A combination of a lithium-utilizing capacitor and a lithium-ion battery is made in which each member of the combination comprises porous electrode layers prepared by using atmospheric plasma coating devices and processes. The layered, electrochemical, capacitor and battery are assembled in a common pouch and electrically interconnected as a hybridized capacitor-battery, suitable for providing balanced energy and power to electrical load demanding devices.
Electric powered automotive vehicles use multi-cell batteries to provide electrical energy for providing electrical power for driving the vehicle and for providing electrical energy to many devices on the vehicle. Batteries comprising many lithium-ion electrochemical cells are examples of such electrical power sources. And such batteries are used in many non-automotive applications.
In some applications it may be useful to combine a lithium-ion battery with an electrochemical capacitor which also uses lithium ions. For example, such capacitors may be charged during braking of the vehicle and the stored electrical charge used later in recharging cells of a lithium-ion battery.
There is a need for manufacturing practices to jointly prepare cells for lithium-ion batteries and such electrochemical capacitors for efficiency in their mutual interconnection and interaction.
It is believed that there are applications in electrically powered automotive vehicles (and in non-automotive applications) in which suitable lithium-containing capacitor structures and suitable lithium-ion battery structures may be placed close to each other, as in a common pouch or like container, and share a common volume of a lithium-ion conducting electrolyte, with a suitable amount of electrolyte constituents for both devices. A hybridized combination of capacitor and battery is thus provided. The capacitor and battery each use lithium, and a lithium-ion conducting electrolyte, in its electrochemical function.
Here the capacitors include (1) electric double layer capacitors (ELDC), (2) supercapacitors, and (3) hybridcapacitors. An ELDC-type capacitor is based on the formation of electric double layers on the surfaces of electrodes, where cations and anions of an electrolyte form Helmholz layers on the surfaces of both electrodes. During cell charge-discharge, positive ions such as lithium cations in the electrolyte adsorb on one electrode while the negative ions, anions such as (PF6)− adsorb on the other electrode. The fundamental process is adsorption and desorption, which enables the faster rate of charging and discharging. Supercapacitors utilize the hybridization of electric double layer capacitance with redox capacitance, where the composite electrode material is prepared to consist of porous carbon and fine metal particles. Hybridcapacitors (or asymmetric supercapacitors) are proposed to get high capacitance and high energy density using different material at the two electrodes, anode and cathode, such as graphitized carbon at the anode and activated carbon at the cathode, where the intercalation/de-intercalation of Li+ at the anode and the formation of electric double layers at the cathode are intended to occur.
In the lithium-ion battery cell, the negative electrode (anode) releases lithium ions (de-intercalates lithium ions) during discharging of the cell, and the positive electrode absorbs lithium ions. The negative electrode releases electrons to the external circuit and the positive electrode receives them. The reverse electrochemical process occurs when the battery is charged. The close proximity of the separate capacitor and lithium-ion battery cell structures simplifies electrical connections and facilitates their interaction in providing electrical energy to nearby electrical loads.
In such hybrid applications, the outline shapes of the respective current collectors, porous electrode material layers, and porous separators may be similar and complementary so as to suggest the simultaneous manufacture of both the capacitor electrodes and the battery electrodes and their interrelated functions. The manufacturing process of this invention is particularly useful in making hybrid combinations of a lithium-using capacitor and lithium-ion battery cell.
In accordance with practices of this invention, atmospheric plasma spray devices and methods are used to form the porous particulate electrodes of both a capacitor and a lithium-ion cell. The plasma-spray methods of forming porous layered electrodes of the capacitor are comparable and compatible with plasma-spray methods that may be used for forming the porous layered electrodes of a lithium-ion battery. In some preferred embodiments of this invention, the electrodes and separator for a capacitor and the electrodes and separator for a lithium-ion cell may be prepared contemporaneously, but separately, and a capacitor and a lithium-ion cell may be placed, spaced-apart, in a suitable pouch module or other container and the porous electrodes and separators infiltrated with a lithium-ion transporting, non-aqueous, liquid electrolyte.
In an illustrative example, each member of the capacitor and battery may be prepared in a rectangular shape of suitable predetermined dimensions for assembly of the complementary, hybridized members in operating units. Pre-formed current collector foils for each of the positive and negative electrodes of the capacitor and battery may serve as substrates for the plasma deposition of porous layers of the respective electrode materials. Such current collector foils are typically flat and are sized with opposing rectangular surfaces (faces) of suitable area for the deposit of a suitable layer of selected electrode material on each side (major face) of the foil. The foil may have an uncoated tab extending from one side for electrical connection of the electrode material with other electrodes or with an electrical circuit.
In another embodiment of the invention, a porous polymer separator may serve as a substrate for the plasma deposition of particulate electrode material. A layer of positive capacitor electrode material may be deposited by plasma deposition on one side of a suitably sized, rectangular porous separator and a porous layer of negative capacitor electrode material is deposited by plasma deposition on the other side of the separator. In each embodiment, the deposited electrode material and its substrate are assembled with other members of the capacitor structure. A complementary lithium battery may be made using a like process.
Atmospheric plasma spray devices are commercially available, and practices for their use in the deposition of capacitor electrode materials and battery electrode materials will be described and illustrated in more detail below. The deposition process will be initially described with reference to a capacitor. But substantially the same practices may be used to make the members of the battery.
In summary, a quantity of small particles of electrode material is prepared. Suitable portions are continually introduced into a confined stream of unheated air (or other suitable carrier gas) flowing in a suitable duct or housing. The confined air stream is directed through a plasma generator, within the housing, in which the stream-borne particles are momentarily, rapidly heated. The energized stream of electrode material particles is passed through a suitable nozzle and directed so as to progressively form an adherent, porous, particulate coating on a major surface of a current collector foil or on a major surface of a separator. A porous layer of the particles is formed having a generally predetermined uniform thickness. The thickness of the electrode material layer for the capacitor, which is often in the range of about 100-200 micrometers, is determined to provide a porous electrode layer for infiltration with a lithium-ion conducting electrolyte, to provide suitable lithium ion transporting properties for the capacitor.
Examples of suitable anode materials for the capacitor include graphite, activated carbon, and lithium-titanium containing oxides and phosphates. Examples of suitable cathode materials include certain lithium-metal oxides and phosphates, activated carbon, graphite, and additional materials which will be identified below in this specification. It may also be helpful to coat some of the respective electrode material particles with small metal particles (or other binder materials) which are at least partially melted or softened in the plasma and serve to bond the electrode material particles to each other and to their current collector or separator substrate.
After the electrode materials for the capacitor have been suitably deposited on and bonded in a porous layer to their current collector foils or separators, the assembly of the elements for formation of a layered capacitor is completed for placement in a suitable pouch or other module container. Both the capacitor and the lithium-ion battery may have several layers of electrodes (with interspersed porous separators) with their respective current collectors. The current collectors are suitably connected so that the capacitor and lithium-ion battery each have two terminals. In preferred embodiments of the invention, an assembly of like-sized elements of both the capacitor member and the lithium-ion cell member are placed in the pouch, but the capacitor is separated from the battery cell. The pores of the electrode members of the capacitor and the lithium-ion cell, and their respective separators, are infiltrated with a common lithium ion transporting, non-aqueous lithium electrolyte solution.
Other aspects and features of our invention will be further understood following a more detailed description of illustrated examples of forming electrodes for capacitors which are to be used in combination with a lithium-ion cell or group of cells.
In
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In accordance with practices of this invention, hybrid electrochemical capacitors are prepared, consisting of a capacitor and a lithium-ion battery which are fabricated by plasma powder electrode coating technology, delivering a balanced energy-power performance. Both the capacitor and the battery will adsorb or intercalate lithium ions and both the capacitor and battery will be combined in a common pouch or other suitable container. Accordingly, electrode members for both the capacitor and the battery may be prepared using atmospheric plasma spray devices or like plasma deposition devices. As stated, a uniform layer of particulate electrode material may be deposited over a selected surface area of a metal foil current collector or over a selected surface area of a porous separator member. The formation of electrode layers on current collectors and separator surfaces may be conducted in sequential or complementary steps to accommodate the assembly of positive and negative electrodes on opposite sides of a compatible separator. The positive electrode-separator-negative electrode structures for a capacitor and a lithium-ion cell may thus be prepared separately, but contemporaneously, for assembly into a pouch and infiltration with a common volume of a non-aqueous, lithium-ion conducting electrolyte.
In accordance with practices of this invention, it is intended that selected electrode materials, for both the electrochemical capacitor positive and negative electrodes be prepared in the form of micrometer size particles for deposition on a selected substrate. The selected electrode material compositions are deposited on compatible metal current collector foils, or on a sheet of porous separator material, using one or more atmospheric plasma spray devices. The particles of electrode materials, prepared for the plasma deposition, may have been coated with smaller particles of a metal or of other suitable binder material. Electrode materials for the lithium-ion cell are likewise separately prepared and plasma deposited on selected cell substrates for assembly into lithium-ion cells and placement with a compatible lithium-ion absorbing capacitor in a container.
Suitable materials for plasma deposition as cathode (positive electrode) particles for the capacitor include:
Metal oxides, MOx, where M is one or more of Pb, Ge, Co, Ni, Cu, Fe, Mn, Ru, Rh, Pd, Cr, Mo, W, and Nb.
A lithium-metal-oxide including: LixMO2 in which M is Co, Ni, Mn, Cr, or V.
LixM2O4 , in which M is Co, Ni, Mn, Cr, or V.
LixNiyM1-yO2, in which m is Fe or Mn.
LiNi1-x-y-zCoxM1yM2zO2, in which M1, M2 are different metals selected from Al, Ni, Co, Fe, Mn, V, Cr, Ti, W, Ta, or Mo.
LiMn2-xMxO4 in which M is one of Co, Ni, Fe, Cu, Cr, V.
One of LiNiVO4, LiNbO3, LiFePO4, LiTi2(PO4)3, or Li3V2(PO4)3.
LiMPO4 in which M is one of Ti, Ge, Zr, Hf.
One or more of Li3FeV(PO4)3, LiFeNb(PO4)3, Li2FeNb(PO4)3, LixFeyMn1-yPO4, LiMSiO4 (M=Mn, Fe), LixFe2(WO4)3, LixFe2(SO4)3, and LiFeO2.
A metal sulfide: NiS, Ag4Hf3S8, CuS, FeS, and FeS2.
Activated carbon.
A polymer such as: poly (3-methyl thiophene), polyaniline, polypyrrole, poly (para-phenylene), or polyacene.
As further described in this specification, cathode particles for the capacitor are usually plasma-deposited on an aluminum current collector foil or on a porous polymer separator.
Suitable materials for plasma deposition as anode (negative electrode) particles for the capacitor include:
Li4Ti5O12, LiTi2O4, LiCrTiO4, LiTi2(PO4)3, and graphite or activated carbon.
Positive electrode material for the capacitor is preferably plasma deposited on an aluminum current collector foil or on a polymeric separator such as a porous layer of polyethylene, polypropylene, or an ethylene-propylene copolymer.
After the assembling of electrodes and separator and filling their pores with the electrolyte, the hybrid capacitor and battery undergo a formation cycle and are then degassed. The plasma powder coating method can optimize the surface area of the material layers coated on the foil or the separator, and can also control the porosity of the respective electrodes, in order to improve both the energy and power performance of the hybrid capacitor-battery.
Recently, a lithium and titanium containing spinel structure, Li4Ti5O12, listed above, has been demonstrated as a promising negative electrode material for use in combination with activated carbon as the positive electrode material for hybrid capacitor applications. Accordingly, the power density depends on the rate capability of the intercalated compound Li4Ti5O12, which is associated with the Li-ion diffusion coefficient and the diffusion distance in the intercalated compound particle. To obtain a high rate capability, plasma powder electrode coating technology can be introduced to develop a nanosize-Li4Ti5O12 electrode with well controlled porosity, in which conductive metal particle and no polymer binder will benefit the rate performance. In addition, the energy density of the capacitor is critically dependent on the energy density of the carbon positive electrode material. Plasma powder electrode coating technology can be used to enlarge the surface area of carbon material in the electrode by size and porosity optimization to improve the specific capacity.
The lithium-ion cell component of this capacitor-cell combination may be formed of like current collector foils and like porous separator materials.
Examples of suitable particulate materials for positive electrodes for lithium-ion cells include lithium manganese nickel cobalt oxide, lithium manganese oxide, lithium cobalt oxide, lithium nickel aluminum cobalt oxide, lithium iron phosphate, and other lithium oxides and phosphates. Examples of particulate negative electrode materials for lithium-ion cells include lithium titanate, graphite, activated carbon, and silicon-based materials such as silicon, silicon-based alloys, SiOx, silicon-tin composites, and lithium-silicon alloys.
The common electrolyte for the capacitor cell and the lithium-ion cell may be a lithium salt dissolved in one or more organic liquid solvents. Examples of salts include lithium hexafluorophosphate (LiPF6), lithium tetrafluoroborate (LiBF4), lithium perchlorate (LiClO4), lithium hexafluoroarsenate (LiAsF6), and lithium trifluoroethanesulfonimide. Some examples of solvents that may be used to dissolve the electrolyte salt include ethylene carbonate, dimethyl carbonate, methylethyl carbonate, and propylene carbonate. There are other lithium salts that may be used and other solvents. But a combination of lithium salt and non-aqueous liquid solvent is selected for providing suitable mobility and transport of lithium ions between the opposing electrodes in the operation of the cell. The electrolyte is carefully dispersed into and between closely spaced layers of the electrode elements and separator layers of each of the capacitor cell and the battery cell. The electrolyte is not illustrated in the following drawing figures because it is difficult to illustrate the electrolyte between tightly compacted electrode layers pressing on an interposed separator.
A thin porous separator layer is interposed between the major outer face of the negative electrode material layer and the major outer face of the positive electrode material layer of each of the capacitor and the battery unit. The porous separator may be formed of a porous film or of porous interwoven fibers of suitable polymer material, or of ceramic particles, or a polymer material filled with ceramic particles. In the assembly of the hybrid capacitor and separated lithium-ion cell units, the porous separator layer is filled with a liquid lithium-ion containing electrolyte and enables the transport of lithium ions between the porous electrode members. But the separator layer is used to prevent direct electrical contact between each of the negative and positive electrode material layers in each unit, and is shaped and sized to serve this function.
As stated above in this specification, in actual practice each capacitor will be formed of several layers of positive electrodes, negative electrodes, and separators, prepared as described in the following paragraphs. The like-charged electrode layers are connected by tabs on their current collectors, respectively, in a positive terminal and a negative terminal for the capacitor. The positive and negative tabs for the groups of positive and negative capacitor electrodes may be connected with other devices in an electrical circuit as desired. Lithium-ion batteries are also typically formed of many positive electrodes connected to a positive terminal and many negative electrodes connected to a negative terminal. But since the focus of this specification is on the use of plasma deposition methods and devices to make such electrodes and separators, the illustrations of
The illustrated electrochemical, capacitor 12 comprises a positive electrode, which in this example comprises a rectangular aluminum foil current collector 18 with a connector tab 18′ extending from its top side and through the overlapping surface of pouch 16. The positive electrode of the capacitor further comprises porous particulate layers of electrode material 20 which have been deposited by atmospheric plasma deposition on each face of the aluminum foil current collector 18. The positive electrode material for the capacitor may, for example, be activated carbon. The thickness of the current collector foil 18 may be, for example, about ten micrometers and the lengths of the sides of the foil may, for example be in the range of 75 mm to 100 mm, not including the tab 18′. The porous layers of electrode material 20 may, for example, be about 10 to 500 micrometers in thickness and applied to substantially cover the rectangular faces of current collector foil 18, but not tab 18′.
The electrochemical capacitor 12 further comprises a negative electrode, which in this example comprises a rectangular copper foil current collector 22 with a connector tab 22′ extending from its top side and through the overlying surface of pouch 16. The negative electrode of the capacitor further comprises porous particulate layers of electrode material 24 which have also been deposited by atmospheric plasma deposition on each face of the copper foil current collector 22, but not on tab 22′. The negative electrode material for the capacitor may, for example, also be activated carbon. The side lengths and thickness of the copper current collector foil 22 are suitably like the dimensions of the positive electrode current collector foil. The porous layers of negative electrode material 24 may, for example, be of complementary thickness to that of the positive electrode materials and applied to substantially cover the rectangular faces of current collector foil 22, but not tab 22′.
As illustrated in
The liquid electrolyte is not illustrated in
The structure of the lithium-ion cell or battery 14 is similar to that of capacitor 12 and the outline sizes and thickness of the respective current collector foils, electrode material layers and separator of battery 14 are comparable to the similar structural elements of capacitor 12. But the electrode materials may be different and the electrochemical reactions are different.
In this example and simplified illustration, batteryl4 includes an aluminum positive electrode current collector foil 30 with a connector tab 30′ extending through the overlying pouch material 16. Plasma deposited positive electrode layers 32 (e.g., activated carbon) are formed on both major faces of the aluminum current collector foil 30. The positive electrode material 32 for the battery 14 may, for example, be particles of LiFePO4. A copper negative current collector foil 34 with tab 34′ is plasma coated on both of its major faces with layers of negative electrode material 36. The particle layers of negative electrode material 36 may comprise activated carbon or resin-bonded activated carbon. The facing porous layers of positive electrode material 32 and of negative electrode material 36 are kept apart by porous polymer separator 38. In the assembled battery 14, placed in pouch 16, the pores of separator 38 and of electrode layers 32 and 36 are filled with a suitable non-aqueous, lithium-ion conducting electrolyte. The electrolyte may, for example, comprise lithium hexafluorophosphate (LiPF6) dissolved in a mixture of dimethyl carbonate and methylethyl carbonate as solvent.
In
In this example and illustration, the electrodes and separator of capacitor 112 may be substantially identical in shapes and compositions with respect to the corresponding elements of capacitor 12 as shown in
The main difference between
Thus, in the parallel connection arrangement of the electrodes of capacitor 112 and battery 114, the two components may be designed to operate in a common voltage window and to achieve a higher power in their common voltage range.
In this example, the current collector foil 18 is placed and carried on a movable work surface 202, such as a conveyor belt, or the like, for locating the current collector foil 18, with its upper surface 17, under the plasma application device. This process may be conducted in air and in a normal ambient workplace atmosphere.
In this example, the copper current collector foil 18 is illustrated in the form of a thin, square layer of about 100 millimeters length on each side, but the capacitor elements are also often made in other rectangular shapes and dimensions depending on the intended size of the capacitor elements and assembled capacitor modules. The copper current collector foil layer 18 is often about ten to twelve micrometers in thickness. The substrate 202 is moved and placed in a flat position at ambient conditions under a suitable atmospheric plasma spray generator apparatus 200 with a nozzle for directing its flow stream of electrode material particles. The spray device(s) and/or workpiece may be carried on a suitable support and moved under suitable programmable controls for sequential deposition of particulate electrode material on the surface 17 of one or more copper current collectors 18.
In practices of this invention, and with reference to
In this example, the stream 216 of air-based plasma and suspended, plasma-activated, activated carbon electrode material particles is progressively directed by the nozzle 214 to deposit particles as a layer of electrode material 20 onto the surface of the upper surface 17 of the copper foil current collector 18. The nozzle 214 and stream 216 of suspended electrode material is moved in a suitable path and at a suitable rate such that the particulate activated carbon electrode material 208 is deposited as a porous layer 20 of specified thickness of the electrode particles on the surface 17 of the current collector foil 18.
The relative movement of the plasma spray stream 216 and/or the substrate 202 is continues until the entire face 17 of current collector foil 18 (but not tab 18′) is covered with a generally uniformly thick layer of capacitor positive electrode material 20. The current collector foil may then be turned over so that its opposing face is likewise coated with a layer of positive electrode material 20.
The above described plasma spray deposition device and method may be used to deposit porous layers of particulate negative capacitor electrode material on a suitable metal foil current collector material. For example,
In the above described process, both the positive electrode and the negative electrode for a capacitor cell were prepared by plasma deposition of particles of the electrode material onto both sides of a suitable metal current collector. The assembly of the capacitor elements is then advanced by placing one face of positive electrode material against one side of a porous separator and one face of a negative electrode material against the opposite face of the separator. The assembled capacitor is illustrated in
When capacitor 12 has been assembled with a like-shaped and like- made battery (e.g., battery 14) in a suitable container, like pouch 16, both the capacitor and battery will be suitably infiltrated with a shared lithium-ion transporting electrolyte.
In the above described plasma application process, particulate cathode material was plasma coated on both sides of an aluminum current collector foil to form a capacitor cathode, and particulate anode material was plasma coated onto both sides of a copper current collector foil to form a capacitor anode. The assembly of the capacitor cell was then completed by placing a cathode on one side of a suitable porous separator and a cathode on the other side of the separator. A like plasma deposition process, using suitable electrode materials, may be used to make and assemble a lithium-ion battery cell for the hybrid combination.
In a second plasma deposition process, similar to that illustrated in
As stated, either plasma deposition process, using appropriate particulate electrode materials and current collector material may be used to make the electrochemical cell structures of either a lithium-ion using capacitor or a lithium-ion battery. The plasma deposition process can be conducted, for example, in parallel or other complementary manufacturing lines to simultaneously produce complementary capacitors and batteries for assembly into suitable containers for hybrid combination. The porous elements of the combined assembly are then infiltrated or impregnated with a suitable lithium ion containing electrolyte. And capacitor and battery members of the combination may be charged or otherwise prepared for their respective electrochemical functions.
As stated, the layers of the respective electrode material particles is pre-deposited on a compatible current collector surface or a compatible separator surface using one or more atmospheric plasma nozzles or deposition devices. Such plasma nozzles for this application are commercially available and may also be carried and used on robot arms, under multi-directional computer control, to apply suitable electrode particles to coat the surfaces of each metal current collector foil or separator surface for a lithium-using capacitor and, separately, for a lithium-ion cell. Multiple nozzles may be required and arranged in such a way that a desired coating speed may be achieved in terms coated area per unit of time.
The atmospheric plasma nozzle typically has a metallic tubular housing which provides a flow path of suitable length for receiving the flow of working gas, receiving and dispersing particles of electrode material, and for enabling the formation of the plasma stream in an electromagnetic field established within the flow path of the tubular housing. The tubular housing terminates in a conically tapered outlet, shaped to direct a suitably shaped plasma stream toward an intended substrate to be coated. An electrically insulating ceramic tube is typically inserted at the inlet of the tubular housing such that it extends along a portion of the flow passage. A stream of a working gas, such as air (or nitrogen or argon), and carrying dispersed particles of a specified electrode material, is introduced into the inlet of the nozzle. The flow of the air-particle mixture may be caused to swirl turbulently in its flow path by use of a swirl piece with flow openings, also inserted near the inlet end of the nozzle. A linear (pin-like) electrode is placed at the ceramic tube site, along the flow axis of the nozzle at the upstream end of the flow tube. During plasma generation the electrode is powered by a suitable generator at a frequency in the 0.1 hertz to gigahertz range and to a suitable potential of a few kilovolts. Plasma generation technology such as corona discharge, radio wave, and microwave sources, and the like, may be employed. The metallic housing of the plasma nozzle is grounded. Thus, an electrical discharge can be generated between the axial pin electrode and the housing. No vacuum chamber is used.
When the generator voltage is applied, the frequency of the applied voltage and the dielectric properties of the ceramic tube produce a corona discharge at the stream inlet and the electrode. As a result of the corona discharge, an arc discharge from the electrode tip to the housing is formed. This arc discharge is carried by the turbulent flow of the air/particulate electrode material stream to the outlet of the nozzle. A reactive plasma of the air (or other carrier gas) and dispersed electrode particles is formed at a relatively low temperature. A copper nozzle at the outlet of the plasma container is shaped to direct the plasma stream in a suitably confined path against the surfaces of the current collector substrates for the lithium-ion cell electrode members. The energy of the plasma may be determined and managed for the material to be applied.
Thus, specific examples have been presented for the use of plasma spray deposition devices and methods in the preparation of lithium-ion incorporating capacitors and batteries for assembly into a common container to serve as hybrid electrochemical devices for provision of electrical power in many devices consuming electrical energy. The examples are intended to illustrate practices of the invention and not the scope of the following claims.
Filing Document | Filing Date | Country | Kind |
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PCT/CN2015/075046 | 3/25/2015 | WO | 00 |