Shan Feng , Maolan Li , Xudong Yu , Lin Wang , Qin Huang
{"title":"三元体系RbCl -聚乙二醇(PEG6000) - H2O在T =(288.2, 298.2和308.2)K时的相平衡:测量,相关性和热力学模型","authors":"Shan Feng , Maolan Li , Xudong Yu , Lin Wang , Qin Huang","doi":"10.1016/j.cjche.2024.12.020","DOIUrl":null,"url":null,"abstract":"<div><div>The phase equilibria relationship of the system RbCl-PEG6000-H<sub>2</sub>O 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.</div></div>","PeriodicalId":9966,"journal":{"name":"Chinese Journal of Chemical Engineering","volume":"81 ","pages":"Pages 105-114"},"PeriodicalIF":3.7000,"publicationDate":"2025-05-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"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\",\"authors\":\"Shan Feng , Maolan Li , Xudong Yu , Lin Wang , Qin Huang\",\"doi\":\"10.1016/j.cjche.2024.12.020\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>The phase equilibria relationship of the system RbCl-PEG6000-H<sub>2</sub>O 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.</div></div>\",\"PeriodicalId\":9966,\"journal\":{\"name\":\"Chinese Journal of Chemical Engineering\",\"volume\":\"81 \",\"pages\":\"Pages 105-114\"},\"PeriodicalIF\":3.7000,\"publicationDate\":\"2025-05-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chinese Journal of Chemical Engineering\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S1004954125001004\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chinese Journal of Chemical Engineering","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1004954125001004","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
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
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.
期刊介绍:
The Chinese Journal of Chemical Engineering (Monthly, started in 1982) is the official journal of the Chemical Industry and Engineering Society of China and published by the Chemical Industry Press Co. Ltd. The aim of the journal is to develop the international exchange of scientific and technical information in the field of chemical engineering. It publishes original research papers that cover the major advancements and achievements in chemical engineering in China as well as some articles from overseas contributors.
The topics of journal include chemical engineering, chemical technology, biochemical engineering, energy and environmental engineering and other relevant fields. Papers are published on the basis of their relevance to theoretical research, practical application or potential uses in the industry as Research Papers, Communications, Reviews and Perspectives. Prominent domestic and overseas chemical experts and scholars have been invited to form an International Advisory Board and the Editorial Committee. It enjoys recognition among Chinese academia and industry as a reliable source of information of what is going on in chemical engineering research, both domestic and abroad.