Measurement and prediction of pyrene solubility in pure, binary, ternary and quaternary solvent systems

被引:7
作者
Ali, Sami H. [1 ]
机构
[1] Kuwait Univ, Dept Chem Engn, Safat 13060, Kuwait
关键词
solid-liquid equilibria; modeling; pyrene; solvents;
D O I
10.1016/j.fluid.2007.11.001
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this Study, the solubility of a common polyaromatic hydrocarbon, pyrene, was investigated in various solvent systems containing p-xylene, octane, iso-octane and/or octanol over a temperature range from 293 to 318 K. The collected experimental data for the solubility of pyrene in pure solvents follow the Van't Hoff relationship with high accuracy. The experimental solubility data for six binary solvent systems were used to predict the interaction parameters for different models; Wilson, modified Wilson, nearly ideal binary solvent (NIBS)/Redlich-Kister and UNIQUAC. The interaction parameters for these models were expressed as a second order polynomial function in temperature. These obtained interaction parameters for the different used activity coefficient models were tested on more complex systems for the solubility of pyrene in ternary and quaternary solvent mixtures composed of different ratios of p-xylene, octane, iso-octane and/or octanol at different temperatures (ranging from 293 to 318 K). Using extended forms of the NIBS/Redlich-Kister model resulted in improvements in the prediction of pyrene solubility. Functional group contribution models (UNIFAC, UNIFAC-SG, SUPERFAC, SUPERFAC-SG, Dortmund UNIFAC and Dortmund UNIFAC-SG) were tested against all the pure, binary, ternary and quaternary solvent systems. Detailed comparison between all of these models is presented. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:29 / 44
页数:16
相关论文
共 31 条
[2]   Solubility of anthracene in two binary solvents containing toluene [J].
Al-Sharrah, GK ;
Ali, SH ;
Fahim, MA .
FLUID PHASE EQUILIBRIA, 2002, 193 (1-2) :191-201
[3]   Solubility of polycyclic aromatics in binary solvent mixtures using activity coefficient models [J].
Ali, SH ;
Al-Mutairi, FS ;
Fahim, MA .
FLUID PHASE EQUILIBRIA, 2005, 230 (1-2) :176-183
[4]   Thermodynamics of mobile order theory: comparison of experimental and predicted anthracene and pyrene solubilities in binary alkane plus alcohol solvent mixtures [J].
Borders, TL ;
McHale, MER ;
Powell, JR ;
Coym, KS ;
Hernandez, CE ;
Roy, LE ;
Acree, WE ;
Williams, DC ;
Campbell, SW .
FLUID PHASE EQUILIBRIA, 1998, 146 (1-2) :207-221
[5]   SOLUBILITIES OF POLYNUCLEAR AROMATIC-HYDROCARBONS IN MIXTURES OF COMMON ORGANIC-SOLVENTS [J].
COON, JE ;
TROTH, M ;
MCLAUGHLIN, E .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1987, 32 (02) :233-240
[6]   COMPUTERIZED DESIGN OF MULTICOMPONENT DISTILLATION-COLUMNS USING UNIFAC GROUP CONTRIBUTION METHOD FOR CALCULATION OF ACTIVITY-COEFFICIENTS [J].
FREDENSLUND, A ;
GMEHLING, J ;
MICHELSEN, ML ;
RASMUSSEN, P ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (04) :450-462
[7]   A modified UNIFAC (Dortmund) model. 4. Revision and extension [J].
Gmehling, J ;
Wittig, R ;
Lohmann, J ;
Joh, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1678-1688
[8]   VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION - REVISION AND EXTENSION .2. [J].
GMEHLING, J ;
RASMUSSEN, P ;
FREDENSLUND, A .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1982, 21 (01) :118-127
[9]   A modified UNIFAC (Dortmund) model. 3. Revision and extension [J].
Gmehling, J ;
Lohmann, J ;
Jakob, A ;
Li, JD ;
Joh, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (12) :4876-4882
[10]   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