Application of the van der Waals equation of state to polymers .4. Correlation and prediction of lower critical solution temperatures for polymer solutions

被引:24
作者
Saraiva, A
Kontogeorgis, GM
Harismiadis, VI
Fredenslund, A
Tassios, DP
机构
[1] NATL TECH UNIV ATHENS,DEPT CHEM ENGN,GR-15773 ZOGRAFOS,GREECE
[2] KONINKLIJKE SHELL EXPTL PROD LAB,DEPT 2,1031 CM AMSTERDAM,NETHERLANDS
[3] TECH UNIV DENMARK,INST KEMITEKN,DEPT CHEM ENGN,IVC SEP,ENGN RES CTR,DK-2800 LYNGBY,DENMARK
关键词
theory; application; method of calculation; equation of state; cubic; liquid-liquid equilibria; lower critical solution temperature; polymer solutions;
D O I
10.1016/0378-3812(95)02834-X
中图分类号
O414.1 [热力学];
学科分类号
摘要
The van der Waals equation of state is used for the correlation and the prediction of the lower critical solution behavior or mixtures including a solvent and a polymer. The equation of state parameters for the polymer are estimated from experimental volumetric data at low pressures. The equation of state parameters for the solvent are estimated via the classical Soave method, i.e. using the critical properties and a generalized equation for the energy parameter. When extended to mixtures, the van der Waals one-fluid mixing rules along with the Berthelot combining rule for the molecular cross energy parameter are used. The arithmetic mean combining rule is used for the cross co-volume parameter. The deviations from the Berthelot combining rule are taken into account via a simple expression which has been previously obtained from vapor-liquid equilibrium data of athermal polymer solutions and has been successfully used for the prediction of upper critical solution temperatures for various binary polymer solutions. In this work, we demonstrate and explain some of the problems which cubic equations of state exhibit in describing the lower critical solution behavior for polymer solutions. These problems are overcome by using a temperature-dependent interaction parameter, even for small temperature ranges, leading to excellent results. Despite the problems, we have developed an empirical methodology in using the van der Waals equation of state with a single interaction parameter for predicting the lower critical solution behavior of polymer/solvent solutions. The results are satisfactory. typically, the difference between the predicted and the experimental lower critical solution temperatures is between 10 and 35 degrees C.
引用
收藏
页码:73 / 93
页数:21
相关论文
共 23 条
[1]   CLOUD-POINT CURVES OF POLYMER-SOLUTIONS FROM THERMOOPTIC MEASUREMENTS [J].
BAE, YC ;
LAMBERT, SM ;
SOANE, DS ;
PRAUSNITZ, JM .
MACROMOLECULES, 1991, 24 (15) :4403-4407
[2]   LOWER CRITICAL SOLUTION TEMPERATURES OF POLYISOBUTYLENE PLUS ISOMERIC ALKANES [J].
BARDIN, JM ;
PATTERSO.D .
POLYMER, 1969, 10 (04) :247-&
[3]   GROUP CONTRIBUTION METHOD FOR THE PREDICTION OF LIQUID DENSITIES AS A FUNCTION OF TEMPERATURE FOR SOLVENTS, OLIGOMERS, AND POLYMERS [J].
ELBRO, HS ;
FREDENSLUND, A ;
RASMUSSEN, P .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (12) :2576-2582
[4]   LOWER CRITICAL POINTS IN POLYMER SOLUTIONS [J].
FREEMAN, PI ;
ROWLINSON, JS .
POLYMER, 1960, 1 (01) :20-26
[5]   APPLICATION OF THE VAN-DER-WAALS-EQUATION OF STATE TO POLYMERS .3. CORRELATION AND PREDICTION OF UPPER CRITICAL SOLUTION TEMPERATURES FOR POLYMER-SOLUTIONS [J].
HARISMIADIS, VI ;
KONTOGEORGIS, GM ;
SARAIVA, A ;
FREDENSLUND, A ;
TASSIOS, DP .
FLUID PHASE EQUILIBRIA, 1994, 100 :63-102
[6]   APPLICATION OF THE VAN-DER-WAALS-EQUATION OF STATE TO POLYMERS .2. PREDICTION [J].
HARISMIADIS, VI ;
KONTOGEORGIS, GM ;
FREDENSLUND, A ;
TASSIOS, DP .
FLUID PHASE EQUILIBRIA, 1994, 96 :93-117
[7]  
HIGH MS, 1992, POLYM SOLUTION HDB
[8]  
KONIGSVELD R, 1970, J POLYM SCI A, V2, P261
[9]   APPLICATION OF THE VAN-DER-WAALS-EQUATION OF STATE TO POLYMERS .1. CORRELATION [J].
KONTOGEORGIS, GM ;
HARISMIADIS, VI ;
FREDENSLUND, A ;
TASSIOS, DP .
FLUID PHASE EQUILIBRIA, 1994, 96 :65-92
[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