This invention relates generally to battery electrodes, and, more specifically, to lithium metal electrodes that can be used safely in batteries that have either solid or liquid electrolytes.
The specific energy achievable in current ion lithium batteries is about 200 Wh/kg, when the weights of the electrodes, electrolyte, current collectors, and packaging are all taken into account. Secondary lithium ion batteries use lithium intercalated graphite anodes predominantly. It is well known that replacing such anodes with simple lithium metal foils can lead to a substantial increase in energy density to values as high as 300 Wh/kg or more. However, manufacturing safe lithium metal batteries in a cost-effective manner has proven to be very difficult.
The development of secondary batteries employing lithium metal as the negative electrode has been plagued with safety problems. As the battery is cycled, lithium that is deposited during charging tends to form dendrites extending out from the negative electrode into the adjacent separator or solid electrolyte. The dendrites can grow through the separator or electrolyte and short out to the positive electrode or they can react with the electrolyte, causing the battery to overheat. The melting point of lithium is 180° C. or lower, depending on the amount of impurities in the lithium, and the dendrites can melt easily. Molten lithium is violently reactive, especially with solvent-based electrolytes. Such reactions are highly exothermic and the heat generated can easily lead to catastrophic or explosive failure of the battery.
What is needed is a way to use lithium metal foils as battery anodes without suffering the drawbacks of volatility and high manufacturing expense.
The foregoing aspects and others will be readily appreciated by the skilled artisan from the following description of illustrative embodiments when read in conjunction with the accompanying drawings. The drawings are schematic only and are not intended to convey any information about the relative or absolute sizes of the various elements shown therein. The figures are not drawn to scale.
The preferred embodiments are illustrated in the context of lithium metal electrodes in batteries. The skilled artisan will readily appreciate, however, that the materials and methods disclosed herein will have application in a number of other electrical devices where lithium metal as an ion source is desirable, particularly where stability and safety are important.
These and other objects and advantages of the present invention will become more fully apparent from the following description taken in conjunction with the accompanying drawings.
In this disclosure, the terms “negative electrode” and “anode” are both used to mean “negative electrode”. Likewise, the terms “positive electrode” and “cathode” are both used to mean “positive electrode”.
It is to be understood that when the terms “lithium metal” or “lithium foil” are used herein with respect to negative electrodes, they are meant to include both pure lithium metal and lithium-rich metal alloys as are known in the art. Examples of lithium rich metal alloys suitable for use as anodes include Li—Al, Li—Si, Li—Sn, Li—Hg, Li—Zn, Li—Pb, Li—C or any other Li-metal alloy suitable for use in lithium metal batteries. Other negative electrode materials that can be used in the embodiments of the invention include materials in which lithium can intercalate, such as graphite. Many embodiments described herein are directed to batteries with solid polymer electrolytes, which serve the functions of both electrolyte and separator. As is well known in the art, batteries with liquid electrolytes use an inactive separator that is distinct from the liquid electrolyte and generally cannot be used safely with lithium metal anodes in secondary batteries.
The thickness of each of the current collectors 120, 140 is generally in a range of about 10-30 μm. Together the current collectors 120, 140 contribute about 10-20% to the overall weight of the battery 100. The thickness of the current collectors 120, 140 is chosen to give the anode film 110 and the cathode film 130 sufficient support. If supporting the electrodes were not a consideration, thinner current collectors 120, 140 could be used without compromising their current carrying function. Thinner current collectors 120, 140 could, of course, result in a battery with less weight without compromising performance.
It has long been recognized that replacing the Li intercalated graphitic anode with a lithium foil can dramatically improve energy density due to the dramatically higher capacity of metallic lithium. However, lithium foil is not electrochemically stable in the presence of typical lithium ion battery liquid electrolytes and thus a simple replacement of graphitic anodes with lithium foils is not possible. It was found that polyethyleneoxide (PEO), a solid polymer, mixed with a lithium salt such as Li[N(SO2CF3)2], forms a stable passivating layer when contacted with a lithium foil. Unfortunately PEO-based polymers exhibited other limitations that have prevented their use in the successful creation of a lithium metal battery.
The inventive electrode assembly 205 also eliminates a major safety risk associated with previous lithium metal batteries. If a battery overheats to a temperature where lithium 210 begins to melt and become unstable, the surrounding nanostructured block copolymer electrolyte 250 maintains its stability, does not melt and can prevent the lithium from getting out of the encapsulation, thus preventing a runaway reaction and catastrophic failure.
The electrode assembly 205 can be made in a variety of ways. First, a lithium or lithium alloy foil with desired dimensions is provided. In some arrangements, the foil can be pre-coated with an inorganic salt(s) such as AlF3 or BF3. In one embodiment of the invention, the assembly 205 is formed using a coater. A solution of block copolymer electrolyte is applied to a set of rollers on the coater. The foil is run through the rollers, receives a coating of the block copolymer electrolyte, and is thus enclosed within the electrolyte. In another embodiment of the invention, a static charge is applied to the foil. Particles of block copolymer electrolyte are sprayed onto the foil. The foil coated with electrolyte particles is annealed, causing the particles to coalesce into a film, thus enclosing the foil within the electrolyte. In yet another embodiment of the invention, the assembly is formed using an extruder. Two layers of block copolymer electrolyte are applied to a foil—one layer on each side. The layers can be planar, they can be long beads, or they can have any other form known to be useful in extrusion processes. The foil with the block copolymer electrolyte on either side is fed into an extruder. The extruder presses against the layers, ensuring that the block copolymer electrolyte spreads over the foil and encloses it. In one arrangement, electronically-conductive leads 215 can be applied to the foil before foil is coated with electrolyte. In another arrangement, the lead(s) 215 can be inserted through the electrolyte 250 to make contact with the electrode 210 after the assembly 205 is formed.
There is an optional second electrolyte layer 460 adjacent the nanostructured block copolymer electrolyte 450. In one example, polysiloxane is used as the second polymer electrolyte 460. The second electrolyte layer 460 can be a very useful feature. Polymers that work well to perform useful structural, conductive, and safety functions for the lithium metal anode 410, such as the nanostructured block copolymer electrolyte 450, may not be optimized to interact with cathode 430. Multi-layered 450, 460 polymer electrolytes, optimized for specific roles within the battery, can be employed easily in the present inventive design, as virtually all polymers are sparingly soluble in one another. In one arrangement, the polymer electrolyte 450 is optimized to support and to stabilize the anode 410 and the second electrolyte layer 460 is a polymer optimized to interact with the cathode 430, that is, both to be incorporated into the cathode and to provide ionic conduction between the polymer electrolyte 450 and the cathode 430. In another arrangement, the cathode 430 incorporates a different polymer material than either the polymer electrolyte 450 or the second electrolyte layer 460. In arrangements where the optional second electrolyte layer 460 is not used, the electrolyte 450 can be adjacent the cathode 430.
When only liquid electrolytes are used in a battery, it is not possible to use multi-layered electrolytes because most electrolyte liquids are miscible in one another and the liquid layers would mix together. In one embodiment of the present invention, a separator and a liquid electrolyte that neither interacts with nor is miscible with the nanostructured block copolymer electrolyte 450 can be used as both the second electrolyte layer 460 (with a separator) and for permeating the cathode 430. There is a current collector 440 associated with the cathode 430. Although
In one example, the nano structured block copolymer electrolyte is a polystyrene-polyethyleneoxide-polystyrene (PS-PEO-PS) triblock copolymer doped with a lithium salt. The PS-PEO-PS/salt mixture serves both as the solid electrolyte 550 and as structural support to the thin lithium foil; the PEO block provides ion conducting channels, and the PS block provides mechanical integrity. The PS-PEO-PS/salt mixture serves also to ensure that even if the lithium metal becomes unstable or melts, no catastrophic battery failure will occur.
The embodiment of the invention shown in
In one example, the nano structured block copolymer electrolyte is a polystyrene-polyethyleneoxide-polystyrene (PS-PEO-PS) triblock copolymer doped with a lithium salt. The PS-PEO-PS/salt mixture serves both as the solid electrolyte 650 and as structural support to the thin lithium foil; the PEO block provides ion conducting channels, and the PS block provides mechanical integrity. The PS-PEO-PS/salt mixture serves also to ensure that even if the lithium metal becomes unstable or melts, no catastrophic battery failure will occur.
The second electrolyte layer 660 can be a very useful feature. Polymers that work well to perform useful structural, conductive, and safety functions for the lithium metal anode 610, such as nanostructured block copolymer electrolyte 650, may not be optimized to interact with cathode 630. Multi-layered 650, 660 polymer electrolytes, optimized for specific roles within the battery, can be employed easily in the present inventive design, as virtually all polymers are sparingly soluble in one another. In one arrangement, the polymer electrolyte 650 is optimized to support and to stabilize the anode 610 and the second electrolyte layer 660 is a polymer optimized to interact with the cathode 630, that is, both to be incorporated into the cathode and to provide ionic conduction between the polymer electrolyte 650 and the cathode 630. In another arrangement, the cathode 630 incorporates a different polymer material than either the polymer electrolyte 650 or the second electrolyte layer 660.
When only liquid electrolytes are used in a battery, it is not possible to use multi-layered electrolytes because most electrolyte liquids are miscible in one another and the liquid layers would mix together. In one embodiment of the present invention, a separator and a liquid electrolyte that neither interacts with nor is miscible with the nanostructured block copolymer electrolyte 650 can be used for both the second electrolyte layer 660 (with a separator) and for permeating the cathode 630. There is a conventional current collector 640 associated with the cathode 630.
As described in detail above, a block copolymer electrolyte can be used in the embodiments of the invention.
Multiple diblock polymer molecules 700 can arrange themselves to form a first domain 715 of a first phase made of the first polymer blocks 710 and a second domain 725 of a second phase made of the second polymer blocks 720, as shown in
In one arrangement the first polymer domain 715 is ionically conductive, and the second polymer domain 725 provides mechanical strength to the nanostructured block copolymer.
Multiple triblock polymer molecules 800 can arrange themselves to form a first domain 815 of a first phase made of the first polymer blocks 810a, a second domain 825 of a second phase made of the second polymer blocks 820, and a third domain 815b of a first phase made of the third polymer blocks 810b as shown in
In one arrangement the first and third polymer domains 815a, 815b are ionically conductive, and the second polymer domain 825 provides mechanical strength to the nanostructured block copolymer. In another arrangement, the second polymer domain 825 is ionically conductive, and the first and third polymer domains 815 provide a structural framework.
Multiple triblock polymer molecules 900 can arrange themselves to form a first domain 915 of a first phase made of the first polymer blocks 910a, a second domain 925 of a second phase made of the second polymer blocks 920, and a third domain 935 of a third phase made of the third polymer blocks 930 as shown in
In one arrangement the first polymer domains 915 are ionically conductive, and the second polymer domains 925 provide mechanical strength to the nanostructured block copolymer. The third polymer domains 935 provides an additional functionality that may improve mechanical strength, ionic conductivity, chemical or electrochemical stability, may make the material easier to process, or may provide some other desirable property to the block copolymer. In other arrangements, the individual domains can exchange roles.
Choosing appropriate polymers for the block copolymers described above is important in order to achieve desired electrolyte properties. In one embodiment, the conductive polymer (1) exhibits ionic conductivity of at least 10−5 Scm−1 at electrochemical cell operating temperatures when combined with an appropriate salt(s), such as lithium salt(s); (2) is chemically stable against such salt(s); and (3) is thermally stable at electrochemical cell operating temperatures. In one embodiment, the structural material has a modulus in excess of 1×105 Pa at electrochemical cell operating temperatures. In one embodiment, the third polymer (1) is rubbery; and (2) has a glass transition temperature lower than operating and processing temperatures. It is useful if all materials are mutually immiscible.
In one embodiment of the invention, the conductive phase can be made of a linear polymer. Conductive linear polymers that can be used in the conductive phase include, but are not limited to, polyethers, polyamines, polyimides, polyamides, alkyl carbonates, polynitriles, and combinations thereof. The conductive linear polymers can also be used in combination with polysiloxanes, polyphosphazines, polyolefins, and/or polydienes to form the conductive phase.
In another exemplary embodiment, the conductive phase is made of comb polymers that have a backbone and pendant groups. Backbones that can be used in these polymers include, but are not limited to, polysiloxanes, polyphosphazines, polyethers, polydienes, polyolefins, polyacrylates, polymethacrylates, and combinations thereof. Pendants that can be used include, but are not limited to, oligoethers, substituted oligoethers, nitrile groups, sulfones, thiols, polyethers, polyamines, polyimides, polyamides, alkyl carbonates, polynitriles, other polar groups, and combinations thereof.
Further details about polymers that can be used in the conductive phase can be found in U.S. Provisional Patent Application No. 61/056,688, filed May 28, 2008, U.S. Provisional Patent Application No. 61/091,626, filed Aug. 25, 2008, U.S. Provisional Patent Application No. 61/145,518 filed Jan. 16, 2009, U.S. Provisional Patent Application No. 61/145,507, filed Jan. 16, 2009, U.S. Provisional Patent Application No. 61/158,257 filed Mar. 6, 2009, and U.S. Provisional Patent Application No. 61/158,241, filed Mar. 6, 2009, all of which are included by reference herein.
There are no particular restrictions on the electrolyte salt that can be used in the block copolymer electrolytes. Any electrolyte salt that includes the ion identified as the most desirable charge carrier for the application can be used. It is especially useful to use electrolyte salts that have a large dissociation constant within the polymer electrolyte.
Suitable examples include alkali metal salts, such as Li salts. Examples of useful Li salts include, but are not limited to LiPF6, LiN(CF3SO2)2, Li(CF3SO2)3C, LiN(SO2CF2CF3)2, LiB(C2O4)2, B12FxH12-x, B12F12, and mixtures thereof.
In one embodiment of the invention, single ion conductors can be used with electrolyte salts or instead of electrolyte salts. Examples of single ion conductors include, but are not limited to sulfonamide salts, boron based salts, and sulfates groups.
In one embodiment of the invention, the structural phase can be made of polymers such as polystyrene, polymethacrylate, poly(methyl methacrylate), polyvinylpyridine, polyvinylcyclohexane, polyimide, polyamide, polypropylene, polyolefins, poly(t-butyl vinyl ether), poly(cyclohexyl methacrylate), poly(cyclohexyl vinyl ether), poly(t-butyl vinyl ether), polyethylene, fluorocarbons, such as polyvinylidene fluoride, or copolymers that contain styrene, methacrylate, or vinylpyridine.
Additional species can be added to nanostructured block copolymer electrolytes to enhance the ionic conductivity, to enhance the mechanical properties, or to enhance any other properties that may be desirable.
The ionic conductivity of nanostructured block copolymer electrolyte materials can be improved by including one or more additives in the ionically conductive phase. An additive can improve ionic conductivity by lowering the degree of crystallinity, lowering the melting temperature, lowering the glass transition temperature, increasing chain mobility, or any combination of these. A high dielectric additive can aid dissociation of the salt, increasing the number of Li+ ions available for ion transport, and reducing the bulky Li+[salt] complexes. Additives that weaken the interaction between Li+ and PEO chains/anions, thereby making it easier for Li+ ions to diffuse, may be included in the conductive phase. The additives that enhance ionic conductivity can be broadly classified in the following categories: low molecular weight conductive polymers, ceramic particles, room temp ionic liquids (RTILs), high dielectric organic plasticizers, and Lewis acids.
Other additives can be used in the polymer electrolytes described herein. For example, additives that help with overcharge protection, provide stable SEI (solid electrolyte interface) layers, and/or improve electrochemical stability can be used. Such additives are well known to people with ordinary skill in the art. Additives that make the polymers easier to process, such as plasticizers, can also be used.
Further details about block copolymer electrolytes are described in U.S. patent application Ser. No. 12/225,934, filed Oct. 1, 2008, U.S. patent application Ser. No. 12/271,1828, filed Nov. 14, 2008, and PCT Patent Application Number PCT/US09/31356, filed Jan. 16, 2009, all of which are included by reference herein.
This invention has been described herein in considerable detail to provide those skilled in the art with information relevant to apply the novel principles and to construct and use such specialized components as are required. However, it is to be understood that the invention can be carried out by different equipment, materials and devices, and that various modifications, both as to the equipment and operating procedures, can be accomplished without departing from the scope of the invention itself.
This application claims priority to U.S. Patent Provisional Application 61/046,685, filed Apr. 21, 2008, which is incorporated by reference herein. Examples of solid nanostructured block copolymer electrolyte systems referenced to by this application are disclosed in various of Applicant's other applications, including International Application No. PCT/US09/31356, filed Jan. 16, 2009 entitled “Gel Polymer Electrolytes for Batteries” and U.S. patent application Ser. No. 12/271,829, filed Nov. 14, 2008 entitled “A Solid Electrolyte Material Manufacturable by Conventional Polymer Processing Methods,” the entire contents of both of which are incorporated by reference herein.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US09/41180 | 4/21/2009 | WO | 00 | 10/18/2010 |
Number | Date | Country | |
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61046685 | Apr 2008 | US |