US2004202934A1PendingUtilityA1

Li4Ti5O12, Li(4-alpha)Zalpha Ti5O12 or Li4ZbetaTi(5-beta)O12 particles, processes for obtaining same and use as electrochemical generators

Assignee: HYDRO QUEBEC 75 BOULEVARD RENEPriority: Dec 5, 2000Filed: Apr 23, 2004Published: Oct 14, 2004
Est. expiryDec 5, 2020(expired)· nominal 20-yr term from priority
H01G 11/86H01G 11/50H01G 11/06H01G 11/46Y02E60/10C01P 2004/64H01M 10/0525H01M 2300/0082H01M 4/131C01P 2004/03C01G 23/005C01P 2002/88H01M 4/745H01M 4/525H01M 4/366H01M 10/0565H01M 4/625H01M 2300/004H01M 4/5825H01M 4/661H01M 4/505H01M 10/0562B82Y 30/00Y02E60/13Y10T428/2982H01M 2300/0085H01M 4/485H01M 4/136H01M 4/0471C01P 2002/77C01G 23/003Y02P70/50H01M 4/623C01P 2006/40H01M 4/02H01G 11/04
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Claims

Abstract

Synthesis process for new particles of Li 4 Ti 5 O 12 , Li (4−α) Z α Ti 5 O 12 or Li 4 Z β Ti (5−β) O 12 , preferably having a spinel structure, wherein β is greater than 0 and less than or equal to 0.5 (preferably having a spinel structure), α representing a number greater than zero and less than or equal to 0.33, Z representing a source of at least one metal, preferably chosen from the group made up of Mg, Nb, Al, Zr, Ni, Co. These particles coated with a layer of carbon notably exhibit electrochemical properties that are particularly interesting as components of anodes and/or cathodes in electrochemical generators.

Claims

exact text as granted — not AI-modified
1 - 42 . (canceled)  
     
     
         43 . A process for synthesizing Li 4 Ti 5 O 12  particles coated with carbon, wherein said particles comprise from 0.01 to 10% by weight of carbon, the quantity of carbon being expressed with respect to the total weight of the Li 4 Ti 5 O 12  particles, said process comprising the steps of: 
 a) preparing a dispersion of a ternary mixture of TiO x —Li z Y-carbon, wherein 
 x is a number between 1 and 2,  
 z is 1 or 2, and  
 Y is a radical selected from the group consisting of CO 3 , OH, O, TiO 3  and mixtures thereof; and  
   b) heating the dispersion;    wherein the operating conditions are chosen in such a way as to yield a conversion of the initial products into Li 4 Ti 5 O 12 .    
     
     
         44 . A process for synthesizing particles of Li (4−α) Z α Ti 5 O 12  coated with carbon, wherein α is a number greater than zero and less than or equal to 0.33 and Z is a source of at least one metal, wherein said particles contain from 0.01 to 10% by weight of carbon, the quantity of carbon being expressed with respect to the total weight of the Li (4−α) Z α Ti 5 O 12  particles, said process comprising the steps of: 
 a) preparing a dispersion of an intimate ternary mixture of TiO x —Li z Y-carbon, wherein 
 x is a number between 1 and 2,  
 z is 1 or 2, and  
 Y is a radical chosen among CO 3 , OH, O and TiO 3  or a mixture thereof;  
 
 b) heating the dispersion; and  
 c) adding a source of at least one metal Z to the ternary mixture;  
 wherein the operating conditions are chosen in such a way as to yield a conversion of the initial products into Li (4−α) Z α Ti (5−β) O 12 .  
 
     
     
         45 . A process for sythesizing particles of the formula Li 4 Z β Ti 5 O 12 , wherein β is greater than 0 and less than or equal to 0.5, coated with carbon and Z is a source of at least one metal, said particles containing from 0.01 to 10% by weight of carbon, the quantity of carbon being expressed with respect to the total weight of the particles of Li 4 Z β Ti (5−β) O 12  formula; said process comprising the steps of: 
 a) preparing a dispersion of an intimate ternary mixture of TiO x —Li z Y -carbon, wherein 
 x is a number between 1 and 2,  
 z is 1 or 2, and  
 Y is a radical selected from the group consisting of CO 3 , OH, O and TiO 3  and mixtures thereof; and  
 
 b) heating the dispersion; and  
 c) adding a source of at least one metal Z to the ternary reaction mixture;  
 wherein the operating conditions are chosen in such a way as to yield a conversion of the initial products into Li 4 Z β Ti (5−β) O 12 .  
 
     
     
         46 . The process of  claim 43 , wherein the dispersion of the ternary mixture is heated at a temperature of about 600° C.  
     
     
         47 . The process of  claim 46 , wherein the dispersion is heated in two steps, the first step being carried out until the dispersion reaches a temperature of about 400° C. and the second step being carried out until the dispersion reaches a temperature of about 600° C.  
     
     
         48 . The process of  claim 47 , wherein the first step is carried out by rapid heating to around 400° C.  
     
     
         49 . The process of  claim 47 , wherein the second step is carried out by slow heating.  
     
     
         50 . The process of  claim 47 , wherein at least one step of step a) or step b) is carried out in air.  
     
     
         51 . The process of  claim 47 , wherein at least one step of step a) or step b) is carried out at least in part in inert atmosphere.  
     
     
         52 . The process of  claim 43 , wherein dispersion of the ternary mixture is prepared using water and/or at least one solvent.  
     
     
         53 . The process of  claim 43 , wherein the dispersion is carried out dry, without solvent.  
     
     
         54 . The process of  claim 43 , wherein the Li z Y compound comprises at least one compound selected from the group consisting of Li 2 O, Li 2 CO 3 , and LiOH.  
     
     
         55 . The process of  claim 54 , wherein the Li z Y compound comprises exclusively Li 2 CO 3 .  
     
     
         56 . The process of  claim 43 , wherein the dispersion is carried out by mechanical milling.  
     
     
         57 . The process of  claim 43 , wherein TiO x  is of the anatase or rutile TiO 2  type, or a mixture of both.  
     
     
         58 . The process of  claim 43 , wherein the compound Li z Y comprises Li 2 TiO 3 .  
     
     
         59 . The process of  claim 43 , wherein the carbon is: 
 selected from the group consisting of natural or artificial graphite, carbon black, Shawinigan black, Ketjen black and cokes and is added to the reaction mixture;    produced in the course of said process; or    produced at the surface of the particles by calcination of an organic and/or inorganic material deposited, in the course of said process, on the surface of the Li 4 Ti 5 O 12  and/or on the surface of the particles based on Li 4 Ti 5 O 12  and/or on the surface of at least one reagent used for the preparation of the dispersion of said ternary mixture.    
     
     
         60 . The process of  claim 43 , wherein the carbon is in the form of particles having a specific surface area greater than or equal to 2 m 2 /g.  
     
     
         61 . The process of  claim 43 , wherein the process is carried out in the presence of an atmosphere containing oxygen and wherein a part of the carbon present in the ternary mixture is consumed during said process.  
     
     
         62 . The process of  claim 43 , wherein a coating of carbon is obtained from the presence of a powder of Shawinigan carbon and/or at least one polymer.  
     
     
         63 . The process of  claim 57 , wherein the TiO 2  used as an initial product is coated with at least one inorganic material.  
     
     
         64 . The process of  claim 57 , wherein the TiO 2  used is coated with a hybrid inorganic-organic material.  
     
     
         65 . The process of  claim 43 , wherein the size of particles in the ternary mixture is between 100 nanometers and 10 micrometers.  
     
     
         66 . A particle obtained by the process of  claim 43 .  
     
     
         67 . A particle comprising a nucleus coated with carbon, wherein the nucleus of said particle is based on: 
 Li 4 Ti 5 O 12 ; and/or    Li (4−α) Z α Ti 5 O 12 , wherein α is greater than zero and less than or equal to 0.33 and wherein Z is a source of at least one metal; and/or    at least one compound of the formula Li 4 Z β Ti (5−β) O 2 , wherein β is greater than 0 and/or less than or equal to 0.5 and Z is a source of at least one metal.    
     
     
         68 . The particle of  claim 67 , wherein the nucleus comprises at least 65% of Li 4 Ti 5 O 12 , Li (4−α) Z α Ti 5 O 12 , Li 4 Z β Ti (5−β) O 12 , or a mixture thereof.  
     
     
         69 . The particle of  claim 68 , wherein the nucleus is exclusively made up of Li 4 Ti 5 O 12 , Li (4−α) Z α Ti 5 O 12 , Li 4 Z β Ti (5−β) O 12 , or a mixture thereof.  
     
     
         70 . The particle of  claim 67 , wherein said particle has a reversible capacity between 155 and 170 mAh/g.  
     
     
         71 . The particle of  claim 67 , wherein said particle comprises a nucleus of Li 4 Ti 5 O 12  particles coated with a carbon layer.  
     
     
         72 . The particle of  claim 67 , wherein said particle has a size between 10 and 950 nanometers.  
     
     
         73 . The particle of  claim 67 , wherein the size of the nucleus of said particle is between 10 and 500 nanometers.  
     
     
         74 . The particle of  claim 67 , wherein the thickness of the carbon coating is between 10 and 450 nanometers.  
     
     
         75 . A cathode of an electrochemical generator comprising at least one particle of  claim 67 .  
     
     
         76 . An anode for an electrochemical generator comprising at least one particle of  claim 67 .  
     
     
         77 . An electrochemical generator of the lithium type comprising an anode of the metallic lithium type and a cathode of  claim 75 , wherein said cathode is of the Li 4 Ti 5 O 12  type and/or of the Li (4−α) Z α Ti 5 O 12  type and/or of the Li 4 Z β Ti (5−β) O 12  type.  
     
     
         78 . An electrochemical generator of the lithium-ion type comprising an anode of  claim 76 , wherein said anode is of the Li 4 T 5 O 12  type and/or the Li (4−α) Z α Ti 5 O 12  type and/or the Li 4 Z β Ti (5−β) O 12 , and a cathode of the LiFePO 4 , LiCoO 2 , LiMn 2 O 4  and/or LiNiO 2  type.  
     
     
         79 . An electrochemical generator of  claim 77 , wherein the anode and/or the cathode are equipped with a current collector of solid aluminum or of expanded metal (Exmet) type.  
     
     
         80 . An electrochemical generator of  claim 77 , wherein said generator does not require any prior forming of the battery.  
     
     
         81 . A hybrid-type supercapacitor comprising an anode of  claim 76 , wherein said anode is of the Li 4 Ti 5 O 12  type and/or the Li (4−α) Z α Ti 5 O 12  type and/or the Li 4 Z β Ti (5−β) O 12  and a cathode of the graphite or carbon type with a specific surface area, and wherein the supercapacitor does not require any preliminary formation.  
     
     
         82 . The supercapacitor of  claim 80 , wherein the anode and/or the cathode are equipped with a current collector of solid aluminum or of expanded metal (Exmet) type.  
     
     
         83 . A generator of  claim 77 , further comprising a dry polymer, gel, liquid, or ceramic electrolyte.  
     
     
         84 . A supercapacitor of  claim 81 , further comprising a dry polymer, gel, liquid, or ceramic electrolyte.  
     
     
         85 . The process of  claim 43 , wherein the concentration of components of the ternary mixture submitted to dispersion is chosen in such a way as to yield a conversion of the initial products into Li 4 Ti 5 O 12 .  
     
     
         86 . The process of  claim 44 , wherein the concentration of components of the ternary mixture submitted to dispersion is chosen in such a way as to yield a conversion of the initial products into Li (4−α) Z α Ti 5 O 12 .  
     
     
         87 . The process of  claim 45 , wherein the concentration of components of the ternary mixture submitted to dispersion is chosen in such a way as to yield a conversion of the initial products into Li 4 Z β Ti (5−β) O 12 .

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