Influence of methane and carbon monoxide in the volumetric behaviour of the anthropogenic CO2: Experimental data and modelling in the critical region
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Javier Fernández | Clara Rivas | Manuela Artal | Inmaculada Velasco | I. Velasco | Sofía T. Blanco | Javier Fernández | M. Artal | C. Rivas | Javier Fernández
[1] B. Sage,et al. Phase Equilibrium in Hydrocarbon Systems.Methane–Carbon Dioxide System in the Gaseous Region , 1944 .
[2] Manuela Artal,et al. Experimental setup to measure critical properties of pure and binary mixtures and their densities at different pressures and temperatures: Determination of the precision and uncertainty in the results , 2008 .
[3] Benjamin C.-Y. Lu,et al. Simultaneous determination of vapor-liquid equilibrium and molar volumes for coexisting phases up to the critical temperature with a static method , 1993 .
[4] M. W. George,et al. How does the critical point change during a chemical reaction in supercritical fluids? A study of the hydroformylation of propene in supercritical CO(2). , 2001, Journal of the American Chemical Society.
[5] A. Ben-Naim. Inversion of the Kirkwood–Buff theory of solutions: Application to the water–ethanol system , 1977 .
[6] Andrea Cipollina,et al. Experimental P−T−ρ Measurements of Supercritical Mixtures of Carbon Dioxide, Carbon Monoxide, and Hydrogen and Semiquantitative Estimation of Their Solvent Power Using the Solubility Parameter Concept , 2007 .
[7] Javier Fernández,et al. Influence of methane in CO2 transport and storage for CCS technology. , 2012, Environmental science & technology.
[8] Ioannis Skarmoutsos,et al. Local intermolecular structure and dynamics in binary supercritical solutions. A molecular dynamics simulation study of methane in carbon dioxide , 2006 .
[9] Jinyue Yan,et al. Viscosities, thermal conductivities and diffusion coefficients of CO2 mixtures:Review of experimental data and theoretical models , 2011 .
[10] Gabriele Sadowski,et al. Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain Molecules , 2001 .
[11] I. Velasco,et al. Experimental determination of the critical loci for {n-C6H14 or CO2 + alkan-1-ol} mixtures. Evaluation of their critical and subcritical behavior using PC-SAFT EoS , 2012 .
[12] A. Teja,et al. Krichevskii Parameters and the Solubility of Heavy n-Alkanes in Supercritical Carbon Dioxide , 2000 .
[13] Tzimas Evangelos,et al. Technical and Economic Characteristics of a CO2 Transmission Pipeline Infrastructure , 2011 .
[14] P. Parris. MOLECULAR SIMULATION STUDIES IN THE SUPERCRITICAL REGION , 2010 .
[15] D. Viswanath,et al. Compression factors and second virial coefficients of H2, CH4, {xCO2 + (1 − x)H2}, and {xCO2 + (1 − x)CH4} , 1990 .
[16] André Faaij,et al. A state-of-the-art review of techno-economic models predicting the costs of CO2 pipeline transport , 2013 .
[17] M. McLinden,et al. NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 8.0 , 2007 .
[18] J. Saldo,et al. Effect of high carbon dioxide atmosphere packaging and soluble gas stabilization pre-treatment on the shelf-life and quality of chicken drumsticks. , 2013, Meat science.
[19] Zhimin Liu,et al. Study on intermolecular interactions in supercritical fluids by partial molar volume and isothermal compressibility , 2002 .
[20] F. Baglin,et al. Interaction induced Raman light scattering as a probe of the local density structure of binary supercritical solutions , 2000 .
[21] Julia Race,et al. Transporting the Next Generation of CO2 for Carbon, Capture and Storage: The Impact of Impurities on Supercritical CO2 Pipelines , 2008 .
[22] Mark R. Wilkins,et al. Carbon dioxide conversion to fuels and chemicals using a hybrid green process , 2013 .
[23] Joachim Gross,et al. Application of the Perturbed-Chain SAFT Equation of State to Associating Systems , 2002 .
[24] D. Viswanath,et al. Compression factors and second virial coefficients of CO2, CO, and {xCO+ (1 − x)CO2}☆ , 1987 .
[25] Michael W. George,et al. Densities of the carbon dioxide + hydrogen, a system of relevance to carbon capture and storage , 2013 .
[26] E. A. Brignole,et al. Rescaling of three-parameter equations of state: PC-SAFT and SPHCT , 2005 .
[27] J. Magee,et al. Isochoric (p, v, T) measurements on CO2 and (0.98 CO2+0.02 CH4) from 225 to 400 K and pressures to 35 MPa , 1988 .
[28] J. Trusler,et al. 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)] , 2012 .
[29] I. Velasco,et al. Accurate values of some thermodynamic properties for carbon dioxide, ethane, propane, and some binary mixtures. , 2011, The journal of physical chemistry. B.
[30] Maria E. Mondejar,et al. Experimental Determination of (p, ρ, T) Data for Three Mixtures of Carbon Dioxide with Methane for the Thermodynamic Characterization of Nonconventional Energy Gases , 2012 .
[31] B. Sage,et al. Phase Equilibria in Hydrocarbon Systems , 1936 .
[32] J. C. Seitz,et al. Volumetric properties for {(1 −x)CO2+xCH4}, {(1 −x)CO2+xN2}, and {(1 −x)CH4+xN2} at the pressures (9.94, 19.94, 29.94, 39.94, 59.93, 79.93, and 99.93) MPa and temperatures (323.15, 373.15, 473.15, and 573.15) K , 1996 .
[33] Huy T. Vo,et al. Comparison of disinfection effect of pressurized gases of CO2, N2O, and N2 on Escherichia coli. , 2013, Water research.
[34] D. Peng,et al. A New Two-Constant Equation of State , 1976 .
[35] P. Cummings,et al. Comment on ‘Near critical phase behaviour of dilute mixtures’ , 1995 .
[36] K. Gutkowski,et al. Determination of the Krichevskii function in near-critical dilute solutions of I2(s) and CHI3(s) , 1998 .
[37] Donald L. Katz,et al. Phase Equilibria in the Carbon Dioxide–Methane System , 1954 .
[38] S. Klein,et al. An improved extended corresponding states method for estimation of viscosity of pure refrigerants and mixtures , 1997 .
[39] James G. Blencoe,et al. Volumetric properties for {(1 –x)CO2+xCH4},{(1 −x)CO2+xN2}, and {(1 −x)CH4+xN2} at the preessures (19.94, 29.94, 39.94, 59.93, 79.93, and 99.93) MPa and the temperature 673.15 K , 1996 .
[40] J. Wheeler. Behavior of a Solute Near the Critical Point of an Almost Pure Solvent , 1972, Berichte der Bunsengesellschaft für physikalische Chemie.
[41] Wan Ramli Wan Daud,et al. Nano-structured carbon as electrode material in microbial fuel cells: A comprehensive review , 2013 .
[42] Dominique Richon,et al. An enhanced method to calibrate vibrating tube densimeters , 2001 .
[43] W. Wagner,et al. A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple‐Point Temperature to 1100 K at Pressures up to 800 MPa , 1996 .
[44] Jennifer Wilcox,et al. Molecular simulation studies of CO2 adsorption by carbon model compounds for carbon capture and sequestration applications. , 2013, Environmental science & technology.
[45] J. Trusler,et al. Equation of State for Solid Phase I of Carbon Dioxide Valid for Temperatures up to 800 K and Pressures up to 12 GPa , 2011 .
[46] G. V. Stepanov,et al. The critical properties of binary mixtures containing carbon dioxide: Krichevskii parameter and related thermodynamic properties , 2007 .
[47] R. M. Dicharry,et al. Compressibility Factors for CO2-Methane Mixtures , 1977 .
[48] Kris Piessens,et al. Pipeline design for a least-cost router application for CO2 transport in the CO2 sequestration cycle , 2008 .
[49] Kenneth N. Marsh,et al. Densities of Carbon Dioxide + Methane Mixtures from 225 K to 350 K at Pressures up to 35 MPa , 1997 .
[50] 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 .
[51] B. E. Gammon,et al. Experimental cross virial coefficients for binary mixtures of carbon dioxide with nitrogen, methane and ethane at 300 and 320 K , 1989 .
[52] J. Kirkwood,et al. The Statistical Mechanical Theory of Solutions. I , 1951 .
[53] Johanna M. H. Levelt Sengers,et al. Critical Behavior of Fluids: Concepts and Applications , 1994 .
[54] H. Beer. Compressibility factors for the argon‐carbon dioxide system , 1969 .
[55] Yasuhiko Arai,et al. THE EXPERIMENTAL DETERMINATION OF THE P-V-T-X RELATIONS FOR THE CARBON DIOXIDE-NITROGEN AND THE CARBON DIOXIDE-METHANE SYSTEMS , 1971 .
[56] P. Debenedetti,et al. Attractive, weakly attractive, and repulsive near‐critical systems , 1989 .
[57] W. Wagner,et al. The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004 , 2012 .
[58] Morten Hammer,et al. Equilibrium and transport properties of CO2 + N2O and CO2 + NO mixtures: Molecular simulation and equation of state modelling study , 2012 .