期刊文献+

亚/超临界水-乙醇体系中煤与杜氏盐藻共液化制备液体燃料 被引量:1

Production of liquid fuel via co-liquefaction of coal and Dunaliella tertiolecta in sub/supercritical water-ethanol system
下载PDF
导出
摘要 在间歇式高温高压反应釜中,对亚/超临界水-乙醇体系中煤和杜氏盐藻共液化制备液体燃料进行了研究。考察了水-乙醇介质中乙醇质量分数、反应温度、料液比和反应时间等对共液化效果的影响,通过FT-IR和GC-MS等分析方法对液化产物进行了分析。研究结果表明:当亚/超临界水-乙醇介质中乙醇质量分数为60%,反应温度为360℃,料液比为1∶10,反应时间为30 min时,所得液体燃料的产率和转化率分别为40.29%和70.62%。FT-IR分析结果表明,在亚/超临界水-乙醇体系下,煤和杜氏盐藻中各主要成分均得到了有效转化。GC-MS分析结果说明,液体燃料中的乙酯类物质较多,这主要是因为乙醇与液化产物中的酸类物质发生了酯化反应。由此说明,杜氏盐藻的加入,显著的促进了煤的液化,提升了液体燃料的产率和转化率,同时也提高了液体燃料的品质,为煤的清洁化利用提供了理论基础。 The co-liquefaction of coal and Dunaliella tertiolecta (D. tertiolecta) with sub/supercritical water-ethanol as the reaction medium is investigated in a batch autoclave under high temperature and high pressure. The effects of reaction conditions such as volume fraction of ethanol to water, reaction temperature, ratio of feedstock/solvent and reaction time on the co-liquefaction rate are studied. The produced liquid fuel is analyzed with FT-IR and GC-MS. The experimental results show that the liquid fuel yield and conversion in the co-liquefaction are 40. 29% and 70. 62% , respectively,under the following conditions: 60% (volume fraction) of ethanol, 360~C of reaction temperature, 30 minutes of reaction time and 1 : 10 of the ratio of feedstock/solvent. FT-IR analysis results show that the main components of coal and D. tertiolecta could be liquefied effectively in the sub/supercritical water-ethanol medium. The GC-MS analysis results indicate that there is more carboxylic acid ethyl ester in the liquid fuel, which is mainly because of the esterification reaction between acids and ethanol in the co-liquefaction. Thereby, the addition of D. tertiolecta can significantly promote the coal liquefaction. The liquid fuel yield, conversion and the quality of liquid fuel have been improved, which provides a theoretical basis and practical significance for the clean utilization of coal.
出处 《现代化工》 CAS CSCD 北大核心 2013年第4期82-86,共5页 Modern Chemical Industry
基金 国家自然科学基金(21176142) 清华大学自主科研计划(2011Z08141) 中国石油科技创新基金项目(2010D50060406)
关键词 超临界水-乙醇 杜氏盐藻 共液化 液体燃料 sb/supercritical water-ethanol coal dunaliella tertiolecta co-liquefaction liquid fuel
  • 相关文献

参考文献17

  • 1Hayvanovyeh V, Pyshyev S. Desulufrization of low-rank coal with high sulfur content is the first stage of coal burning at heat electric stations [J ]. Energy & Fuels,2003,17 ( 5 ) : 1186 - 1190.
  • 2Shen Y, Wu H Y, Pan Z Y. Co-liquefaction of coal and polypropyl- ene or polystyrene in hot compressed water at 360 -430℃ [ J]. Fuel Processing Technology,2012,104:281 - 286.
  • 3Toshinori Inoue, Osamu Okuma, Kaoru Masuda,et al. Hydrothermal treatment of brown coal to improve the space time yield of a direct liquefaction reactor [ J ]. Energy & Fuels, 2012,26 ( 4 ) : 2198 - 2203.
  • 4Leila Emami Taba, Muhammad Faisal Irfan,Wan Ashri Mohd Wan Daud, et al. The effect of temperature on various parameters in coabion/ass and CO-gasification: A review [ J]. Renewable and Sustainable Energy Reviews ,2012,16:5584 - 5596.
  • 5尚琳琳,程世庆,张海清.生物质与煤共热解特性研究[J].太阳能学报,2006,27(8):852-856. 被引量:25
  • 6张杰.浅谈煤化工发展趋势[J].现代化工,2011,31(7):6-7. 被引量:8
  • 7常丽萍.煤液化技术研究现状及其发展趋势[J].现代化工,2005,25(10):17-20. 被引量:17
  • 8Guo Z X, Bai Z Q, Bai J, et al. Co-liquefaction of lignite and saw- dust under syngas [ J . Fuel Processing Technology,2011,92 ( 1 ) : 119 - 125.
  • 9Shui H F, Shah C J, Cai Z Y, et al. Co-liquefaction behavior of a sub-bituminous coal and sawdust [ J]. Energy, 2011,36 ( 11 ) : 6645 - 6650.
  • 10Karaca F, Bolat E. Coprocessing of a Turkish lignite with a cellulos- ic waste material : 1 The effect of coprocessing on liquefaction yields at different reaction temperatures[ J . Fuel Processing Technology, 2000,64(1/3) :47 -55.

二级参考文献42

共引文献50

同被引文献2

引证文献1

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