Modelling (vapour plus liquid) and (vapour plus liquid plus liquid) equilibria of {water (H2O) + methanol (MeOH) plus dimethyl ether (DME) plus carbon dioxide (CO2)} quaternary system using the Peng-Robinson EoS with Wong-Sandler mixing rule

Ye K, Freund H, Sundmacher K (2011)


Publication Status: Published

Publication Type: Journal article

Publication year: 2011

Journal

Publisher: Elsevier

Book Volume: 43

Pages Range: 2002-2014

Journal Issue: 12

DOI: 10.1016/j.jct.2011.07.016

Abstract

The (vapour + liquid) equilibria (VLE) and (vapour + liquid + liquid) equilibria (VILE) binary data from literature were correlated using the Peng-Robinson (PR) equation of state (EoS) with the Wong-Sandler mixing rule (WS). Two group contribution activity models were used in the PRWS: UNIFAC-PSRK and UNIFAC-Lby. The systems were successfully extrapolated from the binary systems to ternary and quaternary systems. Results indicate that the PRWS-UNIFAC-PSRK generally displays a better performance than the PRWS-UNIFAC-Lby. (C) 2011 Elsevier Ltd. All rights reserved.

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APA:

Ye, K., Freund, H., & Sundmacher, K. (2011). Modelling (vapour plus liquid) and (vapour plus liquid plus liquid) equilibria of {water (H2O) + methanol (MeOH) plus dimethyl ether (DME) plus carbon dioxide (CO2)} quaternary system using the Peng-Robinson EoS with Wong-Sandler mixing rule. Journal of Chemical Thermodynamics, 43(12), 2002-2014. https://doi.org/10.1016/j.jct.2011.07.016

MLA:

Ye, Kongmeng, Hannsjörg Freund, and Kai Sundmacher. "Modelling (vapour plus liquid) and (vapour plus liquid plus liquid) equilibria of {water (H2O) + methanol (MeOH) plus dimethyl ether (DME) plus carbon dioxide (CO2)} quaternary system using the Peng-Robinson EoS with Wong-Sandler mixing rule." Journal of Chemical Thermodynamics 43.12 (2011): 2002-2014.

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