J. Trusler

发表

Experimental and molecular modeling study of the three-phase behavior of (n-decane + carbon dioxide + water) at reservoir conditions.

Amparo Galindo, Esther Forte, A. Galindo, 2011, The journal of physical chemistry. B.

Density and Phase Behavior of the CO2 + Methylbenzene System in Wide Ranges of Temperatures and Pressures

J. Trusler, Y. Sanchez-Vicente, Weparn J. Tay, 2020, Industrial & Engineering Chemistry Research.

Thermodynamics of carbon dioxide-hydrocarbon systems

J. Trusler, Y. Sanchez-Vicente, Weparn J. Tay, 2018, Applied Energy.

Carbon capture and storage (CCS): the way forward

Solomon F. Brown, C. Adjiman, E. Rubin, 2018 .

Interfacial tensions in the (CH4 + CO2 + H2O) system under two- and three-phase conditions

J. Trusler, P. Lv, M. Stevar, 2020 .

Experimental density and an improved Helmholtz-energy-explicit mixture model for (CO2 + CO)

R. Span, J. Trusler, L. F. Souza, 2019, Applied Energy.

Interfacial tensions of (H2O + H2) and (H2O + CO2 + H2) systems at temperatures of (298–448) K and pressures up to 45 MPa

J. Trusler, G. Maitland, Y. T. F. Chow, 2018, Fluid Phase Equilibria.

Measurement and modelling of the vapor–liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa

J. Trusler, S. A. Ghafri, L. F. Souza, 2018, The Journal of Chemical Thermodynamics.

Interfacial Tension of (Brines+CO2): CaCl2(aq), MgCl2(aq), and Na2SO4(aq) at Temperatures between (343 and 423) K, Pressures between (2 and 50) MPa, and Molalities of (0.5 to 5) mol.kg-1

E. Boek, J. Trusler, G. Maitland, 2012 .

Interfacial Tension of (Brines + CO2): (0.864 NaCl + 0.136 KCl) at Temperatures between (298 and 448) K, Pressures between (2 and 50) MPa, and Total Molalities of (1 to 5) mol·kg–1

E. Boek, J. Trusler, G. Maitland, 2012 .

Solubility of carbon dioxide in aqueous solution of monoethanolamine or 2-amino-2-methyl-1-propanol: Experimental measurements and modelling

P. Fennell, J. Gibbins, J. Trusler, 2012 .

Saturated phase densities of (CO2 + H2O) at temperatures from (293 to 450) K and pressures up to 64 MPa

J. Trusler, Y. Sanchez-Vicente, Emmanuel C. Efika, 2016 .

Residual entropy model for predicting the viscosities of dense fluid mixtures.

J. Trusler, Malyanah Binti Mohd Taib, 2020, The Journal of chemical physics.

The Viscosity and Density of n-Dodecane and n-Octadecane at Pressures up to 200 MPa and Temperatures up to 473 K

W. Wakeham, V. Vesovic, J. Trusler, 2004 .

Experimental and modeling study of the phase behavior of synthetic crude oil+CO2

J. Trusler, S. A. Ghafri, G. Maitland, 2014 .

Combined Helmholtz energy, extended corresponding states and local-composition model for fluid mixtures ☆

J. Trusler, A. D. Mendoza, J. Estela-Uribe, 2004 .

Virial equation of state for natural gas systems

J. Trusler, M. A. Salazar, J. Estela-Uribe, 2003 .

Solubility of CO2 in aqueous amine solutions: A study to select solvents for carbon capture from natural-gas power plant

P. Fennell, J. Trusler, Danlu Tong, 2015 .

Viscosity and Density of Carbon Dioxide + 2,6,10,15,19,23-Hexamethyltetracosane (Squalane) †

V. Vesovic, J. Trusler, G. Maitland, 2009 .

Effect of CO2 Dissolution on the Rheology of a Heavy Oil/Water Emulsion

J. Trusler, J. Crawshaw, R. Hu, 2017 .

Refractive Index Effects in Pendant Drop Tensiometry

Ziqing Pan, J. Trusler, 2022, International Journal of Thermophysics.

Measurements and interpretation of crude Oil-Water/Brine dynamic interfacial tension at subsurface representative conditions

A. Georgiadis, J. Trusler, Kaiqiang Zhang, 2022, Fuel.

Interfacial Tension Measurements of the (H2O + n-Decane + CO2) Ternary System at Elevated Pressures and Temperatures

A. Bismarck, J. Trusler, A. Georgiadis, 2011 .

Phase behaviour of mixed-gas hydrate systems containing carbon dioxide

J. Trusler, L. Ruffine, 2010 .

Experimental and Modeling Study of the Phase Behavior of (Heptane + Carbon Dioxide + Water) Mixtures

A. Galindo, Esther Forte, J. Trusler, 2015 .

Primary acoustic thermometry betweenT = 90 K andT = 300 K

J. Trusler, M. B. Ewing, 2000 .

The speed of sound and derived thermodynamic properties of methane at temperatures between 275 K and 375 K and pressures up to 10 MPa

J. Trusler, M. P. Zarari, 1992 .

Employing SAFT Coarse-Grained Force Fields for the Molecular Simulation of Thermodynamic and Transport Properties of CO2–n-Alkane Mixtures

E. A. Müller, J. Trusler, Lingru Zheng, 2020, Journal of Chemical & Engineering Data.

Modelling the Diffusion Coefficients of Dilute Gaseous Solutes in Hydrocarbon Liquids

J. Trusler, M. M. Taib, Yasser A. Aljeshi, 2021, International Journal of Thermophysics.

Measurement of the Viscosity and Density of Two Reference Fluids, with Nominal Viscosities at T = 298 K and p = 0.1 MPa of (16 and 29) mPa·s, at Temperatures between (298 and 393) K and Pressures below 55 MPa

A. Goodwin, K. Marsh, J. Trusler, 2005 .

Measurements and Modelling of Vapour–Liquid Equilibrium for (H2O + N2) and (CO2 + H2O + N2) Systems at Temperatures between 323 and 473 K and Pressures up to 20 MPa

J. Trusler, Y. Sanchez-Vicente, 2022, Energies.

The effect of pH, dilution, and temperature on the viscosity of ocular lubricants—shift in rheological parameters and potential clinical significance

J. Trusler, K. Ramaesh, M. Q. Rahman, 2012, Eye.

Design of a laboratory for experiments with a pulsed neutron source

G. Memoli, J. Trusler, A. Ziver, 2009, Journal of radiological protection : official journal of the Society for Radiological Protection.

Vapor pressure and density of thermotropic liquid crystals: MBBA, 5CB, and novel fluorinated mesogens.

G. Jackson, J. Trusler, J. Deschamps, 2008, The journal of physical chemistry. B.

The speed of sound in gaseous propane at temperatures between 225 K and 375 K and at pressures up to 0.8 MPa

J. Trusler, M. P. Zarari, 1996 .

Viscosities and Densities of Binary Mixtures of Hexadecane with Dissolved Methane or Carbon Dioxide at Temperatures from (298 to 473) K and at Pressures up to 120 MPa

J. Trusler, Fausto Ciotta, M. Mohammed, 2017 .

International Standard for viscosity at temperatures up to 473 K and pressures below 200 MPa (IUPAC Technical Report)

Marc J. Assael, J. Trusler, R. Enick, 2018, Chemistry International.

Phase equilibria of (CO2 + butylbenzene) and (CO2 + butylcyclohexane) at temperatures between (323.15 and 423.15) K and at pressures up to 21 MPa

J. Trusler, G. Maitland, Shu-Xin Hou, 2015 .

Electroreduction of CO2/CO to C2 Products: Process Modeling, Downstream Separation, System Integration, and Economic Analysis

P. Webley, T. Breugelmans, T. Vlugt, 2021, Industrial & engineering chemistry research.

Extended hard-sphere model for the viscosity of dense fluids

V. Vesovic, J. Trusler, Fausto Ciotta, 2014 .

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 .

Surrogate Models for Studying the Wettability of Nanoscale Natural Rough Surfaces Using Molecular Dynamics

A. Georgiadis, E. A. Müller, J. Trusler, 2020, Energies.

A shortcut pressure swing adsorption analogue model to estimate Gas-in-Place and CO2 storage potential of gas shales

R. Pini, J. Trusler, G. Maitland, 2021 .

Hydrogen Liquefaction: A Review of the Fundamental Physics, Engineering Practice and Future Opportunities

T. Funke, J. Trusler, Saif Z. S. Al Ghafri, 2022, Energy & Environmental Science.

Liquid−Liquid Equilibria in Aqueous Two-Phase Systems of Poly(ethylene glycol) and Poly(ethyleneimine): Experimental Measurements and Correlation

G. Cholakov, J. Trusler, D. Yankov, 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 .

Supercritical adsorption in micro- and meso-porous carbons and its utilisation for textural characterisation

R. Pini, J. Trusler, G. Maitland, 2020, Microporous and Mesoporous Materials.

Viscosity and Density of Five Hydrocarbon Liquids at Pressures up to 200 MPa and Temperatures up to 473 K

W. Wakeham, V. Vesovic, J. Trusler, 2009 .

Solubility of hydrogen in sodium chloride brine at high pressures

J. Trusler, Geraldine A. Torín-Ollarves, 2021, Fluid Phase Equilibria.

Supplementary Information to Perspective on the hydrogen economy as a pathway to reach net-zero CO 2 emissions in Europe

Matteo, S. T. Munkejord, M. Mazzotti, 2021 .

Hybrid Pore-Scale Adsorption Model for CO2 and CH4 Storage in Shale

R. Pini, J. Trusler, H. Ansari, 2022, Energy & Fuels.

Extension of Vibrating-Wire Viscometry to Electrically Conducting Fluids and Measurements of Viscosity and Density of Brines with Dissolved CO2 at Reservoir Conditions

J. Trusler, G. Maitland, Claudio Calabrese, 2019, Journal of Chemical & Engineering Data.

Measurement and modeling of the viscosity of (nitrogen + carbon dioxide) mixtures at temperatures from (253.15 to 473.15) K with pressures up to 2 MPa

R. Span, J. Trusler, M. Richter, 2018 .

Speeds of Sound in n-Pentane at Temperatures from 233.50 to 473.15 K at Pressures up to 390 MPa

J. Trusler, Y. Sanchez-Vicente, M. Thol, 2020 .

Phase equilibria of (Methylbenzene + Carbon dioxide + Methane) at elevated pressure: Experiment and modelling

J. Trusler, Saif Z. S. Al Ghafri, J. P. M. Trusler, 2019, The Journal of Supercritical Fluids.

SAFT coarse grained force fields for the molecular simulation of thermophysical and transport properties of CO 2 – n-alkane mixtures

E. A. Müller, J. Trusler, Lingru Zheng, 2019 .

Improvement of Quality in Publication of Experimental Thermophysical Property Data: Challenges, Assessment Tools, Global Implementation, and Online Support

Michael D. Frenkel, Vladimir Diky, Kenneth N. Marsh, 2013 .

Influence of Lactic Acid on the Formation of Aqueous Two-Phase Systems Containing Poly(ethylene glycol) and Phosphates

B. Yordanov, J. Trusler, D. Yankov, 2008 .

Phase behavior and physical properties of petroleum reservoir fluids from acoustic measurements

A. Goodwin, J. Trusler, S. Ball, 2002 .

Mutual Diffusion Coefficients of Aqueous KCl at High Pressures Measured by the Taylor Dispersion Method

W. Wakeham, J. Trusler, G. Maitland, 2011 .

Review of density and viscosity data of pure fatty acid methyl ester, ethyl ester and butyl ester

J. Trusler, C. Wedler, 2023, Fuel.

Brine chemistry effects in calcite dissolution kinetics at reservoir conditions

J. Trusler, J. Crawshaw, B. Anabaraonye, 2019, Chemical Geology.

High-Pressure Electrochemical Reduction of CO2 to Formic Acid/Formate: Effect of pH on the Downstream Separation Process and Economics

T. Breugelmans, T. Vlugt, W. Jong, 2019, Industrial & Engineering Chemistry Research.

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 .

Predicting the pressure dependence of the viscosity of 2,2,4-trimethylhexane using the SAFT coarse-grained force field

E. A. Müller, J. Trusler, Lingru Zheng, 2019, Fluid Phase Equilibria.

High Pressure Electrochemical Reduction of CO2 to Formic Acid/Formate: A Comparison between Bipolar Membranes and Cation Exchange Membranes

T. Vlugt, M. Ramdin, J. Trusler, 2019, Industrial & engineering chemistry research.

Measurement and modeling of the phase behavior of the (carbon dioxide + water) mixture at temperatures from 298.15 K to 448.15 K

J. Trusler, G. Maitland, Shu-Xin Hou, 2013 .

Kinetics of calcite dissolution in CO2-saturated water at temperatures between (323 and 373) K and pressures up to 13.8 MPa

J. Trusler, G. Maitland, J. Crawshaw, 2015 .

Kinetics of carbonate mineral dissolution in CO2-acidified brines at storage reservoir conditions.

J. Trusler, G. Maitland, J. Crawshaw, 2016, Faraday discussions.

The pH of CO2-saturated water at temperatures between 308 K and 423 K at pressures up to 15 MPa

John P. Crawshaw, Geoffrey C. Maitland, J. Trusler, 2013 .

Rheology of diluted heavy crude oil saturated with carbon dioxide

E. Boek, J. Trusler, J. Crawshaw, 2015 .

Wettability of calcite under carbon storage conditions

C. Böhm, J. Trusler, M. Stevar, 2019, International Journal of Greenhouse Gas Control.

Cloud Curves of Polystyrene or Poly(methyl methacrylate) or Poly(styrene-co-methyl methacrylate) in Cyclohexanol Determined with a Thermo-Optical Apparatus

J. Trusler, J. Higgins, V. G. Sakai, 2006 .

Erratum: “Equation of state for solid benzene valid for temperatures up to 470 K and pressures up to 1800 MPa” [J. Phys. Chem. Ref. Data 50, 043104 (2021)]

J. Trusler, Saif Z. S. Al Ghafri, E. May, 2022, Journal of Physical and Chemical Reference Data.

Equation of State for Solid Benzene Valid for Temperatures up to 470 K and Pressures up to 1800 MPa

J. Trusler, Saif Z. S. Al Ghafri, E. May, 2021, Journal of Physical and Chemical Reference Data.

Anthony Robert Holmes Goodwin (1961–2014)

W. Wakeham, J. Trusler, 2015 .

A robust vibrating wire viscometer for reservoir fluids: results for toluene and n-decane

Anthony R. H. Goodwin, A. Goodwin, J. Trusler, 2004 .

Experimental and molecular modelling study of the three-phase behaviour of (propane + carbon dioxide + water) at reservoir conditions

Amparo Galindo, Esther Forte, A. Galindo, 2013 .

Reference materials for phase equilibrium studies. 2. Solid–liquid equilibria (IUPAC Technical Report)

J. D. Olson, D. Nordstrom, W. Acree, 2021, Chemistry International.

Viscosities of Liquid Cyclohexane and Decane at Temperatures between (303 and 598) K and Pressures up to 4 MPa Measured in a Dual-Capillary Viscometer

J. Trusler, Q. Bi, Zhaohui Liu, 2015 .

Viscosity and Density of 1,3-Dimethylbenzene + Carbon Dioxide at Temperatures from 298 to 423 K and at Pressures up to 100 MPa

J. Trusler, Malyanah Binti Mohd Taib, 2020 .

New Experimental Data and Reference Models for the Viscosity and Density of Squalane

J. Trusler, G. Maitland, K. Schmidt, 2015 .

3 The virial equation of state

J. Trusler, 2000 .

Viscosity of liquid mixtures: the Vesovic-Wakeham method for chain molecules.

George Jackson, Astrid S de Wijn, G. Jackson, 2012, The Journal of chemical physics.

A kinetic theory description of the viscosity of dense fluids consisting of chain molecules.

G. Jackson, V. Vesovic, J. Trusler, 2008, The Journal of chemical physics.

Viscosities of Liquid Hexadecane at Temperatures between 323 K and 673 K and Pressures up to 4 MPa Measured Using a Dual-Capillary Viscometer

J. Trusler, Y. Sanchez-Vicente, I. Emerson, 2019, Journal of Chemical & Engineering Data.

Atomistic Molecular Dynamics Simulations of Carbon Dioxide Diffusivity in n-Hexane, n-Decane, n-Hexadecane, Cyclohexane, and Squalane.

A. Panagiotopoulos, I. Economou, J. Trusler, 2016, The journal of physical chemistry. B.

Density, sound speed and derived thermophysical properties of n-nonane at temperatures between (283.15 and 473.15) K and at pressures up to 390 MPa

J. Trusler, Weparn J. Tay, 2018, The Journal of Chemical Thermodynamics.

Thermodynamic properties of mixtures of N-methyl-2-pyrrolidinone and methanol at temperatures between 298.15 K and 343.15 K and pressures up to 60 MPa

J. Trusler, M. J. Dávila, J. P. Martin Trusler, 2009 .

Thermodynamic Properties of Liquid Toluene from Speed-of-Sound Measurements at Temperatures from 283.15 K to 473.15 K and at Pressures up to 390 MPa

S. Dhakal, J. Trusler, Weparn J. Tay, 2021, International Journal of Thermophysics.

Identification of environmentally acceptable low-sound speed liquids

J. Trusler, L. Cusco, 1995 .

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 .

Densities of Aqueous MgCl2(aq), CaCl2(aq), KI(aq), NaCl(aq), KCl(aq), AlCl3(aq), and (0.964 NaCl + 0.136 KCl)(aq) at Temperatures Between (283 and 472) K, Pressures up to 68.5 MPa, and Molalities up to 6 mol·kg–1

Geoffrey C. Maitland, J. Trusler, S. A. Ghafri, 2012 .

Phase behavior of (CO2 + H2) and (CO2 + N2) at temperatures between (218.15 and 303.15) K at pressures up to 15 MPa

J. Trusler, J. P. Martin Trusler, David Vega-Maza, 2015 .

Extended corresponding states model for fluids and fluid mixtures: I. Shape factor model for pure fluids

J. Trusler, J. F. Estela-Uribe, J.P.M. Trusler, 2003 .

Extended corresponding states equation of state for natural gas systems

J. Trusler, J. F. Estela-Uribe, J.P.M. Trusler, 2001 .

An Industrial Reference Fluid for Moderately High Viscosity

K. R. Harris, A. Leipertz, A. P. Fröba, 2008 .

Experimental and modelling study of the phase behavior of (methyl propanoate + carbon dioxide) at temperatures between (298.15 and 423.15) K and pressures up to 20 MPa

J. Trusler, Saif Z. S. Al Ghafri, S. A. Ghafri, 2020 .

Densities and bubble points of binary mixtures of carbon dioxide and n-heptane and ternary mixtures of n-butane, n-heptane and n-hexadecane

W. Wakeham, J. Trusler, A. Fenghour, 2001 .

Densities and bubble points of ternary mixtures of methane, n-butane and n-hexadecane and quaternary mixtures of methane, n-butane, n-heptane and n-hexadecane

W. Wakeham, J. Trusler, A. Fenghour, 2001 .

Rheology and Phase Behavior of Carbon Dioxide and Crude Oil Mixtures

E. Boek, J. Trusler, J. Crawshaw, 2017 .

Circulating pump for high-pressure and high-temperature applications

A. Goodwin, J. Trusler, G. Maitland, 2005 .

Viscosity of Liquid Di-isodecyl Phthalate at Temperatures Between (274 and 373) K and at Pressures up to 140 MPa

J. Trusler, F. Peleties, 2011 .

The Viscosity of Organic Liquid Mixtures

W. Wakeham, V. Vesovic, J. Trusler, 2006 .

Extended corresponding states model for fluids and fluid mixtures: II. Application to mixtures and natural gas systems

J. Trusler, A. D. Mendoza, J. F. Estela-Uribe, 2004 .

Experimental and modeling study of the phase behavior of (methane + CO2 + water) mixtures.

Esther Forte, Esther Forte, J. Trusler, 2014, Journal of Physical Chemistry B.

Densities of SrCl2(aq), Na2SO4(aq), NaHCO3(aq), and Two Synthetic Reservoir Brines at Temperatures between (298 and 473) K, Pressures up to 68.5 MPa, and Molalities up to 3 mol·kg–1

Geoffrey C. Maitland, J. Trusler, S. A. Ghafri, 2013 .

Prediction of the viscosity of dense fluid mixtures

W. Wakeham, V. Vesovic, J. Trusler, 2003 .

Improved Understanding of Vibrating-Wire Viscometer−Densimeters

J. Trusler, Fausto Ciotta, 2010 .

Phase behaviour and density of (methane+n-butane)

W. Wakeham, J. Trusler, A. Fenghour, 1999 .

Shape factors for the light hydrocarbons

J. Trusler, J. F. Estela-Uribe, J.P.M. Trusler, 1998 .

Phase behaviour and density of model reservoir fluids at high temperature and pressure

W. Wakeham, J. Trusler, A. Fenghour, 1999 .

Viscosity and Density of Aqueous Solutions of Carbon Dioxide at Temperatures from (274 to 449) K and at Pressures up to 100 MPa

Geoffrey C. Maitland, J. Trusler, G. Maitland, 2015 .

Phase equilibria of (CO2 + H2O + NaCl) and (CO2 + H2O + KCl): Measurements and modeling

Geoffrey C. Maitland, J. Trusler, G. Maitland, 2013 .

Density and Viscosity of Partially Carbonated Aqueous Tertiary Alkanolamine Solutions at Temperatures between (298.15 and 353.15) K

P. Fennell, J. Trusler, Jiafei Zhang, 2015 .

Reference materials for phase equilibrium studies. 1. Liquid–liquid equilibria (IUPAC Technical Report)

J. D. Olson, W. Acree, V. Diky, 2021, Pure and Applied Chemistry.

Speed of Sound in (Carbon Dioxide + Propane) and Derived Sound Speed of Pure Carbon Dioxide at Temperatures between (248 and 373) K and at Pressures up to 200 MPa

J. Trusler, C.-W. Lin, J.P.M. Trusler, 2014 .

Speeds of Sound in Liquid and Supercritical Hexafluoropropylene (HFP) and Hexafluoropropylene Oxide (HFPO) at Pressures up to 400 MPa

J. Trusler, D. Ramjugernath, P. Reddy, 2012 .

Composition Analysis and Viscosity Prediction of Complex Fuel Mixtures Using a Molecular-Based Approach

P. Ungerer, R. Lugo, J. Trusler, 2012 .

Application of the statistical associating fluid theory for potentials of variable range (SAFT-VR) coupled with renormalisation-group (RG) theory to model the phase equilibria and second-derivative properties of pure fluids

A. Galindo, Esther Forte, F. Llovell, 2013 .

Determination of the thermodynamic properties of water from the speed of sound

J. Trusler, E. Lemmon, 2017 .

The speed of sound in gaseous argon at temperatures between 110 K and 450 K and at pressures up to 19 MPa

J. Trusler, A. F. Estrada-Alexanders, 1995 .

Erratum: "Physical apparatus parameters and model for vibrating tube densimeters at pressures to 140 MPa and temperatures to 473 K" [Rev. Sci. Instrum. 85, 095111 (2014)].

J. Trusler, Weparn J. Tay, E. May, 2015, The Review of scientific instruments.

Physical apparatus parameters and model for vibrating tube densimeters at pressures to 140 MPa and temperatures to 473 K.

J. Trusler, Weparn J. Tay, E. May, 2014, The Review of scientific instruments.

Measurement and Modelling of the Interfacial Tensions of Co2 + Decane-Iododecane Mixtures at High Pressures and Temperatures

Ziqing Pan, J. Trusler, 2022, SSRN Electronic Journal.

Density and Phase Behaviour of ( CO 2 + Methylbenzene ) in Wide Ranges of Temperatures and Pressures

J. Trusler, Y. Sanchez-Vicente, Weparn J. Tay, 2021 .

Speed of sound in carbon dioxide at temperatures between (220 and 450) K and pressures up to 14 MPa

J. Trusler, A. F. Estrada-Alexanders, J.P.M. Trusler, 1998 .

Predicting the viscosity of liquid refrigerant blends: comparison with experimental data

W. Wakeham, V. Vesovic, J. Trusler, 2005 .

Diffusion Coefficients of Carbon Dioxide in Brines Measured Using 13C Pulsed-Field Gradient Nuclear Magnetic Resonance

J. Hallett, J. Trusler, Shane P. Cadogan, 2015 .

Diffusion Coefficients of CO2 and N2 in Water at Temperatures between 298.15 K and 423.15 K at Pressures up to 45 MPa

J. Trusler, Shane P. Cadogan, G. Maitland, 2014 .

Interfacial Tension Measurements of the (H2O + CO2) System at Elevated Pressures and Temperatures†

A. Bismarck, J. Trusler, A. Georgiadis, 2010 .

Interfacial tensions of systems comprising water, carbon dioxide and diluent gases at high pressures: Experimental measurements and modelling with SAFT-VR Mie and square-gradient theory

A. Galindo, G. Jackson, A. J. Haslam, 2016 .

Interfacial tension measurements and modelling of (carbon dioxide + n-alkane) and (carbon dioxide + water) binary mixtures at elevated pressures and temperatures

A. Galindo, G. Jackson, A. Georgiadis, 2010 .

Experimental and Modelling Study of the Interfacial Tension of (n-Decane + Carbon Dioxide + Water) in the Three Phase Region

Ziqing Pan, J. Trusler, 2023, Fluid Phase Equilibria.

Thermophysical Properties and Phase Behavior of Fluids for Application in Carbon Capture and Storage Processes.

J. Trusler, J. P. M. Trusler, 2017, Annual review of chemical and biomolecular engineering.

Interfacial tensions of the (CO2 + N2 + H2O) system at temperatures of (298 to 448) K and pressures up to 40 MPa

J. Trusler, G. Maitland, Y. T. F. Chow, 2016 .

Molecular dynamics simulations of CO2 and brine interfacial tension at high temperatures and pressures.

E. Boek, J. Trusler, G. Maitland, 2013, The journal of physical chemistry. B.

Diffusion Coefficients of Methane in Methylbenzene and Heptane at Temperatures between 323 K and 398 K at Pressures up to 65 MPa

J. Trusler, M. M. Taib, 2020, International Journal of Thermophysics.

Interfacial tensions of systems comprising N2, 7 mass% KI (aq), decane and iododecane at elevated pressures and temperatures

Ziqing Pan, J. Trusler, 2021, Fluid Phase Equilibria.

Erratum to “Interfacial tensions of (H2O + H2) and (H2O + CO2 + H2) systems at temperatures of (298 to 448) K and pressures up to 45 MPa” [Fluid Phase Equil. 475 (2018) 37–44]

J. Trusler, G. Maitland, Y. T. F. Chow, 2020 .

Solubility of CO2 in Aqueous Solutions of CaCl2 or MgCl2 and in a Synthetic Formation Brine at Temperatures up to 423 K and Pressures up to 40 MPa

Danlu Tong, J. Trusler, Danlu Tong, 2013 .

Phase Behavior of the System (Carbon Dioxide + n-Heptane + Methylbenzene): A Comparison between Experimental Data and SAFT-γ-Mie Predictions

J. Trusler, S. A. Ghafri, G. Maitland, 2017 .

Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa

J. Trusler, Shane P. Cadogan, G. Maitland, 2016 .

The pH of CO2-saturated aqueous NaCl and NaHCO3 solutions at temperatures between 308 K and 373 K at pressures up to 15 MPa

J. Trusler, G. Maitland, J. Crawshaw, 2018 .

Heat Transfer in Pure Critical Fluids Surrounded by Finitely Conducting Boundaries in Microgravity

W. Wakeham, J. Trusler, T. Karapantsios, 1997 .

Measurement of the Universal Gas Constant R Using a Spherical Acoustic Resonator

T. J. Edwards, R. Davis, M. Moldover, 1988, Journal of Research of the National Bureau of Standards.

Application of a renormalization-group treatment to the statistical associating fluid theory for potentials of variable range (SAFT-VR).

Amparo Galindo, Felix Llovell, Esther Forte, 2011, The Journal of chemical physics.

Thermophysical properties of alkanes from speeds of sound determined using a spherical resonator I. Apparatus, acoustic model, and results for dimethylpropane

A. Goodwin, J. Trusler, M. L. Mcglashan, 1987 .

Measurements and modelling of the viscosity of six synthetic crude oil mixtures

V. Vesovic, J. Trusler, T. Nguyen, 2020 .

Equation of state for gaseous propane determined from the speed of sound

J. Trusler, 1997 .

Speed of Sound of n-Hexane and n-Hexadecane at Temperatures Between 298 and 373 K and Pressures up to 100 MPa

S. J. Ball, J. Trusler, J.P.M. Trusler, 2001 .

Delft University of Technology High pressure electrochemical reduction of CO2 to formic acid/formate A comparison between bipolar membranes and cation exchange membranes

T. Vlugt, W. Jong, M. Ramdin, 2019 .

Equation of State for Solid Phase I of Carbon Dioxide Valid for Temperatures up to 800 K and Pressures up to 12 GPa

J. Trusler, J. P. Martin Trusler, 2011 .

Measurements and modelling of the viscosity of (methane + ethane) mixtures at temperatures from (253.15 to 473.15) K with pressures up to 2 MPa

R. Span, J. Trusler, M. Richter, 2020 .

Speed of Sound Measurements in Helium at Pressures from 15 to 100 MPa and Temperatures from 273 to 373 K

J. Trusler, C. Wedler, 2023, Journal of chemical and engineering data.

Guidelines for reporting of phase equilibrium measurements (IUPAC Recommendations 2012)

W. M. Haynes, Vicente Rives, J. D. Olson, 2012 .

Diffusion Coefficients of N2O and H2 in Water at Temperatures between 298.15 and 423.15 K with Pressures up to 30 MPa

Ziqing Pan, T. Zhou, J. Trusler, 2023, Journal of Chemical & Engineering Data.

Erratum: Equation of State for Solid Phase I of Carbon Dioxide Valid for Temperatures up to 800 K and Pressures up to 12 GPa [J. Phys. Chem. Ref. Data 40, 043105 (2011)]

J. Trusler, J. P. Martin Trusler, 2012 .

The speed of sound in two methane-rich gas mixtures at temperatures between 250 K and 350 K and at pressures up to 20 MPa

M. Gomes, J. Trusler, 1998 .

The speed of sound in (0.8CH4 + 0.2C2H6)(g) at temperatures between 200 K and 375 K and amount-of-substance densities up to 5 mol·dm-3

J. Trusler, 1994 .

Accurate acoustic thermometry. I: The triple point of gallium

M. Moldover, J. Trusler, J. Trusler, 1988 .

Measurement of the universal gas constant R using a spherical acoustic resonator.

Davis, T. J. Edwards, Mehl, 1987, Physical review letters.

Microwave Measurements of the Thermal Expansion of a Spherical Cavity

M. Moldover, J. Trusler, J. Trusler, 1988 .

Speed of sound in (0.4C2H6 + 0.6CO2) at temperatures betweenT = 220 K andT = 450 K and pressures up top = 1.2 MPa

J. Trusler, A. F. Estrada-Alexanders, J.P.M. Trusler, 1999 .

Second and third interaction virial coefficients of the (methane+propane) system determined from the speed of sound

W. Wakeham, J. Trusler, M. P. Zarari, 1996 .

The speed of sound in gases. II: Acoustic virial coefficients and perfect-gas heat capacities for 2,2-dimethylpropane obtained using a cylindrical interferometer

J. Trusler, M. L. Mcglashan, J. Trusler, 1986 .

Perspective on the hydrogen economy as a pathway to reach net-zero CO 2 emissions in Europe † PERSPECTIVE

S. T. Munkejord, M. Mazzotti, Christian Bauer, 2022 .

Perspective on the hydrogen economy as a pathway to reach net-zero CO 2 emissions in Europe † PERSPECTIVE

S. T. Munkejord, M. Mazzotti, Christian Bauer, 2022 .

High Pressure Electrochemical Reduction of CO2 to Formic Acid/Formate: A Comparison between Bipolar Membranes and Cation Exchange Membranes

T. Vlugt, M. Ramdin, J. Trusler, 2019, Industrial & engineering chemistry research.

Speeds of Sound in Binary Mixtures of Water and Carbon Dioxide at Temperatures from 273 K to 313 K and at Pressures up to 50 MPa

J. Trusler, Saif Z. S. Al Ghafri, E. May, 2023, International Journal of Thermophysics.

Speed of sound and derived thermodynamic properties of para-xylene at temperatures between (306 and 448) K and at pressures up to 66 MPa

J. Trusler, E. May, P. Stanwix, 2019, The Journal of Chemical Thermodynamics.

Influence of Solvents and Salts on CO2 Solubility and the Impact on an Esterification Reaction

G. Sadowski, J. Trusler, C. Held, 2023, Journal of Chemical & Engineering Data.

Saturated-Phase Densities of ( CO 2 + Methylcyclohexane ) at Temperatures from 298 to 448 K and Pressures up to the Critical Pressure

J. Trusler, Y. Sanchez-Vicente, 2022 .