期刊文献+

二甲醚经低碳烯烃合成汽油组分正辛烷、对二甲苯热力学分析

Thermodynamic analysis for DME conversion to n-octane and p-xylene of gasoline via light olefins
下载PDF
导出
摘要 采用原子矩阵法确定了二甲醚经低碳烯烃制正辛烷和对二甲苯的独立反应数,并通过建立平衡关系,采用文献介绍方法,计算了各个反应的反应热、平衡常数及反应平衡时的平衡组分浓度。经分析表明,反应属放热反应;模型中绝大多数反应能自发进行,并且平衡转化率较高;低温高压有利于正辛烷的生成,而低温低压有利于对二甲苯的生成;丙烯生成正辛烷和对二甲苯的转化率远高于乙烯和丁烯,因此控制中间产物丙烯的含量有利于控制目的产物的产出。 The number of independent reactions of dimethyl ether (DME) to n-octane and p-xylene via light olefins was obtained by atomic matrix method. Reactions heat, equilibrium constants, equilibrium relationships among the produets of all those reactions were calculated through building equilibrium relationships with the methods from literatures. The results show that most of the reac- tions are exothermic reactions. Most of the reactions in models could proceed spontaneously with high equilibrium conversion. Low temperature and high pressure are beneficial to improve the yield of n-octane, but low temperature and low pressure are beneficial to improve the yield of p-xylene; conversion rates of propylene to n-octane and p-xylene were higher than that to ethane and butylene. The product yield could be improved through controlling the content of propylene.
出处 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 2010年第1期1-5,12,共6页 Natural Gas Chemical Industry
基金 中国科学院知识创新工程重要方向项目(KGCX2-YW-318-2)
关键词 二甲醚制低碳烯烃 低碳烯烃制汽油 热力学计算 正辛烷 对二甲苯 平衡组成 DME to lower olefins lower olefins to gasoline thermodynamic calculation n-octane p-xylene equilibrium composition
  • 相关文献

参考文献12

  • 1Zaidi H A, Pant K K. Catalytic conversion of methanol to gasoline range hydrocarbons [J]. Catal Today, 2004, 96:155-160.
  • 2Zeng D L, Yang J, Wang J Q, et al. Solid-state NMR studies of methanol-to-aromatics reaction over silver exchanged HZSM-5 zeolite[J].Microporous Mesoporous Mater,2007, 98: 214-219.
  • 3Bjorgen M, Svelle S, Joensen F,et al. Conversion of methanol to hydrocarbons over zeohte H-ZSM-5: On the origin of the olefinic species[J]J Catal, 2007,249:195-207.
  • 4Kanazirev V, Tsoncheva T. A study of the nonstationary character of the methanol to hydrocarbons conversion[J]. Can J Chem,1992,70:1997-2002.
  • 5Chang C D. A kinetic model for methanol conversion to hydroearbons[J].Chem Eng Sci,1980,35:619-622.
  • 6Sedran U, Mahay A, Delasa H I.Modelling methanol conversion to hydrocarbons: revision and testing of a simple kinetic model[J].Chem Eng Sci, 1990,45(5):1161-1165.
  • 7杜明仙,郝栩,胡惠民,黄哲,胡杰南.甲醇制汽油(MTG)集总动力学模型[J].煤炭转化,1994,17(2):14-19. 被引量:2
  • 8齐国祯,谢在库,钟思青,张成芳,陈庆龄.甲醇制低碳烯烃(MTO)反应热力学研究[J].石油与天然气化工,2005,34(5):349-353. 被引量:25
  • 9杨明平,罗娟.甲醇制低碳烯烃反应体系的热力学计算与分析[J].煤化工,2008,36(3):44-48. 被引量:7
  • 10于海卫,刘盛林,刘伟成,王清遐,徐龙伢.汽油中烯烃异构和芳构化偶合热力学分析[J].石油学报(石油加工),2007,23(2):51-56. 被引量:3

二级参考文献18

  • 1吴青,何鸣元.催化裂化汽油改质过程的八集总动力学模型研究[J].炼油技术与工程,2004,34(11):22-26. 被引量:11
  • 2齐国祯,谢在库,钟思青,张成芳,陈庆龄.煤或天然气经甲醇制低碳烯烃工艺研究新进展[J].现代化工,2005,25(2):9-13. 被引量:31
  • 3刘福安,侯栓弟,武雪锋,赵俊鹏.催化裂化汽油改质反应动力学模型研究[J].炼油技术与工程,2005,35(6):25-30. 被引量:5
  • 4齐国祯,谢在库,钟思青,张成芳,陈庆龄.甲醇制低碳烯烃(MTO)反应热力学研究[J].石油与天然气化工,2005,34(5):349-353. 被引量:25
  • 5[4]Bos A N R,Tromp PJ J,Akse H N.Conversion of Methanol to Lower Olefins.Kinetic Modeling,Reactor Simulation and Selection[J].Ind Eng Chem Res,1995,34 (11):3 808-3 816.
  • 6[6]Reid R C,Prausnitz J M,Poling B E.The Properties of Gases and Liquids (4th Edition).[M] New York:McGraw-Hill,1987.125-137.
  • 7[7]Wu X C,Michael,Rayford G.Methanol Conversion on SAPO-34 with Reaction Condition for Fixed-bed Reactor[J].Applied Catalysis,2004,60 (12):63-69.
  • 8Chang C D,Catal Rev-Sci Eng,1983年,25卷,1页
  • 9Reid R C, Prausnitz J M and Poling B E. The Properties of Gases and Liquids[M], 4th Edition, New York, Mcgraw-Hill, Appendix A, 1987.
  • 10Aguayo A T, Campo A E S, Gayubo A G, et, al. Deactivation by Coke of A Catalyst Based on A SAPO -34 in the Transformation of Methanol to Olefins[J], J.Chem.Tech.Biotech, 1999,74:315~321.

共引文献31

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