PBF mobile disc vacuum filter
The moving disc vacuum belt filter is a traditional filtration equipment, which uses the filter cloth or filter screen as the medium, so that the slurry is horizontally arranged on the filter medium, and makes full use of the slurry gravity and vacuum suction to achieve solid-liquid separation.
Be applicable to
Materials under a variety of concentration conditions, suitable for thixotropic, washing materials, so it is preferred by many industrial sectors.
PLC control, easy to remote and centralized control.
Serpentine correction is adopted to solve the deviation and creasing of the filter cloth.
The slurry enters from above the equipment. Horizontal settlement, the slurry under the action of gravity solid layer from coarse to fine, to achieve the ideal filtration performance, and then under the action of vacuum to form a filter cake. And no other power is required to discharge the filtrate.
The dissolved material is cleaned from the porous structure of the cake. The horizontal cake is easy to be evenly and completely wetted in the washing area. During the step suction process, the porous structure is improved because the cake is slightly compressed, which makes infiltration washing extremely efficient. Countercurrent washing can be performed to save the amount of washing water.
In addition to vacuum dehydration, other drying systems are available: hot air or steam can be used to achieve the desired drying effect. If necessary, it can also be equipped with compressed air purging device, high temperature, microwave, mechanical extrusion device.
The cake is discharged from the discharge roll by a scraper.
After unloading the cake, the filter cloth goes into the cleaning bucket, the front and back of the filter cloth are washed by high pressure, and the filter cloth is sucked dry if necessary. To improve the service life of the filter cloth and high filtration performance.
|
Filter area M2 |
Filter width MM |
Filter length M |
Weight T |
Overall dimension(LxWxH) M |
| 1.9~8.4 | 625 | 3~13.5 | 2.4~3.8 | 6.13~16.63X2.1X1.67 |
| 3.8~16.9 | 1250 | 3~13.5 | 2.85~4.6 | 6.13~16.63X2.8X1.67 |
| 4.8~21.6 | 1600 | 3~13.5 | 3.1~5.2 | 6.13~16.63X3.2X1.77 |
| 6~27 | 2000 | 3~13.5 | 3.4~5.85 | 6.13~16.63X4.2X1.77 |
| 7.5~33.8 | 2500 | 3~13.5 | 3.8~6.6 | 6.15~16.65X4.15X1.87 |
| 9~40.5 | 3600 | 3~13.5 | 4.2~7.35 | 6.15~16.65x4.65x1.87 |
| Material name | Liquid-solid ratio | Filter cake moisture content% | Production efficiency kg/m2.h | Material name | Liquid-solid ratio | Filter cake moisture content % | Production efficiency kg/m2.h | |||
| Citric acid | 5/1-3/1 | 15 | 25.8 | Caustic soda &CUS | April 1st | 19.6 | 416 | |||
| Zinc oxide | October 1st | 51.2 | 75.9 | ABSResin | 10月1日 | 36-38 | 170-232 | |||
| Manganese oxide acid leaching | 3.1 | 45.06 | 88.46 | Calcium phosphate pulp | 3.5/1 | 21.5 | 345 | |||
| Magnetite | 2.5/1-4/1 | 7.6 | 500-1000 | Soluble phosphate fertilizer | 2/1-5/1 | July 10th | 1000-2000 | |||
| Sulfur concentrate | 4/1-2.5/1 | 11.63 | 360-800 | Sulfuric acid sludge | 1.5/1 | 37-40 | 665-780 | |||
| Copper concentrate | 4/1-2.5/1 | 12 | 400-600 | Aluvanite | 5/1-4/1 | 26.4-29 | 1700 | |||
| All tailings | 9/1-4/1 | 21.4 | 300-500 | Causticized mud | April 1st | 47-51 | 266-613 | |||
| Refined iron ore | 2/1-1.5/1 | August 10th | 2000-3000 | Aluminium sulphate residue silicon | 1.5/1 | 37 | 200 | |||
| Manganese ore | 2月1日 | 15-17 | 800-1000 | Fermentation broth | 1/1-2/1 | 33.1 | 78.5 | |||
| Aluminium hydroxide | April 1st | 15-17 | 350 | Crude zinc oxide | April 1st | 23.5 | 233 | |||
| Fluorspar powder | February 1st | 11 | 800 | Fluorinated lime | 4/1-5/1 | 42-51 | 200-560 | |||
| Causticized mud | April 1st | 47-51 | 266-613 | Ammonium salt | April 1st | 18-20 | 1000-1500 | |||
| Vanadium pentoxide | On March 1st | 33 | 174 | Sodium silicofluoride | On March 1st | 15-20 | 300-500 | |||
| soot | October 1st | 20.7 | 4.9m3 | Wet cement | February 1st | 16-20 | 787 | |||
| Gold concentrate | February 1st | 25-27 | 111 | Coal preparation and cleaning | April 1st | 22.4 | 218 | |||
| Ammonium child tungstate | 2月1日 | 71 | 200 | Finishing coal tail coal | June 1st | 25 | 100 | |||
| Azo dye | 30/1-20/1 | 69 | 100 | Zinc sulfate pulp | The first of May | 45-50 | 312 | |||
| 4Azeolite | 80-100 g/L | ≤43 | 164 | Pseudoboehmite | The first of August | 60 | 30-50 | |||
| Seed agate | 260-600g/L | ≤15 | 125 | Silica slag | 4.5 | ≤35 | 342 | |||
| Aluminium hydroxide seed | 400-800g/L | ≤15 | 2000 | Desulfurized gypsum | January 1st | ＜10 | 800-1000 | |||
| Plant agate seeds | 200-400g/L | ≤20 | 684 | |||||||
