中国科学院机构知识库网格
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Design and operation of integrated pilot-scale dimethyl ether synthesis system via pyrolysis/gasification of corncob

文献类型:期刊论文

作者Li, Yuping1; Wang, Tiejun1; Yin, Xiuli1; Wu, Chuangzhi1; Ma, Longlong1; Li, Haibin1; Sun, Li2
刊名fuel
出版日期2009-11-01
卷号88期号:11页码:2181-2187
关键词Pilot-scale Dimethyl ether (DME) Bio-syngas Synthesis
ISSN号0016-2361
通讯作者liyp@ms.giec.ac.cn ; wangtj@ms.giec.ac.cn
中文摘要the integrated pilot-scale dimethyl ether (dme) synthesis system from corncob was demonstrated for modernizing utilization of biomass residues. the raw bio-syngas was obtained by the pyrolyzer/gasifier at the yield rate of 40-45 nm(3)/h. the content of tar in the raw bio-syngas was decreased to less than 20 mg/nm(3) by high temperature gasification of the pyrolysates under o-2-rich air. more than 70% co2 in the raw bio-syngas was removed by pressure-swing adsorption unit (psa). the bio-syngas (h-2/co approximate to 1) was catalytically converted to dme in the fixed-bed tubular reactor directly over cu/zn/al/hzsm-5 catalysts. co conversion and space-time yield of dme were in the range of 82.0-73.6% and 124.3-203.8 kg/m(cat)(3)/h, respectively, with a similar dme selectivity when gas hourly space velocity (ghsv, volumetric flow rate of syngas at stp divided by the volume of catalyst) increased from 650 h(-1) to 1500 h(-1) at 260 degrees c and 4.3 mpa. and the selectivity to methanol and c-2(+) products was less than 0.65% under typical synthesis condition. the thermal energy conversion efficiency was ca. 32.0% and about 16.4% carbon in dried corncob was essentially converted to dme with the production cost of ca. (sic) 3737/ton dme. cu (111) was assumed to be the active phase for dme synthesis, confirmed by x-ray diffraction (xrd) characterization.
英文摘要the integrated pilot-scale dimethyl ether (dme) synthesis system from corncob was demonstrated for modernizing utilization of biomass residues. the raw bio-syngas was obtained by the pyrolyzer/gasifier at the yield rate of 40-45 nm(3)/h. the content of tar in the raw bio-syngas was decreased to less than 20 mg/nm(3) by high temperature gasification of the pyrolysates under o(2)-rich air. more than 70% co(2) in the raw bio-syngas was removed by pressure-swing adsorption unit (psa). the bio-syngas (h(2)/co approximate to 1) was catalytically converted to dme in the fixed-bed tubular reactor directly over cu/zn/al/hzsm-5 catalysts. co conversion and space-time yield of dme were in the range of 82.0-73.6% and 124.3-203.8 kg/m(cat)(3)/h, respectively, with a similar dme selectivity when gas hourly space velocity (ghsv, volumetric flow rate of syngas at stp divided by the volume of catalyst) increased from 650 h(-1) to 1500 h(-1) at 260 degrees c and 4.3 mpa. and the selectivity to methanol and c(2)(+) products was less than 0.65% under typical synthesis condition. the thermal energy conversion efficiency was ca. 32.0% and about 16.4% carbon in dried corncob was essentially converted to dme with the production cost of ca. (sic) 3737/ton dme. cu (111) was assumed to be the active phase for dme synthesis, confirmed by x-ray diffraction (xrd) characterization. (c) 2009 elsevier ltd. all rights reserved.
WOS标题词science & technology ; technology
类目[WOS]energy & fuels ; engineering, chemical
研究领域[WOS]energy & fuels ; engineering
关键词[WOS]biomass ; methanol ; catalysts ; biofuels ; syngas ; fuel ; gas
收录类别SCI
资助信息most of china [2007cb210207]; national nature science foundation of china ; national 863 plan [2007aa05z416]
原文出处http://www.sciencedirect.com/science/journal/00162361
语种英语
WOS记录号WOS:000268914900016
公开日期2010-09-16
源URL[http://ir.giec.ac.cn/handle/344007/3306]  
专题中国科学院广州能源研究所
作者单位1.Chinese Acad Sci, Key Lab Renewable Energy & Gas Hydrate, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China
2.Shandong Acad Sci, Energy Res Inst, Jinan 250014, Peoples R China
推荐引用方式
GB/T 7714
Li, Yuping,Wang, Tiejun,Yin, Xiuli,et al. Design and operation of integrated pilot-scale dimethyl ether synthesis system via pyrolysis/gasification of corncob[J]. fuel,2009,88(11):2181-2187.
APA Li, Yuping.,Wang, Tiejun.,Yin, Xiuli.,Wu, Chuangzhi.,Ma, Longlong.,...&Sun, Li.(2009).Design and operation of integrated pilot-scale dimethyl ether synthesis system via pyrolysis/gasification of corncob.fuel,88(11),2181-2187.
MLA Li, Yuping,et al."Design and operation of integrated pilot-scale dimethyl ether synthesis system via pyrolysis/gasification of corncob".fuel 88.11(2009):2181-2187.

入库方式: OAI收割

来源:广州能源研究所

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