Prediction of the McAllister model parameters by using the group-contribution method:: n-alkane liquid systems

被引:8
|
作者
Nhaesi, AH [1 ]
Al-Gherwi, W [1 ]
Asfour, AFA [1 ]
机构
[1] Univ Windsor, Windsor, ON N9B 3P4, Canada
关键词
D O I
10.1021/ie050461z
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The McAllister model is considered to be the best correlating technique for viscosity-composition data. In a series of publications, Asfour et al. and Nhaesi and Asfour successfully converted the McAllister model into a predictive model which requires only the viscosities of the pure components and the molecular parameters of the constituents of a liquid mixture. They validated the model for the cases of n-alkane and regular liquid systems by using data on a large number of liquid mixtures at different temperatures. In this paper, we propose a novel technique for predicting the McAllister model parameters, for n-alkane systems, by the group-contribution method. The predictive capability of the McAllister model in this case is shown, for n-alkane binary and multicomponent systems, to be better or at least as good as the techniques reported earlier. The main advantage of the technique we are proposing here is that we expect it to be able to successfully and reliably predict more classes of liquid solutions than earlier methods.
引用
收藏
页码:9962 / 9968
页数:7
相关论文
共 50 条
  • [21] SOLID-LIQUID EQUILIBRIA USING DISQUAC - PREDICTION FOR 1-ALKANOL PLUS N-ALKANE SYSTEMS
    GONZALEZ, JA
    DELAFUENTE, IG
    COBOS, JC
    CASANOVA, C
    DOMANSKA, U
    FLUID PHASE EQUILIBRIA, 1994, 94 : 167 - 179
  • [22] EVALUATION OF THE CARBOXYLATE CHLORINE INTERACTION PARAMETERS USING THE DISQUAC GROUP-CONTRIBUTION MODEL
    FARKOVA, J
    WICHTERLE, I
    KEHIAIAN, HV
    FLUID PHASE EQUILIBRIA, 1995, 112 (01) : 23 - 32
  • [23] Prediction of the settling of every n-alkane in diesel by the thermodynamic model
    Lu, Ya
    Chen, Shufen
    ENERGY & FUELS, 2008, 22 (03) : 1807 - 1811
  • [24] PHASE-EQUILIBRIA IN MODEL SYSTEMS CONTAINING PHENOL .2. PREDICTION USING GROUP-CONTRIBUTION METHODS
    SCHMELZER, J
    OBST, SO
    SUHNEL, K
    QUITZSCH, K
    CHEMISCHE TECHNIK, 1991, 43 (07): : 261 - 265
  • [25] PREDICTION OF GAS SOLUBILITIES IN PURE AND MIXED-SOLVENTS USING A GROUP-CONTRIBUTION METHOD
    CATTE, M
    ACHARD, C
    DUSSAP, CG
    GROS, JB
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (09) : 2193 - 2198
  • [26] PREDICTION OF THERMODYNAMIC PROPERTIES OF POLYMER-SOLUTIONS USING THE UNIFAC GROUP-CONTRIBUTION METHOD
    PRICE, GJ
    ASHWORTH, AJ
    POLYMER, 1987, 28 (12) : 2105 - 2109
  • [27] PREDICTION OF VAPOR-LIQUID-EQUILIBRIUM OF SATURATED HIGH FATTY-ACID USING ASOG GROUP-CONTRIBUTION METHOD
    RALEV, N
    DOBRUDJALIEV, D
    FLUID PHASE EQUILIBRIA, 1991, 65 : 159 - 165
  • [28] Phase equilibria in model systems containing phenol part II. Prediction using group-contribution methods
    Schmelzer
    Obst
    Suebnel
    Quitzsch
    Chemische Technik (Leipzig), 1991, 43 (07):
  • [29] PREDICTION OF PHASE-EQUILIBRIA USING UNIFAC GROUP-CONTRIBUTION
    RASMUSSEN, P
    SKJOLDJORGENSEN, S
    FREDENSLUND, A
    POLISH JOURNAL OF CHEMISTRY, 1980, 54 (10) : 2025 - 2033
  • [30] GROUP-CONTRIBUTION VISCOSITY PREDICTIONS OF LIQUID-MIXTURES USING UNIFAC-VLE PARAMETERS
    CAO, WH
    KNUDSEN, K
    FREDENSLUND, A
    RASMUSSEN, P
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (09) : 2088 - 2092