Solution of the Span-Wagner equation of state using a density-energy state function for fluid-dynamic simulation of carbon dioxide

Industrial and Engineering Chemistry Research

Volumn 51, Issue 2, 2012, Pages 1006-1014

  Giljarhus, Knut Erik Teigen ^a   Munkejord, Svend Tollak ^a   Skaugen, Geir ^a  

^a SINTEF ENERGY RESEARCH   (Norway)

Author keywords

[No Author keywords available]

Indexed keywords

CARBON CAPTURE AND STORAGE; CARBON EMISSIONS; DEPRESSURIZATIONS; EFFICIENT SIMULATION; EQUATION OF STATE; EQUATION SYSTEMS; INTERNAL ENERGIES; MASS AND ENERGY BALANCE; SATURATION LINE; STATE FUNCTIONS;

CARBON CAPTURE; CARBON DIOXIDE; COMPUTER SIMULATION;

TRANSPORT PROPERTIES;

EID: 84860110948     PISSN: 08885885     EISSN: 15205045     Source Type: Journal    
DOI: 10.1021/ie201748a     Document Type: Conference Paper

References (32)

1. 2 in Pipelines, Newcastle, U.K., 2010.
2. 2 pipeline integrity: A new evaluation methodology. Energy Procedia 2011, 4, 3000-3007.
3. 2 Emission Quotas Principles and Practice. In OECD Economics Department Working Papers; Organisation for Economic Co-operation and Development: Paris, 1995; No. 153.
4. Michelsen, M. L. State function based flash specifications. Fluid Phase Equilib. 1999, 158-160, 617-626.
5. Gani, R.; Perregaard, J.; Johansen, H. Simulation strategies for design and analysis of complex chemical processes. Chem. Eng. Res. Des. 1990, 68, 407-417.
6. Flatby, P.; Lundström, P.; Skogestad, S. Rigorous dynamic simulation of distillation columns based on UV-flash. Presented at IFAC Symposium ADCHEM'94, Kyoto, Japan, 1994.
7. Eckert, E.; Kubícek, M. Modelling of dynamics for multiple liquid-vapour equilibrium stage. Chem. Eng. Sci. 1994, 49, 1783-1788.
8. Müller, D.; Marquardt, W. Dynamic multiple-phase flash simulation: Global stability analysis versus quick phase determination. Comput. Chem. Eng. 1997, 21, S817-S822.
9. Saha, S.; Carroll, J. J. The isoenergetic-isochoric flash. Fluid Phase Equilib. 1997, 138, 23-41.
10. Gonçalves, F.; Castier, M.; Araújo, O. Dynamic simulation of flash drums using rigorous physical property calculations. Braz. J. Chem. Eng. 2007, 24, 277-286.
11. Castier, M. Solution of the isochoric-isoenergetic flash problem by direct entropy maximization. Fluid Phase Equilib. 2009, 276, 7-17.
12. Castier, M. Dynamic simulation of fluids in vessels via entropy maximization. J. Ind. Eng. Chem. 2010, 16, 122-129.
13. Arendsen, A. R. J.; Versteeg, G. F. Dynamic Thermodynamics with Internal Energy, Volume, and Amount of Moles as States: Application to Liquefied Gas Tank. Ind. Eng. Chem. Res. 2009, 48, 3167-3176.
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. Linstrom, P., Mallard, W., Eds. NIST Chemistry WebBook; National Institute of Standards and Technology: Gaithersburg MD, 2011 (available via the Internet at http://webbook.nist.gov, accessed February 16, 2011).
16. Huang, F.; Li, M.; Lee, L. L.; Starling, K. E.; Chung, F. T. H. An accurate equation of state for carbon dioxide. J. Chem. Eng. Jpn. 1975, 18, 490-496.
17. Kim, Y. Equation of state for carbon dioxide. J. Mech. Sci. Technol. 2007, 21, 799-803.
18. Menikoff, R.; Plohr, B. J. The Riemann problem for fluid flow of real materials. Rev. Mod. Phys. 1989, 61, 75-130.
19. Menikoff, R. Shock Wave Science and Technology Reference Library, Vol. 2: Solids; Springer-Verlag: Berlin, 2007; pp 143-188.
20. Peng, D.; Robinson, D. B. A New Two-Constant Equation of State. Ind. Eng. Chem. Fundam. 1976, 15, 59-64.
21. Span, R.; Lemmon, E. W.; Jacobsen, R. T.; Wagner, W.; Yokozeki, A. A Reference Equation of State for the Thermodynamic Properties of Nitrogen for Temperatures from 63.151 to 1000 K and Pressures to 2200 MPa. J. Phys. Chem. Ref. Data 2000, 29, 1361-1433.
22. Michelsen, M. L.; Mollerup, J. Thermodynamic Models: Fundamentals and Computational Aspects; Tie-Line Publications: Holte, Denmark, 2007.
23. Haines, E. Point in polygon strategies. In Graphics Gems IV; Academic Press: Boston, 1994.
24. Toro, E. F. MUSTA: A multi-stage numerical flux. Appl. Numer. Math. 2006, 56, 1464-1479.
25. Titarev, V. A.; Toro, E. F. MUSTA schemes for multi-dimensional hyperbolic systems: analysis and improvements. Int. J. Numer. Methods Fluids 2005, 49, 117-147.
26. Munkejord, S. T.; Evje, S.; Flåtten, T. The multi-stage centredscheme approach applied to a drift-flux two-phase flow model. Int. J. Numer. Methods Fluids 2006, 52, 679-705.
27. Munkejord, S. T.; Jakobsen, J. P.; Austegard, A.; Mølnvik, M. J. Thermo- and fluid-dynamical modelling of two-phase multi-component carbon dioxide mixtures. Int. J. Greenhouse Gas Control 2010, 4, 589-596.
28. Flåtten, T.; Lund, H. Relaxation two-phase flow models and the subcharacteristic condition. Math. Models Methods Appl. Sci. 2011, 21, 1-29.
29. Lemmon, E. W.; Huber, M. L.; McLinden, M. O. NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 9.0; National Institute of Standards and Technology, Standard Reference Data Program: Gaithersburg, MD, 2010.
30. Petzold, L. Description of DASSL: A differential/algebraic system solver. Technical Report, No. SAND-82-8637, Sandia National Laboratories, Albuquerque, NM, 1982.
31. 2 sequestration. Energy Convers. Manage. 2006, 47, 702-715.
32. Lund, H.; Flåtten, T.; Munkejord, S. T. Depressurization of carbon dioxide in pipelines-Models and methods. Energy Procedia 2011, 4, 2984-2991.