Romain Privat , Jean-Noël Jaubert , Georgios M. Kontogeorgis
{"title":"让我们重新考虑三次状态方程的高级混合规则","authors":"Romain Privat , Jean-Noël Jaubert , Georgios M. Kontogeorgis","doi":"10.1016/j.fluid.2025.114455","DOIUrl":null,"url":null,"abstract":"<div><div>One of the most challenging aspects of using a Van der Waals type equation of state for mixtures is determining the appropriate expressions for the coefficients <span><math><mi>a</mi></math></span> (attractive parameter) and <span><math><mi>b</mi></math></span> (covolume) involved in this equation. It has been 45 years since Huron and Vidal first proposed the “EoS/<span><math><msup><mi>g</mi><mi>E</mi></msup></math></span>” advanced mixing rules. By equating under infinite reference pressure, the mathematical expression of the excess Gibbs energy <span><math><msup><mi>g</mi><mi>E</mi></msup></math></span> derived from an equation of state, to the same quantity issued from an explicit activity coefficient model, they deduced an expression for the ratio <span><math><mrow><mi>a</mi><mo>/</mo><mi>b</mi></mrow></math></span>. A decade after Huron and Vidal’s initial proposal, building upon the original proposal, Michelsen subsequently derived the “zero reference pressure” (ZRP) approach and proposed the approximate ZRP mixing rules MHV1 and MHV2. Throughout the 1990′s and 2000′s, the Huron-Vidal and ZRP approaches were subject, often empirically, to multiple revisions in order to remedy some of their well identified shortcomings. It would appear that the debates surrounding advanced mixing rules are now over, with the latest conclusions proposed in the 2000s enjoying a degree of consensus.</div><div>The objective of this article is to reopen the debate in light of the scientific insights gained from our recent research on advanced mixing rules for cubic equations of state. The concept of deriving mixing rules by equating the excess Gibbs energy expressed from an equation of state to the same quantity expressed from an activity coefficient model (this equality is called a “<em>matching equation”</em>) was undoubtedly an appealing one. However, experience has shown that such a matching equation is not without its limitations, particularly due to the lack of sufficient constraints. We have reached the conclusion that the only way to derive advanced mixing rules that are free from shortcomings is to ensure that not only are the complete expressions of <span><math><msup><mi>g</mi><mi>E</mi></msup></math></span> from an equation of state and from an activity coefficient model equal but also that the three separate contributions that make it up (i.e., combinatorial, residual and the product of the pressure by the excess volume <span><math><mrow><mi>P</mi><mo>·</mo><msup><mi>v</mi><mi>E</mi></msup></mrow></math></span>) are equal. As discussed in this paper, achieving this objective is challenging and we conclude that the best and unique solution for developing safe mixing rules is to modify the matching equation proposed by Huron-Vidal and Michelsen and to only equate the residual contributions.</div><div>Based on this observation, we demonstrate how the demonstrations of the ZRP and HV mixing rules can be reworked to arrive at a unique and universal (independent of the reference pressure) mixing rule, called UHVM (Unified Huron Vidal Michelsen) mixing rule. We hope that this result will encourage new thinking on mixing rules for cubic equations.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"596 ","pages":"Article 114455"},"PeriodicalIF":2.7000,"publicationDate":"2025-04-27","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Let us rethink advanced mixing rules for cubic equations of state\",\"authors\":\"Romain Privat , Jean-Noël Jaubert , Georgios M. Kontogeorgis\",\"doi\":\"10.1016/j.fluid.2025.114455\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>One of the most challenging aspects of using a Van der Waals type equation of state for mixtures is determining the appropriate expressions for the coefficients <span><math><mi>a</mi></math></span> (attractive parameter) and <span><math><mi>b</mi></math></span> (covolume) involved in this equation. It has been 45 years since Huron and Vidal first proposed the “EoS/<span><math><msup><mi>g</mi><mi>E</mi></msup></math></span>” advanced mixing rules. By equating under infinite reference pressure, the mathematical expression of the excess Gibbs energy <span><math><msup><mi>g</mi><mi>E</mi></msup></math></span> derived from an equation of state, to the same quantity issued from an explicit activity coefficient model, they deduced an expression for the ratio <span><math><mrow><mi>a</mi><mo>/</mo><mi>b</mi></mrow></math></span>. A decade after Huron and Vidal’s initial proposal, building upon the original proposal, Michelsen subsequently derived the “zero reference pressure” (ZRP) approach and proposed the approximate ZRP mixing rules MHV1 and MHV2. Throughout the 1990′s and 2000′s, the Huron-Vidal and ZRP approaches were subject, often empirically, to multiple revisions in order to remedy some of their well identified shortcomings. It would appear that the debates surrounding advanced mixing rules are now over, with the latest conclusions proposed in the 2000s enjoying a degree of consensus.</div><div>The objective of this article is to reopen the debate in light of the scientific insights gained from our recent research on advanced mixing rules for cubic equations of state. The concept of deriving mixing rules by equating the excess Gibbs energy expressed from an equation of state to the same quantity expressed from an activity coefficient model (this equality is called a “<em>matching equation”</em>) was undoubtedly an appealing one. However, experience has shown that such a matching equation is not without its limitations, particularly due to the lack of sufficient constraints. We have reached the conclusion that the only way to derive advanced mixing rules that are free from shortcomings is to ensure that not only are the complete expressions of <span><math><msup><mi>g</mi><mi>E</mi></msup></math></span> from an equation of state and from an activity coefficient model equal but also that the three separate contributions that make it up (i.e., combinatorial, residual and the product of the pressure by the excess volume <span><math><mrow><mi>P</mi><mo>·</mo><msup><mi>v</mi><mi>E</mi></msup></mrow></math></span>) are equal. As discussed in this paper, achieving this objective is challenging and we conclude that the best and unique solution for developing safe mixing rules is to modify the matching equation proposed by Huron-Vidal and Michelsen and to only equate the residual contributions.</div><div>Based on this observation, we demonstrate how the demonstrations of the ZRP and HV mixing rules can be reworked to arrive at a unique and universal (independent of the reference pressure) mixing rule, called UHVM (Unified Huron Vidal Michelsen) mixing rule. We hope that this result will encourage new thinking on mixing rules for cubic equations.</div></div>\",\"PeriodicalId\":12170,\"journal\":{\"name\":\"Fluid Phase Equilibria\",\"volume\":\"596 \",\"pages\":\"Article 114455\"},\"PeriodicalIF\":2.7000,\"publicationDate\":\"2025-04-27\",\"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/S0378381225001256\",\"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/S0378381225001256","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}
Let us rethink advanced mixing rules for cubic equations of state
One of the most challenging aspects of using a Van der Waals type equation of state for mixtures is determining the appropriate expressions for the coefficients (attractive parameter) and (covolume) involved in this equation. It has been 45 years since Huron and Vidal first proposed the “EoS/” advanced mixing rules. By equating under infinite reference pressure, the mathematical expression of the excess Gibbs energy derived from an equation of state, to the same quantity issued from an explicit activity coefficient model, they deduced an expression for the ratio . A decade after Huron and Vidal’s initial proposal, building upon the original proposal, Michelsen subsequently derived the “zero reference pressure” (ZRP) approach and proposed the approximate ZRP mixing rules MHV1 and MHV2. Throughout the 1990′s and 2000′s, the Huron-Vidal and ZRP approaches were subject, often empirically, to multiple revisions in order to remedy some of their well identified shortcomings. It would appear that the debates surrounding advanced mixing rules are now over, with the latest conclusions proposed in the 2000s enjoying a degree of consensus.
The objective of this article is to reopen the debate in light of the scientific insights gained from our recent research on advanced mixing rules for cubic equations of state. The concept of deriving mixing rules by equating the excess Gibbs energy expressed from an equation of state to the same quantity expressed from an activity coefficient model (this equality is called a “matching equation”) was undoubtedly an appealing one. However, experience has shown that such a matching equation is not without its limitations, particularly due to the lack of sufficient constraints. We have reached the conclusion that the only way to derive advanced mixing rules that are free from shortcomings is to ensure that not only are the complete expressions of from an equation of state and from an activity coefficient model equal but also that the three separate contributions that make it up (i.e., combinatorial, residual and the product of the pressure by the excess volume ) are equal. As discussed in this paper, achieving this objective is challenging and we conclude that the best and unique solution for developing safe mixing rules is to modify the matching equation proposed by Huron-Vidal and Michelsen and to only equate the residual contributions.
Based on this observation, we demonstrate how the demonstrations of the ZRP and HV mixing rules can be reworked to arrive at a unique and universal (independent of the reference pressure) mixing rule, called UHVM (Unified Huron Vidal Michelsen) mixing rule. We hope that this result will encourage new thinking on mixing rules for cubic equations.
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.