SPE Journal
Volume 14, Number 3, September 2009, pp. 441-449

SPE-113492-PA

Compositional Space Parameterization: Multicontact Miscible Displacements and Extension to Multiple Phases

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DOI  More information 10.2118/113492-PA http://dx.doi.org/10.2118/113492-PA

Citation

  • Voskov, D.V. and Tchelepi, H.A. 2009. Compositional Space Parameterization: Multicontact Miscible Displacements and Extension to Multiple Phases. SPE J.  14 (3): 441-449. SPE-113492-PA. doi: 10.2118/113492-PA.

Discipline Categories

  • 6.3.2 Multi-phase Flow
  • 6.3.1 Flow in Porous Media
  • 6.2.2 Fluid Modeling, Equations of State
  • 6.4.2 Gas-Injection Methods

Keywords

  • compositional flow, tie-line parameterization, thermodynamics, reservoir simulation, nonlinear transport

Summary

We generalize the compositional space parameterization (CSP) approach, which was originally developed for immiscible two-phase multicomponent problems, to multicontact miscible displacements. The tie-line based parameterization method improves both the accuracy of the phase-behavior representation as well as the efficiency of equation of state (EOS) computations in compositional flow simulation. For immiscible compositional simulation, compositional space adaptive tabulation (CSAT) can be used to avoid most of the redundant EOS calculations. Because the supercritical region cannot be parameterized using tie-lines, the original CSAT approach is not effective for modeling multicontact miscible gas injection processes. To deal with supercritical compositions, a supercritical state criteria (SSC) algorithm based on adaptive tabulation of the minimal critical pressure (MCP) tie-lines is proposed. For general-purpose simulation of miscible and immiscible compositional displacement processes, we combined the adaptive CSAT strategy in the region of tie-line extensions and the adaptive SSC scheme; we refer to the overall framework as CSAT. Results of several challenging tests of practical interest indicate that the general CSAT strategy is quite robust and that it leads to an order of magnitude gain in computational efficiency. We also describe the extension of the CSP framework for mixtures that form more than two phases.

© 2009. Society of Petroleum Engineers

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History

  • Original manuscript received: 12 February 2008
  • Meeting paper published: 20 April 2008
  • Revised manuscript received: 18 August 2008
  • Manuscript approved: 21 August 2008
  • Published online: 13 August 2009
  • Version of record: 28 September 2009