Additional screening-gravity separation process before phosphate rock positive flotation operation
A technology of positive flotation and pre-operation, which is applied in the field of adding screening-gravity separation process before the positive flotation of phosphate rock, can solve the problems of non-universality, and achieve the guarantee of separation efficiency, smooth surface of chute, The effect of increasing sensitivity
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Embodiment 1
[0020] A screening-gravity separation process is added before the positive flotation of phosphate rock. The method described in this embodiment is:
[0021] Will P 2 o 5 Grade is 18.0wt%, MgO content is 3.0wt%, Al 2 o 3 The phosphate slurry with a content of 5.5wt% and a particle size of less than 0.074mm accounting for 70~85wt% is fed into the vibrating screen. The aperture of the vibrating screen is 0.15mm. The material on the screen is used as phosphorus concentrate I, and the material under the screen is fed into the third section Spiral chute re-election process, one-stage roughing to obtain phosphorus concentrate II and roughing tailings, the roughing tailings are fed into the second-stage sweeping to obtain phosphorous concentrate III and sweeping tailings, and the sweeping tailings are fed into Three stages of sweeping to obtain phosphorous concentrate IV and gravity tailings, gravity tailings fed into thickener, after the thickener thickened, concentration is 25wt...
Embodiment 2
[0025] A screening-gravity separation process is added before the positive flotation of phosphate rock. The method described in this embodiment is:
[0026] Will P 2 o 5 Grade is 24.7wt%, MgO content is 1.4wt%, Al 2 o 3 Content 4.7wt%, particle size less than 0.074mm accounted for 55 ~ 65wt% phosphate slurry is fed into the vibrating screen, the aperture of the vibrating screen is 0.10mm, the material on the screen is used as phosphorus concentrate I, and the material under the screen is fed into the spiral chute Gravity separation process, one-stage roughing to obtain phosphorous concentrate II and roughing tailings, the roughing tailings are sent to the second-stage sweeping to obtain phosphorous concentrate III and gravity tailings, and the gravity tailings are fed to the thickener After thickening by the thickener, the dense underflow with a concentration of 30wt% is fed into the positive flotation operation for flotation, and the phosphorous concentrate I, phosphorous...
Embodiment 3
[0030] A screening-gravity separation process is added before the positive flotation of phosphate rock. The method described in this embodiment is:
[0031] Will P2 o 5 Grade is 27.5wt%, MgO content is 1.2wt%, Al 2 o 3 Content 3.7wt%, particle size less than 0.074mm accounted for 45 ~ 54wt% phosphate slurry is fed into the vibrating screen, the aperture of the vibrating screen is 0.08mm, the material on the sieve is used as phosphorus concentrate I, and the material under the sieve is fed into the third section Spiral chute re-election process, one-stage roughing to obtain phosphorus concentrate II and roughing tailings, the roughing tailings are fed into the second-stage sweeping to obtain phosphorous concentrate III and sweeping tailings, and the sweeping tailings are fed into Three stages of sweeping to obtain phosphorus concentrate IV and gravity separation tailings, gravity separation tailings feed thickener, after thickener concentration, concentration is 35wt% dense ...
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