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The incorporation of the effects of CO/sub 2/ solubility in brine into a compositional simulator

Conference ·
OSTI ID:5586285
 [1];  [2]
  1. Oak Ridge Associated Universities Fellow, Univ. of Pittsburgh (US)
  2. USDOE Morgantown Energy Technology Center, WV (USA)

The effects of the dissolution of carbon dioxide into an aqueous phase containing dissolved solids on the displacement of oil by carbon dioxide evaluated by using a one-dimensional compositional simulator. The Henry constant and partial molar volume of carbon dioxide in water at infinite dilution were determined for the CO/sub 2//H/sub 2/O system over the 25{sup 0}C (77{sup 0}F) to 250{sup 0}C (482{sup 0}F) temperature range and the 4.83 MPa (700 psia) to 72.41 MPa (10,500 psia) pressure range. The decreased solubility of CO/sub 2/ in brine is accounted for empirically by a factor correlated to the weight percent of dissolved solids. The effects of dissolved solids on the density and viscosity of the aqueous phase over the 25{sup 0}C (77{sup 0}F) to 100{sup 0}C (212{sup 0}F) temperature range correlated to the amount of dissolved solids. Ultimate oil recoveries in simulations accounting for the solubility of CO/sub 2/ in brine are less than those attained in simulations which did not incorporate solubility of CO/sub 2/ in the aqueous phase.

OSTI ID:
5586285
Report Number(s):
CONF-881143--
Country of Publication:
United States
Language:
English