J. Segovia

发表

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.

Volumetric behaviour of (carbon dioxide + hydrocarbon) mixtures at high pressures

Daniel Lozano-Martín, J. Segovia, J. Zambrano, 2016 .

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

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

Low temperature heat source for power generation: Exhaustive analysis of a carbon dioxide transcritical power cycle

G. Antolín, F. Chejne, J. Segovia, 2011 .

Measurement and prediction of high-pressure viscosities of biodiesel fuels

J. Coutinho, J. Segovia, J. Zambrano, 2014 .

Comparative study of working fluids for a Rankine cycle operating at low temperature

Farid Chejne, Ana Quijano, Fredy Vélez, 2012 .

Density and viscosity measurements of (piperazine + water) and (piperazine + 2-dimethylaminoethanol + water) at high pressures

J. Segovia, Alejandro Moreau, M. C. Martín, 2020 .

An experimental setup for isobaric heat capacities for viscous fluids at high pressure: Squalane, bis(2-ethylhexyl) sebacate and bis(2-ethylhexyl) phthalate

J. Segovia, M. C. Martín, Josefa Fernández, 2012 .

Thermodynamic characterization of deep eutectic solvents at high pressures

M. Carmen Martín, José J. Segovia, Pedro J. Carvalho, 2019, Fluid Phase Equilibria.

Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels

J. Segovia, Alejandro Moreau, J. Zambrano, 2018, The Journal of Chemical Thermodynamics.

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 .

Uncertainty calculation of the effective emissivity of cylinder-conical blackbody cavities

José J. Segovia, J. Lucas, J. Segovia, 2016 .

Measurement and Analysis of the Temperature Gradient of Blackbody Cavities, for Use in Radiation Thermometry

J. Lucas, J. Segovia, 2018 .

Density and viscosity measurements of aqueous amines at high pressures: DEA-water, DMAE-water and TEA-water mixtures

J. Segovia, M. C. Martín, E. Concepción, 2017 .

Measurements and predictions of densities and viscosities in CO2 + hydrocarbon mixtures at high pressures and temperatures: CO2 + n-pentane and CO2 + n-hexane blends

I. Polishuk, D. Tůma, J. Segovia, 2022, Journal of Molecular Liquids.

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 .

Solubility of CO 2 in three cellulose‐dissolving ionic liquids

S. Pereda, J. Segovia, Alejandro Moreau, 2020 .

A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination

J. Segovia, M. C. Martín, D. del Campo, 2019, The Journal of Chemical Thermodynamics.

Excess enthalpies of oxygenated compounds + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and 2,2,4-trimethylpentane at 298.15 K

F. Alaoui, F. Aguilar, E. Montero, 2010 .

Excess enthalpies of binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol, and heptane at T = 298.15 K and 313.15 K

F. Alaoui, F. Aguilar, E. Montero, 2010 .

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 ether + alcohol + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and benzene at 298.15 K and 313.15 K

F. Alaoui, F. Aguilar, E. Montero, 2009 .

Excess Enthalpies of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and 1-Butanol at 298.15 K†

F. Alaoui, F. Aguilar, E. Montero, 2009 .

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 .

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 .

Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether+biphenyl) mixtures

J. Segovia, M. C. Martín, L. Lugo, 2016 .

Enhancement of hydrogen release kinetics from ethane 1,2 diamineborane (EDAB) by micronization using Supercritical Antisolvent (SAS) precipitation

J. Segovia, Ángel Martín, Miriam Rueda, 2016 .

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 .

Improvement of the kinetics of hydrogen release from ammonia borane confined in silica aerogel

J. Segovia, Ángel Martín, Miriam Rueda, 2017 .

Thermodynamic properties of biofuels: heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa and the pure compounds using a new flow calorimeter

J. Segovia, M. C. Martín, R. Villamañán, 2011 .

Density and viscosity of aqueous solutions of Methyldiethanolamine (MDEA) + Diethanolamine (DEA) at high pressures

J. Segovia, Alejandro Moreau, M. C. Martín, 2020 .

Speed of sound and phase equilibria for (CO2 + C3H8) mixtures

J. Segovia, M. C. Martín, T. Fernández-Vicente, 2021, The Journal of Chemical Thermodynamics.

High pressure densities of carbon dioxide + dipentaerythritol hexaheptanoate: New experimental setup and volumetric behavior

J. Segovia, Josefa Fernández, L. Lugo, 2011 .

Energy and Economic Analysis of the Hydrothermal Reduction of CO2 into Formate

J. Segovia, M. Bermejo, Ángel Martín, 2021, Industrial & Engineering Chemistry Research.

Speed of sound data and acoustic virial coefficients of two binary (N2 + H2) mixtures at temperatures between (260 and 350) K and at pressures between (0.5 and 20) MPa

D. Tůma, J. Segovia, Alejandro Moreau, 2022, The Journal of Chemical Thermodynamics.

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

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

A Spanish Inter-laboratory Comparison on the Characterization of Sterilization Autoclaves

J. Segovia, D. Campo, J. Cordero, 2014 .

Hydrothermal reduction of CO2 captured as NaHCO3 into formate with metal reductants and catalysts

J. Segovia, M. Bermejo, Ángel Martín, 2023, Journal of CO2 Utilization.

Exergetic Analysis of a Continuous Plant for the Hydrothermal Reduction of Co2 into Formate

J. Segovia, M. Bermejo, Ángel Martín, 2022, SSRN Electronic Journal.

Automated densimetric system: Measurements and uncertainties for compressed fluids

J. Segovia, M. C. Martín, Josefa Fernández, 2009 .

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

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

Heat capacities and densities of the binary mixtures containing ethanol, cyclohexane or 1-hexene at high pressures

J. Trusler, J. Segovia, M. C. Martín, 2013 .

High-pressure isobaric heat capacities using a new flow calorimeter

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

Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane

J. Segovia, Alejandro Moreau, M. C. Martín, 2016 .

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 .

Vapor-liquid equilibria of the binary systems (cyclohexanone + 2-heptanone) and (cyclohexanone + hexanal) at different temperatures

J. Rubio, J. Segovia, Alejandro Moreau, 2020, Journal of Molecular Liquids.

Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15 K and 313.15 K

F. Alaoui, F. Aguilar, E. Montero, 2012 .

Vapour–liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane

F. Aguilar, J. Segovia, Alejandro Moreau, 2013 .

Vapor-liquid equilibria and excess enthalpies of the binary systems 1-pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels

J. Segovia, Alejandro Moreau, M. C. Martín, 2018 .

Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels

J. Rubio, J. Segovia, Alejandro Moreau, 2016 .

Thermodynamic behaviour of second generation biofuels: Vapour–liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane

J. Segovia, Alejandro Moreau, M. C. Martín, 2014 .

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 .

Density, Viscosity, and Isobaric Heat Capacity of the Mixture (1-Butanol + 1‑Hexene)

J. Segovia, M. C. Martín, M. Villamañán, 2013 .

Viscosities and densities of different alcohols (1-propanol, 2-propanol, 1-pentanol and 2-pentanol) at high pressures

J. Segovia, Alejandro Moreau, J. Zambrano, 2021, Journal of Molecular Liquids.

Characterization of an Ecuadorian crude using a vibrating-tube densimeter and a vibrating-wire viscometer

J. Segovia, J. Zambrano, M. C. Martín, 2018, Petroleum science and technology.

Viscosities of binary mixtures containing 1-butanol + 2,2,4-trimethylpentane or + 1,2,4-trimethylbenzene at high pressures for the thermophysical characterization of biofuels

J. Segovia, J. Zambrano, M. C. Martín, 2016 .

Viscosity and density measurements of aqueous amines at high pressures: MDEA-water and MEA-water mixtures for CO2 capture

J. Segovia, M. C. Martín, E. Concepción, 2016 .

On the viscosity of two 1-butyl-1-methylpyrrolidinium ionic liquids: effect of the temperature and pressure

J. Segovia, Josefa Fernández, M. Comuñas, 2015 .

Thermophysical properties of 1,2,4-trimethylbenzene in admixtures with 1-butanol or 2-butanol at high pressures

J. Segovia, M. C. Martín, Geraldine A. Torín-Ollarves, 2017 .

Excess enthalpies of ternary mixtures of oxygenated additives + hydrocarbon mixtures in fuels and bio-fuels: Dibutyl ether (DBE) and 1-butanol and 1-hexene or cyclohexane or 2,2,4 trimethylpentane at 298.15 K and 313.15 K

F. Alaoui, F. Aguilar, E. Montero, 2013 .

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 .

High pressure liquid densities and excess volumes of the (di-isopropyl ether + 1-hexanol) system

F. Aguilar, E. Montero, J. Segovia, 2017 .

Dynamic and kinematic viscosities, excess volumes and excess Gibbs energies of activation for viscous flow in the ternary mixture {1- propanol+ N,N-dimethylformamide + chloroform} at temperatures between 293.15 K and 323.15 K

J. Segovia, M. Villamañán, A. Aitkaci, 2014 .

Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa

J. Trusler, J. Segovia, D. Vega‐Maza, 2010 .

Thermodynamic characterization of the mixture (1-butanol + iso-octane): Densities, viscosities, and isobaric heat capacities at high pressures

J. Segovia, M. C. Martín, M. Villamañán, 2012 .

Isothermal vapor–liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1-hexene + methylbenzene at 313.15 K

Latifa Negadi, J. Segovia, R. Villamañán, 2015 .

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 .

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 .

Vapour–liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels

J. Segovia, Alejandro Moreau, M. C. Martín, 2015 .

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

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

The Boltzmann project

G Sutton, F Sparasci, G Machin, 2018, Metrologia.

Speed of sound data, derived perfect-gas heat capacities, and acoustic virial coefficients of a calibration standard natural gas mixture and a low-calorific H2-enriched mixture

J. Segovia, Alejandro Moreau, M. C. Martín, 2021, The Journal of Chemical Thermodynamics.

Determination of density, viscosity and vapor pressures of mixtures of dimethyl sulfoxide + 1-allyl-3-methylimidazolium chloride at atmospheric pressure

J. Segovia, M. C. Martín, Ángel Martín, 2018, The Journal of Chemical Thermodynamics.

Determination of density and excess molar volume of dimethyl sulfoxide + 1-allyl-3-methylimidazolium chloride mixtures at high pressure

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

Influence of water concentration in the viscosities and densities of cellulose dissolving ionic liquids. Correlation of viscosity data

M. J. Cocero, J. Segovia, J. Zambrano, 2015 .

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. Pérez-Sanz, J. Segovia, M. C. Martín, 2014 .

A technical, economical and market review of organic Rankine cycles for the conversion of low-grade heat for power generation

Farid Chejne, Ana Quijano, Fredy Vélez, 2012 .

Speed of Sound Measurements of Biogas from a Landfill Biomethanation Process

J. Segovia, Alejandro Moreau, D. Vega-Maza, 2023, Energies.

Speeds of sound for (CH4 + He) mixtures from p = (0.5 to 20) MPa at T = (273.16 to 375) K

J. Segovia, M. C. Martín, D. Vega-Maza, 2019 .

Speeds of sound for a biogas mixture CH4 + N2 + CO2 + CO from p = (1–12) MPa at T = (273, 300 and 325) K measured with a spherical resonator

J. Segovia, M. C. Martín, D. Campo, 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 .

Measurement and Analysis of the Temperature Gradient of Blackbody Cavities, for Use in Radiation Thermometry

J. Segovia, J. de Lucas, 2018, International journal of thermophysics.

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

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

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

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

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 .