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A systematic and consistent approach to determine binary interaction coefficients for the Peng-Robinson equation of state

Journal Article · · SPE (Society of Petroleum Engineers) Reservoir Engineering; (USA)
DOI:https://doi.org/10.2118/16941-PA· OSTI ID:5275984
 [1]
  1. Dansk Operatorselskab I/S (DK)
A new technique to determine binary interaction coefficients for a cubic equation of state (EOS) is introduced. The technique is physically consistent and easy to apply when an EOS is tuned to laboratory-measured PVT data. The method's simplicity provides a rational way of evaluating the sensitivity of binary interaction coefficients to fluid composition and temperature. Laboratory-measured expansion data are demonstrated to be crucial for proper determination of binary interaction coefficients for near-critical fluids. The ability of the technique has been demonstrated by matching laboratory-measured constant-composition-expansion curves for six fluid compositions, including black-oil, volatile-oil, rich-gas-condensate, and lean-gas-condensate systems. In addition, the near-critical fluid behavior has been evaluated by matching constant-composition expansion data for a fluid at four temperatures in the near-critical range, two on either side of the critical temperature. The literature reports that the Peng-Robinson EOS (PR-EOS) cannot predict the retrograde phase behavior of the rich-gas-condensate fluids applied in this study. This paper shows that this is because insufficient and/or improper binary interaction coefficients were used in the fluid characterization.
OSTI ID:
5275984
Journal Information:
SPE (Society of Petroleum Engineers) Reservoir Engineering; (USA), Journal Name: SPE (Society of Petroleum Engineers) Reservoir Engineering; (USA) Vol. 4:4; ISSN SREEE; ISSN 0885-9248
Country of Publication:
United States
Language:
English