Method for producing battery-grade nickel sulfate by using laterite nickel ore
US-11952288-B2 · Apr 9, 2024 · US
US10501824B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10501824-B2 |
| Application number | US-201515524708-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 10, 2015 |
| Priority date | Nov 10, 2014 |
| Publication date | Dec 10, 2019 |
| Grant date | Dec 10, 2019 |
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A process of treating complex sulfide concentrate includes the steps of roasting wet or slurried complex sulfide concentrate in a furnace at a temperature of at least 720° C. to obtain a calcine; smelting the calcine under inert or oxygen free atmosphere in a smelting furnace to obtain a matte, and optionally granulating the matte to obtain a granulated matte.
Opening claim text (preview).
The invention claimed is: 1. A process of treating complex sulfide concentrate, wherein the complex sulfide ore comprises 2 to 20 wt % Ni, 0 to 15 wt % Cu, and 10 to 55 wt % Fe of the total weight of the concentrate and the complex sulfide concentrate is obtained from complex sulfide ores comprising sulfides of two or more metals, comprising the steps of: (a) roasting wet or slurried complex sulfide concentrate in a furnace at a temperature from 720° C. to 870° C. to obtain a calcine, wherein oxygen is introduced into the roasting step (a) as oxygen enriched air, wherein the oxygen partial pressure is below 1000 Pa; and (b) smelting the calcine obtained in step (a) at a temperature from 1250° C. to 1500° C. under inert or oxygen free atmosphere in a smelting furnace to obtain a matte. 2. The process as claimed in claim 1 , further comprising: (c) granulating the matte obtained in step (b) to obtain a granulated matte. 3. The process as claimed in claim 1 , wherein the complex sulfide concentrate comprises Ni, Cu, Co, Fe and/or PGM. 4. The process as claimed in claim 1 , wherein the calcine has sulfur content below 10% w/w. 5. The process as claimed in claim 1 , wherein the furnace in step (a) is a drum furnace or a fluidizing bed furnace. 6. The process as claimed in claim 1 , wherein the roasting temperature in step (a) is from 780 to 820° C. 7. The process as claimed in claim 1 , wherein roasting in step (a) is accomplished in a bubbling bed. 8. The process as claimed in claim 1 , wherein the smelting temperature in step (b) is from 1300 to 1450° C. 9. The process as claimed in claim 1 , wherein a first part of the complex sulfide concentrate is introduced into the roasting step (a) and a remaining second part is introduced into the smelting step (b) after drying. 10. The process as claimed in claim 1 , wherein the smelting furnace is an electric furnace. 11. The process as claimed in claim 1 , wherein the roasting temperature in step (a) is from 750 to 850° C.
with formation of a matte or by matte refining or converting into nickel or cobalt, e.g. by the Oxford process (leaching of mattes C22B23/04) · CPC title
Preliminary treatment of ores, e.g. by roasting or by the Krupp-Renn process · CPC title
Oxidizing roasting · CPC title
by sulfides; Roasting reaction methods · CPC title
Smelting or converting · CPC title
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