Method and System for Preparing Lithium Carbonate from Lithium Ore

Abstract

Disclosed by the invention is a method for preparing lithium carbonate from lithium ore, comprising the steps of: preparing lithium sulfate leachate from lithium ore concentrate, removing Fe2+ and Al3+ from the lithium sulfate leachate by adding alkali, removing Ca2+ and Mg2+ from the lithium sulfate leachate by an ion exchange method, adding a saturated solution of soda ash into the obtained concentrated solution of lithium sulfate leachate, precipitating lithium carbonate, filtering and separating the lithium carbonate precipitate, washing with hot water and drying to obtain a finished lithium carbonate product. The invention saves the production cost, and obviously improves the purity of lithium carbonate as a final product. In addition, disclosed by the invention is also a system for realizing the method for preparing lithium carbonate from lithium ore.

Description

TECHNICAL FIELD

The invention relates to the technical field of lithium salt production process, in particular to a method and a system for preparing lithium carbonate from lithium ore.

BACKGROUND

Salt lake brine and lithium ore are main raw materials for preparing lithium carbonate. In recent years, China has actively exploited lithium resources in salt lakes, but made slow progress due to the limitation of resources and technology. So, lithium is mainly extracted from lithium ore in China. The lithium ore for this purpose generally refers to lithium-containing ores such as lithium ore, lepidolite and montebrasite.

In the prior art, the sulfuric acid process with high recovery rate is mainly used for preparing lithium carbonate from lithium ore, comprising the steps of roasting lithium ore, preparing lithium sulfate leachate, treating lithium sulfate leachate and precipitating lithium; according to the above process, purification and concentration of lithium sulfate leachate directly affect the final quality of lithium carbonate products. A series of steps adopted by most manufacturers for treating lithium sulfate leachate include impurity removal, filtration, evaporation and concentration. In particular, the impurity removal mainly refers to removing Fe²⁺, Al³⁺, Ca²⁺, Mg²⁺ and other ions from the lithium sulfate leachate by adding a large amount of alkali, which will affect the purity of the obtained lithium carbonate. So, this step is directly related to the final lithium carbonate product quality. In the prior art, the method for removing impurities by adding a large amount of alkali will affect the production benefit and cost to a certain extent, make the final impurity removal incomplete, and result in unstable quality of the lithium carbonate product.

The applicant disclosed a new process for producing lithium salt by sulfuric acid process in Chinese patent document CN106044804A, in which the impurity removal of lithium sulfate leachate was achieved mainly by the ion exchange method or nanofiltration membrane method; specifically, Fe²⁺, Al³⁺, Ca²⁺ and Mg²⁺ were removed from lithium sulfate leachate by the ion exchange method, which completely replaced the original impurity removal method by adding a large amount of alkali, and could improve the quality of lithium carbonate products to a certain extent. However, the production cost of the above method is higher than that of the method by adding alkali, and the service life of ion exchange resin used in the ion exchange method is short, which further increases the production cost. No matter whether the ion exchange time is prolonged or the amount of ion exchange resin is changed, the quality of the obtained lithium carbonate product cannot be further improved.

SUMMARY

The main purpose of the invention is to provide a method and a system for preparing lithium carbonate from lithium ore, so as to solve the problem of low product quality in the process of preparing lithium carbonate from lithium ore in the prior art.

The technical problem to be solved by the invention is to provide a method for preparing lithium carbonate from lithium ore, comprising the steps of:

• • 1) preparing lithium sulfate leachate from lithium ore concentrate;
  • 2) adjusting the pH value of the lithium sulfate leachate to 9-10 by adding alkali, and precipitating Fe²⁺ and Al³⁺ in the lithium sulfate leachate;
  • 3) filtering the lithium sulfate leachate obtained in 2) and removing Fe²⁺ and Al³⁺ precipitates therefrom;
  • 4) treating the filtered lithium sulfate leachate by an ion exchange method and removing Ca²⁺ and Mg²⁺ therefrom;
  • 5) performing membrane concentration on the lithium sulfate leachate obtained by the ion exchange treatment to produce a concentrated solution of lithium sulfate leachate, wherein the concentration of Fe²⁺, Al³⁺, Ca²⁺ and Mg²⁺ in the concentrated solution is less than 0.0005%, 0.0005%, 0.0024% and 0.0040% respectively, and the concentration of lithium sulfate in the concentrated solution is 15-20%; and
  • 6) adding a saturated solution of soda ash into the concentrated solution of lithium sulfate leachate obtained in 5), precipitating lithium carbonate, filtering and separating the lithium carbonate precipitate, washing with hot water and drying to obtain a finished lithium carbonate product.

According to the method for preparing lithium carbonate from lithium ore in the invention, Fe²⁺ and Al³⁺ are removed in the alkali addition process at the previous stage, which improves the purity of lithium carbonate as a final product, and avoids the loss of the exchange capacity of ion exchange resin after being oxidized in the presence of Fe²⁺ and structurally changed. Then, Fe²⁺ and Al³⁺ precipitates are firstly filtered, which can avoid the poisoning of inorganic matters of ion exchange resin when ion exchange resin channels are blocked by these precipitates, and ensure the effectiveness of ion exchange resins. The ion exchange method is used in the later stage of the invention, which can remove Ca²⁺ and Mg²⁺ from the lithium sulfate leachate more thoroughly, and improve the purity of the final lithium carbonate product.

Further, the suspended matter in the lithium sulfate leachate is removed and the pH value thereof is adjusted before the lithium sulfate leachate is concentrated in 5).

Further, the membrane concentration process in 5) comprises ultrafiltration membrane filtration and reverse osmosis filtration.

In addition, disclosed by the invention is a system for preparing lithium carbonate from lithium ore, comprising a Li₂SO₄ leachate production system, a lithium precipitation system and a drying system. The system for preparing lithium carbonate from lithium ore comprises a precision filtration device, an ion exchange device and a membrane concentration filtration system sequentially connected, a liquid inlet of the precision filtration device is connected with a liquid outlet of the Li₂SO₄ leachate production system, and a concentrated solution outlet of the membrane concentration filtration system is sequentially connected with the lithium precipitation system and the drying system.

In the invention, Li₂SO₄ leachate is filtered by a precision filtration device for precise filtration, which shows a better filtration effect compared with the plate and frame filter in the prior art. The ion exchange resin can remove Ca²⁺ and Mg²⁺ with simple process and better removal effect. Then, the membrane concentration filtration system replaces the original evaporation concentration system, thus reducing the production energy consumption and improving the product quality. It can be seen that the invention reveals better treatment effect on Li₂SO₄ leachate, simpler structure and lower production cost compared with the prior art. The system for preparing lithium carbonate from lithium ore can realize the method for preparing lithium carbonate from lithium ore, and is suitable for the production process of lithium carbonate by the sulfuric acid process.

Further, the membrane concentration filtration system comprises an ultrafiltration membrane filtration device and at least one-stage disk-tube reverse osmosis membrane filtration device sequentially connected. The ultrafiltration membrane filtration device mainly intercepts macromolecular particulate matter, which is then concentrated in the single-stage or multi-stage disk-tube reverse osmosis membrane filtration device. The water produced by the whole system can return to the production system for use, and the concentration of Li₂SO₄ after concentration can reach 15-20%.

Further, the ultrafiltration membrane filtration device is capable of intercepting substances with molecular weight greater than 2000 and diameter of 0.005-0.05 μm. In this case, the ultrafiltration membrane filtration device has a better interception effect on macromolecular particulate matter.

Further, the disk-tube reverse osmosis membrane filtration device is capable of intercepting substances with molecular weight of 50-150 and diameter of 0.0001-0.001 μm. In this case, the disk-tube reverse osmosis membrane filtration device reveals the best concentration effect on filtered Li₂SO₄ leachate.

Further, the precision filtration device is capable of intercepting substances with diameter greater than 0.1 μm. In this case, most of the solid impurities in Li₂SO₄ leachate can be intercepted.

Further, a pretreatment device is arranged between the ion exchange device and the membrane concentration filtration system. The pretreatment device ensures the quality of liquid entering the membrane concentration filtration system.

Further, the pretreatment device comprises a primary filtration device and a pH adjustment device, which are used to control the impurity concentration and pH of Li₂SO₄ leachate entering the membrane concentration filtration system, and ensure a better concentration effect.

The invention will be further described in combination with drawings and preferred embodiments. Some additional aspects and advantages of the invention will be described in the following paragraphs and can be obvious through the description below or learned through the practice of the invention.

BRIEF DESCRIPTION OF DRAWINGS

The drawings described here are used for further understanding of the invention, and form a part thereof. The contents provided in the drawings and their related descriptions in the invention are used to explain the invention, but not improperly limit thereto. In the drawings:

FIG. 1 is a flow diagram of the devices relating to the method and system for preparing lithium carbonate from lithium ore of the invention.

Relevant marks in the above drawings are as follows:

1: Precision filtration device;

2: Ion exchange device;

3: Pretreatment device;

4: Ultrafiltration membrane filtration device;

5: Disk-tube reverse osmosis membrane filtration device;

6: Li₂SO₄ leachate production system;

7: Lithium precipitation system;

8: Drying system.

DETAILED DESCRIPTION

The invention will be clearly and completely described in combination with drawings. Those skilled in the art will be able to implement the invention based on these descriptions. Before the invention is described with reference to the drawings, it should be particularly noted that:

In the invention, the technical solutions and technical features provided in various parts, including the following description, can be combined with each other without conflict.

In addition, the embodiments of the invention referred to in the following description are generally only part of embodiments of the invention, but not all embodiments. Therefore, based on the embodiments of the invention, all other embodiments obtained by those skilled in the art without creative work shall fall within the protection scope of the invention.

With respect to terms and units in the invention, the terms “comprising”, “having” and any variations thereof in the specification, claims and related parts of the invention are intended to cover non-exclusive inclusion.

The invention provides a method for preparing lithium carbonate from lithium ore, comprising the steps of:

• • 1) preparing lithium sulfate leachate from lithium ore concentrate, wherein the specific preparation process of lithium sulfate leachate is based on the prior art, and the preparation process of lithium sulfate leachate in this specific embodiment is as follows: roasting and cooling lithium ore concentrate to obtain lithium ore calcine; grinding lithium ore calcine to obtain lithium ore powder; adding sulfuric acid into lithium ore powder, and roasting to obtain acid clinker; adding calcium carbonate into acid clinker to obtain a mixture, adding water into the mixture, and filtering when the pH value of the mixture is 5.5-6.0 to obtain lithium sulfate leachate;
  • 2) adjusting the pH value of the lithium sulfate leachate to 9-10 by adding alkali, and precipitating Fe²⁺ and Al³⁺ in the lithium sulfate leachate;
  • 3) filtering the lithium sulfate leachate obtained in 2) and removing Fe²⁺ and Al³⁺ precipitates therefrom;
  • 4) treating the filtered lithium sulfate leachate by an ion exchange method and removing Ca²⁺ and Mg²⁺ therefrom;
  • 5) performing membrane concentration on the lithium sulfate leachate obtained by the ion exchange treatment to produce a concentrated solution of lithium sulfate leachate, wherein the concentration of Fe²⁺, Al³⁺, Ca²⁺ and Mg²⁺ in the concentrated solution is less than 0.0005%, 0.0005%, 0.0024% and 0.0040% respectively, and the concentration of lithium sulfate in the concentrated solution is 15-20%; and
  • 6) adding a saturated solution of soda ash into the concentrated solution of lithium sulfate leachate obtained in 5), precipitating lithium carbonate, filtering and separating the lithium carbonate precipitate, washing with hot water and drying to obtain a finished lithium carbonate product.

The suspended matter in the lithium sulfate leachate is removed and the pH value thereof is adjusted before the lithium sulfate leachate is concentrated in 5).

The membrane concentration process in 5) comprises ultrafiltration membrane filtration and reverse osmosis filtration.

The invention is described in detail below by comparing several groups of methods for preparing lithium carbonate from lithium ore and the method for preparing lithium carbonate from lithium ore in the invention:

Comparative experiment 1: Lithium sulfate leachate was prepared from lithium ore concentrate, and then only a large amount of alkali was added to the lithium sulfate leachate to remove impurities therefrom;

Comparative experiment 2: Lithium sulfate leachate was prepared from lithium ore concentrate, and then lithium carbonate leachate was purified by the ion exchange method.

Example 1: The method for preparing lithium carbonate from lithium ore of the invention was used.

Table 1 compares the experimental effects of the above three groups of experimental methods:

			Ion concentration
			of lithium sulfate
			leachate after
Experimental			impurity removal
method	Experimental effect	Production cost	(%)
Comparative	The experiment could not	The reagent cost was a factor	c(Fe2+) < 0.0005
experiment 1	guarantee the impurity removal	that must be considered. The	c(Al3+) < 0.0005
	effect due to complex system	treatment cost of this method	c(Ca2+) < 0.0027
	equipment and many process	was the highest among the three	c(Mg2+) < 0.0045
	steps.	methods, which was about 240-
		340 yuan/ton of water.
Comparative	Ionic resin was prone to “iron	The recycling rate of resin was	c(Fe2+) < 0.0005
experiment 2	poisoning” due to the existence	low, which indirectly increased	c(Al3+) < 0.0005
	of iron ions. Thus, resin was	the treatment cost, about 150-	c(Ca2+) < 0.0026
	deactivated and could not be	270 yuan/ton of water.	c(Mg2+) < 0.0043
	recycled, which increased the
	treatment cost. The resin should
	be treated as solid waste.
Example	Less process steps;	This method could reduce the	c(Fe2+) < 0.0005
1	Ensure recycling rate of the	treatment cost and ensure the	c(Al3+) < 0.0005
	resin;	ion removal rate, with low risk	c(Ca2+) < 0.0024
	Impurity removal effect superior	of resin poisoning and high	c(Mg2+) < 0.0040
	to the previous two methods.	recycling rate. Its treatment cost
		was the lowest among the three
		methods, about 120-200 yuan
		per ton of water.

According to Table 1, Example 1 of the invention has the best experimental effect, the lowest production cost, and the highest quality of lithium carbonate products produced from lithium sulfate leachate. The above ion concentration refers to the mass ratio of ion to lithium sulfate leachate.

In Example 1, the concentration of lithium sulfate in the concentrated solution in 5) was changed to 15%, 18% and 20% as three groups of examples, and the final experimental effect was the same as that in Example 1.

The term “precision filtration” refers to a filtration treatment process for removing fine suspended matters or colloidal particles from water that cannot be filtered by sand filtration. It is often used for water treatment as a pretreatment device for preparing ultrapure water.

The embodiment of the invention further provides a system for preparing lithium carbonate from lithium ore. As shown in FIG. 1, the system for preparing lithium carbonate from lithium ore in this specific embodiment comprises a Li₂SO₄ leachate production system 6, a precision filtration device 1, an ion exchange device 2, a pretreatment device 3, an ultrafiltration membrane filtration device 4, a disk-tube reverse osmosis membrane filtration device 5, a lithium precipitation system 7 and a drying system 8 that are sequentially connected.

Further, the pretreatment device 3 comprises a primary filtration device and a pH adjustment device. The precision filtration device 1 is a filtration device with filtering temperature being controlled at 50-70° C.

Preferably, the precision filtration device 1 is capable of intercepting substances with diameter greater than 0.1 μm; the ultrafiltration membrane filtration device 4 is capable of intercepting substances with molecular weight greater than 2000 and diameter of 0.005-0.05 μm; and the disk-tube reverse osmosis membrane filtration device 5 is capable of intercepting substances with molecular weight of 50-150 and diameter of 0.0001-0.001 μm.

The Li₂SO₄ leachate production system 6 is mainly used to obtain Li₂SO₄ leachate after finely grinding lithium ore concentrate, roasting, adding sulfuric acid and CaCO₃.

The lithium precipitation system 7 is mainly used to obtain a liquid containing lithium carbonate solid by controlling the temperature of Li₂SO₄ concentrated solution produced by the disk-tube reverse osmosis membrane filtration device 5 at 85-95° C. and adding saturated Na₂CO₃ solution. The liquid containing lithium carbonate solid is subject to solid-liquid separation and dried by the drying system 8 to obtain a Li₂CO₃ finished product.

Based on the system for preparing lithium carbonate from lithium ore in this specific embodiment, Li₂SO₄ leachate is filtered by a precision filtration device 1 for precision filtration, which showed a better filtration effect compared with the plate and frame filter in the prior art. The ion exchange resin in the ion exchange device 2 can remove Ca²⁺ and Mg²⁺ with simple process and better removal effect. Then, the primary filtration device and pH adjustment device as the pretreatment devices are used to control impurity concentration and pH of Li₂SO₄ leachate entering the membrane concentration and filtration system. Finally, the ultrafiltration membrane filter device 4 and disk-tube reverse osmosis membrane filtration device 5 replace the original evaporation concentration system, thus reducing the production energy consumption and improving the product quality.

The system for preparing lithium carbonate from lithium ore in this embodiment requires the use of ion exchange resin in the ion exchange device, which can remove Ca²⁺ and Mg²⁺ more thoroughly compared with the prior art. Instead of the evaporation process, the membrane concentration filtration system can reduce energy consumption and save cost, and allow the produced water to be reused in the production system. The system can be widely applied to purification and concentration treatment in the lithium salt production industry by the sulfuric acid process, reveal low operation cost and simple control, and avoid secondary pollution to the environment.

The relevant contents of the invention are as described above. Those skilled in the art will be able to implement the invention based on these descriptions. Based on the above contents of the invention, all other examples obtained by those skilled in the art without creative work shall fall within the protection scope of the invention.

The above mentioned embodiments are only preferred embodiments of the invention and not used to limit the invention. Any modification, equivalent replacement and improvement made according to the spirit and rule of the invention can be incorporated in the protection scope of the invention.

The relevant contents of the invention are as described above. Those skilled in the art are able to implement the invention based on these descriptions. The above contents of the invention can be obtained by those skilled in the art without making creative work.

Claims

1-10. (canceled)

11. A system for preparing lithium carbonate from lithium ore, comprising: a leachate production system (6) to produce Li2SO4 leachate from lithium ore;a lithium precipitation system (7) for precipitating wet Li2CO3 from a concentrated Li2SO4 leachate; anda drying system (8) to produce a Li2CO3 finished product from the wet Li2CO3, characterized in that the system comprises:a precision filtration device (1) to remove Fe2+ and Al3+ from the Li2SO4 leachate and produce a filtered Li2SO4 leachate;an ion exchange device (2) to remove Ca2+ and Mg2+ from the filtered Li2SO4 leachate and produce a deionized Li2SO4 leachate; anda membrane concentrator (4,5) to produce the concentrated Li2SO4 leachate from the deionized Li2SO4 leachate, whereinthe concentrated Li2SO4 leachate from the membrane concentrator is provided to the lithium precipitation system and the drying system to produce the Li2CO3 finished product.

12. The system of claim 11, further comprising: a pretreatment device (3) to ensure a quality of the deionized Li2SO4 leachate entering the membrane concentrator.

13. The system of claim 12 wherein the pretreatment device comprises a primary filtration device to control an impurity concentration of the deionized Li2SO4 leachate entering the membrane concentrator.

14. The system of claim 12 wherein the pretreatment device comprises a pH adjustment device to control a pH of the deionized Li2SO4 leachate entering the membrane concentrator.

15. The system of claim 11, wherein the membrane concentrator comprises an ultrafiltration membrane filtration device (5) followed by a disk-tube reverse osmosis membrane filtration device (5).

16. The system of claim 15 wherein the disk-tube reverse osmosis membrane filtration device is a single stage device.

17. The system of claim 15 wherein the disk-tube reverse osmosis membrane filtration device is a multi-stage device.

18. The system of claim 15 wherein the ultrafiltration membrane filtration device is operative to intercept substances with molecular weight greater than 2000 and diameter of 0.005-0.05 μm.

19. The system of claim 15 wherein the disk-tube reverse osmosis membrane filtration device is operative to intercept substances with molecular weight 50-150 and diameter of 0.0001-0.001 μm.

20. The system of claim 11, wherein the membrane concentrator emits concentrated Li2SO4 leachate having a concentration of at least 15%.

21. The system of claim 11, wherein the membrane concentrator emits concentrated Li2SO4 leachate having a concentration between 15% and 20%.

22. The system of claim 11 wherein the precision filtration device removes Fe2+ and Al3+ from the Li2SO4 leachate by a process comprising: adding alkali to adjust a pH of the Li2SO4 leachate and cause precipitation of the Fe2+ and Al3+; andfiltering the Fe2+ and Al3+ precipitates to produce the filtered Li2SO4 leachate.

23. The system of claim 22 wherein adding alkali to adjust the pH of the Li2SO4 leachate is adding alkali to adjust the pH of the Li2SO4 leachate to between 9 and 10.

24. The system of claim 11 wherein the ion exchange device removes Ca2+ and Mg2+ from the filtered Li2SO4 leachate by a process comprising: exposing the filtered Li2SO4 leachate to an ion exchange resin.

25. The system of claim 11 wherein the filtered Li2SO4 leachate has a concentration of Fe2+ of less than 0.005% and a concentration of Al3+ of less than 0.005%.

26. The system of claim 11 wherein the deionized Li2SO4 leachate has a concentration of Ca2+ of less than 0.0024% and a concentration of Mg2+ of less than 0.0040%.

27. The system of claim 11 wherein the lithium precipitation system produces wet Li2CO3 from the concentrated Li2SO4 leachate by a process comprising: adding a saturated solution of soda ash into the concentrated Li2SO4 leachate to precipitate lithium carbonate; andwashing the lithium carbonate with hot water to produce wet Li2CO3.