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Flotation of Chromite Ore

· The flotation procedure included 0, 1, 5, and 20minute conditioning periods in the flotation cell with sulfuric acid at pH 20 Total reagent consumptions were 10 pound of Armac C and 130 to 210 pounds of H2SO4 per ton of ore Results (table 6) show that acid scrubbing caused a significant increase in flotation response Raising the conditioning time

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(PDF) Flotation of chromite and serpentine ResearchGate

The flotation was also found to favour the recovery of chromite particles with high chrome to iron ratioThe experiments showed a distinct abundance between the

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· May 15, 2019 Chrome process equipment is wet type strong magnetic separator, and spiral chute (chrome spiral plant) of gravity separator 3 Experimental results and discussion 31 Chrome magnetic separation process The chrome raw ore is a flotation tail ore, which is mainly formed in the chromite, and the chromite is the target recovering mineral

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The flotation was also found to favour the recovery of chromite particles with high chrome to iron ratioThe experiments showed a distinct abundance between the chromite surface charge and the

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· Chrome process equipment is wet type strong magnetic separator, and spiral chute (chrome spiral plant) of gravity separator 3 Experimental results and discussion 31 Chrome magnetic separation process The chrome raw ore is a flotation tail ore, which is mainly formed in the chromite, and the chromite is the target recovering mineral

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TREATING CHROME TAILINGS FOR PGMs Miningreview

· This is followed by flotation banks comprising 10 cleaner and five recleaner cells that take the concentrate recovery level of about 44% of the contained PGMs Collector reagents are used to make the PGMs aerophilic, depressors are used to make the chrome hydrophilic, in addition to the frother The optimal use of reagents is determined by the initial blend of

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· The flotation reagents can be added in a feedforward fashion based on the plant raw coal tonnage Automatic feedback control of the flotation reagent addition rates has been lacking due to the unavailability of sensors for determining the quality of the froth cell tailings Expensive nuclearbased sensors have been tried with limited success Other control