Method for producing battery-grade nickel sulfate by using laterite nickel ore

Patent metadata

Field	Value
Publication number	US-11952288-B2
Application number	US-202118042207-A
Country	US
Kind code	B2
Filing date	Aug 3, 2021
Priority date	Aug 17, 2020
Publication date	Apr 9, 2024
Grant date	Apr 9, 2024

Abstract

Disclosed is a method for producing battery-grade nickel sulfate by using laterite nickel ore comprising the following steps: sorting the laterite nickel ore to obtain lump ore and sediment ore; crushing the lump ore, and then performing heap leaching, to obtain a crude nickel sulfate solution A; separating the sediment ore to obtain high chromium ore, low iron, high magnesium ore, and high iron, low magnesium ore, and drying, roasting, reducing, and sulfurating the low iron, high magnesium ore to obtain low nickel matte; blowing and performing water extraction on the low nickel matte, and then performing oxygen pressure leaching, to obtain a crude nickel sulfate solution B; performing pressure leaching on the high iron, low magnesium ore to obtain a crude nickel sulfate solution C; and performing extraction on the crude nickel sulfate solutions A, B, and C, and then evaporating and crystallizing, to obtain battery-grade nickel sulfate.

First claim

The invention claimed is:

1. A method for producing battery-grade nickel sulfate by using laterite nickel ore, comprising the following steps:
(1) sorting the laterite nickel ore to obtain lump ore and sediment ore; wherein the lump ore and the sediment ore are sorted according to a particle size, where a particle size of the lump ore is greater than 10 mm, and a particle size of the sediment ore is less than 10 mm
(2) crushing the lump ore, and then performing heap leaching, to obtain a crude nickel sulfate solution A;
(3) separating the sediment ore to obtain high chromium ore, low iron, high magnesium ore, and high iron, low magnesium ore, and drying, roasting, reducing, and sulfurating the low iron, high magnesium ore to obtain low nickel matte; wherein the high chromium ore comprises 30-40% by mass of chromium and 0.1-0.2% by mass of nickel; the low iron, high magnesium ore is mainly garnierite and comprises 1.5-2.1% by mass of nickel, 15-25% by mass of magnesium, 8-25% by mass of iron, and 35-50% by mass of silicon; and the high iron, low magnesium ore is mainly limonite and comprises 0.8-1.3% by mass of nickel, 30-50% by mass of iron, 0.1-10% by mass of magnesium, and 10-30% by mass of silicon;
(4) blowing and performing water extraction on the low nickel matte, and then performing oxygen pressure leaching, to obtain a crude nickel sulfate solution B;
(5) performing pressure leaching on the high iron, low magnesium ore to obtain a crude nickel sulfate solution C; and
(6) performing extraction on the crude nickel sulfate solution A, the crude nickel sulfate solution B, and the crude nickel sulfate solution C, and then evaporating and crystallizing, to obtain battery-grade nickel sulfate; wherein, in the battery-grade nickel sulfate, a content of Mg<0.002 mass %, a content of Si<0.001 mass %, a content of magnetic substance<0.08 mass %, and a content of Co<0.002 mass %.

2. The method according to claim 1 , wherein in step (1), the laterite nickel ore comprises the following components by mass percentage: 1.2-2% of Ni, 15-40% of Fe, 6-20% of Mg, 0.03-0.25% of Co, and 10-40% of Si.

3. The method according to claim 1 , wherein in step (2), a specific operation of the heap leaching comprises: putting the crushed lump ore into a heap leaching pool, and then leaching nickel from the ore in a manner of spraying and soaking in sulfuric acid, to obtain the crude nickel sulfate solution; and in step (2), for the heap leaching, a temperature is 40-60° C., and a time is 30-50 days.

4. The method according to claim 1 , wherein in step (3), for the roasting, a temperature is 800-1000° C., and a time is 1-3 h; and in step (3), for the reducing, a temperature is 1400-1600° C., and a time is 2-4 h.

5. The method according to claim 1 , wherein in step (3), a reducing agent used for the reducing is at least one of coke, semi-coke, or anthracite.

6. The method according to claim 1 , wherein in step (3), for the sulfurating, a temperature is 1100-1400° C., and a time is 0.5-3 h; in step (4), for the oxygen pressure leaching, a temperature is 100-250° C., and a pressure is 1-5 MPa; and in step (5), for the pressure leaching, a temperature is 170-260° C., and a pressure is 1-5 MPa.

7. The method according to claim 1 , wherein in step (6), an acidic extractant is used in the extraction, Fe3+, Mn2+, Co2+, Mg2+, and Ca2+ are extracted to obtain a nickel sulfate solution, and the acidic extractant is at least one of diisooctyl phosphate, mono 2-ethylhexyl 2-ethylhexyl phosphate, or di(2,4,4-trimethylpentyl).

8. The method according to claim 7 , wherein in step (6), a specific operation of the extraction comprises: under conditions of a temperature of 50-80° C. and a pH value of 2-5, first extracting Fe3+ and Mn2+ by using diisooctyl phosphate, and then extracting Co2+, Mg2+, and Ca2+ by using either or both of mono 2-ethylhexyl 2-ethylhexyl phosphate and di(2,4,4-trimethylpentyl), to obtain the nickel sulfate solution.

Assignees

• Guangdong Brunp Recycling Technology Co Ltd
• Hunan Brunp Recycling Tech Co Ltd
• Hunan Brunp Vehicles Recycling Co Ltd
• Ningde Brunp Recycling Tech Co Ltd

Inventors

• Li Changdong
• Tang Honghui
• Wang Chunyi
• Pei Xinan
• Li Xingdui

Classifications

• C01G53/10 Primary

  Sulfates · CPC title

• C22B1/06

  Sulfating roasting · CPC title

• C22B3/08 Primary

  Sulfuric acid {, other sulfurated acids or salts thereof} · CPC title

• C22B3/3842

  Phosphinic acid, e.g. H2P(O)(OH) · CPC title

• C22B3/3844

  Phosphonic acid, e.g. H2P(O)(OH)2 · CPC title