Treatment of complex sulfide concentrate
US-2018298467-A1 · Oct 18, 2018 · US
US9068244B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9068244-B2 |
| Application number | US-201214384616-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 6, 2012 |
| Priority date | Apr 6, 2012 |
| Publication date | Jun 30, 2015 |
| Grant date | Jun 30, 2015 |
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A method for recovering chromite from ore slurry obtained by processing nickel oxide ore, the raw material, in a plant for the wet smelting of nickel oxide ore. In the method chromite is separated and recovered from an ore slurry obtained from a nickel oxide ore when nickel and cobalt are recovered from the nickel oxide ore. The method has a grain diameter separation step for separating the ore slurry on the basis of a predetermined classification point according to the difference in the grain diameter of particles contained in the supplied ore slurry and a sedimentation separation step for causing the oversized ore slurry separated in the grain diameter separation step to undergo sedimentation and concentration on the basis of a target classification point, and recovering the chromite. The coarse particle content of the oversized ore slurry separated in the grain diameter separation step is adjusted to 30-50%.
Opening claim text (preview).
The invention claimed is: 1. A chromite recovery method for separating and recovering chromite from ore slurry produced from nickel oxide ore when recovering nickel and cobalt from the nickel oxide ore, the method comprises: a particle diameter separation step of separating the ore slurry which has a particle size of 2 mm or less based on a predetermined classification point depending on a particle diameter difference of particles contained in the ore slurry to be supplied; and a sedimentation separation step of sedimenting and concentrating oversized ore slurry separated in the particle diameter separation step to recover the chromite, wherein a content percentage of coarse particles in the oversized ore slurry separated in the particle diameter separation step is adjusted to 30 to 50%. 2. The recovery method for chromite according to claim 1 , wherein a concentration of ore slurry supplied to the particle diameter separation step is 10% by weight. 3. A hydrometallurgical process for nickel oxide slurry for transporting ore slurry produced by slurrying nickel oxide ore to a high pressure acid leach facility where nickel and cobalt are leached to recover the nickel and cobalt from leachate produced by solid-liquid separation leached slurry, the process comprises: a chromite recovery step including: a particle diameter separation step of separating the ore slurry which has a particle size of 2 mm or less based on a classification point depending on a particle diameter difference of particles contained in the ore slurry; and a sedimentation separation step of sedimenting and concentrating oversized ore slurry separated in the particle diameter separation step based on a target classification point to recover chromite, wherein a content percentage of coarse particles in the oversized ore slurry separated in the particle diameter separation step is adjusted to 30 to 50%.
Preliminary treatment of ores, e.g. by roasting or by the Krupp-Renn process · CPC title
by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title
by wet processes (recovery or separation of nickel or cobalt using organic agents C22B3/00) · CPC title
Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage · CPC title
Sulfurated acids or salts thereof · CPC title
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