corneliusd
Chemical
- Jun 19, 2016
- 9
Hello all,
Another question regarding Non-Newtonian fluids:
Is anyone aware of the appropriate approach for sizing restriction orifices when the fluid is Non-Newtonian? Initially I am using the same equations as per incompressible fluids, and the only modification so far is that I am estimated the Cd with the corrected Reynolds number (power law, Bignham plastic or Herschel-Bulkley Reynolds).
As I mentioned in a previous post, my goal is to complete a hydraulic model of NN fluids (a simple one) just for testing purposes. I believe I am close to achieving it and at this point, I have equations for frictional pressure drop, pipe fittings and control valves. I hope that I can get some help/validation with the restriction orifices before finally looking at the pumps.
Best!
Another question regarding Non-Newtonian fluids:
Is anyone aware of the appropriate approach for sizing restriction orifices when the fluid is Non-Newtonian? Initially I am using the same equations as per incompressible fluids, and the only modification so far is that I am estimated the Cd with the corrected Reynolds number (power law, Bignham plastic or Herschel-Bulkley Reynolds).
As I mentioned in a previous post, my goal is to complete a hydraulic model of NN fluids (a simple one) just for testing purposes. I believe I am close to achieving it and at this point, I have equations for frictional pressure drop, pipe fittings and control valves. I hope that I can get some help/validation with the restriction orifices before finally looking at the pumps.
Best!