The present invention relates generally to electrolyte materials. More particularly, the present invention relates to solid polymer electrolyte materials that are ionically conductive, mechanically robust, and manufacturable by conventional polymer processing methods. Merely by way of illustration, an exemplary polymer electrolyte material has an elastic modulus in excess of 1×106 Pa at 25 degrees C. and is characterized by an ionic conductivity of at least 1×10−5 Scm−1 at 90 degrees C. Many uses are contemplated for the solid polymer electrolyte materials. By way of example, the present invention can be applied to improve Li-based batteries by means of enabling higher energy density, better thermal and environmental stability, lower rates of self-discharge, enhanced safety, lower manufacturing costs, and novel form factors.
The demand for rechargeable batteries has grown by leaps and bounds as the global demand for technological products such as cellular phones, laptop computers and other consumer electronic products has escalated. In addition, interest in rechargeable batteries has been fueled by current efforts to develop green technologies such as electrical-grid load leveling devices and electrically-powered vehicles, which are creating an immense potential market for rechargeable batteries with high energy densities.
Li-ion batteries represent one of the most popular types of rechargeable batteries for portable electronics. Li-ion batteries offer high energy and power densities, slow loss of charge when not in use, and they do not suffer from memory effects. Because of many of their benefits, including their high energy density, Li-ion batteries have also been used increasingly in defense, aerospace, back-up storage, and transportation applications.
The electrolyte is an important part of a typical Li-ion rechargeable battery. Traditional Li-ion rechargeable batteries have employed liquid electrolytes. An exemplary liquid electrolyte in Li-ion batteries consists of lithium-salt electrolytes, such as LiPF6, LiBF4, or LiClO4, and organic solvents, such as an alkyl carbonate. During discharging, the electrolyte may serve as a simple medium for ion flow between the electrodes, as a negative electrode material is oxidized, producing electrons, and a positive electrode material is reduced, consuming electrons. These electrons constitute the current flow in an external circuit.
While liquid electrolytes dominate current Li-based technologies, solid electrolytes may constitute the next wave of advances for Li-based batteries. The lithium solid polymer electrolyte rechargeable battery is an especially attractive technology for Li-ion batteries because, among other benefits, the solid polymer electrolyte exhibits high thermal stability, low rates of self-discharge, stable operation over a wide range of environmental conditions, enhanced safety, flexibility in battery configuration, minimal environmental impacts, and low materials and processing costs. Moreover, solid polymer electrolytes may enable the use of lithium metal anodes, which offer higher energy densities than traditional lithium ion anodes.
Lithium batteries with solid electrolytes function as follows. During charging, a voltage applied between the electrodes of a battery causes lithium ions and electrons to be withdrawn from lithium hosts at the battery's positive electrode. Lithium ions flowing from the positive electrode to the battery's negative electrode through a polymer electrolyte are reduced at the negative electrode. During discharge, the opposite reaction occurs. Lithium ions and electrons are allowed to re-enter lithium hosts at the positive electrode as lithium is oxidized at the negative electrode. This energetically favorable, spontaneous process converts chemically stored energy into electrical power that an external device can use.
Polymeric electrolytes have been the subject of academic and commercial battery research for several years. Polymer electrolytes have been of exceptional interest partly due to their low reactivity with lithium and potential to act as a barrier to the formation of metallic lithium filaments (or dendrites) upon cycling.
According to one example, polymer electrolytes are formed by incorporating lithium salts into appropriate polymers to allow for the creation of electronically insulating media that are ionically conductive. Such a polymer offers the potential to act both as a solid state electrolyte and separator in primary or secondary batteries. Such a polymer can form solid state batteries that exhibit high thermal stability, low rates of self-discharge, stable operation over a wide range of environmental conditions, enhanced safety, and higher energy densities as compared with conventional liquid-electrolyte batteries.
Despite their many advantages, the adoption of polymer electrolytes has been curbed by the inability to develop an electrolyte that exhibits both high ionic conductivity and good mechanical properties. This difficulty arises because high ionic conductivity, according to standard mechanisms, calls for high polymer chain mobility. But high polymer chain mobility, according to standard mechanisms, tends to produce mechanically soft polymers.
As an example, a prototypical polymer electrolyte is one composed of polyethylene oxide (PEO)/salt mixtures. PEO generally offers good mechanical properties at room temperature. However, PEO is also largely crystalline at room temperature. The crystalline structure generally restricts chain mobility, reducing conductivity. Operating PEO electrolytes at high temperature (i.e., above the polymer's melting point) solves the conductivity problem by increasing chain mobility and hence improving ionic conductivity. However, the increased conductivity comes at a cost in terms of deterioration of the material's mechanical properties. At higher temperatures, the polymer no longer behaves as a solid.
In general, attempts to stiffen PEO, such as through addition of hard colloidal particles, increasing molecular weight, or cross-linking, have been found to also cause reduced ionic conductivity. Similarly, attempts to increase the conductivity of PEO, such as through addition of low molecular weight plasticizers, have led deterioration of mechanical properties.
Therefore, there has been and is still a strong need for a polymeric electrolyte material with high ionic conductivity and mechanical stability where the material is amenable to standard high-throughput polymer processing methods.
The present invention relates generally to electrolyte materials. More particularly, the present invention relates to solid polymer electrolyte materials that are ionically conductive, mechanically robust, and can be formed into desirable shapes using conventional polymer processing methods. Merely by way of illustration, an exemplary polymer electrolyte material has an elastic modulus in excess of 1×106 Pa at 25 degrees C. and is characterized by an ionic conductivity of at least 1×10−5 Scm−1 at 90 degrees C. Many uses are contemplated for the solid polymer electrolyte materials. By way of examples, the present invention can be applied to improve Li-based batteries by means of enabling higher energy density, better thermal and environmental stability, lower rates of self-discharge, enhanced safety, lower manufacturing costs, and novel form factors.
According to an embodiment, the present invention provides a rigid, ionically conductive polymeric electrolyte material that may be processed by means of high-throughput or industrial processing techniques. The unique and novel properties of the material stem in part from morphological features of the polymer domains, determined in part by the molecular arrangements within the material.
According to the embodiment, the material enables large-scale processing and production of an ionically conductive, yet mechanically stable electrolyte that may be used in lithium metal or lithium ion batteries. In lithium-based batteries the material can afford high thermal stability, low rates of self-discharge, stable operation over a wide range of environmental conditions, improved cycle life, enhanced safety, and/or higher energy densities as compared with conventional liquid-electrolytes.
According to an embodiment, a polymer electrolyte containing two primary phases of at least two disparate polymeric materials is provided. An exemplary material system includes a conductive domain and a structural domain. The structural domain and the conductive domain are made of different polymers and may be arranged in layered structures. In a specific embodiment, the domains are arranged in a lamellar structure where the domains are arranged in layers. In another specific embodiment, the domains are arranged in a perforated lamellar structure where one layer extends into perforations in another layer of the lamellar structure, and where the perforating of one layer by another may help to impede the formation of crystalline structures.
According to a specific embodiment, the electrolyte is characterized by a two domain morphology and is made of linear diblock or triblock copolymers. An exemplary material contains conductive and structural phases in a morphology that leads to a mechanically unique and favorable bonding configuration to offer unique properties. According to an embodiment, the processibility of the material is improved through enhanced mechanical properties, such as increased yield strain and increased impact strength.
According to an embodiment, the electrolyte is characterized by a three-domain morphology and is made of linear triblock copolymers. An exemplary material system includes two primary phases forming a conductive and a structural domain and an additional third disparate polymer material forming a third domain. According to an embodiment, the third domain helps to improve the processibility of the materials by enhancing the mechanical properties, such as increasing yield strain and increasing impact strength and toughness of the material. According to the embodiment, a third domain also serves to impede the formation of crystalline phases in the conductive domain, enhancing the conductivity properties of the material.
According to an embodiment, a conductive linear polymer block making up a conductive domain is a polyether. In one arrangement, the linear polymer block making up a conductive domain is polyethylene oxide. In another arrangement, the conductive linear polymer block is a polyamine. In one arrangement, the conductive linear polymer block is a linear copolymer. In one arrangement, the linear copolymer contains an ether.
According to an embodiment, a structural polymer block making up a structural domain is selected from a group including non-ionic-conducting polymers characterized by a bulk modulus of greater than 106 Pa at 90 degrees C. The structural polymer block can be selected from a group including polystyrene, polymethacrylate, polyvinylpyridine, polyvinylcyclohexane, polyimide, polyamide, and polypropylene. The structural polymer block can include a component selected from a group comprising styrene, methacrylate, vinylpyridine, vinylcyclohexane, imide, amide, and propylene. In one arrangement, the structural polymer block is polystyrene. In one arrangement, the structural polymer block is polymethacrylate. In one arrangement, the structural polymer block is polyvinylpyridine. In one arrangement, the structural polymer block is polyvinylcyclohexane. In one arrangement, the structural polymer block is polyimide. In one arrangement, the structural polymer block is polyamide. In one arrangement, the structural polymer block is polypropylene.
According to an embodiment, a third polymer block making up a third domain is a rubbery polymer. A rubbery polymer can increase the toughness of the block copolymer, making it less brittle or friable. The third polymer block can be a polysiloxane, such as polydimethylsiloxane. The third polymer block can also be a polyacrylate, such as poly(2-ethylhexyl acrylate), polydecyl methacrylate, or polylauryl methacrylate. The third polymer block can also be a polydiene, such as polyisoprene and polybutadiene.
Other details and other embodiments of the current invention involving material systems for a solid electrolyte material that is ionically conductive, mechanically robust, and manufacturable by conventional polymer processing methods are described throughout this disclosure. While these inventions have been described in the context of the above specific embodiments, a person of skill in the art will recognize that other modifications and variations are possible. Accordingly, the scope and breadth of the present invention should not be limited by the specific embodiments described herein and should instead be determined by the following claims and their full extent of equivalents.
It should be understood that the drawings are not drawn to scale and are intended only to help the reader in understanding the embodiment of the invention.
Embodiments of the present invention relate generally to electrolyte materials. More particularly, the embodiments relate to solid polymer electrolyte materials that are ionically conductive, mechanically robust, and manufacturable by conventional polymer processing methods. Merely by way of illustration, an exemplary polymer electrolyte material has an elastic modulus in excess of 1×106 Pa at 25 degrees C. and is characterized by an ionic conductivity of at least 1×10−5 Scm−1 at 90 degrees C. Many uses are contemplated for the solid polymer electrolyte materials. By way of example, the present invention can be applied to improve Li-based batteries by means of enabling higher energy density, better thermal and environmental stability, lower rates of self-discharge, enhanced safety, lower manufacturing costs, and novel form factors.
The current invention includes solid polymeric electrolyte materials. According to an embodiment, the material includes unique molecular architectures and unique morphological features. In general, specific morphological features of a solid electrolyte material can arise depending on processing as well as the specific composition, volume fraction, and molecular architectures of the particular coexisting phases of polymers.
According to an embodiment, a solid polymer electrolyte material is characterized by a two-domain morphology with one domain being a conductive domain and the other domain being a structural domain. An exemplary solid polymer electrolyte may also include a three-domain morphology with a first domain being a conductive domain, a second domain being a structural domain, and a third domain interspersed between the conductive domain and the structural domain.
Lamellae of the conductive domains provide pathways for ion conduction through a bulk electrolyte material. Perforations in the conductive lamellae may serve as an impediment to crystallization and enhance the conductivity of the conductive domains. Lamellae of the structural domains provide sufficient support to confer structural stability to a bulk electrolyte material. Optional additional domains of a third, minor phase may serve to increase the yield strain or impact strength of a bulk electrolyte material. In addition, domains of a third, minor phase may serve as an impediment to crystallinity of the conductive domains and thereby enhance conductivity of a bulk electrolyte material.
According to an embodiment, the conductive region 104 provides at least one pathway for ion conduction to flow through the electrolyte 100.
In general, a two-domain copolymer solid polymer electrolyte can be made of several materials. For example, according to the embodiment, a solid polymer electrolyte can be made of poly(styrene-block-ethylene oxide) (SEO) diblock copolymers containing a first domain made of polystyrene and a second domain made of polyethylene oxide. According to a specific embodiment, a SEQ diblock copolymer electrolyte with molecular weight of ˜400,000 Daltons may be friable and breaks apart easily when attempts are made to form a free-standing thin film upon removal of solvent.
According to an embodiment, the first domain is a conductive domain, where layers 210 and 230 constitute conductive polymers. According to the embodiment, the second domain is a structural domain, where layers 220 and 240 constitute structural polymers. According to another embodiment, the first domain is a structural domain, where layers 210 and 230 constitute structural polymers. According to the embodiment, the second domain is a conductive domain, where layers 220 and 240 constitute conductive polymers.
As is illustrated, in general, layer 210 of the first domain is made of polymer block 250 and polymer block 255 where polymer block 250 and polymer block 255 are not covalently bonded to each other. According to an embodiment, polymer block 250 and polymer block 255 may consequently slide relative to each other along a region 252. Similarly, as is also illustrated, layer 230 of the first domain is made of polymer block 270 and polymer block 275. According to an embodiment, polymer block 270 and polymer block 275 are also not covalently bonded to each other and may consequently also slide relative to each other along a region 272.
As is illustrated, in general, layer 220 of the second domain is made of polymer block 260 and polymer block 265. According to an embodiment, polymer block 260 and polymer block 265 are not covalently bonded to each other and may consequently slide relative to each other along a region 262. Similarly, as is also illustrated, layer 240 is made of polymer block 280 and polymer block 285. According to an embodiment, polymer block 280 and polymer block 285 are also not covalently bonded to each other and may consequently also slide relative to each other along a region 282.
According to an embodiment, a first domain extends into perforations into a second domain when the volume fraction of the first domain is larger than the volume fraction of the second domain. According to an embodiment, the first domain extending into the second domain is a conductive domain, and the second domain is a structural domain. According to the embodiment, the plurality of extensions 295 is adapted to conduct ions between one surface 240 of the electrolyte and another surface 245 of the electrolyte. According to another embodiment, the first domain extending into the second domain is a structural domain, and the second domain is a conductive domain.
As illustrated in
The linear polymer block 412 and the linear polymer block 414 of the conductive layer 420 are not covalently bonded to each other. The linear polymer block 412 and the linear polymer block 414 have free ends approximately along region 422, which can slide relative to one another or can entangle with one another. Similarly, the linear polymer block 432 and the linear polymer block 434 of the conductive layer 440 are not covalently bonded to each other and have free ends approximately along region 442, which can slide relative to one another or can entangle with one another. In contrast, the structural domains 410, 430, and 450 contain only single polymer blocks. In some arrangements, the additional entanglements in the conductive domains 420, 440 can toughen the electrolyte, making it easier to process than similar electrolytes made from diblock polymers.
As illustrated in
The polymer block 462 and the polymer block 464 of structural domain 465 are not covalently bonded to each other along region 463. Similarly, the polymer block 482 and the polymer block 484 of structural domain 485 are not covalently bonded to each other along region 483. In one arrangement, the structural domains 465, 485 are glassy polymers; they have similar mechanical properties whether or not there are covalent bonds in the regions 463, 483. Conductive domains 455, 475, and 495 contain only single linear polymer blocks 460, 470, 490, respectively. Each linear polymer block 470 is tethered at each end by the structural polymer blocks 464, 482. Similarly, each linear polymer block 460 is tethered at each end by the structural polymer blocks 462 and the unlabeled one at the left, and each linear polymer block 490 is tethered at each end by the structural polymer blocks 484 and the unlabeled one at the right. In one embodiment, this tethering of the conductive linear polymer blocks at both ends increases the toughness of the electrolyte, making it less brittle and friable, and easier to process than an electrolyte made from diblock-based block copolymers described previously.
The solid polymer electrolytes described in
In one embodiment of the invention, the third domain has a volume between about 2% and 20% of the sum of the volumes of the first domain and the second domain. In one embodiment of the invention, the third domain has a volume between about 2% and 10% of the sum of the volumes of the first domain and the second domain. In one embodiment of the invention, the third domain has a volume between about 2% and 5% of the sum of the volumes of the first domain and the second domain.
According to the embodiment, one of the primary domains (either the grey domain or the white domain) is a structural domain and the other one of the primary domains is a conductive domain. The third domain need not be conductive or structural but should either form a contiguous region or form a plurality of regions of material different from that of the primary domains between the conductive domain and the structural domain, according to an embodiment.
Choosing appropriate polymers for the structures described herein is important in order to achieve the desired properties. In one embodiment, the conductive linear 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 1×107 Pa at electrochemical cell operating temperatures. In one embodiment, the third material (1) is rubbery; and (2) has a glass transition temperature lower than operating and processing temperatures. In order to form the desired morphologies, all materials are mutually immiscible.
In general, conductive polymers have greater conductivity when they are not in glassy or crystalline forms. In one embodiment of the invention, the polymer that makes up the conductive domain of the polymer electrolyte is somewhat crystalline at 25 degrees C. As discussed above, the perforated lamellar structure can be useful in reducing crystallinity. In one arrangement, the crystalline phase makes up no more than 10% of the conductive domain. In one arrangement, the determination of crystal content can be measured by differential scanning calorimetry.
In one embodiment of the invention, the conductive linear block polymer has a molecular weight greater than 50,000 Daltons. In another embodiment of the invention, the conductive linear block polymer has a molecular weight greater than 100,000 Daltons. In one embodiment of the invention, the structural block polymer has a molecular weight greater than 50,000 Daltons. In another embodiment of the invention, the structural block polymer has a molecular weight greater than 100,000 Daltons. In one embodiment of the invention, the linear diblock copolymer that makes up the domains of the electrolyte has a molecular weight greater than 150,000 Daltons. In another embodiment of the invention, the linear diblock copolymer that makes up the domains of the electrolyte has a molecular weight greater than 350,000 Daltons. In one embodiment of the invention, the linear triblock copolymer that makes up the domains of the electrolyte has a molecular weight greater than 250,000 Daltons. In another embodiment of the invention, the linear triblock copolymer that makes up the domains of the electrolyte has a molecular weight greater than 400,000 Daltons.
According to an embodiment, the solid polymer electrolyte materials described here may be improved if one or more additives (or species) that enhance(s) ionic conductivity is included in the ionically conductive domain. The additive can improve ionic conductivity in the conductive domain by lowering the degree of crystallinity, melting temperature, and glass transition temperature, and further by increasing chain mobility. The ionic conductivity improvement can be as much as an order of magnitude or more. Moreover, 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. Finally, additives that can weaken the interaction between Li+ and PEO chains/anion, thereby making it easier for Li+ ions to diffuse, may be included in the conductive domain. The kinds of additives that enhance ionic conductivity can be described by the following:
In some arrangements, additives that enhance ionic conductivity are predominantly or exclusively in the conductive domain. Thus, the additives have little or no effect on the structural domain, so the mechanical properties of block copolymer electrolytes are unchanged by the use of additives.
According to the embodiment, the additive can be ceramic particles, such as Al2O3 particles, TiO2 particles, and SiO2 particles. In some arrangements, the particles are nanoparticles with no dimension larger than 10 nm. In other arrangements, the nanoparticles have no dimension larger than 5 nanometers.
In another embodiment, the additive is a room temperature ionic liquid. Examples of RTILs include N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)imide [PYR14+TFSI−] and 1-butyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide [BMITFSI].
In another embodiment, the additive is a high dielectric organic plasticizer(s). Examples of high dielectric organic plasticizers include ethylene carbonate and propylene carbonate.
In another embodiment, the additive is a Lewis acid(s). Examples of Lewis acids include polyethylene glycol borate ester and polyethylene glycol aluminate ester.
In one embodiment of the invention, the linear diblock copolymer that makes up the conductive and structural domains of the electrolyte has a molecular weight of at least 150,000 Daltons. In another embodiment of the invention, the linear diblock copolymer that makes up the conductive and structural domains of the electrolyte has a molecular weight of at least 350,000 Daltons.
The following are examples of various processing techniques that can be employed to manufacture a solid electrolyte material according to embodiments of the invention. According to an embodiment, the domain structure is formed and maintained through kinetic control of the various phases, and in particular kinetic restriction of an otherwise thermodynamically favored phase separation. Disparate homopolymers blended in solution may form the desired domain structures through fast removal of solvent, and in some cases slight activation by then heating the dry polymer. To maintain the morphology, the material may then either be kept at low temperatures to prevent phase separation, or with variations of these homopolymers, covalent cross linking may be used to effectively freeze the morphological state.
According to another embodiment employing block-copolymer based electrolytes as described above, the morphology is maintained through covalent bonding between phases, and the specific morphology obtained is dependent on the composition, volume fraction, and molecular architecture of polymer. An exemplary method for synthesizing poly(styrene-block-ethylene oxide) (SEO) diblock copolymer includes synthesizing polystyrene (PS) as a first block and synthesizing ethylene oxide (EO) as a second block. The method includes distilling purified benzene into a reactor on a vacuum line and taking the reactor from the vacuum line into a glove box where an initiator such as s-butyllithium may be added. The method includes returning the reactor to the vacuum line to be degassed and distilling styrene monomers into the reactor.
The method includes heating the reactor to room temperature, stirring for at least six hours, and isolating an aliquot of living polystyrene precursors in the glove box for molecular weight determination. The method includes returning the reactor to the vacuum line to be thoroughly degassed and distilling a few milliliters of ethylene oxide into the degassed reactor. The method includes heating the reactor to a room temperature, stirring for two hours, taking the reactor back to the glove box, and adding a strong base in 1:1 molar ratio to an initiator. The method includes adding t-butyl phosphazene base (t-BuP4) as the strong base.
The method includes returning the reactor to the vacuum line to be thoroughly degassed, stirring at room temperature for 12 hours to allow the t-BuP4 to react with the ethylene oxide-terminated PS chains, and distilling a desired amount of ethylene oxide into the reactor using dry ice/isopropanol. The method includes heating the reactor to 50° C. and stirring for five days in a hot water bath. The method includes returning the reactor to the glove box, terminating the living SEQ diblock copolymer using methanol, and isolating the SEQ diblock copolymer by precipitation in hexane and vacuum freeze drying from benzene.
An exemplary method for making a poly(styrene-block-ethylene oxide-block-styrene) (SEOS) triblock copolymers is similar to the method of making SEQ as described above. However, instead of terminating the final polymer with methanol, dichlorodimethylsilane is preferably used as a bifunctional terminator. According to the embodiment, the bifunctional terminator couples two SEQ chains together to form SEOS chains.
The method includes, after the addition of the bifunctional terminator, allowing the reaction mixture to stir for 5 days to enable the slow reaction to proceed to completion. The method includes adding methanol to terminate any remaining living chains and isolating SEOS triblock copolymers by precipitation in hexane and vacuum freeze drying from benzene.
An exemplary method for synthesizing poly(ethylene oxide-block-styrene-block-ethylene oxide) (EOSEO) triblock copolymers is similar to the method for making SEQ as described above. However, instead of initiating the styrene with s-butyllithium, a bifunctional initiator is preferably used. According to the embodiment, the initiator allows the PS chain to grow from both chain ends. In a specific embodiment, potassium naphthalene in THF can be used as the bifunctional initiator.
According to an embodiment, an exemplary method further includes isolating an aliquot of the living polystyrene precursor in the glove box for molecular weight determination and returning the reactor to the vacuum line to be thoroughly degassed. The method includes distilling a few milliliters of ethylene oxide into the degassed reactor. The method includes heating the reactor to a room temperature, stirring for two hours, taking the reactor back to the glove box, and adding a strong base in 1:1 molar ratio to an initiator. The method includes adding t-butyl phosphazene base (t-BuP4) as the strong base. The method includes returning the reactor to the vacuum line to be thoroughly degassed, stirring at room temperature for 12 hours to allow the t-BuP4 to react with the ethylene oxide-terminated PS chains, and distilling a desired amount of ethylene oxide into the reactor using dry ice/isopropanol. The method includes heating the reactor to 50° C., stirring for five days in a hot water bath, and returning the reactor to the glove box. The method includes terminating the living EOSEO triblock copolymer using methanol and isolating the EOSEO triblock copolymer by precipitation in hexane and by vacuum freeze drying from benzene.
An exemplary method for synthesizing poly(isoprene-block-styrene-block-ethylene oxide) (ISEO) triblock copolymers includes synthesizing a polyisoprene block in benzene. The method includes distilling purified benzene into a reactor on a vacuum line, taking the reactor from the vacuum line into the glove box where an initiator such as s-butyllithium is added. The method includes returning the reactor to the vacuum line to be degassed, distilling the isoprene monomer into the reactor, stirring the mixture for at least six hours, and isolating an aliquot of the living polyisoprene precursor in the glove box for molecular weight determination.
The method includes returning the reactor to the vacuum line to be thoroughly degassed, distilling the styrene into the living polyisoprene solution and allowing the reaction to proceed for at least six hours to form polyisoprene-block-polystyrene living polymers. The method includes cooling the reactor with dry ice/isopropanol, distilling a few milliliters of ethylene oxide into the reactor, heating the reactor to room temperature, and stirring for two hours. The method includes taking the reactor to the glove box and adding a strong base in a 1:1 molar ratio to the initiator. The method includes adding t-butyl phosphazene base (t-BuP4) as the strong base.
The method includes returning the reactor to the vacuum line to be thoroughly degassed, stirring at room temperature for 12 hours to allow the t-BuP4 to react with the ethylene oxide-terminated PI-PS chains, and distilling a desired amount of ethylene oxide into the reactor using dry ice/isopropanol. The method includes heating the reactor to 50° C. and stirring for five days in a hot water bath. The method includes returning the reactor to the glove box, terminating the living ISEO triblock copolymers using methanol, and isolating the ISEO diblock copolymer by precipitation in hexane and vacuum freeze drying from benzene.
According to an embodiment for purifying benzene to make a solid electrolyte material, starting material benzene may be purchased from Aldrich. An exemplary method for purifying benzene includes stirring on freshly ground calcium hydride for at least eight hours in a long neck flask attached to a vacuum line. The method includes freezing the mixture of calcium hydride using liquid nitrogen and degassing the mixture under vacuum. The method includes distilling benzene out of the calcium hydride mixture onto a s-butyllithium purification stage, stirring the benzene on the s-butyllithium for at least eight hours, and degassing.
According to an embodiment for purifying styrene to make a solid electrolyte material, starting material styrene may be purchased from Aldrich. An exemplary purified styrene may be stored in a freezer prior to use. According to the embodiment, the method includes pouring styrene into a flask attached to the vacuum line, freezing and degassing. The method includes pipetting dibutylmagnesium (1.0 M in heptane) into a second flask in a glove box, adding ten mL of dibutylmagnesium for every 100 mL of styrene to purify. The method includes attaching the flask to the vacuum line, distilling the heptane out of the dibutylmagnesium flask, distilling the styrene onto the dibutylmagnesium, stirring the styrene on the dibutylmagnesium for at least eight hours, and thoroughly degassing.
According to an embodiment for purifying isoprene to make a solid electrolyte material, starting material isoprene may be purchased from Aldrich. An exemplary purified isoprene may be stored in a freezer prior to use. According to the embodiment, the method includes pouring isoprene into a long neck flask containing freshly ground calcium hydride, attaching the flaks to a vacuum line, and freezing and degassing. The method includes pipetting s-butyllithium (1.4 M in cyclohexane) into a second long neck flask, adding ten mL of s-butyllithium for every 100 mL of isoprene to purify, distilling the cyclohexane of the s-butyllithium flask, and distilling the isoprene into the dried s-butyllithium using dry ice/isopropanol as the coolant. The method includes removing the mixture from the dry ice and stirring without coolant for three minutes, ensuring that the flask is not left out of the cooling bath for longer than three minutes. The method includes freezing the mixture in liquid nitrogen, degassing, repeating the stirring/degassing procedure twice more to enhance purity, and distilling isoprene into a measuring ampoule to get the isoprene to be ready to use.
According to an embodiment for purifying ethylene oxide to make a solid electrolyte material, starting material ethylene oxide may be purchased from Aldrich. An exemplary method includes condensing ethylene oxide into a long neck flask containing freshly ground calcium hydride using dry ice/isopropanol as the coolant and freezing and degassing ethylene oxide, which may be stored in a gas cylinder in a refrigerator prior to use. The method includes stirring ethylene oxide for a minimum of eight hours on the calcium hydride while packed in dry ice/isopropanol, pipetting n-butyllithium into a second long neck flask, attaching the flask to the vacuum line and degassing.
The method includes adding ten mL of n-butyllithium in hexane for every 100 mL of ethylene oxide to purify, distilling hexane out of the n-butyllithium flask, and distilling ethylene oxide into the dried n-butyllithium using dry ice/isopropanol as coolant. The method includes removing and replacing a dry ice/isopropanol bath, stirring the mixture for 30 minutes at 0° C., and ensuring the mixture does not warm above 0° C. in order to prevent unsafe runaway reactions. The method includes distilling ethylene oxide out of the n-butyllithium into a measuring ampoule using dry ice/isopropanol as the coolant and keeping the ampoule at 0° C. to get the ethylene oxide to be ready to use.
According to an embodiment for purifying dichlorodimethylsilane to make a solid electrolyte material, starting material dichlorodimethylsilane may be purchased from Aldrich. According to the embodiment, the method includes stirring on freshly ground calcium hydride for at least eight hours in a long neck flask attached to a vacuum line. The method includes freezing the dichlorodimethylsilane and degassing thoroughly prior to use.
According to an embodiment, the final steps for preparing an electrolyte includes preparing, dissolving, and mixing polymers and the lithium salt in an effective solvent system. The solvent is removed either by freeze drying or evaporation to yield a dry polymeric material that can be molded or otherwise processed into film for use as an electrolyte. Alternatively, the polymer/salt solution may be cast (e.g. spin cast, solution cast, etc.) or printed (i.e. screen printed, ink-jet printed, etc.) or otherwise deposited to form a film. According to the embodiment, the desired domain structure and morphology naturally may arise upon removal of solvent. Alternatively, the desired domain structure and morphology may arise soon after slight activation of the material such as by heating of the dry polymer material.
According to an embodiment, the final steps for preparing an electrolyte that includes species that enhance ionic conductivity includes preparing, dissolving, and mixing polymers and the lithium salt and the conductivity-enhancing species in an effective solvent system. The solvent is removed either by freeze drying or evaporation to yield a dry polymeric material that can be molded or otherwise processed into film for use as an electrolyte. Alternatively, the polymer/salt/species solution may be cast (e.g. spin cast, solution cast, etc.) or printed (i.e. screen printed, ink-jet printed, etc.) or otherwise deposited to form a film. According to the embodiment, the desired domain structure and morphology naturally may arise upon removal of solvent. Alternatively, the desired domain structure and morphology may arise soon after slight activation of the material such as by heating of the dry polymer material.
In conclusion, the present invention provides various embodiments of material systems for a solid electrolyte material that is ionically conductive, mechanically robust, and manufacturable by conventional polymer processing methods. While these inventions have been described in the context of the above specific embodiments, modifications and variations are possible. Accordingly, the scope and breadth of the present invention should not be limited by the specific embodiments described above and should instead be determined by the following claims and their full extend of equivalents.
This application claims priority to U.S. Provisional Patent Application 60/988,085, filed Nov. 14, 2007, which is incorporated by reference herein. This application is a continuation-in-part of U.S. patent application Ser. No. 12/225,934, filed Jun. 19, 2009, which is a national phase application of PCT Application Number PCT/US2007/008435, filed Apr. 3, 2007, which claims priority to U.S. Provisional Patent Application No. 60/744,243, filed Apr. 4, 2006 and U.S. Provisional Patent Application No. 60/820,331, filed Jul. 25, 2006, all of which are incorporated by reference herein.
The invention described and claimed herein was made in part utilizing funds supplied by the U.S. Department of Energy under Contract No. DE-AC02-05CH11231. The Government has certain rights in this invention.
Number | Name | Date | Kind |
---|---|---|---|
3355513 | Sadron et al. | Nov 1967 | A |
3711412 | Sawyer | Jan 1973 | A |
4311566 | McCann | Jan 1982 | A |
4582876 | Weemes | Apr 1986 | A |
4657833 | Hadley et al. | Apr 1987 | A |
5013619 | Cook | May 1991 | A |
5196484 | Giles | Mar 1993 | A |
5219681 | Yamada et al. | Jun 1993 | A |
5523180 | Armand | Jun 1996 | A |
5622792 | Brochu | Apr 1997 | A |
5639574 | Hubbard | Jun 1997 | A |
5658685 | Oliver | Aug 1997 | A |
6096234 | Nakanishi | Aug 2000 | A |
6322924 | Hirahara | Nov 2001 | B1 |
6361901 | Mayes | Mar 2002 | B1 |
6428933 | Christensen et al. | Aug 2002 | B1 |
6537704 | Akashi | Mar 2003 | B1 |
6673273 | Ba Le et al. | Jan 2004 | B2 |
6743550 | Gan | Jun 2004 | B2 |
6749961 | Nguyen et al. | Jun 2004 | B1 |
6835495 | Michot | Dec 2004 | B2 |
6841601 | Serpico et al. | Jan 2005 | B2 |
7026071 | Mayes | Apr 2006 | B2 |
7282302 | Visco | Oct 2007 | B2 |
7315106 | Asaka | Jan 2008 | B2 |
7318982 | Gozdz | Jan 2008 | B2 |
20030094599 | Le et al. | May 2003 | A1 |
20040151985 | Munshi | Aug 2004 | A1 |
20050034993 | Gozdz et al. | Feb 2005 | A1 |
20050181254 | Uensal et al. | Aug 2005 | A1 |
20050221193 | Kinouchi et al. | Oct 2005 | A1 |
20050256256 | Muramoto et al. | Nov 2005 | A1 |
20060270822 | Norsten | Nov 2006 | A1 |
20060289405 | Oberste-Berghaus | Dec 2006 | A1 |
20090104523 | Mullin et al. | Apr 2009 | A1 |
20090263725 | Balsara et al. | Oct 2009 | A1 |
20110033755 | Eitouni et al. | Feb 2011 | A1 |
Number | Date | Country |
---|---|---|
297281 | Jan 1992 | DE |
1 553 117 | Jul 2005 | EP |
2006-036925 | Feb 2006 | JP |
8803154 | May 1988 | WO |
88 03154 | May 1988 | WO |
2007113236 | Oct 2007 | WO |
2007142731 | Dec 2007 | WO |
2010039606 | Aug 2010 | WO |
Number | Date | Country | |
---|---|---|---|
20090075176 A1 | Mar 2009 | US |
Number | Date | Country | |
---|---|---|---|
60988085 | Nov 2007 | US | |
60744243 | Apr 2006 | US | |
60820331 | Jul 2006 | US |
Number | Date | Country | |
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Parent | 12225934 | US | |
Child | 12271829 | US |