Problems with pusher centrifuges
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Is there any member of this forum who is involved in work related to pusher centrifuges? I would like to consult regarding the feed particle size and concentration ratio for pusher centrifuges. Thank you all.
Is it piston feeding or screw feeding?
Piston-driven displacement of the concentrated brine after evaporation and crystallization; thank you~~
We do both piston feeding and screw feeding
This post was last edited by li*nji on 2016-12-16 at 16:35. The concentration of the HR piston feeder is above 40%, with a D50 value of over 80–100 microns; the concentration of the LWL spiral filter type is above 30%, with a D50 value of over 120–200 microns, yielding good results
Gap parameter. (The number of cycles may not be adjustable; it could be Zhejiang Light Machinery’s P60.) Particle size/solid-liquid ratio of the material. Whether to use a cyclone, and the yield and moisture content after material separation. Describe the problem in as much detail as possible to facilitate analysis.
Hello, we are Zhejiang Qingji, zhejiangqingji@163.com
It’s indeed a good idea that can broaden the application of piston centrifuges.
Now, the piston has been replaced by sedimentation filtration. . . . . . . Once organic matter is present in the piston, it can clog the filters; sedimentation filtration is used for professional treatment of the salts that come from the evaporator