Mineralization method of calcium chloride-type from lithium-containing salt lake brine by evaporation and brine mixing

Patent metadata

Field	Value
Publication number	US-2024262704-A1
Application number	US-202218260031-A
Country	US
Kind code	A1
Filing date	Aug 26, 2022
Priority date	Feb 28, 2022
Publication date	Aug 8, 2024
Grant date	—

Abstract

The invention discloses a mineralization method of a calcium chloride-type from lithium-containing salt lake brine by evaporation and brine mixing, comprising the following steps of: (1) naturally evaporating the calcium chloride-type from lithium-containing salt lake brine to precipitate sodium salt and potassium-containing mixed salt; and (2) when calcium in the brine is saturated, adding saturated solution of magnesium chloride in a certain proportion for brine mixing operation, and then naturally evaporating to precipitate carnallite, wherein a lithium-containing old brine with low potassium and sodium contents is obtained when magnesium in the brine is saturated. The method has the characteristics of simple process, simple and convenient operation, high potassium yield and easy extraction of lithium from lithium-containing brine, and has practical significance for the development and utilization of potassium and lithium resources in calcium chloride salt lakes.

First claim

1 . A mineralization method of a calcium chloride-type lithium-containing salt lake brine by evaporation and brine mixing, comprising the following steps of:
(1) naturally evaporating a calcium chloride-type lithium-containing salt lake brine to precipitate a sodium salt and a potassium-containing mixed salt; and (2) adding a saturated solution of magnesium chloride in a proportion into the brine when calcium is saturated for brine mixing, and then performing naturally evaporation to precipitate carnallite, wherein a lithium-containing old brine with low potassium and sodium contents is obtained when magnesium in the brine is saturated; wherein in step (1), the calcium chloride-type lithium-containing salt lake brine is located in a potassium chloride area in a phase diagram of a quinary salt-water system Na + , K + , Mg 2+ , Ca 2+ //Cl − —H 2 O, at 25° C., and a mass ratio of Ca/Mg is 2 to 50; wherein in step (2), a proportion for brine mixing is such that the saturated solution of magnesium chloride is added according to a total Mg/K molar ratio of a calcium-saturated brine and the saturated solution of magnesium chloride of 2 to 10; and when magnesium in the brine is saturated, the brine with K + between 0.5 g/L and 5 g/L, Ca 2+ between 140 g/L and 200 g/L and Mg 2+ between 30 g/L and 80 g/L is the lithium-containing old brine with low potassium and sodium contents.

2 . The mineralization method of the calcium chloride-type lithium-containing salt lake brine by evaporation and brine mixing according to claim 1 , wherein in step (1), after the calcium chloride-type lithium-containing salt lake brine is naturally evaporated to precipitate sodium chloride, when potassium in the brine in a sodium chloride pool is saturated, the brine is pumped into a potassium mixed salt pool for evaporating continuously to precipitate the potassium-containing mixed salt.

3 . (canceled)

4 . The mineralization method of the calcium chloride-type lithium-containing salt lake brine by evaporation and brine mixing according to claim 2 , wherein in step (1), when the potassium in the brine is saturated, K + is between 23 g/L and 28 g/L, Ca 2+ is between 120 g/L and 180 g/L, and Mg 2+ is between 3 g/L and 8 g/L.

5 . The mineralization method of the calcium chloride-type lithium-containing salt lake brine by evaporation and brine mixing according to claim 1 , wherein in step (2), when the calcium in the brine is saturated, K + is between 22 g/L and 35 g/L, Ca 2+ is between 140 g/L and 240 g/L, and Mg 2+ is between 4 g/L and 9 g/L.

6 . (canceled)

7 . The mineralization method of the calcium chloride-type lithium-containing salt lake brine by evaporation and brine mixing according to claim 1 , wherein in step (2), the proportion for brine mixing is such that the saturated solution of magnesium chloride is added according to a total Mg/K molar ratio of the calcium-saturated brine and the saturated magnesium chloride solution of 2.5 to 7.5.

8 . (canceled)

9 . A lithium-containing old brine prepared by the mineralization method according to claim 1 .

10 . A battery-grade lithium carbonate, wherein the battery-grade lithium carbonate is obtained by a method comprising: separating the lithium-containing old brine of claim 9 by an electrodialysis membrane method or a nanofiltration membrane, then subjecting to evaporation and concentration, impurity removal and lithium precipitation to obtain a crude lithium carbonate, and then washing, drying and demagnetizing the crude lithium carbonate.

11 . A lithium-containing old brine prepared by the mineralization method according to claim 2 .

12 . (canceled)

13 . A lithium-containing old brine prepared by the mineralization method according to claim 4 .

14 . A lithium-containing old brine prepared by the mineralization method according to claim 5 .

15 . (canceled)

16 . A lithium-containing old brine prepared by the mineralization method according to claim 7 .

17 . (canceled)

18 . A battery-grade lithium carbonate, wherein the battery-grade lithium carbonate is obtained by a method comprising: separating the lithium-containing old brine of claim 11 by an electrodialysis membrane method or a nanofiltration membrane, then subjecting to evaporation and concentration, impurity removal and lithium precipitation to obtain a crude lithium carbonate, and then washing, drying and demagnetizing the crude lithium carbonate.

19 . A battery-grade lithium carbonate, wherein the battery-grade lithium carbonate is obtained by a method comprising: separating the lithium-containing old brine of claim 13 by an electrodialysis membrane method or a nanofiltration membrane, then subjecting to evaporation and concentration, impurity removal and lithium precipitation to obtain a crude lithium carbonate, and then washing, drying and demagnetizing the crude lithium carbonate.

20 . A battery-grade lithium carbonate, wherein the battery-grade lithium carbonate is obtained by a method comprising: separating the lithium-containing old brine of claim 14 by an electrodialysis membrane method or a nanofiltration membrane, then subjecting to evaporation and concentration, impurity removal and lithium precipitation to obtain a crude lithium carbonate, and then washing, drying and demagnetizing the crude lithium carbonate.

21 . A battery-grade lithium carbonate, wherein the battery-grade lithium carbonate is obtained by a method comprising: separating the lithium-containing old brine of claim 16 by an electrodialysis membrane method or a nanofiltration membrane, then subjecting to evaporation and concentration, impurity removal and lithium precipitation to obtain a crude lithium carbonate, and then washing, drying and demagnetizing the crude lithium carbonate.

Assignees

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

Inventors

• Lai Xueming
• Li Shengkang
• Dong Rui
• Xiao Wenjian
• Tang Honghui
• Li Changdong

Classifications

• C22B26/12

  Obtaining lithium · CPC title

• C01D15/08 Primary

  Carbonates; Bicarbonates · CPC title

• C01D3/06 Primary

  Preparation by working up brines; seawater or spent lyes · CPC title

• C01D7/26 Primary

  by precipitation or adsorption · CPC title

• C01F11/24

  Chlorides · CPC title