342248 Conversion of Residual Ethylene Oxide in the Ionic Liquid Catalyzed CO2 Cycloaddition Process

Wednesday, November 6, 2013: 2:20 PM
Powell A (Hilton)
Jian Sun1, Weiguo Cheng1, Jinquan Wang1, Junping Zhang2 and Suojiang Zhang3, (1)Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, China, (2)Institute of Process Engineering, Chinese Academy of Sciences, Beijing, China, (3)State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, China

Conversion of residual ethylene oxide in the ionic liquid catalyzed CO2 cycloaddition process

Jian Sun, Weiguo Cheng, Jinquan Wang, Junping Zhang and Suojiang Zhang

Institute of Process Engineering, Chinese Academy of Sciences,100190, Beijing, PR China

*Contact information: jsun@home.ipe.ac.cn

Recently, the synthesis of cyclic carbonates via cycloaddition of CO2 to epoxides is much attractive not only because of its efficiency in CO2 conversion, but also becuase of its widely derivative high-value chemicals.[1] Although a number of efficient catalysts including ionic liquids (ILs) have been developed, [2] attention on the trace residual epoxide in the reaction system, especially in gas phase, is rarely covered, which could cause a potential explosion of epoxide when unreacted CO2 is compressed for recyle. As a continous work for CO2 conversion,[3] herein, studies on the conversion of residual trace epoxide (0.2 wt%) in an IL catalyzed CO2 cycloaddition process to produce ethylene carbonate (EC) were carried out. The effect parameters including pressure, temperature, time and solvents (e.g. H2O, EC+ethylene glycol+H2O, BmimCl, BmimPF6, BmimBF4, etc) were systematically screened, and a >99.9% conversion of EO could be realized by reduding the partial pressure of EO in the system. The results indicated that a vapor-liquid equilibriuma of EO in the reaction system has a more important effect on EO elimination rather than reaction time and temperature.

Refferences

[1]  B. Schaffner, F. Schaffner, S.P. Verevkin and A. Borner, Chem. Rev., 2010, 110, 4554.

[2]  a) J. M. Zhang, J. Sun, X. C. Zhang, Y. S. Zhao, S. J. Zhang. Greenhouse Gas Sci Technol., 2011, 2:142-159; b) M. North, R. Pasquale, C. Young, Green Chem., 2010, 12, 1514.

[3]  a) J.Q. Wang, J. Sun, W.G Cheng, S.J. Zhang. Phys. Chem. Chem. Phys., 2012, 14, 11021; b) J. Sun, L. J. Han, W. G. Cheng , J. Q. Wang, X. P. Zhang, S. J. Zhang. ChemSusChem, 2011, 4: 502; c) J. Sun, J.Q. Wang, W. G. Cheng, J. X. Zhang, X. H. Li, S. J. Zhang, Y. B. She. Green Chem., 2012, 14: 654; d) J. Sun, W. G. Cheng, W. Fan, Y. H. Wang, Z. Y. Meng, S. J. Zhang. Catal. Today, 2009, 148: 361.

Acknowledgments

This work was supported by National Basic Research Program of China (2009CB219901), and National Science Fund of China (21006117).


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