![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
![]() |
|||
![]() |
![]() |
![]() |
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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 |
||
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/p> |
||