Method for selecting sulfur from tailings discarded by mineral separation
A technology for selecting sulfur and tailings, which is applied in chemical instruments and methods, wet separation, solid separation, etc., and can solve problems such as the inability of sulfur production to meet market demand, the lack of development and utilization of tailings resources, and the lack of pricing power. , to achieve the effect of considerable economic benefits, saving pharmaceutical costs, and increasing sales prices
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Embodiment 1
[0034] See figure 1 :A method for selecting sulfur from tailings discharged from beneficiation, including the following steps:
[0035] 1) Feed the ore, send the tailings raw ore after beneficiation to the plate feeder through the hopper, and then transport it to the ball mill through the belt conveyor;
[0036] 2) Ball mill, the raw ore slurry obtained after grinding the tailings raw ore sent to the ball mill is sent to the mixing tank; the process conditions are: the raw ore input of the ball mill is 32t / h, and the amount of water added is about 52m 2 / h, the grinding fineness is 200 mesh, and the discharge concentration is 39%;
[0037] 3) Stir, the mixing bucket will stir the raw ore slurry evenly and send the evenly stirred slurry to the 6-S shaker;
[0038] 4) For ore dressing, the slurry is separated by a 6-S shaker to separate the concentrate grade from other substances. The process conditions are: back tilt angle α=2°, angle β between bed surfaces 40°, shaker stroke 28mm...
Embodiment 2
[0044] 1) To mine, the same as Example 1;
[0045] 2) Ball mill, the raw ore slurry obtained after grinding the tailings raw ore sent to the ball mill is sent to the mixing tank; the process conditions are: the raw ore input of the ball mill is 30t / h, and the water addition is about 49m 2 / h, the fineness of ore grinding is 200 mesh, and the concentration of ore discharge is 40%;
[0046] 3) Stirring, same as in Example 1;
[0047] 4) Ore beneficiation, the slurry is separated by 6-S type shaking table to separate the concentrate grade from other substances. The technological conditions are: back tilt angle α = 1°, angle β between bed surfaces 42°, and shaker stroke 15mm, 260 strokes / minute; flushing water volume 1T / set H. Obtained sulfur concentrate mines with a sulfur grade of 50%, middle mines with a sulfur grade of 16%, and tailings mines with a sulfur grade of 4%;
[0048] Others are the same as in Example 1.
Embodiment 3
[0050] 1) To mine, the same as Example 1;
[0051] 2) Ball mill, the raw ore slurry obtained after grinding the tailings raw ore sent to the ball mill is sent to the mixing tank; the process conditions are: the raw ore input of the ball mill is 31t / h, and the water volume is about 48m 2 / h, the fineness of grinding is 200 mesh, and the discharge concentration is 38%;
[0052] 3) Stirring, same as in Example 1;
[0053] 4) Ore beneficiation, the slurry is separated by 6-S type shaking table to separate the concentrate grade from other substances. The technological conditions are: back tilt angle α = 1°, angle β between bed surfaces 42°, and shaker stroke 34mm, 240 strokes / minute; the slurry concentration is 20-30%, and the flushing water volume is 0.7-1T / set H. Obtained a sulfur concentrate mine area with a sulfur content of 42%, a middle mine area with a sulfur content of 12% and a tailing mine area with a sulfur content of 4%;
[0054] Others are the same as in Example 1.
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