WO2001091208A2 - Lithium-ion electrochemical cell and battery - Google Patents
Lithium-ion electrochemical cell and battery Download PDFInfo
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- WO2001091208A2 WO2001091208A2 PCT/US2001/040781 US0140781W WO0191208A2 WO 2001091208 A2 WO2001091208 A2 WO 2001091208A2 US 0140781 W US0140781 W US 0140781W WO 0191208 A2 WO0191208 A2 WO 0191208A2
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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
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
- H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
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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
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
- H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
- H01M50/417—Polyolefins
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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
- H01M10/0568—Liquid materials characterised by the solutes
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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
- H01M10/0569—Liquid materials characterised by the solvents
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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
- H01M4/362—Composites
- H01M4/364—Composites as mixtures
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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
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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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
- H01M4/04—Processes of manufacture in general
- H01M4/043—Processes of manufacture in general involving compressing or compaction
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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
- the present invention relates generally to improvements in a lithium-ion electrochemical cell and battery, including the use of carbon- carbon composite as active material for the negative electrode (anode) to improve (i) cycle life and self discharge characteristics, (ii) overcharge and overdischarge acceptance ability, and (iii) cathode utilization characteristics of such cell and battery.
- lithium-ion batteries carbon or graphite is used as an anode, a lithiated transition metal intercalation compound is used as a cathode and LiPF ⁇ is used as an electrolyte in carbonate-based organic solvents.
- LiPF ⁇ is used as an electrolyte in carbonate-based organic solvents.
- hard carbon or graphite is used as active anode material in commercial lithium-ion batteries.
- Polyvinyledene fluoride (PVDF) is used as a binder to improve the mechanical integrity of the electrode.
- Copper is universally used as the substrate for anode.
- Hard carbon or graphite material is mixed with PVDF in an organic solvent and the mixture is coated on the copper substrate to produce the anode.
- Another disadvantage of the state-of-the-art lithium-ion battery is its relatively high self-discharge.
- the present lithium-ion battery loses 7% to 12% capacity per month at ambient temperature. The loss is even higher at higher temperatures.
- the present state-of-the-art lithium-ion cells require overcharge/overdischarge protection circuits and/or devices so that the cells can charge and discharge within certain voltage regimes.
- Overdischarge causes dissolution of copper that is used as the substrate for carbon anode and degrades cell performance.
- overcharge/overdischarge protection circuits and/or devices also increase(s) the weight and cost of the lithium-ion cell. Reliable and inexpensive overcharge/overdischarge protection for multi-cell lithium-ion battery is a major obstacle to commercialization of the systems in electric vehicle and other high voltage applications.
- LiCoO 2 , LiNiCoO 2 , and LiMn 2 ⁇ 4 are attractive as cathode materials for lithium-ion battery systems.
- LiCoO 2 and LiNiCoO 2 have a layered structure, where lithium and transition metal cations occupy alternate layers of octahedral sites in a distorted cubic close-packed oxygen-ion lattice.
- the layered metal oxide framework provides a two-dimensional interstitial space, which allows for easy removal of the lithium ions.
- the Li n 2 O 4 spinel framework possesses a three-dimensional space via face sharing octahedral and tetrahedral structures, which provide conducting pathways for the insertion and extraction of lithium ions.
- LiCoO 2 ⁇ LH.XCOO2 + xLi + + xe LiNiCoO 2 ⁇ Li 1 . x NiCoO 2 + xLi + + xe " LiMn 2 O 4 ⁇ - Li 1 . ⁇ Mn 2 O 4 + x i + + xe "
- the value of x for LiCoO 2 is less than or equal to 0.5 (-140 mAh/g), for UNiCoO 2 , x is less than or equal to 0.6 (-165 mAh/g) and for LiMn 2 O 4 , x is less than or equal to 0.85 (-125 mAh/g).
- the value of x of these cathode materials can be increased at if the cell is charged at higher voltage. If an anode can accept higher cathode capacity at higher voltage without plating metallic lithium and deteriorating mechanical integrity (cycle life), a lithium-ion battery system with higher specific energy and energy density may result.
- the present state-of-the-art lithium-ion battery systems which use anodes of relatively poor mechanical integrity and low active materials limit their charge voltages to relatively low values and thereby limit the cathode capacity utilization. If the present anode with copper substrate was loaded with more active anode material, the resulting anode will be thicker and heavier and will result in lower cycle life without significant improvement in specific energy (Wh/kg) and energy density (Wh/I).
- the present invention provides new and useful concepts in a lithium-ion electrochemical cell and battery, including the use of carbon- carbon composite as active material for the anode, to improve (i) cycle life and self discharge characteristics, (ii) overcharge and overdischarge acceptance ability, and (iii) cathode utilization.
- Cycle Life and Self Discharge It is a primary objective of the present invention to improve the cycle life of lithium-ion electrochemical cells and battery systems using such cells.
- Another objective of the present invention is to improve the self- discharge characteristics of lithium-ion electrochemical cells and battery systems using such cells.
- the anode comprises carbon- carbon composite material, having high electronic conductivity and high lithium-ion intercalation capacity.
- the composite can accept repeated expansion and contraction as a result of intercalation and de-intercalation of lithium-ions during charge-discharge process with a little or no change in mechanical integrity.
- the impedance of the anode therefore, remains almost the same.
- the cycling behavior of the lithium-ion cells made with the carbon- carbon composite shows significant improvement.
- a carbon- carbon composite electrode consists of a single phase, does not contain any binder and there is no metal carbon interface. The self-discharge behavior of an electrochemical cell made with the carbon-carbon composite material as anode is, therefore, improved.
- carbon film of high electronic conductivity provides a carbon based substrate, and on which carbon material having high lithium-ion intercalation capacity is coated to produce the anode.
- Carbon-carbon composite of high electrical and thermal conductivity can also be used to form the anode.
- the substrate of the carbon- carbon composite anode is carbon, and the lithium-ion cell can accept repeated overdischarge without performance degradation.
- the anode substrate and anode itself comprises carbon material, and each can accept lithium-ions during charge from cathode of lithiated intercalation compounds.
- the substrate can, therefore, act as a sink of lithium-ions.
- additional lithium- ions from the cathode can, therefore, be stored to the anode substrate without causing metallic lithium deposition.
- the anode made according to this aspect of the present invention allows the acceptance ability for overcharge and overdischarge of a lithium- ion cell.
- the present invention improves the specific energy and energy density of lithium-ion electrochemical cells and battery systems using such cells.
- a lithium-ion cell structure having an anode comprising a carbon-carbon composite with a deliverable capacity at least 65% of the theoretical capacity of the cathode of the cell.
- the cell is charged at a potential configured to optimize the energy density of the cell, to improve cathode capacity utilization and thereby improve the specific energy and energy density of the cells and batteries.
- Figure 1 is a schematic representation of a lithium-ion cell embodying a carbon substrate based anode in accordance with the present invention.
- Figure 2 is a graph representing the cycling behavior of a lithium-ion cell made with carbon-carbon composite anode in accordance with the present invention
- Figure 3 represents the cycle life of a lithium-ion cell made in accordance with the prior art
- Figure 4 represents a comparison of the cycling behavior of lithium-ion cells made in accordance with the prior art (1) and in accordance with the present invention (2);
- Figure 5 represents a comparison of the voltage decay of lithium-ion cells made in accordance with the prior art (1 )and in accordance with the present invention (2);
- Figure 6 represents the discharge behavior (before-1 and after storage- 2) of a lithium-ion cell made in accordance with the prior art
- Figure 7 represents the discharge behavior (before-1 and after storage- 2) of a lithium-ion cell made in accordance with the present invention.
- Figure 8 is a graph representing the overdischarge characteristics of a lithium-ion cell made in accordance with the present invention.
- Figure 9 represents voltage and temperature responses during overcharge of a lithium-ion cell made in accordance with the present invention.
- Figure 10 represents repeated overcharge/overdischarge characteristics of a lithium-ion cell made in accordance with the present invention.
- Figure 11 is a graph representing the cathode capacity utilization of a lithium-ion cell made with carbon-carbon composite anode and lithium nickel cobalt dioxide cathode at different charge voltages in accordance with the present invention
- Figure 12 represents the deliverable capacity of a lithium-ion cell with respect to the total weight of the negative and positive electrodes made in accordance to the present invention
- Figure 13 represents the cycling behavior at higher cathode capacity utilization of a lithium-ion cell made in accordance with the present invention
- Figure 14 represents the cathode capacity utilization of a lithium-ion cell made in accordance with Example 7;
- Figure 15 represents the deliverable capacity of a lithium-ion cell with respect to the total weight of the negative and positive electrodes made in accordance with Example 7.
- Figure 16 represents a comparison of the cycling behavior of lithium- ion cells made in accordance with Example 7 (1 ) and in accordance with the present invention (2); DETAILED DESCRIPTION
- a lithium-ion cell is comprised of a negative electrode of carbon-carbon composite material heat treated in the range of 1000°C to 3000°C and having high electronic and thermal conductivity, and a positive electrodes containing LiCoO 2 , LiNiO 2 , LiNiCoO 2 , LiMn 2 O 4 , LiMnO 2 , LiV 2 O 5 , LiV 6 O ⁇ 3 , LiTiS 2 , Li 3 FeN 2 , Li 7 VN 4 , U 7 M0N 4 , Li 2 ZrN 2 or combinations of these materials.
- the carbon-carbon composite material is also used as the substrate for the negative electrode.
- the electrolyte used in a lithium-ion cell and battery of the present invention is a non-aqueous aprotic organic electrolyte and preferably a non- aqueous solution consisting of a solute, such as LiPF 6 , UBF , LiAsF ⁇ , LiCF 3 SO 3 , LiN(CF 3 SO 2 ) 2 or LiCIO 4 , dissolved in a solvent such as propylene carbonate, ethylene carbonate, diethyl carbonate, dimethyl carbonate, ethyl methyl carbonate and as well as mixtures thereof.
- a solute such as LiPF 6 , UBF , LiAsF ⁇ , LiCF 3 SO 3 , LiN(CF 3 SO 2 ) 2 or LiCIO 4
- a solvent such as propylene carbonate, ethylene carbonate, diethyl carbonate, dimethyl carbonate, ethyl methyl carbonate and as well as mixtures thereof.
- the carbon-carbon composite is made for this invention by heat treating at the temperature range of 1000-3000°C in inert atmosphere and can have density, specific resistance, and thermal conductivity in the range of 1.3-2.0 g/cc, 50- 1 ,000 ⁇ ohm-cm, and 50-600 Wm "1 K "1 , respectively.
- the carbon fiber used to make the carbon-carbon composite can be pitch-, PAN-, and/or rayon-based fiber.
- pitch and PAN-based fibers are preferable.
- the present invention is not limited to any specific approach to produce carbon- carbon composite.
- a preferred form of lithium-ion cell embodying a carbon-carbon composite anode is shown in Figure 1. Wherein the assembled cell 101 is shown with the anode, cathode, and electrolyte enclosed in a sealed sandwich structure with the carbon-carbon composite anode electrically accessible by means of protruding nickel conductive tab 102 and the lithiated intercalation compound cathode electrically accessible by means of a protruding conductive aluminum tab 103.
- the anode (not shown) and cathode (not shown) of the assembled cell 101 are separated by a porous separator (not shown) that is permeated with an aprotic non-aqueous electrolyte (not shown) that is in effective contact with both the anode and cathode.
- FIG. 1 above the assembled cell 101 , there is also shown the components of the cell 101 , comprised of a pair of one-sided cathodes 104A and 104B and a carbon-carbon composite anode 105, suitable to be assembled as a sandwich (cell 101) with the anode 105 positioned between the respective cathodes 104A and 104B being separated from the anode 105 by respective porous separators 106A and 106B that are permeated with an aprotic, non-aqueous electrolyte that is in effective contact with both the cathode and the facing anodes.
- aprotic, non-aqueous electrolyte that is in effective contact with both the cathode and the facing anodes.
- Conductive aluminum tabs 103A and 103B are provided for the respective cathodes 104A and 104B and a nickel conductive tab 102A is provided for the anode 105, whereby the respective electrodes of the cell 101 are electrically accessible when assembled as a sandwich and enclosed within a sealed enclosure.
- the materials of the respective anodes and cathodes of the cell 101 may be formed of materials, as described herein in further detail.
- the anode comprises carbon-carbon composite.
- the cathode may be formed of LiCoO 2 , LiNiCoO 2 , LiNiO 2 , LiMn 2 O 4 , LiMnO 2 , LiV 2 O 5 , LiV 6 O ⁇ 3 , LiTiS 2 , Li 3 FeN 2 , Li 7 VN 4 , Li 7 MoN 4 , Li 2 ZrN 2 or a combination thereof, supported by an aluminum foil substrate.
- the respective anode and cathode electrodes are maintained spaced from one another by a respective electrically non-conductive separator that is permeable, whereby the aprotic, non-aqueous electrolyte is carried by the spacers and maintained in effective electrochemical contact with both the cathode and facing anode.
- the permeable separator may be formed of a micro-porous poly-olefin film.
- a plurality of electrochemical cells as described above can be used to assemble a battery of such cells by connecting the respective electrodes of the assembly of cells in an electrical circuit and in a known fashion to produce a battery with the voltage or current characteristics as determined by the number of cells connected in series or parallel circuit relationship.
- Carbon-carbon composite heat-treated to 2600°C in an inert atmosphere was used as an anode of a lithium-ion cell to evaluate the concept of the present invention.
- the carbon-carbon composite was used as a thin film of thickness 300 ⁇ m.
- the lithium-ion cell included a negative electrode made from the carbon-carbon composite, a lithiated nickel dioxide positive electrode and 1M LiPF ⁇ electrolyte in a mixture (1 :1 v/v) of ethylene carbonate/dimethyl carbonate (EC/DMC) solvents.
- EC/DMC ethylene carbonate/dimethyl carbonate
- a micro-porous poly-olefin (Celgard 2400) separator was used in between the positive and negative electrodes to isolate them electronically.
- the positive electrode was made from a mixture of 85% LiNi ⁇ 8 C ⁇ o.
- the developed cell was charged at a constant current of 0.5 mA/cm 2 to
- FIG. 1 shows the cycling characteristics of the developed cell according to the present invention.
- the cell delivered 580 cycles with 91.8% capacity retention.
- a lithium-ion cell was made with the same components as described above except the negative electrode was made from a mixture of 90% MCMB 2528 carbon and 10% PVDF in DMF by coating on to a copper foil. It is noteworthy to mention that MCMB 2528 carbon is used as an active material of anode for commercial lithium-ion cell.
- the cell was charged and discharged under the same conditions as the previous cell.
- Figure 3 shows the cycling behavior of this prior art cell. The cell lost 20% capacity after delivering only 557 cycles.
- Figure 4 shows a comparison to the cycling behavior of the cell made in accordance to the present invention (shown at 2 in Figure 4 and that made according to the prior art (shown at 1 in Figure 4).
- a lithium-ion cell was made as in Example 1 with the carbon-carbon composite heat treated to 2800°C as anode, lithiated cobalt oxide as active cathode material and an electrolyte comprising 1 M LiPF ⁇ in a mixture of ethylene carbonate and diethyl carbonate (1:1 v/v).
- the cell was first charged at a constant current of 0.5 mA/cm 2 to 4.1 V and then at a constant voltage (4.1 V) for a period of three hours or until the current dropped to 0.02 mA/cm 2 .
- the cell was then discharged at a constant current of 0.5 mA/cm 2 to a cut-off voltage of 3.0 V.
- the charge-discharge process was repeated at least two times in order to obtain a cycling efficiency greater than 99%.
- the cell was then fully charged and left at open-circuit voltage (OCV) at ambient temperatures to evaluate the self-discharge behavior.
- OCV open-circuit voltage
- the cell was left at OCV for a period of a month (720 hours). After storage, the cell was discharged at a constant current of 0.5 mA/cm 2 to a cut-off voltage Of 3.0 V.
- a lithium ion cell was made with the same components as described above except the negative electrode was made from a mixture of 90% MCMB 2528 carbon and 10% PVDF in DMF by coating on to a copper foil. The above experimental steps were repeated with the cell.
- Figure 5 shows a comparison of voltage decay with time for the lithium- ion cells made in accordance with the present invention (shown at 2 in Figure 5) and in accordance with the prior art (shown at 1 in Figure 5).
- a voltage decay of only 10 mV was observed with the cell made in accordance to the present invention.
- a voltage decay of 60 mV was observed.
- the discharge behavior (before and after storage; the "before” is shown at 1 and “after” is shown at 2 in Figure 6) of the lithium-ion cell made in accordance with the prior art is shown in Figure 6.
- the cell lost a capacity of 11% due to storage for a month.
- Figure 7 shows the discharge behavior (before and after storage; the "before” is shown at 1 and “after” is shown at 2 in Figure 7) of the lithium-ion cell made in accordance with the present invention. This cell lost only 2% capacity after storage for a month.
- Example 3 Commercially available carbon conductive film (COER-X from REXAM) was used as a substrate for anode of a lithium-ion cell to evaluate the overcharge/overdischarge aspect of the present invention.
- the anode was made from a mixture of 90% MCMB 2528 graphite and 10% PVDF in DMF by coating on to the carbon film.
- the lithium-ion cell included the negative electrode, a lithiated cobalt dioxide positive electrode and 1 M LiPF 6 electrolyte in a mixture (1 :1 v/v) of ethylene carbonate/dimethyl carbonate (EC/DMC) solvents.
- EC/DMC ethylene carbonate/dimethyl carbonate
- a micro-porous poly-olefin (Celgard 2400) separator was used in between the positive and negative electrodes to isolate them electronically.
- the positive electrode was made from a mixture of 85% LiCoO 2 , 6% carbon black and 9% PVDF in DMF by coating on to an aluminum foil.
- the developed cell was charged at a constant current of 30 mA to 4.1
- FIG. 8 represents a plot of repeated overdischarge.
- the cell was discharged at a constant current of 30 mA to -1.0 V. For the first two cycles, the cell was charged to 4.1 V and for the last two cycles, the charge voltage was 4.2 V.
- the capacities delivered during overdischarges are 180 mAh, 179 mAh, 193 mAh, and 193 mAh for the 1 to 4 cycles, respectively. The cell did not show any performance degradation.
- Two lithium-ion cells were made as in Example 3 with the carbon- carbon composite heat treated to 2800°C as anode, lithiated cobalt oxide as active cathode material and an electrolyte comprising 1M LiPF ⁇ in a mixture of ethylene carbonate and diethyl carbonate (1 :1 v/v).
- the cells were first charged at a constant current of 0.5 mA/cm 2 to 4.1 V and then at a constant voltage (4.1 V) for a period of three hours or until the current dropped to 0.02 mA/cm 2 .
- the cells were then discharged at a constant current of 0.5 mA/cm 2 to a cut-off voltage of 3.0 V.
- the charge-discharge process was repeated at least two times in order to obtain a cycling efficiency greater than 99%.
- the cells were then used to carry out the overcharge experiment.
- the cells were overcharged at 1 C and C/3 rates.
- the voltage and temperature responses of the fully charged cells during overcharge at two different rates are shown in Figure 9.
- the temperatures recorded were the outside body temperature of the cells.
- a lithium-ion cell was made as in Example 3 with the carbon-carbon composite heat treated to 2600°C as anode, lithiated cobalt oxide as active cathode material and an electrolyte comprising 1 M LiPF 6 in a mixture of ethylene carbonate and diethyl carbonate (1 :1 v/v).
- the cell was first charged at a constant current of 0.5 mA/cm 2 to 4.1 V and then at a constant voltage (4.1 V) for a period of three hours or until the current dropped to 0.02 mA/cm 2 .
- the cell was then discharged at a constant current of 0.5 mA/cm 2 to a cut-off voltage of 3.0 V.
- the charge-discharge process was repeated at least two times in order to obtain a cycling efficiency greater than 99%.
- the cell was then used to carry out repeated overcharge/overdischarge experiment.
- Figure 10 shows the repeated overcharge-overdischarge characteristics at 50 mA of the lithium-ion cell made in accordance with the present invention. There was no safety hazard or thermal run away of the cell. The cell can accept repeated overcharge and overdischarge and still deliver excellent capacity.
- Carbon-carbon composite heat-treated to 2400°C in an inert atmosphere was used as an anode of a lithium-ion cell to evaluate the concept of the present invention.
- the carbon-carbon composite was used as a thin film of 210 ⁇ m thickness.
- the lithium-ion cell included a negative electrode made from the carbon-carbon composite, a lithiated nickel cobalt dioxide positive electrode and 1 M LiPF ⁇ electrolyte in a mixture (1 :1 v/v) of ethylene carbonate/dimethyl carbonate (EC/DMC) solvents.
- the total weight of the negative electrode was 0.76 g.
- a micro-porous poly-olefin (Celgard 2400) separator was used in between the positive and negative electrodes to isolate them electronically.
- the positive electrode was made from a mixture of 85% LiNi 0 . 8 C ⁇ o.2 ⁇ 2 , 6% carbon black and 9% PVDF in DMF by coating on to an aluminum foil.
- the weight of the cathode excluding the weight of aluminum foil was 1.1 g.
- the developed cell was charged at a constant current of 0.5 mA/cm 2 to 4.0 V and then at a constant voltage (4.0 V) for 3 hours or until the current dropped to 0.02 mA/cm 2 .
- the cell was then discharged at a constant current of 0.5 mA/cm 2 to a cut-off voltage of 2.50 V.
- the cell was then charged at 4.2 V and 4.3 V and discharged to 2.5 V in order to obtain the deliverable discharge capacities under these conditions.
- Figure 11 shows the cathode capacity utilization of the cell.
- Figure 12 represents the deliverable capacity of the cell with respect to the total weight of negative and positive electrodes.
- the charge discharge process was repeated at a charge voltage of 4.2 V in order to evaluate the cycle life.
- Figure 13 shows the cycling characteristics of the developed cell according to the present invention.
- Example 7 A lithium-ion cell was made with the same components as described in
- Example 6 except the negative electrode was made from a mixture of 90% MCMB 2528 carbon and 10% PVDF in DMF by coating on to a copper foil. It is noteworthy to mention that MCMB 2528 carbon is used as an active material of anode for commercial lithium-ion cell.
- the total weight of the negative electrode was 1.3 g of which 0.76 g was for MCMB, 0.08 g was for PVDF, and 0.46 g was for copper foil.
- the anode was 240 ⁇ m thick.
- the objective of the cell of Example 7 was to use components similar to those currently used to create lithium-ion cells, but to compensate the theoretical capacity of the cathode, by using higher amount of anode material.
- Figure 14 shows the cathode capacity utilization of the cell of Example 7 at different charge voltage.
- Figure 15 represents the deliverable capacities of the cell of Example 1 with respect to the total weight of negative and positive electrodes at different charge voltages. The deliverable capacities of this cell are significantly lower (and hence energy density) than that obtained from the cell made in accordance to the present invention (Example 6) particularly at higher cathode utilization voltage.
- Figure 16 shows a comparison to the cycling behavior of the cells made in accordance to the present invention (shown at 2 in Figure 16) and that made according to Example 7 (shown at 1 in Figure 16). The capacity fade on cycling of the cell of Example 7 is very high at higher cathode utilization voltage.
Abstract
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Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2001268747A AU2001268747A1 (en) | 2000-05-24 | 2001-05-22 | Lithium-ion electrochemical cell and battery |
JP2001587501A JP5069836B2 (en) | 2000-05-24 | 2001-05-22 | Lithium ion electrochemical battery and storage battery |
EP01946735A EP1340275A2 (en) | 2000-05-24 | 2001-05-22 | Lithium-ion electrochemical cell and battery |
KR1020027015846A KR100830247B1 (en) | 2000-05-24 | 2001-05-22 | Lithium-ion electrochemical cell and battery |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
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US09/577,638 | 2000-05-24 | ||
US09/577,639 | 2000-05-24 | ||
US09/577,638 US6436576B1 (en) | 2000-05-24 | 2000-05-24 | Carbon-carbon composite as an anode for lithium secondary non-aqueous electrochemical cells |
US09/577,639 US6489061B1 (en) | 2000-05-24 | 2000-05-24 | Secondary non-aquenous electrochemical cell configured to improve overcharge and overdischarge acceptance ability |
US26477201P | 2001-01-29 | 2001-01-29 | |
US60/264,772 | 2001-01-29 |
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WO2001091208A2 true WO2001091208A2 (en) | 2001-11-29 |
WO2001091208A3 WO2001091208A3 (en) | 2002-03-07 |
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PCT/US2001/040781 WO2001091208A2 (en) | 2000-05-24 | 2001-05-22 | Lithium-ion electrochemical cell and battery |
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---|---|
EP (1) | EP1340275A2 (en) |
JP (1) | JP5069836B2 (en) |
KR (2) | KR100830247B1 (en) |
AU (1) | AU2001268747A1 (en) |
WO (1) | WO2001091208A2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6949314B1 (en) | 2002-08-19 | 2005-09-27 | Litech, L.L.C. | Carbon-carbon composite anode for secondary non-aqueous electrochemical cells |
EP2436077A1 (en) * | 2009-05-26 | 2012-04-04 | Searete LLC | System and method of altering temperature of an electrical energy storage device or an electrochemical energy generation device using high thermal conductivity materials |
US8715875B2 (en) | 2009-05-26 | 2014-05-06 | The Invention Science Fund I, Llc | System and method of operating an electrical energy storage device or an electrochemical energy generation device using thermal conductivity materials based on mobile device states and vehicle states |
US8802266B2 (en) | 2009-05-26 | 2014-08-12 | The Invention Science Fund I, Llc | System for operating an electrical energy storage device or an electrochemical energy generation device using microchannels based on mobile device states and vehicle states |
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EP0803926A2 (en) * | 1990-09-03 | 1997-10-29 | Matsushita Electric Industrial Co., Ltd. | A secondary battery or cell with a non-aqueous electrolyte |
WO1998047195A1 (en) * | 1997-04-15 | 1998-10-22 | Duracell Inc. | Process for improving lithium ion cell |
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JPH05283061A (en) * | 1992-03-31 | 1993-10-29 | Osaka Gas Co Ltd | Negative electrode for lithium secondary battery and lithium secondary battery using same electrode |
JPH06223821A (en) * | 1993-01-22 | 1994-08-12 | Tokai Carbon Co Ltd | Manufacture of negative electrode for lithium secondary battery |
JPH08138651A (en) * | 1994-11-08 | 1996-05-31 | Dainippon Ink & Chem Inc | Carbonaceous electrode plate for non-aqueous electrolyte secondary battery and secondary battery |
JPH1021916A (en) * | 1996-07-05 | 1998-01-23 | Toyota Central Res & Dev Lab Inc | Manufacture of carbon substrate for lithium secondary battery negative electrode, and negative electrode for lithium secondary battery |
JP3698516B2 (en) * | 1997-03-18 | 2005-09-21 | パイロットプレシジョン株式会社 | Film electrode and manufacturing method thereof |
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- 2001-05-22 AU AU2001268747A patent/AU2001268747A1/en not_active Abandoned
- 2001-05-22 WO PCT/US2001/040781 patent/WO2001091208A2/en active Application Filing
- 2001-05-22 KR KR1020027015846A patent/KR100830247B1/en not_active IP Right Cessation
- 2001-05-22 KR KR1020087000947A patent/KR20080011352A/en not_active Application Discontinuation
- 2001-05-22 JP JP2001587501A patent/JP5069836B2/en not_active Expired - Fee Related
- 2001-05-22 EP EP01946735A patent/EP1340275A2/en not_active Withdrawn
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EP0803926A2 (en) * | 1990-09-03 | 1997-10-29 | Matsushita Electric Industrial Co., Ltd. | A secondary battery or cell with a non-aqueous electrolyte |
WO1998047195A1 (en) * | 1997-04-15 | 1998-10-22 | Duracell Inc. | Process for improving lithium ion cell |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6949314B1 (en) | 2002-08-19 | 2005-09-27 | Litech, L.L.C. | Carbon-carbon composite anode for secondary non-aqueous electrochemical cells |
EP2436077A1 (en) * | 2009-05-26 | 2012-04-04 | Searete LLC | System and method of altering temperature of an electrical energy storage device or an electrochemical energy generation device using high thermal conductivity materials |
EP2436077A4 (en) * | 2009-05-26 | 2013-07-17 | Searete Llc | System and method of altering temperature of an electrical energy storage device or an electrochemical energy generation device using high thermal conductivity materials |
US8715875B2 (en) | 2009-05-26 | 2014-05-06 | The Invention Science Fund I, Llc | System and method of operating an electrical energy storage device or an electrochemical energy generation device using thermal conductivity materials based on mobile device states and vehicle states |
US8802266B2 (en) | 2009-05-26 | 2014-08-12 | The Invention Science Fund I, Llc | System for operating an electrical energy storage device or an electrochemical energy generation device using microchannels based on mobile device states and vehicle states |
US9065159B2 (en) | 2009-05-26 | 2015-06-23 | The Invention Science Fund I, Llc | System and method of altering temperature of an electrical energy storage device or an electrochemical energy generation device using microchannels |
US9093725B2 (en) | 2009-05-26 | 2015-07-28 | The Invention Science Fund I, Llc | System for altering temperature of an electrical energy storage device or an electrochemical energy generation device using microchannels based on states of the device |
US9433128B2 (en) | 2009-05-26 | 2016-08-30 | Deep Science, Llc | System and method of operating an electrical energy storage device or an electrochemical energy generation device, during charge or discharge using microchannels and high thermal conductivity materials |
Also Published As
Publication number | Publication date |
---|---|
KR20030005388A (en) | 2003-01-17 |
WO2001091208A3 (en) | 2002-03-07 |
JP2003534636A (en) | 2003-11-18 |
KR20080011352A (en) | 2008-02-01 |
JP5069836B2 (en) | 2012-11-07 |
EP1340275A2 (en) | 2003-09-03 |
AU2001268747A1 (en) | 2001-12-03 |
KR100830247B1 (en) | 2008-05-16 |
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