Ten years with the CPA (Cubic-Plus-Association) equation of state. Part 1. Pure compounds and self-associating systems

被引:378
作者
Kontogeorgis, Georgios M. [1 ]
Michelsen, Michael L. [1 ]
Folas, Georgios K. [1 ]
Derawi, Samer [1 ]
von Solms, Nicolas [1 ]
Stenby, Erling H. [1 ]
机构
[1] Tech Univ Denmark, Ctr Phase Equilibria & Separat Proc IVC SEP, Dept Chem Engn, DK-2800 Lyngby, Denmark
关键词
D O I
10.1021/ie051305v
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
CPA (Cubic-Plus-Association) is an equation of state that is based on a combination of the Soave-Redlich-Kwong (SRK) equation with the association term of the Wertheim theory. The development of CPA started in 1995 as a research project funded by Shell ( Amsterdam), and the model was first published in 1996. Since then, it has been successfully applied to a variety of complex phase equilibria, including mixtures containing alcohols, glycols, organic acids, water, and hydrocarbons. Focus has been placed on cases of industrial importance, e. g., systems with gas-hydrate inhibitors ( methanol, glycols), glycol regeneration and gas dehydration units, oxygenate additives in gasoline, alcohol separation, etc. This manuscript, which is the first of a series of two papers, offers a review of previous applications and illustrates current focus areas related to the estimation of pure compound parameters, alcohol-hydrocarbon vapor-liquid equilibria (VLE) and solid-liquid equilibria (SLE), as well as aqueous systems. The capabilities and limitations of CPA are discussed and suggestions for extension of the model to systems not covered in this work are provided.
引用
收藏
页码:4855 / 4868
页数:14
相关论文
共 94 条
[1]   EXTENSION OF THE AEOS MODEL TO SYSTEMS CONTAINING ANY NUMBER OF ASSOCIATING AND INERT COMPONENTS [J].
ANDERKO, A .
FLUID PHASE EQUILIBRIA, 1989, 50 (1-2) :21-52
[2]   A SIMPLE EQUATION OF STATE INCORPORATING ASSOCIATION [J].
ANDERKO, A .
FLUID PHASE EQUILIBRIA, 1989, 45 (01) :39-67
[3]  
[Anonymous], 2001, PHYS THERMODYNAMIC P
[4]   Challenges in thermodynamics [J].
Arlt, W ;
Spuhl, O ;
Klamt, A .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (03) :221-238
[5]   VAPOR-LIQUID-EQUILIBRIUM IN THE BUTYL ALCOHOL - N-DECANE SYSTEM AT 85, 100 AND 115-DEGREES-C [J].
BERNATOVA, S ;
LINEK, J ;
WICHTERLE, I .
FLUID PHASE EQUILIBRIA, 1992, 74 :127-132
[6]   EXCESS GIBBS ENERGIES AND EXCESS VOLUMES OF 1-BUTANOL NORMAL-HEXANE AND 2-METHYL-1-PROPANOL NORMAL-HEXANE BINARY-SYSTEMS [J].
BERRO, C ;
ROGALSKI, M ;
PENELOUX, A .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1982, 27 (03) :352-355
[7]   A novel experimental technique for measuring methanol partitioning between aqueous and hydrocarbon phases at pressures up to 69 MPa [J].
Bruinsma, DFM ;
Desens, JT ;
Notz, PK ;
Sloan, ED .
FLUID PHASE EQUILIBRIA, 2004, 222 :311-315
[8]   ELECTROSTATIC MODELS OF HYDROGEN-BONDED DIMERS - A DONOR-ACCEPTOR SCALE FOR HYDROGEN HALIDES AND PSEUDOHALIDES [J].
BUCKINGHAM, AD ;
FOWLER, PW .
JOURNAL OF MOLECULAR STRUCTURE, 1988, 189 (1-2) :203-210
[9]   (VAPOR + LIQUID) EQUILIBRIUM BEHAVIOR OF (N-PENTANE + ETHANOL) AT 372.7, 397.7, AND 422.6 K [J].
CAMPBELL, SW ;
WILSAK, RA ;
THODOS, G .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1987, 19 (05) :449-460
[10]   CHEMICAL THEORY FOR MIXTURES CONTAINING ANY NUMBER OF ALCOHOLS [J].
CAMPBELL, SW .
FLUID PHASE EQUILIBRIA, 1994, 102 (01) :61-84