Hello again all.
Wherever I have got with the rod-mill / rod-milling and sieve-analysis quantifiying that comminution is good enough for now. [I have another test-milled comminute where have the sub-150micron to sieve to +75micron and -75micron, plus the very-very-fines I separated by sedimentation (I stirred the comminute in a trug of water, left it a settling time in the seconds range then ladled-out from the near-surface the water there - which although barely-transluscent, mostly opaque, pours straight through the 75micron sieve) to dry, then weigh and plot the mass-fraction at size distribution graph]. The experiences along this path are the enough for now.
Rod-mill now - updated
I've already used "Stokes' Law" for the "sedimentation" trick. Which gives by removing the very-very-fines
- expecially the fractured silica, which is hazardous, absent from the dried everything else
- leaves gritty/"sandy" particles which sieve readily no "clogging"
If using sedimentation, elutriation, or "just" to classify comminute if I form a circuit in processing minerals, it looks like I need to use hydrocyclone(s). Plastic ones are readily available in the small size range for removing very-fines to the underflow (very few 10's of mm diameter and very few hundreds of mm long).
Pumping?
My guess is
- centrifugal pump (would tolerate the fines)
- 3-phase motor, controlling speed with a VFD (Variable Frequency Drive) [as already used on the rod-mill] to give target pressure into the hydrocylone
What would you really do?
The first intent, by the way, is to recover the water for re-use immediately. Thus, a simplification in specifying the hydrocyclone is maximum solids to the underflow, minumum solids to the overflow; thus no target split on size, for what that's worth.
Thanks in advance.
Rich Smith