Noel Y

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...

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 standard conditions; however, if I referred to the viscosity curves of the pseudos generated with the characterization,...

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 standard conditions; however, if I referred to the viscosity curves of the pseudos generated with the characterization, I did...