Hydrometallurgical process for nickel oxide ore
US-2016076121-A1 · Mar 17, 2016 · US
US10507471B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10507471-B2 |
| Application number | US-201615758510-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 23, 2016 |
| Priority date | Sep 25, 2015 |
| Publication date | Dec 17, 2019 |
| Grant date | Dec 17, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided is a gravity separation device wherein occurrences of shelving, flashing, and the like inside the device can be suppressed, variations in the flow rate of underflow obtained by gravity separation can be minimized and underflow can be stably extracted. This gravity separation device, which separates overflow and underflow using differences in specific gravity from mixed material, is provided with a separation section that has a supply pipe for supplying a slurry of the mixed material at the top and separates that slurry into overflow and underflow, and a deposition section that is positioned below the separation section and wherein the underflow that has been separated by precipitation is deposited. An extraction pipe for extracting the underflow is connected to the deposition section, and a valve for extracting the underflow and a metering pump for quantitatively extracting the underflow are provided in the extraction pipe.
Opening claim text (preview).
The invention claimed is: 1. A gravity separation device separating an overflow and an underflow using a difference in specific gravity from a slurry of laterite ore including two or more types of ore particles having different specific gravities, wherein the percentage of ore particles contained in the slurry and having a particle size of 2000 μm or less is 100% and the percentage of ore particles contained in the slurry and having a particle size of 75 μm or less is 70% to 90%, the gravity separation device comprising: a separation section that has a supply pipe for supplying the slurry of laterite ore to an upper portion and separates the slurry into an overflow and an underflow; and a deposition section that is positioned at the lower side of the separation section and in which the underflow separated by precipitation is deposited, wherein a pressure meter for measuring a pressure inside the separation section is provided in the separation section, an extraction pipe for discharging the underflow is connected to the deposition section, a valve for discharging the underflow and a metering pump for quantitatively discharging the underflow are provided in the extraction pipe, and the metering pump controls a discharged amount of the underflow on the basis of a measurement value obtained by the pressure meter. 2. The gravity separation device according to claim 1 , wherein a controller, which receives a signal of a pressure measurement value measured by the pressure meter and transmits, to the metering pump, an instruction signal to perform the operation at such a rotation number that the discharged amount of the underflow becomes a predetermined discharged amount on the basis of the measurement value, is further provided. 3. The gravity separation device according to claim 1 , wherein a second valve is provided between the valve and the metering pump in the extraction pipe. 4. The gravity separation device according to claim 2 , wherein a second valve is provided between the valve and the metering pump in the extraction pipe. 5. The gravity separation device according to claim 1 , wherein an injected water supply pipe for supplying injected water is provided in the vicinity of the middle stage thereof and the injected water supplied from the injected water supply pipe flows upward to become upward flow, and specific gravity separation of the ore particles contained in the slurry of laterite ore is performed by a difference between the upward flow of the injected water and the precipitation rate of the precipitated particles. 6. The gravity separation device according to claim 2 , wherein an injected water supply pipe for supplying injected water is provided in the vicinity of the middle stage thereof and the injected water supplied from the injected water supply pipe flows upward to become upward flow, and specific gravity separation of the ore particles contained in the slurry of laterite ore is performed by a difference between the upward flow of the injected water and the precipitation rate of the precipitated particles. 7. The gravity separation device according to claim 3 , wherein an injected water supply pipe for supplying injected water is provided in the vicinity of the middle stage thereof and the injected water supplied from the injected water supply pipe flows upward to become upward flow, and specific gravity separation of the ore particles contained in the slurry of laterite ore is performed by a difference between the upward flow of the injected water and the precipitation rate of the precipitated particles. 8. The gravity separation device according to claim 4 , wherein an injected water supply pipe for supplying injected water is provided in the vicinity of the middle stage thereof and the injected water supplied from the injected water supply pipe flows upward to become upward flow, and specific gravity separation of the ore particles contained in the slurry of laterite ore is performed by a difference between the upward flow of the injected water and the precipitation rate of the precipitated particles.
Preliminary treatment of ores or scrap · CPC title
Upward current classifiers · CPC title
General arrangement of separating plant, e.g. flow sheets · CPC title
Control arrangements specially adapted for wet-separating apparatus or for dressing plant, using physical effects · CPC title
Preliminary treatment of ores, e.g. by roasting or by the Krupp-Renn process · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.