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Decompression wave speed in CO2 mixtures: CFD modelling with the GERG-2008 equation of state

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  • Elshahomi, Alhoush
  • Lu, Cheng
  • Michal, Guillaume
  • Liu, Xiong
  • Godbole, Ajit
  • Venton, Philip

Abstract

The development of CO2 pipelines for Carbon Capture and Storage (CCS) raises new questions regarding the control of ductile fracture propagation and fracture arrest toughness criteria. The decompression behaviour in the fluid must be determined accurately in order to estimate the proper pipe toughness. However, anthropogenic CO2 may contain impurities that can modify the fluid decompression characteristics quite significantly. To determine the decompression wave speed in CO2 mixtures, the thermodynamic properties of these mixtures must be determined by using an accurate equation of state. In this paper we present a new decompression model developed using the Computational Fluid Dynamics (CFD) package ANSYS Fluent. The GERG-2008 Equation of State (EOS) was implemented into this model through User Defined Functions (UDF) to predict the thermodynamic properties of CO2 mixtures. The model predictions were in good agreement with the experimental data of two ‘shock tube’ tests. A range of representative CO2 mixtures was examined in terms of the changes in fluid properties from the initial conditions, with time and distance, immediately after a sudden pipeline opening at one end. Phase changes that may occur within the fluid due to condensation of ‘impurities’ in the fluid were also investigated. Simulations were also conducted to examine how the initial temperature and impurities would affect the decompression wave speed.

Suggested Citation

  • Elshahomi, Alhoush & Lu, Cheng & Michal, Guillaume & Liu, Xiong & Godbole, Ajit & Venton, Philip, 2015. "Decompression wave speed in CO2 mixtures: CFD modelling with the GERG-2008 equation of state," Applied Energy, Elsevier, vol. 140(C), pages 20-32.
  • Handle: RePEc:eee:appene:v:140:y:2015:i:c:p:20-32
    DOI: 10.1016/j.apenergy.2014.11.054
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    References listed on IDEAS

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    1. Luo, Xiaobo & Wang, Meihong & Oko, Eni & Okezue, Chima, 2014. "Simulation-based techno-economic evaluation for optimal design of CO2 transport pipeline network," Applied Energy, Elsevier, vol. 132(C), pages 610-620.
    2. Li, Hailong & Jakobsen, Jana P. & Wilhelmsen, Øivind & Yan, Jinyue, 2011. "PVTxy properties of CO2 mixtures relevant for CO2 capture, transport and storage: Review of available experimental data and theoretical models," Applied Energy, Elsevier, vol. 88(11), pages 3567-3579.
    3. Li, H. & Yan, J., 2009. "Evaluating cubic equations of state for calculation of vapor-liquid equilibrium of CO2 and CO2-mixtures for CO2 capture and storage processes," Applied Energy, Elsevier, vol. 86(6), pages 826-836, June.
    4. Li, H. & Yan, J., 2009. "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," Applied Energy, Elsevier, vol. 86(12), pages 2760-2770, December.
    5. Zhang, Yingying & Ji, Xiaoyan & Lu, Xiaohua, 2014. "Energy consumption analysis for CO2 separation from gas mixtures," Applied Energy, Elsevier, vol. 130(C), pages 237-243.
    6. Liu, Xiong & Godbole, Ajit & Lu, Cheng & Michal, Guillaume & Venton, Philip, 2014. "Source strength and dispersion of CO2 releases from high-pressure pipelines: CFD model using real gas equation of state," Applied Energy, Elsevier, vol. 126(C), pages 56-68.
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    Cited by:

    1. Guo, Xiaolu & Yan, Xingqing & Yu, Jianliang & Zhang, Yongchun & Chen, Shaoyun & Mahgerefteh, Haroun & Martynov, Sergey & Collard, Alexander & Proust, Christophe, 2016. "Pressure response and phase transition in supercritical CO2 releases from a large-scale pipeline," Applied Energy, Elsevier, vol. 178(C), pages 189-197.
    2. Munkejord, Svend Tollak & Hammer, Morten & Løvseth, Sigurd W., 2016. "CO2 transport: Data and models – A review," Applied Energy, Elsevier, vol. 169(C), pages 499-523.
    3. Bin Liu & Xiong Liu & Cheng Lu & Ajit Godbole & Guillaume Michal & Anh Kiet Tieu, 2017. "Multi‐phase decompression modeling of CO 2 pipelines," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 7(4), pages 665-679, August.
    4. Dall’Acqua, D. & Terenzi, A. & Leporini, M. & D’Alessandro, V. & Giacchetta, G. & Marchetti, B., 2017. "A new tool for modelling the decompression behaviour of CO2 with impurities using the Peng-Robinson equation of state," Applied Energy, Elsevier, vol. 206(C), pages 1432-1445.
    5. Liu, Bin & Liu, Xiong & Lu, Cheng & Godbole, Ajit & Michal, Guillaume & Tieu, Anh Kiet, 2018. "A CFD decompression model for CO2 mixture and the influence of non-equilibrium phase transition," Applied Energy, Elsevier, vol. 227(C), pages 516-524.

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