Extension of the PPR78 model (Predictive 1978, Peng-Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing naphtenic compounds

被引:100
作者
Vitu, Stephane [1 ]
Jaubert, Jean-Noel [1 ]
Mutelet, Fabrice [1 ]
机构
[1] Ecole Natl Super Ind Chim, Inst Natl Polytech Lorraine, Lab Thermodynam Milieux Polyphases, F-54000 Nancy, France
关键词
equation of state; vapor-liquid equilibrium; predictive model; binary interaction parameters; critical locus;
D O I
10.1016/j.fluid.2006.02.004
中图分类号
O414.1 [热力学];
学科分类号
摘要
In 2004, we started to develop a group contribution method aimed at estimating the temperature dependent binary interaction parameters (k(ij)(T)) for the widely used Peng-Robinson equation of state (EOS). In this approach, the k(ij) between two components i and j is a function of temperature (T) and of the pure component critical temperatures (T-c.i and T-c.j), critical pressures (P-c.i and P-c.j) and acentric factors (omega(i), omega(j)). Because our model relies on the Peng-Robinson EOS as published by Peng and Robinson in 1978 and because the addition of a group contribution method to estimate the k(ij) makes it predictive, this model was called PPR78 (predictive 1978, Peng-Robinson EOS). In our previous papers eight groups were defined: CH3, CH2, CH, C, CH4 (methane), C2H6 (ethane), CHaro, and C-aro. It was thus possible to estimate the k(ij) for any mixture containing alkanes and aromatics whatever the temperature. In this study, the PPR78 model is extended to systems containing naphtenic (cyclic hydrocarbons) compounds. To do so, two new groups were added: CH2,cyclic and CHcyclic = C-cyclic (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:9 / 28
页数:20
相关论文
共 188 条
[1]   MEASUREMENT OF VAPOR-LIQUID-EQUILIBRIUM IN SYSTEMS WITH COMPONENTS OF VERY DIFFERENT VOLATILITY BY TOTAL PRESSURE STATIC METHOD [J].
AIM, K .
FLUID PHASE EQUILIBRIA, 1978, 2 (02) :119-142
[2]   NITROGEN SOLUBILITY AND VAPOR-PRESSURE OF BINARY MIXED-SOLVENTS CONTAINING BENZENE, CARBON-TETRACHLORIDE, CYCLOHEXANE AND 1-HEXANE [J].
AKIMOTO, T ;
NITTA, T ;
KATAYAMA, T .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1984, 17 (06) :637-641
[3]  
ANISIMOVA ZK, 1973, TEPLOFIZ SVOISTVA VE, P137
[4]   VAPOR-PRESSURES AND EXCESS GIBBS ENERGIES IN BINARY-MIXTURES OF HYDROCARBONS AT 313.15K .1. METHYLCYCLOHEXANE-BENZENE, METHYLCYCLOHEXANE-TOLUENE, METHYLCYCLOHEXANE-ORTHO-XYLENE, METHYCYCLOHEXANE-PARA-XYLENE, METHYLCYCLOHEXANE-ETHYLBENZENE, AND METHYLCYCLOHEXANE-PROPYLBENZENE [J].
ASMANOVA, N ;
GORAL, M .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1980, 25 (02) :159-161
[5]  
BARHALA A, 2001, REV ROUM CHIM, V46, P773
[7]   UNTERSUCHUNGEN UBER DAS DAMPF-FLUSSIGKEITS-PHASENGLEICHGEWICHT DES SYSTEMS N-HEXAN/METHYLCYCLOPENTAN/BENZOL BEI 60 DEGREES C UNTER VERWENDUNG EINER GASCHROMATOGRAPHISCHEN ANALYSENMETHODE [J].
BEYER, W ;
SCHUBERT.H ;
LEIBNITZ, E .
JOURNAL FUR PRAKTISCHE CHEMIE, 1965, 27 (5-6) :276-&
[8]  
BITTRICH HJ, 1979, Z PHYS CHEM-LEIPZIG, V260, P1005
[9]   VAPOR-LIQUID-EQUILIBRIA OF COAL-DERIVED LIQUIDS .3. BINARY-SYSTEMS WITH TETRALIN AT 200 MMHG [J].
BLANCO, B ;
BELTRAN, S ;
CABEZAS, JL ;
COCA, J .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1994, 39 (01) :23-26
[10]  
BOLDYREV AV, 1973, J APPL CHEM-USSR+, V46, P2338