Fluid Phase Equilibria最新文献

{"title":"A robust and efficient augmented free-water flash method for CO2-water-hydrocarbon mixtures","authors":"Juan Heringer ,&nbsp;Michiel Wapperom ,&nbsp;Catinca Secuianu ,&nbsp;Denis Voskov ,&nbsp;Dan Vladimir Nichita","doi":"10.1016/j.fluid.2025.114378","DOIUrl":"10.1016/j.fluid.2025.114378","url":null,"abstract":"<div><div>Three-phase equilibrium calculations for water-CO₂-hydrocarbon mixtures are required in the compositional simulation of various applications in CO₂ storage, geothermal systems, and enhanced oil recovery. The very low solubility of hydrocarbon components in water leads to a special mathematical structure of the problem. Several techniques were suggested, such as the free-water flash (FWF) and the augmented free-water flash (AFWF); in the former, the aqueous phase is pure water, while in the latter only certain components, CO₂ or methane for example, are dissolved in the aqueous phase. However, only the first-order successive substitution method was used in the previous published approaches, making them unattractive for compositional simulations in which a significant number of phase equilibrium calculations are performed. In this work, a robust and efficient AFWF method is proposed, using combined successive substitutions-modified Newton iterations. The new method is general, allowing partial solubility of any selected component in the water-rich phase, depending on the specific compositions and operating conditions. A detailed description of second-order methods in a Gibbs energy minimization framework for the general AFWF is presented. In the AFWF, the dimension of the problem and the number of function evaluations (thus the computation time) are significantly reduced. Moreover, it is shown that the augmented method always has better convergence properties than its conventional multiphase flash counterpart, in both first- and second-order methods. The new AFWF method is tested for various hydrocarbon-water-CO₂ mixtures and proved to be robust and efficient, systematically outperforming the conventional approach. Unlike in previous AFWF formulations, the number of components soluble in water is not limited, leading to a controlled accuracy with respect to a full three-phase equilibrium, even at high pressures and/or large amounts of CO₂.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"594 ","pages":"Article 114378"},"PeriodicalIF":2.8,"publicationDate":"2025-02-12","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143437709","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Chemical equilibrium and liquid–liquid equilibrium in ternary mixtures of formaldehyde, water, and isobutanol/ n-butanol between 295 K and 348 K","authors":"Lukas Winklbauer,&nbsp;Jakob Burger","doi":"10.1016/j.fluid.2025.114364","DOIUrl":"10.1016/j.fluid.2025.114364","url":null,"abstract":"<div><div>Mixtures of formaldehyde, water, and isobutanol/ n-butanol exhibit a ternary liquid–liquid equilibrium, as water and butanol are only partially miscible. In the present work, we study the chemical and liquid–liquid equilibria of the systems (formaldehyde + water + isobutanol) and (formaldehyde + water + n-butanol). The species distributions in the chemical equilibrium of both systems are measured between 298<!--> <!-->K and 348<!--> <!-->K using nuclear magnetic resonance (NMR) spectroscopy. Ternary liquid–liquid equilibrium data are reported between 295<!--> <!-->K and 324<!--> <!-->K. The experimental data is used to develop a model of the reactive liquid–liquid equilibria for mixtures of formaldehyde, water, and isobutanol/n-butanol.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"594 ","pages":"Article 114364"},"PeriodicalIF":2.8,"publicationDate":"2025-02-12","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143455023","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Measurement and correlation of the solubility of Hydrogen in Acetophenone and 1-Methylnaphthalene","authors":"Junwei Cui ,&nbsp;Abdul Mosaur Waseel ,&nbsp;Qing Duan ,&nbsp;Yike Gao ,&nbsp;Chenyang Zhang ,&nbsp;Tao Yang ,&nbsp;Shengshan Bi","doi":"10.1016/j.fluid.2025.114386","DOIUrl":"10.1016/j.fluid.2025.114386","url":null,"abstract":"<div><div>Hydrogen (H₂) solubility in liquid organic hydrogen carriers (LOHCs) is crucial for their widespread applications. This work investigates the solubility of H₂ <em>x</em> in two promising LOHCs: Acetophenone (APO) and 1-Methylnaphthalene (1-MN). Measurements were conducted using an isochoric saturation method within a temperature range of 293 to 363 K and pressures up to 5.8 MPa. The liquid densities <em>ρ</em> of APO and 1-MN, essential for characterizing H₂ solubility, were measured using a vibrating tube densitometer (DMA5000 M) at approximately 0.1 MPa. The experimental <em>ρ</em> for APO and 1-MN were compared with literature data and good agreement can be found. The Krichevsky-Kasarnovsky(K-K) equation was employed to correlate H₂ solubility <em>x</em> in APO and 1-MN, with deviations of mostly within 6 % and 10 %, respectively. Following, the behavior of H₂ solubility <em>x</em> concerning pressure along isothermal lines was analyzed. Finally, the thermodynamic parameter of dissolution of the two binary systems were studied. The enthalpy of dissolution is positive for all the systems, while the entropy of dissolution is negative. Under the same temperature, the Gibbs free energy of dissolution for the H₂ + APO system is smaller than that of the H₂ + 1-MN system.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"594 ","pages":"Article 114386"},"PeriodicalIF":2.8,"publicationDate":"2025-02-12","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143421827","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"An azeotrope in the desert","authors":"Michael Kleiber","doi":"10.1016/j.fluid.2025.114359","DOIUrl":"10.1016/j.fluid.2025.114359","url":null,"abstract":"<div><div>One of the most exciting applications of thermodynamics in chemical industry is the separation of azeotropes. The azeotrope in the system tetrahydrofuran — water seems to be an easy one, as it can be separated in two columns without the help of a selective agent by pressure-swing distillation. The topic of this paper is a case where this principle was applied. As well, a number of other components had to be separated so that two further distillation columns had to be provided. To everyone’s surprise, the water content could often not be kept below the target value of 300<!--> <!-->ppm so that the product was off-spec. The various possible reasons were regarded. While almost everyone concluded that the azeotropic separation did not work, some thermodynamic considerations suggested that the pressure-swing distillation seemed to do its job. To find the reason of the failure, a hygrometer had been calibrated in a way that it could instantaneously indicate the water content in the tetrahydrofuran. It could be proven that the azeotrope of the tetrahydrofuran — water was properly separated. The reason for the moisture in the product could be located downstream the azeotropic separation and easily been corrected.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"594 ","pages":"Article 114359"},"PeriodicalIF":2.8,"publicationDate":"2025-02-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143394513","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Thermodynamic modeling of sugars solubility in pure and mixed solvents using the perturbed hard sphere chain equation of state","authors":"Ayat Hussein Adhab ,&nbsp;Morug Salih Mahdi ,&nbsp;Prakash Kanjariya ,&nbsp;Shelesh krishna saraswat ,&nbsp;Rekha M M ,&nbsp;Pushpa Negi Bhakuni ,&nbsp;Abhayveer Singh ,&nbsp;Bhavik Jain ,&nbsp;Aseel Salah Mansoor ,&nbsp;Usama Kadem Radi ,&nbsp;Nasr Saadoun Abd","doi":"10.1016/j.fluid.2025.114368","DOIUrl":"10.1016/j.fluid.2025.114368","url":null,"abstract":"<div><div>In this work, the Perturbed Hard Sphere Chain (PHSC) equation of state (EoS) has been utilized to model the solubility of sugars in pure and mixed solvents. In this regard, thirteen sugars containing glucose, fructose, xylose, maltose, mannitol, mannose, sorbitol, xylitol, galactose, erythritol, maltitol, trehalose, and sucrose have been considered. The model parameters have been optimized using a binary sugar-water equilibrium data at an arbitrary temperature. The solubilities of sugars in water and alcohols at various temperatures have been predicted using the obtained model parameters. The average AAD% value of sugar solubility in pure solvents has been obtained 0.98%. The model was also applied to predict the solubility of sugars in mixed solvents without using additional adjustable parameters. The results show that the PHSC EoS can predict the solubility of sugars in mixed solvents up to high concentrations accurately. The average AAD% value of the ternary sugar-water-alcohol system has been obtained 6.5%. The results show that the PHSC EoS can be used as a robust thermodynamic model to predict the solubilities of sugars in mixed solvents up to high concentrations and various temperatures accurately.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"594 ","pages":"Article 114368"},"PeriodicalIF":2.8,"publicationDate":"2025-02-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143394512","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Measurement of density, viscosity and vapor pressure of tetrakis(trimethylsiloxy)silane, 3-ethenyl-1,1,1,5,5,5-hexamethyl-3-[(trimethylsilyl)oxy]trisiloxane and (γ-chloropropyl)tri(trimethylsiloxy)silane","authors":"Xu Long,&nbsp;Tingyu Liu,&nbsp;Shuting Zhang,&nbsp;Hong Dong,&nbsp;Chuan Wu","doi":"10.1016/j.fluid.2025.114367","DOIUrl":"10.1016/j.fluid.2025.114367","url":null,"abstract":"<div><div>The saturation temperatures of tetrakis(trimethylsiloxy)silane (TTMS), 3-ethenyl-1,1,1,5,5,5-hexamethyl-3-[(trimethylsilyl)oxy]trisiloxane (VTMS) and (γ-chloropropyl)tri(trimethylsiloxy)silane (TClTMS) were measured over the pressure ranges (3.000 to 91.000) kPa. The density data and viscosity values of TTMS, VTMS, and TClTMS were obtained over the temperature ranges (298.15 to 328.15) K. The density values show a reasonable correlation that can be accurately described with a linear equation. The relationship between the viscosity of these compounds and temperature is strongly supported by the Ghatee, Litovitz, Andrade, and Vogel-Tammann-Fulcher equations, demonstrating their reliability and predictive power. The saturated vapor pressure values were estimated using the Clarke-Glew and Antoine equations. The critical properties of pressure, temperature, and volume were calculated using the group contribution method, specifically the Nannoolal model. The acentric factor (<em>ω</em>) at a reduced vapor pressure was calculated by these critical parameters. The calculated ESP map, HOMO and LUMO energy display the electron density and potential energy. The thermodynamic properties of TTMS, VTMS, and TClTMS are crucial values for designing and operating industrial separation processes.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"595 ","pages":"Article 114367"},"PeriodicalIF":2.8,"publicationDate":"2025-02-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143592505","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Accurate calculation and reliable prediction of second virial coefficients for nonpolar mixtures","authors":"Liu Xu ,&nbsp;Kang Qin ,&nbsp;Yuan-Yuan Duan","doi":"10.1016/j.fluid.2025.114365","DOIUrl":"10.1016/j.fluid.2025.114365","url":null,"abstract":"<div><div>The virial equation of state has a theoretical advantage in the calculations of mixtures. The second mixture virial coefficients are with the theoretically rigid mixing rules and composed of the second virial coefficients for pure fluids and the cross second virial coefficients. Based on the generalized corresponding state principle second virial coefficient model for pure fluids we proposed before, the generalized cross second virial coefficient models were established with three characteristic parameters for nonpolar binaries in this work. The calculation of the mixture critical temperature requires the binary interaction coefficients (<em>k_ij</em>). The mixture acentric factor was determined by the arithmetic mean. The mixture critical pressure could be calculated without the critical specific volume. For the most sensitive mixing rule of the mixture critical temperature, the <em>k_ij</em> was optimized for 145 nonpolar binaries. An easily accessible characteristic correlating parameter, the reduced diameter, was proposed to develop the predictive <em>k_ij</em> correlations for common nonpolar binaries. Due to the complex intermolecular interactions between two different molecules, the <em>k_ij</em> correlations were proposed respectively for alkane/alkane binaries, nonpolar binaries containing fluorocarbon, nonpolar binaries containing nitrogen or oxygen, nonpolar binaries containing simple fluids, nonpolar binaries containing carbon dioxide and nonpolar binaries containing neon. Our work was validated to perform satisfactorily from the comparison with the Chueh-Prausnitz <em>k_ij</em> correlation, Fender-Halsey <em>k_ij</em> correlation, and Meng <em>k_ij</em> correlation. Together with our previous work, this work could accurately calculate and reliably predict the second virial coefficients for common nonpolar mixtures.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"593 ","pages":"Article 114365"},"PeriodicalIF":2.8,"publicationDate":"2025-02-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143372510","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Evaluation of thermodynamic models for the prediction of derivative properties for non-polar compounds","authors":"Javad Amanabadi,&nbsp;Georgios M. Kontogeorgis,&nbsp;Xiaodong Liang","doi":"10.1016/j.fluid.2025.114366","DOIUrl":"10.1016/j.fluid.2025.114366","url":null,"abstract":"<div><div>Thermodynamic models have been developed for many decades, while a persistent challenge remains in identifying the most effective model for specific systems. In this study, a wide range of thermodynamic models, including SRK, PR, CPA, CK-SAFT, PC-SAFT, SAFT-VR Mie, SAFT-γ Mie, and GERG-2008, have been analyzed to evaluate their performance in predicting the first- and second-order derivative properties of compounds such as alkanes, N₂, and CO₂. Properties such as saturation pressure, liquid density, isobaric and isochoric heat capacities including their residual terms, speed of sound, and Joule-Thomson coefficient have been examined. While GERG-2008, as a multiparameter equation of state consistently outperforms other models across most properties, among general thermodynamic models, SAFT-VR Mie and SAFT-γ Mie have demonstrated superior performance over conventional cubic models, particularly in predicting second-order derivative properties, and PC-SAFT has shown superior results for isobaric heat capacity and Joule-Thomson coefficient. To gain deeper insights into the results, further examination of the model's performance in predicting selected second-order derivative properties (<em>dP/dT, dP/dV</em>, <span><math><msub><mrow><mo>(</mo><mrow><msup><mrow><mi>∂</mi></mrow><mn>2</mn></msup><msup><mrow><mi>A</mi></mrow><mtext>res</mtext></msup><mo>/</mo><mi>∂</mi><msup><mrow><mi>V</mi></mrow><mn>2</mn></msup></mrow><mo>)</mo></mrow><mrow><mi>T</mi><mo>,</mo><mi>n</mi></mrow></msub></math></span>, <span><math><msub><mrow><mo>(</mo><mrow><msup><mrow><mi>∂</mi></mrow><mn>2</mn></msup><msup><mrow><mi>A</mi></mrow><mtext>res</mtext></msup><mo>/</mo><mi>∂</mi><mi>T</mi><mi>∂</mi><mi>V</mi></mrow><mo>)</mo></mrow><mi>n</mi></msub></math></span>, and <span><math><msub><mrow><mo>(</mo><mrow><msup><mrow><mi>∂</mi></mrow><mn>2</mn></msup><msup><mrow><mi>A</mi></mrow><mtext>res</mtext></msup><mo>/</mo><mi>∂</mi><msup><mrow><mi>T</mi></mrow><mn>2</mn></msup></mrow><mo>)</mo></mrow><mrow><mi>V</mi><mo>,</mo><mi>n</mi></mrow></msub></math></span>) has been conducted. Additionally, the contributions of hard-sphere, chain, and dispersion terms to the second-order derivatives of Helmholtz energy have been analyzed, highlighting the significant impact of these terms on volume and temperature derivatives. This manuscript also discusses possible challenges and potential improvements in these models' predictive capabilities.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"594 ","pages":"Article 114366"},"PeriodicalIF":2.8,"publicationDate":"2025-02-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143445152","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Solubility of Acetone-Methanol Mixtures in Matrimid Glassy Polymer: Experimental Data and Modelling through NET-GP and PC-SAFT","authors":"Lorenzo Merlonghi,&nbsp;Ferruccio Doghieri,&nbsp;Marco Giacinti Baschetti","doi":"10.1016/j.fluid.2025.114362","DOIUrl":"10.1016/j.fluid.2025.114362","url":null,"abstract":"<div><div>In this work, the PC-SAFT equation of state and the NET-GP approach have been considered for the description of the thermodynamic equilibrium between liquid acetone-methanol mixture and Matrimid glassy polymer. Pure component parameters of the PC-SAFT EoS for the system under consideration were retrieved from literature and checked by predicting the vapor pressure and saturated molar volumes of both Methanol and Acetone. Considering the binary mixture, isothermal VLE data at 35°C were fitted by using PC-SAFT, in order to derive binary interaction coefficients, the latter then proved to be able to correctly describe also the volume of the liquid mixture at 35°C and 1 bar. Considering the binary Acetone-Matrimid and Methanol-Matrimid systems, binary interaction and swelling coefficients needed for the description of the glassy phase were retrieved by fitting pure component vapor sorption isotherms at 35°C through the NET-GP approach coupled with PC-SAFT equation of state. Finally, based on the parameters obtained from the binary mixtures, the ternary Acetone-Methanol-Matrimid system at 35°C and 1 bar was predicted, without using additional parameters. The results were compared with experimental data related to liquid sorption in the polymer as obtained by coupling FTIR-ATR analysis and gravimetric methods. The agreement was remarkable testifying to the ability of the proposed approach to describe sorption of binary mixtures involving hydrogen bonding compounds in glassy polymers.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"593 ","pages":"Article 114362"},"PeriodicalIF":2.8,"publicationDate":"2025-02-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143372512","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Multiscale modeling of dimerization thermodynamics of formic acid","authors":"Dominika O. Wasik ,&nbsp;Silvia Lasala ,&nbsp;Olivier Herbinet ,&nbsp;Konstantin Samukov ,&nbsp;Sofía Calero ,&nbsp;Thijs J.H. Vlugt","doi":"10.1016/j.fluid.2025.114356","DOIUrl":"10.1016/j.fluid.2025.114356","url":null,"abstract":"<div><div>Heat pumps, which recycle waste heat, are a promising technology for reducing CO<span><math><msub><mrow></mrow><mrow><mn>2</mn></mrow></msub></math></span> emissions. Efficiently using low-grade waste heat remains challenging due to the limitations of standard heat exchangers and the need for more effective working fluids. This work introduces a multi-scale methodology that combines force field-based Monte Carlo simulations, quantum mechanics, and equations of state to explore the potential of formic acid as a new reactive fluid in thermodynamic cycles. Formic acid exhibits dimerization behavior, forming cyclic dimers in the gas phase, which can enhance the thermodynamic efficiency of heat recovery systems. The dimerization reaction of formic acid is crucial because it integrates chemical energy into thermodynamic processes, potentially improving the performance of heat pumps and other energy systems. The study implements umbrella sampling in Monte Carlo simulations to compute the thermodynamic properties of HCOOH dimerization, including equilibrium constants, enthalpy, and entropy. Results from two different methods to study dimer formation, namely the dimer counter method and the potential of mean force method, show strong agreement with the enthalpy of dimerization of −60.46 kJ mol⁻¹ and −62.91 kJ mol⁻¹, and entropy of −137.36 J mol⁻¹K⁻¹ and −146.98 J mol⁻¹K⁻¹, respectively. A very good agreement of the Monte Carlo results with Quantum Mechanics and experimental data validates the accuracy of the simulations. For phase equilibrium properties, the Peng–Robinson equation of state, coupled with advanced mixing rules, was applied and compared to Monte Carlo simulations in the Gibbs ensemble. This approach enabled the determination of the Global Phase Equilibrium of the system, vaporization enthalpy, phase composition, vapor and liquid densities of the coexisting phases, and entropy as a function of temperature. The agreement between the thermodynamic model and Monte Carlo simulations confirms the reliability of the methodology in capturing the phase behavior of the system. The findings demonstrate a promising approach for discovering and characterizing new reactive fluids, contributing to more efficient and sustainable energy technologies.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"594 ","pages":"Article 114356"},"PeriodicalIF":2.8,"publicationDate":"2025-02-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143353411","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}