IP Library › Granted Patent US 9,711,789
Granted Patent B2
US 9,711,789 · App. 13/969,359 · Granted Jul 18, 2017

Supercritical continuous hydrothermal synthesis of lithium titanate anode materials for lithium-ion batteries

Inventors: Wenting Zhu (Anhui, CN); Maoping Yang (Anhui, CN); Xulai Yang (Anhui, CN); Xiaoming Xu (Anhui, CN); Jia Xie (Lake Jackson, TX); Zhen Li (Anhui, CN)
Assignee: Hefei Guoxuan High-Tech Power Energy Co., Ltd.
H01M4/485C01D15/02C01G23/005C01P2002/72H01M10/0525Y02P20/544
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Quick Facts
Patent No.
US 9,711,789
App. No.
13/969,359
Granted
Jul 18, 2017
Kind
B2
Abstract

A method for synthesizing lithium titanate includes preparing a supercritical fluid from water; reacting a solution containing lithium and titanium with the supercritical fluid under a condition that maintains the supercritical fluid in its supercritical state to produce a reaction mixture comprising the lithium titanate; and collecting the lithium titanate. The supercritical fluid is prepared at a temperature of 375-500° C. and a pressure of 22-35 MPa. The solution containing lithium and titanium is prepared by mixing a solution containing lithium, prepared by dissolving a lithium source in a selected solvent, and a solution containing titanium, prepared by dissolving a titanium source in the selected solvent, wherein a molar ratio of lithium:titanium is between 4.0:5.0 and 4.5:5.0. The lithium source is lithium hydroxide, lithium carbonate, lithium acetate, lithium oxalate, lithium nitrate, or lithium oxide, and the titanium source is tetrabutyl titanate.

Claims (22)

1. A method for synthesizing lithium titanate, comprising:

preparing a supercritical fluid from water in a first reactor;

reacting a solution comprising lithium and titanium in the pre-formed supercritical fluid under a condition that maintains the pre-formed supercritical fluid hi its supercritical state to produce a reaction mixture comprising the lithium titanate, wherein the solution comprising lithium and titanium is a premixed solution from a solution containing lithium and a solution containing titanium, wherein the reacting is conducted in a continuous fashion by pumping the solution comprising lithium and titanium and the pre-formed supercritical fluid into a second reactor, wherein a flow rate of water for the supercritical fluid is about 5-25 g/min and a flow rate for the solution is about 1.7-3.0 g/min; and

collecting the lithium titanate.

2. The method of claim 1 , wherein the solution comprising lithium is prepared by dissolving a lithium source in a selected solvent different from water, and the solution comprising titanium is prepared by dissolving a titanium source in the selected solvent.

3. The method of claim 2 , wherein the selected solvent is an alcohol.

4. The method of claim 2 , wherein the lithium source is selected from lithium hydroxide, lithium carbonate, lithium acetate, lithium oxalate, lithium nitrate, lithium oxide, or a combination thereof, and the titanium source is tetrabutyl titanate.

5. The method of claim 2 , wherein the solution comprising lithium and the solution comprising titanium are bubbled with an inert gas to remove a dissolved gas.

6. The method of claim 5 , wherein the inert gas is nitrogen.

7. The method of claim 1 , wherein the water is bubbled with an inert gas to remove a dissolved gas prior to the preparing the supercritical fluid.

8. The method of claim 7 , wherein the inert gas is nitrogen.

9. The method of claim 1 , further comprising cooling the reaction mixture or allowing the reaction mixture to cool prior to the collecting the lithium titanate.

10. The method of claim 1 , wherein the collecting the lithium titanate is by filtration or centrifugation.

11. The method of claim 1 , wherein the supercritical fluid is prepared at a temperature in a range of about 375-500° C. and a pressure in a range of about 22-35 MPa.

12. The method of claim 1 , wherein the supercritical fluid is prepared at a temperature of about 400° C. and a pressure of about 25 MPa.

13. The method of claim 1 , wherein a molar ratio of lithium:titanium in the solution is between about 4.0:5.0 and about 4.5:5.0.

14. The method of claim 1 , wherein a molar ratio of lithium:titanium in the solution is between about 4.0:5.0 and about 4.2:5.0.

15. The method of claim 1 , wherein a molar ratio of lithium:titanium in the solution is about 4.2:5.0.

16. The method of claim 1 , further comprising purifying the collected lithium titanate by:

suspending the collected lithium titanate in water to produce a suspension;

sonicating the suspension; and

centrifuging the suspension to collect purified lithium titanate.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 19, 2013
From: ZHU, WENTING; YANG, MAOPING; YANG, XULAI; XU, XIAOMING; XIE, JIA; LI, ZHEN
To: HEFEI GUOXUAN HIGH-TECH POWER ENERGY CO., LTD.
Reel/Frame 031038/0739 →
Priority Claims (1)
CN 2012 1 0385211 · Oct 12, 2012 · national
Continuity (1)
Related Publication 20140105811A1 · Apr 17, 2014