Masato Urabe , Masaki Ota , Richard Lee Smith Jr. , Masaru Watanabe
{"title":"液态CO2与乙醇-水混合物的高压相平衡","authors":"Masato Urabe , Masaki Ota , Richard Lee Smith Jr. , Masaru Watanabe","doi":"10.1016/j.fluid.2025.114450","DOIUrl":null,"url":null,"abstract":"<div><div>Although many data have been reported for the CO<sub>2</sub> (1) - ethanol (2) - water (3) system, gaps in the literature exist for liquid CO<sub>2</sub> at conditions where stripping of ethanol for flavor fractionation has been suggested. In this work, a flow-type device was used to measure the phase equilibria of CO<sub>2</sub> - ethanol - water mixtures at (278 to 298) K and (8 to 20) MPa. Ethanol/water feed ratios were varied from 0.22 to 1.7 which gave corresponding equilibrium ratios (=<em>y</em><sub>i</sub>/<em>x</em><sub>i</sub>) of <em>K</em><sub>1</sub> (39 to 4), <em>K</em><sub>2</sub> (0.12 to 0.21) and <em>K</em><sub>3</sub> (0.006 to 0.04) giving ethanol/water selectivities, <em>β</em> (=<em>K</em><sub>2</sub>/<em>K</em><sub>3</sub>), that ranged from 27.9 to 5. While the <em>K</em><sub>2</sub> values tended to be invariant with ethanol/water feed ratio, the <em>K</em><sub>1</sub> and <em>K</em><sub>3</sub> values varied greatly. Among the equations of state evaluated in this work, the Peng-Robinson equation of state with the Wong-Sandler mixing rule model based on the NRTL activity coefficient expression gave the lowest deviations and could correlate <em>K</em> values for CO<sub>2</sub>, ethanol and water with an average relative deviation of 6.9 %, 22.3 % and 28.1 %, respectively.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"597 ","pages":"Article 114450"},"PeriodicalIF":2.8000,"publicationDate":"2025-04-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"High-pressure phase equilibria of liquid CO2 with ethanol - water mixtures\",\"authors\":\"Masato Urabe , Masaki Ota , Richard Lee Smith Jr. , Masaru Watanabe\",\"doi\":\"10.1016/j.fluid.2025.114450\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Although many data have been reported for the CO<sub>2</sub> (1) - ethanol (2) - water (3) system, gaps in the literature exist for liquid CO<sub>2</sub> at conditions where stripping of ethanol for flavor fractionation has been suggested. In this work, a flow-type device was used to measure the phase equilibria of CO<sub>2</sub> - ethanol - water mixtures at (278 to 298) K and (8 to 20) MPa. Ethanol/water feed ratios were varied from 0.22 to 1.7 which gave corresponding equilibrium ratios (=<em>y</em><sub>i</sub>/<em>x</em><sub>i</sub>) of <em>K</em><sub>1</sub> (39 to 4), <em>K</em><sub>2</sub> (0.12 to 0.21) and <em>K</em><sub>3</sub> (0.006 to 0.04) giving ethanol/water selectivities, <em>β</em> (=<em>K</em><sub>2</sub>/<em>K</em><sub>3</sub>), that ranged from 27.9 to 5. While the <em>K</em><sub>2</sub> values tended to be invariant with ethanol/water feed ratio, the <em>K</em><sub>1</sub> and <em>K</em><sub>3</sub> values varied greatly. Among the equations of state evaluated in this work, the Peng-Robinson equation of state with the Wong-Sandler mixing rule model based on the NRTL activity coefficient expression gave the lowest deviations and could correlate <em>K</em> values for CO<sub>2</sub>, ethanol and water with an average relative deviation of 6.9 %, 22.3 % and 28.1 %, respectively.</div></div>\",\"PeriodicalId\":12170,\"journal\":{\"name\":\"Fluid Phase Equilibria\",\"volume\":\"597 \",\"pages\":\"Article 114450\"},\"PeriodicalIF\":2.8000,\"publicationDate\":\"2025-04-24\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Fluid Phase Equilibria\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0378381225001207\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"CHEMISTRY, PHYSICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Fluid Phase Equilibria","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0378381225001207","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
High-pressure phase equilibria of liquid CO2 with ethanol - water mixtures
Although many data have been reported for the CO2 (1) - ethanol (2) - water (3) system, gaps in the literature exist for liquid CO2 at conditions where stripping of ethanol for flavor fractionation has been suggested. In this work, a flow-type device was used to measure the phase equilibria of CO2 - ethanol - water mixtures at (278 to 298) K and (8 to 20) MPa. Ethanol/water feed ratios were varied from 0.22 to 1.7 which gave corresponding equilibrium ratios (=yi/xi) of K1 (39 to 4), K2 (0.12 to 0.21) and K3 (0.006 to 0.04) giving ethanol/water selectivities, β (=K2/K3), that ranged from 27.9 to 5. While the K2 values tended to be invariant with ethanol/water feed ratio, the K1 and K3 values varied greatly. Among the equations of state evaluated in this work, the Peng-Robinson equation of state with the Wong-Sandler mixing rule model based on the NRTL activity coefficient expression gave the lowest deviations and could correlate K values for CO2, ethanol and water with an average relative deviation of 6.9 %, 22.3 % and 28.1 %, respectively.
期刊介绍:
Fluid Phase Equilibria publishes high-quality papers dealing with experimental, theoretical, and applied research related to equilibrium and transport properties of fluids, solids, and interfaces. Subjects of interest include physical/phase and chemical equilibria; equilibrium and nonequilibrium thermophysical properties; fundamental thermodynamic relations; and stability. The systems central to the journal include pure substances and mixtures of organic and inorganic materials, including polymers, biochemicals, and surfactants with sufficient characterization of composition and purity for the results to be reproduced. Alloys are of interest only when thermodynamic studies are included, purely material studies will not be considered. In all cases, authors are expected to provide physical or chemical interpretations of the results.
Experimental research can include measurements under all conditions of temperature, pressure, and composition, including critical and supercritical. Measurements are to be associated with systems and conditions of fundamental or applied interest, and may not be only a collection of routine data, such as physical property or solubility measurements at limited pressures and temperatures close to ambient, or surfactant studies focussed strictly on micellisation or micelle structure. Papers reporting common data must be accompanied by new physical insights and/or contemporary or new theory or techniques.