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Total membrane separation method of producing lithium extracting mother liquor with multi-stage membrane concentration of salt lake brine

A technology of salt lake brine and lithium extraction mother liquor, which is applied in the field of membrane separation, can solve the problems of limited magnesium and lithium separation capacity, poor brine treatment effect, failure to obtain local materials, etc., and achieves wide water quality, is conducive to popularization and application, and flexible design Effect

Active Publication Date: 2018-07-24
西安金藏膜环保科技有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The Chinese patent application with the application number 201310571755.2 discloses the separation of magnesium ions and lithium ions through the nanofiltration system, the enrichment of lithium ions by the reverse osmosis system, and the evaporation and concentration of salt fields, which can make the concentration of lithium ions reach the concentration required for refining lithium carbonate; however, the application The series of the designed nanofiltration system is only one level, the separation capacity of magnesium and lithium is limited, and the treatment effect on brine with high magnesium-lithium ratio is not good, which has certain limitations; in addition, it still takes a long time to Salt field evaporation and further concentration can make the lithium ion concentration meet the requirements for lithium carbonate production
The Chinese patent application publication with the application number 201610751304.0 pointed out that the use of forward osmosis system can concentrate lithium-containing solution and enrich lithium ions. It is still necessary to add alkali to remove magnesium in depth, and to further concentrate the refined lithium-containing solution through high-energy multi-effect evaporation to increase the concentration of lithium ions; and the forward osmosis system uses ammonium bicarbonate solution as the drawing solution, which cannot be obtained locally and fully utilized Salt obtained from drying in salt pans

Method used

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  • Total membrane separation method of producing lithium extracting mother liquor with multi-stage membrane concentration of salt lake brine
  • Total membrane separation method of producing lithium extracting mother liquor with multi-stage membrane concentration of salt lake brine
  • Total membrane separation method of producing lithium extracting mother liquor with multi-stage membrane concentration of salt lake brine

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Embodiment approach

[0045] figure 1 A flow chart of the method of the present invention is given. The present invention has multiple implementations of the full-membrane separation process for the production of lithium-extracting mother liquor by multi-stage membrane concentration of salt lake brine, including the following steps:

[0046] (1) Use a microfiltration purification system to pretreat salt lake brine to remove suspended solids, colloids and other impurities, and then dilute it with fresh water 2 to 5 times to obtain microfiltration pretreated brine.

[0047] Among them, the magnesium-lithium ratio of salt lake brine is (10-1000):1 by mass ratio, the mass concentration of lithium ions is 0.1-5 g / L, and the pH value is 5-8.

[0048] The number of stages of the microfiltration purification system is 1 to 2, which is composed of one or two of the filtration precisions of 1 to 5 μm, 0.45 to 1 μm or 0.1 to 0.45 μm according to the pore size; The material of the filter membrane is one or m...

Embodiment 1

[0063] like figure 2 As shown, in this embodiment, a three-stage nanofiltration salt separation system, a forward osmosis and reverse osmosis system, and a nanofiltration deep magnesium removal system are selected. Include the following steps:

[0064] (1) The salt lake brine with pH=5 is pretreated using a microfiltration purification system, wherein the magnesium-lithium ratio of the salt lake brine is 281:1 by mass ratio, the mass concentration of lithium ions is 0.391g / L, and the pH value is 8. Remove suspended solids, colloids and other impurities, and then dilute 2.5 times with fresh water to obtain microfiltration pretreated brine.

[0065] Among them, the microfiltration purification system is composed of two microfiltration systems with a filtration precision of 2 μm and 0.45 μm in sequence, and the materials of the microfiltration membrane are polypropylene and polyvinyl chloride in sequence.

[0066] (2) Send the microfiltration pretreatment brine obtained in st...

Embodiment 2

[0080] like image 3 As shown, the present embodiment selects a two-stage nanofiltration salt separation system, which is one level less than the nanofiltration salt separation system in Example 1. Except for the following differences, other parts are the same as in Example 1. In this example:

[0081] (1) The pH of salt lake brine is 6.4, the mass concentration of magnesium ions is 51.75g / L, the mass concentration of lithium ions is 0.535g / L, and the ratio of magnesium to lithium (by mass ratio) is 100:1; diluted 5 times, microfiltration The purification system is composed of two microfiltration systems with a filtration precision of 1 μm and 0.1 μm in sequence, and the materials of the microfiltration membrane are polypropylene and polyvinylidene fluoride in sequence.

[0082] (2) present embodiment selects two-stage nanofiltration salt separation system for use, and the first stage nanofiltration salt separation system uses DT nanofiltration membrane, and its rejection rat...

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Abstract

The invention discloses a total membrane separation method of producing a lithium extracting mother liquor with multi-stage membrane concentration of salt lake brine. The total membrane separation method comprises the following steps of (1) using a microfiltration purification system to perform pretreatment on the salt lake brine, removing suspended matters, colloid and other impurities in the salt lake brine, and then diluting the salt lake brine with fresh water to acquire microfiltration pretreated brine; (2) feeding the obtained microfiltration pretreated brine into a nanofiltration salt separation system, and performing separation to acquire a filtrate with monovalent cation as a priority and a concentrated solution with multivalent cation as a priority; (3) feeding the filtrate in the step (2) into a membrane concentration system, and performing concentration to obtain a lithium-enriched concentrated solution; and (4) feeding the lithium-enriched concentrated solution obtained inthe step (3) into a nanofiltration deep magnesium removing system, and performing deep magnesium removal with a nanofiltration membrane to obtain the lithium extracting mother liquor. The technologyis low in energy consumption, high in recovery rate, low in production cost, continuous and controllable in technology, high in reliability, low in magnesium-lithium ratio of the prepared lithium extracting mother liquor, high in lithium ion concentration and stable in quality and can be used for large-scale production.

Description

technical field [0001] The invention belongs to the technical field of membrane separation, and in particular relates to a full-membrane separation process for producing lithium-extracting mother liquor through multi-stage membrane concentration of salt lake brine. Background technique [0002] Lithium and its compounds play an extremely important role in energy, petrochemical, metallurgy, ceramics, medicine, aerospace, refrigeration and other fields, and are called "energy metals in the 21st century". Salt lake brine is an important source of lithium. At present, more than 80% of the world's total lithium salt production comes from salt lake brine. [0003] At present, the main methods for extracting lithium from salt lake brine include evaporation crystallization separation method, precipitation method, calcination leaching method, organic solvent extraction method, ion exchange adsorption method, electrodialysis method, Xu's method and nanofiltration method, etc. The post...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01D15/00
CPCC01D15/00
Inventor 王磊王佳璇王旭东吕永涛陈立成
Owner 西安金藏膜环保科技有限公司
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