Aput
Petroleum
- Feb 17, 2017
- 1
Hello,
I have a fluid that has proven to be shear thinning using a spindle rheometer at ambient pressure, showing an apparent viscosity decrease by a factor of about 3x when running a shear sweep from 5 to 100 1/s at constant temperature.
If I were able to put said fluid in a spindle rheometer under 10,000 psi of mechanical pressure (not using a gas pressure source), could I still expect similar decrease in apparent viscosity with shear, and could I be absolutely certain that the fluid would still be shear thinning?
Translate the above question to viscosity measurement in a tube-style viscometer; could I expect the same apparent viscosity curve that I saw in the spindle-type rheometer? The flow would be comfortably laminar.
I have a fluid that has proven to be shear thinning using a spindle rheometer at ambient pressure, showing an apparent viscosity decrease by a factor of about 3x when running a shear sweep from 5 to 100 1/s at constant temperature.
If I were able to put said fluid in a spindle rheometer under 10,000 psi of mechanical pressure (not using a gas pressure source), could I still expect similar decrease in apparent viscosity with shear, and could I be absolutely certain that the fluid would still be shear thinning?
Translate the above question to viscosity measurement in a tube-style viscometer; could I expect the same apparent viscosity curve that I saw in the spindle-type rheometer? The flow would be comfortably laminar.