Technique of adjusting and controlling electric potential for floatation of sulphide ore of lead and zinc
A potential control, sulfide ore technology, applied in flotation, solid separation and other directions, can solve the problems of long operation and control of lead-zinc sulfide ore flotation process, low resource utilization rate, poor product quality and other problems, and can achieve flotation power. The effect of reducing energy consumption and equipment operating costs, shortening the flotation process, and improving the recovery rate
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example 1
[0018] Utilize raw ore ore sample to add the lime of different dosage in table 1 in mill, ore is ground to -200 order 72%, make lead, zinc, sulfur fully monomer dissociation, add 40 grams / ton ethylsulfide nitrogen at the same time, then Add foaming agent into the ground pulp for lead selection. See Table 1 for relevant technical indicators.
[0019] It can be seen from Table 1 that when the lead potential is controlled at 150-180mv, the recovery rate of lead and the grade of lead reach the best at the same time, and the floatability of sulfur iron and zinc is poor at this time. When the potential is at 166mv, the grade and recovery rate of galena are the best at the same time, and the floatability of sphalerite and pyrite is very poor. Effective separation of lead, zinc and sulfur.
[0020] Lime dosage kg / t
example 2
[0022] Use raw ore samples to add lime into the mill, grind the ore to -200 mesh 72%, so that lead, zinc, and sulfur are fully dissociated, and at the same time add the same amount but different ratios of ethiazide and butyl xanthate Collector, the pulp potential is controlled at 160-170mv, and then a foaming agent is added to the ground pulp for lead selection. See Table 2 for relevant technical indicators.
[0023] As can be seen from Table 2, the selected lead potential is controlled at 160-170mv, and the recovery rate of lead with a certain proportion of butylxanthate properly mixed in the selected lead collector will be higher. When the ratio of ethiazide and butyl xanthate is 3:1, the grade and recovery rate of lead are both higher, which is the optimal ratio of medicaments.
[0024]
example 3
[0026] Use raw ore samples to add lime to the mill, grind the ore to -200 mesh 72%, so that the lead, zinc, and sulfur are fully dissociated, and at the same time add ethiazide as the main butyl xanthate as the auxiliary lead selection and capture Collecting agent, adding different amounts of zinc sulfate to carry out the comparison test of the amount of inhibitor zinc sulfate, the pulp potential is controlled at 160-170mv, and then add foaming agent to the ground pulp for lead selection. See Table 3 for relevant technical indicators.
[0027] It can be seen from Table 3 that adding a small amount of zinc sulfate is still helpful to improve the main grade of lead concentrate and reduce the lead and zinc content.
[0028] Inhibitor
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