2010-2016
- Speeds of sound in (0.95 N2 + 0.05 CO and 0.9 N2 + 0.1 CO) gas mixtures at T = (273 and 325) K and pressure up to 10 MPa(F.J. Pérez-Sanz, J.J. Segovia, M.C. Martín, D. del Campo, M.A. Villamañán). The Journal of Chemical Thermodynamics, 2014.
- Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4-trimethylpentane and 1-hexene at 313.15 K (A. Belabbaci, S. Ghellai, R.M. Villamañán, M.C. Martín, L. Negadi, M.A. Villamañán).Fluid Phase Equilibria, 2014
- Vapour–liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K.(S. Ghellai, A. Belabbaci, R.M. Villamañán, M.C. Martín, M.A. Villamañán, L. Negadi), en The Journal of Chemical Thermodynamics, 2013
- World geothermal power production status: Energy, environmental and economic study of high enthalpy technologies. (C.R. Chamorro, M.E. Mondéjar, R. Ramos, J.J. Segovia, M.C. Martín, M.A. Villamañán), en Energy, 2012.
- High pressure densities of carbon dioxide plus dipentaerythritol hexaheptanoate: New experimental setup and volumetric behavior : Journal of Supercritical Fluids, 58, 2, 189- 197, 20 11 Fandino, O, Lugo, L, Segovia, J.J., Lopez, ER, Comunas, MJP, Fernandez, J.
- Improvement of the measurement uncertainty of a high accuracy single sinker densimeter via setup modifications based on a state point uncertainty analysis.Mondéjar, M.E., Segovia, J.J., Chamorro, C.R.Measurement: Journal of the International Measurement Confederation, 44 (9) 1768-1780 2011.
- Thermodynamic characterization of the mixture (1-butanol + iso- octane): Densities, viscosities, and isobaric heat capacities at high pressures. Torín -Ollarves, G.A., Segovia, J.J., Martín, M.C., Villamañán, M.A. The Journal of Chemical Thermodynamics , in press 2011.
- Low tem perature heat source for power generation: Exhaustive analysis of a carbon dioxide transcritical power cycle.Vélez, F., Segovia, J., Chejne, F., Antolín, G., Quijano, A., Carmen Martín, M. Energy , 36 (9): 5497- 5507 2011.
- Thermodynamic properties of biofuels: Heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa and the pure c ompounds using a new flow calorimeter. The Journal of Chemical Thermodynamics, in press 2011 Vega-Maza, D., Segovia, J.J., Carmen Martín, M., Villamañán, R.M., Villamañán, M.A.
- World geothermal power production status: Energy, environmental and economic study of high enthalpy technologies. Chamorro, C.R., Mondéjar , M.E., Ramos, R., Segovia, J.J., Martín, M.C., Villamañán, M.A. Energy, in press 2011 .
- Thermodynamic characterization of bio-fuels: Excess functions for binary mixtures containing ETBE and hydrocarbons’ (J.J. Segovia, R.M. Villamañán, M.C. Martín, C.R. Chamorro, M.Á. Villamañán), en Energy, 2010.
- Thermodynamic Properties of Binary and Ternary Mixtures Containing Di-isopropyl Ether, 2-Propanol, and Benzene at T = 313.15 K’ (R.M. Villamañán, M.C. Martín, M.Á. Villamañán, C.R. Chamorro, J.J. Segovia), en Journal of Chemical and Engineering Data, 2010
- An Apparatus Based on a Spherical Resonator for Measuring the Speed of Sound in Gases and for Determining the Boltzmann Constant. Segovia, J.J., Vega- Maza, D., Martin, M. C., Gomez, E., Tabacaru, C., del Campo, D.International Journal of Thermophysics , 31 (7): 1294- 1309 2010.
1998-2009
- Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter’ (J.J. Segovia, M.C. Martín, D. Vega-Maza, C.R. Chamorro, M.Á. Villamañán), en The Journal of Chemical Thermodynamics, 2009.
- Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K’ (R.M. Villamañán, J.J. Segovia, M.C. Martín, D. Vega-Maza, C.R. Chamorro, M.Á. Villamañán), en The Journal of Chemical Thermodynamics, 2009.
- Volumetric behaviour of (carbon dioxide + hydrocarbon) mixtures at high pressures.
- 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.
- Automated Densimetric System: Measurements and Uncertainties for Compressed Fluids. José J. Segovia, Olivia Fandiño, Enriqueta R. López,. Luis Lugo, Carmen Martín, Josefa Fernández. The Journal of Chemical Thermodynamics , 41 (5):632- 638 2009.
- Excess ent halpies of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and 1-butanol at 298.15 K. F. Aguilar, F.M. Alaoui, C. Alonso- Tristán, J.J. Segovia, M.A. Villamañán, E.A. Montero. Journal of Chemical and Engineering Data. 54 (6):1672-1679 2009.
- Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter.José J. Segovia, M. Carmen Martín, David Vega Maza, César R. Chamorro. The Journal of Chemical Thermodynamics, 41 (6):759-763 2009.
- Thermodynamics of fuels with a bio- synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K. Rosa M. Villamañán, José J. Segovia, M. Carmen Martín, David Vega- Maza, César R.Chamorro, Miguel A. Villamañán The Journal of Chemical Thermodynamics , 41, 2, 189- 192, 2009.
- High -pressure isobaric heat capacities using a new flow calorimeter. José J. Segovia, David Vega-Maza, César R. Chamorro and M. Carmen Martín. Journal of Supercritical Fluids, 46, 3, 258- 264, 2008.
- Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether,Cyclohexane, and Heptane or 1-Hexene at T = 313.15 K. C. Alonso-Tristán , M.A. Villamañán, C.R. Chamorro, J.J. Segovia.Journal of Chemical and Engineering Data, 53, (1486-1491), 2008.
- Thermodynamics of fuels with a biosynthetic component (III): Vapor–liquid equilibrium data for theternary mixture ethyl 1,1-dimethylethyl ether, n-heptane and 1-hexene at T = 313.15 K. R.M. Villamañán, David Vega- Maza, C.R. Chamorro, M.A. Villamañán, J.J. SegoviaFluid. Phase Equilibria 265 (1-2) (12- 16), 2008.
- 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.Cristina Alonso, César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán . Fluid Phase Equilibria.
- 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.César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán. The Journal of Chemical Thermodynamics, Volume 34, Issue 1, January 2002, Pages 13-28 .
- 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. César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán. Fluid Phase Equilibria.
- 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.César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán . Fluid Phase Equilibria Volume 191, Issues 1-2, 15 November 2001.
- 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. César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán. Fluid Phase Equilibria, Volume 182, Issues 1-2, 5 June 2001, Pages 229-239.
- 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. Cristina Alonso, Eduardo A. Montero, César R. Chamorro, José J. Segovia, María C. Martín and Miguel A. Villamañán. Fluid Phase Equilibria, Volume 182, Issues 1-2, 5 June 2001, Pages 241-25.
- Experimental investigation of the vapor–liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME)+n-heptane+methanol1.César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañá. Fluid Phase Equilibria, Volume 165, Issue 2, 25 November 1999.
- Excess thermodynamic properties of binary and ternary mixtures containing methyl 1,1-dimethylethyl ether (MTBE),n-heptane, and methanol atT = 313.15 K. César R. Chamorro, José J. Segovia, María C. Martín y Miguel A. Villamañán. The Journal of Chemical Thermodynamics, Volume 31, Issue 9, September 1999.
- Phase equilibrium properties of binary and ternary systems containing tert-amylmethyl ether (TAME) as oxygenate additive and gasoline substitution hydrocarbons at 313.15 K.César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán. , Fluid Phase Equilibria, Volume 156, Issues 1-2, 15 March 1999, Pages 73-87.
- 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. José J. Segovia, María C. Martín, César R. Chamorro, y Miguel A. Villamañán. Fluid Phase Equilibria, Volume 133, Issues 1-2, June 1997, Pages 163-172
- 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. César R. Chamorro, José J. Segovia, María C. Martín, Eduardo A. Montero y Miguel A. Villamañán. Fluid Phase Equilibria, Volume 152, Issue 2, 30 October 1998, Pages 265-276.
