C. R. Chamorro

发表

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, J. Segovia, M. Villamañán, 2008 .

Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor–Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K

J. Segovia, R. Villamañán, M. Villamañán, 2006 .

Phase Equilibrium Properties of Binary and Ternary Mixtures Containing 1,1-Dimethylethyl Methyl Ether, 1-Propanol, and Hexane at T = 313.15 K

E. Montero, C. Alonso-Tristán, J. Segovia, 2006 .

Phase equilibria properties of binary and ternary systems containing di-isopropyl ether + isobutanol + benzene at 313.15 K

J. Segovia, M. C. Martín, R. Villamañán, 2006 .

Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15 K

J. Segovia, R. Villamañán, M. Villamañán, 2006 .

Vapor−Liquid Equilibrium of Binary and Ternary Mixtures Containing Isopropyl Ether, 2-Butanol, and Benzene at T = 313.15 K

J. Segovia, M. C. Martín, R. Villamañán, 2006 .

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

J. Segovia, M. Villamañán, Marı́a C Martı́n, 2002 .

Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor−Liquid Equilibrium of Ternary Mixtures Containing Di-isopropyl Ether or Cyclohexane and 1-Hexene + Benzene at 313.15 K

J. Segovia, M. Villamañán, A. M. T. Martín, 2002 .

Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor−Liquid Equilibrium of Binary and Ternary Mixtures Containing Di-isopropyl Ether or Heptane and 1-Hexene + Cyclohexane at 313.15 K

J. Segovia, M. Villamañán, A. M. T. Martín, 2001 .

Vapour–liquid equilibrium of octane-enhancing additives in gasolines: 2. Total pressure data and gE for binary and ternary mixtures containing tert-amylmethyl ether (TAME), tert-amyl alcohol (TAOH) and n-hexane

E. Montero, J. Segovia, M. Villamañán, 2001 .

Experimental investigation of the vapor–liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME)+n-heptane+methanol

J. Segovia, M. Villamañán, Marı́a C Martı́n, 1999 .

Excess thermodynamic properties of binary and ternary mixtures containing methyl 1,1-dimethylethyl ether (MTBE),n-heptane, and methanol atT = 313.15 K

J. Segovia, M. Villamañán, Marı́a C Martı́n, 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

E. Montero, J. Segovia, M. Villamañán, 1999 .

Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons

E. Montero, J. Segovia, M. Villamañán, 1998 .

Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and GE for methyl tert-butyl etherbenzenecyclohexane at 313.15 K

J. Segovia, M. Villamañán, Marı́a C Martı́n, 1997 .

Thermodynamic characterization of bio-fuels: excess functions for binary mixtures containing ETBE and hydrocarbons.

J. Segovia, M. C. Martín, R. Villamañán, 2010 .

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

E. Montero, J. Segovia, M. Villamañán, 2004 .

Experimental Determination of (p, ρ, T) Data for Three Mixtures of Carbon Dioxide with Methane for the Thermodynamic Characterization of Nonconventional Energy Gases

Maria E. Mondejar, M. Mondejar, F. Haloua, 2012 .

Measurement of the (pressure, density, temperature) relation of two (methane + nitrogen) gas mixtures at temperatures between 240 and 400 K and pressures up to 20 MPa using an accurate single-sinker densimeter

J. Trusler, J. Segovia, M. C. Martín, 2006 .

Speeds of sound in {(1 − x)CH4 + xN2} with x = (0.10001, 0.19999, and 0.5422) at temperatures between 170 K and 400 K and pressures up to 30 MPa

J. Trusler, J. Segovia, M. C. Martín, 2006 .

Accurate (p, ρ, T) data for two new (carbon dioxide + nitrogen) mixtures from (250 to 400) K at pressures up to 20 MPa

Maria E. Mondejar, M. Mondejar, R. Span, 2012 .

Thermophysical Properties of Hydrogen Mixtures Relevant for the Development of the Hydrogen Economy: Analysis of Available Experimental Data and Thermodynamic Models

Alejandro Moreau, C. R. Chamorro, D. Lozano-Martín, 2022, SSRN Electronic Journal.

Characterization of a biomethane-like synthetic gas mixture through accurate density measurements from (240 to 350) K and pressures up to 14 MPa

D. Campo, R. Hernández-Gómez, M. Valkova, 2017 .

Integration of biogas in the natural gas grid: Thermodynamic characterization of a biogas-like mixture

Maria E. Mondejar, M. Mondejar, R. Hernández-Gómez, 2015 .

Experimental determination of (p, ρ, T) data for binary mixtures of methane and helium

J. Segovia, R. Hernández-Gómez, C. R. Chamorro, 2016 .

Densities, viscosities, and isobaric heat capacities of the system (1-butanol + cyclohexane) at high pressures

J. Segovia, M. C. Martín, C. R. Chamorro, 2014 .

High-pressure isobaric heat capacities using a new flow calorimeter

J. Segovia, M. C. Martín, D. Vega-Maza, 2008 .

Thermodynamic characterization of second generation biofuels: Vapour–liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol and cyclohexane or toluene

J. Segovia, Alejandro Moreau, M. C. Martín, 2012 .

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. Segovia, M. C. Martín, M. Villamañán, 2009 .

Phase equilibrium properties of the ternary mixture dibutyl ether+toluene+heptane at 313.15K

C. Alonso-Tristán, J. Segovia, M. C. Martín, 2012 .

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

J. Segovia, M. C. Martín, R. Villamañán, 2008 .

Characterization and modelling of a gasoline containing 1,1-dimethylethyl methyl ether (MTBE), diisopropyl ether (DIPE) or 1,1-dimethylpropyl methyl ether (TAME) as fuel oxygenate based on new isothermal binary vapour–liquid data

J. Segovia, M. Villamañán, Marı́a C Martı́n, 2004 .

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

J. Segovia, M. Villamañán, Marı́a C Martı́n, 2002 .

Vapor–liquid equilibrium of octane-enhancing additives in gasolines

J. Segovia, M. Villamañán, Marı́a C Martı́n, 2001 .

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

E. Montero, C. Alonso-Tristán, J. Segovia, 2006 .

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

C. Alonso-Tristán, J. Segovia, M. Villamañán, 2006 .

Phase equilibrium properties of binary and ternary systems containing di-isopropyl ether + 1 -butanol + benzene at 313.15 K

J. Segovia, M. C. Martín, R. Villamañán, 2006 .

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

E. Montero, J. Segovia, M. Villamañán, 2004 .

Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques

César R. Chamorro, M. Carmen Martín, José J. Segovia, 2016 .

Speed of sound for three binary (CH4 + H2) mixtures from p = (0.5 up to 20) MPa at T = (273.16 to 375) K

D. Tůma, Daniel Lozano-Martín, J. Segovia, 2020 .

Vapor−Liquid Equilibrium of Ternary Mixtures Containing Methyl tert-Butyl Ether and/or Substitution Hydrocarbons. Methyl tert-Butyl Ether + Heptane + Cyclohexane and Methyl tert-Butyl Ether + Cyclohexane + 1-Hexene at 313.15 K†

J. Segovia, M. Villamañán, Marı́a C Martı́n, 1998 .

Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor−Liquid Equilibrium of the Ternary Mixtures Methyl tert-Butyl Ether + Heptane + Benzene and Methyl tert-Butyl Ether + Benzene + 1-Hexene at 313.15 K†

J. Segovia, M. Villamañán, Marı́a C Martı́n, 1998 .

Enhanced geothermal systems in Europe: An estimation and comparison of the technical and sustainable potentials

César R. Chamorro, Maria E. Mondejar, M. Mondejar, 2014 .

World geothermal power production status: Energy, environmental and economic study of high enthalpy technologies

César R. Chamorro, Roberto Ramos, José J. Segovia, 2012 .

Low-grade coal and biomass co-combustion on fluidized bed: exergy analysis.

J. Segovia, C. Chamorro, A. Cabanillas, 2006 .

Accurate experimental (p, ρ, T) data of the (CO2 + O2) binary system for the development of models for CCS processes

D. Tůma, Daniel Lozano-Martín, C. Chamorro, 2020, The Journal of Chemical Thermodynamics.

Determination of the force transmission error in a single-sinker magnetic suspension densimeter due to the fluid-specific effect and its correction for use with gas mixtures containing oxygen

M. Mondejar, Daniel Lozano-Martín, J. Segovia, 2020, Measurement.

Influence parameters on the performance of an experimental solar-assisted ground-coupled absorption heat pump in cooling operation

Andrés Macía, Luis A. Bujedo, César R. Chamorro, 2013 .

Accurate experimental (p, ρ, T) data of natural gas mixtures for the assessment of reference equations of state when dealing with hydrogen-enriched natural gas

D. Tůma, Daniel Lozano-Martín, C. Chamorro, 2018, International Journal of Hydrogen Energy.

Accurate thermodynamic characterization of a synthetic coal mine methane mixture

M. Mondejar, M. Villamañán, R. Hernández-Gómez, 2014 .

New (p, ρ, T) data for carbon dioxide – Nitrogen mixtures from (250 to 400) K at pressures up to 20 MPa

M. Mondejar, R. Span, M. C. Martín, 2011 .

Thermodynamic characterization of the (CO2 + O2) binary system for the development of models for CCS processes: Accurate experimental (p, ρ, T) data and virial coefficients

M. C. Martín, D. Vega-Maza, C. R. Chamorro, 2021, The Journal of Supercritical Fluids.

Thermodynamic characterization of the (H2 + C3H8) system significant for the hydrogen economy: Experimental (p, ρ, T) determination and equation-of-state modelling

H. Kipphardt, Peyman Khanipour, C. R. Chamorro, 2022, International Journal of Hydrogen Energy.

Accurate Experimental (p, ρ, T) Data for the Introduction of Hydrogen into the Natural Gas Grid: Thermodynamic Characterization of the Nitrogen–Hydrogen Binary System from 240 to 350 K and Pressures up to 20 MPa

R. Hernández-Gómez, A. Gomez-Hernandez, C. R. Chamorro, 2017 .

Accurate experimental (p, ρ, T) values and virial coefficients for the (methane and helium) binary system

R. Villamañán, R. Hernández-Gómez, C. R. Chamorro, 2016 .

Heat capacities and acoustic virial coefficients for a synthetic coal mine methane mixture by speed of sound measurements at T = (273.16 and 250.00) K

F. Pérez-Sanz, J. Segovia, M. C. Martín, 2016 .

Improvement of the measurement uncertainty of a high accuracy single sinker densimeter via setup modifications based on a state point uncertainty analysis

César R. Chamorro, José J. Segovia, Maria E. Mondejar, 2011 .

Updated determination of the molar gas constant R by acoustic measurements in argon at UVa-CEM

J. Segovia, M. C. Martín, M. Villamañán, 2017 .

An estimation of the enhanced geothermal systems potential for the Iberian Peninsula

César R. Chamorro, Maria E. Mondejar, M. Mondejar, 2014 .

A Comparison of Energy Profile between Castilla Leon, Spain and Aceh, Indonesia

J. Segovia, Carmen M. Martin, M. Villamañán, 2010 .

(p, ρ, T) Behavior of Two Mixtures of Carbon Monoxide with Nitrogen in the Temperature Range from (250 to 400) K and Pressures up to 20 MPa

M. Mondejar, R. Span, M. Villamañán, 2011 .

EXCESS PROPERTIES OF THE TERNARY MIXTURE TERT-AMYL METHYL ETHER (TAME) + METHANOL + HEXANE AT 313.15 K

E. Montero, C. Alonso-Tristán, J. Segovia, 2005 .

OF THE VAPOUR-LIQUID EQUILIBRIUM OF BINARY AND TERNARY MIXTURES CONTAINING DIBUTYL ETHER ( DBE ) , CYCLOHEXANE AND TOLUENE AT 313 . 15

E. Montero, C. Alonso-Tristán, J. Segovia, 2005 .

Thermophysical properties of hydrogen mixtures relevant for the development of the hydrogen economy: Review of available experimental data and thermodynamic models

Alejandro Moreau, C. R. Chamorro, D. Lozano-Martín, 2022, Renewable Energy.