Franklin Okoro, Friday Junior Owuna, Antonin Chapoy, Pezhman Ahmadi, Rod Burgass
{"title":"富二氧化碳双星系统中H2(高达~ 5%)的气泡点和密度","authors":"Franklin Okoro, Friday Junior Owuna, Antonin Chapoy, Pezhman Ahmadi, Rod Burgass","doi":"10.1016/j.fluid.2024.114321","DOIUrl":null,"url":null,"abstract":"<div><div>In this study, experimental measurements of the bubble points of binary mixtures containing varying concentrations of CO<sub>2</sub> (99.5 %, 99 %, 98.5 %,98 %, and ∼ 95 %) with hydrogen (H<sub>2</sub>) were made. These measurements were carried out from low temperatures (240.20 K) up to 294.84 K (with uncertainties of 0.14 K) using the constant composition expansion method. The experimental data were used to validate two thermodynamic models - the Peng-Robinson and Multi-Fluid Helmholtz Energy Approximation Equation of state (PR-EoS and MFHEA-EoS). From the results, the presence of H<sub>2</sub> in CO<sub>2</sub> at concentrations between 0.5 and 5 % caused a significant (∼19–980 %) positive deviation from the phase behaviour of CO<sub>2</sub> stream compared to that of pure CO<sub>2</sub>. This effect intensified with higher concentrations of H<sub>2</sub> and decreased with rising temperatures. Both models demonstrated good agreement with the experimental bubble point data, exhibiting <4 % average deviation for the system. Notably, the PR-EoS outperformed the MFHEA-EoS, showing <3 % average deviation. Densities of CO<sub>2</sub> (99.5 %) with H<sub>2</sub> were measured at 278.14, 298.34, 323.55, and 348.40 K and pressures up to 35 MPa. While the densities of CO<sub>2</sub> (94.99 %) with H<sub>2</sub> were measured at 278.06, 288.13, 298.26, and 323.53 K and pressures up to 35 MPa using a vibrating tube densimeter which was calibrated using water and hydrogen. For the 99.5 % CO<sub>2</sub> binary mixture, the average absolute relative deviations (AARD) of the model predictions were 0.09 % and 0.26 % against MFHEA and PR EoS respectively. The AARD of the model predictions for the 94.99 % CO<sub>2</sub> were 0.33 % and 1.49 % with MFHEA and PR EoS respectively. Furthermore, even at low concentrations (0.5 %), the presence of H<sub>2</sub> led to a substantial reduction (>35 %) in the density of the mixture compared to that of pure CO<sub>2</sub> at lower pressure conditions with this effect becoming more pronounced at higher temperatures and concentrations of H<sub>2</sub>. Both models predicted the densities of the system well (with <2 % deviations from the experimental data), though MFHEA-Eos was more accurate with <0.4 % maximum relative deviation (MaxRD) for all the data points.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"592 ","pages":"Article 114321"},"PeriodicalIF":2.8000,"publicationDate":"2025-01-03","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Bubble points and densities of H2 (up to ∼ 5%) in CO2-rich binary systems\",\"authors\":\"Franklin Okoro, Friday Junior Owuna, Antonin Chapoy, Pezhman Ahmadi, Rod Burgass\",\"doi\":\"10.1016/j.fluid.2024.114321\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>In this study, experimental measurements of the bubble points of binary mixtures containing varying concentrations of CO<sub>2</sub> (99.5 %, 99 %, 98.5 %,98 %, and ∼ 95 %) with hydrogen (H<sub>2</sub>) were made. These measurements were carried out from low temperatures (240.20 K) up to 294.84 K (with uncertainties of 0.14 K) using the constant composition expansion method. The experimental data were used to validate two thermodynamic models - the Peng-Robinson and Multi-Fluid Helmholtz Energy Approximation Equation of state (PR-EoS and MFHEA-EoS). From the results, the presence of H<sub>2</sub> in CO<sub>2</sub> at concentrations between 0.5 and 5 % caused a significant (∼19–980 %) positive deviation from the phase behaviour of CO<sub>2</sub> stream compared to that of pure CO<sub>2</sub>. This effect intensified with higher concentrations of H<sub>2</sub> and decreased with rising temperatures. Both models demonstrated good agreement with the experimental bubble point data, exhibiting <4 % average deviation for the system. Notably, the PR-EoS outperformed the MFHEA-EoS, showing <3 % average deviation. Densities of CO<sub>2</sub> (99.5 %) with H<sub>2</sub> were measured at 278.14, 298.34, 323.55, and 348.40 K and pressures up to 35 MPa. While the densities of CO<sub>2</sub> (94.99 %) with H<sub>2</sub> were measured at 278.06, 288.13, 298.26, and 323.53 K and pressures up to 35 MPa using a vibrating tube densimeter which was calibrated using water and hydrogen. For the 99.5 % CO<sub>2</sub> binary mixture, the average absolute relative deviations (AARD) of the model predictions were 0.09 % and 0.26 % against MFHEA and PR EoS respectively. The AARD of the model predictions for the 94.99 % CO<sub>2</sub> were 0.33 % and 1.49 % with MFHEA and PR EoS respectively. Furthermore, even at low concentrations (0.5 %), the presence of H<sub>2</sub> led to a substantial reduction (>35 %) in the density of the mixture compared to that of pure CO<sub>2</sub> at lower pressure conditions with this effect becoming more pronounced at higher temperatures and concentrations of H<sub>2</sub>. Both models predicted the densities of the system well (with <2 % deviations from the experimental data), though MFHEA-Eos was more accurate with <0.4 % maximum relative deviation (MaxRD) for all the data points.</div></div>\",\"PeriodicalId\":12170,\"journal\":{\"name\":\"Fluid Phase Equilibria\",\"volume\":\"592 \",\"pages\":\"Article 114321\"},\"PeriodicalIF\":2.8000,\"publicationDate\":\"2025-01-03\",\"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/S0378381224002966\",\"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/S0378381224002966","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}
Bubble points and densities of H2 (up to ∼ 5%) in CO2-rich binary systems
In this study, experimental measurements of the bubble points of binary mixtures containing varying concentrations of CO2 (99.5 %, 99 %, 98.5 %,98 %, and ∼ 95 %) with hydrogen (H2) were made. These measurements were carried out from low temperatures (240.20 K) up to 294.84 K (with uncertainties of 0.14 K) using the constant composition expansion method. The experimental data were used to validate two thermodynamic models - the Peng-Robinson and Multi-Fluid Helmholtz Energy Approximation Equation of state (PR-EoS and MFHEA-EoS). From the results, the presence of H2 in CO2 at concentrations between 0.5 and 5 % caused a significant (∼19–980 %) positive deviation from the phase behaviour of CO2 stream compared to that of pure CO2. This effect intensified with higher concentrations of H2 and decreased with rising temperatures. Both models demonstrated good agreement with the experimental bubble point data, exhibiting <4 % average deviation for the system. Notably, the PR-EoS outperformed the MFHEA-EoS, showing <3 % average deviation. Densities of CO2 (99.5 %) with H2 were measured at 278.14, 298.34, 323.55, and 348.40 K and pressures up to 35 MPa. While the densities of CO2 (94.99 %) with H2 were measured at 278.06, 288.13, 298.26, and 323.53 K and pressures up to 35 MPa using a vibrating tube densimeter which was calibrated using water and hydrogen. For the 99.5 % CO2 binary mixture, the average absolute relative deviations (AARD) of the model predictions were 0.09 % and 0.26 % against MFHEA and PR EoS respectively. The AARD of the model predictions for the 94.99 % CO2 were 0.33 % and 1.49 % with MFHEA and PR EoS respectively. Furthermore, even at low concentrations (0.5 %), the presence of H2 led to a substantial reduction (>35 %) in the density of the mixture compared to that of pure CO2 at lower pressure conditions with this effect becoming more pronounced at higher temperatures and concentrations of H2. Both models predicted the densities of the system well (with <2 % deviations from the experimental data), though MFHEA-Eos was more accurate with <0.4 % maximum relative deviation (MaxRD) for all the data points.
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.