Authors: Chamorro, CR Segovia, JJ Martin, MC Villamanan, MA

Citation: Cr. Chamorro et al., Vapor-liquid equilibrium of octane-enhancing additives in gasolines 1. Total pressure data and g(E) for binary and ternary mixtures containing di-isopropyl ether (DIPE), n-heptane and benzene at 313.15 K, FLU PH EQUI, 182(1-2), 2001, pp. 229-239

Authors: Alonso, C Montero, EA Chamorro, CR Segovia, JJ Martin, MC Villamanan, MA

Citation: C. Alonso et al., Vapour-liquid equilibrium of octane-enhancing additives in gasolines 2. Total pressure data and g(E) for binary and ternary mixtures containing tert-amylmethyl ether (TAME), tert-amyl alcohol (TAOH) and n-hexane, FLU PH EQUI, 182(1-2), 2001, pp. 241-255

Authors: Chamorro, CR Segovia, JJ Martin, MC Villamanan, MA

Citation: Cr. Chamorro et al., Thermodynamics of octane-enhancing additives in gasolines: Vapor-liquid equilibrium of binary and ternary mixtures containing di-isopropyl ether or heptane and 1-hexene plus cyclohexane at 313.15 K, J CHEM EN D, 46(6), 2001, pp. 1574-1579

Authors: Chamorro, CR Segovia, JJ Martin, MC Villamanan, MA

Citation: Cr. Chamorro et al., Experimental investigation of the vapor-liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME) plus n-heptane plus methanol, FLU PH EQUI, 165(2), 1999, pp. 197-208

Authors: Chamorro, CR Segovia, JJ Martin, MC Montero, EA Villamanan, MA

Citation: Cr. Chamorro et al., Phase equilibrium properties of binary and ternary systems containing tert-amylmethyl ether (TAME) as oxygenate additive and gasoline substitution hydrocarbons at 313.15 K, FLU PH EQUI, 156(1-2), 1999, pp. 73-87

Authors: Segovia, JJ Martin, MC Chamorro, CR Villamanan, MA

Citation: Jj. Segovia et al., Excess thermodynamic properties of binary and ternary mixtures containing methyl 1,1-dimethylethyl ether (MTBE), n-heptane, and methanol at T=313.15 K, J CHEM THER, 31(9), 1999, pp. 1231-1246