vanillabeans12
Chemical
- Mar 10, 2024
- 4
I'm working with a slurry that has solids about 0.75 inches in diameter. The liquid isn't that viscous. This is a new slurry in a process where we handle other kinds of slurries no problem. We were draining the slurry from a batch tank to another tank as usual, and it was pumping fine, but when we look at the receiving end, it looks like all the liquid beat the solids, and the solids dragged behind.
It didn't plug the pipes, but the first thing I thought of was slippage. The pump (positive displacement, not centrifugal) was operating at a rather fast flowrate, so that probably didn't help either. I was thinking of increasing the viscosity of the slurry, as well as increasing the agitation in the batch tank to give better distribution of the particles right before it pumps (some of the solids settle towards the bottom before pumping). Is this a good approach? What else am I missing?
It didn't plug the pipes, but the first thing I thought of was slippage. The pump (positive displacement, not centrifugal) was operating at a rather fast flowrate, so that probably didn't help either. I was thinking of increasing the viscosity of the slurry, as well as increasing the agitation in the batch tank to give better distribution of the particles right before it pumps (some of the solids settle towards the bottom before pumping). Is this a good approach? What else am I missing?