CALCULATION OF TERNARY LIQUID-LIQUID EQUILIBRIA

[1] VAPOR PHASE IMPERFECTIONS IN VAPOR-LIQUID EQUILIBRIA - SEMIEMPIRICAL EQUATION [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (03): : 391 - 402

[2] BOBERG TC, 1960, THESIS U MICHIGAN

[3] A NEW METHOD OF CONSTRAINED OPTIMIZATION AND A COMPARISON WITH OTHER METHODS [J]. COMPUTER JOURNAL, 1965, 8 (01) : 42 - 52

[4] Vapor-liquid equilibria of nonideal solutions - Utilization of theoretical methods to extend data [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1942, 34 : 581 - 589

[5] EDWARDS JB, 1962, THESIS GEORGIA I TEC

[6] Hwa S. C. P., 1963, J CHEM ENGNG DATA, V8, P409

[7] JOY DS, 1968, THESIS KANSAS STATE

[8] PREDICTION OF TERNARY LIQUID-LIQUID EQUILIBRIUM FROM BINARY DATA (FOR THE SYSTEM FURFURAL ISO-OCTANE BENZENE) [J]. CHEMICAL ENGINEERING SCIENCE, 1957, 6 (03) : 116 - 122

[9] LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES [J]. AICHE JOURNAL, 1968, 14 (01) : 135 - +

[10] RENON H, 1966, THESIS U CALIFORNIA

[1] VAPOR PHASE IMPERFECTIONS IN VAPOR-LIQUID EQUILIBRIA - SEMIEMPIRICAL EQUATION [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (03): : 391 - 402

[2] BOBERG TC, 1960, THESIS U MICHIGAN

[3] A NEW METHOD OF CONSTRAINED OPTIMIZATION AND A COMPARISON WITH OTHER METHODS [J]. COMPUTER JOURNAL, 1965, 8 (01) : 42 - 52

[4] Vapor-liquid equilibria of nonideal solutions - Utilization of theoretical methods to extend data [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1942, 34 : 581 - 589

[5] EDWARDS JB, 1962, THESIS GEORGIA I TEC

[6] Hwa S. C. P., 1963, J CHEM ENGNG DATA, V8, P409

[7] JOY DS, 1968, THESIS KANSAS STATE

[8] PREDICTION OF TERNARY LIQUID-LIQUID EQUILIBRIUM FROM BINARY DATA (FOR THE SYSTEM FURFURAL ISO-OCTANE BENZENE) [J]. CHEMICAL ENGINEERING SCIENCE, 1957, 6 (03) : 116 - 122

[9] LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES [J]. AICHE JOURNAL, 1968, 14 (01) : 135 - +

[10] RENON H, 1966, THESIS U CALIFORNIA