The impressive impact of including enthalpy and heat capacity of mixing data when parameterising equations of state. Application to the development of the E-PPR78 (Enhanced-Predictive-Peng-Robinson-78) model

被引:15
作者
Jaubert, Jean-Noel [1 ]
Qian, Jun-Wei [1 ]
Lasala, Silvia [1 ]
Privat, Romain [1 ]
机构
[1] Univ Lorraine, Ecole Natl Super Ind Chim, CNRS, UMR 7274,Lab React & Gen Procedes, 1 Rue Grandville, F-54000 Nancy, France
关键词
PPR78; E-PPR78; Enthalpy of mixing; Heat capacity of mixing; Predictive model; VAPOR-LIQUID-EQUILIBRIA; EXCESS MOLAR ENTHALPIES; PRESSURE PHASE-EQUILIBRIA; GIBBS FREE-ENERGIES; SUPERCRITICAL CARBON-DIOXIDE; PENG-ROBINSON EOS; OCTANE-ENHANCING ADDITIVES; 2ND VIRIAL-COEFFICIENTS; ETHANE-PROPANE SYSTEM; NITROGEN PLUS WATER;
D O I
10.1016/j.fluid.2022.113456
中图分类号
O414.1 [热力学];
学科分类号
摘要
PPR78 (Predictive-Peng-Robinson78) is a well-established cubic equation of state in which, the temperature-dependent binary interaction parameters (bips) between two molecules i and j [k(ij) (T)] are predicted by a group-contribution method. In such a model, two group-binary-interaction parameters (G-bips), noted A(kl) and B-kl, are required per (k,l) pair of groups. The purpose of this article is to demonstrate that the inclusion of enthalpy and heat capacity of mixing data in the process of optimisation of the G-bips leads to a remarkable overall reduction of the error on such properties, from 841.51% to 51.42%, while keeping constant the accuracy in the prediction of VLE data, 8.6% (without inclusion of mixing properties) to 8.8% (with inclusion of mixing thermal properties). This new version of the PPR78 model (with the new sets of A(kl) and B-kl G-bips) has thus been called Enhanced-PPR78 (E-PPR78) model. From 2013 to 2017, this model was continuously developed and it is currently based on 40 groups. The many G-bips were fitted over 131,207 vapour liquid equilibrium data and 33,629 mixing properties data (h(M) and c(P)(M)) belonging to 1301 binary systems. After almost 18 years from the initial development of the PPR78 model, this paper summarizes for the first time the overall accuracy of the E-PPR78 model. (c) 2022 The Author(s). Published by Elsevier B.V.
引用
收藏
页数:46
相关论文
共 2055 条
[1]   PHASE-BEHAVIOR IN THE CRITICAL REGION OF 6 BINARY-MIXTURES OF 2-METHYLALKANES [J].
ABARA, JA ;
JENNINGS, DW ;
KAY, WB ;
TEJA, AS .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1988, 33 (03) :242-247
[2]   EXCESS PROPERTIES OF (ETHANE + PROPANE) (L) AND (CARBON-MONOXIDE + METHANE) (L) [J].
ADAMS, WR ;
GOPAL, P ;
ZOLLWEG, JA ;
STREETT, WB .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1987, 19 (01) :39-46
[3]  
Agarwal R, 2001, CHEM ENG PROG, V97, P64
[4]   Effect of impurities in captured CO2 on liquid-vapor equilibrium [J].
Ahmad, Mohammad ;
Gernert, Johannes ;
Wilbers, Erwin .
FLUID PHASE EQUILIBRIA, 2014, 363 :149-155
[5]   LOW-TEMPERATURE PHASE EQUILIBRIA - METHANE-PROPANE SYSTEM [J].
AKERS, WW ;
BURNS, JF ;
FAIRCHILD, WR .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (12) :2531-&
[6]   EXCESS-ENTHALPIES FOR THE BINARY-SYSTEMS NORMAL-OCTANE WITH 2-METHYLPENTANE AND 3-METHYLPENTANE [J].
AMELING, W ;
SIDDIQI, MA ;
LUCAS, K .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1983, 28 (02) :184-186
[7]  
AMICK EH, 1952, CHEM ENG PROG S SER, V48, P65
[8]  
Andrade M., 1970, ACTA CIENT COMPOSTEL, V7, P147
[9]  
[Anonymous], 1961, J CHEM ENG DATA, DOI DOI 10.1021/JE00103A023
[10]  
[Anonymous], 1967, PROC AM PET I DIV RE