Ternary and Quaternary Liquid + Liquid Equilibria for Systems of (Water + Toluene + m-Xylene + Phenol)

نویسندگانمحسن محسن نیا,اسلام پیکر
نشریهJournal of Chemical & Engineering Data
شماره صفحات180
شماره مجلد52
ضریب تاثیر (IF)ثبت نشده
نوع مقالهFull Paper
تاریخ انتشار2007-04-28
رتبه نشریهعلمی - پژوهشی
نوع نشریهالکترونیکی
کشور محل چاپایران
نمایه نشریهJCR

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