| Characteristics: Feed, filter, rinse, remove residue and regeneration of the filter cloth can be finished sequentially and automatically with high automatization. Wash the materials with multilevel advection or refluence, filter liquid and rinse liquid can be separated. Fast filtration with thin layer can be realized for materials with low filterability and high viscidity. The module design can be consolidated freely with high adaptability. PLC control fits for remote and concentrated control. Snake type deviation correction is adopted to prevent deflection and warp of the filter cloth. | |
| Typical Process Drawing: |
| A.Feeding Device H.Vacuum Pump G.Water-return Pump F.Water-expel Separator E.Transfer Valve D.Cloth Washing Device C.Deviation Correction Device B.Rinsing Device |
Materials Name | Liquidtosolid Ratio | Water Content of Filter % | Production Efficiency Kg/m3/h | Materials Name | Liquidtosolid Ratio | Water Content of Filter% | Production EfficiencyKg/m3/h |
Citric Acid | 5/1-3/1 | 15 | 25.8 | Miscible liquids of sodiumhydroxide and CUS | 4/1 | 19.6 | 416 |
Zinc Oxide | 10/1 | 51.2 | 75.9 | ABS resin | 10/1 | 36-38 | 170-232 |
Mining slurry soaked by Mno reductico acid | 3.1 | 45.06 | 88.46 | Calcium Phosphate Ore Magma | 3.5/1 | 21.5 | 345 |
Ferromagnet | 2.5/1-4/1 | 7.6 | 500-1000 | Soluble Phosphor Fertilizer | 2/1-5/1 | 7-10 | 1000-2000 |
Sulphur mine | 4/1-2.5/1 | 11.63 | 360-800 | Vitriol dirt | 1.5/1 | 37-40 | 665-780 |
Copper mine | 4/1-2.5/1 | 12 | 400-600 | Aluminous rocks | 5/1-4/1 | 26.4-29 | 1700 |
Mine remaining part | 9/1-4/1 | 21.4 | 300-500 | Caustic mud | 4/1 | 47-51 | 266-613 |
Iron-stone | 2/1-1.5/1 | 8-10 | 2000-3000 | Residue silicon of aluminium sulphate | 1.5/1 | 37 | 200 |
Manganite | 2/1 | 15-17 | 800-1000 | Fermentated liquid of gentamicin | 1/1-2/1 | 33.1 | 78.5 |
Aluminium Hydroxide | 4/1 | 15-17 | 350 | Coarse zinc oxide | 4/1 | 23.5 | 233 |
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