Mineral dressing collector for poor hematite reverse flotation
A collector and hematite technology, applied in flotation, solid separation, etc., can solve the problems of high viscosity of flotation foam, complex dispensing system, and low collection efficiency, so as to reduce the grade and save heating energy consumption , significant economic benefits
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Embodiment 1
[0013] The poor hematite with a raw ore grade of 28.55% is ground for one stage, and the overflow particle size reaches about 60% of -200 mesh, and it is fed into a coarse and fine-grained cyclone. The final coarse-grained concentrate is controlled by fine sieve, its grade is 66.67%, the yield is 17.17%, and the yield is 40.15%. 26.33%, the yield is 8.56%, and the medium ore is re-grinded and returned to the coarse and fine grading cyclone. Spin overflow (fine-grained grade) adopts weak magnetic and strong magnetic separation to remove mud and throw tails. Its grade is 9.95%, the yield is 30.57%, and the yield is 10.66%. Yield 25.93%, yield 40.63%, get mixed magnetism fine sample 200g, make pH adjusting agent transfer to 10 with NaOH; Add 4ml (concentration 2wt%) CaO and make activator; Add 3ml (concentration 5wt%) mineral dressing of the present invention to collect agent, where C 6 h 19 C(OH) 2 C(OH)COOK is 10% (percentage by weight), C 15 h 31 C(OH) 2 C(OH)COOK is 20...
Embodiment 2
[0015] This embodiment adopts the same ore dressing process to carry out pretreatment to the poor hematite of the same grade described in embodiment 1, adds 3.1ml (concentration 5wt%) ore dressing collector of the present invention, wherein C 10 h 21 C(OH) 2 CH 2 COOK is 20% (weight percentage), C 13 h 27 C(OH) 2 CH 2 COOK is 15% (weight percentage), C 16 h 31 C(OH) 2 CH 2 COOK is 12% (weight percentage), C 18 h 35 C(OH) 2 CH 2 COOK is 53% (percentage by weight). Under the condition of 16°C, a reverse flotation separation of one rough, one fine and three sweeps is carried out, and finally the flotation concentrate with a grade of 68.70% and a weight of 112.20g and a grade of 14.10% and a weight of 87.80g are obtained Flotation tailings.
Embodiment 3
[0017] The present embodiment adopts the same ore dressing process to carry out pretreatment to the poor hematite of the same grade described in embodiment 1, adds 2.8ml (concentration 5wt%) ore dressing collector of the present invention, wherein C 11 h 20 C(OH)C(OH)COOK is 20% (percentage by weight), C 14 h 29 C(OH) 2 CH 2 COOK is 9% (percentage by weight), C 17 h 33 C(OH) 2 CH 2 COOK is 20% (weight percentage), C 19 h 37 C(OH) 2 CH 2 COOK is 51% (percentage by weight). Under the condition of 18°C, a reverse flotation separation of one coarse, one fine and three sweeps is carried out, and finally the flotation concentrate with a grade of 68.60% and a weight of 112.50g and a grade of 14.04% and a weight of 87.50g are obtained Flotation tailings.
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