Updates and bug fixes in PVTsim from 20.0 to 20.1
September 25th, 2011
- Depth gradient option enhanced to ensure consistent P and Psat at Gas Oil Contact also for high vertical temperature gradients.
- For some properties incorrect derivatives returned from Flash Open Structure.
- Enhanced numerical robustness of asphaltene PT-curve option.
- Improved phase identification in asphaltene PT flash.
- Eclipse Black Oil output format changed to handle viscosities as high as 1,000,000 cP.
- Bug corrected in logic for calculating solubility of salt in H2O-MEG solutions.
- Bug corrected in logic for regression on Peneloux volume correction factors for already characterized fluids.
- C6 density erroneously corrected when match of C7+ liquid densities specified in a characterized regression.
- Inconsistent viscosity results reported by different PVTsim options for near critical fluids.
- Phase derivatives of density and entropy added to Flash Open Structure for PT non-aqueous, PT aqueous, PH and PS specifications.
- Flash Open Structure extended to also give derivatives from a PT aqueous flash when aqueous properties calculated from Water Package.
- Asphaltene Module returned incorrect Cv for single phase fluids.
- Rs vs. depth option in Eclipse Black Oil interface did not work with K-factors/Split-factors.
- Incorrect densities from Water Package for pressures in the (approximate) interval fro 750 atm to 1000 atm and temperatures below approximately 263.15 K.
- Some tie-line compositions displayed as zeros when 3 phases found at MMP.
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