نویسندگان | محسن محسن نیا,اسلام پیکر |
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نشریه | Journal of Chemical & Engineering Data |
شماره صفحات | 180 |
شماره مجلد | 52 |
ضریب تاثیر (IF) | ثبت نشده |
نوع مقاله | Full Paper |
تاریخ انتشار | 2007-04-28 |
رتبه نشریه | علمی - پژوهشی |
نوع نشریه | الکترونیکی |
کشور محل چاپ | ایران |
نمایه نشریه | JCR |
چکیده مقاله
Tie line data for ternary systems containing phenol (C 6H 6O), water (H 2O), toluene (C 7H 8), and m-xylene (C 8H 10) were investigated. Phase diagrams of ternary systems of {w1 C7H 8 + w2 C 6H 6 O + (1 - w1 - w2) H2 O} and {w1 C 8H 10 + w2 C 6H 6O + (1 - w1 - w2 ) H2O} at 298.15 and 303.15 K were reported. The quaternary system {w1 C 8H 10 + w2 C 7H 8 + w3 C 6H 6 O + (1 - w1 - w2 - w3) H 2 O} was also studied at 303.15 K. The experimental liquid-liquid equilibrium data have been correlated using the UNIQUAC and NRTL activity coefficient models, and the binary interaction parameters of these components have been presented. The correlated tie line results have been compared with the experimental data. The comparisons indicate the superiority of the NRTL activity coefficient model to UNIQUAC for liquid-liquid equilibrium correlation of studied systems. The tie line data of the studied systems also were correlated using the Hand method
tags: Ternary and Quaternary Systems, Liquid + Liquid Equilibria, Water + Toluene + m-Xylene + Phenol systems, UNIQUAC