Flexible
Feeding size
5-1400t/d
Capacity

The thickener is suitable for the dehydration of concentrates and tailings in concentrators, and is widelyused in metallurgy, chemical, coal, non-metallic beneficiation, environmental protection and other in-dustries. The high-efficiency thickener is actually not a simple settling device, but a new type of dewa.tering device that combines the filtering characteristics of the mud layer.

1.Add flocculant to increase the particle size of settled solid particles and speedup the settling speed;

2.Increase the degassing tank to prevent solid particles from adhering to the airbubbles;

3.There is a receiving tray, and the feeding barrel moves down, so that the fed ore slurry falls evenly and smoothly.

04 The unit processing capacity is 4 to 9 times that of the conventional thickener.Calculated according to the unit processing capacity, the energy consumptionis 30% lower than that of the traditional thickener;
| Model | Tank inner diameter (mm) | Tank height (mm) | Subsidence area (m²) | Rake speed (r/min) | Rake lift height (mm) | Drive motor power (kw) | Lifting device motor power (kw) | Steel tank weight (kg) | Weight (kg) | |
|---|---|---|---|---|---|---|---|---|---|---|
| M-3.6 | 3600 | 1700 | 10.2 | 1.1 | 200 | 1.5 | 1.5 | 2829 | 6650 | |
| M-5.18 | 5182 | 2134 | 21 | 0.4 | 300 | 3 | 0.8 | 5342 | 10460 | |
| M-6 | 6000 | 2500 | 28.3 | 0.8 | 300 | 4 | 2.2 | 6506 | 10573 | |
| 7500 | 2800 | 44.1 | 0.427 | 300 | 5.5 | 2.2 | 10258 | 17320 | ||
| M-7.5 | 9000 | 2800 | 63.6 | 0.427 | 300 | 5.5 | 2.2 | 15990 | 23680 | |
| M-9 | 12000 | 3600 | 110 | 0.35 | 300 | 7.5 | 2.2 | 25589 | 42756 | |
| M-12 | 15000 | 4000 | 177 | 0.15 | 300 | 7.5 | 2.2 | 36050 | 59000 | |
| 18000 | 4400 | 254 | 0.13 | 400 | 7.5 | 5.5 | 52485 | 73296 | ||
| M-15 | 20000 | 4400 | 314 | 0.13 | 400 | 7.5 | 5.5 | 59365 | 76020 | |
| M-18 | ||||||||||
| M-20 |
Note:Any change of technical data shall not be advised additionally.




Before the slurry enters the high-efficiency thickener equipment, after removing most of the gas containedin the gas elimination device, itenters the mixing device from the feeding pipe, and the slurry is fully mixedwith an appropriate amount of flocculant in the mixing device to form a good flocculation state. Thebottom of it diffuses to the surrounding and enters the pre-formed high-concentration sludge layer at thebottom of the concentration tank. At this time, the flocculated slurry settles to the bottom of the pool; theslurry water rises through the sediment layer. Here, the sediment layer acts as a filter, preventing thefine-grained sludge from rising. The slurry that has not been fully flocculated will continue to be in contactwith the flocs when it reaches the sediment layer, so that the flocs continue to grow. Finally, the rake isdriven by the central drive device, and the concentrated material is pushed to the central discharge portfor discharge, and the slurry water flows out from the overflow port.

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