Some useful expressions for deriving component fugacity coefficients from mixture fugacity coefficient

被引:7
作者
Hu, Jiawen [1 ,2 ]
Wang, Rong [3 ]
Mao, Shide [4 ]
机构
[1] Shijiazhuang Univ Econ, Coll Resources, Shijiazhuang 050031, Peoples R China
[2] Chinese Acad Sci, Inst Geol & Geophys, Key Lab Mineral Resources, Beijing 100029, Peoples R China
[3] Nanjing Univ, Sch Chem & Chem Engn, Nanjing 210093, Peoples R China
[4] China Univ Geosci, Sch Earth Sci & Resources, Beijing 100083, Peoples R China
关键词
mixture fugacity coefficient; component fugacity coefficient; equation of state; pressure-explicit; volume-explicit;
D O I
10.1016/j.fluid.2008.03.007
中图分类号
O414.1 [热力学];
学科分类号
摘要
It is proved that the fugacity coefficient (phi) of a mixture and the fugacity coefficient of component i ((phi) over cap) follow the relation In = [partial derivative(n In (phi) over cap)/partial derivative n(i)](T,P,nj)(j not equal i), = [partial derivative(n In phi)/partial derivative n(i)] where n(i) is the amount-of-substance of component i, and T, P, V-t and n are the temperature, pressure, total volume and total amount-of-substance of the system, respectively. This relation is very useful for. the derivation of (phi) over cap (i). It allows the phi function to contain both P and V, so phi can be expressed with various equations of state (either volume-explicit or pressure-explicit). This approach can also use the similarity of the phi expressions of pure fluids and mixtures to simplify the derivation of (phi) over cap. Besides, (phi) over cap can also be directly derived from equation of state through a variation of the approach above. These approaches are much easier than the commonly used ones when the equation of state for fluids is complex. (C) 2008 Elsevier B.V. All rights reserved.
引用
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页码:7 / 13
页数:7
相关论文
共 31 条
[1]  
[Anonymous], 1979, CHEM THERMODYNAMICS
[2]  
[Anonymous], 1947, INTRO CHEM ENG THERM
[3]   HARD-SPHERE EQUATION OF STATE [J].
BOUBLIK, T .
JOURNAL OF CHEMICAL PHYSICS, 1970, 53 (01) :471-&
[4]   Coordination number models and equations of state for square-well pure and mixture fluids, Part I: Coordination number models and Monte Carlo simulation at high density [J].
Cao, DP ;
Wang, WC .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (11) :2099-2109
[5]   A REAL FUNCTION REPRESENTATION FOR THE STRUCTURE OF THE HARD-SPHERE FLUID [J].
CHANG, J ;
SANDLER, SI .
MOLECULAR PHYSICS, 1994, 81 (03) :735-744
[6]  
Chen Z.X., 2001, CHEM ENG THERMODYNAM
[7]   A new cubic equation of state and its applications to the modeling of vapor-liquid equilibria and volumetric properties of natural fluids [J].
Duan, ZH ;
Hu, JW .
GEOCHIMICA ET COSMOCHIMICA ACTA, 2004, 68 (14) :2997-3009
[8]   An equation of state for silicate melts. I. Formulation of a general model [J].
Ghiorso, MS .
AMERICAN JOURNAL OF SCIENCE, 2004, 304 (8-9) :637-678
[9]   Volume-explicit equation of state and phase behavior for mixtures of hard disks [J].
Hamad, EZ ;
Yahaya, GO .
FLUID PHASE EQUILIBRIA, 2000, 168 (01) :59-69
[10]   A general local composition and coordination number model for square-well fluids with variable well width and diameter ratio [J].
Hu, Jiawen ;
Duan, Zhenhao ;
Shi, Xunli ;
Zhu, Ji .
MOLECULAR PHYSICS, 2007, 105 (08) :1019-1037