DELITHIATED COBALT OXIDE AND NICKEL OXIDE PHASES AND METHOD OF PREPARING SAME

Abstract: LiCoO2 and LiNiO2 are fully delithiated electrochemically using solid state electrolytic cells and oxidation-resistant electrolytes to yield new, stable phases of CoO2 and NiO2

Description: DELITHIATED COBALT OXIDE AND NICKEL OXIDE PHASES AND METHOD OF PREPARING SAME BACKGROUND OF THE INVENTION The increasing commercial importance of rechargeable lithium ion battery cells has prompted a desire to identify and to prepare cathode materials better able to reversibly intercalate and deintercalate lithium ions at greater voltages- There are three prominent reversible lithium intercalation compounds used for lithium ion rechargeable batteries: LiCo0 2 and LiNi0 2 compounds, as well as LiMn 2 0 4 spinel. LiCo0 2 cells are of particular interest because of their ability to insert/deinsert lithium reversibly at voltages greater than 4V resulting in batteries that have an output voltage and an energy density 3 times greater than Ni-Cd. The theoretical charge capacity of LiCo0 2 cells is large at about 275 Amp-hours/kilogram (A-h/kg) . In practical application, however, the maximum obtainable capacity for LiCo0 2 cells has been only about 140 A-h/kg, corresponding to a maximum charge voltage of about 4.2 V. Previous attempts to exceed this charge cutoff voltage in LiCo0 2 cells have caused poor cell performance manifested by severe loss of charge capacity in subsequent charge-discharge cycles. The commonly-held reason for the 4.2 volt charge limitation for LiCo0 2 cells was that electrochemical delithiation of LiCo0 2 above this voltage destabilized the structure of the partially delithiated LiCo0 2 phase, impairing intercalation of lithium in subsequent charge-discharge cycles. Lithium cobalt oxide adopts a hexagonal structure consisting of Co0 2 layers separated by a Van der Waals gap'. The octahedral sites within the Van der Waals gap are occupied by the Li + ions. This results in the reversible intercalation of lithium. In such compounds, lithium acts as a glue or cement, screening the repulsive interactions between the negatively charged Co0 2 layers. When the compound is fully lithiated LiCo0 2 , the screening effect is greatest. As lithium is removed, the screening effect is decreased and the repulsions between the two Co0 2 layers are enhanced resulting in an expansion of the c-axis parameter. Due to the screening effect of lithium, it was believed that complete lithium deintercalation to form Co0 2 was not possible. Ohzuku et al. , J. Electrochem . Soc . , Vol. 141, No. 11, Nov. 1994, p. 2972, have succeeded in removing approximately 85% of the lithium. Their efforts revealed a monoclinic phase and questioned the existence of a Co0 2 phase. In another theory, Reimers and Dahn, J. Electrochem. Soc , 139, 2091, (1992), states that excess Co 4 * destroys the crystallinity of the lithium cobalt oxide structure. Apparently, it inhibits the formation of highly crystalline phases at low lithium contents. Wizansky, Rauch, and DiSalvo, Journal of Solid State Chemistry, 81, 203-207 (1989), investigated the delithiation of LiCo0 2 through the use of powerful oxidizing agents such as N0 2 * and MoF 6 . Their results showed that this approach merely decomposes the LiCo0 2 . LiNi0 2 is isostructural with LiCo0 2 and is commercially viable for use in secondary lithium ion batteries. Heretofore, no one has been capable of obtaining the delithiated Ni0 2 phase. Ohzuku et al., J. Electrochem. Soc, Vol. 140, No. 7, July 1993, working with the nickel oxide reported Li 006 NiO 2 and approximated that this was the end phase. Lithium secondary batteries are generally recognized and are described for instance in U.S. Patent No. 5,296,318 to Gozdz et al., which is incorporated in its entirety herein by reference. Lithium metal-free "rocking-chair" batteries may thus be viewed as comprising two lithium-ion-absorbing electrode "sponges" separated by a lithium-ion-conducting electrolyte, usually comprising a Li* salt dissolved in a non- aqueous solvent or mixture of such solvents. Numerous such salts and solvents are known in the arts, as evidence in Canadian Patent Publication No. 2,022,191, dated 30 January 1991. When cells comprising these previously-available electrolytes are cycled to a voltage even slightly greater than 4.3 V, electrolyte oxidation occurs. Although small, this oxidation can jeopardize the capacity, cycle life, and safety of the battery cell. For example, the electrode oxidation reaction consumes part of the charging current, which cannot be recovered when discharging the cell. The result is a continuous loss in the cell capacity over subsequent cycles. Further, if during each charge a small part of the electrolyte is consumed, excess electrolyte must be included when the cell is assembled. The excess electrolyte reduces the amount of active material for a constant volume battery body, thereby decreasing initial capacity. In addition, the oxidation of the electrolyte often generates solid and gaseous by-products. The solid by-products build up a passivating layer on the particles of the active material, essentially increasing the polarization of the cell and lowering the output voltage. Simultaneously, and more importantly, the gaseous by-products increase the internal pressure of the cell, thereby increasing the risk of explosion and leading to unsafe and unacceptable operating conditions. U.S. Patent No. 5,192,629, which is herein incorporated by reference in its entirety, provides a class of electrolyte compositions that are exceptionally useful for minimizing electrolyte decomposition in secondary batteries comprising strongly oxidizing positive electrode materials. These electrolytes are thus uniquely capable of enhancing the cycle life and improving the temperature performance of practical "rocking chair" cells. These electrolyte compositions have a range of effective stability extending up to about 5.0 V at 55°C, as well as at room temperature (about 25°C) . Electrolytes that are substantially inert to oxidation include a 0.5M to 2M solution of LiPF 6 , or LiPF 6 with up to about an equal amount of LiBF 4 added, in a mixture of dimethylcarbonate (DMC) and ethylene carbonate (EC) within the weight percent ratio range from about 95 DMC:5 EC to 20 DMC:80 EC. In a preferred electrolyte solution, the solvent ratio range is about 80 DMC:20 EC to 20 DMC:80 EC. An optimum composition for operation at room temperature and below is an approximately 1.5M LiPF 6 solution in a solvent mixture of about 67 DMC:33 EC. A battery operating at room temperature and higher, e.g., in the range of 55°C, optimally utilizes an electrolyte consisting essentially of an approximately 1.5M LiPF 6 solution in a solvent combination of about 33 DMC:67 EC. An additionally useful electrolyte consists essentially of an approximately 1M to 2M solution of equal parts of LiPF 6 and LiBF 4 in a solvent mixture of about 50 DMC:50 EC. Negligible current increases, after the reversible Li intercalations, at voltages up to about 5 V vs. Li indicates this remarkable stability that enables enhanced cell capacity not only in the "rocking chair" cells comprising negative electrodes of carbon, e.g., petroleum coke, but also in Li negative electrode cells. Such a lithium metal cell utilizing a LiCo0 2 positive electrode may be reasonably expected to achieve normal operating ranges of about 4.3 to 5.1 V. With the aid of electrolytes which are substantially inert to oxidation and solid state electrolytic cells, fully delithiated phases of both Co0 2 and Ni0 2 were obtained. SUMMARY OF THE INVENTION Accordingly, the present invention is directed to metastable Co0 2 and Ni0 2 phases and their use as intercalation compounds for use in lithium ion secondary batteries. Features and advantages of this invention are set forth in the description that follows, and they will be apparent from that description or can be learned by practice of the invention. In one aspect, this invention relates to an electrochemical method for preparing a stable cobalt dioxide phase that includes preparing an electrolytic cell having an anode, an electrolyte substantially inert to oxidation, and a cathode including a lithium cobalt oxide intercalation complex; and applying a voltage to the cell sufficient to completely deintercalate lithium from the lithium cobalt oxide intercalation complex, thereby forming a stable cobalt dioxide phase in the cathode. In a further aspect, this invention relates to a stable cobalt dioxide phase prepared by the foregoing method. In a further aspect, this invention relates to a stable cobalt dioxide phase having the x-ray diffraction pattern: d(A) 4.30 ± 0.02 2.44 ± 0.02 2.12 ± 0.02 1.61 + 0.02 1.41 ± 0.02 1.34 ± 0.02 1.17 + 0.02 In a further aspect, this invention relates to an electrochemical method for preparing a stable nickel dioxide phase that includes providing a lithium nickel oxide intercalation complex having the formula Lij-Ni0 2 wherein x is preferably 0.8 to 1.0, preparing an electrolytic cell having a cathode including the lithium nickel oxide intercalation complex, and applying a voltage to the cell sufficient to' delithiate completely the lithium nickel oxide intercalation complex. In a further aspect, this invention relates to a stable nickel dioxide phase prepared by the above described process. In a further aspect, this invention relates to a stable nickel dioxide phase having the x-ray diffraction pattern: d(A) 4.47 ± 0.02 2.40 ± 0.02 2.29 ± 0.02 1.97 ± 0.02 1.51 ± 0.02 1.41 ± 0.02 1.38 ± 0.02 In a further aspect, the invention relates to the a method of making a secondary electrolytic cell including the stable Co0 2 or Ni0 2 phase and the cell formed thereby. The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and with the description serve to explain the invention and its objects, advantages, and principles. BRIEF DESCRIPTION OF THE DRAWING The present invention will be described with reference to the accompanying drawing of which: FIG. 1 is a series of x-ray diffraction diagrams taken during electrochemical delithiation of LiCo0 2 to form the Co0 2 phase; FIG. 2 is a series of x-ray diffraction diagrams taken during electrochemical intercalation of lithium into the Co0 2 phase; FIG. 3 plots charge and discharge voltage versus lithium content for a cell utilizing the Co0 2 phase; FIGs. 4 and 5 plot charge and discharge voltage versus lithium content for a cell having a LiNi0 2 cathode that has been delithiated to the Ni0 2 phase according to the invention; FIG. 6 plots decomposition reaction heat versus temperature for the Co0 2 and Ni0 2 phase; FIGs. 7 and 8 are x-ray diffraction diagrams for the thermal decomposition products of the Co0 2 and Ni0 2 phases; FIG. 9 plots charge and discharge voltages versus sodium content for a cell using the Co0 2 phase of this invention intercalated with sodium ions; FIG. 10 is an x-ray diffraction diagram taken during electrochemical delithiation of LiNi0 2 to form the Ni0 2 phase; and FIG. 11 is an x-ray diffraction diagram illustrating the effect of atmospheric water on the Co0 2 phase. DESCRIPTION OF THE INVENTION One hindrance to the achievement of the Co0 2 and Ni0 2 phases of the present invention, was removed by the development of electrolytes that are stable (inert to oxidation) at the high voltages thought necessary to achieve the delithiated Co0 2 phase. These electrolytes are exemplified by those described in U.S. Patent No. 5,192,629, the disclosure of which is incorporated herein by reference. Nonetheless, it was commonly held that the Co0 2 phase was unattainable because in the complete absence of lithium ions in the Van der Waals gap between the negatively-charged Co0 2 layers, the repulsive force between the layers would be too great and a completely delithiated Co0 2 phase would never be stable. Using an electrolytic cell incorporating an LiCo0 2 cathode material described herein and a high voltage-stable electrolyte, the Co0 2 phase can be prepared by applying to the cell a charge voltage of 5.2 V, which will deintercalate substantially all the lithium from the LiCo0 2 cathode, forming the Co0 2 phase. The Co0 2 phase is metastable and decomposes above 200°C. Similarly, in an electrolytic cell using a high voltage stable electrolyte and a LiNi0 2 cathode, a substantially complete delithiation to a Ni0 2 phase can be achieved by applying a charge voltage of 5.1 V. Once obtained, the Co0 2 and Ni0 2 phases of the present invention can be reintercalated with lithium, or by other ions such as hydrogen nuclei, sodium (Example 4), potassium, or rubidium. Reintercalation of lithium or other ionic species into the Co0 2 or Ni0 2 phases can be accomplished by electrochemical insertion or by vapor phase transport at temperatures below 200°C. Vapor phase transport is described i a paper by Tarascon et al. , "Synthesis and peculiar properties of InMo 6 S x . 8 Se x , TlMo 6 S x _ β Se J . and Hg y Mo 6 S x .. 8 Se.-" , Physical Review B, Vol. 31, NO. 2, 1985, which is incorporated herein by reference in its entirety. Following reintercalation, these phases can, for example, be cycled with lithium between 3 V and 4.2 V for the Co0 2 phase and 2.8 V and 4.1 V for the Ni0 2 phase without loss of cell capacity. After formation of the Co0 2 phase, CoOOH may be formed by exposure of the phase to atmospheric water. As can be seen from FIG. 11, Co0 2 may be formed in situ in an electrochemical cell. After exposure to air for approximately 30 minutes, two phases are present. After 3 days in air CoOOH was formed, because at an open circuit voltage >4 V the following reaction occurs: 2 H 2 0 - 4 e " > 0 2 + 4 H* Co0 2 + x e ~ + x H* > H x Co0 2 The CoOOH may be used as an electronic conductor in other battery technology. This includes application in the Ni electrode or NiMeH, Ni-H or Ni-Cd batteries in which cobalt is already used. As an alternative, once formed, these phases can be used in any variety of manners. In one preferred embodiment, the cathode of a plastic solid state cell is not laminated to the underlying electrolyte/anode structure, thus allowing ease of removal of the Co0 2 or Ni0 2 phase in a plastic matrix. This plasticized phase can then easily be transported to other environments. For the reasons discussed above, if the pure Co0 2 phase is desired, handling under inert (anhydrous) conditions is preferred. In another embodiment, this plasticized phase is placed into a cell containing, for example, a sodium containing electrolyte and a compatible electrolyte and then the cobalt or nickel oxide phase is reintercalated with the sodium ions. This reintercalation may be stopped short of completion and, in that way, a second or subsequent ion may be added to the reintercalated metal oxide phase. In yet another embodiment, the nickel or cobalt oxide phase may be combined with an organic component to form, for example, either a composite polymer or an activated metal oxide carrier. The redox potential of this phase is high making it potentially useful in many areas. Anticipated applications include, for example, forming inorganic polymer structures and as a biochemical carrier. Such applications would be clearly recognizable to the skilled artisan. The following examples exemplify the practice of the present invention to the prior art. It will be appreciated by those skilled in the art that these examples are not to be construed as limiting the present invention. Example 1 A plastic electrolytic cell was constructed comprising a matrix of polyvinylidene fluoride (PVdF) and hexafluoro- propylene (HFP) , incorporating an electrolyte composition of 2 parts EC to one part DMC and 1M LiPF 6 , which was inert to oxidation at high voltages. The cathode contained LiCo0 2 as an active material and the anode contained carbon. The anode and the solid state electrolyte were laminated to one another and the cathode was placed thereover. This cell was charged to 5.2 V, at which point the LiCo0 2 was fully delithiate to form the Co0 2 phase. The existence of this phase is confirmed by the x-ray data depicted in FIG. 1. FIG. 1 depicts the diffraction pattern at the end of deintercalation of LiCo0 2 beginning at approximately the last known phase disclosed in the prior literature, i.e., monoclinic (Li 015 CoO 2 ) and proceeding to complete delithiation at a voltage of 5.2V. The x-ray diffraction patterns were obtained in-situ through the use of an X-ray diffraction apparatus that allows the use of high voltages without corrosion of the beryllium window. The final x-ray diffraction pattern obtained at 5.2 V is the hexagonal structure associated with the Co0 2 phase. Moreover, once obtained, the Co0 2 phase reconverted to the LiCo0 2 phase during discharge of the cell as shown by the series of x-ray diffraction patterns in FIG. 2. Following attainment of the Co0 2 phase in the cathode and reintercalation of lithium to form the LiCo0 2 phase, this cell was cycled between 3 V and 4.2 V with little loss of charge capacity, as seen in FIG. 3. During the charge cycle of a partially delithiated cobalt oxide, reinsertion of the lithium forms a monoclinic phase; however, reinsertion of lithium into the fully delithiated cobalt oxide resulted in a hexagonal structure, which is the same as the structure of the LiCo0 2 originally incorporated into the electrolytic cell. Example 2 A plastic electrolytic cell was constructed as in Example 1, incorporating an electrolyte composition inert to oxidation at high voltages and a cathode made from LiNi0 2 . This cell was charged to 5.1 V, at which voltage substantially all of the lithium was removed from the LiNi0 2 phase to form the Ni0 2 phase. The existence of the Ni0 2 phase is confirmed by the x-ray data depicted in FIG. 10. The cell was discharged at 200 μA, whereupon 70% of the lithium intercalated back into the Ni0 2 structure, as seen in FIG. 4. Subsequent cycling this cell between 2.8 V and 4.0 V without capacity fading confirmed that the reversible charge characteristics of the Li x Ni0 2 were not destroyed by the attainment of the Ni0 2 phase. Reducing the discharge current to 150 μA resulted in intercalation of all of the lithium to form the LiNi0 2 phase. As shown in FIG. 5, subsequent cycling of this cell between 2.8 V and 4.1 V resulted in a high capacity (greater than 190 A-h/kg) with minimal polarization and slight irreversibility characteristic of LiNi0 2 . These results show that total removal of lithium from LiNi0 2 produces a structure that remains electrochemically active. Example 3 A study of the thermal stability of the Co0 2 phase and Ni0 2 phase was undertaken. Plastic electrodes of LiCo0 2 and LiNi0 2 brought to the Co0 2 phase and the Ni0 2 phase in the manners described in Examples 1 and 2, respectively, were dissolved separately in a dilute acetone solvent at room temperature. The plastic portions of the electrodes dissolved in the solvent, and the insoluble metal oxides settled to the bottom of the vessels. The metal oxides were separated from the solution and analyzed using differential scanning calorimetry (DSC) ramped to 300°C at 10°C/min. As seen in FIG. 6, a relatively strong exothermic reaction occurred at 200°C for both the Co0 2 and Ni0 2 phases. Analysis of the samples by x-ray diffraction after DSC revealed that both phases reduced with attendant oxygen loss according to the reaction M0 2 --> MO + 1/2 0 2 . The x-ray diffraction patterns depicted in FIGs. 7 and 8 confirm that the samples transformed into the mixed rocksalt structures of CoO and NiO, which are known to be electrochemically inactive to lithium intercalation. Example 4 A cell was constructed as in Example 1. The Co0 2 phase was formed by delithiating the plastic cell at 5.2 V for 15 hours. After the Co0 2 phase was formed, the plasticized Co0 2 was removed from the electrolyte/anode structure and then incorporated into a similarly constructed cell contained sodium. The new cell was constructed using the plastic Co0 2 cathode, an NaC10 4 electrolyte and a sodium metal anode. Sodium was introduced into the Co0 2 phase by discharging the cell at 2.2 V to insert the sodium. The cell was then cycled between 2.2 V and 4.1 V, as shown in FIG. 9.

Claims: What is claimed is 1. A method of preparing a stable metal dioxide phase c h a r a c t e r i z e d i n t h a t said method comprises: a) preparing an electrolytic cell having an anode, an electrolyte inert to oxidation, and a cathode comprising a metal oxide selected from the group consisting of a lithium cobalt oxide intercalation complex and a lithium nickel oxide intercalation complex having the formula Li x NiOj wherein x is 0.8 to 1.0; and b) applying to said cell a voltage sufficiently high to deintercalate substantially all lithium from said metal oxide. 2. A method according to claim 1 wherein said voltage is in excess of about 5.0 V. 3. A method according to claim 2 wherein said electrolyte comprises a 0.5M to 2M solution of LiPF 6 , or LiPF 6 with up to about an equal amount of LiBF 4 added, in a mixture of dimethyl- carbonate (DMC) and ethylene carbonate (EC) within the weight percent ratio range from about 95 DMC:5 EC to 20 DMC:80 EC. 4. A method according to claim 1 which further comprises intercalating said stable metal dioxide phase with an element selected from the group consisting of lithium, sodium, potassium, rubidium, and hydrogen. 5. A stable metal dioxide phase prepared according to the method of claim 1 c h a r a c t e r i z e d i n t h a t the metal is selected from the group consisting of cobalt and nickel. 6. A stable cobalt dioxide phase according to claim 5 having the X-ray diffraction pattern: d(A) 4.30 ± 0.02 2.44 ± 0.02 2.12 + 0.02 1.61 ± 0.02 1.41 ± 0.02 1.34 ± 0.02 1.17 ± 0.02 7. A stable nickel dioxide phase according to claim 5 having the X-ray diffraction pattern: d( ) 4.47 ± 0.02 2.40 ± 0.02 2.29 + 0.02 1.97 + 0.02 1.51 ± 0.02 1.41 ± 0.02 1.38 + 0.02 8. A secondary electrolytic cell including an anode, an electrolyte, and a cathode c h a r a c t e r i z e d i n t h a t said cathode comprises a stable metal dioxide phase of claim 5 9. A secondary electrolytic cell according to claim 8 c h a r a c t e r i z e d i n t h a t said cathode further comprises an element selected from the group consisting of lithium, sodium, potassium, rubidium, or hydrogen intercalated into said stable metal dioxide phase.

Inventors: AMATUCCI GLENN G, TARASCON JEAN-MARIE, AMATUCCI, GLENN, G., TARASCON, JEAN-MARIE
Applicants: BELL COMMUNICATIONS RES, BELL COMMUNICATIONS RESEARCH, INC.
Application year: 1996
Main classification: H01M6
IPC codes: C01G51, C01G53, H01M4, H01M10