Simultaneous presentation of VLE, HE and cEp by the PRSV equation of state with the modified van der Waals one-fluid and Huron-Vidal-Orbey-Sandler mixing rules

被引:11
作者
Djordjevic, BD [1 ]
Kijevcanin, ML [1 ]
Serbanovic, SP [1 ]
机构
[1] Univ Belgrade, Fac Technol & Met, Dept Chem Engn, YU-11120 Belgrade, Yugoslavia
关键词
method of calculation; equation of state; excess function; heat capacity; enthalpy; vapor-liquid equilibria; mixture;
D O I
10.1016/S0378-3812(98)00474-9
中图分类号
O414.1 [热力学];
学科分类号
摘要
The Stryjek-Vera modification of the Peng-Robinson equation of state with two parameter van der Waals one-fluid mixing rule suggested by Schwartzentruber and Renon (SR) and the Orbey-Sandler modification of the Huron-Vidal mixing rule (HVOS) was applied for simultaneous description of vapor-liquid equilibrium (VLE), excess enthalpy (H-E) and excess heat capacity (c(p)(E)) data (VLE + H-E, H-E + C-p(E) VLE + c(p)(E) and VLE + HE + CpE). The HVOS mixing rule coupled with the NRTL equation using the temperature dependent parameters with six optimized coefficients gave mostly satisfactory results for simultaneous fitting of VLE + HE, VLE + c(p)(E), H-E + C-p(E) and VLE + H-E + c(p)(E) data of the non-ideal binary systems diverse complexity. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:205 / 218
页数:14
相关论文
共 61 条
[1]   Comparison of Gamma G excess mixing rules for multi-phase equilibria in some ternary systems [J].
AbdelGhani, RM ;
Heidemann, RA .
FLUID PHASE EQUILIBRIA, 1996, 116 (1-2) :495-502
[2]   EXCESS ENTHALPIES OF MIXTURES CONTAINING TETRAHYDROFURFURYLALCOHOL OR TETRAHYDROFURFURYLAMINE [J].
BOLINAGA, R ;
GRACIA, M ;
GUTIERREZLOSA, C .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1978, 10 (07) :667-673
[3]   PREDICTION OF VAPOR-LIQUID-EQUILIBRIUM WITH THE LCVM MODEL - A LINEAR COMBINATION OF THE VIDAL AND MICHELSEN MIXING RULES COUPLED WITH THE ORIGINAL UNIFAC AND THE T-MPR EQUATION OF STATE [J].
BOUKOUVALAS, C ;
SPILIOTIS, N ;
COUTSIKOS, P ;
TZOUVARAS, N ;
TASSIOS, D .
FLUID PHASE EQUILIBRIA, 1994, 92 :75-106
[4]   The Wong-Sandler mixing rules and EOS which are thermodynamically consistent at infinite pressure [J].
Brandani, F ;
Brandani, S ;
Brandani, V .
CHEMICAL ENGINEERING SCIENCE, 1998, 53 (04) :853-856
[5]   On the inapplicability of mixing rules based on the infinite pressure reference state for equations of state which use the hard-sphere repulsive term [J].
Brandani, S ;
Brandani, V .
FLUID PHASE EQUILIBRIA, 1996, 121 (1-2) :179-184
[6]   Excess molar enthalpies and excess molar heat capacities of (chloroform plus tetrahydrofuran plus cyclohexane) at the temperature 298.15 K [J].
Conti, G ;
Gianni, P ;
Tramati, M ;
Lepori, L ;
Matteoli, E .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1997, 29 (08) :865-877
[7]   EXCESS-ENTHALPIES AND EXCESS HEAT-CAPACITIES OF (N,N-DIMETHYLFORMAMIDE PLUS TETRAHYDROFURAN PLUS CYCLOHEXANE) AT THE TEMPERATURE 298.15-K [J].
CONTI, G ;
GIANNI, P ;
MATTEOLI, E .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1994, 26 (12) :1249-1257
[8]   EXCESS-ENTHALPIES AND EXCESS HEAT-CAPACITIES OF THE TERNARY-SYSTEM ETHANOL PLUS N,N-DIMETHYL-FORMAMIDE PLUS CYCLOHEXANE AT 298.15 K [J].
CONTI, G ;
GIANNI, P ;
LEPORI, L ;
MATTEOLI, E .
FLUID PHASE EQUILIBRIA, 1995, 105 (01) :93-107
[9]   EXCESS-ENTHALPIES AND EXCESS HEAT-CAPACITIES OF THE TERNARY-SYSTEM ETHANOL PLUS TETRAHYDROFURAN PLUS CYCLOHEXANE AT 298.15-K [J].
CONTI, G ;
GIANNI, P ;
MATTEOLI, E .
THERMOCHIMICA ACTA, 1994, 247 (02) :293-313
[10]   CAPABILITIES AND LIMITATIONS OF THE WONG-SANDLER MIXING RULES [J].
COUTSIKOS, P ;
KALOSPIROS, NS ;
TASSIOS, DP .
FLUID PHASE EQUILIBRIA, 1995, 108 (1-2) :59-78