Estos son algunos de los últimos artículos publicados en revistas internacionales por miembros de este laboratorio:

 

27- 
Vapour-liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15 K, Fluid Phase Equilibria
 

Cristina Alonso, José J. Segovia, César R. Chamorro, Eduardo A. Montero y Miguel A. Villamañán


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26- 
Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K, Fluid Phase Equilibria
 

Cristina Alonso, José J. Segovia, César R. Chamorro, y Miguel A. Villamañán


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13- 
Excess enthalpies of binary and ternary mixtures containing tert-amyl methyl ether (TAME), tert-amyl alcohol (TAOH) and hexane at 298.15 and 313.15 K, Fluid Phase Equilibria
 

Cristina Alonso, César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán


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12- 
Vapor–liquid equilibrium of octane-enhancing additives in gasolines: 6. Total pressure data and GE for binary and ternary mixtures containing 1,1-dimethylethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K, Fluid Phase Equilibria
 

Cristina Alonso, César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán


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11 
Vapor–liquid equilibrium of octane-enhancing additives in gasolines*1: 5. Total pressure data and GE for binary and ternary mixtures containing 1,1-dimethylpropyl methyl ether (TAME), 1-propanol and n-hexane at 313.15 K,, Fluid Phase Equilibria
 

Cristina Alonso, César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán


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10- 
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-heptane + 1-hexene at 313.15 K, Fluid Phase Equilibria
 

César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán


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9- 
Isothermal v.l.e. and excess molar Gibbs energy of binary and ternary mixtures containing diisopropyl ether,n -heptane and isopropanol at T = 313.15 K, The Journal of Chemical Thermodynamics, Volume 34, Issue 1, January 2002, Pages 13-28
 

César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán


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8- 
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-heptane + cyclohexane at 313.15 K,Fluid Phase Equilibria Volume 191, Issues 1-2, 15 November 2001, Pages 71-82
 

César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán

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7- 
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), n-heptane and benzene at 313.15 K, Fluid Phase Equilibria, Volume 182, Issues 1-2, 5 June 2001, Pages 229-239
 

César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán

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6- 
Vapour–liquid equilibrium of octane-enhancing additives in gasolines*1: 2. Total pressure data and gE for binary and ternary mixtures containing tert-amylmethyl ether (TAME), tert-amyl alcohol (TAOH) and n-hexane,Fluid Phase Equilibria, Volume 182, Issues 1-2, 5 June 2001, Pages 241-255
 

Cristina Alonso, Eduardo A. Montero, César R. Chamorro, José J. Segovia, María C. Martín and Miguel A. Villamañán

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5- 
Experimental investigation of the vapor–liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME)+n-heptane+methanol1, Fluid Phase Equilibria, Volume 165, Issue 2, 25 November 1999, Pages 197-208
 

César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán

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4- 
Excess thermodynamic properties of binary and ternary mixtures containing methyl 1,1-dimethylethyl ether (MTBE),n-heptane, and methanol atT = 313.15 K, The Journal of Chemical Thermodynamics, Volume 31, Issue 9, September 1999, Pages 1231-1246
 

César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán

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3- 
Phase equilibrium properties of binary and ternary systems containing tert-amylmethyl ether (TAME) as oxygenate additive and gasoline substitution hydrocarbons at 313.15 K, Fluid Phase Equilibria, Volume 156, Issues 1-2, 15 March 1999, Pages 73-87
 

César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán

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2- 
Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons: 2. Total-pressure data and GE for methyl tert-butyl ether/n-heptane/1-hexene at 313.15 K, Fluid Phase Equilibria, Volume 152, Issue 2, 30 October 1998, Pages 265-276
 

César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán

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1- 
Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and GE for methyl tert-butyl ether---benzene---cyclohexane at 313.15 K, Fluid Phase Equilibria, Volume 133, Issues 1-2, June 1997, Pages 163-172
 

José J. Segovia, María C. Martín, César R. Chamorro, y Miguel A. Villamañán

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