US20040202934A1 - Li4Ti5O12, Li(4-alpha)Zalpha Ti5O12 or Li4ZbetaTi(5-beta)O12 particles, processes for obtaining same and use as electrochemical generators - Google Patents

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

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US20040202934A1
US20040202934A1 US10/830,240 US83024004A US2004202934A1 US 20040202934 A1 US20040202934 A1 US 20040202934A1 US 83024004 A US83024004 A US 83024004A US 2004202934 A1 US2004202934 A1 US 2004202934A1
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carbon
particles
type
dispersion
mixture
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Karim Zaghib
Michel Gauthier
Fernand Brochu
Abdelbast Guerfi
Monique Masse
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Hydro Quebec
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Hydro Quebec
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Assigned to HYDRO QUEBEC reassignment HYDRO QUEBEC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ARMAND, MICHEL, GAUTHIER, MICHEL, BROCHU, FERNAND, GUERFI, ABDELBAST, MASSE, MONIQUE, ZAGHIB, KARIM
Priority to US11/808,353 priority Critical patent/US20070243467A1/en
Priority to US12/149,535 priority patent/US8114469B2/en
Priority to US13/360,173 priority patent/US9077031B2/en
Priority to US14/461,786 priority patent/US9559356B2/en
Priority to US15/252,944 priority patent/US10734647B2/en
Priority to US16/910,396 priority patent/US20200373570A1/en
Abandoned legal-status Critical Current

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Definitions

  • the present invention relates to new particles based on Li 4 Ti 5 O 12 , based on Li (4 ⁇ ) Z ⁇ Ti 5 O 12 , or based on Li 4 Z ⁇ Ti (5 ⁇ ) O 12 .
  • the present invention also relates to processes that make it possible to prepare these particles and to their use, especially in the area of electrochemical devices such as electrochemical generators.
  • Li-ion batteries Marketing of the lithium-ion battery by Sony, in 1990, was reported by Naguara and Tozawa, Prog. Batt. Solar Cells, 9 (1990), 209. It made possible an expansion and a significant breakthrough of batteries into the area of portable devices (telephone, computer).
  • the technology of Li-ion batteries is based on lithium intercalation electrodes, in particular the anode which is made of graphite.
  • a passivation film is formed on the carbon surface.
  • the chemistry and the composition of this passivation film are complex.
  • the electrochemical formation protocol for this film remains an industrial secret.
  • there is a volume variation of 10% which induces a discontinuity between the particles causing loosening of the interfaces between the electrode and the electrolyte, and between the electrode and the current collector.
  • Titanium oxide spinel Li 4 Ti 5 O 12 is a material for anodes promising for lithium-ion batteries due to its intercalation potential (K. Zaghib et al., 190 th Electrochemical Society Meeting, San Antonio, Abs. no. 93, 1996), cyclability, rapid charging-discharging at high current such as described by K. Zaghib et al. in Proceeding on Lithium Polymer Batteries, PV96-17, p. 223) in The Electrochemical Society Proceeding Series (1996), (K. Zaghib et al., J. Electro chem. Soc. 145, 3135, (1998) and in J. Power Sources, 81-82 (1999) 300-305).
  • the coefficient of diffusion of lithium in Li 4 T 5 O 12 is of a higher order of magnitude than the coefficient of diffusion of lithium in carbons (regarding this subject, see K. Zaghib et al., J. Power Sources, 81-82 (1999) 300-305). This characteristic distinguishes Li 5 Ti 5 O 12 from the other potential candidates for power applications, such as PNGV and GSM pulses.
  • the structure of Li 4 Ti 5 O 12 does not vary in volume, which makes this electrode very stable and thus safe.
  • This study was carried out by Ozhuku and reported in J. Electrochem. Soc., 140, 2490 (1993) by X-ray diffraction and by scanning microscopy in situ by Zayhib et al. (and reported in Proceeding on Lithium Polymer Batteries, PV96-17, p. 223 in The Electrochemical Society Proceeding Series (1996) and in J. Electro chem. Soc. 145, 3135, (1998).
  • the material Li 4 Ti 5 O 12 because of its lack of volume expansion (also called as zero volume expansion (ZEV)) has been easily used in polymer, ceramic or glass electrolyte batteries, which ensures good cycling stability.
  • ZV zero volume expansion
  • the good behavior of this anode at 1.5 V promotes the use of any type of liquid electrode, such as ethylene carbonate (EC), propylene carbonate (PC) or mixtures of these two.
  • EC ethylene carbonate
  • PC propylene carbonate
  • This operation potential increases the life span of the battery, especially for stand-by type applications because of its character as electrode without passivation film.
  • the use of Li 4 Ti 5 O 12 as an anode does not require any prior forming of the battery.
  • the Li 4 Ti 5 O 12 is mentioned as being able to be obtained by a binary mixture of a mixture of LiOH and TiO 2 where the synthesis temperature is greater than 600° C. Residual impurities of the TiO 2 , Li 2 TiO 3 and/or other type in the mixture limit the electrode capacity and limit the size of the particles.
  • the patent U.S. Pat. No. 6,221,531 describes a structure of the spinel type with the general formula Li[Ti 1.67 Li 0.33 ⁇ y M y ]O 4 , wherein Y ⁇ 0 ⁇ 0.33 with M representing magnesium and/or aluminum.
  • This structure is presented as useful for making up a negative electrode for a non-aqueous electrochemical cell and in a non-aqueous battery comprising a plurality of cells, connected electrically, each cell comprising a negative electrode, an electrolyte and a positive electrode, the negative electrode being made up of this spinel structure.
  • FIG. 1 illustrates the different applications of the Li 4 Ti 5 O 12 particles (coated with carbon or not) as anode or as cathode for batteries and supercapacitors.
  • FIG. 2 illustrates comparative performances of a process according to the invention compared with those of a classic process such as described in Prog. Batt. Solar Cells, 9 (1990), 209.
  • FIG. 3 illustrates the double role of carbon in the preparation process for new particles and in the composition of the carbon layer that coats them.
  • FIG. 4 illustrates a classic formation process for Li 4 Ti 5 O 12 (macroscopic particle), in the absence of carbon; this process makes it possible to obtain a spinel structure in the presence of impurities of a TiO 2 or other type. This structure is limited for electrochemical performance, to currents less than 2C.
  • FIG. 5 illustrates the same process illustrated in FIG. 4, with the exception of the reagent LiOH which is substituted by Li 2 CO 3 ; this type of process yields a formation of agglomerates of the Li 4 Ti 5 O 12 type.
  • FIG. 6 illustrates a process according to the invention for the formation of nano-particles of Li 4 Ti 5 O 12 from a ternary mixture LiOH-C-TiO 2 , intimately mixed at high energy, this mixture is heated at 400° C. then to 600° C. This type of process gives rise to the formation of nano-agglomerates of Li 4 T 5 O 12 .
  • FIG. 7 illustrates a process similar to the one shown in FIG. 6, with the exception that LiOH is substituted by Li 2 CO 3 ; this type of process leads to the formation of Li 4 Ti 5 O 12 nano-agglomerates.
  • FIG. 8 illustrates a process similar to the one illustrated in FIG. 7, by adding Li 2 CO 3 to the initial product; this type of process makes it possible to obtain Li 4 Ti 5 O 12 nano-agglomerates.
  • FIG. 9 illustrates a process similar to those shown in FIGS. 6 and 7, with the exception that calcination is carried out in an inert atmosphere; this type of process makes it possible to obtain Li 4 Ti 5 O 12 nano-agglomerates of Li 4 Ti 5 O 12 coated with carbon. This structure gives exceptional electrochemical performance at high current density (12C).
  • FIG. 10 illustrates the advantages of a pretreatment of the mixture milled at high energy. Dry process. Homogeneous precursor. Homogeneous specific surface area. Coating of particles with carbon. Direct contact of particle with carbon. Direct contact via carbon with the reactive particles. Carbon is a very good thermal conductor. Low contamination. Homogeneous dispersion. Acceleration or rapid synthesis. Obtaining a mixture of nanostructures after the thermal treatment.
  • FIG. 11 illustrates the mechanism and the role of carbon coating, the latter coating making it possible to obtain a large diffusion of lithium in Li 4 Ti 5 O 12 and obtain 90% of the nominal capacity at 12C.
  • FIG. 12 illustrates the mechanism of the technology of hybrid supercapacitors using an anode of the nano- Li 4 Ti 5 O 12 type.
  • FIG. 13 is the TGA curve of a mixture of TiO 2 +Li 2 CO 3 + carbon after milling at high energy for 2 hours, in air and in argon; the reaction starts at 400° C. (in argon and in air).
  • FIG. 14 is a SEM photo of microscopic particles of Li 4 Ti 5 O 12 obtained from a mixture of Li 2 CO 3 +TiO 2 .
  • FIG. 15 is a SEM photo of nanoscopic particles of Li 4 Ti 5 O 12 obtained using a mixture of Li 2 CO 3 +TiO 2 + carbon.
  • FIG. 16 illustrates a manufacturing process for nanoparticles of Li 4 Ti 5 O 12 coated with carbon and obtained by coating the particles of TiO 2 with organic formulations of the polyol type and/or of the PE-PO type; the thermal treatment carried out in inert atmosphere transforms the organic part into carbon. This process is carried out in the step of mixed Jar milling with solvent or dry.
  • FIG. 17 illustrates a manufacturing process for nanoparticles of Li 4 Ti 5 O 12 coated with carbon and obtained by coating the particles of TiO 2 with inorganic formulations of the Al 2 O 3 , ZrO 2 type, the thermal treatment carried out in inert atmosphere transforming the organic part to carbon. This process is carried out in the step of mixed Jar milling with solvent or dry.
  • FIG. 18 illustrates a manufacturing process for nanoparticles of Li 4 Ti (5 ⁇ ) AlO 12 coated with carbon and obtained by coating the particles of TiO 2 using a hybrid inorganic-organic formulation.
  • the present invention concerns a synthesis process for new particles of the formula Li 4 Ti 5 O 12 , of the formula Li (4 ⁇ ) Z ⁇ Ti 5 O 12 or of the formula Li 4 Z ⁇ Ti (5 ⁇ ) O 12 , wherein ⁇ represents a number greater than zero and less than or equal to 0.33, ⁇ represents a number greater than 0 and less than or equal to 0.5, Z represents a source of at least one metal, preferably chosen from the group made up of Mg, Nb, Al, Zr, Ni, Co. These particles are coated with a layer of carbon. Use of these particles in electrochemical systems also constitutes an object of the present invention.
  • a first object of the present invention consists of a process that makes possible the preparation of particles comprising:
  • a core of Li 4 Ti 5 O 12 a core of Li (4 ⁇ ) Z ⁇ Ti 5 O 12 or a core of Li 4 Z ⁇ Ti (5 ⁇ ) O 12 , ⁇ representing a number greater than zero and less than or equal to 0.33, ⁇ representing a number greater than 0 and less than or equal to 0.5, Z representing a source of at least one metal, preferably chosen from the group made up of Mg, Nb, Al, Zr, Ni, Co; and
  • this synthesis process makes possible the preparation of particles of Li 4 Ti 5 O 12 (preferably with spinel structure) coated with carbon, said particles comprising from 0.01 to 10%, preferably 1 to 6%, and still more preferably around 2% by weight of carbon, the quantity of carbon being expressed with respect to the total mass of Li 4 Ti 5 O 12 particles;
  • x represents a number between 1 and 2
  • z represents 1 or 2
  • Y represents a radical chosen among CO 3 , OH, O and TiO 3 or a mixture of them.
  • the operating conditions more specifically the concentration conditions of components of the ternary mixture submitted to dispersion, being chosen in such a way as to yield a conversion, preferably a complete conversion, of the initial products into Li 4 Ti 5 O 12 .
  • the process according to the invention makes possible the synthesis of particles of Li (4 ⁇ ) Z ⁇ Ti 5 O 12 (preferably with spinel structure) coated with carbon, ⁇ 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, said particles comprising from 0.01 to 10%, preferably 1 to 6%, and still more preferably around 2% by weight of carbon, the quantity of carbon being expressed with respect to the total mass of Li (4 ⁇ ) Z ⁇ Ti 5 O 12 particles;
  • x represents a number between 1 and 2
  • z represents 1 or 2
  • Y represents a radical chosen among CO 3 , OH, O and TiO 3 or a mixture of them;
  • the operating conditions more specifically the concentration conditions of components of the ternary mixture submitted to dispersion, being chosen in such a way as to yield a conversion, preferably a complete conversion, of the initial products into Li (4 ⁇ ) Z ⁇ Ti 5 O 12 , and
  • the source of at least one metal Z being added to the reaction mixture, preferably in step a) of said process in a content that is preferably from 0.1 to 2% by weight, expressed with respect to the mass of said ternary mixture.
  • Operating conditions that make possible the specific preparation of particles of the formula Li (4 ⁇ ) Z ⁇ Ti 5 O 12 are, more specifically, a control of the initial quantities of each of the compounds present in the ternary mixture that is used for preparation of the dispersion.
  • the process of the invention makes possible the synthesis of particles of the formula Li 4 Z ⁇ Ti (5 ⁇ ) O 12 (preferably with spinel structure), wherein ⁇ is greater than 0 and less than or equal to 0.5, coated with carbon, Z representing a source of at least one metal, preferably chosen from the group made up of Mg, Nb, Al, Zr, Ni, Co, said particles comprising from 0.01 to 10%, preferably 1 to 6%, and still more preferably around 2% by weight of carbon, the quantity of carbon being expressed with respect to the total mass of Li 4 Z ⁇ Ti (5 ⁇ ) O 2 particles;
  • x represents a number between 1 and 2
  • z represents 1 or 2
  • Y represents a radical chosen among CO 3 , OH, O AND TiO 3 or a mixture of them;
  • the operating conditions more specifically the concentration conditions of components of the ternary mixture submitted to dispersion, being chosen in such a way as to yield a conversion, preferably a complete conversion, of the initial products into Li 4 Z ⁇ Ti (5 ⁇ ) O 12 , and
  • the source of at least one metal Z being added to the reaction mixture, preferably in step a) of said process in a content that is preferably from 0.1 to 2% by weight, expressed with respect to the mass of said ternary mixture,
  • the operating conditions that make possible the specific preparation of particles of the formula Li 4 Z ⁇ Ti (5 ⁇ ) O 12 are, more specifically, a control of the initial quantities of each of the constituents present in the ternary mixture that is used for preparation of the dispersion.
  • the dispersion of the ternary mixture is heated at a temperature of around 600° C.
  • the dispersion is heated in two steps, the first step being carried out until the dispersion reaches a temperature of about 400° C., the second step being carried out at approximately 600° C.
  • the first step is preferably carried out by rapid heating at around 400° C., preferably during a period of 1 to 4 hours.
  • the second step is carried out by slow heating, preferably for at least four hours.
  • At least one step which is preferably step a), is carried out in air.
  • At least one step which is preferably step b), is carried out at least partially in inert atmosphere.
  • the dispersion of the ternary mixture is advantageously prepared using water and/or at least one solvent that is preferably an organic solvent.
  • This organic solvent is advantageously chosen from the group made up of ketones, saturated hydrocarbons, unsaturated hydrocarbons, alcohols and mixtures of them, still more preferably the dispersion of the ternary mixture is prepared using water, acetone, heptane, toluene or using a mixture of them.
  • Said dispersion is also prepared dry, without solvent.
  • a compound Li z Y which comprises at least one compound chosen from the group made up of Li 2 O, Li 2 CO 3 and LiOH, is chosen. Still more preferably, the Li z Y compound comprises exclusively Li 2 CO 3 , said Li 2 CO 3 preferably being present in a ratio of 25 to 30% by weight with respect to the total mass of the ternary mixture.
  • the dispersion is carried out by mechanical milling, preferably by high-energy mechanical milling, preferably dry and/or by Jar milling, preferably with a solvent.
  • a TiO x compound of the anatase or rutile TiO 2 type (preferably the anatase TiO 2 type), or a mixture of both, is chosen and TiO 2 is preferably present in said ternary mixture in concentrations of 58 to 71% by weight.
  • the compound Li z Y preferably comprises Li 2 TiO 3 , this Li 2 TiO 3 preferably being present in a quantity of 43 to 48% by weight of Li 2 TiO 3 with respect to the total mass of the ternary mixture.
  • the carbon used to carry out the process according to the invention may come from any source.
  • the carbon is chosen from the group made up of natural or artificial graphite, carbon black (preferably acetylene black), Shawinigan black, Ketjen black and cokes (preferably petrolum coke) and is added to the reaction mixture, preferably at the beginning of the preparation of the dispersion of the ternary mixture.
  • the carbon can also be produced in the course of said process, preferably from at least one free organic material, such as a polymer, present in the reaction mixture.
  • the carbon can also be 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 particles 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 of the reagents used (preferably the TiO 2 ) for the preparation of the dispersion of said ternary mixture.
  • the carbon used is in the form of particles having a specific surface area greater than or equal to 2 m 2 /g, preferably in the form of particles having a specific surface area greater than or equal to 50 m 2 /g.
  • the process of the invention is carried out in the presence of an atmosphere containing oxygen, a part of the carbon present in the reaction mixture then being consumed during said process.
  • the coating of carbon is obtained from the presence, in the reaction mixture, of a powder of Shawinigan carbon and/or at least one polymer, which is preferably a polyol or a polyethylene-polyoxide ethylene copolymer.
  • TiO 2 that is coated with at least one inorganic material with an inorganic material that preferably comprises an aluminum oxide and/or a zirconium oxide and still more preferably at least one organic material that comprises Al 2 O 3 and/or ZrO 2 , is used.
  • TiO 2 that is coated with a hybrid inorganic-organic material is used.
  • a second object of the present invention is made up of particles that can be obtained by use of one of the processes previously defined for the first object of the invention.
  • These particles comprise a core coated with carbon, the core of said particles being:
  • Z representing a source of at least one metal, preferably chosen from the group made up of Mg, Nb, Al, Zr, Ni, Co.
  • a preferred sub-family is made up of particles wherein the core mainly comprises preferably at least 65% of Li 4 Ti 5 O 12 , of Li (4 ⁇ ) Z ⁇ Ti 5 O 12 or Li 4 Z ⁇ Ti (5 ⁇ ) O 12 or a mixture of these.
  • the complement notably being made up of TiO 2 Li 2 TiO 3 or the residues of solvents.
  • the core of the particles according to the invention is exclusively made up of Li 4 Ti 5 O 12 , of Li (4 ⁇ ) Z ⁇ Ti 5 O 12 or Li 4 Z ⁇ Ti (5 ⁇ ) O 12 or a mixture of these.
  • a preferred sub-family of particles of the present invention is made up of particles that have a reversible capacity, measured according to the method defined in the description, which is between 155 and 170 mAh/g.
  • these particles are made up of a core of Li 4 Ti 5 O 12 coated with a layer of carbon.
  • the particles according to the invention are preferably nanostructures. Their size, measured with scanning electron microscopy, is preferably comprised between 10 and 950 nanometers.
  • the particles according to the present invention are also characterized by their core, which has a size measured using scanning electron microscopy that is preferably comprised between 10 and 500 nanometers.
  • the carbon coating that covers these particles is characterized by a thickness that, also measured using scanning electron microscopy, is comprised between 10 and 450 nanometers, still more preferably the thickness of the coating varies between 20 and 300 nanometers.
  • a third object of the present invention is made up of a cathode of an electrochemical generator (preferably a recyclable type electrochemical generator) comprising particles such as previously defined in the second object of the present invention and/or such that can be obtained by using any one of the processes according to the first object of the present invention.
  • an electrochemical generator preferably a recyclable type electrochemical generator
  • a fourth object of the present invention is made up of an anode for an electrochemical generator (preferably a recyclable type electrochemical generator) comprising particles such as previously defined in the second object of the present invention and/or such that can be obtained by using any one of the processes according to the first object of the present invention.
  • an electrochemical generator preferably a recyclable type electrochemical generator
  • a fifth object of the present invention is made up of an electrochemical generator (preferably of the rechargeable type) of the lithium type comprising an anode of the metallic lithium type and a cathode of the Li 4 Ti 5 O 12 type and/or of the Li (4 ⁇ ) Z ⁇ Ti 5 O 12 type and/or of the Li 4 Z ⁇ Ti (5 ⁇ ) O 12 type or mixtures of them, the cathode in this battery being such as previously defined in the third object of the present invention.
  • a sixth object of the present invention is made up of an electrochemical generator (preferably of the rechargeable type) of the lithium-ion type comprising an anode of the Li 4 Ti 5 O 12 type and/or the Li (4 ⁇ ) Z ⁇ Ti 5 O 12 type and/or the Li 4 Z ⁇ Ti (5 ⁇ ) O 12 type or mixtures of them and a cathode of the LiFePO 4 , LiCoO 2 , LiCoPO 4 , LiMn 2 O 4 and/or LiNiO 2 type or mixtures of them wherein the anode is such as defined in the third object of the present invention.
  • such a generator uses, in the anode and/or in the cathode, a current collector of solid aluminum or of the Exmet type (expanded metal).
  • a preferred sub-family of the electrochemical generators according to the present invention is made up of generators that do not require any prior forming of the battery.
  • a seventh object of the present invention is made up of a hybrid-type supercapacitor comprising an anode of the Li 4 Ti 5 O 12 type and/or the Li (4 ⁇ ) Z ⁇ Ti 5 O 12 type and/or the Li 4 Z ⁇ Ti (5 ⁇ ) O 12 type and a cathode of the graphite or carbon type with a large specific surface area, wherein the anode is as defined previously, not requiring any preliminary forming of the supercapacitor.
  • the anode and/or the cathode of such a supercapacitor is (are) equipped with a current collector of solid aluminum or of the Exmet (expanded metal) type.
  • the electrolyte used in the electrochemical generator or in the supercapacitor is dry polymer, gel, liquid or ceramic in nature.
  • the present invention makes available a new synthesis method for Li 4 Ti 5 O 12 that is simple, fast and less costly.
  • the synthesis is based on a ternary mixture of TiO 2 with anatase or rutile structure, of Li 2 CO 3 and carbon.
  • the mixture is well dispersed, then submitted to a heating phase that comprises two steps.
  • the first step is rapid heating to 400° C. in air. This temperature stage helps, on one hand, to eliminate the traces of heptane when this solvent is used and, on the other hand, to stimulate the release of CO 2 .
  • the second step to 600° C. is longer and requires a minimum of 4 hours. This completes the transformation of the ternary mixture to Li 4 Ti 5 O 12 with spinel structure.
  • the fineness of the particle size is obtained due to a longer heating time during the second step (see the illustration given in FIG. 2).
  • the carbon is oxidized with the oxygen in the air, with oxygen coming from TiO 2 while releasing CO 2 .
  • titanium reacts with lithium, forming lithiated titanium. The latter oxidizes with air.
  • the synthesis reaction can be schematically illustrated as follows:
  • An excess of carbon is used to ensure complete transformation. In fact, carbon burns in the presence of air, then its excess reduces TiO 2 and Li 2 CO 3 .
  • carbons that contain oxygen groups at the surface are used. The latter react with the lithium oxide.
  • the TiO 2 -carbon-Li 2 CO 3 mixture can be produced using two methods: in a solvent or in a dry mixture dispersed mechanically. Once the intimate homogeneous powder is obtained, the carbon will play the essential role established according to reaction (2) by obtaining a Li 4 Ti 5 O 12 product without impurities.
  • the synthesis was also carried out with the TiO 2 —Li 2 CO 3 -carbon mixture dispersed by high-energy mechanical milling (HEMM).
  • HEMM high-energy mechanical milling
  • the main step before the passage to HEMM is to disperse the ternary mixture well in order to obtain a homogeneous mixture (FIG. 10), For this, first a co-milling for 15 minutes to 2 hours is used, in addition, this co-milling also helps to lower the synthesis temperature.
  • This process produces particles on the nanostructure scale of Li 4 Ti 5 O 12 (FIGS. 6, 7 and 8 ), compared to the classic method that makes it possible to carry out the formation of the macroscopic particles (FIGS. 4 and 5).
  • Li 4 Ti 5 O 12 applications are presented in FIG. 1.
  • the battery produces 1.5 volts, due to the rechargeability of the Li 4 Ti 5 O 12 , this system becomes very interesting for the rechargeable battery markets, thus replacing the large market of primary alkaline batteries of 1.5 volt.
  • Li 4 Ti 5 O 12 is a white insulating powder, in order to increase its electronic conductivity, it is co-milled with carbon.
  • the latter coats the particles of Li 4 Ti 5 O 12 and gives a good conductivity to the electrode at the time of intercalation and disintercalation of lithium and keeps its capacity (mAh/g) stable at elevated currents (mA/g).
  • carbon plays a double role in this invention, on one hand, it helps to synthesize a final pure product of the Li 4 Ti 5 O 12 type by lowering the synthesis temperature, and on the other, it increases the electronic conductivity by co-milling with Li 4 Ti 5 O 12 for manufacturing electrodes for an electrochemical generator.
  • FIG. 12 uses an insertion anode of the Li 4 Ti 5 O 12 type placed face to face with a cathode of the graphite or carbon type with large specific surface area (double layer) with a polymer, gel, liquid or ceramic electrolyte.
  • the advantage of nano- Li 4 Ti 5 O 12 coated with carbon (FIG. 11) promotes the diffusion of lithium inside the spinel structure, and in particular, at elevated currents like 12C (charge-discharge in 5 minutes). At these ratings, the HSC develops 90% of the nominal capacity.
  • the presence of carbon provides good conductivity at the grain level and on the scale of the electrode, which limits the addition of large proportions of carbon to the electrode. This makes it possible to increase the energy density of the HSC.
  • HSC technology uses two collectors of the Exmet (expanded metal) type in aluminum with an electrolyte having a salt mixture of LiTFSI+LiBF 4 or LiTFSI+LiPF 6 or LiTFSI+BETi+LiBF 4 .
  • This mixture makes it possible to have good ionic conductivity and reduces the collector corrosion during high-voltage charging.
  • the energy density of the HSC is around 60 Wh/kg and the capacity obtained is 90% at charging rates of 12C.
  • HSC technology presents an energy density comparable to Pb-acid or Ni—Cd technologies, in addition this technology has a long cyclability.
  • Li-ion technology graphite/LiCoo 2
  • currents less than 2C (30 minutes) and by the number of cycles which is 1200.
  • This ternary mixture is placed in a steel container and heptane is added in a powder/liquid ratio of around 35 g/150 ml.
  • the heptane is used to reduce the heat and the friction between the particles of powder and the balls and leaves the product inert.
  • Stainless steel balls are added to homogenize the ternary mixture.
  • the success of the co-milling depends on lowering the synthesis temperature.
  • the heating of this co-milled mixture is carried out in two steps. The first step is a rapid heating to 400° C. in air. This temperature stage promotes the elimination of traces of heptane and stimulates the start of CO 2 release.
  • the second step consists of slow heating to 600° C. This completes the transformation of the product into Li 4 Ti 5 O 12 with spinel structure.
  • the X-ray spectrum confirms the presence of peak characteristics of the spinel structure of the Li 4 Ti 5 O 12 .
  • FIG. 15 which is a photograph obtained using scanning electron microscopy, shows that the particles of Li 4 Ti 5 O 12 are of nanoscopic size.
  • FIG. 14 relates to a photo obtained in the same manner, but for particles prepared without the addition of carbon shows that the corresponding particles are of macroscopic size.
  • the particles of Li 4 Ti 5 O 12 , of poly(vinylidene fluoride) (PVDF) and Ketjen black, present in a mass ratio of 87/10/3 are mixed.
  • This mixture is applied to an exmet electrode of aluminum, then heated for 12 hours with nitrogen scavenging.
  • the electrode thus prepared is then heated for 2 hours in vacuum.
  • the electrode is then assembled in an electrochemical cell of around 4 cm 2 with a Celgard type separator facing the lithium metal.
  • the solvent is of the TESA type (tetra ethyl sulfone amine) ethylene carbonate type with LiTFSI salt (lithium trifluoromethanesulfonimide).
  • the cycling is carried out, at ambient temperature, between 1.2 and 2.5 V.
  • the reversible capacity obtained is 155 mAh/g with an average voltage of 1.55 V.
  • Li 4 Ti 5 O 12 and Ketjen black in a volume ratio 40/3, are co-milled in heptane in the presence of stainless steel balls.
  • the mixture is dried, then mixed with a polymer solution based on a polyether marketed by the Baker Hughes Company, USA under the commercial name UNITHOX 750, in a volume ratio 43/57.
  • This mixture is then applied to an aluminum collector, then heated for 12 hours with nitrogen scavenging.
  • the collector thus processed is then heated for 2 hours in vacuum.
  • the electrode is assembled in an electrochemical cell with about 4 cm 2 surface area with a separator of the polymer type based on salt containing polyether prepared in a laboratory, with LiTFSI salt (tetra fluoro sulfur lithium imide) placed face to face with the lithium metal as anode. Cycling is carried out at 80° C. between 1.2 and 2.5 V. The reversible capacity obtained is 155 mAh/g in C/24 and it is 96% of the nominal capacity obtained with a rapid rating in C/1. The cell thus prepared demonstrates good cycling stability, more than 1500 cycles in C/1.
  • the electrochemical result obtained by introduction of this electrode in a cell without solvent (completely solid) comprising a polymer (polyether) at 80° C. is 150 mAh/g in C/24 while only 75% of the nominal value is found with fast loading in C/1. In fact, this is due to the poor dispersion between the oxide and the carbon black. In addition, the reproducibility of the results is uncertain.
  • particles of Li 4 Ti 5 O 12 were prepared using a binary mixture of LiOH—TiO 2 (anatase) of 10.5 and 16 g, respectively, heated for 18 hours in air.
  • the X-ray spectrum obtained for these particles establishes the presence of peak characteristics of the spinel structure of Li 4 Ti 5 O 12 as well as the presence of traces of TiO 2 (rutile) and Li 2 TiO 3 .
  • the Li 4 Ti 5 O 12 powder obtained is mixed with PVDF and with Shawinigan black in a weight ratio 87/10/3. This mixture, which makes up the electrode, is applied to an aluminium Exmet support, then heated for 12 hours with nitrogen scavenging. The electrode thus obtained is then heated for 2 hours in vacuum. Said electrode is assembled in an electrochemical cell about 4 cm 2 with a Celgard type separator placed face to face with lithium metal as anode.
  • the solvent used is of the TESA type (tetra ethylsulfamide)—ethylene carbonate (1:1 by volume) with 1 mol of LiTFSI (bis(trifluoromethane sulfonimide)).
  • the reversible capacity obtained in this case is 140 mAh/g.
  • the capacity obtained by the binary type synthesis is thus appreciably less than that obtained by the using ternary synthesis in the presence of carbon.
  • Li 4 Ti 5 O 12 particles are mixed with PVDF and Shawinigan black in a weight ratio 87/10/3. This mixture is applied on an aluminium Exmet type electrode, then heated for 12 hours with nitrogen scanning. All of this is then heated for 2 hours in vacuum.
  • Cobalt oxide LiCoO 2 is mixed with PVDF and Shawinigan black in a weight ratio 87/10/3. Then the mixture thus obtained is applied to an aluminum Exmet type electrode, the assembly thus obtained is then heated for 12 hours with nitrogen scanning, then in a second step is heated for 2 hours in vacuum.
  • the Li 4 Ti 5 O 12 electrode is assembled in a lithium-ion battery face to face with the LiCoO 2 electrode as cathode with a Celgard type separator.
  • the solvent used is of the ethylene carbonate—methyl ethylene carbonate type (1:1 by volume) with 1 mole of lithium bis(trifluoromethane sulfonimide).
  • the battery voltage tends toward zero volts (33 mV).
  • the battery is cycled between 1.2 V and 2.8 V.
  • the average voltage is around 2.5 V.
  • the irreversible capacity of the first cycle is around 2%. This irreversibility is minimum compared to the conventional carbon/LiCoO 2 system. Because of the fact that the two electrodes of the Li 4 Ti 5 O 12 /LiCoO 2 system have no passivation film, the reversible capacity of the battery is stable for more than 500 cycles. Knowing that 2.5 V yields 70% of the average voltage of the lithium-ion system of the carbon/LiCoO 2 type, a 30% deficit remains to be recaptured. The lack of energy to be obtained from the carbon/LiCoO 2 system can be filled by:
  • an Exmet type collector based on aluminum on the anode that makes it possible to reduce the weight of the battery (conventional carbon/LiCoO 2 system using copper as current collector for the anode);
  • Li 4 Ti 5 O 12 is mixed with PVDF and Shawinigan black in a weight 87/10/3. This mixture is applied to an aluminium Exmet type electrode.
  • Natural graphite NG7 (Kansai Coke, Japan) is mixed with PVDF in a weight ratio 90/10. This mixture is applied to an aluminium Exmet type electrode. The assembly thus obtained is heated for 12 hours with nitrogen scavenging, then heated 2 hours in vacuum.
  • the Li 4 Ti 5 O 12 electrode is mounted face to face with the graphite electrode separated by a Celgard.
  • the solvent used is PC+EC+TESA (1:1:1 by volume) containing 1 mol of LiPF 5 +LiTFSI.
  • the graphite electrode is used as cathode and the intercalation reaction is an electrolytic reaction of the double layer, of which the anion PF 6 is absorbed at the surface of the graphite.
  • the voltage cycling limits are between 1.5 V and 3.0 V, for an average voltage of 2.25 V. This average voltage value increases the energy density by 50% with respect to values obtained with a conventional carbon-carbon system.
  • Li 4 Ti 5 O 12 is mixed with PVDF and Shawinigan black in a weight ratio 87/10/3. This mixture is applied to an aluminium Exmet electrode. All of this is heated for 12 hours with nitrogen scavenging, then for 2 hours in vacuum.
  • the Li 4 Ti 5 O 12 electrode is mounted face to face with a carbon electrode as cathode, separated by a Celgard.
  • the solvent used is EC+PC+DMC (1:1:1 by volume) containing 1 mole of LiTFSI+LiBF 4 .
  • the carbon electrode is used as cathode.
  • the intercalation reaction in this case is a double layer electrolytic reaction, wherein the PF6 and TFSI anions are absorbed at the carbon surface.
  • the cycling voltage limits are between 1.5 V and 3.0 V with an average potential of 2.25 V. This average voltage value increases the energy density by 50% comparatively to the conventional carbon-carbon system.
  • Li 4 Ti 5 O 12 is mixed with PVDF and Shawinigan black in a weight ratio 87/10/3. This mixture is applied to an aluminium Exmet electrode. All of this is heated for 12 hours with nitrogen scavenging at a temperature of 120° C., then for 2 hours in vacuum at a temperature of 120° C.
  • a conductive polymer of the polyaniline type is mixed with PVDF and Shawinigan black in a weight ratio 87:10:3.
  • the mixture thus obtained is applied to an aluminium Exmet electrode, then heated for 12 hours with nitrogen scavenging at a temperature of 120° C., then for 2 hours in vacuum at a temperature of 120° C.
  • the Li 4 Ti 5 O 12 electrode is mounted face to face with the carbon electrode as cathode separated by a Celgard.
  • the solvent used is EC+PC+DMC (1:1:1 by volume), commonly called, containing 1 mole of LiTFSI+LiBF 4 .
  • the polymer electrode conductor is used as cathode.
  • the intercalation reaction is then a doping reaction of the PF 6 and TFSI anions across the conductive polymer chains.
  • the cycling voltage limits are comprised between 1.5 V and 3.0 V with an average voltage of 2.25 V. The performance observed is comparable to that obtained in the preceding example.
  • the particles according to the present invention present a surprisingly notable spreading capacity, an excellent nominal capacity, an excellent cycling stability and a remarkable high current power in electrochemical devices that use them, in particular at the electrode level, as well as flexibility regarding electrode thickness that can be produced using these particles.
  • the particles in nano form yield 90% of the nominal capacity, while the corresponding macroparticles develop no more than 50% of the capacity.
  • the macros also have a limitation with currents less then 5C.
  • the nano-particles do not have any limitation.

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  • Secondary Cells (AREA)
US10/830,240 2000-12-05 2004-04-23 Li4Ti5O12, Li(4-alpha)Zalpha Ti5O12 or Li4ZbetaTi(5-beta)O12 particles, processes for obtaining same and use as electrochemical generators Abandoned US20040202934A1 (en)

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US11/808,353 US20070243467A1 (en) 2000-12-05 2007-06-08 Li4Ti5O12, Li(4-a)ZaTi5O12 OR Li4ZbetaTi(5-beta)O12 particles, process for obtaining same and use as electrochemical generators
US12/149,535 US8114469B2 (en) 2000-12-05 2008-05-02 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-βO12 particles, processes for obtaining same and use as electrochemical generators
US13/360,173 US9077031B2 (en) 2000-12-05 2012-01-27 Li4Ti5O12, Li(4-α)ZαTi5O12or Li4ZβTi(5-β)O12 particles, processes for obtaining same and their use in electrochemical generators
US14/461,786 US9559356B2 (en) 2000-12-05 2014-08-18 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-β)O12 particles, processes for obtaining same and use as electrochemical generators
US15/252,944 US10734647B2 (en) 2000-12-05 2016-08-31 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-β)O12, particles, processes for obtaining same and use as electrochemical generators
US16/910,396 US20200373570A1 (en) 2000-12-05 2020-06-24 Li4Ti5O12, Li(4-a)ZaTi5O12 OR Li4ZßTi(5-ß)O12, PARTICLES, PROCESSES FOR OBTAINING SAME AND USE AS ELECTROCHEMICAL GENERATORS

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CA002327370A CA2327370A1 (fr) 2000-12-05 2000-12-05 Nouvelle methode de fabrication de li4ti5o12 pur a partir du compose ternaire tix-liy-carbone: effet du carbone sur la synthese et la conductivite de l'electrode
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US12/149,535 Division US8114469B2 (en) 2000-12-05 2008-05-02 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-βO12 particles, processes for obtaining same and use as electrochemical generators

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US11/808,353 Abandoned US20070243467A1 (en) 2000-12-05 2007-06-08 Li4Ti5O12, Li(4-a)ZaTi5O12 OR Li4ZbetaTi(5-beta)O12 particles, process for obtaining same and use as electrochemical generators
US12/149,535 Expired - Fee Related US8114469B2 (en) 2000-12-05 2008-05-02 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-βO12 particles, processes for obtaining same and use as electrochemical generators
US13/360,173 Expired - Fee Related US9077031B2 (en) 2000-12-05 2012-01-27 Li4Ti5O12, Li(4-α)ZαTi5O12or Li4ZβTi(5-β)O12 particles, processes for obtaining same and their use in electrochemical generators
US14/461,786 Expired - Lifetime US9559356B2 (en) 2000-12-05 2014-08-18 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-β)O12 particles, processes for obtaining same and use as electrochemical generators
US15/252,944 Expired - Lifetime US10734647B2 (en) 2000-12-05 2016-08-31 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-β)O12, particles, processes for obtaining same and use as electrochemical generators
US16/910,396 Abandoned US20200373570A1 (en) 2000-12-05 2020-06-24 Li4Ti5O12, Li(4-a)ZaTi5O12 OR Li4ZßTi(5-ß)O12, PARTICLES, PROCESSES FOR OBTAINING SAME AND USE AS ELECTROCHEMICAL GENERATORS

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US12/149,535 Expired - Fee Related US8114469B2 (en) 2000-12-05 2008-05-02 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-βO12 particles, processes for obtaining same and use as electrochemical generators
US13/360,173 Expired - Fee Related US9077031B2 (en) 2000-12-05 2012-01-27 Li4Ti5O12, Li(4-α)ZαTi5O12or Li4ZβTi(5-β)O12 particles, processes for obtaining same and their use in electrochemical generators
US14/461,786 Expired - Lifetime US9559356B2 (en) 2000-12-05 2014-08-18 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-β)O12 particles, processes for obtaining same and use as electrochemical generators
US15/252,944 Expired - Lifetime US10734647B2 (en) 2000-12-05 2016-08-31 Li4Ti5O12, Li(4-α)ZαTi5O12 or Li4ZβTi(5-β)O12, particles, processes for obtaining same and use as electrochemical generators
US16/910,396 Abandoned US20200373570A1 (en) 2000-12-05 2020-06-24 Li4Ti5O12, Li(4-a)ZaTi5O12 OR Li4ZßTi(5-ß)O12, PARTICLES, PROCESSES FOR OBTAINING SAME AND USE AS ELECTROCHEMICAL GENERATORS

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