1. Field of the Invention
Embodiments of the present invention relate generally to high-capacity energy storage devices and methods and apparatus for fabricating high-capacity energy storage devices. More specifically, methods and apparatus for material spray deposition of high solid percentage slurries for forming battery active materials are disclosed.
2. Description of the Related Art
High-capacity energy storage devices, such as lithium-ion (Li-ion) batteries, are used in a growing number of applications, including portable electronics, medical devices, transportation, grid-connected large energy storage, renewable energy storage, and uninterruptible power supplies (UPS).
Li-ion batteries typically include an anode electrode, a cathode electrode and a separator positioned between the anode electrode and the cathode electrode. Lithium is stored in the active materials in the electrodes. The active electrode material in the positive electrode of a Li-ion battery is typically selected from lithium transition metal oxides, such as LiMn2O4, LiCoO2, LiFePO4, LiNiO2, or combinations of Ni, Li, Mn, and Co oxides and includes electroconductive particles, such as carbon or graphite, and binder material. Graphite and MCMB (meso carbon micro beads) are usually used as the active electrode material of the negative electrode having a mean diameter of approximately 10 μm. The lithium-intercalation MCMB or graphite powder is dispersed in a polymeric binder matrix. The typical polymers for the binder matrix include PVDF (Polyvinylidene fluoride), SBR (Styrene-Butadiene Rubber), CMC (Carboxymethyl cellulose). The polymeric binder serves to bind together the active material powders to preclude crack formation and prevent disintegration of the active material powder on the surface of the current collector, as well as for good adhesion to the substrate. The quantity of polymeric binder may be in the range of 2% to 30% by weight. The separator of Li-ion batteries is typically made from microporous polyolefin polymer, such as polyethylene foam, and is applied in a separate manufacturing step.
For most energy storage applications, the charge time and capacity of energy storage devices are important parameters. In addition, the size, weight, and/or expense of such energy storage devices can be significant limitations.
One method for manufacturing anode electrodes and cathode of electrodes for energy storage devices is principally based on slit coating of viscous solvent-based powder slurry mixtures of cathodically or anodically active material onto a conductive current collector followed by prolonged heating to form a dried cast sheet. A slow drying process is needed in order to prevent cracking in thick coatings and as a result, the length of the dryers needed are very long. The thickness of the electrode after drying which evaporates the solvents is finally determined by compression or calendering which adjusts the density and porosity of the final layer. Slit coating of viscous slurries is a highly developed manufacturing technology which is very dependent on the formulation, formation, and homogenation of the slurry. The formed active layer is extremely sensitive to the rate and thermal details of the drying process.
Among other problems and limitations of this technology is the slow and costly drying component which requires both a large footprint (e.g., up to 70 to 90 meters long) at coating speeds 5-40 meters/min, and an elaborate collection and recycling system for the evaporated volatile components. Many of these are volatile organic compounds which additionally require an elaborate abatement system. Further, the resulting electrical conductivity of these types of electrodes also limits the thickness of the electrode and thus the energy density of the battery cells.
Accordingly, there is a need in the art for high volume, cost effective manufacturing processes and apparatus for manufacturing high-capacity energy storage devices.
Embodiments described herein include a material spray deposition system including at least a substrate conveyor system and a electrode forming solution dispenser. In one embodiment, an apparatus for depositing a battery active material on a surface of a substrate includes a substrate conveyor system, a material spray assembly disposed above the substrate conveyor system, and a first heating element disposed adjacent to the material spray assembly above the substrate conveyor system.
In another embodiment, the spray deposition is electrospray.
In another embodiment, a material electrospray assembly used in an apparatus for depositing a battery active material on a surface of a substrate includes a manifold having a plurality of nozzles formed therein, at least one dummy nozzle formed in the plurality of nozzles formed in the manifold, and an extractor plate coupled to the manifold, wherein the extractor plate further comprises a plurality of apertures formed in the extractor plate aligning with the nozzles formed in the manifold.
In yet another embodiment, a method for depositing a battery active material on a surface of a substrate includes depositing battery active materials from a material electrospray dispenser assembly onto a substrate disposed in a substrate conveyor system; and heating the deposition materials disposed on the substrate by a plurality of heaters disposed above the substrate conveyor system adjacent to the material electrospray dispenser assembly. The substrate may be in web form continuous supplied in the substrate conveyor system, or be one of a plurality of discrete substrates moving through the substrate conveyor system.
In another embodiment, a tip of the nozzle is coated with hydrophobic coating.
So that the manner in which the above-recited features of the present invention can be understood in detail, a more particular description of the invention, briefly summarized above, may be had by reference to embodiments, some of which are illustrated in the appended drawings. It is to be noted, however, that the appended drawings illustrate only typical embodiments of this invention and are therefore not to be considered limiting of its scope, for the invention may admit to other equally effective embodiments.
To facilitate understanding, identical reference numerals have been used, where possible, to designate identical elements that are common to the figures. It is contemplated that elements disclosed in one embodiment may be beneficially utilized on other embodiments without specific recitation.
The methods and apparatus described herein include a material spray deposition system including at least a substrate conveyor system and a material deposition spray assembly disposed adjacent the substrate conveyor system. The material spray assembly includes nozzles configured to deposit material having good center to edge thickness uniformity, good homogeneity through the film thickness, and to enable rapid deposition rates. The material spray deposition system is particularly useful in depositing material layer(s) utilized for electrode structures, such as battery active material layers, from high solid content electrode forming solutions.
The substrate conveyor system 101 includes a supply roll 108, at least one conveying roller 106, and optionally, a take-up roll 111. The conveying roller may optionally be heated to assist drying deposition materials on the substrate 102. The supply roll 108 that contains at least a portion of substrate 102 wound on a core 109. The substrate 102 is fed from the supply roll 108 across to the conveying roller 106 to expose the deposition surface 104 of the substrate 102 adjacent the material electrospray dispenser assembly 110. The substrate 102 may be spliced to itself to form a continuous web so that a given region of the substrate 102 may be passed under the material electrospray dispenser assembly 110 multiple times until a desired thickness of material has been deposited on the substrate 102. Alternatively, the substrate 102 may be routed from the supply roll 108 and passed under the material electrospray dispenser assembly 110 a single time prior to collecting on the take-up roll 111, as shown in phantom.
The supply roll 108 is removable from the substrate conveyor system 101 to facilitate loading another supply roll containing substrate materials for processing when needed. The supply roll 108 may be replaced once deposition materials with desired thickness are formed on the substrate 102. After processing, the substrate 102 may be rewound on the supply roll 108 for removal from the substrate conveyor system 101, if a separate take-up roll 111 is not utilized.
The material electrospray dispenser assembly 110 is utilized to spray deposit deposition materials on the substrate 102, for example, using an electrospray process. The deposition materials deposited on the substrate 102 may be a battery-active material layer. More specifically in the embodiment depicted in
In the embodiment depicted in
In one embodiment, the heater 114 may provide light radiation to heat the substrate 102. The light radiation from the heater 114 (i.e., thermal energy) may be used to control the temperature of the substrate 102 to between about 10 degrees Celsius and about 250 degrees Celsius.
An air knife 170 may be disposed at a position adjacent to the supply roll 108 to assist blowing off contaminants or residuals present on the substrate 102 before being taken up by the take-up roll 111 or passing again below material electrospray dispenser assembly 110 for subsequent deposition of additional deposited material. The air knife 170 may provide air or other gas at a predetermined flow rate as needed to substrate surface passing thereby to blow off contaminant or residuals from the substrate 102. The air provided by the air knife 170 may optionally be heated, for example, to between about 10 degrees Celsius and about 250 degrees Celsius, to further assist in drying the deposited material disposed on the substrate 102.
Additionally, the use of multiple material electrospray dispenser assemblies 120, each depositing a thin layer, permits each thin layer to be thoroughly dried prior to deposition of the next thin layer. The resulting thicker layer of deposited material has a uniform composition therethrough because volatiles cannot become trapped in the center of the deposition material, which sometimes is the case in bulk or other rapidly deposited layers. Moreover, as the thin layer dry quickly, the thickness of the deposited material may be built up more rapidly than thickly deposited layers which require substantial time to allow for volatiles to be evaporated completely from the film. Accordingly, the material spray deposition system 119 with multiple material electrospray dispenser assemblies 120 allows for increased deposition throughput and efficiency. It is noted that the number of the material electrospray dispenser assemblies 120 utilized in the material spray deposition system 119 may vary as needed to facilitate deposition efficiency and performance.
A first plurality of heaters 124a, 124b may be disposed adjacent to the material electrospray dispenser assemblies 120 above the substrate 102 to assist drying the electrode forming solution 112 sprayed onto the substrate 102. In the embodiment depicted in
The substrate 102 is sequentially routed through each of the conveying rollers 158a, 159a, 158b, 158c, 159b, 158d, creating a tortuous (i.e., serpentine) path through the vertical path 162 and the horizontal path 164, thereby extending the total length of time the substrate 102 travels through the system 185. The tortuous path created by the substrate conveyor system 152 may provide increased locations for positioning additional material electrospray dispenser assemblies 120, thereby improving the deposition efficiency without increasing footprint of the substrate conveyor system 103, and desirably reducing the cost of manufacture.
The electrode forming solution 112 supplied from the deposition material source 280 may comprise an electro-active material and an electro-conductive material. The electro-active material and the electro-conductive material may be in a water-based solution. The electrode forming solution 112 may also include a solvent, such as N-Methylpyrollidone (NMP), or other suitable solvent or water. The electrode forming solution 112 may optionally include at least one of a binding agent and a drying agent. The electrode forming solution 112 may have a baseline conductivity of at least about 10−5 Siemens/meter.
Exemplary electro-active materials which may be deposited using the embodiments described herein include but are not limited to cathodically active particles selected from the group comprising lithium cobalt dioxide (LiCoO2), lithium manganese dioxide (LiMnO2), titanium disulfide (TiS2), LiNixCo1-2xMnO2, LiMn2O4, iron olivine (LiFePO4) and it is variants (such as LiFe1-xMgPO4), LiMoPO4, LiCoPO4, Li3V2(PO4)3, LiVOPO4, LiMP2O7, LiFe1.5P2O7, LiVPO4F, LiAlPO4F, Li5V(PO4)2F2, Li5Cr(PO4)2F2, Li2CoPO4F, Li2NiPO4F, Na5V2(PO4)2F3, Li2FeSiO4, Li2MnSiO4, Li2VOSiO4, other qualified powders, composites thereof and combinations thereof.
Other exemplary electro-active materials which may be deposited using the embodiments described herein include but are not limited to anodically active particles selected from the group comprising graphite, graphene hard carbon, carbon black, carbon coated silicon, tin particles, copper-tin particles, tin oxide, silicon carbide, silicon (amorphous or crystalline), silicon alloys, doped silicon, lithium titanate, any other appropriately electro-active powder, composites thereof and combinations thereof.
Exemplary drying agents include, but are not limited to, isopropyl alcohol, methanol, and acetone. Exemplary binding agents include, but are not limited to, polyvinylidene difluoride (PVDF) and water-soluble binding agents, such as styrene butadiene rubber (SBR) and sodium carboxymethyl cellulose (CMC). Exemplary electro-conductive materials include, but are not limited to, carbon black (“CB”) and acetylene black (“AB”).
The electrode forming solution may have a solids content greater than 30 percent by weight (wt. %), such as between about 30 wt. % and about 85 wt. %. In one embodiment, the electrode forming solution may have a solids content of between about 40 wt. % and about 70 wt. %, such as between about 50 wt. % and about 60 wt. %.
Conventionally, electrospray technology is limited for use with solid-free liquids or liquids containing particles less than 1 micrometer. The embodiments described herein enables electrospraying of solutions having much larger particle sizes. The solids within the electrode forming solution generally have a particle size larger than conventional depositions systems, thereby allowing higher deposition rates. For example, solid particles within the electrode forming solution may have a mean diameter in the range of between about 1.0 μm to about 20.0 μm, such as between about 3.0 μm to about 15.0 μm. The solids present in the electrode forming solution comprise at least one or both of active material and conductive material. The only known technology which can utilized such large particle size for battery active material deposition are slit coating systems which are as discussed above, suffer from long drying times and film cracking, and additionally suffer from poor thickness uniformity control, making slit coating systems undesirable for next generation battery devices. As described herein, the material electrospray dispenser assembly 200 enables rapid deposition of high solid content battery active materials with good uniformity control in a system having a cost effective, smaller footprint with no film cracking problems, thereby enhancing development and fabrication of next generation battery devices.
An optional extractor plate 206 having a plurality of apertures 208 may be formed therein aligning with the nozzles 204 extending in the manifold 202. The extractor plate 206 may have an upper surface 212 facing the manifold 202 and a lower surface 210 facing the substrate 102. The upper surface 212 of the extractor plate 206 may be parallel to the lower surface 214 of the manifold 202. The extractor plate 206 may be coupled to the manifold 202 using suitable mechanical attachments, such as screws or bolts, adhesive materials or any other suitable attachment techniques. The plurality of apertures 208 in the extractor plate 206 may reactively align with the nozzles 204 coupled to the manifold 202 so as to facilitate and confine flow of the deposition materials from the deposition material source 280 to the substrate 102. In one embodiment, the lower surface 214 of the manifold 202 may have a distance 250 between about 5 mm and about 55 mm to the upper surface 212 of the extractor plate 206. The nozzle 204 may have distance 252 between about 10 mm and about 50 mm to the upper surface 212 of the extractor plate 206.
In one embodiment, the apertures 208 formed in the extractor plate 206 may have a predetermined size to accommodate the flow volume of the deposition material supplied from the nozzles 204. Different sizes of the nozzle 204 may result in different flux of the deposition materials flowing therethrough passing the apertures 208 of the extractor plate 206 to the substrate surface. In one embodiment, the diameter of the apertures 208 may be selected between about 0.3 mm and about 5 mm.
The plurality of nozzles 204 coupled to the manifold 202 may have different configurations, shape, features, and numbers to meet different process requirements. The nozzles 204 and the apertures 208 formed in the extractor plate 206 may collectively form a material path that allows deposition material from the material source 280 to pass therethrough to the substrate 102. In the embodiment depicted in
A first circuit arrangement 232 couples to the material electrospray dispenser assembly 200 to a power source 270. The first circuit arrangement 232 is adapted to provide power to the material electrospray dispenser assembly 200. In operation, the manifold 202 and the extractor plate 206 may each act as an electrode. A first voltage V1 may be applied to the manifold 202 and the extractor plate 206, establishing a first electric field that atomizes deposition materials passing therethrough. In one embodiment, the first voltage V1 may be between about 5 KVolts and about 50 KVolts. A second circuit arrangement 234 is coupled between the material electrospray dispenser assembly 200 and the substrate 102. As the substrate 102 is fabricated from a metallic material, such as an aluminum foil, the substrate 102 may also act as an electrode during operation. Similarly, a second voltage V2 may be applied to the substrate 102 and the extractor plate 206, establishing a second electric field to enable acceleration the atomized electrode forming solutions passing through the apertures 208 in the extractor plate 206 on to the substrate 102. The second voltage V2 may be between 5 KVolts and about 50 KVolts. The substrate 102 may coupled to ground 230, for example, through one of the rollers 106. The second voltage V2 may be greater than the first voltage V1, for example by about 5 KVolts.
In one embodiment, the plurality of the nozzles 204 coupled to the manifold 202 may have an arrangement selected so as to assist deposition materials (i.e., electrode forming solution 112) provided from the deposition material source 280 to be evenly distributed on the substrate 102. In one embodiment, dummy nozzles 218, fabricated from an electrically conductive material, for example a metal such as stainless steel, may be disposed at edges of the manifold 202 to reduce tilting of the spray exiting the outermost nozzles 204 due to an imbalance in the electric field at the last nozzle 204. In some cases, deposition materials supplied through the outermost nozzles 204 disposed at the edges of the manifold 202 may have a tilted spray trajectory compared to the spray trajectory of the inner nozzles 204, thereby adversely impacting the film uniformity at the edge of the substrate 102. In embodiments employing dummy nozzles 218 disposed around ends of the manifold 202 outward of the last nozzle 204, a voltage may be applied to the dummy nozzle 218 to create an electric field with the extractor plate 206 in the same manner as between the nozzles 204 and the extractor plate 206. Thus, the electric field may be uniformly extended laterally outward of the outer most nozzles 204 so that electric fields acting on the spray exiting the center and outer nozzles 204 are substantially the same, thereby allowing the spray trajectory to be essentially uniform (i.e., vertical) between the outermost and center nozzles 204, and enhancing center to edge deposition uniformity on the substrate 102. Although only one dummy nozzle 218 is shown at each end of the manifold 202, it is noted that the dummy nozzles may be coupled to the manifold 202 at any desirable location.
The arrangement of the nozzles 204 within the material spray dispenser assembly 200 allows for greater flow rates of high solid content electrode forming solution, which in conjunction with the high drying rates facilitated by the material spray deposition system 100 or other system described herein, results in fast deposition of homogeneous battery-active materials with uniform center to edge thickness. For example, each nozzle 204 of the material spray dispenser assembly 200 may deliver about 0.15 ml/min to about 15.0 ml/min of high solid content (i.e., greater than 10 wt. %) electrode forming solution.
In the embodiment depicted in
The arrangement of the nozzles 204 within the material electrospray dispenser assembly 200 allows for greater flow rates of high solid content electrode forming solution, which in conjunction with the high drying rates facilitated by the material spray deposition system 100 or other system described herein, results in fast deposition of homogeneous battery-active materials with uniform center to edge thickness. For example, each nozzle 204 of the material electrospray dispenser assembly 200 may deliver about 0.15 ml/min to about 15.0 ml/min of high solid content (i.e., greater than 10 wt. %) electrode forming solution.
In some embodiments, the flow through the nozzles 204 located in the edge zones 260 may be different, for example greater, than the flow through the nozzles 204 located in the center zone 262. This may be coupled with a less voltage applied to the nozzles 204 located in the edge zones 260 compared to the voltage applied to the nozzles 204 located in the center zone 262, which compensates for tendencies to have faster deposition in the center of the substrate 102, thereby contributing for more uniform edge to center thickness of the deposited battery active material.
In one embodiment, an angled nozzle 406 may be formed at an edge 420 of the center plate 412. It is believed that the angled nozzle 406 may assist directing the deposition material more inward to a center of the substrate 102 so as to reduce the tilting effect of the outermost spray trajectory and thereby improve thickness uniformity of the deposited film formed on the substrate 102. The angled nozzle 406 may be an outermost one of the nozzles coupled to the center plate 412. Alternatively, the angled nozzle 406 may be located in another suitable position in the center plate 412. It is noted that the angled nozzle 406 may also be configured in different configurations, such as cone shape, square shape, oval shape, or other suitable configurations. More details regarding the angled nozzle 406 will be further discussed below with reference to
The deposition material exiting the nozzle 204 may wet and creep up the tip 606 of the nozzle 204, thereby undesirably increasing the diameter of the stream of materials exiting the nozzle, making process control difficult and undesirably increasing potential arcing between nozzles. Selecting a ratio between the first outer diameter 634 and an inside diameter 618 through which the electrode forming solution flows balances the ability to obtain high deposition rates while minimizing the potential for arcing between nozzles. For example, it has been demonstrated that a ratio between the first outer diameter 634 and the inside diameter 618 of 4:1 and 3:1 will provide good deposition results without arcing when nozzles 204 are spaced at distances as close as 12 mm or even 9 mm between nozzle centerlines.
In certain embodiments, the effective diameter of the material exiting from the tip 606 towards the substrate surface may be controlled by a hydrophobic coating applied to an exterior of the tip 306 and/or the body 602 of the nozzle 204 to change (i.e., increase) the contact angle 608 formed between the droplet and the tip 606 of the nozzle 204 and to prevent wetting of the nozzle by the deposition material. In one embodiment, the contact angle 608 may be controlled greater than 20 degrees, such as greater than 30 degrees, for example between about 20 degrees and about 90 degrees. In one embodiment, the hydrophobic coating utilized to coat on the tip 606 may be polytetrafluoroethylene (PTFE), perfluorodecyltrichlorosilane (FDTS) and the like.
It has also been found that fabricating the tip 606 to have a smooth exterior surface will also minimize wetting of the nozzle 204. In one embodiment, the exterior surface of the tip 606 is fabricated to have a surface roughness of about 16 Ra or smoother.
While the foregoing is directed to embodiments of the invention, other and further embodiments of the invention may be devised without departing from the basic scope thereof.
Filing Document | Filing Date | Country | Kind |
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PCT/US14/20410 | 3/4/2014 | WO | 00 |
Number | Date | Country | |
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61786918 | Mar 2013 | US |