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Method for preparing large-particle lithium carbonate from salt lake lithium-rich brine

A technology of large particles and lithium carbonate, which is applied in the direction of lithium carbonate; Effect of improving purity and yield

Active Publication Date: 2019-09-10
QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In the prior art, the purity and yield of lithium carbonate primary products are low, which causes problems such as long-term refining and carbonization process flow, high equipment requirements and high energy consumption.
The lithium carbonate particle size d (0.9) that existing technology produces: between 10-39 micron, because lithium carbonate particle is little, thereby caused yield and purity to be low, in actual production, the fluidity of lithium carbonate product is poor, "sticking wall "The phenomenon is serious, and the equipment loss rate is high

Method used

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  • Method for preparing large-particle lithium carbonate from salt lake lithium-rich brine
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  • Method for preparing large-particle lithium carbonate from salt lake lithium-rich brine

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Embodiment 1

[0066] A method for preparing large particles of lithium carbonate from salt lake lithium-rich brine, wherein the content of lithium ions in the lithium-rich brine of the salt lake is 2.52 wt%, the content of potassium ions is 0.25 wt%, the content of magnesium ions is 0.09 wt%, and the content of sodium ions is 0.74 wt%. wt%, the sulfate content is 0.08wt%.

[0067] Include the following steps:

[0068] Step 1: Stir and heat 180 g of salt lake lithium-rich brine to 78°C. After the heating is completed, maintain stirring and temperature and add 7.4 g of surfactant to the salt lake lithium-rich brine. The added mass of the surfactant per minute is the Said salt lake lithium-rich brine quality 0.35%, obtains the salt lake lithium-rich brine after pretreatment;

[0069] Described surfactant is the aqueous solution of polypropylene ammonium salt (molecular weight is 3~100,000 daltons), sodium lauryl sulfate and sodium hexametaphosphate, and the mass of polypropylene ammonium salt...

Embodiment 2

[0081] A method for preparing large particles of lithium carbonate from salt lake lithium-rich brine, wherein the content of lithium ions in the lithium-rich brine of the salt lake is 2.00 wt%, the content of potassium ions is 0.1 wt%, the content of magnesium ions is 0.08 wt%, and the content of sodium ions is 0.20 wt%. wt%, the sulfate content is 0.02wt%.

[0082] Include the following steps:

[0083] Step 1: Stir and heat 180 g of salt lake lithium-rich brine to 70°C. After heating, maintain stirring and temperature and add 10 g of surfactant to the salt lake lithium-rich brine. The mass of surfactant added per minute is the The quality of salt lake lithium-rich brine is 0.2%, and the pretreated salt lake lithium-rich brine is obtained;

[0084] Described surfactant is the aqueous solution of polypropylene ammonium salt (molecular weight is 3~100,000 daltons), sodium lauryl sulfate and sodium hexametaphosphate, and the mass of polypropylene ammonium salt in described surfa...

Embodiment 3

[0089] A method for preparing large particles of lithium carbonate from salt lake lithium-rich brine, wherein the content of lithium ions in the lithium-rich brine of the salt lake is 3.00 wt%, the content of potassium ions is 0.4 wt%, the content of magnesium ions is 0.1 wt%, and the content of sodium ions is 1.00 wt%. wt%, the sulfate content is 0.10wt%.

[0090] Include the following steps:

[0091] Step 1: Stir and heat 180 g of salt lake lithium-rich brine to 85°C. After the heating is completed, maintain stirring and temperature and add 10 g of surfactant to the salt lake lithium-rich brine. The added mass of the surfactant per minute is the The quality of salt lake lithium-rich brine is 0.5%, and the salt lake lithium-rich brine after pretreatment is obtained;

[0092] Described surfactant is the aqueous solution of polypropylene ammonium salt (molecular weight is 3~100,000 daltons), sodium lauryl sulfate and sodium hexametaphosphate, the quality of polypropylene ammon...

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Abstract

The invention discloses a method for preparing large-particle lithium carbonate from salt lake lithium-rich brine. The method comprises the following steps: step 1, heating the salt lake lithium-richbrine to 70-85 DEG C, after heating is completed, maintaining the temperature and adding a surfactant into the salt lake lithium-rich brine; step 2, maintaining the temperature in the step 1, adding acarbonate solution into the pre-treated salt lake lithium-rich brine, and performing a reaction for 1-3 h to obtain reaction product slurry; and step 3, allowing the reaction product slurry to standfor 10-20 h, performing solid-liquid separation, washing the obtained solid particles, and performing drying to obtain the large-particle lithium carbonate. According to the method provided by the invention, the certain surfactant is added into the reaction system, so that a particle size of the lithium carbonate is increased in the precipitation process, and the obtained lithium carbonate has a particle size d(0.9) of 300-600 [mu]m; and meanwhile impurity ions adsorbed at the surface of the lithium carbonate product are reduced, and purity and a yield of a primary product are improved, wherein the purity of the primary product is >=95%.

Description

technical field [0001] The invention belongs to the technical field of inorganic chemistry, and in particular relates to a method for preparing large-grain lithium carbonate from salt lake lithium-rich brine. Background technique [0002] The process route of lithium extraction from salt lake brine can be summarized as three processes: preparation of lithium-rich brine, purification process (deep impurity removal), and lithium carbonate precipitation; the purification process is divided into two processes, namely, magnesium-lithium separation and deep removal Miscellaneous, magnesium and lithium are generally separated by ion-exchange membrane electrodialysis. (Deep impurity removal) is to carry out Li + The separation process from impurity elements will directly affect the Li 2 CO 3 Product quality and yield. The lithium carbonate precipitation process is to add alkali to the purified lithium-rich solution to precipitate Li 2 CO 3 The product process that determines L...

Claims

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Application Information

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IPC IPC(8): C01D15/08
CPCC01D15/08C01P2006/80C01P2004/60
Inventor 马艳芳张志宏李成宝刘鑫李志伟苏彤张永明
Owner QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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