Patent Application
20130130131
A battery cell is a particularly useful article that provides stored electrical energy which can be used to energize a multitude of devices requiring an electrical power source. A battery cell, which is often referred to, somewhat inaccurately, in an abbreviated form as a “battery,” is an electrochemical apparatus typically formed of at least one electrolyte (also referred to as an “electrolytic conductor”) disposed between a pair of spaced apart electrodes. The electrodes and electrolyte are the reactants for a chemical reaction that causes an electric current to flow between the electrodes when the electrode ends that are not in contact with the electrolyte are connected to one another through an object or device (generally referred to as the “load”) to be powered. The flow of electrons through the free ends of the electrodes is accompanied and caused by the creation and flow of ions in and through the electrolyte under a reaction potential between the electrodes.
In a non-rechargeable battery cell, the chemical reaction that produces the flow of electric current also causes one or more of the reactants to be consumed or degraded over time as the cell discharges, thereby depleting the cell. In contrast, in a rechargeable battery cell, after the cell has partially or fully discharged its electrical potential, the chemical reaction may be reversed by applying an electric current to the cell that causes electrons to flow in an opposite direction between the electrodes and an associated flow of ions. Thus, it can be appreciated that rechargeable battery cells are extremely useful as a source of electrical power that can be replenished.
A problem in utilizing rechargeable batteries is that it is often difficult to return the reactants to their original, pre-use state, that is, the pristine or ideal (or as close as possible) condition that the reactants are in before the cell is used. This problem relates to specific problems associated with returning each individual reactant to its original state.
Lithium air batteries are attractive batteries because they provide high energy density from easily-obtainable and inexpensive electrode reactant materials, namely, lithium and air. In a lithium air battery, lithium serves as the anode and the cathode is formed of a light-weight, inexpensive substrate that is capable of supporting a catalyst for facilitating oxygen's role as a reactant.
A problem with rechargeable lithium air batteries is that they are particularly difficult to recharge multiple times due to the characteristics of lithium. Specifically, it is often difficult to return the lithium anode to its pre-discharge condition because of imperfections formed on the surface of the anode during the discharge-recharge cycling. Imperfection problems include a roughening of the surface of the anode and the formation of pores in the anode. Another serious imperfection problem is that the surface of the lithium anode that is in contact with the electrolyte may be degraded by the formation of dendrites. Dendrites are thin protuberances that can grow upon and outwardly of a surface of an electrode during recharging of the cell. Recharging causes a re-plating of the lithium anode. Not only do dendrites inhibit proper plating or re-plating of the electrode, but also, one or more branches of dendrites may grow long enough so as to extend through the electrolyte between the anode and cathode and thereby provide a direct connection that can electrically short circuit the cell. An electrical short is undesirable in and of itself but, in addition, the current passing through an electrical short may cause the temperature through the electrolyte to increase to a point wherein the electrolyte is no longer effective and/or the electrolyte and/or the cell itself may ignite. Thus, known lithium air batteries have a very limited useful life. It can thus be appreciated that it would be useful to develop a rechargeable lithium air battery cell that can be discharged and recharged effectively many times.
A concern in recharging a rechargeable battery is how much electrical energy will be required to restore the battery to its pre-discharged state and potential. This level of electrical is typically greater than the electrical energy initially provided by the battery. However, it is desirable that the electrical energy required to recharge a rechargeable battery be minimized so as to reduce the cost of operation and to prevent damage to the battery. Thus, it can be appreciated that it would be useful to develop a rechargeable lithium air battery in which the voltage level and amount of energy required to recharge the battery are minimized. The excess energy required during recharge is associated with a difficulty in reversing the reactions that take place in an air cathode. Reactions in the cathode are plagued with parasitic reactions involving the electrolyte. These reactions can consume the electrolyte and cause degradations in performance. Therefore, a more stable electrolyte is needed.
Most battery systems developed to date are based on aqueous-based alkaline electrolytes. A popular example is the zinc/oxygen battery that is in commercial use for hearing aids. Electric Fuel Corp. produces primary zinc air batteries for cellular phone applications. Electrically rechargeable zinc air batteries use bifunctional oxygen electrodes so that both the charge and discharge processes take place within the battery structure. AER Energy Resources, Inc. (Atlanta, Ga.) designed an electrically rechargeable zinc air cell; however, the cyclability of this battery is too low to satisfy the requirements of many commercial applications.
In recent years, there has been a renewed interest in the development of lithium oxygen batteries. To overcome water corrosion problems, non-aqueous electrolytes typically used in lithium and lithium ion batteries have been utilized. For example, U.S. Pat. No. 5,510,209 describes a lithium oxygen battery based on an organic electrolyte using carbon powder as an air electrode and cobalt phthalocyanine as a catalyst. The battery was shown to have an open-circuit potential of approximately 3V and an operating voltage between 2.0 to 2.8V.
Although the '209 patent suggests that the lithium/oxygen batteries were rechargeable, no more than two complete cycles were reported. On the other hand, the formation of Li2O2 in the discharged air electrode was observed by chemical titration analysis, but the disappearance of Li2O2 in the recharged (not original) air electrode was not shown. Therefore, the rechargeability of this lithium oxygen battery is not conclusive.
The discharge mechanism of a lithium oxygen battery is primarily the deposition of Li2O2 in the carbon-based air electrode. Since the reduction of O2 to O2− occurs only in the presence of a catalyst, the product is often the peroxide, O22−. The reactions of lithium with oxygen are:
2Li+O2→Li2O2 E°=3.10 V
4Li+O2→2Li2O E°=2.91V
Before completely forming peroxide, an oxygen molecule can reduce to form a superoxide radical which links with one lithium cation, forming lithium superoxide. This intermediate can precipitate within the cathode, forming peroxide, which may support ongoing cycling or attack carbonate based solvents through nucleophilic mechanisms, thus choking off cycling. Lithium superoxide is not a stable compound and will convert to peroxide, but this in part depends upon the stability of the solvent. The superoxide reaction is expected to proceed as follows:
O2+Li++e−→LiO2
2LiO2→Li2O2+O2
There remains a need in the art for further improvements in battery structure to maximize the potential of rechargeable lithium air and lithium oxygen batteries.
This invention relates to rechargeable battery cells, and more particularly, the invention relates to electrolytes for rechargeable, lithium air battery cells.
According to the present invention, a rechargeable lithium air battery comprises a non-aqueous, organic-solvent-based electrolyte including a lithium salt and an additive containing an alkylene group, disposed between a spaced apart pair of an anode and an air cathode.
In one embodiment of the invention, the alkylene additive is selected from the group consisting of alkylene carbonate, alkylene siloxane, and a combination of alkylene carbonate and alkylene siloxane.
In an aspect of this embodiment, alkylene carbonate is selected from the group consisting of vinylene carbonate, butylene carbonate, and a combination of vinylene carbonate and butylene carbonate.
In another aspect of this embodiment, alkylene siloxane is a polymerizable silane. And in a further aspect, the polymerizable silane is triacetoxyvinylsilane.
In another embodiment of the invention, a separator is disposed between the air cathode and the anode and is infused with the non-aqueous, organic-solvent-based electrolyte including a lithium salt and an alkylene additive.
The invention also relates to a rechargeable lithium air battery comprising a lithium based anode, an air cathode, and a non-aqueous electrolyte, wherein the electrolyte comprises a lithium salt and at least one organosilicon compound, and wherein the anode and the cathode are spaced apart from one another and electrochemically coupled to one another by the electrolyte.
Additionally, a cathode for a rechargeable lithium air battery comprises a carbon-based, porous electrode and a non-aqueous electrolyte comprising a lithium salt and at least one organosilicon compound.
The foregoing summary, as well as the following detailed description of the invention, will be better understood when read in conjunction with the appended drawings. For the purpose of illustrating the invention, there are shown in the drawings embodiments which are presently preferred. It should be understood, however, that the invention is not limited to the precise arrangements and instrumentalities shown.
Embodiments of the present invention are described herein. The disclosed embodiments are merely exemplary of the invention that may be embodied in various and alternative forms, and combinations thereof. As used herein, the word “exemplary” is used expansively to refer to embodiments that serve as illustrations, specimens, models, or patterns. The figures are not necessarily to scale and some features may be exaggerated or minimized to show details of particular components. In other instances, well-known components, systems, materials, or methods have not been described in detail in order to avoid obscuring the present invention. Therefore, at least some specific structural and functional details disclosed herein are not to be interpreted as limiting, but merely as a basis for the claims and as a representative basis for teaching one skilled in the art to variously employ the present invention.
As an overview, the invention teaches a first electrolyte for a rechargeable battery that has a lithium anode and an air cathode, which improved electrolyte helps to increase the useful life and effectiveness of the battery. This electrolyte according to the invention also optimizes (lowers) the level of charge voltage required by the battery during recharging, thereby further increasing the usefulness of the battery. The electrolyte is also stable in the presence of the superoxide radical.
Non-aqueous electrolytes are often used with lithium cells to avoid undesirable reactions between lithium and water-based electrolytes. However, in a cell, a film will typically form on a lithium electrode immersed in a non-aqueous electrolyte. These films form when the lithium metal immersed in the non-aqueous liquid electrolyte generally reacts with the electrolyte solvent, the electrolyte salt, and trace impurities or dissolved gases to form the film. Rather than leaving the nature of the surface film that forms to chance, in one embodiment, the invention modifies the film by introducing additives to the electrolyte solution. These additives are tailored to react with the electrode surfaces and form a surface stabilizing film that is conducive to lithium cycling. This electrolyte of the invention changes the chemical composition of the film such that it adopts characteristics that inhibit the growth of dendrites on the lithium electrode. The invention thus converts the natural presence of the film to a beneficial use in fighting dendrite growth. To convert the film to a desirable composition, the invention uses as additives a class of organic compounds that are capable of being dissolved in the electrolyte solution and capable of polymerizing when placed in contact with lithium metal.
A second electrolyte according to the invention contains an organosilicon compound. These compounds have been found to improve the reversibility of batteries. Silicon-based electrolytes are advantageous due to high conductivity, safety, and favorable electrochemical and chemical properties. The premise behind organosilicon based electrolytes is that they are not susceptible to nucleophilic attack, but maintain properties needed for lithium air cycling. Thus, silicon-containing electrolytes represent a growing area of interest as a means for improving the safety of lithium air batteries.
As a further aspect of this overview and introduction, it is to be noted that the air cathode that is utilized in the invention comprises a porous substrate which supports a material that serves as a catalyst to facilitate oxygen's role in the electrochemical reaction that produces energy. In a lithium air battery, oxygen is the cathode reactant for the overall electrochemical reaction that creates electricity. Oxygen is placed in condition for reacting at the substrate that forms the cathode support member. The cathode may employ a catalyst that facilitates oxygen's participation in the electrochemical reaction. The oxygen may be in an isolated (or pure state), or the cathode may use oxygen that is present in ambient air. The oxygen in ambient air is a natural component of air. Hence, the use of the term “air battery” or “lithium air battery.” For the purposes of this disclosure, the term “lithium air battery” may also be understood to encompass “lithium oxygen batteries.” In both systems, lithium reacts with oxygen, forming Li2O or Li2O2. The distinction between lithium air and lithium-oxygen batteries is the type of oxygen source that is used: oxygen from a tank or oxygen from air. The electrolytes according to the invention are appropriate for both types of systems.
Although the term “battery” technically may more properly define a combination of two or more cells, it has come to be used popularly to refer to a single cell. Thus the term battery by itself is sometimes used herein for convenience of explanation to refer to what is actually a single cell. The teachings herein that are applicable to a single cell are applicable equally to each cell of a battery containing multiple cells.
Referring now to the drawings, wherein like numerals indicate like elements throughout the several views, the drawings illustrate certain of the various aspects of exemplary embodiments.
Referring first to
Referring now to
An anode current-collector rod 32 is disposed in contact with the anode current-collector 30 and provides an anode connecting point for the cell 20. The anode current-connector rod 32 may be formed of a copper-based material such as copper metal or a copper alloy. A cathode current-connector rod 34 is disposed in contact with the air cathode 24 and provides a cathode connecting point for the cell 20. The cathode current-connector rod 34 may be formed of an aluminum material, such as aluminum metal or an aluminum alloy (aluminum fused with zinc or copper, for example), or may be carbon mesh or an alternative carbon material. The above structures may be supported by a base 40 of rigid, non-reactive, non-electrically conductive material, such as the polymer sold in block form under the brand name Teflon®.
All of the various components described above in the second embodiment of the rechargeable cell 20 may be secured in a housing 50 forming a container. The components may be secured together and to the housing 50 by various securing mechanisms such as nuts 42, 44 that help secure the lower ends of the current-collector rods 32, 34 to the base 40 and nuts 48 that help secure the upper ends of the current-collector rods 32, 34 to the housing. Spacer elements 46 press the electrode stack together while allowing oxygen to reach the cathode 24. The anode current-collector rod 32 extends through and helps secure the position of the separator 25 and the anode current-collector 30 while the cathode current-collector rod 34 extends though and helps secure the position of the separator 25 and air cathode 24. The anode 22 is secured at least in part by being sandwiched between the separator 25 and anode current-connector 30. The housing 50 may contain a quantity of oxygen or air 52 for reaction with the air cathode 24. The housing 50 may have an orifice or aperture 54 through which oxygen or ambient air 52 is introduced into the interior of the housing 50. A removable orifice cover 56 may be used to seal the orifice 54 until injection of oxygen or air is desired.
In either the first or second embodiment described above, the lithium anode 12, 22 is formed of lithium metal, a lithium-metal based alloy, a lithium-intercalation compound, or lithium titanate (Li2TiO3). As used herein, the term “lithium-intercalation compound” means those substances having a layered structure that is suitable for receiving and storing lithium compounds for later use (such as in a reaction). Thus, these materials may also be considered “lithium-storage materials.” These lithium-intercalation, or lithium-intercalating compounds, are typically types of carbon. Lithium titanate functions similarly to a lithium-loaded intercalation compound when used as an anode material in a battery cell.
The air cathode 14, 24, described in more detail below, is predominantly a porous substrate, and may be infused with an oxygen-reduction catalyst to facilitate the oxygen reaction at the air cathode. Suitable oxygen-reduction catalysts comprise at least one of electrolytic manganese (IV) dioxide, ruthenium (IV) oxide, copper (II) oxide, copper (II) hydroxide, iron (II) oxide, iron (II,III) oxide, cobalt (II,III) oxide, nickel (II) oxide, silver, platinum and iridium.
The separator 25 is preferably made of a non-conductive polymer. The non-conductive polymer material may be porous, for example, in the nature of a sponge, so as to effectively hold the electrolyte described herein.
An embodiment of a cell constructed in accordance with the teachings of the invention is sealed in an enclosure wherein oxygen or air is injected to a predetermined pressure. Suitable operating pressure is in the range from about 0.1 atm to about 100 atm, and an optimum range is from about 0.5 atm to about 20 atm.
Referring to
Reference is now made generally to
Referring now to
Referring now to
In one embodiment, the invention modifies the lithium film that forms on a lithium electrode to produce a film that is conducive to lithium cycling (that is, discharging and recharging the cell). The film is modified by providing an electrolyte containing one or more additives that react with the electrode surfaces to form a surface-stabilizing film that is conducive to cycling.
An electrolyte for a battery cell typically comprises a salt dissolved in a solvent, often water. The invention employs a non-aqueous, organic-solvent-based electrolyte including a lithium salt and an alkylene additive. A non-aqueous electrolyte is used to avoid the damaging effects that water has upon lithium.
A suitable lithium salt for producing the electrolyte comprises at least one of lithium hexafluorophosphate, lithium tetrafluoroborate, lithium hexafluoroarsenate, lithium perchlorate, lithium bis(trifluorosulfonyl)imide, lithium bis(perfluoroethylsulfonyl)imide, lithium triflate, lithium bis(oxalato)borate, lithium tris(pentafluoroethyl)trifluorophosphate, lithium bromide, and lithium iodide. For convenience, the following table provides (molecular) chemical formulas for these salts:
To form the electrolyte solution, one or more of the above salts is dissolved in a solvent. Salt concentrations may range from 0.01-5 molar, but the preferred range is 0.5-1.5 molar. Examples of suitable solvents include two solvent mixtures: 1:2 (w:w) propylene carbonate and tetraglyme (PC:Tetraglyme) (“tetraglyme” is an amalgam of “tetraethylene glycol dimethyl ether”) and 1:2 (w:w) propylene carbonate and 1,2-dimethoxyethane (PC:DME).
Other suitable electrolyte solutions that may be employed in the invention are electrolyte solutions that are typically used for lithium-ion batteries. Such electrolyte solutions contain solvents that are based upon carbonates, esters, ethers, amines, amides, nitriles and sulfones. Such solvents include propylene carbonate, ethylene carbonate, dimethyl carbonate, diethyl carbonate, ethylene carbonate, 1,2-dimethoxyethane, diethyl carbonate, ethyl methyl carbonate, gamma-butyrolactone, sulfolane, 1,3-dioxolane, tetrahydrofuran, dimethoxyethane, diglyme, tetraglyme, diethyl ether, 2-methyl tetrahydrofuran, tetrahydropyran, pyridine, n-methyl pyrrolidone, dimethyl sulfone, ethyl methyl sulfone, ethyl acetate, dimethyl formamide, dimethyl sulfoxide, acetonitrile, and methyl formate.
Suitable proportions of alkylene additives range from less than 1% up to 10% by weight based on the weight of the electrolyte solution.
The additive for the non-aqueous, organic-solvent-based electrolyte comprises an alkylene compound. Suitable alkylene compounds are capable of dissolving in the electrolyte solution and also capable of polymerizing when coming into contact with lithium metal. Suitable alkylene compounds are alkylene carbonates, alkylene siloxanes, and combinations of alkylene carbonate and alkylene siloxane.
Suitable alkylene carbonates are vinylene carbonate, butylene carbonate, and a combination of vinylene carbonate and butylene carbonate. Vinylene carbonate, which for convenience is sometimes herein abbreviated as “VC,” has the following structural formula:
A suitable alkylene siloxane is a polymerizable silane such as triacetoxyvinylsilane. Triacetoxyvinylsilane, which for convenience is sometimes herein abbreviated as “VS,” has the following structural formula:
In a second embodiment, the electrolyte used in the lithium air cell contains at least one organosilicon compound. Such compounds have been found to improve the reversibility of batteries. Silicon-based electrolytes are advantageous due to high conductivity, safety, and favorable electrochemical and chemical properties. Thus, silicon-containing electrolytes represent a growing area of interest as a means for improving the safety of lithium air batteries.
Preferably, the organosilicon compound is a silane compound or a siloxane compound. The term “siloxane” technically describes a class of compounds containing alternate silicon and oxygen atoms with the silicon atoms bound to hydrogen atoms or organic groups. Silanes are compounds containing silicon-carbon bonds, analogous to alkanes. However, the terms “silane” and “siloxane” are often used interchangeably and incorrectly in the literature, and, for the purposes of this disclosure, these terms are not meant to be limited to the literal definitions thereof.
Preferred organosilicon compounds for use in the electrolyte according to the invention are those containing polyethylene oxide (PEO) side chains. Most preferred organosilicon compounds are trimethylsilane compounds having Formula (1) below, in which “n” is an integer representing the number of ethylene oxide units in the molecule and may range from 1 to about 20. Other preferred compounds are silanes containing more than one PEO side chain on the central silicon atom, including silanes having two, three, and four PEO side chains on the central silicon atom. Substituents on the silicon which are not PEO side chains may be hydrogen, substituted or unsubstituted alkyl groups having at least one carbon atom (methyl), or other substituted or unsubstituted organic groups. It is also within the scope of the invention for the electrolyte to contain more than one organosilicon compound.
The electrolyte further contains a salt, preferably a lithium salt as previously described. Preferred salts are LiBOB and LiTFSI. In a preferred embodiment, the electrolyte contains only the organosilicon compound with salt dissolved therein, preferably at a concentration of about 1 molar. No additional solvent is present in the electrolyte in a preferred embodiment. The electrolyte may contain additional organosilicon compound(s) and/or task specific additives in amounts of up to about 10 weight percent based on the total weight of the electrolyte. Such additives are known in the art or may be determined by routine experimentation.
Suitable anode materials include, but are not limited to lithium metal, lithium-metal-based alloys (for example, Li—Al, Li—Sn, and Li—Si), lithium-intercalating compounds that are typically used in lithium ion batteries (such as but not limited to graphite, mesocarbon microbead (MCMB) carbon, and soft carbon), and lithium titanate, which is also frequently used in lithium ion batteries.
The invention also encompasses cathode materials and air cathodes, such as for lithium air and/or lithium oxygen batteries. An air electrode according to the invention contains a carbon-based porous electrode (containing cathode active material, binder, and optionally oxidation reduction catalyst) and the non-aqueous electrolyte containing a lithium salt and an organosilicon compound or an alkylene additive according to the invention. Exemplary and preferred lithium salts, organosilicon compounds, and alkylene additives have been previously described.
The air cathode may be infused with or contain an oxidation reduction catalyst to facilitate oxygen reduction at the air cathode. Suitable oxidation reduction catalysts comprise at least one of electrolytic manganese (IV) dioxide, ruthenium (IV) oxide, copper (II) oxide, copper (II) hydroxide, iron (II) oxide, iron (II,III) oxide, cobalt (II,III) oxide, nickel (II) oxide, silver, platinum and iridium.
An exemplary reversible air cathode according to the invention initially contains about 14% lithium peroxide (Li2O2); however, the cell will operate effectively if the air cathode contains from about 0.5% to about 50% Li2O2. The addition of lithium peroxide to the air cathode helps facilitate the preservation of initial porosity of the air cathode. The lithium peroxide initially attaches to the porous structure of the substrate and then, when the cell is charged, the lithium peroxide participates in a chemical reaction that causes it to vacate the porous substrate, thereby increasing the porosity of the substrate. The lithium peroxide thus helps preserve the intended initial porosity by essentially serving as a placeholder for open space in the air cathode.
Battery capacity increases with increasing proportion of active carbon and porosity. Suitable porous cathode active materials include but are not limited to Calgon™ carbon (activated carbon), carbon black (such as Timcal Super P Li carbon), metal powders (such as Ni powder), activated carbon cloths, porous carbon fiber papers, and metal foams.
Suitable binders for the carbon electrodes include, but are not limited to, carboxymethyl cellulose (CMC), polyimide (PI), polyvinylidene fluoride (PVDF) fluoropolymer resin, polytetrafluoroethylene (PTFE) fluoropolymer resin, Teflon® AF amorphous fluoropolymers (Teflon® is a registered trademark of E. I. du Pont de Nemours and Company), and fluorinated ethylene propylene (FEP).
The separator included in the battery according to the invention is preferably made of a non-conductive polymer. The non-conductive polymer material may be porous, for example, in the nature of a sponge, so as to effectively hold the electrolyte described herein. Appropriate separator materials are well known in the art and need not be described. Thus, a battery according to the invention contains, in a preferred embodiment, electrolyte between the cathode and the anode, as well as electrolyte contained in the separator and in the air cathode.
The term “air” as used herein is not intended to be limited to ambient air, but includes other combinations of gases containing oxygen as well as pure oxygen. As previously noted herein, oxygen is a reactant in the electrochemical process of the invention and references to the term “air” are meant to imply that it is the oxygen in air that is applicable. Thus this broad definition of “air” applies to all uses of that term herein, including but not limited to lithium air, air battery, air cathode, and air supply.
It is to be understood that the described invention may include a battery that has not yet formed the active material of the anode or a battery which includes a preformed anode containing active material. When the battery does not yet include active anode material, the active anode material is formed upon initial charging of the battery.
The invention provides a lithium air battery (battery cell) having an electrolyte that is non-volatile, stable in contact with metallic lithium, stable against cathode oxidation during lithium air charging and able to improve the round-trip charge/discharge efficiency. The invention also provides a battery having an electrolyte that contains at least one organosilicon compound, which provides high conductivity, safety, and favorable electrochemical and chemical properties.
The invention will now be described in connection with the following, non-limiting examples. It should be understood, however, that the invention is not limited to the specific details set forth in the example. Parts and percentages set forth herein are by weight unless otherwise specified.
Cathodes were prepared by milling 3 g KS10 graphite (carbon), 3 g Super P® Li (carbon black, Timcal SA/Timcal AG/Timcal Ltd Corporation of Switzerland), 0.75 g vapor-grown carbon fiber (VGCF) 24 LD carbon fiber (such as the carbon nanofibers manufactured by Pyrograf Products, Inc., an affiliate of Applied Sciences, Inc.), 2.09 g Kynar® PVDF, 1.16 g EMD (electrolytic manganese dioxide, MnO2), and 70 g ZrO2 milling media with 130 mL acetone in a ZrO2 jar at 300 rpm for 17.5 hours in a planetary mill. The milling media was removed by passing the resulting slurry through a wire screen. Cathodes were cast by spreading the slurry at a depth of 20 mil wet thickness onto a 19 cm×39 cm sheet of 0.2 oz/yd2 (6.8 g/m2) non-woven carbon veil. The cathodes were allowed to dry under a cover with a ¼″ wide slot down the center, and cut into individual cathodes using a punch. The cathodes were then weighed and a group having a narrow mass range was selected to minimize variation due to the cathode during observation and testing.
An air cathode was prepared using a fluoropolymer resin binder as a negatively charged, hydrophobic colloid, containing approximately 60% (by total weight) of 0.05 to 0.5 μm polytetrafluoroethylene (PTFE) resin particles suspended in water containing approximately 6% (by weight of PTFE) of a nonionic wetting agent and stabilizer. To produce a Teflon®-bonded cell, a Calgon™ carbon (activated carbon, Calgon Carbon Corporation)-based air cathode was prepared by first wetting 14.22 g of Calgon™ carbon (activated carbon), 0.56 g of Acetylene Black (carbon black pigment), and 0.38 g of electrolytic manganese dioxide with a 60 ml mixture of isopropanol and water (1:2 ratio). The electrolytic manganese dioxide is an oxygen-reduction catalyst, optimally provided in a concentration of 1% to 30% by weight; ruthenium oxide, silver, platinum, or iridium could have been used as alternatives.
Next, 2.92 g of Teflon® 30 (60% Teflon® emulsion in water) were added to the above mixture, mixed, and placed in a bottle with ceramic balls to mix overnight on a roller-run jar mill. Alternatively, the slurry could be planetary milled for 6 hours. After mixing, the slurry/paste was dried in an oven at 110° C. for at least 6 hours to evaporate the water and yield a dry, fibrous mixture. The dry mixture was again wetted by a small quantity of water to form a thick paste, which was then spread over a clean glass plate (or polyester sheet). The mixture was kneaded to the desired thickness as it dried on the glass plate. After drying, it was cold pressed on an Adcote™-brand-adhesive-coated aluminum mesh at 4000 psi for 3 minutes. To remove any cracks in the paste, the cathode assembly was passed through stainless steel rollers. The cathode was then cut into smaller pieces such that the active area of the cathode was 2″ by 2″. A small portion of the aluminum mesh was exposed so that it could be used as the cathode current-collector tab.
Cell assembly was performed inside of an argon-filled glove box to reduce or eliminate undesirable effects on the lithium electrode that are caused by water (particularly water vapor, or moisture, in air).
The cathode was wetted by a non-aqueous, organic-solvent based electrolyte including a lithium salt and an alkylene carbonate and/or an alkylene siloxane additive. Specifically, the electrolyte contained lithium hexafluorophosphate dissolved in a mixture of propylene carbonate and dimethyl ether to a 1 molar concentration (1M LiPF6 in PC:DME). A pressure-sensitive, porous polymeric separator membrane, such as Policell type B38 (product of Policell Technologies, Inc.) was loaded with a non-aqueous, organic-solvent based electrolyte including a lithium salt and an alkylene additive (vinylene carbonate, butylene carbonate, or an alkylene siloxane such as triacetoxyvinylsilane. The electrolyte-loaded separator membrane was placed on the cathode with the shiny side of the membrane facing away from the cathode. Next, thin lithium foil was placed on the shiny side of the wetted separator, and a 1.5 cm by 4 cm strip of copper mesh is placed along one edge of the thin lithium foil (to serve as an anode current-collector tab), away from the aluminum-mesh cathode current-collector tab. Another cathode piece wetted by the electrolyte and covered with a second electrolyte-loaded separator was placed directly on top of the lithium foil and copper-mesh strip. This is an example of a “double-cell assembly,” illustrated schematically in
The double-cell assembly was laminated on a hot press at 100° C. and 500 lb pressure for 30 to 40 seconds. After the sample was withdrawn from the press, the heat-activated separator bound the sample together.
Completed, enclosed cells were produced comprising a cell assembly placed in an enclosure with an electrolyte and then activated for use. The cell assembly comprises the cathode-anode-separator assembly, such as the double-cell assembly described above. Although the example described above is based upon a double cell, the teachings of the invention are equally applicable to a single-cell configuration or a multiple-cell configuration other than the single anode-dual cathode configuration described. The completed cells were also assembled in a glove box to isolate the components.
Various samples of completed cells were prepared for testing, in which the liquid electrolyte employed contained no additive or one of two general types of additives: (a) 2% by weight VS (triacetoxyvinylsilane, a polymerizable silane according to the invention) or (b) 5% by weight VC (vinylene carbonate, an alkylene carbonate additive).
Liquid electrolytes used for testing were 1 M solutions of lithium trifluoromethanesulfonimide (LiTFSI) or lithium hexafluorophosphate (LiPF6). The lithium salts were used in solvent mixtures containing a 1:2 (w:w) ratio of propylene carbonate and tetraglyme (PC:Tetraglyme) or a 1:2 (w:w) ratio of propylene carbonate and 1,2-dimethoxyethane (PC:DME). Cells constructed in accordance with the teachings of the invention were sealed in an enclosure wherein oxygen or air was injected to a predetermined pressure, preferably about 0.1 atm to about 100 atm, and more preferably about 0.5 atm to about 20 atm.
Embodiments of cells incorporating the teachings of the invention and comparative cells were tested to compare their performances. Three performance characteristics were tested: Rest Voltage Before Cycling, Discharge Voltage During Second Cycle, and Charge Voltage During Second Cycle.
The results of testing were compared and analyzed utilizing the statistics methodology known as Analysis of Variance (ANOVA). Measurements taken during the second cycle exhibited differences that were considered to be statistically significant and have been described herein.
Referring to
Referring now to
Referring now to
When the VS additive was utilized in combination with a nonvolatile, liquid electrolyte such as 1 M LiTFSI in 2:1 (PC):tetraglyme, the VS additive served to increase the round-trip efficiency by reducing the charge voltage. Round-trip efficiency is a tool that may be used to compare the effectiveness of one rechargeable cell to another. Round-trip efficiency may be described as a ratio of the total discharge energy Edis (watt-hours) that is dissipated by a cell during a cycle as compared to the total energy Ech (watt hours) required to be applied to fully re-charge a cell after discharge during a cycle. The relationship may be described mathematically as follows:
wherein
As noted above, Round-Trip Efficiency is expressed as a percentage (%).
The invention provides a cell that requires a lesser amount of charge energy Ech, thus increasing the round-trip efficiency.
For testing, a standard carbon based cathode was coupled to lithium metal anode via a porous propylene separator (Celgard) to form a lithium/oxygen battery. The electrolyte solution was comprised of propylene carbonate (PC) and tetraglyme in a specific ratio with LITFSI at one molar. As shown in
A battery cell was prepared in which an air cathode was cycled versus lithium metal anode using an electrolyte containing an organosilicon compound having Formula (1) in which n=2 (obtained from Argonne National Labs, IL.) The electrolyte was composed of LiTFSI salt dissolved in 1NM2 organosilicon solvent to 1 molar. The cycling data was recorded on a Maccor battery tester and is presented in
It will be appreciated by those skilled in the art that changes could be made to the embodiments described above without departing from the broad inventive concept thereof. It is understood, therefore, that this invention is not limited to the particular embodiments disclosed, but it is intended to cover modifications within the spirit and scope of the present invention as defined by the appended claims.
This application is a continuation-in-part of co-pending U.S. patent application Ser. No. 12/752,754, filed Apr. 1, 2010, which is a continuation-in-part of U.S. patent application Ser. No. 11/843,814 filed Aug. 23, 2007, and further claims priority to U.S. patent application No. 61/558,553, filed Nov. 11, 2011, the entirety of which are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 61558553 | Nov 2011 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 12752754 | Apr 2010 | US |
| Child | 13675579 | US | |
| Parent | 11843814 | Aug 2007 | US |
| Child | 12752754 | US |
