China Uktrafine Milling System Fluidized Bed Opposed Jet Mill, Find details about China Air Jet Mill Fluidized Bed, Fluidized Bed Opposed Jet Mill from Uktrafine Milling System Fluidized Bed Opposed Jet Mill
Uktrafine Milling System Fluidized Bed Opposed Jet Mill
Features and Advantages:
1. | Available particle size D50:1-25μm |
2. | The jet mill is suitable for dry grinding of various materials with Moh's hardness below 9, especially for the materials with high hardness, high purity and high added value |
3. | The grinding process is completed by the collision of the materials themselves., Fully self-grinding, So The device is durable and the purity of products is high in contrast |
4. | PLC control system, easy operation |
5. | Can be used in series with multi-stage classifiers to produce products with multiple sizes at one time |
6. | Optional explosion-proof design, can also be upgraded to nitrogen circulation system to meet the ultra-fine grinding processing requirements of flammable and explosive oxide material. |
Technical Parameters:
Parameters/ specifications | MQL03 | MQL06 | MQL10 | MQL20 | MQL40 | MQL60 | MQL80 | MQL120 |
Feed Size (mm) | <5 | <5 | <5 | <5 | <5 | <5 | <5 | <5 |
Product Size (d97:um) | 8~150 | 8~150 | 8~150 | 8~150 | 10~150 | 10~150 | 10~150 | 10~150 |
Production Capacity (kg/h) | 5~100 | 10~200 | 20~400 | 50~800 | 150~1500 | 300~2000 | 400~6000 | 600~10000 |
Air consumption (m3/min) | 3 | 6 | 10 | 20 | 40 | 60 | 80 | 120 |
Air Pressure (Mpa) | 0.7~0.85 | 0.7~0.85 | 0.7~0.85 | 0.7~0.85 | 0.7~0.85 | 0.7~0.85 | 0.7~0.85 | 0.7~0.85 |
Installed Power (kw) | 26~37 | 46~68 | 68~106 | 145~184 | 276~310 | 402~427 | 520~600 | 720~900 |
Note: The production capacity is closely related to the particle size, specific gravity, hardness, moisture and other indicators of the raw materials. The above is only for selection reference.
Working Principle:
Fluidized(Fluidised) bed opposed jet mill works with cyclone separator, dust collector and suction fan to form a complete grinding system.Compressed air flow after filtration and drying would go into milling chamber from nozzles, and meet in the center area, where material would be impacted and ground and sheared.
Milled powder would go up to the classifying chamber by the air flow from suction fan. The high-speed rotation of classifier wheel would create a strong centrifugal force to separate coarse powder and fine powder.Qualified fine powder would go through the wheel vane then into the cyclone separator or dust collector, while mixture of coarse powder and fine powder would fall down to the milling chamber to be milled again.
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