{"title":"CO2 Solubility in Aqueous Solution in a Hydrate–Liquid Two-Phase Equilibrium System","authors":"Xiao-Hui Wang, Yi-Wei Wu, Zhen-Bin Xu, Teng-Hua Zhang, Le Zhao, Hong-Shuai Wang, Li-Yong Bao, Chang-Yu Sun, Guang-Jin Chen","doi":"10.1021/acs.iecr.5c00035","DOIUrl":null,"url":null,"abstract":"In marine environments, natural gas hydrates can be surrounded by seawater, forming a hydrate–liquid (H–L<sub>w</sub>) two-phase system. This work developed a new experimental method to prepare an H–L<sub>w</sub> two-phase equilibrium system and then measured the gas solubility in the corresponding liquid phase. The experimental temperature range is 274.25–282.25 K, and the experimental pressure range is 1.407–7.184 MPa. Ninety-two experimental data points of CO<sub>2</sub> solubility in the H–L<sub>w</sub> two-phase equilibrium system are reported in this work. The experimental results indicate that the CO<sub>2</sub> solubility in the liquid phase is almost unaffected by the liquid-phase pressure, while it significantly increases with the increase in system temperature in the H–L<sub>w</sub> two-phase equilibrium system. The effect of NaCl concentration on the CO<sub>2</sub> solubility in the H–L<sub>w</sub> two-phase equilibrium system is complex and also related to the system temperature.","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"45 1","pages":""},"PeriodicalIF":3.8000,"publicationDate":"2025-05-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1021/acs.iecr.5c00035","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}
引用次数: 0
Abstract
In marine environments, natural gas hydrates can be surrounded by seawater, forming a hydrate–liquid (H–Lw) two-phase system. This work developed a new experimental method to prepare an H–Lw two-phase equilibrium system and then measured the gas solubility in the corresponding liquid phase. The experimental temperature range is 274.25–282.25 K, and the experimental pressure range is 1.407–7.184 MPa. Ninety-two experimental data points of CO2 solubility in the H–Lw two-phase equilibrium system are reported in this work. The experimental results indicate that the CO2 solubility in the liquid phase is almost unaffected by the liquid-phase pressure, while it significantly increases with the increase in system temperature in the H–Lw two-phase equilibrium system. The effect of NaCl concentration on the CO2 solubility in the H–Lw two-phase equilibrium system is complex and also related to the system temperature.
期刊介绍:
ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.