Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)

被引:11
作者
Mascato, Eva [1 ]
Mussari, Lelia [2 ]
Postigo, Miguel [2 ]
Mariano, Alejandra B. [2 ]
Pineiro, Manuel M. [1 ]
Legido, Jose Luis [1 ]
Andrade, M. I. Paz [3 ]
机构
[1] Univ Vigo, Fac Ciencias, Dept Fis Aplicada, E-36310 Vigo, Spain
[2] Univ Nacl Comahue, Fac Ingn, Dept Quim, Lab Fisicoquim, RA-14008300 Buenos Aires, Neuquen, Argentina
[3] Univ Santiago de Compostela, Fac Fis, Dept Fis Aplicada, E-15706 Santiago De Compostela, Spain
关键词
TEMPERATURE-DEPENDENCE; UNIFAC MODEL; 298.15; K; HEXANE; PREDICTION; METHANOL; HEPTANE; OCTANE; SYSTEM;
D O I
10.1021/je8004613
中图分类号
O414.1 [热力学];
学科分类号
摘要
Excess molar enthalpies, H-E(x, T), at T = 298.15 K, densities, rho(x, T), and speeds of sound, u(x, T), at temperatures T = (288.15 to 308.15) K and atmospheric pressure have been measured for the ternary system methyl tert-butyl ether (MTBE) (1) + butan-1-ol (2) + octane (3). Also, densities, p(x, 7) and speeds of sound, u(x, 7), for the binary mixture MTBE (1) + octane (3) and excess molar enthalpies: H E(X, T), T = 298.15 K, for the binary mixture butan-1-ol (2) + octane (3) have been measured. From experimental data, excess molar volumes, V-E(x, T), and excess isentropic compressibility, kappa(E)(S)(x, T), were calculated. The Cibulka equation was used to correlate the ternary contribution to the experimental excess molar volume and excess isentropic compressibility. Additionally, excess molar enthalpies were correlated with the Nagata and Tamura equation, and the experimental results are compared with the estimations obtained by applying the group-contribution models of UNIFAC and DISQUAC.
引用
收藏
页码:453 / 458
页数:6
相关论文
共 22 条
[1]   EVALUATION OF EXCESS ISENTROPIC COMPRESSIBILITIES AND ISOCHORIC HEAT-CAPACITIES [J].
BENSON, GC ;
KIYOHARA, O .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1979, 11 (11) :1061-1064
[2]  
Bevington P. R., 1969, DATA REDUCTION ERROR
[4]   PREDICTION OF ENTHALPIES OF MIXING WITH A UNIFAC MODEL [J].
DANG, D ;
TASSLOS, DP .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (01) :22-31
[5]   Temperature dependence of thermophysical properties of octane+1-butanol system [J].
de Cominges, BE ;
Piñeiro, MM ;
Mosteiro, L ;
Mascato, E ;
Mato, MM ;
Iglesias, TP ;
Legido, JL .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2002, 70 (01) :217-227
[6]   A MODIFIED UNIFAC MODEL .2. PRESENT PARAMETER MATRIX AND RESULTS FOR DIFFERENT THERMODYNAMIC PROPERTIES [J].
GMEHLING, J ;
LI, JD ;
SCHILLER, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (01) :178-193
[7]  
KEHIAIAN H, 1969, B SOC CHIM FR, P1561
[8]  
KEHIAIAN HV, 1978, J CHIM PHYS PCB, V75, P11
[9]   A MODIFIED UNIFAC GROUP-CONTRIBUTION MODEL FOR PREDICTION OF PHASE-EQUILIBRIA AND HEATS OF MIXING [J].
LARSEN, BL ;
RASMUSSEN, P ;
FREDENSLUND, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (11) :2274-2286
[10]   Temperature dependence of volumetric behaviour for methyl tert-butylether+1-butanol system [J].
Mascato, E ;
Mosteiro, L ;
Piñeiro, MM ;
de Cominges, BE ;
Mato, MM ;
Legido, JL .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2002, 70 (01) :235-241