US20100035152A1 - Electrochemical cell including functionally graded and architectured components and methods - Google Patents
Electrochemical cell including functionally graded and architectured components and methods Download PDFInfo
- Publication number
- US20100035152A1 US20100035152A1 US12/535,632 US53563209A US2010035152A1 US 20100035152 A1 US20100035152 A1 US 20100035152A1 US 53563209 A US53563209 A US 53563209A US 2010035152 A1 US2010035152 A1 US 2010035152A1
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- Prior art keywords
- anode
- cathode
- electrochemical cell
- electrolyte
- nanocomposite
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- the present invention relates generally to electrochemical cells. More particularly, the present invention provides methods and devices having a functionally graded and an architectured component for electrode(s). Merely by way of example, the invention can be applied to a variety of applications including automotive, telecommunication, general energy storage, portable electronics, power tools, power supplies, among others.
- electrochemical cells are used to store energy for a variety of applications. These applications include portable electronics such as cell phones, personal digital assistants, music players, video cameras, and the like. Applications also include power tools, power supplies for military use (e.g., communications, lighting, imaging and the like), power supplies for aerospace applications (e.g., power for satellites), and power supplies for vehicle applications (e.g., hybrid electric vehicles, plug-in hybrid electric vehicles, and fully electric vehicles), and others.
- military use e.g., communications, lighting, imaging and the like
- aerospace applications e.g., power for satellites
- vehicle applications e.g., hybrid electric vehicles, plug-in hybrid electric vehicles, and fully electric vehicles
- Li 2 MnO 3 -stabilized LiMO 2 (M ⁇ Mn, Ni, Co) Electrodes for Lithium-Ion Batteries, Journal of Material Chemistry 17 , 3112 - 3125 , 2007 ”.
- This type of cells typically has non-aqueous electrolyte sandwiched between a cathode layer and an anode layer of similar geometry.
- the cathode is often, LiCoO 2 , LiMn 2 O 4
- the electrolyte is often lithium-phosphorous-oxynitride (LIPON) and anode is lithium foil.
- Thin-film Li-ion cells have been demonstrated to have energy densities of 1,000 Wh/Kg and power densities of 10,000 W/Kg with potentially unlimited number of discharge-charge cycles.
- a central challenge to create cost-effectively microarchitectured and functionally graded electrodes, cells or batteries is precisely tuning material properties for the specific role of that material needed.
- In order to achieve precise material properties spanning through an electrochemical cell manufacturing has to be inside a controlled environment.
- Traditional thin-film electrochemical cells have been manufactured inside the clean room for aerospace and implantable batteries. However, such a process is too costly and can not be used for mass production of high-tech electrochemical cells.
- the present invention provides methods and devices having a functionally graded and an architectured component for electrode(s).
- the invention can be applied to a variety of applications including automotive, telecommunication, general energy storage, portable electronics, power tools, power supplies, among others.
- Embodiments of the present invention comprise a microarchitectured thin-film electrochemical cell with continuously deposited layers that have varying at least one of (or more) intensive properties as a function of at least one of (or more) the extensive properties, and related methods to manufactured such type of electrochemical cell.
- the intensive properties are, but are not limited to, density, composition, concentration, thermal/electronic/ionic conductivities, thermal/ionic diffusivities, maximum strain, ultimate strength, moduli, ductility, and plasticity, combinations, and the like.
- the extensive properties are, but are not limited to, volume, area, and thickness, combinations, and the like.
- the invention has been provided with use of lithium based cells, but it would be recognized that other materials such as zinc, silver, copper and nickel could be designed in the same or similar fashion.
- Deposition of layers and formation of microarchitecture of layers are accomplished by one of several processes, used separately or in conjunction with one another.
- Continuous manufacturing of electrodes and batteries is accomplished via a variety of techniques.
- the manufacturing processes of the present invention is finished inside the deposition chamber, which is equipped with sufficient materials to create complete batteries, via deposition of anode, cathode, electrolyte, separator and current collector layers.
- the term “continuous process” shall mean a substantially free from any breaks or each of the processes is within a predetermined environment, e.g., vacuum. Batteries constructed using this approach have at least one anode, one cathode, an electrolyte, and may have a separator, depending upon the electrochemistry used. Of course, there can be other variations, modifications, and alternatives.
- one or more material comprises a microarchitectured morphology having at least one mechanism to mitigate intercalation and thermal expansion stresses, strengthen the electrode material.
- one or more material comprises a functionally graded structure having one or more intensive properties varying as function of one or more extensive properties of the material.
- Intensive characteristics include but are not limited to density, composition, concentration, thermal/electronic/ionic conductivities, thermal/ionic diffusivities, maximum strain, ultimate strength, moduli, ductility, and plasticity.
- Extensive characteristics include but are not limited to volume, area, and thickness.
- an anode material having a composition containing at least one element from Groups IA, IVA, VIA, and IIB;
- a cathode material is provided that having a composition containing at least one element from Groups IA, VIII, IVA, VIA, IB, IVB and VIIB;
- microarchitecture is created using one or more of the following techniques.
- the anode current collector material is formed on a microarchitectured substrate by using physical vapor deposition techniques, or is a stand-alone microarchitectured film without needing a substrate.
- the cathode current collector material is formed on a microarchitectured substrate by using physical vapor deposition techniques, or it is a stand-alone microarchitectured film without requiring a substrate.
- the microarchitectured electrochemical cell comprises anode, electrolyte and cathode deposited sequentially or in reverse order by physical vapor deposition techniques.
- the term “microarchitectured” shall be interpreted by ordinary meaning and the description herein should not be limiting.
- the term microarchitectured shall include feature sizes ranging from about 100 nanometers to about 100 micrometers and less than 500 micrometers, but can be others.
- a method comprises of manipulating the configuration of the electrode to create breadloafing.
- the anode connected with the anode current collector and a second side is interlocked with the electrolyte.
- the electrolyte of present invention wherein a first side is interlocked with the anode layer and a second side is interlocked with the cathode layer.
- the cathode of claim 1 wherein a first side is interlocked with the electrolyte and a second side is connected with the cathode current collector.
- methods comprise of manipulating the materials to form nanocomposite electrode.
- a nanocomposite material is formed by depositing two or more layers of same material with different crystal structures.
- a nanocomposite material is formed by depositing two or more layers of the same material with different crystal structures, and using masks on alternate layers to create patterns.
- a nanocomposite material is formed by depositing two or more layers of different materials.
- a nanocomposite material is formed by depositing two or more layers of different materials, and using masks on alternate layers to create patterns.
- a nanocomposite material is formed by depositing two or more materials at the same time to create one or more nanodisperse phases within the main matrix grains of active material. In another embodiment, a nanocomposite material is formed by depositing two or more materials at the same time to create dispersion of secondary phases around the grain boundaries of the matrix of active material. In yet another embodiment, a nanocomposite material is formed by depositing two or more materials at the same time to create a dispersion of secondary phases both inside and around the grains of the matrix of active material. In another embodiment, a nanocomposite material is formed by depositing two or more materials at the same time to induce phase separation. As used herein, the term nanocomposite shall include feature sizes ranging from about 50 ⁇ about 500 nanometers and less, but can be other sizes according to ordinary meaning.
- methods comprise of fabricating the functionally graded, microarchitectured solid electrodes using a plurality of techniques containing at least one from the group of evaporation, physical vapor deposition (PVD), chemical vapor deposition, sputtering, radio frequency magnetron sputtering, microwave plasma enhanced chemical vapor deposition (MPECVD), pulsed laser deposition (PLD), laser ablation, spray deposition, spray pyrolysis, spray coating or plasma spraying, and fabricating functionally graded, microarchitectured nonaqueous electrolyte using a plurality of techniques containing at least one from the group of physical vapor deposition, laser deposition, centrifuge, spinning, microwave, thermal control, spray, and chemical vapor deposition.
- methods comprise of masking, and deposition to define a precise morphology of active region for neutralizing internal stresses, stopping crack growth, maximizing material strength, and stabilizing active material structure in anode, electrolyte, cathode and current collectors.
- morphology of periodic, irregular but not arbitrary electrode is identified by using one of the optimization techniques, but not limited to, surrogate-base analysis, genetic algorithm, adaptive topology optimization, design of experiments, ANOVA/MANOVA, basin based analysis, solid isotropic microstructure with intermediate mass penalization (SIMP), power penalized stiffness model, topology optimization of continuum structure, normal boundary intersection (NBI) optimization method, multivariable optimization method, or multidisciplinary design optimization.
- optimization techniques but not limited to, surrogate-base analysis, genetic algorithm, adaptive topology optimization, design of experiments, ANOVA/MANOVA, basin based analysis, solid isotropic microstructure with intermediate mass penalization (SIMP), power penalized stiffness model, topology optimization of continuum structure, normal boundary intersection (NBI) optimization method, multivariable optimization method, or multidisciplinary design optimization.
- microarchitectured electrodes are characterized by periodic pattern by using a patterning technique selected from a group including but not limited to: periodically varying magnetic field, electric field, temperature gradient, and optical beam intensity, periodically seeding the current collector or substrate with precursor, periodically modifying the current collector or substrate using drilling, masking, molding, indentation, nanoimprint, abrasive, laser ablation, radiation and neutron scattering.
- a patterning technique selected from a group including but not limited to: periodically varying magnetic field, electric field, temperature gradient, and optical beam intensity, periodically seeding the current collector or substrate with precursor, periodically modifying the current collector or substrate using drilling, masking, molding, indentation, nanoimprint, abrasive, laser ablation, radiation and neutron scattering.
- the various cell elements can be formed using one or more techniques. These techniques include evaporation, physical vapor deposition (PVD), chemical vapor deposition, low pressure chemical vapor deposition (LPCVD), atomic layer deposition (ALD), direct laser writing (DLW), sputtering, radio frequency magnetron sputtering, microwave plasma enhanced chemical vapor deposition (MPECVD), pulsed laser deposition (PLD), nanoimprint, ion implantation, laser ablation, spray deposition, spray pyrolysis, spray coating or plasma spraying.
- PVD physical vapor deposition
- LPCVD low pressure chemical vapor deposition
- ALD atomic layer deposition
- DLW direct laser writing
- MPECVD microwave plasma enhanced chemical vapor deposition
- PLD pulsed laser deposition
- the present invention provides a micro-architectured electrochemical cell and/or battery device.
- the cell and/or battery device includes an anode and a cathode arranged anti-symmetrically with the anode.
- the device has a predetermined distance between the cathode and the anode.
- An electrical insulation is provided to separate the anode from the cathode.
- the electrical insulation is characterized by a graded material property that changes within a portion of the predetermined distance or one or more layers of insulating material to separate the anode from the cathode.
- the device has a nanocomposite anode material characterizing the anode.
- the nanocomposite anode material has one or more first intensive characteristics that is a function of one or more second extensive characteristics.
- a nanocomposite cathode material characterizes the cathode.
- the nanocomposite cathode material has one or more first intensive characteristics that is a function of one or more second extensive characteristics.
- an electrolyte material is provided between the anode and the cathode.
- the device has a cathode current collector in communication with the cathode and an anode current collector in communication with the anode.
- the present invention provides an electrochemical cell.
- the cell has an anode member having one or more first spatial features and formed substantially from a first nanocomposite material, which has an average feature size ranging from about 50 ⁇ to about 500 nanometers.
- the first nanocomposite material has a first resistivity value of greater than 8 micro-ohms centimeters, but can be others.
- the cell has a cathode member having one or more second spatial features. The cathode member is operably coupled the anode member and is formed substantially from a second nanocomposite material, which has an average feature size ranging from about 50 ⁇ to about 500 nanometers.
- the second nanocomposite has a second resistivity value of greater than 14.3 ohms centimeters, but can be others.
- the device has a predetermined gap between the anode and the cathode. In a specific embodiment, the predetermined gap is greater than 500 nanometers.
- the device also has an electrolyte provided between the anode and the cathode and a separator provided between the anode and the cathode.
- the device has a first current collector coupled to the anode via at least a first contact and a second current collector coupled to the cathode via at least a second contact.
- the present invention provides a method for fabricating an electrochemical cell.
- the method includes providing a substrate member having a predetermined spatial pattern, e.g., patterned, periodic.
- the method includes depositing a first thickness of material using one or more species overlying the predetermined spatial pattern in a conformal manner.
- the first thickness of material is characterized as a nanocomposite structure having an average feature size of about 500 nanometers and less.
- the method includes adjusting one or more parameters related to the deposition during a time period associated with the deposition of the first thickness of material from a first spatial region of the first thickness of material to a second spatial region of the first thickness of material to form a first electrode element having a graded feature of one or more characteristics from the first spatial region to the second spatial region.
- the method forms an electrolyte overlying the first electrode element and forms a second electrode element overlying the electrolyte.
- the present invention provides a method for fabricating an electrode for an electrochemical cell.
- the method includes providing a substrate member comprising a current collector.
- the method includes depositing a thickness of material using one or more species overlying a surface region of the substrate member.
- the thickness of material is characterized as a nanocomposite material.
- the method includes adjusting one or more parameters during a time period associated with the depositing of the thickness of material from a first spatial region of the thickness of material to a second spatial region of the thickness of material.
- the method also includes causing formation of an electrode element having a graded feature of one or more characteristics from the first spatial region to the second spatial region.
- the present invention provides a method for fabricating a periodic geometric feature for an electrochemical cell.
- the method includes masking and exposing a region of substrate for an electrode member or current collector by periodically varying one or more parameters selected from at least a magnetic field, an electric field, a temperature gradient, and an optical beam intensity to seed the exposed region of the substrate with one or more precursors.
- the method also includes periodically modifying one or more spatial regions of the exposed region of the substrate using at least one or more processes selected from drilling, masking, molding, indentation, nanoimprint, abrasive, laser ablation, radiation and neutron scattering.
- processes selected from drilling, masking, molding, indentation, nanoimprint, abrasive, laser ablation, radiation and neutron scattering.
- the benefits of the invention include the ability it confers in rational design and combination of multiple materials to produce electrochemical cells, in novel arrangements. These in, turn, confer superior properties to designed cells, and elimination of costly-trial and error in construction of prototype cells. Depending upon the embodiment, one or more of these benefits can be achieved.
- FIG. 1 Periodic, irregular but not arbitrary electrode according to an embodiment of the present invention.
- FIGS. 2 (A)-(B) are simplified cross-sectional views showing fabrication of a functionally graded electrode according to an embodiment of the present invention.
- FIGS. 3 (A)-(C) are simplified cross-sectional views showing fabrication of an electrode exhibiting a sinusoidal microarchitecture according to an embodiment of the present invention.
- FIGS. 4 (A)-(D) are simplified cross-sectional views showing fabrication of an electrode exhibiting a nanocomposite material for electrode according to an alternative embodiment of the present invention.
- FIG. 5(A) illustrates a cathode with thin-film design according to an alternative embodiment of the present invention
- FIG. 5(B) illustrates a cathode with column design according to an alternative embodiment of the present invention
- FIG. 5(C) illustrates a cathode with sinusoidal design according to an alternative embodiment of the present invention
- FIG. 5(D) illustrates contours of von-Mises stress on column design electrode.
- the present invention provides a method and system for manufacture of three-dimensional elements for three-dimensional interdigitated electrochemical cells.
- the invention has been provided with use of lithium based cells, but it would be recognized that other materials such as zinc, silver, copper and nickel could be designed in the same fashion.
- batteries can be used for a variety of applications such as portable electronics (cell phones, personal digital assistants, music players, video cameras, and the like), power tools, power supplies for military use (communications, lighting, imaging and the like), power supplies for aerospace applications (power for satellites), and power supplies for vehicle applications (hybrid electric vehicles, plug-in hybrid electric vehicles, and fully electric vehicles).
- the present invention provides a structure that is irregular in shape, but has a periodic spatial feature.
- the irregularity is not arbitrary in shape or size.
- the irregularity has a predetermined spatial feature.
- the structure has a first periodic spatial feature domain and a second periodic spatial feature domain.
- each of the domains include common features, which may include a pyramidal shape, trapezoidal shape, dome shape, or any other shapes, including combinations, and the like.
- a device of electrochemical cells comprises of functionally graded and periodically spatial feature electrodes that would benefit its usage to extend lifetime and efficiency by mitigating the stress due to the ionic intercalation, alleviating thermal stress due to the electrochemical reaction, stabilizing the host material lattice structure during the charge-discharge process, and increasing the kinetic properties of the host material.
- the electrode described herein is referring to anode and cathode of a single electrochemical cell. The anode and cathode referring herein are based on the electric current direction and the mode.
- the anode is the negative terminal in a discharge electrochemical cell (or also known as galvanic cell), but it would the positive terminal in a recharging electrochemical cell (or also known as electrolytic cell).
- the cathode is vice versa.
- the functionally graded electrodes described herein are characterized by the variation in composition and structure gradually over spatially volume of single electrode or whole electrochemical cells.
- the periodically spatial feature of electrodes or electrochemical cells of the device described herein is employed to strengthen material performance locally to facilitate the ionic diffusion, electronic conduction, and mitigating stress inside the electrodes.
- the host active material is the material within an electrode responsible for the electronic energy exchange with counter electrode during the electrochemical reaction.
- the function described herein includes, but not limited to, mitigating intercalation stress due to the host material lattice increment, alleviating thermal stress due to the energy exchange within the whole device, and increasing the kinetic properties of the electrode in specific region, etc.
- utilizing Li 2 MnO 3 will stabilize LiMO 2 lattice structure, where M include Mn, Ni and Co, during the charge-discharge process in a Li ion battery as described in U.S. Pat. No. 6,680,143 B2.
- the function of stabilizing lattice structure of the host active material is the only one.
- a method is provided that periodically spatial feature of the electrode is identified as shown in FIG. 1 .
- the diagram includes a first period and a second period according to a specific embodiment.
- each of the periods includes various shapes, e.g., pyramid, trapezoid, dome.
- the spatial feature of the electrode has impacts on the cell performance, such as mitigating stresses due to Li+ intercalation and temperature increment, etc.
- the preferred spatial feature will be identified by utilizing any optimization techniques.
- the optimization method comprises one technique from, but not limited to, the group of surrogate-base analysis, genetic algorithm, adaptive topology optimization, design of experiments, ANOVA/MANOVA, basin based analysis, solid isotropic microstructure with intermediate mass penalization (SIMP), power penalized stiffness model, topology optimization of continuum structure, normal boundary intersection (NBI) optimization method, multivariable optimization method, or multidisciplinary design optimization.
- a preferred embodiment of the present invention would be having a sinusoidal electrode profile, wherein the amplitude and frequency of the sinusoid will be determined by the optimization techniques listed above to have robust performance, long lifetime, and high safety.
- a preferred embodiment of the present invention would be having a sinusoidal electrode profile, wherein the amplitude and frequency of the sinusoid will be determined by the optimization techniques listed above to have robust performance, long lifetime, and high safety.
- the atmosphere associated with the electrode material deposition may be changed.
- the suitable atmosphere comprises a oxygen atmosphere to create metal oxide materials.
- the atmosphere may be a nitrogen atmosphere to create electrolyte layers or nitride materials.
- the temperature associated to the electrode materials formation may be varied, continuously or step-wise to achieve particular materials microstructures.
- an annealing step up to 800° C. may be introduced to induce re-crystallization of amorphous metal oxides material layers.
- ambient temperature may be maintained constant by cooling the substrate and removing heat at a constant rate.
- architectured components of the battery having geometric features ranging from 100 nanometers to 100 micrometers or below 500 micrometers, may be fabricated using any suitable technique from the following list, individually or in combination with each other: evaporation, physical vapor deposition (PVD), chemical vapor deposition, low pressure chemical vapor deposition (LPCVD), atomic layer deposition (ALD), direct laser writing (DLW), sputtering, radio frequency magnetron sputtering, microwave plasma enhanced chemical vapor deposition (MPECVD), pulsed laser deposition (PLD), nanoimprint, ion implantation, laser ablation, spray deposition, spray pyrolysis, spray coating or plasma spraying.
- PVD physical vapor deposition
- LPCVD low pressure chemical vapor deposition
- ALD atomic layer deposition
- DLW direct laser writing
- MPECVD microwave plasma enhanced chemical vapor deposition
- PLD pulsed laser deposition
- nanoimprint ion implantation, laser ablation, spray deposition, spray pyro
- each member includes, but not limited to, a substrate material comprising of copper (Cu), aluminum (Al), stainless steel, or other suitable conductive alloy in the form of a thin foil and bearing, an anode material comprising lithium metal (Li), lithium titanium oxide (Li 4 Ti 5 O 12 ), graphite (C), or meso-carbon structures such as microbeads or other microstructures; an electrolyte material overlying the first electrode material and comprising lithium phosphorus oxynitride (LIPON), lithium salts such as LiClO 4 /LiPF 6 mixed with poly-ethylene oxide (PEO), poly-vinylidene fluoride (PVDF), or combination of PEO and PVDF; and a cathode material overlying the electrolyte material and comprising layered metal oxide materials such as LiCoO 2 , spinel materials such as LiMn 2 O 4 , olivine materials such as LiFePO 4 , Li(Ni 1/3 Mn
- Example 1A functionally graded electrode and its manufacturing technique
- a functionally graded graphite anode is created by focusing a laser beam through polymer electrolyte layer by layer gradually from current collector to some desired distance toward the surface of the polymer electrolyte with decreasing the frequency of turning on-and-off the laser beam as the focus point of the laser beam is gradually moved away from the current collector.
- the electrode 1 comprises of polymer electrolyte (LiPF 6 plus polyethyleneoxide, PEO) 2 coated on top of copper current collector 3 as detailed described in FIG. 2A . Because of the high-energy of the Nd:YAG laser beam 4 , the polymer in polymer electrolyte, where the laser beam is aimed, will be graphitized as 9 in FIG. 2B .
- a microarchitectured LiMn 2 O 4 cathode having a periodic but non-arbitrary geometry is made using a silicon (Si) substrate 11 as a template.
- a Nd:YAG laser 13 is used to machine the substrate and remove material 14 , creating a set of channels and ridges that follows a predetermined geometry obtained using a Computer Aided Design (CAD) software as 12 .
- CAD Computer Aided Design
- the design is reflecting minimization of intercalation stresses in the LiMn 2 O 4 material according to computer simulations.
- PVD physical vapor deposition
- a first titanium (Ti) 18 attachment layer having a thickness of 50 ⁇ or less
- a second aluminum (Al) layer 19 having a thickness of 500 nanometers or higher, to serve as cathode current collector.
- the active material (LiMn 2 O 4 ) 20 is formed following the same geometry imprinted by the substrate.
- the thickness of the active material is 1-10 ⁇ m.
- a LiMn 2 O 4 partially stabilized cathode is fabricated by depositing conformal material layers using physical vapor deposition (PVD).
- PVD physical vapor deposition
- a first layer of LiMn 2 O 4 , 23 is deposited having a thickness of 100-500 nanometers.
- a mask, 26 having geometric features of 100 nanometers or higher, is applied onto it and a layer of Li 2 MnO 3 , 29 , is deposited.
- the mask is removed and another layer of LiMn 2 O 4 , 34 , having a thickness of 100-500 nanometers, is deposited to embed the Li 2 MnO 3 features previously created.
- sputtering of Li 2 MnO 3 can be employed to create irregular second phase regions on the first layer followed by a layer of LiMn 2 O 4 , having a thickness of 100-500 nanometers deposited to embed the second phases.
- a third option is to create a uniform layer of Li 2 MnO 3 onto the first layer of LiMn 2 O 4 having a thickness of 50-100 nanometers and then a new layer of LiMn 2 O 4 , having a thickness of 100-500 nanometers to sandwich the Li 2 MnO 3 layer.
- the function of the Li 2 MnO 3 regions is to stabilize the spinel crystal structure of LiMn 2 O 4 when, during discharge the number of Li+ ions is depleted and the structure becomes metastable.
- the cathode material would transform to a more stable spinel-type configuration degrading the high potential and limiting capacity and rechargeability of the electrode, however the second phase prevents this from happening.
- This example demonstrates the process of identifying a new electrochemical cell with the optimal morphological shape of the electrode.
- three different morphological designs of three-dimensional electrodes are provided: thin-film in FIG. 5A , columnar shape in FIG. 5B , and a sinusoidal shape in FIG. 5C .
- the materials for the three-dimensional electrochemical cells are copper as anode current collector ( 101 in FIG. 5A , 108 in FIG. 5B , 113 in FIG. 5C ), lithium metal as anode ( 102 in FIG. 5A , 109 in FIG. 5B , 114 in FIG. 5C ), lithium manganese oxide as cathode ( 103 in FIG. 5A , 110 in FIG.
Abstract
Electrochemical cells or batteries featuring functional gradations, and having desirable, periodic configurations, and methods for making the same. One or more methods, in alone or in combination, are utilized to fabricate components of such electrochemical cells or batteries, which are designed to achieve certain thermal, mechanical, kinetic and spatial characteristics, and their effects, singly and in all possible combinations, on battery performance. The thermal characteristics relate to temperature distribution during charge and discharge processes. The kinetic characteristics relate to rate performance of the cells or batteries such as the ionic diffusion process and electron conduction. The mechanical characteristics relate to lifetime and efficiency of the cells or batteries such as the strength and moduli of the component materials. Finally, the spatial characteristics relate to the energy and power densities, stress and temperature mitigation mechanisms, and diffusion and conduction enhancements. The electrochemical cells or batteries constructed according to the methods presented in this invention are useful for all applications that require high rate performance, high energy/power density, good durability, high safety and long lifetime.
Description
- This application claims priority to U.S. Provisional Patent Application No. 61/086,161, filed Aug. 5, 2008, the disclosure of which is hereby incorporated by reference for all purposes.
- The present invention relates generally to electrochemical cells. More particularly, the present invention provides methods and devices having a functionally graded and an architectured component for electrode(s). Merely by way of example, the invention can be applied to a variety of applications including automotive, telecommunication, general energy storage, portable electronics, power tools, power supplies, among others.
- As noted, electrochemical cells are used to store energy for a variety of applications. These applications include portable electronics such as cell phones, personal digital assistants, music players, video cameras, and the like. Applications also include power tools, power supplies for military use (e.g., communications, lighting, imaging and the like), power supplies for aerospace applications (e.g., power for satellites), and power supplies for vehicle applications (e.g., hybrid electric vehicles, plug-in hybrid electric vehicles, and fully electric vehicles), and others.
- Conventional electrochemical cells are manufactured using paper-making techniques. The conventional electrochemical cells have been fabricated without accounting for internal mechanical stresses, intercalation and thermal induced stresses. Thus, drawbacks exist with these conventional cells. The drawbacks include limited lifetime, premature failure, limited storage capability, and other imperfections. To increase the electrochemical cell energy and power density, without compromising lifetime, other manufacturing approaches have been proposed. Concurrently, electrode architectures have been developed that use thin-film, microarchitectured, functionally graded materials such as Li2MnO3-stabilized LiMO2 (M═Mn, Ni, Co) described in “M. M. Thackeray, S.-H. Kang, C. S. Johnson, Li2MnO3-stabilized LiMO2 (M═Mn, Ni, Co) Electrodes for Lithium-Ion Batteries, Journal of Material Chemistry 17, 3112-3125, 2007”. This type of cells typically has non-aqueous electrolyte sandwiched between a cathode layer and an anode layer of similar geometry. For example, in a typical thin-film lithium ion cell, the cathode is often, LiCoO2, LiMn2O4, while the electrolyte is often lithium-phosphorous-oxynitride (LIPON) and anode is lithium foil. Thin-film Li-ion cells have been demonstrated to have energy densities of 1,000 Wh/Kg and power densities of 10,000 W/Kg with potentially unlimited number of discharge-charge cycles.
- A central challenge to create cost-effectively microarchitectured and functionally graded electrodes, cells or batteries is precisely tuning material properties for the specific role of that material needed. In order to achieve precise material properties spanning through an electrochemical cell manufacturing has to be inside a controlled environment. Traditional thin-film electrochemical cells have been manufactured inside the clean room for aerospace and implantable batteries. However, such a process is too costly and can not be used for mass production of high-tech electrochemical cells.
- As a consequence, cost-effective high throughput manufacturing techniques and microarchitectured and functionally graded electrodes are desirable.
- According to the present invention, techniques for electrochemical cells are provided. More particularly, the present invention provides methods and devices having a functionally graded and an architectured component for electrode(s). Merely by way of example, the invention can be applied to a variety of applications including automotive, telecommunication, general energy storage, portable electronics, power tools, power supplies, among others.
- Embodiments of the present invention comprise a microarchitectured thin-film electrochemical cell with continuously deposited layers that have varying at least one of (or more) intensive properties as a function of at least one of (or more) the extensive properties, and related methods to manufactured such type of electrochemical cell. The intensive properties are, but are not limited to, density, composition, concentration, thermal/electronic/ionic conductivities, thermal/ionic diffusivities, maximum strain, ultimate strength, moduli, ductility, and plasticity, combinations, and the like. Also, the extensive properties are, but are not limited to, volume, area, and thickness, combinations, and the like.
- Merely by way of example, the invention has been provided with use of lithium based cells, but it would be recognized that other materials such as zinc, silver, copper and nickel could be designed in the same or similar fashion. Deposition of layers and formation of microarchitecture of layers are accomplished by one of several processes, used separately or in conjunction with one another. Continuous manufacturing of electrodes and batteries is accomplished via a variety of techniques. The manufacturing processes of the present invention is finished inside the deposition chamber, which is equipped with sufficient materials to create complete batteries, via deposition of anode, cathode, electrolyte, separator and current collector layers. As used herein, the term “continuous process” shall mean a substantially free from any breaks or each of the processes is within a predetermined environment, e.g., vacuum. Batteries constructed using this approach have at least one anode, one cathode, an electrolyte, and may have a separator, depending upon the electrochemistry used. Of course, there can be other variations, modifications, and alternatives.
- An embodiment of the present invention, one or more material is provided that comprises a microarchitectured morphology having at least one mechanism to mitigate intercalation and thermal expansion stresses, strengthen the electrode material.
- In another embodiment of the present invention, one or more material is provided that comprises a functionally graded structure having one or more intensive properties varying as function of one or more extensive properties of the material. Intensive characteristics include but are not limited to density, composition, concentration, thermal/electronic/ionic conductivities, thermal/ionic diffusivities, maximum strain, ultimate strength, moduli, ductility, and plasticity. Extensive characteristics include but are not limited to volume, area, and thickness.
- In yet another embodiment of the present invention, an anode material is provided that having a composition containing at least one element from Groups IA, IVA, VIA, and IIB; a cathode material is provided that having a composition containing at least one element from Groups IA, VIII, IVA, VIA, IB, IVB and VIIB;
- In a still another embodiment of the present invention, microarchitecture is created using one or more of the following techniques. The anode current collector material is formed on a microarchitectured substrate by using physical vapor deposition techniques, or is a stand-alone microarchitectured film without needing a substrate. The cathode current collector material is formed on a microarchitectured substrate by using physical vapor deposition techniques, or it is a stand-alone microarchitectured film without requiring a substrate. The microarchitectured electrochemical cell comprises anode, electrolyte and cathode deposited sequentially or in reverse order by physical vapor deposition techniques. As used herein, the term “microarchitectured” shall be interpreted by ordinary meaning and the description herein should not be limiting. As an example, the term microarchitectured shall include feature sizes ranging from about 100 nanometers to about 100 micrometers and less than 500 micrometers, but can be others.
- In another embodiment of the present invention, a method is provided that comprises of manipulating the configuration of the electrode to create breadloafing. The anode connected with the anode current collector and a second side is interlocked with the electrolyte. The electrolyte of present invention, wherein a first side is interlocked with the anode layer and a second side is interlocked with the cathode layer. The cathode of claim 1, wherein a first side is interlocked with the electrolyte and a second side is connected with the cathode current collector.
- In another embodiment of the present invention, methods are provided that comprise of manipulating the materials to form nanocomposite electrode. A nanocomposite architecture of the cathode material to neutralize internal stresses, stop crack growth, maximize material strength, and stabilize active material structure. A nanocomposite material is formed by depositing two or more layers of same material with different crystal structures. In one embodiment, a nanocomposite material is formed by depositing two or more layers of the same material with different crystal structures, and using masks on alternate layers to create patterns. In another embodiment, a nanocomposite material is formed by depositing two or more layers of different materials. In yet another embodiment, a nanocomposite material is formed by depositing two or more layers of different materials, and using masks on alternate layers to create patterns. In yet another embodiment, a nanocomposite material is formed by depositing two or more materials at the same time to create one or more nanodisperse phases within the main matrix grains of active material. In another embodiment, a nanocomposite material is formed by depositing two or more materials at the same time to create dispersion of secondary phases around the grain boundaries of the matrix of active material. In yet another embodiment, a nanocomposite material is formed by depositing two or more materials at the same time to create a dispersion of secondary phases both inside and around the grains of the matrix of active material. In another embodiment, a nanocomposite material is formed by depositing two or more materials at the same time to induce phase separation. As used herein, the term nanocomposite shall include feature sizes ranging from about 50 Å about 500 nanometers and less, but can be other sizes according to ordinary meaning.
- In another embodiment of the present invention, methods are provided that comprise of fabricating the functionally graded, microarchitectured solid electrodes using a plurality of techniques containing at least one from the group of evaporation, physical vapor deposition (PVD), chemical vapor deposition, sputtering, radio frequency magnetron sputtering, microwave plasma enhanced chemical vapor deposition (MPECVD), pulsed laser deposition (PLD), laser ablation, spray deposition, spray pyrolysis, spray coating or plasma spraying, and fabricating functionally graded, microarchitectured nonaqueous electrolyte using a plurality of techniques containing at least one from the group of physical vapor deposition, laser deposition, centrifuge, spinning, microwave, thermal control, spray, and chemical vapor deposition.
- In another embodiment of the present invention, methods are provided that comprise of masking, and deposition to define a precise morphology of active region for neutralizing internal stresses, stopping crack growth, maximizing material strength, and stabilizing active material structure in anode, electrolyte, cathode and current collectors.
- In another embodiment of the present invention, methods are provided that morphology of periodic, irregular but not arbitrary electrode is identified by using one of the optimization techniques, but not limited to, surrogate-base analysis, genetic algorithm, adaptive topology optimization, design of experiments, ANOVA/MANOVA, basin based analysis, solid isotropic microstructure with intermediate mass penalization (SIMP), power penalized stiffness model, topology optimization of continuum structure, normal boundary intersection (NBI) optimization method, multivariable optimization method, or multidisciplinary design optimization.
- In another embodiment of the present invention, methods are provided that comprise of preparing microarchitectured electrodes. The microarchitectured electrode is characterized by periodic pattern by using a patterning technique selected from a group including but not limited to: periodically varying magnetic field, electric field, temperature gradient, and optical beam intensity, periodically seeding the current collector or substrate with precursor, periodically modifying the current collector or substrate using drilling, masking, molding, indentation, nanoimprint, abrasive, laser ablation, radiation and neutron scattering.
- In a specific embodiment, the various cell elements can be formed using one or more techniques. These techniques include evaporation, physical vapor deposition (PVD), chemical vapor deposition, low pressure chemical vapor deposition (LPCVD), atomic layer deposition (ALD), direct laser writing (DLW), sputtering, radio frequency magnetron sputtering, microwave plasma enhanced chemical vapor deposition (MPECVD), pulsed laser deposition (PLD), nanoimprint, ion implantation, laser ablation, spray deposition, spray pyrolysis, spray coating or plasma spraying. Of course, there can be other variations, modifications, and alternatives.
- Moreover, the present invention provides a micro-architectured electrochemical cell and/or battery device. The cell and/or battery device includes an anode and a cathode arranged anti-symmetrically with the anode. In a specific embodiment, the device has a predetermined distance between the cathode and the anode. An electrical insulation is provided to separate the anode from the cathode. In a specific embodiment, the electrical insulation is characterized by a graded material property that changes within a portion of the predetermined distance or one or more layers of insulating material to separate the anode from the cathode. In a specific embodiment, the device has a nanocomposite anode material characterizing the anode. In a preferred embodiment, the nanocomposite anode material has one or more first intensive characteristics that is a function of one or more second extensive characteristics. A nanocomposite cathode material characterizes the cathode. In a specific embodiment, the nanocomposite cathode material has one or more first intensive characteristics that is a function of one or more second extensive characteristics. In a specific embodiment, an electrolyte material is provided between the anode and the cathode. In a specific embodiment, the device has a cathode current collector in communication with the cathode and an anode current collector in communication with the anode.
- Still further, the present invention provides an electrochemical cell. The cell has an anode member having one or more first spatial features and formed substantially from a first nanocomposite material, which has an average feature size ranging from about 50 Å to about 500 nanometers. In a specific embodiment, the first nanocomposite material has a first resistivity value of greater than 8 micro-ohms centimeters, but can be others. In a specific embodiment, the cell has a cathode member having one or more second spatial features. The cathode member is operably coupled the anode member and is formed substantially from a second nanocomposite material, which has an average feature size ranging from about 50 Å to about 500 nanometers. In a specific embodiment, the second nanocomposite has a second resistivity value of greater than 14.3 ohms centimeters, but can be others. In a specific embodiment, the device has a predetermined gap between the anode and the cathode. In a specific embodiment, the predetermined gap is greater than 500 nanometers. The device also has an electrolyte provided between the anode and the cathode and a separator provided between the anode and the cathode. The device has a first current collector coupled to the anode via at least a first contact and a second current collector coupled to the cathode via at least a second contact.
- Still further, the present invention provides a method for fabricating an electrochemical cell. The method includes providing a substrate member having a predetermined spatial pattern, e.g., patterned, periodic. The method includes depositing a first thickness of material using one or more species overlying the predetermined spatial pattern in a conformal manner. In a specific embodiment, the first thickness of material is characterized as a nanocomposite structure having an average feature size of about 500 nanometers and less. The method includes adjusting one or more parameters related to the deposition during a time period associated with the deposition of the first thickness of material from a first spatial region of the first thickness of material to a second spatial region of the first thickness of material to form a first electrode element having a graded feature of one or more characteristics from the first spatial region to the second spatial region. The method forms an electrolyte overlying the first electrode element and forms a second electrode element overlying the electrolyte.
- In an alternative specific embodiment, the present invention provides a method for fabricating an electrode for an electrochemical cell. The method includes providing a substrate member comprising a current collector. The method includes depositing a thickness of material using one or more species overlying a surface region of the substrate member. In a specific embodiment, the thickness of material is characterized as a nanocomposite material. The method includes adjusting one or more parameters during a time period associated with the depositing of the thickness of material from a first spatial region of the thickness of material to a second spatial region of the thickness of material. The method also includes causing formation of an electrode element having a graded feature of one or more characteristics from the first spatial region to the second spatial region.
- Moreover, the present invention provides a method for fabricating a periodic geometric feature for an electrochemical cell. The method includes masking and exposing a region of substrate for an electrode member or current collector by periodically varying one or more parameters selected from at least a magnetic field, an electric field, a temperature gradient, and an optical beam intensity to seed the exposed region of the substrate with one or more precursors. In other embodiments, the method also includes periodically modifying one or more spatial regions of the exposed region of the substrate using at least one or more processes selected from drilling, masking, molding, indentation, nanoimprint, abrasive, laser ablation, radiation and neutron scattering. Of course, there can be other variations, modifications, and alternatives.
- The benefits of the invention include the ability it confers in rational design and combination of multiple materials to produce electrochemical cells, in novel arrangements. These in, turn, confer superior properties to designed cells, and elimination of costly-trial and error in construction of prototype cells. Depending upon the embodiment, one or more of these benefits can be achieved.
-
FIG. 1 Periodic, irregular but not arbitrary electrode according to an embodiment of the present invention. -
FIGS. 2 (A)-(B) are simplified cross-sectional views showing fabrication of a functionally graded electrode according to an embodiment of the present invention. - FIGS. 3(A)-(C) are simplified cross-sectional views showing fabrication of an electrode exhibiting a sinusoidal microarchitecture according to an embodiment of the present invention.
- FIGS. 4(A)-(D) are simplified cross-sectional views showing fabrication of an electrode exhibiting a nanocomposite material for electrode according to an alternative embodiment of the present invention.
-
FIG. 5(A) illustrates a cathode with thin-film design according to an alternative embodiment of the present invention; -
FIG. 5(B) illustrates a cathode with column design according to an alternative embodiment of the present invention; -
FIG. 5(C) illustrates a cathode with sinusoidal design according to an alternative embodiment of the present invention; -
FIG. 5(D) illustrates contours of von-Mises stress on column design electrode. - According to the present invention, techniques relate to manufacture of three-dimensional interdigitated electrochemical cells. More particularly, the present invention provides a method and system for manufacture of three-dimensional elements for three-dimensional interdigitated electrochemical cells. Merely by way of example, the invention has been provided with use of lithium based cells, but it would be recognized that other materials such as zinc, silver, copper and nickel could be designed in the same fashion. Additionally, such batteries can be used for a variety of applications such as portable electronics (cell phones, personal digital assistants, music players, video cameras, and the like), power tools, power supplies for military use (communications, lighting, imaging and the like), power supplies for aerospace applications (power for satellites), and power supplies for vehicle applications (hybrid electric vehicles, plug-in hybrid electric vehicles, and fully electric vehicles). The design of such batteries is also applicable to cases in which the battery is not the only power supply in the system, and additional power is provided by a fuel cell, other battery, IC engine or other combustion device, capacitor, solar cell, etc. Of course, there can be other variations, modifications, and alternatives.
- It is to be understood that both the forgoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the invention, as claimed. It may be noted that, as used in the specification and the appended claims, the singular forms “a”, “an”, and “the” include plural referents unless the context clearly dictates otherwise. Thus, for example, reference to “a material” may include mixture of materials; reference to “a compound” may include multiple compounds.
- In a specific embodiment, the present invention provides a structure that is irregular in shape, but has a periodic spatial feature. In a preferred embodiment, the irregularity is not arbitrary in shape or size. The irregularity has a predetermined spatial feature. As shown in
FIG. 1 , the structure has a first periodic spatial feature domain and a second periodic spatial feature domain. In a specific embodiment, each of the domains include common features, which may include a pyramidal shape, trapezoidal shape, dome shape, or any other shapes, including combinations, and the like. Of course, there can be other variations, modifications, and alternatives. - In a specific embodiment of the present invention, a device of electrochemical cells comprises of functionally graded and periodically spatial feature electrodes that would benefit its usage to extend lifetime and efficiency by mitigating the stress due to the ionic intercalation, alleviating thermal stress due to the electrochemical reaction, stabilizing the host material lattice structure during the charge-discharge process, and increasing the kinetic properties of the host material. The electrode described herein is referring to anode and cathode of a single electrochemical cell. The anode and cathode referring herein are based on the electric current direction and the mode. Therefore, the anode is the negative terminal in a discharge electrochemical cell (or also known as galvanic cell), but it would the positive terminal in a recharging electrochemical cell (or also known as electrolytic cell). The cathode is vice versa. The functionally graded electrodes described herein are characterized by the variation in composition and structure gradually over spatially volume of single electrode or whole electrochemical cells. The periodically spatial feature of electrodes or electrochemical cells of the device described herein is employed to strengthen material performance locally to facilitate the ionic diffusion, electronic conduction, and mitigating stress inside the electrodes.
- One advantage of using functionally graded electrode is that a specific function of a material is integrated with the host active material so that the benefit of that specific function would be added to improve overall electrode performance. The host active material referring herein is the material within an electrode responsible for the electronic energy exchange with counter electrode during the electrochemical reaction. The function described herein includes, but not limited to, mitigating intercalation stress due to the host material lattice increment, alleviating thermal stress due to the energy exchange within the whole device, and increasing the kinetic properties of the electrode in specific region, etc. For example, utilizing Li2MnO3 will stabilize LiMO2 lattice structure, where M include Mn, Ni and Co, during the charge-discharge process in a Li ion battery as described in U.S. Pat. No. 6,680,143 B2. But in this patent, the function of stabilizing lattice structure of the host active material is the only one.
- In another embodiment of the present invention, a method is provided that periodically spatial feature of the electrode is identified as shown in
FIG. 1 . As shown, the diagram includes a first period and a second period according to a specific embodiment. In a specific embodiment, each of the periods includes various shapes, e.g., pyramid, trapezoid, dome. The spatial feature of the electrode has impacts on the cell performance, such as mitigating stresses due to Li+ intercalation and temperature increment, etc. The preferred spatial feature will be identified by utilizing any optimization techniques. The optimization method comprises one technique from, but not limited to, the group of surrogate-base analysis, genetic algorithm, adaptive topology optimization, design of experiments, ANOVA/MANOVA, basin based analysis, solid isotropic microstructure with intermediate mass penalization (SIMP), power penalized stiffness model, topology optimization of continuum structure, normal boundary intersection (NBI) optimization method, multivariable optimization method, or multidisciplinary design optimization. A preferred embodiment of the present invention would be having a sinusoidal electrode profile, wherein the amplitude and frequency of the sinusoid will be determined by the optimization techniques listed above to have robust performance, long lifetime, and high safety. Of course, there can be other variations, modifications, and alternatives. - In certain embodiments of the present invention the atmosphere associated with the electrode material deposition may be changed. In one embodiment, the suitable atmosphere comprises a oxygen atmosphere to create metal oxide materials. In other embodiments the atmosphere may be a nitrogen atmosphere to create electrolyte layers or nitride materials.
- In some embodiments of the present invention the temperature associated to the electrode materials formation may be varied, continuously or step-wise to achieve particular materials microstructures. In one embodiment an annealing step up to 800° C. may be introduced to induce re-crystallization of amorphous metal oxides material layers.
- In other embodiments ambient temperature may be maintained constant by cooling the substrate and removing heat at a constant rate.
- In some embodiments of the present invention, architectured components of the battery, having geometric features ranging from 100 nanometers to 100 micrometers or below 500 micrometers, may be fabricated using any suitable technique from the following list, individually or in combination with each other: evaporation, physical vapor deposition (PVD), chemical vapor deposition, low pressure chemical vapor deposition (LPCVD), atomic layer deposition (ALD), direct laser writing (DLW), sputtering, radio frequency magnetron sputtering, microwave plasma enhanced chemical vapor deposition (MPECVD), pulsed laser deposition (PLD), nanoimprint, ion implantation, laser ablation, spray deposition, spray pyrolysis, spray coating or plasma spraying. Of course, there can be other variations, modifications, and alternatives.
- In another embodiment of the present invention, preferred materials for each member include, but not limited to, a substrate material comprising of copper (Cu), aluminum (Al), stainless steel, or other suitable conductive alloy in the form of a thin foil and bearing, an anode material comprising lithium metal (Li), lithium titanium oxide (Li4Ti5O12), graphite (C), or meso-carbon structures such as microbeads or other microstructures; an electrolyte material overlying the first electrode material and comprising lithium phosphorus oxynitride (LIPON), lithium salts such as LiClO4/LiPF6 mixed with poly-ethylene oxide (PEO), poly-vinylidene fluoride (PVDF), or combination of PEO and PVDF; and a cathode material overlying the electrolyte material and comprising layered metal oxide materials such as LiCoO2, spinel materials such as LiMn2O4, olivine materials such as LiFePO4, Li(Ni1/3Mn1/3Co1/3)O2, LiNixCoyAl(1-x-y)O2 (NCA), LiNixMnyCo(l-x-y)O2 (NCM). Further details of the methods and devices can be found throughout the present specification and more particularly below. The following descriptions are merely examples, which should not unduly limit the scope of the claims herein. One of ordinary skill in the art would recognize other variations, modifications, and alternatives.
- In
FIGS. 2A and 2B , a functionally graded graphite anode is created by focusing a laser beam through polymer electrolyte layer by layer gradually from current collector to some desired distance toward the surface of the polymer electrolyte with decreasing the frequency of turning on-and-off the laser beam as the focus point of the laser beam is gradually moved away from the current collector. The electrode 1 comprises of polymer electrolyte (LiPF6 plus polyethyleneoxide, PEO) 2 coated on top of copper current collector 3 as detailed described inFIG. 2A . Because of the high-energy of the Nd:YAG laser beam 4, the polymer in polymer electrolyte, where the laser beam is aimed, will be graphitized as 9 inFIG. 2B . Also, because of decreasing the frequency of turning on-and-off the laser beam (as shown in 6 to 8 inFIG. 2B ), the area of graphitized polymer in one layer will be decreased. Hence, concentration of the graphite-like electrode will be gradually decreased moving away from the current collector as 9 illustratedFIG. 2B . The strength of color black 9 indicates the concentration of graphite. Of course, there can be other variations, modifications, and alternatives. - In
FIGS. 3A , B, and C, a microarchitectured LiMn2O4 cathode having a periodic but non-arbitrary geometry is made using a silicon (Si) substrate 11 as a template. A Nd:YAG laser 13 is used to machine the substrate and remove material 14, creating a set of channels and ridges that follows a predetermined geometry obtained using a Computer Aided Design (CAD) software as 12. The design is reflecting minimization of intercalation stresses in the LiMn2O4 material according to computer simulations. Once the substrate machining is completed conformal material layers are deposited using physical vapor deposition (PVD) onto the substrate. Respectively, a first titanium (Ti) 18 attachment layer, having a thickness of 50 Å or less, followed by a second aluminum (Al) layer 19, having a thickness of 500 nanometers or higher, to serve as cathode current collector. After deposition of the current collector, the active material (LiMn2O4) 20 is formed following the same geometry imprinted by the substrate. The thickness of the active material is 1-10 μm. Of course, there can be other variations, modifications, and alternatives. - In
FIGS. 4A , B, C, and D, a LiMn2O4 partially stabilized cathode is fabricated by depositing conformal material layers using physical vapor deposition (PVD). The same procedure illustrated here can be used with or without the pre-existence of a substrate 22. In this latter case, the current collector is also serving as substrate material 22. A first layer of LiMn2O4, 23, is deposited having a thickness of 100-500 nanometers. After the first layer is completed a mask, 26, having geometric features of 100 nanometers or higher, is applied onto it and a layer of Li2MnO3, 29, is deposited. Finally the mask is removed and another layer of LiMn2O4, 34, having a thickness of 100-500 nanometers, is deposited to embed the Li2MnO3 features previously created. - Alternatively to using a mask, sputtering of Li2MnO3 can be employed to create irregular second phase regions on the first layer followed by a layer of LiMn2O4, having a thickness of 100-500 nanometers deposited to embed the second phases. As a third option is to create a uniform layer of Li2MnO3 onto the first layer of LiMn2O4 having a thickness of 50-100 nanometers and then a new layer of LiMn2O4, having a thickness of 100-500 nanometers to sandwich the Li2MnO3 layer. The function of the Li2MnO3 regions is to stabilize the spinel crystal structure of LiMn2O4 when, during discharge the number of Li+ ions is depleted and the structure becomes metastable. Normally the cathode material would transform to a more stable spinel-type configuration degrading the high potential and limiting capacity and rechargeability of the electrode, however the second phase prevents this from happening. Of course, there can be other variations, modifications, and alternatives.
- This example demonstrates the process of identifying a new electrochemical cell with the optimal morphological shape of the electrode. As an example of the problems encountered by the designer, three different morphological designs of three-dimensional electrodes are provided: thin-film in
FIG. 5A , columnar shape inFIG. 5B , and a sinusoidal shape inFIG. 5C . The materials for the three-dimensional electrochemical cells are copper as anode current collector (101 inFIG. 5A , 108 inFIG. 5B , 113 inFIG. 5C ), lithium metal as anode (102 inFIG. 5A , 109 inFIG. 5B , 114 inFIG. 5C ), lithium manganese oxide as cathode (103 inFIG. 5A , 110 inFIG. 5B , 115 inFIG. 5C ), polymer (polyethyleneoxide, PEO) with lithium salts (LiPF6) as the electrolyte (104 inFIG. 5A , 111 inFIG. 5B , 116 inFIG. 5C ), and aluminum as cathode current collector (105 inFIG. 5A , 112 inFIG. 5B , 117 inFIG. 5C ). Because a polymer electrolyte is used, a separator is unnecessary. These three electrochemical cells (100, 106, and 112) are produced by physical vapor deposition (PVD) technique. Hence, the breadloafing is not avoidable. Cell performance of 100 would not be suitable for high-rate performance due to the low kinetic properties of LiMn2O4 103, such as the diffusivity of Li+ and electronic conductivity. Therefore, increasing the surface area of LiMn2O4 electrode would increase LiMn2O4 electrode exposure to the electrolyte; hence, increase the high-rate performance. The morphology of 106 and 112 are two possibilities. By utilizing the computational technique, described in commonly assigned, co-pending U.S. patent application Ser. No. 12/484,959, which is hereby incorporated by reference, as a numerical experiment, it shows that the maximum stress occurred at the edge, where the LiMn2O4, 110, connect with the current collector, 111 as indicated inFIG. 5D . Of course, there can be other variations, modifications, and alternatives. - While the above is a full description of the specific embodiments, various modifications, alternative constructions and equivalents may be used. Therefore, the above description and illustrations should not be taken as limiting the scope of the present invention which is defined by the appended claims.
Claims (40)
1. A micro-architectured electrochemical cell and/or battery device comprising:
an anode;
a cathode arranged anti-symmetrically with the anode;
a predetermined distance between the cathode and the anode;
an electrical insulation provided to separate the anode from the cathode, the electrical insulation being characterized by a graded material property that changes within a portion of the predetermined distance or one or more layers of insulating material to separate the anode from the cathode;
a nanocomposite anode material characterizing the anode, the nanocomposite anode material having one or more first intensive characteristics that is a function of one or more second extensive characteristics;
a nanocomposite cathode material characterizing the cathode, the nanocomposite cathode material having one or more first intensive characteristics that is a function of one or more second extensive characteristics;
an electrolyte material provided between the anode and the cathode;
a cathode current collector in communication with the cathode; and
an anode current collector in communication with the anode.
2. The device of claim 1 further comprising a substrate to support the current collector if depositing current collector material mechanical properties are not suitable for further deposition.
3. An electrochemical cell comprising:
an anode member having one or more first spatial features and formed substantially from a first nanocomposite material, the first nanocomposite material having an average feature size ranging from about 50 Å to about 500 nanometers, the first nanocomposite material having a first resistivity value of greater than 8 microohms centimeters;
a cathode member having one or more second spatial features, the cathode member being operably coupled the anode member and formed substantially from a second nanocomposite material, the second nanocomposite material having an average feature size ranging from about 50 Å to about 500 nanometers, the second nanocomposite having a second resistivity value of greater than 14.3 ohms centimeters;
a predetermined gap between the anode and the cathode, the predetermined gap being greater than 500 nanometers;
an electrolyte provided between the anode and the cathode;
a separator provided between the anode and the cathode;
a first current collector coupled to the anode via at least a first contact; and
a second current collector coupled to the cathode via at least a second contact.
4. The electrochemical cell of claim 3 further comprising an aggregate resistance, the aggregate resistance being derived from a sum of resistance values from one or more leads, the first contact, the second contact, the first resistance value, the second resistance value, and one or more resistance values between one or more different elements of the electrochemical cell.
5. The electrochemical cell of claim 3 wherein the first nanocomposite material is substantially free from a localized charge of 1 eV and greater.
6. The electrochemical cell of claim 3 wherein the second nanocomposite material is substantially free from a localized charge of 1 eV and greater.
7. The electrochemical cell of claim 3 wherein the first nanocomposite material is selected from at least a transition metal, oxide of a metal, Groups IA, IVA, VIA, and IIB.
8. The electrochemical cell of claim 3 wherein the second nanocomposite material is selected from at least a transition metal, oxide of a metal, Groups IA, VIII, IVA, VIA, IB, IVB and VIIB.
9. The electrochemical cell of claim 3 wherein the electrolyte is selected from a liquid, solid, or gel.
10. The electrochemical cell of claim 3 wherein the electrolyte is selected from a ceramic, a semiconductor, a polymeric material, or any material in an aqueous solution.
11. The electrochemical cell of claim 3 wherein the electrolyte is either homogeneous or inhomogeneous.
12. The electrochemical cell of claim 3 wherein the electrolyte is a nanocomposite, microcomposite, or other heterogeneous structure.
13. The electrochemical cell of claim 3 wherein the electrolyte comprises one or more first intensive characteristics referenced against one or more second extensive characteristics.
14. The electrochemical cell of claim 3 wherein the anode member and/or cathode member comprises a dopant to maintain surfaces of either or both the anode member and/or the cathode member substantially free from dendrites.
15. The electrochemical cell of claim 14 wherein the dopant is selected from any one or more combinations of Groups IA through VIIA, and Groups IIB-VIIB, and Group VIII, inclusive and in any permutation.
16. The electrochemical cell of claim 14 wherein the dopant is provide in a homogeneous configuration or graded configuration.
17. A method for fabricating an electrode for an electrochemical cell, the method comprising:
providing a substrate member having a predetermined spatial pattern;
depositing a thickness of material using one or more species overlying the predetermined spatial pattern in a conformal manner, the thickness of material being characterized as a nanocomposite structure having an average feature size of about 500 nanometers and less;
adjusting one or more parameters related to the deposition during a time period associated with the deposition of the thickness of material from a first spatial region of the thickness of material to a second spatial region of the thickness of material; and
outputting an electrode element having a graded feature of one or more characteristics from the first spatial region to the second spatial region.
18. The method of claim 17 wherein the electrodes are formed using at least one technique from the group of evaporation, physical vapor deposition (PVD), chemical vapor deposition, low pressure chemical vapor deposition (LPCVD), atomic layer deposition (ALD), direct laser writing (DLW), sputtering, radio frequency magnetron sputtering, microwave plasma enhanced chemical vapor deposition (MPECVD), pulsed laser deposition (PLD), nanoimprint, ion implantation, laser ablation, spray deposition, spray pyrolysis, spray coating or plasma spraying.
19. The method of claim 17 further comprises adding a non liquid electrolyte for an electrochemical cell using the electrode element, the non-liquid electrolyte being made using a process selected from physical vapor deposition, laser deposition, centrifuge, spinning, microwave, thermal gradient, sintering, spray deposition, and chemical vapor deposition.
20. The method of claim 19 wherein an anode element, the electrolyte, and a cathode member are deposited sequentially or in reverse order.
21. The method of claim 17 wherein the one or more characteristics is selected from an intensive property including mass density, energy density, power density, composition, concentration, thermal/electronic/ionic conductivities, thermal/ionic diffusivities, maximum strain, ultimate strength, moduli, ductility, and plasticity.
22. The method of claim 17 wherein the electrode element is characterized by an optimized morphology created for neutralizing internal stresses, stopping crack growth, maximizing material strength, and stabilizing active material structure in anode, electrolyte, cathode and current collectors.
23. The method of claim 17 further comprising a refresh process to reintroduce the graded feature of one or more characteristics from the first spatial region to the second spatial region if the graded feature is diminished from the first spatial region to the second spatial region.
24. The method of claim 17 wherein the predetermined spatial pattern is an electrode design, the electrode design being provided by a mathematical process.
25. The method of claim 24 wherein the mathematical process uses a minimization or maximization of an intensive characteristic from within an allowed set of material characteristics.
26. The method of claim 25 wherein the mathematical process is selected from at least a surrogate-base analysis, genetic algorithm, adaptive topology optimization, design of experiments, ANOVA/MANOVA, basin based analysis, solid isotropic microstructure with intermediate mass penalization (SIMP), power penalized stiffness model, topology optimization of continuum structure, normal boundary intersection (NBI) optimization method, multivariable optimization method, or multidisciplinary design optimization.
27. The method of claim 17 wherein the depositing and adjusting is provided in a deposition chamber.
28. The method of claim 27 wherein the deposition chamber is provided to output a complete battery.
29. A method for fabricating an electrochemical cell, the method comprising:
providing a substrate member having a predetermined spatial pattern;
depositing a first thickness of material using one or more species overlying the predetermined spatial pattern in a conformal manner, the first thickness of material being characterized as a nanocomposite structure having an average feature size of about 500 nanometers and less;
adjusting one or more parameters related to the deposition during a time period associated with the deposition of the first thickness of material from a first spatial region of the first thickness of material to a second spatial region of the first thickness of material to form a first electrode element having a graded feature of one or more characteristics from the first spatial region to the second spatial region;
forming an electrolyte overlying the first electrode element; and
forming a second electrode element overlying the electrolyte.
30. The method of claim 29 wherein the first electrode element, the second electrode element, and the electrolyte are provided within one or more deposition chambers.
31. The method of claim 29 wherein the first electrode element is a cathode and the second electrode element is an anode.
32. The method of claim 29 wherein the first electrode element is an anode and the second electrode element is a cathode.
33. The method of claim 29 further comprising depositing an anode current collector and a cathode current collector.
34. The method of claim 29 wherein the first electrode element, the electrolyte, and the second electrode element are deposited sequentially.
35. The method of claim 29 wherein the first electrode element, the electrolyte, and the second electrode element are deposited sequentially and continuously without breaking vacuum.
36. The method of claim 29 further comprising providing a separator between the first electrode element and the second electrode element.
37. The method of claim 36 wherein the separator is provided within the electrolyte.
38. A method for fabricating an electrode for an electrochemical cell, the method comprising:
providing a substrate member comprising a current collector;
depositing a thickness of material using one or more species overlying a surface region of the substrate member, the thickness of material being characterized as a nanocomposite material;
adjusting one or more parameters during a time period associated with the depositing of the thickness of material from a first spatial region of the thickness of material to a second spatial region of the thickness of material; and
causing formation of an electrode element having a graded feature of one or more characteristics from the first spatial region to the second spatial region.
39. A method for fabricating a periodic geometric feature for an electrochemical cell, the method comprising:
masking and exposing a region of substrate for an electrode member or current collector, or exposing the electrode member itself, by periodically varying one or more parameters selected from at least a magnetic field, an electric field, a temperature gradient, and an optical beam intensity to seed the exposed region of the substrate with one or more precursors.
40. The method of claim 39 further comprising periodically modifying one or more spatial regions of the exposed region of the substrate for the electrode member or the electrode member itself, using at least one or more processes selected from drilling, masking, molding, indentation, nanoimprint, abrasive, laser ablation, radiation and neutron scattering.
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---|---|---|---|---|
US20090325063A1 (en) * | 2008-06-20 | 2009-12-31 | Sakti3, Inc. | Method for high volume manufacture of electrochemical cells using physical vapor deposition |
US20110202159A1 (en) * | 2008-06-20 | 2011-08-18 | Sakti3, Inc. | Computational method for design and manufacture of electrochemical systems |
US20120046776A1 (en) * | 2011-10-31 | 2012-02-23 | Sakti3, Inc. | Computer aided solid state battery design method and manufacture of same using selected combinations of characteristics |
US8357464B2 (en) | 2011-04-01 | 2013-01-22 | Sakti3, Inc. | Electric vehicle propulsion system and method utilizing solid-state rechargeable electrochemical cells |
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US20140272560A1 (en) * | 2013-03-13 | 2014-09-18 | Apple Inc. | Method to Improve LiCoO2 Morphology in Thin Film Batteries |
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SE2250839A1 (en) * | 2022-07-04 | 2024-01-05 | Northvolt Ab | Electrode for a secondary cell |
Families Citing this family (14)
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US11590568B2 (en) | 2019-12-19 | 2023-02-28 | 6K Inc. | Process for producing spheroidized powder from feedstock materials |
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WO2022094528A1 (en) | 2020-10-30 | 2022-05-05 | 6K Inc. | Systems and methods for synthesis of spheroidized metal powders |
Citations (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62122057A (en) * | 1985-11-22 | 1987-06-03 | Toshiba Battery Co Ltd | Button type battery |
US6022590A (en) * | 1994-07-14 | 2000-02-08 | Competitive Technologies, Inc. | Stepwise formation of multilayered nanostructures from macromolecular precursors |
US6442743B1 (en) * | 1998-06-12 | 2002-08-27 | Monterey Design Systems | Placement method for integrated circuit design using topo-clustering |
US20030027033A1 (en) * | 2001-06-29 | 2003-02-06 | Seabaugh Matthew M. | Nano-composite electrodes and method of making the same |
US20030082446A1 (en) * | 2000-10-20 | 2003-05-01 | Yet-Ming Chiang | Reticulated and controlled porosity battery structures |
US20030099884A1 (en) * | 2001-07-27 | 2003-05-29 | A123Systems, Inc. | Battery structures, self-organizing structures and related methods |
US20040131934A1 (en) * | 2001-03-20 | 2004-07-08 | Francois Sugnaux | Mesoporous network electrode for electrochemical cell |
US20040265690A1 (en) * | 2003-01-08 | 2004-12-30 | Hon Hai Precision Industry Co., Ltd. | Secondary battery with improved energy density and method for making the same |
US6982132B1 (en) * | 1997-10-15 | 2006-01-03 | Trustees Of Tufts College | Rechargeable thin film battery and method for making the same |
US20060057354A1 (en) * | 2000-05-30 | 2006-03-16 | Penn State Research Foundation | Electronic and opto-electronic devices fabricated from nanostructured high surface to volume ratio thin films |
US20060141137A1 (en) * | 2003-04-28 | 2006-06-29 | Harlan Anderson | Method for fabricating nanostructured solid oxide fuel cells and cell components |
JP2006185800A (en) * | 2004-12-28 | 2006-07-13 | Dainippon Printing Co Ltd | Transfer sheet for manufacturing electrode-polyelectrolyte membrane junction, electrode-polyelectrolyte membrane junction and their manufacturing methods |
US20060275668A1 (en) * | 2005-05-13 | 2006-12-07 | Saft | Nanocomposite material for the anode of a lithium cell |
US20070036978A1 (en) * | 2005-05-20 | 2007-02-15 | University Of Central Florida | Carbon nanotube reinforced metal composites |
US20070059573A1 (en) * | 2005-09-13 | 2007-03-15 | Debe Mark K | Enhanced catalyst interface for membrane electrode assembly |
US20070202403A1 (en) * | 2005-09-06 | 2007-08-30 | Eun-Suok Oh | Composite binder containing carbon nanotube and lithium secondary battery employing the same |
US20080044732A1 (en) * | 2004-12-23 | 2008-02-21 | Commissariat A L'energie Atomique | Nanostructured Electrode for a Microbattery |
US20080044685A1 (en) * | 2003-12-31 | 2008-02-21 | Sungho Jin | Articles Comprising High-Electrical-Conductivity Nanocomposite Material and Method for Fabricating Same |
WO2008059740A1 (en) * | 2006-11-15 | 2008-05-22 | Toyota Jidosha Kabushiki Kaisha | Accumulator |
US20080128021A1 (en) * | 2006-09-06 | 2008-06-05 | The Research Foundation Of State University Of New York | Nanocomposite devices, methods of making them, and uses thereof |
US20090032394A1 (en) * | 2006-01-23 | 2009-02-05 | Hitachi Chemical Co., Ltd. | Ionic polymer devices and methods of fabricating the same |
US20110169193A1 (en) * | 2004-08-11 | 2011-07-14 | Cornell Research Foundation | Modular fabrication systems and methods |
Family Cites Families (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3940546B2 (en) * | 1999-06-07 | 2007-07-04 | 株式会社東芝 | Pattern forming method and pattern forming material |
US6680143B2 (en) | 2000-06-22 | 2004-01-20 | The University Of Chicago | Lithium metal oxide electrodes for lithium cells and batteries |
JP4375042B2 (en) * | 2003-02-18 | 2009-12-02 | 三菱化学株式会社 | Negative electrode material and negative electrode for non-aqueous lithium ion secondary battery, and non-aqueous lithium ion secondary battery |
CN1266785C (en) * | 2003-08-03 | 2006-07-26 | 鸿富锦精密工业(深圳)有限公司 | Cell and its preparing method |
JP2005093373A (en) * | 2003-09-19 | 2005-04-07 | Matsushita Electric Ind Co Ltd | Energy device and its manufacturing method |
JP4850405B2 (en) * | 2003-11-27 | 2012-01-11 | パナソニック株式会社 | Lithium ion secondary battery and manufacturing method thereof |
US8187740B2 (en) * | 2004-04-27 | 2012-05-29 | Tel Aviv University Future Technology Development L.P. | 3-D microbatteries based on interlaced micro-container structures |
EP1834369B1 (en) * | 2005-01-06 | 2014-03-05 | Rutgers, The State University of New Jersey | Electrochemically self assembled batteries |
JP4861633B2 (en) * | 2005-03-14 | 2012-01-25 | 独立行政法人科学技術振興機構 | Method for producing carbon / tin oxide nanocomposite |
TWI467840B (en) * | 2005-09-02 | 2015-01-01 | A123 Systems Inc | Nanocomposite electrodes and related devices |
EP1770817A3 (en) * | 2005-09-29 | 2007-12-05 | Air Products and Chemicals, Inc. | Surface-lithiated metal oxide nanoparticles for lithium battery electrolytes |
JP2007250210A (en) * | 2006-03-13 | 2007-09-27 | Nissan Motor Co Ltd | Electrode catalyst layer for fuel cell and its manufacturing method |
JP5145648B2 (en) * | 2006-04-14 | 2013-02-20 | 日産自動車株式会社 | Lithium ion secondary battery |
WO2008086041A1 (en) * | 2007-01-10 | 2008-07-17 | Nanoexa, Inc. | Lithium batteries with nano-composite positive electrode material |
US7945344B2 (en) | 2008-06-20 | 2011-05-17 | SAKT13, Inc. | Computational method for design and manufacture of electrochemical systems |
-
2009
- 2009-08-04 CN CN201410314611.3A patent/CN104183819A/en active Pending
- 2009-08-04 CN CN2009801393132A patent/CN102171873A/en active Pending
- 2009-08-04 US US12/535,632 patent/US20100035152A1/en active Pending
- 2009-08-04 CN CN201610136606.7A patent/CN105762324A/en active Pending
- 2009-08-04 EP EP09805459.6A patent/EP2311122A4/en not_active Withdrawn
- 2009-08-04 JP JP2011522189A patent/JP5846910B2/en active Active
- 2009-08-04 KR KR1020117005215A patent/KR101259455B1/en active IP Right Grant
- 2009-08-04 WO PCT/US2009/052745 patent/WO2010017227A1/en active Application Filing
- 2009-08-04 MY MYPI2011000520A patent/MY163851A/en unknown
-
2015
- 2015-06-05 US US14/732,630 patent/US10777804B2/en active Active
Patent Citations (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62122057A (en) * | 1985-11-22 | 1987-06-03 | Toshiba Battery Co Ltd | Button type battery |
US6022590A (en) * | 1994-07-14 | 2000-02-08 | Competitive Technologies, Inc. | Stepwise formation of multilayered nanostructures from macromolecular precursors |
US6982132B1 (en) * | 1997-10-15 | 2006-01-03 | Trustees Of Tufts College | Rechargeable thin film battery and method for making the same |
US6442743B1 (en) * | 1998-06-12 | 2002-08-27 | Monterey Design Systems | Placement method for integrated circuit design using topo-clustering |
US20060057354A1 (en) * | 2000-05-30 | 2006-03-16 | Penn State Research Foundation | Electronic and opto-electronic devices fabricated from nanostructured high surface to volume ratio thin films |
US7341774B2 (en) * | 2000-05-30 | 2008-03-11 | The Penn State Research Foundation | Electronic and opto-electronic devices fabricated from nanostructured high surface to volume ratio thin films |
US20030082446A1 (en) * | 2000-10-20 | 2003-05-01 | Yet-Ming Chiang | Reticulated and controlled porosity battery structures |
US20040131934A1 (en) * | 2001-03-20 | 2004-07-08 | Francois Sugnaux | Mesoporous network electrode for electrochemical cell |
US20030027033A1 (en) * | 2001-06-29 | 2003-02-06 | Seabaugh Matthew M. | Nano-composite electrodes and method of making the same |
US20030099884A1 (en) * | 2001-07-27 | 2003-05-29 | A123Systems, Inc. | Battery structures, self-organizing structures and related methods |
US20040265690A1 (en) * | 2003-01-08 | 2004-12-30 | Hon Hai Precision Industry Co., Ltd. | Secondary battery with improved energy density and method for making the same |
US7090891B2 (en) * | 2003-04-28 | 2006-08-15 | Curators Of The University Of Missouri | Method for fabricating nanostructured solid oxide fuel cells and cell components |
US20060141137A1 (en) * | 2003-04-28 | 2006-06-29 | Harlan Anderson | Method for fabricating nanostructured solid oxide fuel cells and cell components |
US20080044685A1 (en) * | 2003-12-31 | 2008-02-21 | Sungho Jin | Articles Comprising High-Electrical-Conductivity Nanocomposite Material and Method for Fabricating Same |
US20110169193A1 (en) * | 2004-08-11 | 2011-07-14 | Cornell Research Foundation | Modular fabrication systems and methods |
US20080044732A1 (en) * | 2004-12-23 | 2008-02-21 | Commissariat A L'energie Atomique | Nanostructured Electrode for a Microbattery |
JP2006185800A (en) * | 2004-12-28 | 2006-07-13 | Dainippon Printing Co Ltd | Transfer sheet for manufacturing electrode-polyelectrolyte membrane junction, electrode-polyelectrolyte membrane junction and their manufacturing methods |
US20060275668A1 (en) * | 2005-05-13 | 2006-12-07 | Saft | Nanocomposite material for the anode of a lithium cell |
US20070036978A1 (en) * | 2005-05-20 | 2007-02-15 | University Of Central Florida | Carbon nanotube reinforced metal composites |
US20070202403A1 (en) * | 2005-09-06 | 2007-08-30 | Eun-Suok Oh | Composite binder containing carbon nanotube and lithium secondary battery employing the same |
US20070059573A1 (en) * | 2005-09-13 | 2007-03-15 | Debe Mark K | Enhanced catalyst interface for membrane electrode assembly |
US20090032394A1 (en) * | 2006-01-23 | 2009-02-05 | Hitachi Chemical Co., Ltd. | Ionic polymer devices and methods of fabricating the same |
US20080128021A1 (en) * | 2006-09-06 | 2008-06-05 | The Research Foundation Of State University Of New York | Nanocomposite devices, methods of making them, and uses thereof |
US20090017371A1 (en) * | 2006-11-15 | 2009-01-15 | Yoshiyuki Nakamura | Power Storage Device |
WO2008059740A1 (en) * | 2006-11-15 | 2008-05-22 | Toyota Jidosha Kabushiki Kaisha | Accumulator |
Non-Patent Citations (1)
Title |
---|
Machine translation of Nishimura et al., JP 2006-185800 A. * |
Cited By (70)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110202159A1 (en) * | 2008-06-20 | 2011-08-18 | Sakti3, Inc. | Computational method for design and manufacture of electrochemical systems |
US20110212268A1 (en) * | 2008-06-20 | 2011-09-01 | Sakti3, Inc. | Method for high volume manufacture of electrochemical cells using physical vapor deposition |
US20110217578A1 (en) * | 2008-06-20 | 2011-09-08 | Sakti3, Inc. | Method for high volume manufacture of electrochemical cells using physical vapor deposition |
US9666895B2 (en) | 2008-06-20 | 2017-05-30 | Sakti3, Inc. | Computational method for design and manufacture of electrochemical systems |
US20090325063A1 (en) * | 2008-06-20 | 2009-12-31 | Sakti3, Inc. | Method for high volume manufacture of electrochemical cells using physical vapor deposition |
US9303315B2 (en) | 2008-06-20 | 2016-04-05 | Sakti3, Inc. | Method for high volume manufacture of electrochemical cells using physical vapor deposition |
US9249502B2 (en) | 2008-06-20 | 2016-02-02 | Sakti3, Inc. | Method for high volume manufacture of electrochemical cells using physical vapor deposition |
US8889285B2 (en) | 2011-04-01 | 2014-11-18 | Sakti3, Inc. | Electric vehicle propulsion system and method utilizing solid-state rechargeable electrochemical cells |
US9929440B2 (en) | 2011-04-01 | 2018-03-27 | Sakti3, Inc. | Electric vehicle propulsion system and method utilizing solid-state rechargeable electrochemical cells |
US8357464B2 (en) | 2011-04-01 | 2013-01-22 | Sakti3, Inc. | Electric vehicle propulsion system and method utilizing solid-state rechargeable electrochemical cells |
JP2013214489A (en) * | 2011-07-04 | 2013-10-17 | Nissan Motor Co Ltd | Positive electrode active material for electric device, positive electrode for electric device, and electric device |
WO2013060422A1 (en) | 2011-10-29 | 2013-05-02 | Karlsruher Institut für Technologie | Electrode material for lithium ion batteries and method for the production thereof |
DE102011120893B3 (en) * | 2011-10-29 | 2013-03-07 | Karlsruher Institut für Technologie | Electrode material for lithium-ion batteries and method for its production |
US20120046776A1 (en) * | 2011-10-31 | 2012-02-23 | Sakti3, Inc. | Computer aided solid state battery design method and manufacture of same using selected combinations of characteristics |
US8301285B2 (en) * | 2011-10-31 | 2012-10-30 | Sakti3, Inc. | Computer aided solid state battery design method and manufacture of same using selected combinations of characteristics |
US9631269B2 (en) | 2011-11-08 | 2017-04-25 | Sakti3, Inc. | Thermal evaporation process for manufacture of solid state battery devices |
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US9127344B2 (en) | 2011-11-08 | 2015-09-08 | Sakti3, Inc. | Thermal evaporation process for manufacture of solid state battery devices |
US10770745B2 (en) | 2011-11-09 | 2020-09-08 | Sakti3, Inc. | Monolithically integrated thin-film solid state lithium battery device having multiple layers of lithium electrochemical cells |
US9627717B1 (en) | 2012-10-16 | 2017-04-18 | Sakti3, Inc. | Embedded solid-state battery |
US10497984B2 (en) | 2012-10-16 | 2019-12-03 | Sakti3, Inc. | Embedded solid-state battery |
US10439187B2 (en) | 2012-11-27 | 2019-10-08 | Apple Inc. | Laminar battery system |
US10211433B2 (en) | 2012-11-27 | 2019-02-19 | Apple Inc. | Battery packaging |
US9711770B2 (en) | 2012-11-27 | 2017-07-18 | Apple Inc. | Laminar battery system |
US10033029B2 (en) | 2012-11-27 | 2018-07-24 | Apple Inc. | Battery with increased energy density and method of manufacturing the same |
US20140272560A1 (en) * | 2013-03-13 | 2014-09-18 | Apple Inc. | Method to Improve LiCoO2 Morphology in Thin Film Batteries |
US9899661B2 (en) * | 2013-03-13 | 2018-02-20 | Apple Inc. | Method to improve LiCoO2 morphology in thin film batteries |
US9601751B2 (en) | 2013-03-15 | 2017-03-21 | Apple Inc. | Annealing method for thin film electrodes |
US11508984B2 (en) | 2013-03-15 | 2022-11-22 | Apple Inc. | Thin film pattern layer battery systems |
US9570775B2 (en) | 2013-03-15 | 2017-02-14 | Apple Inc. | Thin film transfer battery systems |
US9887403B2 (en) | 2013-03-15 | 2018-02-06 | Apple Inc. | Thin film encapsulation battery systems |
US10141600B2 (en) | 2013-03-15 | 2018-11-27 | Apple Inc. | Thin film pattern layer battery systems |
US9553314B2 (en) * | 2013-04-12 | 2017-01-24 | The Regents Of The University Of Michigan | Pulsed laser chemical vapor deposition and surface modification |
US20140308587A1 (en) * | 2013-04-12 | 2014-10-16 | The Regents Of The University Of Michigan | Pulsed laser chemical vapor deposition and surface modification |
US20150056432A1 (en) * | 2013-08-26 | 2015-02-26 | Palo Alto Research Center Incorporated | Co-extrusion of periodically modulated structures |
US10800086B2 (en) * | 2013-08-26 | 2020-10-13 | Palo Alto Research Center Incorporated | Co-extrusion of periodically modulated structures |
US9748569B2 (en) * | 2013-09-04 | 2017-08-29 | Applejack 199 L.P. | Porous, thin film electrodes for lithium-ion batteries |
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US11271205B2 (en) | 2014-07-17 | 2022-03-08 | Ada Technologies, Inc. | Extreme long life, high energy density batteries and method of making and using the same |
US9755235B2 (en) | 2014-07-17 | 2017-09-05 | Ada Technologies, Inc. | Extreme long life, high energy density batteries and method of making and using the same |
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US10930915B2 (en) | 2014-09-02 | 2021-02-23 | Apple Inc. | Coupling tolerance accommodating contacts or leads for batteries |
US9627709B2 (en) | 2014-10-15 | 2017-04-18 | Sakti3, Inc. | Amorphous cathode material for battery device |
US10593985B2 (en) | 2014-10-15 | 2020-03-17 | Sakti3, Inc. | Amorphous cathode material for battery device |
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EP3254328A4 (en) * | 2015-02-02 | 2018-08-22 | Sakti3, Inc. | Solid state energy storage device |
US10217571B2 (en) | 2015-05-21 | 2019-02-26 | Ada Technologies, Inc. | High energy density hybrid pseudocapacitors and method of making and using the same |
US10692659B2 (en) | 2015-07-31 | 2020-06-23 | Ada Technologies, Inc. | High energy and power electrochemical device and method of making and using same |
WO2017045945A1 (en) * | 2015-09-16 | 2017-03-23 | Robert Bosch Gmbh | Active material for a positive electrode of a battery cell, positive electrode and battery cell |
US10790502B2 (en) | 2015-09-16 | 2020-09-29 | Robert Bosch Gmbh | Active material for a positive electrode of a battery cell, positive electrode, and battery cell |
US10476080B2 (en) | 2016-01-19 | 2019-11-12 | Samsung Electronics Co., Ltd. | Electrode containing both anion-absorbing and cation-absorbing active materials |
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US10818929B2 (en) | 2016-08-25 | 2020-10-27 | Lg Chem, Ltd. | Electrode for secondary battery having fine holes |
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US11456488B2 (en) | 2016-09-28 | 2022-09-27 | Samsung Electronics Co., Ltd. | All solid type three-dimensional battery and method of manufacturing the same |
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US10343552B2 (en) | 2017-02-08 | 2019-07-09 | Samsung Electronics Co., Ltd. | Heterogeneous electrical energy storage system |
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Also Published As
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KR101259455B1 (en) | 2013-04-29 |
CN104183819A (en) | 2014-12-03 |
MY163851A (en) | 2017-10-31 |
WO2010017227A1 (en) | 2010-02-11 |
CN102171873A (en) | 2011-08-31 |
JP2011530787A (en) | 2011-12-22 |
KR20110045038A (en) | 2011-05-03 |
JP5846910B2 (en) | 2016-01-20 |
US20150270532A1 (en) | 2015-09-24 |
CN105762324A (en) | 2016-07-13 |
EP2311122A4 (en) | 2014-04-02 |
EP2311122A1 (en) | 2011-04-20 |
US10777804B2 (en) | 2020-09-15 |
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