SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2025, Vol. 81 ›› Issue (5): 105-114.DOI: 10.1016/j.cjche.2024.12.020

Previous Articles     Next Articles

Phase equilibria of ternary system RbCl - polyethylene glycol (PEG6000) - H2O at T = (288.2, 298.2, and 308.2) K: Measurement, correlation, and thermodynamic modeling

Shan Feng1, Maolan Li1,2, Xudong Yu1, Lin Wang1, Qin Huang1   

  1. 1. College of Materials and Chemistry & Chemical Engineering, Chengdu University of Technology, Chengdu 610059, China;
    2. China KIDE Engineering Corporation, Chengdu 610100, China
  • Received:2024-09-25 Revised:2024-11-30 Accepted:2024-12-10 Online:2025-03-11 Published:2025-05-28
  • Contact: Xudong Yu,E-mail:xwdlyxd@126.com
  • Supported by:
    This work was supported by the National Natural Science Foundation of China (U1507111).

Phase equilibria of ternary system RbCl - polyethylene glycol (PEG6000) - H2O at T = (288.2, 298.2, and 308.2) K: Measurement, correlation, and thermodynamic modeling

Shan Feng1, Maolan Li1,2, Xudong Yu1, Lin Wang1, Qin Huang1   

  1. 1. College of Materials and Chemistry & Chemical Engineering, Chengdu University of Technology, Chengdu 610059, China;
    2. China KIDE Engineering Corporation, Chengdu 610100, China
  • 通讯作者: Xudong Yu,E-mail:xwdlyxd@126.com
  • 基金资助:
    This work was supported by the National Natural Science Foundation of China (U1507111).

Abstract: The phase equilibria relationship of the system RbCl-PEG6000-H2O were investigated at temperatures of 288.2, 298.2, and 308.2 K, the compositions of solid-liquid equilibria(SLE) and liquid-liquid equilibria(LLE) were determined. The complete phase diagrams, binodal curve diagrams, and tie-line diagrams were all plotted. Results show that both solid-liquid equilibria and liquid-liquid equilibria relationships at each studied temperature. The complete phase diagrams at 288.2 K, 298.2 K and 308.2 K consist of six phase regions: unsaturated liquid region (L), two saturated solutions with one solid phase of RbCl (L + S), one saturated liquid phase with two solid phases of PEG6000 and RbCl (2S + L), an aqueous two-phase region (2L), and a region with two liquids and one solid phase of RbCl (2L + S). With the increase in temperature, the layering ability of the aqueous two-phase system increases, and both regions (2L) and (2L + S) increase. The binodal curves were fitted using the nonlinear equations proposed by Mistry, Hu, and Jayapal. Additionally, the tie-line data were correlated with the Othmer-Tobias, Bancroft, Hand, and Bachman equations. The liquid-liquid equilibria at 288.2 K, 298.2 K and 308.2 K were calculated using the NRTL model. The findings confirm that the experimental and calculated values are in close agreement, demonstrating the model’s effectiveness in representing the system’s behavior.

Key words: Phase equilibria, Solubility, Thermodynamic properties, Liquid-liquid phase equilibria, Solid-liquid phase equilibria, NRTL model

摘要: The phase equilibria relationship of the system RbCl-PEG6000-H2O were investigated at temperatures of 288.2, 298.2, and 308.2 K, the compositions of solid-liquid equilibria(SLE) and liquid-liquid equilibria(LLE) were determined. The complete phase diagrams, binodal curve diagrams, and tie-line diagrams were all plotted. Results show that both solid-liquid equilibria and liquid-liquid equilibria relationships at each studied temperature. The complete phase diagrams at 288.2 K, 298.2 K and 308.2 K consist of six phase regions: unsaturated liquid region (L), two saturated solutions with one solid phase of RbCl (L + S), one saturated liquid phase with two solid phases of PEG6000 and RbCl (2S + L), an aqueous two-phase region (2L), and a region with two liquids and one solid phase of RbCl (2L + S). With the increase in temperature, the layering ability of the aqueous two-phase system increases, and both regions (2L) and (2L + S) increase. The binodal curves were fitted using the nonlinear equations proposed by Mistry, Hu, and Jayapal. Additionally, the tie-line data were correlated with the Othmer-Tobias, Bancroft, Hand, and Bachman equations. The liquid-liquid equilibria at 288.2 K, 298.2 K and 308.2 K were calculated using the NRTL model. The findings confirm that the experimental and calculated values are in close agreement, demonstrating the model’s effectiveness in representing the system’s behavior.

关键词: Phase equilibria, Solubility, Thermodynamic properties, Liquid-liquid phase equilibria, Solid-liquid phase equilibria, NRTL model