期刊文献+

烟煤在超临界水中催化气化的研究 被引量:5

CATALYTIC GASIFICATION OF BITUMINOUS COAL IN SUPERCRITICAL WATER
下载PDF
导出
摘要 以鄂尔多斯烟煤为例,利用间歇反应釜,在超临界水条件下考察了反应温度、水煤比以及K2CO3添加量等因素对煤气化反应的影响.结果表明,温度对煤的转化率和气相收率有重要影响,且转化率和气相收率随温度的升高而增加;增加水煤比会提高煤转化率和气相收率,但其对气体组成和煤转化率影响的幅度随水煤比的增加而减小;在5%~20%(质量分数)煤催化剂添加条件下,煤转化率随催化剂添加量的增加而迅速增加.在研究考察范围内,煤颗粒尺寸在80目~150目范围内,最佳的反应条件是:反应温度为650℃,水煤比为20∶1,K2CO3添加量为20%(质量分数)煤.相应的反应结果是:煤转化率达到84%以上,气相收率高于3 000 mL/g daf coal,其中氢气收率为1 900 mL/g daf coal,甲烷收率为450 mL/g daf coal. The Erdos bituminous coal is gasified with K2CO3 as the catalyst in supercritical water (SCW) using a batch tank reactor. The effects of temperature, H2O/eoal ratio, and amount of K2 CO3 loadings are tested and investigated. Experimental results indicate that temperature has significant effect on the coal conversion and gas yield, and both the conversion rate and gas yield increase with increasing temperature; greater water/coal ratio can increase the coal conversion rate and gas yield, but the effect is less profound as the water/coal ratio increases; in the range of the catalyst loading between 5%-20%coal, the coal conversion increases appreciably with increasing catalyst loading amount. In this investigation, the optimum operating conditions are found at 650 ℃, 25 MPa, coal particle size within the range of 80 mesh-150 mesh, water/coal mass ratio of 20 : 1, and K2CO3 concentration of 20%coal, and the coal conversion, gas yield, hydrogen yield, and methane yield are 84 % than 450 mL/g daf coal respectively. , 3 000 mL/g daf coal, 1 900 mL/g daf coal and more
出处 《煤炭转化》 CAS CSCD 北大核心 2011年第2期17-21,45,共6页 Coal Conversion
基金 河北省重大科技创新项目(09213914Z)
关键词 烟煤 催化气化 超临界水 bituminous coal, catalytic gasification, supercritical water
  • 相关文献

参考文献9

二级参考文献23

  • 1任永强,许世森,郜时旺.干法进料煤气化技术在中国的进展与发展趋势[J].中国电力,2004,37(6):49-52. 被引量:15
  • 2苏晓丽,赵玉龙,张荣,毕继诚.加热速率和粒径对聚乙烯在超临界水中转化的影响[J].燃料化学学报,2006,34(4):509-511. 被引量:3
  • 3王春云.超临界水分解二恶英类物质的技术状况及课题[J].化工科技动态,1998,14(8):38-39.
  • 4华东理工大学 兖矿鲁南化肥厂 中国天辰化学工程公司.粉煤加压气化技术简介[EB/OL].http:icct.ecust.edu.cn/pcg.pdf,2004-12-11.
  • 5Jr ANTAL M J,ALLEN S G,SCHULMAN D,XU X,DLVILIU R J.Biomass gasification in supercritical water[J].Ind Eng Chem Res,2000,39(11):4040-4053.
  • 6HONG G T,SPRITZER M H.Supercritical water partial oxidation Proceedings of the 2002 U.S.DOE Hydrogen Program Review[DB/OL].NREL/CP-610-32405.http://www1.eere.energy.gov/hydrogenandfuelcells/pdfs/32405a12.pdf.
  • 7LIN S Y,SUZUKI Y,HATANO H,HARADA M.Hydrogen production from hydrocarbon by integration of water-carbon reaction and carbon dioxide removal (HyPr-RING Method)[J].Energy Fuels,2001,15(2):339-343.
  • 8WANG J,TAKARADA T.Role of calcium hydroxide in supercritical water gasification of low-rank coal[J].Energy Fuels,2001,15(2):356-362.
  • 9CHENG L M,ZHANG R,BI J C.Pyrolysis of a low rank coal in sub-and supercritical water[J].Fuel Process Technol,2004,85(8-10):921-932.
  • 10HUPPERT G L,WU B C,TOWNSEND S H,KLEIN M T,PASPEK S C.Hydrolysis in supercritical water:Identification and implications of a polar transition state[J].Ind Eng Chem Res,1989,28(2):161-165.

共引文献152

同被引文献59

引证文献5

二级引证文献13

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部