PVTx Modeling of CO2 Pipeline at Depressurization Conditions Using SPUNG Equation of State (EoS) with a Comparison to SRK

Abstract The proper modeling of CO 2 depressurization is very important for the design for safety of a pipeline. One key element of the modeling process is the thermodynamics and transport properties modeling. In this work, an analysis of the error in thermodynamics for modeling CO 2 at depressurization conditions was conducted. For the study presented here, the sophisticated equation of state (EoS) SPUNG was used. The results were compared to an EoS of a different level of complexity and, consequently, accuracy. This EoS is the cubic equation Soave–Redlich–Kwong (SRK) with van der Waal's mixing rules. The results show the significance of the thermodynamics modeling at a set of pressures, temperatures and compositions PVTx over time steps complying with two sets of experimental data.

[1]  George Jackson,et al.  New reference equation of state for associating liquids , 1990 .

[2]  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 .

[3]  G. Soave Equilibrium constants from a modified Redlich-Kwong equation of state , 1972 .

[4]  Sigmund Clausen,et al.  Depressurization of a 50 km long 24 inches CO2 pipeline , 2012 .

[5]  M. Huron,et al.  New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures☆ , 1979 .

[6]  Hailong Li,et al.  Evaluation of SPUNG* and Other Equations of State for Use in Carbon Capture and Storage Modelling , 2012 .

[7]  Dimitrios P. Tassios,et al.  An Equation of State for Associating Fluids , 1996 .

[8]  J. Ely,et al.  Thermophysical Properties of Fluids. II. Methane, Ethane, Propane, Isobutane, and Normal Butane , 1987 .

[9]  M. McLinden,et al.  NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 8.0 , 2007 .

[10]  M. Michelsen,et al.  Modeling phase equilibria for acid gas mixtures using the CPA equation of state. Part II: Binary mix , 2011 .

[11]  D. Peng,et al.  A New Two-Constant Equation of State , 1976 .

[12]  Ivar S. Ertesvåg,et al.  Modelling CO2 - water mixture thermodynamics using various equations of state (EoSs) with emphasis on the potential of the SPUNG EoS , 2014 .

[13]  Gelein de Koeijer,et al.  Experiments and modeling of two-phase transient flow during CO2 pipeline depressurization , 2009 .

[14]  Ivar S. Ertesvåg,et al.  Preliminary Evaluation of the SPUNG Equation of State for Modelling the Thermodynamic Properties of CO2-Water Mixtures , 2012 .

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

[16]  Ivar S. Ertesvåg,et al.  Modelling CO2-water thermodynamics using SPUNG equation of state (EOS) concept with various reference fluids , 2014 .

[17]  Jørgen Mollerup,et al.  Thermodynamic properties from corresponding states theory , 1980 .

[18]  Ioannis G. Economou,et al.  Modeling the phase equilibria of a H2O–CO2 mixture with PC-SAFT and tPC-PSAFT equations of state , 2012 .