Noel Y - 2024-08-20

Dear Daniel, I've tried to make an oil characterization trough the Bulk C7+ Tool, upon PVT data... apparently everything was going fair enough with the MW, density, phase equilibria, until I tried to evaluate the pressure drop in a pipe, which gave me a tremendous delta P, so when I took a second look at the properties, I noticed that the liquid viscosity indicated values of 6x10^3 cP at operating conditions (28 °C & 9 barg) and higher than 120x10^3 cP at standard conditions; however, if I referred to the viscosity curves of the pseudos generated with the characterization, I did not check, they were all between 1 to 6 cP at std, as I expected. So, I don't know what the source of the error in said viscosity results could be.

 

Last edit: Noel Y 2024-08-20