Dew-point measurements for water in compressed carbon dioxide

AIChE Journal

Volumn 61, Issue 9, 2015, Pages 2913-2925

  Meyer, Christopher W ^a   Harvey, Allan H ^a  

^a NATIONAL INSTITUTE OF STANDARDS AND TECHNOLOGY   (United States)

Author keywords

Carbon dioxide; Dew point; Phase equilibrium; Thermodynamics classical; Virial coefficients; Water

Indexed keywords

CORROSION; PHASE EQUILIBRIA; THERMODYNAMICS; UNCERTAINTY ANALYSIS; WATER;

COVERAGE FACTORS; DEW POINT MEASUREMENTS; DEW POINTS; FLOW APPARATUS; SECOND VIRIAL COEFFICIENTS; VIRIAL COEFFICIENT; WATER DEW POINT; WATER MOLE FRACTION;

CARBON DIOXIDE;

EID: 84938635764     PISSN: 00011541     EISSN: 15475905     Source Type: Journal    
DOI: 10.1002/aic.14818     Document Type: Article

References (32)

1. Haszeldine RS. Carbon capture and storage: how green can black be? Science. 2009;325:1647-1652.
2. Dennis RA, Harp R. Overview of the U.S. Department of Energy's Office of Fossil Energy Advanced Turbine Program for coal based power systems with carbon capture. Proceedings of ASME Turbo Expo 2007, Vol. 2. New York: ASME Press, 2007:1093-1104.
3. 2 capture technology - the U.S. Department of Energy's Carbon Sequestration Program. Int J Greenhouse Gas Control. 2008;2:9-20.
4. Wagner W, Pruss A. International equations for the saturation properties of ordinary water substance. Revised according to the International Temperature Scale of 1990. J Phys Chem Ref Data. 1993;22:783-787.
5. Hyland RW, Wexler A. Formulations for the thermodynamic properties of dry air from 173.15 K, and of saturated moist air from 173.15 K to 372.15 K, at pressures to 5 MPa. ASHRAE Trans. 1983;89-IIa:520-535.
6. 2 dimer. J Chem Phys. 2011;134:134309.
7. Coan CR, King AD Jr. Solubility of water in compressed carbon dioxide, nitrous oxide, and ethane. Evidence for hydration of carbon dioxide and nitrous oxide in the gas phase. J Am Chem Soc. 1971;93:1857-1862.
8. Gillespie PC, Wilson GM. Vapor-liquid and liquid-liquid equilibria: water-methane, water-carbon dioxide, water-hydrogen sulfide, water-npentane, water-methane-npentane. GPA Technical Report RR-48. Tulsa, OK: Gas Processors Association, 1982.
9. Bamberger A, Sieder G, Maurer G. High-pressure (vapor+liquid) equilibrium in binary mixtures of (carbon dioxide+water or acetic acid) at temperatures from 313 to 353 K. J Supercrit Fluids. 2000;17:97-110.
10. Valtz A, Chapoy A, Coquelet C, Paricaud P, Richon D. Vapour-liquid equilibria in the carbon dioxide-water system, measurement and modelling from 278.2 to 318.2 K. Fluid Phase Equilib. 2004;226:333-344.
11. Koglbauer G, Wendland M. Water vapor concentration enhancement in compressed humid nitrogen, argon, and carbon dioxide measured by Fourier transform infrared spectroscopy. J Chem Eng Data. 2008;53:77-82.
12. Hou S-X, Maitland GC, Trusler JPM. Measurement and modeling of the phase behavior of the (carbon dioxide+water) mixture at temperatures from 298.15 K to 448.15 K. J Supercrit Fluids. 2013;73:87-96.
13. Harvey AH, Lemmon EW. Correlation for the second virial coefficient of water. J Phys Chem Ref Data. 2004;33:369-376.
14. Span R, Wagner W. 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. J Phys Chem Ref Data. 1996;25:1509-1596.
15. Wagner W, Pruß A. The IAPWS formulation 1995 for the thermodynamic properties of ordinary water substance for general and scientific use. J Phys Chem Ref Data. 2002;31:387-534.
16. Meyer CW, Hodges JT, Hyland RW, Scace GE, Valencia-Rodriguez J, Whetstone JR. The second-generation NIST standard hygrometer. Metrologia. 2010;47:192-207.
17. Meyer CW, Hodges JT, Huang PH, Miller WW, Ripple DC, Scace GE. Calibration of Hygrometers with the Hybrid Humidity Generator. NIST Special Publication 250-83. Gaithersburg, MD: National Institute of Standards and Technology, 2008.
18. Hyland RW, Wexler A. The enhancement of water vapor in carbon dioxide-free air at 30, 40, and 50 °C. J Res Natl Bur Stand. 1973;77A:115-131.
19. ISO. Guide to the Expression of Uncertainty in Measurement. Geneva: International Organization for Standardization, 1993.
20. 2 in hydrate forming conditions. Fluid Phase Equilib. 2000;175:75-89.
21. Prausnitz JM, Lichtenthaler RN, Gomes de Azevedo E. Molecular Thermodynamics of Fluid-Phase Equilibria, 3rd ed. Upper Saddle River, NJ: Prentice Hall, 1999.
22. Lemmon EW, Huber ML, McLinden MO. REFPROP: Reference Fluid Thermodynamic and Transport Properties, NIST Standard Reference Database 23, Version 9.1. Gaithersburg, MD: National Institute of Standards and Technology, 2013.
23. Harvey AH, Kaplan SG, Burnett JH. Effect of dissolved air on the density and refractive index of water. Int J Thermophys. 2005;26:1495-1514.
24. Carroll JJ, Slupsky JD, Mather AE. The solubility of carbon dioxide in water at low pressure. J Phys Chem Ref Data. 1991;20:1201-1209.
25. Yang S, Schultz AJ, Kofke DA, Harvey AH. Interpreting gas-saturation vapor-pressure measurements using virial coefficients derived from molecular models. J Chem Eng Data. 2014;59:3183-3192.
26. Hyland RW, Mason EA. Third virial coefficient for air-water vapor mixtures. J Res Natl Bur Stand A. 1967;71A:219-224.
27. Tee LS, Gotoh S, Stewart WE. Molecular parameters for normal fluids: the Lennard-Jones 12-6 potential. Ind Eng Chem Fundam. 1966;5:356-363.
28. 12 for the gas mixture (carbon dioxide+water) from 300 to 1000 K. J Chem Thermodyn. 1981;13:203-211.
29. Patel MR, Holste JC, Hall KR, Eubank PT. Thermophysical properties of gaseous carbon dioxide - water mixtures. Fluid Phase Equilib. 1987;36:279-299.
30. Hellmann R. Ab initio potential energy surface for the carbon dioxide molecule pair and thermophysical properties of dilute carbon dioxide gas. Chem Phys Lett. 2014;613:133-138.
31. Singh JK, Kofke DA. Mayer sampling: calculation of cluster integrals using free-energy perturbation methods. Phys Rev Lett. 2004;92:220601.
32. 2 capture, transport and storage: Review of available experimental data and theoretical models. Appl Energy. 2011;88:3567-3579.