Li4Ti5O12, Li(4-alpha)Zalpha Ti5O12 or Li4ZbetaTi(5-beta)O12 particles, processes for obtaining same and use as electrochemical generators
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-modified1 - 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 .Join the waitlist — get patent alerts
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