuclear |
| WOS记录号 | WOS:000274090300007 |
| 引用统计 | |
| 文献类型 | 期刊论文 |
| 条目标识符 | http://ir.giec.ac.cn/handle/344007/8512 |
| 专题 | 中国科学院广州能源研究所 生物质能源 生物质化工品制备实验室 |
| 作者单位 | 1.Chinese Acad Sci, Guangzhou Inst Energy Convers, Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Peoples R China 2.Chinese Acad Sci, Grad Univ, Beijing 100039, Peoples R China |
| 推荐引用方式 GB/T 7714 | Wang, Chenguang,Wang, Tiejun,Ma, Longlong,et al. Steam reforming of biomass raw fuel gas over NiO-MgO solid solution cordierite monolith catalyst[J]. ENERGY CONVERSION AND MANAGEMENT,2010,51(3):446-451. |
| APA | Wang, Chenguang,Wang, Tiejun,Ma, Longlong,Gao, Yan,&Wu, Chuangzhi.(2010).Steam reforming of biomass raw fuel gas over NiO-MgO solid solution cordierite monolith catalyst.ENERGY CONVERSION AND MANAGEMENT,51(3),446-451. |
| MLA | Wang, Chenguang,et al."Steam reforming of biomass raw fuel gas over NiO-MgO solid solution cordierite monolith catalyst".ENERGY CONVERSION AND MANAGEMENT 51.3(2010):446-451. |
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