Knowledge Management System Of Guangzhou Institute of Energy Conversion, CAS
Hydrogen-rich gas production from biomass catalytic gasification | |
Lv, PM; Chang, J; Wang, TJ; Fu, Y; Chen, Y; Zhu, JX | |
2004 | |
Source Publication | ENERGY & FUELS |
Volume | 18Issue:1Pages:228-233 |
Abstract | With the use of dolomite in the fluidized-bed gasifier and the use of nickel-based catalysts in the fixed bed reactor downstream from the gasifier, the characteristics of hydrogen yield from biomass are investigated in the present study. Some calcined dolomite is placed initially in the gasifier with an amount of 120 g/(kg h(-1)) biomass. To replace the eroded and elutriated dolomite, calcined dolomite (0.3-0.45 mm) is continuously fed and its feeding rate is determined by preliminary test. The influence of the operating conditions in the catalytic reactor on the production of gases, especially H-2, is studied over the temperature range of 650-850 degreesC, for weight hourly space velocity (WHSV) in the range of 2.68-10.72 h(-1). In the gaseous product, the average content of H-2 exceeds 50 vol %; C-2 content is lowered to below 1 vol %, and nearly half of CH4 is converted after the catalytic reactor. Over the ranges of experimental conditions examined, the highest gas yield reaches 3.31 Nm(3)/kg biomass, wet basis; the maximum hydrogen yield reaches 130.28 g H-2/kg biomass, wet basis. This system shows a good performance over a lifetime test of 350 min. |
Subtype | Article |
WOS Headings | Science & Technology ; Technology |
DOI | 10.1021/ef0301203 |
WOS Subject Extended | Energy & Fuels ; Engineering |
WOS Keyword | STEAM REFORMING CATALYSTS ; FLUIDIZED-BED ; HOT GAS ; OXYGEN MIXTURES ; RAW GAS ; AIR ; DOLOMITE |
Indexed By | SCI |
Language | 英语 |
WOS Subject | Energy & Fuels ; Engineering, Chemical |
WOS ID | WOS:000188415000028 |
Citation statistics | |
Document Type | 期刊论文 |
Identifier | http://ir.giec.ac.cn/handle/344007/10475 |
Collection | 中国科学院广州能源研究所 |
Affiliation | 1.Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510070, Peoples R China 2.Univ Western Ontario, London, ON N6A 5B9, Canada |
Recommended Citation GB/T 7714 | Lv, PM,Chang, J,Wang, TJ,et al. Hydrogen-rich gas production from biomass catalytic gasification[J]. ENERGY & FUELS,2004,18(1):228-233. |
APA | Lv, PM,Chang, J,Wang, TJ,Fu, Y,Chen, Y,&Zhu, JX.(2004).Hydrogen-rich gas production from biomass catalytic gasification.ENERGY & FUELS,18(1),228-233. |
MLA | Lv, PM,et al."Hydrogen-rich gas production from biomass catalytic gasification".ENERGY & FUELS 18.1(2004):228-233. |
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