Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method for combined extracting boron, magnesium and lithium from salt lake bittern

A technology of combined extraction and salt lake brine, applied in the field of magnesium, lithium, and boron joint extraction, can solve the problems of lithium carbonate containing many impurities, low resin utilization rate, high energy consumption, etc., achieve good filtration and washing performance, and save production energy consumption , The effect of small system logistics

Inactive Publication Date: 2009-08-19
WESTERN MINING GROUP +1
View PDF2 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The feature of this method is that no additional chemical reagents are needed for the separation of magnesium and lithium, but the energy consumption is high, the recovery rate of lithium is low, and the lithium carbonate produced contains many impurities; the magnesium hydroxide obtained by the hydration of magnesium oxide has very poor filtration and washing performance. Moreover, it contains a large amount of boron; it should be pointed out that 100 tons of low-concentration hydrochloric acid should be produced as a by-product for every 1 ton of lithium carbonate produced. If the place of origin cannot digest it, it will be very difficult to store and transport; (2) Carbonate precipitation method (2) Industrial soda ash Na 2 CO 3 When added to brine, the following reaction occurs: Na 2 CO 3 +2Li + -Li 2 CO 3 ↓+2Na + This method is used to extract lithium salt (Li 2 CO 3 ), this method is not suitable for the brine with high ratio of magnesium to lithium, because it is very uneconomical to remove magnesium with a large amount of soda ash before extracting lithium; (3) the adsorption method utilizes artificial resin to directly add in the brine to absorb Li + , the resin utilization rate of this method is low, and the adsorption effect is lost after only 2 to 3 times, so this method is not economical, and large-scale production is still a problem; (4) organic solvent extraction method uses tributyl phosphate to extract the Lithium, there are two problems in this method, one is high cost, and the other is that organic solvents cause serious environmental pollution to the salt lake area; President J.Hsu (Xu Jinghua) used the "evaporation pump principle" and the in-situ "chemical reaction pool method" to carry out indoor and field lithium extraction experiments on the old brine discharged from the Qinghai Qerhan Salt Lake Potash Plant in my country and achieved some success. There are also two problems, one is magnesium bischofite (MgCl 2 .6H 2 O) crystallization output, the value is not high, the 2nd, in the process of evaporating and concentrating, though the lithium that is mixed in bischofolite is not high in relative content (0.98%), but absolute content is big, so the loss of lithium is big, and extraction rate (5) Membrane separation method uses membranes made of special materials to separate magnesium and lithium, and then use sodium carbonate and sodium hydroxide to remove magnesium in depth, and then use sodium carbonate to convert lithium carbonate. The main problem is that the membrane used to separate magnesium and lithium needs to be imported from abroad, and the service life of the membrane needs to be tested in production practice. On the other hand, the power consumption is also very high.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for combined extracting boron, magnesium and lithium from salt lake bittern

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] (1) Use brine near saturated magnesium chloride after evaporation and concentration of salt fields to remove most of the sodium and potassium as raw material, wherein the content of diboron trioxide is 2-4%, the concentration of magnesium ions is about 80-120g / L, and the concentration of lithium ions is about 3-4%. 8g / L; purification of raw brine

[0042] (2) With the raw material brine containing boron, magnesium, lithium, remove impurities such as silt and other solid suspended matter by filter press filter, make raw material brine be purified;

[0043] (3) Sulfuric acid or hydrochloric acid method for boric acid

[0044] In an enamel reactor with an effective volume of 10000L, add 9m 3 The purified brine is heated, and when heated to a temperature of 55°C, slowly add 180 L of concentrated sulfuric acid, stirring while adding, and continue stirring for about 1 hour after the addition, and then cooling. When cooled to 15°C, filter and separate with a centrifuge or a ...

Embodiment 2

[0058] (1) Use brine near saturated magnesium chloride after evaporation and concentration of salt fields to remove most of the sodium and potassium as raw material, wherein the content of diboron trioxide is 2-4%, the concentration of magnesium ions is about 80-120g / L, and the concentration of lithium ions is about 3-4%. 8g / L; purification of raw brine

[0059] (2) With the raw material brine containing boron, magnesium, lithium, remove impurities such as silt and other solid suspended matter by filter press filter, make raw material brine be purified;

[0060] (3) Sulfuric acid or hydrochloric acid method for boric acid

[0061] In an enamel reactor with an effective volume of 10000L, add 9m 3 Heating the raw material brine after purification, when the temperature is 60°C, slowly add 1000L concentrated hydrochloric acid, stirring while adding, continue stirring for about 0.5 hours after adding, and then cooling. When cooled to 0°C, use a centrifuge or a filter press to fil...

Embodiment 3

[0075] (1) Use brine near saturated magnesium chloride after evaporation and concentration of salt fields to remove most of the sodium and potassium as raw material, wherein the content of diboron trioxide is 2-4%, the concentration of magnesium ions is about 80-120g / L, and the concentration of lithium ions is about 3-4%. 8g / L; purification of raw brine

[0076] (2) With the raw material brine containing boron, magnesium, lithium, remove impurities such as silt and other solid suspended matter by filter press filter, make raw material brine be purified;

[0077] (3) Sulfuric acid or hydrochloric acid method for boric acid

[0078] In an enamel reactor with an effective volume of 10000L, add 9m 3 Heating the raw material brine after purification, when the temperature is 65°C, slowly add 250L of concentrated sulfuric acid, stirring while adding, continue stirring for about 0.5 hours after adding, and then cooling. When cooled to -5°C, use a centrifuge or a filter press to filter...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The present invention relates to the development and comprehensive utilization of salt lake resources, in particular to a kind of salt lake brine containing boron, magnesium, and lithium as raw materials, and adopts a combined separation and extraction process to prepare boric acid, magnesium hydroxide, lithium carbonate, and ammonium chloride respectively. A method for jointly extracting boron, magnesium and lithium from salt lake brine. The method of the present invention uses the brine containing boron, magnesium, lithium, etc. after being concentrated and removed most of sodium and potassium by the salt field method as raw material, and undergoes acidification treatment to prepare boric acid; magnesium precipitation by ammonia method; concentration by salt field method; magnesium precipitation by carbonate; Secondary magnesium precipitation mother liquor salt field method concentration; sodium hydroxide solution deep magnesium precipitation; sodium carbonate solution reaction method to prepare lithium carbonate. The recovery rates of boron, magnesium and lithium are over 87%, 95% and 92% respectively. The method has the characteristics of simple process, less investment in equipment, high resource utilization rate, high recovery rate of boron, magnesium and lithium, good product quality, low production cost, and no "three wastes", which fully meets the requirements of developing circular economy and improving the ecological environment of salt lakes. Require.

Description

technical field [0001] The present invention relates to the development and comprehensive utilization of salt lake resources, in particular to a kind of salt lake brine containing boron, magnesium, and lithium as raw materials, and adopts a combined separation and extraction process to prepare boric acid, magnesium hydroxide, lithium carbonate, and ammonium chloride respectively. A method for jointly extracting boron, magnesium and lithium from salt lake brine. Background technique [0002] my country is a country rich in salt lake resources. According to incomplete statistics, the area is greater than 1km 2 There are 813 inland salt lakes in China. Among them, there are 234 in Tibet, 71 in Qinghai, 375 in Inner Mongolia, and the rest are scattered in Jilin, Hebei, Shaanxi, Ningxia, Gansu and other provinces. Among the salt lake resources, potassium, sodium, magnesium, lithium, and boron are the most abundant resources. The reserves of potassium, sodium, magnesium, lithiu...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C01D15/08C01F5/14C01B35/10C01B21/09
Inventor 徐徽毛小兵李增荣石西昌庞全世陈白珍杨喜云王华伟
Owner WESTERN MINING GROUP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products