JohnWeal
Mechanical
- Dec 16, 2012
- 124
I have a pump which transfers grout through a 40mm sch40s stainless steel pipe downhill. The drop in elevation is 9.6m from the pump discharge to the outlet. (there are some horizontal sections also but the trend is mainly downwards as the overall length of the pipe is 12.5m
From the calculations I have done, the velocity or flowrate wants to discharge faster than the pump even given that the slurry is viscous / laminar flow.
The Fluid is a cement grout with a density of 1773 kg/m3 and viscosity of 122.5 cP
My fear is that because it is a grout, no restrictions can be put in the pipeline except for either reducing the pipe diameter or adding more bends.
Any advice appreciated.
Regards
John
From the calculations I have done, the velocity or flowrate wants to discharge faster than the pump even given that the slurry is viscous / laminar flow.
The Fluid is a cement grout with a density of 1773 kg/m3 and viscosity of 122.5 cP
My fear is that because it is a grout, no restrictions can be put in the pipeline except for either reducing the pipe diameter or adding more bends.
Any advice appreciated.
Regards
John