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Theoretical Prediction and Experimental Determination of Vapour-Liquid Equilibrium for Ternary Systems Trimethyl Borate-Methanol-N,N-Dimethylformamide/N,N-Dimethylacetamide
Corresponding Author(s) : Jiao Xu
Asian Journal of Chemistry,
Vol. 27 No. 8 (2015): Vol 27 Issue 8
Abstract
Vapour-liquid equilibrium prediction of ternary systems: trimethyl borate-methanol-N,N-dimethylformamide and trimethyl borate-methanol-N,N-dimethylacetamide were conducted through combined utilization of Materials Studio, COSMO-SAC program and ChemCAD. The vapour-liquid equilibrium data obtained were compared with the experimentally measured data. Results showed that predicted values were comparatively conservative than measured ones, which indicated better performance of solvents can be achieved actually. Measured data were correlated using three frequently used activity coefficient models, of which binary interaction coefficients were obtained. The solvents displayed obvious solvent effect, especially N,N-dimethylacetamide. This proves the validity of N,N-dimethylacetamide as an effective solvent.
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- J. Gmehling and U. Onken, Vapor-Liquid Equilibrium Data Collection, Dechema, Frankfurt, Vol. 1, Part-2a (1982).
- R. Will, CEH Product Review-Specialty Boron Chemicals, In: Chemical Economics Handbook, SRI International, Menlo Park, California, pp. 510.5000 A-510.5001 N (1991).
- F.M. Khoury, Multistage Separation Process, CRC Press, New York Ch. 10 (2005).
- E.R. Foucher, M.F. Doherty and M.F. Malone, Ind. Eng. Chem. Res., 30, 760 (1991); doi:10.1021/ie00052a021.
- B. van Dyk and I. Nieuwoudt, Ind. Eng. Chem. Res., 39, 1423 (2000); doi:10.1021/ie9904753.
- L. Wu, W.X. Chang and G.F. Guan, Ind. Eng. Chem. Res., 46, 1254 (2007); doi:10.1021/ie060022f.
- Y. Peng, J. Fu and X. Lu, Fluid Phase Equilib., 363, 220 (2014); doi:10.1016/j.fluid.2013.11.036.
- Q. Li, P. Liu, L. Cao, F. Wen, S. Zhang and B. Wang, Fluid Phase Equilib., 360, 439 (2013); doi:10.1016/j.fluid.2013.09.060.
- F. Cai, X. Wu, C. Chen, X. Chen, C. Asumana, M.R. Haque and G. Yu, Fluid Phase Equilib., 352, 47 (2013); doi:10.1016/j.fluid.2013.05.021.
- X. Song, Y. Wang, K. Wang and R. Xu, Ind. Eng. Chem. Res., 51, 13438 (2012); doi:10.1021/ie300914h.
- L. Changshi, J. Chem. Eng. Data, 56, 2 (2011); doi:10.1021/je100453x.
- J. Gmehling and U. Onken, Vapor-Liquid Equilibrium Data Collection, Dechema, Frankfurt Vol. 1, Part-5 (1982).
- Z. Tian, X.B. Cui, J.L. Cai, Y. Zhang, T.Y. Feng, Y.M. Peng and L.X. Xue, Fluid Phase Equilib., 352, 75 (2013); doi:10.1016/j.fluid.2013.05.020.
References
J. Gmehling and U. Onken, Vapor-Liquid Equilibrium Data Collection, Dechema, Frankfurt, Vol. 1, Part-2a (1982).
R. Will, CEH Product Review-Specialty Boron Chemicals, In: Chemical Economics Handbook, SRI International, Menlo Park, California, pp. 510.5000 A-510.5001 N (1991).
F.M. Khoury, Multistage Separation Process, CRC Press, New York Ch. 10 (2005).
E.R. Foucher, M.F. Doherty and M.F. Malone, Ind. Eng. Chem. Res., 30, 760 (1991); doi:10.1021/ie00052a021.
B. van Dyk and I. Nieuwoudt, Ind. Eng. Chem. Res., 39, 1423 (2000); doi:10.1021/ie9904753.
L. Wu, W.X. Chang and G.F. Guan, Ind. Eng. Chem. Res., 46, 1254 (2007); doi:10.1021/ie060022f.
Y. Peng, J. Fu and X. Lu, Fluid Phase Equilib., 363, 220 (2014); doi:10.1016/j.fluid.2013.11.036.
Q. Li, P. Liu, L. Cao, F. Wen, S. Zhang and B. Wang, Fluid Phase Equilib., 360, 439 (2013); doi:10.1016/j.fluid.2013.09.060.
F. Cai, X. Wu, C. Chen, X. Chen, C. Asumana, M.R. Haque and G. Yu, Fluid Phase Equilib., 352, 47 (2013); doi:10.1016/j.fluid.2013.05.021.
X. Song, Y. Wang, K. Wang and R. Xu, Ind. Eng. Chem. Res., 51, 13438 (2012); doi:10.1021/ie300914h.
L. Changshi, J. Chem. Eng. Data, 56, 2 (2011); doi:10.1021/je100453x.
J. Gmehling and U. Onken, Vapor-Liquid Equilibrium Data Collection, Dechema, Frankfurt Vol. 1, Part-5 (1982).
Z. Tian, X.B. Cui, J.L. Cai, Y. Zhang, T.Y. Feng, Y.M. Peng and L.X. Xue, Fluid Phase Equilib., 352, 75 (2013); doi:10.1016/j.fluid.2013.05.020.