US20040151951A1 - Lithium based electrochemical cell systems - Google Patents
Lithium based electrochemical cell systems Download PDFInfo
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- US20040151951A1 US20040151951A1 US10/738,400 US73840003A US2004151951A1 US 20040151951 A1 US20040151951 A1 US 20040151951A1 US 73840003 A US73840003 A US 73840003A US 2004151951 A1 US2004151951 A1 US 2004151951A1
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- cell system
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- degassing agent
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/14—Cells with non-aqueous electrolyte
- H01M6/16—Cells with non-aqueous electrolyte with organic electrolyte
- H01M6/162—Cells with non-aqueous electrolyte with organic electrolyte characterised by the electrolyte
- H01M6/168—Cells with non-aqueous electrolyte with organic electrolyte characterised by the electrolyte by additives
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
- H01M10/0567—Liquid materials characterised by the additives
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/4235—Safety or regulating additives or arrangements in electrodes, separators or electrolyte
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/52—Removing gases inside the secondary cell, e.g. by absorption
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
- H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- Gas generation in both Li-ion and lithium-metal based primary and secondary electrochemical cells may become a serious problem both during normal cell operation at room temperature and, more especially, at elevated temperatures.
- the consequence of gas build up includes cell can expansion and subsequent can rupture, leading to cell and or battery failure.
- the gassing problem has been observed to be extremely serious in large electric vehicle type cell systems and in pouch type cell systems where rupture of the cell containment leads to serious safety problems.
- the gassing problem is also very serious in lithium-metal based primary cells using liquid and/or solid electrolytes in vivo applications such as for heart pacemakers and similar devices.
- This invention is directed toward the development of both primary and secondary Li-ion and lithium-metal based electrochemical cell systems in which the suppression of gas generation is achieved through the addition of an additive or additives to the electrolyte system of the respective cell, or to the cell whether it be a liquid, a solid- or plastized polymer electrolyte system.
- the gas suppression additives in this patent application are primarily based on unsaturated hydrocarbons and nitrogen containing organic materials.
- FIG. 1 shows cycle life characteristics of a Li-ion cell (ANL-1) containing 1.0 wt % 2,3 dimethyl-1,3 butadiene with the 1 M LiPF 6 dissolved in ethylene carbonate (30%) and ethyl-methyl carbonate (70%);
- FIG. 2 shows cycle life characteristics of a Li-ion cell (ANL-2) containing 2.0 wt % VEC and 1.0 wt % 2,3 dimethyl-1,3 butadiene with the 1 M LiPF 6 dissolved in ethylene carbonate (20%), propylene carbonate (20%), and diethyl carbonate (60%); and
- FIG. 3 shows changes of gas pressure change during ARC measurements of negative electrodes and electrolytes from Li-ion (ANL-1) cells with additives and a reference cell negative electrode and electrolyte from a (ANL-1) cell, but without additives.
- the primary and secondary electrochemical Li-ion cells of this invention have minimal gassing and possess high specific energy and power, as well as excellent calendar and cycle life across a broad temperature range.
- the additives that are capable of ameliorating gas generation in the lithium based electrochemical cells include at least the following class of organic compounds, which will be described in more detail hereinafter: (a) CH 2 ⁇ R 1 ⁇ CH 2 , where R 1 is an aliphatic carbon chain of 1 to 7 carbons, either linear or branched (b) CH ⁇ R 1 ⁇ CH, (c) CH 2 ⁇ R 1 , (d) CH ⁇ R 1 , (e) R 2 —CH ⁇ R 1 ⁇ CH 2 , where R 2 is an aromatic (toluene or benzene), a cyclic hydrocarbon, (f) R 2 —C ⁇ R 1 ⁇ CH, (g) R 2 —CH ⁇ R 1 , (h) R 2 —C ⁇ R 1 , (i) st
- the present invention provides electrochemical lithium-based primary and secondary cells with excellent calendar life across a broad temperature, and includes cells with liquid and solid- and plastized polymer electrolytes.
- FIG. 1 shows the improved cycle life characteristics of a Li-ion cell (ANL-1) containing 1.0 wt % 2,3 dimethyl-1,3 butadiene (DMB).
- the cell utilized a crystalline graphite anode, a LiNi 0.8 Co 0.2 O 2 cathode and an electrolyte containing 1 M LiPF 6 dissolved in a blend of ethylene carbonate and ethyl-methyl carbonate.
- FIG. 2 shows the improved cycle life characteristics of a Li-ion cell (ANL-2) containing 2.0 wt % VEC and 1.0 wt % 2,3 dimethyl-1,3 butadiene with the 1 M LiPF 6 dissolved in blend of ethylene carbonate, propylene carbonate, and dimethyl carbonate.
- the cell utilized the same cathode and anode as cell (ANL-1).
- FIG. 3 shows the gas pressures developed by studies of the respective negative electrodes with electrolyte from cell (ANL-1) and compares the pressures developed by the negative electrodes and electrolyte from a similar cell that did not contain the 2,3 dimethyl-1,3 butadiene.
- the results of these studies indicate the additives significantly reduce the degree of gassing in the negative electrodes of cell (ANL-1), as compared to the negative electrode/electrolyte gassing from a similar cell but without the additive package.
- the additive effects in reducing pressure buildup are especially effective with the negative electrodes.
- the additives were also found to increase the activation energy and decrease the heat of reaction around the onset temperature that is believed to be the onset temperature for thermal runaway in the commercial lithium ion cells. The result of these studies indicate that these additives may be very effective in reducing gas buildup in high energy lithium-based cells for many different applications such as electric and hybrid vehicles, as well as in vivo applications such as for heart pacemakers and other implantable devices for the human body.
- lithium electrochemical cell systems include:
- a secondary Li-ion cell comprising a lithium metal oxide positive electrode, a negative electrode containing a crystalline carbon like graphite, an electrolyte composed of a lithium salt, and a blend of at least two aprotic solvents.
- the solvents include ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, propylene carbonate, or diethyl carbonate, and finally a compound that reduces cell gassing.
- the salts include LiPF 6 , LiBF 4 , LiAsF 6 , and other salts currently being used or being developed such as the lithium bisoxlatoborate (LiBOB) salts.
- These electrolytes also contain a degassing agent.
- a lithium-metal based primary or secondary electrochemical cell This cell is similar to those described above except that they use lithium metal as the negative electrode, a metal oxide positive electrode such as LiCoO 2 , LiNiO 2 , LiNi 1-x Co y Me z O 2 , LiMn 0.5 Ni 0.5 O 2 , LiMn 0.3 Co 0.3 Ni 0.3 O 2 , LiFePO 4 , LiMn 2 O 4 , LiFeO 2 , LiMc 0.5 Mn 1.5 O 4 , vanadium oxide, and mixtures thereof, wherein Me is Al, Mg, Ti, B, Ga, or Si, and Mc is a divalent metal such as Fe, Co, Cu, Cr and Ni, and either a liquid electrolyte described in (i) liquid or solid polymer or plastized electrolyte described in cell types (ii) above and that contains a degassing agent.
- a metal oxide positive electrode such as LiCoO 2 , LiNiO 2 , LiNi 1-x Co
- the agents or additives described herein include the following class of organic compounds; (a) CH 2 ⁇ R 1 ⁇ CH 2 , where R 1 is an aliphatic carbon chain of 1 to 7 carbons, either linear or branched (b) CH ⁇ R 1 ⁇ CH, (c) CH 2 ⁇ R 1 , (d) CH ⁇ R 1 , (e) R 2 —C ⁇ R 1 ⁇ CH 2 , where R 2 is an aromatic (toluene or benzene), a cyclic hydrocarbon, a pyrrole, a piperazine, or a piperidine molecule, (f) R 2 —C ⁇ R 1 ⁇ CH, (g) R 2 —CH ⁇ R 1 , (h) R 2 —C ⁇ R 1 , (i) styrene carbonate, (j) aromatic carbonates, (k) vinyl pyrrole, (l) vinyl piperazine, (m) vinyl piperidine, (n) vinyl pyridine (o) triphenyl
- the agents or additives described herein can include, for example, 2,3 dimethyl-1,3 butadiene, 1,3 butadiene, is 2,3 dimethyl-1,4 pentadiene, 1,5 hexadiene, a blend of 2,3 dimethyl-1,3 butadiene and vinyl ethylene carbonate, and a blend of 2,3 dimethyl-1,4 pentadiene and vinyl pyridine.
- additives or agents include a blend of 1,5 hexadiene and piperazine, a blend of 2,3 dimethyl-1,3 butadiene and styrene, a blend of 2,3 dimethyl-1,3 butadiene and piperidine, a blend of hexadiene and vinyl pyridine, a blend of 2,3 dimethyl-1,3 butadiene and triphenyl phosphate, a blend of 2,3 dimethyl-1,3 butadiene and vinyl pyridine, styrene carbonate, and a blend of styrene carbonate and vinyl piperazine.
- the additive or agent can also be a blend of two or more of the additives described above. According to one embodiment of the invention, the total concentration of additives ranges from 0.1 to 25 wt %, with an optimum concentration varying from 0.1 to 10 wt %.
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- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Inorganic Chemistry (AREA)
- Secondary Cells (AREA)
Abstract
Description
- This application claims priority to U.S. Provisional Patent Application No. 60/434,214, filed on Dec. 17, 2002 and incorporated herein by reference.
- [0002] This invention was made with government support under Contract No. W-31-109-ENG-38 awarded to the Department of Energy. The Government has certain rights in this invention.
- Gas generation in both Li-ion and lithium-metal based primary and secondary electrochemical cells may become a serious problem both during normal cell operation at room temperature and, more especially, at elevated temperatures. The consequence of gas build up includes cell can expansion and subsequent can rupture, leading to cell and or battery failure. For example, the gassing problem has been observed to be extremely serious in large electric vehicle type cell systems and in pouch type cell systems where rupture of the cell containment leads to serious safety problems. The gassing problem is also very serious in lithium-metal based primary cells using liquid and/or solid electrolytes in vivo applications such as for heart pacemakers and similar devices.
- Because both the negative and positive electrodes in the charged states of nearly all lithium based electrochemical cell systems are thermodynamically unstable in respect to the electrolyte, it is especially important that electrolyte additives be developed to stabilize the electrodes by decreasing the kinetics of the respective electrode reactions and thereby reducing the gas generation.
- This invention is directed toward the development of both primary and secondary Li-ion and lithium-metal based electrochemical cell systems in which the suppression of gas generation is achieved through the addition of an additive or additives to the electrolyte system of the respective cell, or to the cell whether it be a liquid, a solid- or plastized polymer electrolyte system. The gas suppression additives in this patent application are primarily based on unsaturated hydrocarbons and nitrogen containing organic materials.
- FIG. 1 shows cycle life characteristics of a Li-ion cell (ANL-1) containing 1.0 wt % 2,3 dimethyl-1,3 butadiene with the 1 M LiPF 6 dissolved in ethylene carbonate (30%) and ethyl-methyl carbonate (70%);
- FIG. 2 shows cycle life characteristics of a Li-ion cell (ANL-2) containing 2.0 wt % VEC and 1.0 wt % 2,3 dimethyl-1,3 butadiene with the 1 M LiPF 6 dissolved in ethylene carbonate (20%), propylene carbonate (20%), and diethyl carbonate (60%); and
- FIG. 3 shows changes of gas pressure change during ARC measurements of negative electrodes and electrolytes from Li-ion (ANL-1) cells with additives and a reference cell negative electrode and electrolyte from a (ANL-1) cell, but without additives.
- By use of appropriate additive or additives, the primary and secondary electrochemical Li-ion cells of this invention have minimal gassing and possess high specific energy and power, as well as excellent calendar and cycle life across a broad temperature range. The additives that are capable of ameliorating gas generation in the lithium based electrochemical cells include at least the following class of organic compounds, which will be described in more detail hereinafter: (a) CH 2═R1═CH2, where R1 is an aliphatic carbon chain of 1 to 7 carbons, either linear or branched (b) CH≡R1≡CH, (c) CH2═R1, (d) CH≡R1, (e) R2—CH═R1═CH2, where R2 is an aromatic (toluene or benzene), a cyclic hydrocarbon, (f) R2—C≡R1≡CH, (g) R2—CH═R1, (h) R2—C≡R1, (i) styrene carbonate, (j) aromatic carbonates, (k) vinyl pyrrole, (l) vinyl piperazine, (m) vinyl piperidine, (n) vinyl pyridine, (o) triphenyl phosphate and blends thereof. These blends may involve other additives such as vinyl ethylene carbonate to protect against exfoliation in propylene carbonate based Li-ion electrolyte systems.
- The present invention provides electrochemical lithium-based primary and secondary cells with excellent calendar life across a broad temperature, and includes cells with liquid and solid- and plastized polymer electrolytes.
- FIG. 1 shows the improved cycle life characteristics of a Li-ion cell (ANL-1) containing 1.0 wt % 2,3 dimethyl-1,3 butadiene (DMB). The cell utilized a crystalline graphite anode, a LiNi 0.8Co0.2O2 cathode and an electrolyte containing 1 M LiPF6 dissolved in a blend of ethylene carbonate and ethyl-methyl carbonate.
- FIG. 2 shows the improved cycle life characteristics of a Li-ion cell (ANL-2) containing 2.0 wt % VEC and 1.0 wt % 2,3 dimethyl-1,3 butadiene with the 1 M LiPF 6 dissolved in blend of ethylene carbonate, propylene carbonate, and dimethyl carbonate. The cell utilized the same cathode and anode as cell (ANL-1).
- FIG. 3 shows the gas pressures developed by studies of the respective negative electrodes with electrolyte from cell (ANL-1) and compares the pressures developed by the negative electrodes and electrolyte from a similar cell that did not contain the 2,3 dimethyl-1,3 butadiene. The results of these studies indicate the additives significantly reduce the degree of gassing in the negative electrodes of cell (ANL-1), as compared to the negative electrode/electrolyte gassing from a similar cell but without the additive package. The additive effects in reducing pressure buildup are especially effective with the negative electrodes. The additives were also found to increase the activation energy and decrease the heat of reaction around the onset temperature that is believed to be the onset temperature for thermal runaway in the commercial lithium ion cells. The result of these studies indicate that these additives may be very effective in reducing gas buildup in high energy lithium-based cells for many different applications such as electric and hybrid vehicles, as well as in vivo applications such as for heart pacemakers and other implantable devices for the human body.
- According to one embodiment of the invention, lithium electrochemical cell systems include:
- (i) A secondary Li-ion cell comprising a lithium metal oxide positive electrode, a negative electrode containing a crystalline carbon like graphite, an electrolyte composed of a lithium salt, and a blend of at least two aprotic solvents. The solvents include ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, propylene carbonate, or diethyl carbonate, and finally a compound that reduces cell gassing. The salts include LiPF 6, LiBF4, LiAsF6, and other salts currently being used or being developed such as the lithium bisoxlatoborate (LiBOB) salts.
- (ii) A Li-ion secondary electrochemical cell similar to the cell type (i) described above except that the electrolyte is either a liquid gel or solid polymer with a dissolved salt such as LiClO 4, LiPF6, LiBF4, LiAsF6, LiCF3SO3, Li(CF3SO2)2N, Li(CF3SO2)3C, LiN(SO2C2F5)2, lithium alkyl fuorophosphate, lithium bis(chelato)borates and mixtures thereof; or a solid polymer blended with the electrolyte described above in cell type (i), called a plastized electrolyte. These electrolytes also contain a degassing agent.
- (iii) A lithium-metal based primary or secondary electrochemical cell. This cell is similar to those described above except that they use lithium metal as the negative electrode, a metal oxide positive electrode such as LiCoO 2, LiNiO2, LiNi1-xCoyMezO2, LiMn0.5Ni0.5O2, LiMn0.3Co0.3Ni0.3O2, LiFePO4, LiMn2O4, LiFeO2, LiMc0.5Mn1.5O4, vanadium oxide, and mixtures thereof, wherein Me is Al, Mg, Ti, B, Ga, or Si, and Mc is a divalent metal such as Fe, Co, Cu, Cr and Ni, and either a liquid electrolyte described in (i) liquid or solid polymer or plastized electrolyte described in cell types (ii) above and that contains a degassing agent.
- The agents or additives described herein include the following class of organic compounds; (a) CH 2═R1═CH2, where R1 is an aliphatic carbon chain of 1 to 7 carbons, either linear or branched (b) CH≡R1≡CH, (c) CH2═R1, (d) CH≡R1, (e) R2—C═R1═CH2, where R2 is an aromatic (toluene or benzene), a cyclic hydrocarbon, a pyrrole, a piperazine, or a piperidine molecule, (f) R2—C≡R1≡CH, (g) R2—CH═R1, (h) R2—C≡R1, (i) styrene carbonate, (j) aromatic carbonates, (k) vinyl pyrrole, (l) vinyl piperazine, (m) vinyl piperidine, (n) vinyl pyridine (o) triphenyl phosphate, (p) and blends thereof. These blends may involve other additives, such as vinyl ethylene carbonate, to protect against exfoliation in propylene carbonate based Li-ion electrolyte systems.
- The agents or additives described herein can include, for example, 2,3 dimethyl-1,3 butadiene, 1,3 butadiene, is 2,3 dimethyl-1,4 pentadiene, 1,5 hexadiene, a blend of 2,3 dimethyl-1,3 butadiene and vinyl ethylene carbonate, and a blend of 2,3 dimethyl-1,4 pentadiene and vinyl pyridine. Other additives or agents include a blend of 1,5 hexadiene and piperazine, a blend of 2,3 dimethyl-1,3 butadiene and styrene, a blend of 2,3 dimethyl-1,3 butadiene and piperidine, a blend of hexadiene and vinyl pyridine, a blend of 2,3 dimethyl-1,3 butadiene and triphenyl phosphate, a blend of 2,3 dimethyl-1,3 butadiene and vinyl pyridine, styrene carbonate, and a blend of styrene carbonate and vinyl piperazine. Additionally, the additive or agent can also be a blend of two or more of the additives described above. According to one embodiment of the invention, the total concentration of additives ranges from 0.1 to 25 wt %, with an optimum concentration varying from 0.1 to 10 wt %.
- It should be understood that the above description of the invention and the specific examples and embodiments therein, while indicating the preferred embodiments of the present invention, are given only by demonstration and not limitation. Many changes and modifications within the scope of the present invention may therefore be made without departing from the spirit of the invention, and the invention includes all such changes and modifications.
Claims (20)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/738,400 US20040151951A1 (en) | 2002-12-17 | 2003-12-17 | Lithium based electrochemical cell systems |
| US11/943,462 US8168325B2 (en) | 2002-12-17 | 2007-11-20 | Lithium based electrochemical cell systems having a degassing agent |
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| Application Number | Priority Date | Filing Date | Title |
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| US43421402P | 2002-12-17 | 2002-12-17 | |
| US10/738,400 US20040151951A1 (en) | 2002-12-17 | 2003-12-17 | Lithium based electrochemical cell systems |
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| US11/943,462 Expired - Fee Related US8168325B2 (en) | 2002-12-17 | 2007-11-20 | Lithium based electrochemical cell systems having a degassing agent |
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Cited By (40)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050019670A1 (en) * | 2003-07-17 | 2005-01-27 | Khalil Amine | Long life lithium batteries with stabilized electrodes |
| US20050233220A1 (en) * | 2004-02-06 | 2005-10-20 | Gozdz Antoni S | Lithium secondary cell with high charge and discharge rate capability |
| US20060147809A1 (en) * | 2004-05-28 | 2006-07-06 | The University Of Chicago | Long life lithium batteries with stabilized electrodes |
| US20060240322A1 (en) * | 2005-04-25 | 2006-10-26 | Ferro Corporation | Non-aqueous electrolytic solution with mixed salts |
| US20060240327A1 (en) * | 2005-04-25 | 2006-10-26 | Ferro Corporation | Non-aqueous electrolytic solution |
| US20060236528A1 (en) * | 2005-04-25 | 2006-10-26 | Ferro Corporation | Non-aqueous electrolytic solution |
| US20060269844A1 (en) * | 2005-05-26 | 2006-11-30 | Ferro Corporation | Triazine compounds for removing acids and water from nonaqueous electrolytes for electrochemical cells |
| US20060269845A1 (en) * | 2005-05-26 | 2006-11-30 | Ferro Corporation | Nonaqueous electrolytic solution for electrochemical cells |
| US20060269846A1 (en) * | 2005-05-26 | 2006-11-30 | Ferro Corporation | Nonaqueous electrolytic solution for electrochemicals cells |
| US20070111099A1 (en) * | 2005-11-15 | 2007-05-17 | Nanjundaswamy Kirakodu S | Primary lithium ion electrochemical cells |
| US20070166617A1 (en) * | 2004-02-06 | 2007-07-19 | A123 Systems, Inc. | Lithium secondary cell with high charge and discharge rate capability and low impedance growth |
| US20090029248A1 (en) * | 2005-01-26 | 2009-01-29 | Masaki Deguchi | Nonaqueous electrolyte and secondary battery containing same |
| US20090263707A1 (en) * | 2008-04-16 | 2009-10-22 | Buckley James P | High Energy Lithium Ion Secondary Batteries |
| US20090305131A1 (en) * | 2008-04-25 | 2009-12-10 | Sujeet Kumar | High energy lithium ion batteries with particular negative electrode compositions |
| US20100086854A1 (en) * | 2008-09-30 | 2010-04-08 | Sujeet Kumar | Fluorine doped lithium rich metal oxide positive electrode battery materials with high specific capacity and corresponding batteries |
| US20100119942A1 (en) * | 2008-11-11 | 2010-05-13 | Sujeet Kumar | Composite compositions, negative electrodes with composite compositions and corresponding batteries |
| US20100285355A1 (en) * | 2009-05-08 | 2010-11-11 | Robert Bosch Gmbh | Li-ION BATTERY WITH POROUS ANODE SUPPORT |
| WO2010129859A1 (en) * | 2009-05-08 | 2010-11-11 | Robert Bosch Gmbh | Li-ion battery with over-charge/over-discharge failsafe |
| US20110017528A1 (en) * | 2009-07-24 | 2011-01-27 | Sujeet Kumar | Lithium ion batteries with long cycling performance |
| US20110076572A1 (en) * | 2009-09-25 | 2011-03-31 | Khalil Amine | Non-aqueous electrolytes for electrochemical cells |
| US20110086248A1 (en) * | 2008-06-04 | 2011-04-14 | Kensuke Nakura | Assembled battery |
| US20110111298A1 (en) * | 2009-11-11 | 2011-05-12 | Lopez Herman A | Coated positive electrode materials for lithium ion batteries |
| US20110136019A1 (en) * | 2009-12-04 | 2011-06-09 | Shabab Amiruddin | Lithium ion battery with high voltage electrolytes and additives |
| US20110236751A1 (en) * | 2010-03-26 | 2011-09-29 | Shabab Amiruddin | High voltage battery formation protocols and control of charging and discharging for desirable long term cycling performance |
| US8076032B1 (en) * | 2004-02-04 | 2011-12-13 | West Robert C | Electrolyte including silane for use in electrochemical devices |
| US20120115041A1 (en) * | 2003-09-10 | 2012-05-10 | West Robert C | Electrochemical device having electrolyte including disiloxane |
| US20120135313A1 (en) * | 2004-02-04 | 2012-05-31 | West Robert C | Electrolyte including silane for use in electrochemical devices |
| US8741484B2 (en) | 2010-04-02 | 2014-06-03 | Envia Systems, Inc. | Doped positive electrode active materials and lithium ion secondary battery constructed therefrom |
| US9083062B2 (en) | 2010-08-02 | 2015-07-14 | Envia Systems, Inc. | Battery packs for vehicles and high capacity pouch secondary batteries for incorporation into compact battery packs |
| US9093722B2 (en) | 2010-09-30 | 2015-07-28 | Uchicago Argonne, Llc | Functionalized ionic liquid electrolytes for lithium ion batteries |
| US9159990B2 (en) | 2011-08-19 | 2015-10-13 | Envia Systems, Inc. | High capacity lithium ion battery formation protocol and corresponding batteries |
| US9166222B2 (en) | 2010-11-02 | 2015-10-20 | Envia Systems, Inc. | Lithium ion batteries with supplemental lithium |
| US9780358B2 (en) | 2012-05-04 | 2017-10-03 | Zenlabs Energy, Inc. | Battery designs with high capacity anode materials and cathode materials |
| US10020491B2 (en) | 2013-04-16 | 2018-07-10 | Zenlabs Energy, Inc. | Silicon-based active materials for lithium ion batteries and synthesis with solution processing |
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Also Published As
| Publication number | Publication date |
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| US8168325B2 (en) | 2012-05-01 |
| US20080070121A1 (en) | 2008-03-20 |
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