Decompression wave speed in CO2 mixtures: CFD modelling with the GERG-2008 equation of state
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Cheng Lu | Guillaume Michal | Phillip Venton | Xiong Liu | Ajit R Godbole | Xiong Liu | Ajit R. Godbole | Cheng Lu | Guillaume Michal | Alhoush Elshahomi | Phillip Venton | Alhoush Elshahomi | A. Godbole
[1] Haroun Mahgerefteh,et al. An Interpolation Technique for Rapid CFD Simulation of Turbulent Two-Phase Flows , 2007 .
[2] J. F. Kiefner,et al. Ductile fracture arrest in gas pipelines , 1976 .
[3] G. Soave. Equilibrium constants from a modified Redlich-Kwong equation of state , 1972 .
[4] J. R. Chen,et al. Modelling of two-phase blowdown from pipelines—II. A simplified numerical method for multi-component mixtures , 1995 .
[5] Julia Race,et al. Transporting the Next Generation of CO2 for Carbon, Capture and Storage: The Impact of Impurities on Supercritical CO2 Pipelines , 2008 .
[6] Amyn S. Teja,et al. A NEW CUBIC EQUATION OF STATE FOR FLUIDS AND FLUID MIXTURES , 1982 .
[7] 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 .
[8] Randi Moe,et al. The dynamic two-fluid model OLGA; Theory and application , 1991 .
[9] M. McLinden,et al. NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 8.0 , 2007 .
[10] M. Liou,et al. A New Flux Splitting Scheme , 1993 .
[11] Cheng Lu,et al. Investigation of the Effects of Pipe Wall Roughness and Pipe Diameter on the Decompression Wave Speed in Natural Gas Pipelines , 2012 .
[12] H Mahgerefteh,et al. Modelling outflow following rupture in pipeline networks , 2006 .
[13] D. Feakins,et al. The thermodynamics of solutions , 1989 .
[14] Jinyue Yan,et al. Impacts of equations of state (EOS) and impurities on the volume calculation of CO2 mixtures in the applications of CO2 capture and storage (CCS) processes , 2009 .
[15] Meihong Wang,et al. Simulation-based techno-economic evaluation for optimal design of CO 2 transport pipeline network , 2014 .
[16] B. Metz. IPCC special report on carbon dioxide capture and storage , 2005 .
[17] D. Lempe,et al. Density improvement of the SRK equation of state , 1997 .
[18] D. Peng,et al. A New Two-Constant Equation of State , 1976 .
[19] K. Botros,et al. Extension of the semi-empirical correlation for the effects of pipe diameter and internal surface roughness on the decompression wave speed to include High Heating Value Processed Gas mixtures , 2013 .
[20] Hailong Li,et al. Evaluating cubic equations of state for calculation of vapor–liquid equilibrium of CO2 and CO2-mixtures for CO2 capture and storage processes , 2009 .
[21] Xiaoyan Ji,et al. Energy consumption analysis for CO2 separation from gas mixtures , 2014 .
[22] S. F. Brown,et al. CFD modelling of outflow and ductile fracture propagation in pressurised pipelines , 2011 .
[23] 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 .
[24] P. Bishnoi,et al. Calculation of the thermodynamic sound velocity in two-phase multicomponent fluids , 1987 .
[25] Andrew Cosham,et al. GASDECOM: Carbon Dioxide and Other Components , 2010 .
[26] Heqin Xu,et al. Effect of Grade on Ductile Fracture Arrest Criteria for Gas Pipelines , 2006 .
[27] Julian Barnett,et al. The Decompression Behaviour of Carbon Dioxide in the Dense Phase , 2012 .
[28] B. Lu,et al. Simultaneous calculations of VLE and saturated liquid and vapor volumes by means of a 3P1T cubic EOS , 1987 .
[29] K. K. Botros,et al. Measurements of Speed of Sound in Lean and Rich Natural Gas Mixtures at Pressures up to 37 MPa Using a Specialized Rupture Tube , 2010 .
[30] Zhenhao Duan,et al. PVTx properties of the CO2–H2O and CO2–H2O–NaCl systems below 647 K: Assessment of experimental data and thermodynamic models , 2007 .
[31] J. Pain,et al. Gas Dynamics , 2018, Nature.
[32] Haroun Mahgerefteh,et al. A study of the effects of friction, heat transfer, and stream impurities on the decompression behavior in CO2 pipelines , 2012 .
[33] Andre Peneloux,et al. A consistent correction for Redlich-Kwong-Soave volumes , 1982 .
[34] O. Redlich,et al. On the thermodynamics of solutions; an equation of state; fugacities of gaseous solutions. , 1949, Chemical reviews.
[35] Kenneth R. Hall,et al. An algebraic method that includes Gibbs minimization for performing phase equilibrium calculations for any number of components or phases , 2003 .
[36] S. H. Hashemi,et al. Correction factors for safe performance of API X65 pipeline steel , 2009 .
[37] P. Bishnoi,et al. The importance of real‐fluid behavior and nonisentropic effects in modeling decompression characteristics of pipeline fluids for application in ductile fracture propagation analysis , 1988 .
[38] H Mahgerefteh,et al. Modelling the impact of stream impurities on ductile fractures in CO2 pipelines , 2012 .
[39] Thomas J. Ahrens,et al. Equation of State , 1993 .
[40] J. Kiefner,et al. Failure Stress Levels of Flaws in Pressurized Cylinders , 1973 .
[41] Arne Dugstad,et al. Update of DNV recommended practice RP-J202 with focus on CO2 Corrosion with Impurities , 2014 .
[42] P. Bishnoi,et al. The importance of real‐fluid behavior in predicting release rates resulting from high‐pressure sour‐gas pipeline ruptures , 1989 .
[43] Xiong Liu,et al. Source strength and dispersion of CO2 releases from high-pressure pipelines: CFD model using real gas equation of state , 2014 .
[44] J. X. Wen,et al. Predicting the Decompression Characteristics of Carbon Dioxide Using Computational Fluid Dynamics , 2012 .
[46] Haroun Mahgerefteh,et al. Fast numerical simulation for full bore rupture of pressurized pipelines , 1999 .
[47] K. E. Starling,et al. Enthalpy of Mixtures by Modified BWR Equation , 1970 .