Experimental measurements and thermodynamic modeling of paraffinic wax formation in undercooled solutions

被引:61
作者
Coutinho, JAP [1 ]
RuffierMeray, V [1 ]
机构
[1] INST FRANCAIS PETR,F-92852 RUEIL MALMAISON,FRANCE
关键词
D O I
10.1021/ie960817u
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The crystallization of paraffinic materials from hydrocarbon mixtures subject to a cold environment is one of the problems faced by the petroleum industry. It can be found during oil production and in the transport and even in the use of refined materials such as diesels and fuels. A better understanding of the crystallization process and the capacity to model the wax formation would help to overcome this problem. This work is focused on the study of the two-phase region by developing a new experimental technique for measuring the composition of the phases in equilibrium and the amount of paraffins precipitating from a hydrocarbon mixture. The crystallization of several model systems, constituted by a mixture of normal alkanes between n-C19H40 and n-C28H58 dissolved in ethylbenzene in mass concentrations up to 25% weight, was promoted in an optical cell. The composition of the phases in equilibrium at several different temperatures below the cloud point was determined by chromatography. The amount of waxes formed and the cloud points were obtained by differential scanning calorimetry (DSC). The new technique is shown to be simple and accurate. Some particularities of paraffin crystallization were studied as well as the influence of aromatic compounds on the wax formation. A thermodynamic model was used to describe the measured data. It is based on the Flory-free-volume model for the liquid phase and on the predictive local composition model, a predictive form of the Wilson equation, for the nonideality of the solid solution. The model is shown to provide a good description of the SLE data for the studied systems.
引用
收藏
页码:4977 / 4983
页数:7
相关论文
共 15 条
[1]   Predictive local composition models for solid/liquid equilibrium in n-alkane systems: Wilson equation for multicomponent systems [J].
Coutinho, JAP ;
Stenby, EH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (03) :918-925
[2]   EVALUATION OF ACTIVITY-COEFFICIENT MODELS IN PREDICTION OF ALKANE SOLID-LIQUID EQUILIBRIA [J].
COUTINHO, JAP ;
ANDERSEN, SI ;
STENBY, EH .
FLUID PHASE EQUILIBRIA, 1995, 103 (01) :23-39
[3]   A local composition model for paraffinic solid solutions [J].
Coutinho, JAP ;
Knudsen, K ;
Andersen, SI ;
Stenby, EH .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (12) :3273-3282
[4]  
DARRIDON JL, 1996, FLUID PHASE EQUILIBR, V117, P241
[5]   X-RAY-DIFFRACTION AND CALORIMETRIC PHASE STUDY OF A BINARY PARAFFIN - C23H48-C24H50 [J].
DENICOLO, I ;
CRAIEVICH, AF ;
DOUCET, J .
JOURNAL OF CHEMICAL PHYSICS, 1984, 80 (12) :6200-6203
[6]  
Fredenslund A., 1977, Vapor -liquid equilibra using UNIFAC
[7]  
Gerson A.R., 1991, AICHE S SER, V284, P138
[8]   SOLUBILITY OF NORMAL PARAFFIN HYDROCARBONS (C20 TO C24) AND SOME OF THEIR BINARY-MIXTURES (C22+C24) AND (C23+C24) IN ETHYLBENZENE [J].
GHOGOMU, PM ;
DELLACHERIE, J ;
BALESDENT, D .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1989, 21 (09) :925-934
[9]   VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION .5. REVISION AND EXTENSION [J].
HANSEN, HK ;
RASMUSSEN, P ;
FREDENSLUND, A ;
SCHILLER, M ;
GMEHLING, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (10) :2352-2355
[10]   SIMPLE ACTIVITY-COEFFICIENT MODEL FOR THE PREDICTION OF SOLVENT ACTIVITIES IN POLYMER-SOLUTIONS [J].
KONTOGEORGIS, GM ;
FREDENSLUND, A ;
TASSIOS, DP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (02) :362-372