Method for enriching lithium from lithium clay

Patent metadata

Field	Value
Publication number	US-12098442-B2
Application number	US-202218029656-A
Country	US
Kind code	B2
Filing date	Sep 22, 2022
Priority date	Aug 17, 2022
Publication date	Sep 24, 2024
Grant date	Sep 24, 2024

Abstract

A method for enriching lithium from a lithium clay includes the following steps (1) the raw ore were crushed to produce fine particles, (2) performing rougher on the fine particles by adding ferric sulfate or ferric nitrate, sodium oleate, and cocoamine to obtain rough concentrate and rough tailing, (3) finely separating the rough concentrate to obtain the first part of concentrate, (4) re-grinding the rough tailing by ball mill, (5) performing rougher on the reground tailing to obtain reground rough concentrate and re-ground rough tailing, (6) performing cleaner on the reground rough concentrate to obtain the second part of concentrate, and (7) performing scavenger on the reground rough tailing to obtain the cleaned tailing.

First claim

The invention claimed is:

1. A method for enriching lithium from a lithium clay, comprising the following steps:
(1) crushing the lithium clay to produce the −1 mm size fraction, wherein the mass proportion of the −0.15 mm is ≥60%;
(2) flotating the −1 mm, adding an aqueous solution of ferric sulfate or ferric nitrate, and stirring evenly, then adding regulator to adjust pulp pH value between 9-10, then adding an aqueous solution of sodium oleate and an aqueous solution of cocoamine, stirring evenly, and then flotation to obtain a rough concentrate and a rough tailing;
(3) flotating the rough concentrate, and adding a pH regulator to adjust a pH value of the system to be 9-10, and stirring evenly, then adding an aqueous solution of sodium oleate and an aqueous solution of cocoamine, stirring evenly, and then flotation to obtain a concentrate A and a cleaned tailing;
(4) mixing the rough tailing in step (2) with the cleaned tailing in step (3) and performing a wet ball milling to obtain a tailing A with a mass ratio of a −0.074 mm tailing ≥80%;
(5) flotating the tailing A, adding an aqueous solution of ferric sulfate or ferric nitrate, stirring evenly, adding a pH regulator to adjust a pH value to be 9-10, then adding an aqueous solution of sodium hexametaphosphate, stirring evenly, adding an aqueous solution of sodium oleate and an aqueous solution of cocoamine, stirring evenly, and then flotation to obtain a reground rough concentrate and a reground rough tailing;
(6) flotating the reground rough concentrate, adding a pH regulator to adjust a pH value to be 9-10, then adding an aqueous solution of sodium hexametaphosphate, stirring evenly, adding an aqueous solution of sodium oleate and an aqueous solution of cocoamine, stirring evenly, and then flotation to obtain a concentrate B;
(7) flotating the reground rough tailing, adding a pH regulator to adjust a pH value to be 9-10, then adding an aqueous solution of sodium oleate and an aqueous solution of cocoamine, stirring evenly, and then flotation to obtain a cleaned tailing B; and
(8) using the concentrate A and the concentrate B as a final concentrate, and using the cleaned tailing B as a final tailing.

2. The method of claim 1 , wherein in step (2), based on a mass of the −1 mm raw ore, the dosage of the ferric sulfate or the ferric nitrate is 300-500 g/t, the dosage of the sodium oleate is 500-700 g/t, and the dosage of the cocoamine is 150-300 g/t.

3. The method of claim 1 , wherein the pH regulator is at least one of sodium hydroxide or sodium carbonate.

4. The method of claim 1 , wherein in step (3), based on a mass of the −1 mm raw ore, the dosage of the sodium oleate is 200-300 g/t and the dosage of the cocoamine is 80-150 g/t.

5. The method of claim 1 , wherein in step (5), based on a mass of the −1 mm raw ore, the dosage of the ferric sulfate or the ferric nitrate is 150-250 g/t, the dosage of the sodium hexametaphosphate is 400-600 g/t, the dosage of the sodium oleate is 300-400 g/t, and the dosage of the cocoamine is 80-150 g/t.

6. The method of claim 1 , wherein in step (6), based on a mass of the −1 mm raw ore, the dosage of the sodium hexametaphosphate is 150-250 g/t, the dosage of the sodium oleate is 150-200 g/t, and the dosage of the cocoamine is 30-70 g/t.

7. The method of claim 1 , wherein in step (7), based on a mass of the −1 mm raw ore, the dosage of the sodium oleate is 150-200 g/t and the dosage of the cocoamine is 40-90 g/t.

8. The method of claim 1 , wherein in steps (2), (3), (5), (6) and (7), a mass ratio of the sodium oleate to the cocoamine is (2.8-3.4):1.

9. The method of claim 8 , wherein in steps (2), (3), (5), (6) and (7), a mass ratio of the sodium oleate to the cocoamine is 3:1.

10. The method of claim 1 , wherein a mass fraction of ferric sulfate or ferric nitrate in the aqueous solution of ferric sulfate or ferric nitrate is 1%-3%, a mass fraction of sodium hexametaphosphate in the aqueous solution of sodium hexametaphosphate is 1%-3%, a mass fraction of sodium oleate in the aqueous solution of sodium oleate is 1%-3%, and a mass fraction of cocoamine in the aqueous solution of cocoamine is 0.5%-1.5%.

Assignees

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

Inventors

• Ruan Dingshan
• Zhang Peng
• Li Changdong
• Tang Shijian
• Liu Yuntao

Classifications

• C22B3/12

  in inorganic alkaline solutions · CPC title

• B03D1/02 Primary

  Froth-flotation processes · CPC title

• B03D1/018

  Mixtures of inorganic and organic compounds · CPC title

• C22B26/12 Primary

  Obtaining lithium · CPC title

• B03D1/00

  Flotation (conditioning for flotation, general arrangement of plan B03B) · CPC title