期刊文献+

DFT方法研究酸性沸石上苯与乙烯烷基化反应的机理 被引量:1

Reaction mechanism study on alkylation of benzene with ethylene over acid zeolite based on DFT method
下载PDF
导出
摘要 采用B3LYP/6-31G*水平计算来研究酸性沸石上苯与乙烯的烷基化反应历程,从生成能和反应活化能角度分析并讨论了苯与乙烯的反应机理.选取4T簇模型模拟分子筛的酸性位,使用密度泛函理论对烷基化反应三种不同的反应机理(两个联合反应机理和一个分步反应机理)进行计算分析.结果表明,在联合反应机理中,乙烯的质子化和苯与乙烯间C-C键的形成同时发生;分步反应机理中,首先形成一个稳定的乙醇盐中间物种,然后与苯分子反应形成乙苯.联合机理速控步骤的活化能约为160kJ/mol,分步机理速控步骤的活化能为190.24kJ/mol,因此,酸性沸石上苯与乙烯烷基化反应机理主要以联合机理为主,但分步机理与其有一定程度的竞争。 The acid zeolite catalyzed alkylation of benzene with ethene is investigated at the B3LYP/6-31G level of calculation with a 4T-cluster representing the Brφnsted acid site of the zeolite. The reaction mechanism has been analyzed according to the formation energy and reac- tion activation energy. Three different reaction mechanisms of alkylation, two concerted mech- anism and one stepwise mechanism, have been analyzed by density functional theory. The re- sults showed that ethene protonation and C--C bond formation occur simultaneously in the concerted mechanism. The stepwise mechanism starts with the formation of a stable ethoxide intermediate which subsequently reacts with benzene to form the reaction product. The activa- tion energy for the concerted mechanism was about 160 kJ/mol, while it was 190.24 kJ/mol for the stepwise mechanism. The results showed that alkylation of benzene with ethylene occurred through both concerted mechanism and stepwise mechanism, and they were competitive to each other.
出处 《化学研究》 CAS 2013年第2期189-194,198,共7页 Chemical Research
基金 国家自然科学基金青年基金资助项目(21106073)
关键词 乙烯 烷基化反应 密度泛函 反应机理 benzene ethylene alkylation DFT reaction mechanism
  • 相关文献

参考文献19

  • 1DEGNAN T F,MORRIS SMITH C,VENKAT C R. Alkylation of aromatics with ethylene and propylene: recent develop ments in commercial processes[J]. Appl Catal A, 2001,221: 283- 294.
  • 2SHI Y F, GAO Y, YUAN W K. Benzene-ethylene alkylation in near critical regions[J2. Ind Eng Chem Res, 2001,40: 4253- 4257.
  • 3BELLUSSI G,PAZZUCONI G,PEREGO C,et al. Liquid-phase alkylation of benzene with light olefins catalyzed by/?-zeo lites[J]. J Catal,1995,157 :227-234.
  • 4CHEN N Y,GARWOOD W E. Industrial application of shape-selective catalysis[J]. Catal Rev Sci Eng, l Ubb, Zb: l zsa 264. F.
  • 5RANK B,DAHLKE K,EMIG G,et al. A monte-carlo simulation of diffusion and reaction in zeolites[J]. Microporous Ma- terials, 1993,1 : 43 - 56.
  • 6SNURR R Q,BELL A T, THEODOROU D N. Prediction of adsorption of aromatic hydrocarbons in silicalite from grand canonical monte carlo simulations with biased insertions[J]. J Phys Chem, 1993,97:13742- 13752.
  • 7DEKA R C,VETRIVEL R. Computer-aided search for shape-selective zeolite catalysts for the synthesis of p-isobutylethyl- benzene[J]. Chem Commun, 1996,21 : 2397-2398.
  • 8BELYAEVA V V,FROLOV Y L,VORONKOV M G. Dt(b31yp) calculations of silatranes and their radical cations first i- onization potentials[J]. J Struc Chem, 2005,46 : 1072- 1076.
  • 9HAYASE S, HROVAT D A,BORDEN W T. Ab31yp study of the effects of phenyl substituents on 1,5 hydrogen shifts in 3-(z)-1,3-pentadiene provides evidence against a chameleonic transition structure[J]. J Am Chem Soc, 2004,126:10028- 10034.
  • 10FRISCH M J, TRUCKS G W, SCHLEGEL H B, et al. Gaussian 03, Revision C02ECP]. Gaussian Inc. , Pittsburgh, PA., 2003.

同被引文献8

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