Thermo-physical properties of CO2 mixtures and their impacts on CO2 capture, transport and storage: Progress since 2011

[1]  Bo Chen,et al.  Superior energy-saving splitter in monoethanolamine-based biphasic solvents for CO2 capture from coal-fired flue gas , 2019, Applied Energy.

[2]  E. Thorin,et al.  Impacts of thermos-physical properties on plate-fin multi-stream heat exchanger design in cryogenic process for CO2 capture , 2019, Applied Thermal Engineering.

[3]  E. May,et al.  Densities and dielectric permittivities for (carbon monoxide + carbon dioxide) mixtures determined with a microwave re-entrant cavity resonator , 2019, The Journal of Chemical Thermodynamics.

[4]  Jinyue Yan,et al.  Carbon Capture, Utilization and Storage (CCUS) , 2019, Applied Energy.

[5]  A. Hawkes,et al.  An assessment of CCS costs, barriers and potential , 2018, Energy Strategy Reviews.

[6]  Snorre Foss Westman,et al.  Vapor-liquid equilibrium data for the carbon dioxide and carbon monoxide (CO2 + CO) system at the temperatures 253, 273, 283 and 298 K and pressures up to 13 MPa , 2018, Fluid Phase Equilibria.

[7]  Beatriz Gimeno,et al.  Influence of SO2 on CO2 Transport by Pipeline for Carbon Capture and Storage Technology: Evaluation of CO2/SO2 Cocapture , 2018, Energy & Fuels.

[8]  Snorre Foss Westman,et al.  Thermodynamics of the carbon dioxide plus argon (CO 2  + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213–299 K and pressures up to 16 MPa , 2018, Fluid Phase Equilibria.

[9]  Snorre Foss Westman,et al.  Vapor - liquid equilibrium of the carbon dioxide/methane mixture at three isotherms , 2018 .

[10]  B. Tohidi,et al.  Viscosity of CO2-rich mixtures from 243 K to 423 K at pressures up to 155 MPa: new experimental viscosity data and modelling , 2018 .

[11]  B. Tohidi,et al.  New experimental density data and derived thermophysical properties of carbon dioxide – Sulphur dioxide binary mixture (CO 2 -SO 2 ) in gas, liquid and supercritical phases from 273 K to 353 K and at pressures up to 42 MPa , 2017 .

[12]  Beatriz Gimeno,et al.  Influence of SO2 on CO2 storage for CCS technology: Evaluation of CO2/SO2 co-capture , 2017 .

[13]  H. Knuutila,et al.  Viscosity measurements and modeling of loaded and unloaded aqueous solutions of MDEA, DMEA, DEEA and MAPA , 2017 .

[14]  B. Tohidi,et al.  Measured densities and derived thermodynamic properties of CO2-rich mixtures in gas, liquid and supercritical phases from 273 K to 423 K and pressures up to 126 MPa , 2017 .

[15]  E. Thorin,et al.  Evaluation of viscosity and thermal conductivity models for CO2 mixtures applied in CO2 cryogenic process in carbon capture and storage (CCS) , 2017 .

[16]  Morten Hammer,et al.  Thermodynamic models to accurately describe the PVTxy-behavior of water / carbon dioxide mixtures , 2017 .

[17]  Alireza Rostami,et al.  Genetic Programming (GP) Approach for Prediction of Supercritical CO2 Thermal Conductivity , 2017 .

[18]  P. Paricaud,et al.  Comparative study of vapour-liquid equilibrium and density modelling of mixtures related to carbon capture and storage with the SRK, PR, PC-SAFT and SAFT-VR Mie equations of state for industrial uses , 2017 .

[19]  E. May,et al.  Densities, Dielectric Permittivities, and Dew Points for (Argon + Carbon Dioxide) Mixtures Determined with a Microwave Re-entrant Cavity Resonator , 2017 .

[20]  P. Chiesa,et al.  Measurement and prediction of multi-property data of CO2-N2-O2-CH4 mixtures with the “Peng-Robinson + residual Helmholtz energy-based” model , 2017 .

[21]  Yu Liu,et al.  Density characteristics of CO2–CH4 binary mixtures at temperatures from (300 to 308.15) K and pressures from (2 to 18) MPa , 2017 .

[22]  P. Chiesa,et al.  Modeling the Thermodynamics of Fluids Treated by CO2 Capture Processes with Peng–Robinson + Residual Helmholtz Energy-Based Mixing Rules , 2017 .

[23]  Xiaoxian Yang,et al.  Vapour-phase (p, ρ, T, x) behaviour and virial coefficients for the (ethane + carbon dioxide) system , 2017, The Journal of Chemical Thermodynamics.

[24]  Amir H. Mohammadi,et al.  Predictive model based on ANFIS for estimation of thermal conductivity of carbon dioxide , 2016 .

[25]  P. Chiesa,et al.  VLE properties of CO2 – Based binary systems containing N2, O2 and Ar: Experimental measurements and modelling results with advanced cubic equations of state , 2016 .

[26]  R. Hellmann Cross Second Virial Coefficients and Dilute Gas Transport Properties of the (CH4 + C3H8) and (CO2 + C3H8) Systems from Accurate Intermolecular Potential Energy Surfaces , 2016 .

[27]  R. Span,et al.  Characterisation of a microwave re-entrant cavity resonator for phase-equilibrium measurements and new dew-point data for a (0.25 argon + 0.75 carbon dioxide) mixture , 2016 .

[28]  B. Tohidi,et al.  Densities and derived thermophysical properties of the 0.9505 CO2 + 0.0495 H2S mixture from 273 K to 353 K and pressures up to 41 MPa , 2016 .

[29]  E. Thorin,et al.  Impacts of thermo-physical properties of gas and liquid phases on design of absorber for CO2 capture using monoethanolamine , 2016 .

[30]  Sigurd Weidemann Løvseth,et al.  Vapor-liquid equilibrium data for the carbon dioxide and oxygen (CO2 + O2) system at the temperatures 218, 233, 253, 273, 288 and 298 K and pressures up to 14 MPa , 2016 .

[31]  Zhe Wang,et al.  Accurate density measurements on a binary mixture (carbon dioxide + methane) at the vicinity of the critical point in the supercritical state by a single-sinker densimeter , 2016 .

[32]  E. Thorin,et al.  Property impacts on Carbon Capture and Storage (CCS) processes: A review , 2016 .

[33]  R. Span,et al.  Vapor-Phase (p, ρ, T, x) Behavior and Virial Coefficients for the Binary Mixture (0.05 Hydrogen + 0.95 Carbon Dioxide) over the Temperature Range from (273.15 to 323.15) K with Pressures up to 6 MPa , 2016 .

[34]  Svend Tollak Munkejord,et al.  CO2 transport: Data and models – A review , 2016 .

[35]  Sigurd Weidemann Løvseth,et al.  Vapor-liquid equilibrium data for the carbon dioxide and nitrogen (CO2+N2) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPa , 2016 .

[36]  R. Marriott,et al.  The Volumetric Properties of Carbonyl Sulfide and Carbon Dioxide Mixtures from T = 322 to 393 K and p = 2.5 to 35 MPa: Application to COS Hydrolysis in Subsurface Injectate Streams , 2016 .

[37]  Ioannis G. Economou,et al.  Self-diffusion coefficients of the binary (H2O + CO2) mixture at high temperatures and pressures , 2016 .

[38]  Roland Span,et al.  EOS–CG: A Helmholtz energy mixture model for humid gases and CCS mixtures , 2016 .

[39]  Zheng Li,et al.  Density measurements on binary mixtures (nitrogen + carbon dioxide and argon + carbon dioxide) at temperatures from (298.15 to 423.15) K with pressures from (11 to 31) MPa using a single-sinker densimeter , 2015 .

[40]  Reza Shams,et al.  An intelligent modeling approach for prediction of thermal conductivity of CO2 , 2015 .

[41]  H. Svendsen,et al.  An excess Gibbs free energy based model to calculate viscosity of multicomponent liquid mixtures , 2015 .

[42]  Zheng Li,et al.  Accurate Density Measurements on Ternary Mixtures (Carbon Dioxide + Nitrogen + Argon) at Temperatures from (323.15 to 423.15) K with Pressures from (3 to 31) MPa using a Single-Sinker Densimeter , 2015 .

[43]  Michael W. George,et al.  Measurement of the vapour–liquid equilibrium of binary and ternary mixtures of CO2, N2 and H2, systems which are of relevance to CCS technology , 2015 .

[44]  Roland Span,et al.  Measurements of the viscosity of carbon dioxide at temperatures from (253.15 to 473.15)K with pressures up to 1.2MPa , 2015 .

[45]  R. Privat,et al.  Addition of the Sulfur Dioxide Group (SO2), the Oxygen Group (O2), and the Nitric Oxide Group (NO) to the E-PPR78 Model , 2015 .

[46]  Kenneth N. Marsh,et al.  Viscosity of {xCO2 + (1 - X)CH4} with x = 0.5174 for temperatures between (229 and 348) K and pressures between (1 and 32) MPa , 2015 .

[47]  Richard S. Graham,et al.  A New Equation of State for CCS Pipeline Transport: Calibration of Mixing Rules for Binary Mixtures of CO2 with N2, O2 and H2 , 2015, 1507.01545.

[48]  J. Trusler,et al.  Phase behavior of (CO2 + H2) and (CO2 + N2) at temperatures between (218.15 and 303.15) K at pressures up to 15 MPa , 2015 .

[49]  Christophe Coquelet,et al.  Thermodynamic Study of binary an ternary systems containing CO2 + impurities in the context of CO2 transportation , 2018 .

[50]  Barbara Bosio,et al.  Comparison of equations-of-state with P-ρ-T experimental data of binary mixtures rich in CO2 under the conditions of pipeline transport , 2014 .

[51]  Chris D. Muzny,et al.  Progress toward new Reference Correlations for the Transport Properties of Carbon Dioxide | NIST , 2014 .

[52]  Athanassios Z Panagiotopoulos,et al.  Atomistic molecular dynamics simulations of CO₂ diffusivity in H₂O for a wide range of temperatures and pressures. , 2014, The journal of physical chemistry. B.

[53]  Mohammad Ahmad,et al.  Effect of impurities in captured CO2 on liquid-vapor equilibrium , 2014 .

[54]  A. Amooey A simple correlation to predict thermal conductivity of supercritical carbon dioxide , 2014 .

[55]  J. Trusler,et al.  Diffusion Coefficients of CO2 and N2 in Water at Temperatures between 298.15 K and 423.15 K at Pressures up to 45 MPa , 2014 .

[56]  Mahmoud Nazeri,et al.  Effect of impurities on thermophysical properties and phase behaviour of a CO2-rich system in CCS , 2013 .

[57]  Javier Fernández,et al.  Influence of methane and carbon monoxide in the volumetric behaviour of the anthropogenic CO2: Experimental data and modelling in the critical region , 2013 .

[58]  I-Ming Chou,et al.  Determination of diffusion coefficients of carbon dioxide in water between 268 and 473 K in a high-pressure capillary optical cell with in situ Raman spectroscopic measurements , 2013 .

[59]  Gioia Falcone,et al.  HPHT viscosities measurements of mixtures of methane/nitrogen and methane/carbon dioxide , 2013 .

[60]  Michael W. George,et al.  Densities of the carbon dioxide + hydrogen, a system of relevance to carbon capture and storage , 2013 .

[61]  Ioannis G. Economou,et al.  Evaluation of Cubic, SAFT, and PC-SAFT Equations of State for the Vapor–Liquid Equilibrium Modeling of CO2 Mixtures with Other Gases , 2013 .

[62]  Gioia Falcone,et al.  Rolling Ball Viscometer Calibration with Gas Over Whole Interest Range of Pressure and Temperature Improves Accuracy of Gas Viscosity Measurement , 2012 .

[63]  W. Wagner,et al.  The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004 , 2012 .

[64]  Maria E. Mondejar,et al.  Accurate (p, ρ, T) data for two new (carbon dioxide + nitrogen) mixtures from (250 to 400) K at pressures up to 20 MPa , 2012 .

[65]  Ehsan Heidaryan,et al.  A novel correlation approach to estimate thermal conductivity of pure carbon dioxide in the supercritical region , 2012 .

[66]  Jean-Stéphane Condoret,et al.  Experimental study of high pressure phase equilibrium of (CO2 + NO2/N2O4) mixtures , 2011 .

[67]  M. Mondejar,et al.  New (p, ρ, T) data for carbon dioxide – Nitrogen mixtures from (250 to 400) K at pressures up to 20 MPa , 2011 .

[68]  Hailong Li,et al.  PVTxy properties of CO2 mixtures relevant for CO2 capture, transport and storage: Review of available experimental data and theoretical models , 2011 .

[69]  Jinyue Yan,et al.  Viscosities, thermal conductivities and diffusion coefficients of CO2 mixtures:Review of experimental data and theoretical models , 2011 .

[70]  Masoud Rahimi,et al.  Viscosity of pure carbon dioxide at supercritical region: Measurement and correlation approach , 2011 .

[71]  Jean-Noël Jaubert,et al.  Relationship between the binary interaction parameters (kij) of the Peng–Robinson and those of the Soave–Redlich–Kwong equations of state: Application to the definition of the PR2SRK model , 2010 .

[72]  A. Bahadori,et al.  Predictive tool for an accurate estimation of carbon dioxide transport properties , 2010 .

[73]  John Lohrenz,et al.  Calculating Viscosities of Reservoir Fluids From Their Compositions , 1964 .

[74]  R. Privat,et al.  Phase equilibrium of CCS mixtures: Equation of state modeling and Monte Carlo simulation , 2017 .

[75]  R. Privat,et al.  E-PPR78: A proper cubic EoS for modelling fluids involved in the design and operation of carbon dioxide capture and storage (CCS) processes , 2017 .

[76]  M. W. George,et al.  The phase equilibrium and density studies of the ternary mixtures of CO2 + Ar + N2 and CO2 + Ar + H2, systems relevance to CCS technology , 2017 .

[77]  Geoffrey C. Maitland,et al.  Viscosity and Density of Aqueous Solutions of Carbon Dioxide at Temperatures from (274 to 449) K and at Pressures up to 100 MPa , 2015 .

[78]  G. Valenti,et al.  Supercritical pressure–density–temperature measurements on CO2–N2, CO2–O2 and CO2–Ar binary mixtures , 2012 .

[79]  Aage Fredenslund,et al.  An improved corresponding states model for the prediction of oil and gas viscosities and thermal conductivities , 1987 .