Vapour–liquid equilibrium of octane-enhancing additives in gasolines: 2. Total pressure data and gE for binary and ternary mixtures containing tert-amylmethyl ether …
Vapour–liquid equilibria of the ternary system (tert-amylmethyl ether (TAME)+ tert-amyl
alcohol (TAOH)+ n-hexane) and for their constituent binary systems have been measured at …
alcohol (TAOH)+ n-hexane) and for their constituent binary systems have been measured at …
Vapor–liquid equilibrium of octane-enhancing additives in gasolines: 5. Total pressure data and GE for binary and ternary mixtures containing 1, 1-dimethylpropyl …
Experimental isothermal P–x data at T= 313.15 K for the binary systems 1, 1-dimethylpropyl
methyl ether (TAME)+ 1-propanol, 1-propanol+ n-hexane and the ternary system TAME+ 1 …
methyl ether (TAME)+ 1-propanol, 1-propanol+ n-hexane and the ternary system TAME+ 1 …
Vapor–liquid equilibrium of octane-enhancing additives in gasolines: 6. Total pressure data and GE for binary and ternary mixtures containing 1, 1-dimethylethyl …
Experimental isothermal P–x data at T= 313.15 K for the binary systems 1, 1-dimethylethyl
methyl ether (MTBE)+ n-hexane and methanol+ n-hexane, and the ternary system MTBE+ …
methyl ether (MTBE)+ n-hexane and methanol+ n-hexane, and the ternary system MTBE+ …
Vapor–liquid equilibrium of octane-enhancing additives in gasolines: 1. Total pressure data and gE for binary and ternary mixtures containing di-isopropyl ether (DIPE …
Experimental isothermal P–x data at T= 313.15 K for the ternary system (di-isopropyl ether
(DIPE)+ n-heptane+ benzene) and for one of the previously unmeasured constituent binary …
(DIPE)+ n-heptane+ benzene) and for one of the previously unmeasured constituent binary …
Vapor–liquid equilibrium of octane-enhancing additives in gasolines: 4. Total pressure data and GE for ternary mixtures containing isopropyl ether or benzene and n …
The experimental isothermal P–x data at T= 313.15 K for the two ternary systems (isopropyl
ether+ n-heptane+ 1-hexene) and (1-hexene+ n-heptane+ benzene) are reported. Data …
ether+ n-heptane+ 1-hexene) and (1-hexene+ n-heptane+ benzene) are reported. Data …
Vapor–liquid equilibrium of octane-enhancing additives in gasolines: 3. Total pressure data and gE for ternary mixtures containing di-isopropyl ether or benzene and n …
New experimental isothermal P–x data at T= 313.15 K for two ternary systems (di-isopropyl
ether,(DIPE)+ n-heptane+ cyclohexane) and (benzene+ n-heptane+ cyclohexane) are …
ether,(DIPE)+ n-heptane+ cyclohexane) and (benzene+ n-heptane+ cyclohexane) are …
Thermodynamics of octane-enhancing additives in gasolines: vapor− liquid equilibrium of binary and ternary mixtures containing di-isopropyl ether or heptane and 1 …
Experimental isothermal P− x− y data for the ternary systems di-isopropyl ether (DIPE)+ 1-
hexene+ cyclohexane and 1-hexene+ heptane+ cyclohexane and for the binary system …
hexene+ cyclohexane and 1-hexene+ heptane+ cyclohexane and for the binary system …
Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor− Liquid Equilibrium of the Ternary Mixtures Methyl tert-Butyl Ether+ Heptane+ Benzene and …
Experimental isothermal P− x− y data for the ternary systems methyl tert-butyl ether (MTBE)+
heptane+ benzene and methyl tert-butyl ether (MTBE)+ benzene+ 1-hexene and for the …
heptane+ benzene and methyl tert-butyl ether (MTBE)+ benzene+ 1-hexene and for the …
Vapor-liquid equilibrium for the systems ethyl formate-methyl ethyl ketone, ethyl formate-toluene and ethyl formate-methyl ethyl ketone-toluene: new unifac parameters …
EA Macedo, JM Mendonca, AG Medina - Fluid phase equilibria, 1984 - Elsevier
Vapor-liquid equilibrium data are presented for the binary systems ethyl formate-methyl ethyl
ketone (MEK) at 40° C and 50° C and ethyl formate-toluene at 48° Cand 51° C and for the …
ketone (MEK) at 40° C and 50° C and ethyl formate-toluene at 48° Cand 51° C and for the …
Thermodynamics of octane-enhancing additives in gasolines: vapor− liquid equilibrium of ternary mixtures containing di-isopropyl ether or cyclohexane and 1 …
Experimental isothermal P− x− y data for the ternary systems di-isopropyl ether (DIPE)+ 1-
hexene+ benzene and 1-hexene+ benzene+ cyclohexane at 313.15 K are reported. Data …
hexene+ benzene and 1-hexene+ benzene+ cyclohexane at 313.15 K are reported. Data …