Patent Application
20230197975
None.
Batteries are increasingly becoming more important as several applications requiring a portable source of energy are entering the consumer market. Portable electronics like smart phones, tablets, laptops, etc. are becoming multifunctional and are requiring higher energy densities to operate for longer periods of time. Even health care portable ventilators are being introduced in case there is no electricity available from the grid. Electric vehicles are another major driver of higher energy and power density batteries, where long cycle life and rate performance are few of the essential requirements. As batteries become more integrated into devices that consumers often interact with, these batteries need to satisfy stringent safety requirements and need to contain materials that are non-flammable and non-toxic.
Lithium (Li)-ion batteries are usually proposed and used as the battery of choice in personal electronics because of their relatively high energy density characteristics; however, the Li-ion batteries contain flammable electrolyte and elements like cobalt that can be a catalyst for exothermic reactions and are highly toxic. Additionally, there is the ethical issue of mining cobalt from the mines in Congo, where the artisanal miners are not afforded proper protection. Unfortunately, Li-ion batteries will continue to be used unless there is a suitable alternative.
Metal aqueous batteries like zinc (Zn) anode batteries are attractive compared to non-aqueous batteries like lithium-ion, lithium metal, lithium-sulfur, and magnesium-ion because of their non-flammability, non-toxicity and moderate energy density. The most widely used Zn-anode battery is the conventional manganese dioxide (MnO2)|Zn battery, where it is used in primary battery industry for small-scale applications like remote controls, house clocks, etc. The wide scale use of the conventional MnO2|Zn battery in other applications has been limited because of its relatively low nominal voltage of about 1.2 V to 1.3 V and its non-rechargeable nature. The aqueous nature of the electrolyte and the reactions of the active materials in either alkaline, acidic or neutral solutions has limited the working potential window of the battery less than about 1.5 V. The relatively limited working potential window of the conventional MnO2|Zn battery has long been considered a disadvantage and this has led to various relatively high voltage non-aqueous batteries to replacing it. An ongoing need exists for batteries that are both non-flammable and non-toxic while displaying a relatively wide working potential window.
In some embodiments, a high voltage zinc (Zn)-anode battery comprises a cathode comprising a cathode electroactive material; an anode comprising a Zn electroactive material; a catholyte in contact with the cathode, wherein the catholyte is not in contact with the anode; an anolyte in contact with the anode, wherein the anolyte is not in contact with the cathode; and a separator disposed between the anolyte and the catholyte. The catholyte has a pH of less than 4, and the anolyte has a pH of greater than 10. The separator has ion-selective properties.
In some embodiments, a method of forming a high voltage zinc (Zn)-anode battery comprises disposing a catholyte in contact with a cathode comprising a cathode electroactive material; disposing an anolyte in contact with an anode comprising a Zn electroactive material; and disposing a separator between the anolyte and the catholyte, wherein the catholyte is not in contact with the anode, and wherein the anolyte is not in contact with the cathode. The catholyte has a pH of less than 4, and the anolyte has a pH of greater than 10. The separator has ion-selective properties.
These and other features will be more clearly understood from the following detailed description taken in conjunction with the accompanying claims.
For a more complete understanding of the present disclosure and the advantages thereof, reference is now made to the following brief description, taken in connection with the accompanying drawings and detailed description, wherein like reference numerals represent like parts.
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.” Reference to an “electrode” alone can refer to the anode, cathode, or both. Reference to the term “primary battery” (e.g., “primary battery,” “primary electrochemical cell,” or “primary cell”), refers to a cell or battery that after a single discharge is disposed of and replaced. Reference to the term “secondary battery” (e.g., “secondary battery,” “secondary electrochemical cell,” or “secondary cell”), refers to a cell or battery that can be recharged one or more times and reused. As used herein, a “catholyte” refers to an electrolyte solution in contact with the cathode without being in direct contact with the anode, and an “anolyte” refers to an electrolyte solution in contact with the anode without being in direct contact with the cathode. The term electrolyte alone can refer to the catholyte, the anolyte, or an electrolyte in direct contact with both the anode and the cathode.
Energy storage systems like batteries are required for a range of applications like grid-based, electric vehicles, solar storage, uninterruptible power sources, etc. Lithium-ion and lead acid batteries currently dominate the market; however, they are expensive, flammable and contain toxic elements. Aqueous based metal anode systems like zinc (Zn)-anode batteries can compete with lithium and lead on volumetric and gravimetric energy densities when paired with a cheap and abundant material cathode like manganese dioxide (MnO2). These batteries can deliver >400 Wh/L in aqueous alkaline electrolyte. The high energy density is possible because of the high theoretical capacity of MnO2 and Zn which is around 617 mAh/g and 820 mAh/g based on the first and second electron reactions, respectively.
The irreversibility arises when maximum utilization is tried to be attained which leads to problems like volume expansion, breakdown of crystal structure to form spinels, redistribution of active material, zinc poisoning of the cathode, passivation of the metallic anode and dendritic shorts. The electrolyte, potassium hydroxide (KOH), is the source of some of the problems mentioned. During discharge the 4+ state of Mn reduces to the 3+ state which leads to an increase in its solubility in high KOH concentration at high capacity utilization. The loss of active Mn3+ ions is the cause of capacity loss in the battery. Also, the dissolved Mn3+ ions can also dissociate to form Mn4+ and Mn2+ ions which can lead to the formation of lower oxides like spinels Mn3O4 and pyrochroite [Mn(OH)2]. The reactions get complicated further as Zn delivers its capacity through a dissolution reaction where it forms dissolved zincate ions [Zn(OH)42−]. These dissolved zincate ions also react with the dissolved Mn ions to form inactive Zn spinels like ZnMn2O4. The Zn anodes can also form dendrites during charge which can penetrate the separator to short the battery.
Another problem of the Zn anodes is the active redistribution of the active materials during the dissolution reaction, which leads to a loss of active ions from the current collector and thus, loss in capacity. The cathode also undergoes large volume expansion during its discharge reaction as the protons from the electrolyte intercalate into the crystal structure and this leads to the active material denuding from the current collector and thus, loss in capacity again.
In this disclosure, a high voltage aqueous Zn-anode battery is disclosed, wherein the high voltage aqueous Zn-anode battery has rechargeable characteristics and can act as a primary source of power or energy as well. The high voltage of the battery in this disclosure relates to the battery having a discharge potential between 2 V and 5 V in an aqueous (acid and/or alkaline) electrolyte with Zn as the anode. The high voltage of the battery is achieved through decoupling electrolytes for the cathode and anode side and altering the hydrogen and hydroxyl activity, respectively. The higher the activity (e.g., hydrogen activity, hydroxyl activity), the higher the potential or voltage of the battery. Rechargeability is achieved in this battery system through the addition of dopants or additives to the electrolyte and/or electrodes, as described in more detail below.
In this disclosure, a method of making high voltage Zn aqueous batteries through altering the hydrogen (or proton) and hydroxyl activity for the cathode and anode sides of the battery is disclosed. Generally, a MnO2 cathode can provide for a MnO2|Zn battery to cycle between 1 V and 5 V. Specifically, a MnO2 cathode can provide for a high voltage aqueous MnO2|Zn battery as disclosed herein to cycle between 2 V and 5 V. Altering (e.g., increasing) the hydrogen activity on the MnO2 cathode can increase the discharge potential of a MnO2|Zn battery between 3 and 3.5 V as disclosed herein, which is the highest discharge potential achieved for this chemistry. The high voltage aqueous MnO2|Zn battery as disclosed herein can discharge the theoretical two electron capacity (617 mAh/g) of MnO2 reversibly for thousands of cycles. The high voltage aqueous MnO2|Zn battery as disclosed herein can be also used for primary or single use applications.
In some embodiments, the cathode electroactive material suitable for use in the cathode of the high voltage aqueous Zn-anode battery as disclosed herein may comprise manganese dioxide (MnO2), manganese oxides (Mn2O3, Mn3O4, MnO), manganese hydroxides (MnOOH, Mn(OH)2), silver oxides (AgO, Ag2O), silver (Ag), nickel (Ni), nickel oxide (NiO, Ni2O3), nickel hydroxides (NiOOH, Ni(OH)2), cobalt oxide (Co3O4, CoO), cobalt hydroxides, lead (Pb), lead oxide (PbO, PbO2), copper (Cu) oxide, Cu, copper hydroxide, potassium iron oxide (K2FeO4), barium iron oxide (BaFeO4), copper hexacyanoferrate, lithium iron phosphate, lithium nickel manganese cobalt oxide, lithium manganese oxide (LiMn2O4, Li2MnO3), or any combination thereof.
In this disclosure, the high voltage aqueous Zn-anode battery may employ a MnO2 cathode. The MnO2 cathode is most famously paired with a Zn anode in the primary alkaline battery, wherein its open circuit potential is usually around 1.5 to 1.7 V. The average discharge potential of this battery (MnO2|Zn) is about 1.3 V. The MnO2|Zn battery has a relatively very high theoretical capacity of 617 mAh/g based on two electron reactions. The MnO2|Zn battery displays rechargeable characteristics relative to its one-electron (308 mAh/g) and two-electron (617 mAh/g) capacities in alkaline electrolytes. Despite advantageous relatively high capacity characteristics of the MnO2|Zn battery, its relatively high voltage has been considered an Achilles heel for use in applications like personal electronics. As disclosed herein, by altering the hydrogen and hydroxyl activity in the catholyte and anolyte of the MnO2 and Zn electrodes, respectively, the average discharge potential of this battery system can be advantageously increased to equal to or greater than about 3 V. The conventional MnO2|Zn battery chemistry in either aqueous or non-aqueous electrolyte does not achieve a discharge potential of equal to or greater than about 3 V. The high voltage aqueous MnO2|Zn battery as disclosed herein exhibiting a discharge potential of equal to or greater than about 3 V can open its use in personal electronics, electric vehicles and other important applications powering the modern green economy.
Rechargeable characteristics of the MnO2|Zn battery can be obtained by the addition of dopants or additives to the electrodes and/or electrolytes. The anode material can contain additives that enhance electrochemical activity and reduce gassing in the electrolyte. For electrode dopants, bismuth oxide, bismuth, indium, indium oxide, indium hydroxide, copper oxide, copper, aluminum oxide, aluminum, lead oxide, lead, bismuth sulfide, silver oxide, silver, nickel, nickel oxide, nickel hydroxide, cobalt and cobalt oxide, and any salts thereof, or any combination thereof can be used in both the cathode and the anode. Zn electrodes tend to gas in electrolytes with high hydroxyl activity. For inhibiting gassing of Zn electrodes, additives like bismuth, bismuth oxide, indium, indium oxide, indium hydroxide, cationic surfactants like cetyltrimethylammonium bromide, anion surfactants like sodium dodecyl sulfate, sodium dodecylbenzene sulfonate, polyethylene glycol, zinc oxide, carboxymethyl cellulose, polyvinyl alcohol, or any combination thereof can be used. Electrolyte additives (e.g., catholyte additive) can include manganese sulfate, nickel sulfate, potassium permanganate, manganese chloride, manganese acetate, manganese triflate, bismuth chloride, bismuth nitrate, manganese nitrate, nickel sulfate, nickel nitrate, zinc sulfate, zinc chloride, zinc acetate, zinc triflate, indium chloride, copper sulfate, copper chloride, lead sulfate, sodium persulfate, potassium persulfate, ammonium persulfate, ammonium chloride, vanillin, potassium chloride, sodium chloride, or any combination thereof.
The separation of electrolytes of varying strengths can be important to prevent any neutralization reactions from taking place. In some embodiments, the separation of electrolytes can be achieved by gelling the electrolytes which physically prevents them from mixing. Use of crosslinkers and ionomers in the gelling process can also prevent the crossover of ions, which would allow for the use of cellulose-based separators like cellophane and polymer-based separators like polyvinyl alcohol or cross-linked polyvinyl alcohol. The electrolyte gelling process can be done through the use of free radical polymerization process. Acrylamides and acrylic acids can be made into long polymer chains by mixing with either electrolytes of high proton or hydroxyl activity. Crosslinkers like N,N′-methylenebisacrylamide (MBA) can be used to increase the strength of the polymers and make it more viscous and impart it self-healing properties. The gelling or polymerization of electrolytes can be conducted with the use of initiators like potassium or sodium or ammonium persulfate. In some embodiments, preventing the mixing of the electrolytes can be achieved by using ion selective ceramic separators or membranes like LiSiCON, NaSiCON, Nafion membranes, anion-exchange membranes, bipolar membranes, or any combination thereof.
An advantage of having a dual electrolyte cell with relatively high proton activity in the catholyte on the cathode side and relatively high hydroxyl activity in the anolyte on the anode side is an increase in cell potential. A relatively high proton activity on the cathode side and a relatively high hydroxyl activity on the anode side can increase the cell potential, which in turn can lead to higher average discharge voltages and thus, higher energy from the cell.
Disclosed herein is an aqueous Zn-anode battery that can deliver its average discharge capacity between 2 and 5 V with an operational range between 0 and 5 V, where the battery has both single use and rechargeable characteristics. As an example, in this disclosure it is shown for the first time an average discharge potential of a MnO2|Zn system of greater than about 3 V.
In this disclosure, the high voltage aqueous Zn-anode battery is characterized by an average discharge potential between 2 and 5 V. This relatively high discharge potential can be achieved through decoupling of electrolytes with different strengths related to hydrogen (or proton) and hydroxyl activity. The high voltage aqueous Zn-anode battery can be of single use or can be made rechargeable. In some embodiments, long term rechargeability of the high voltage aqueous Zn-anode battery can be obtained through the use of additives and/or dopants. The separation of anode and cathode in the high voltage aqueous Zn-anode battery can be achieved through gelation of electrolytes with ion-selective ionomers embedded in them to prevent any neutralization by ion-migration. Separation of the anolyte and catholyte can also be obtained by the use of ion-selective ceramic and/or polymeric membranes.
In this disclosure, the high voltage aqueous Zn-anode battery can be made of any geometric form factor if desired. To those skilled in the art, the high voltage aqueous Zn-anode battery can be cylindrical or prismatic. Further, the high voltage aqueous Zn-anode battery can also be made flexible if desired by gelling of electrolytes and electrodes or by using binders in electrodes that allow for flexibility.
Referring to
In some embodiments, the battery 10 can comprise one or more cathodes 12 and one or more anodes 13, which can be present in any configuration or form factor. When a plurality of anodes 13 and/or a plurality of cathodes 12 are present, the electrodes can be configured in a layered configuration such that the electrodes alternate (e.g., anode, cathode, anode, etc.). Any number of anodes 13 and/or cathodes 12 can be present to provide a desired capacity and/or output voltage. In the jellyroll configuration (e.g., as shown in
In an embodiment, housing 7 comprises a molded box or container that is generally non-reactive with respect to the electrolyte solutions in the battery 10, including the electrolyte. In an embodiment, the housing 7 comprises a polymer (e.g., a polypropylene molded box, an acrylic polymer molded box, etc.), a coated metal, or the like.
The cathode 12 can comprise a mixture of components including an electrochemically active material (e.g., cathode electroactive material). Additional components such as a binder, a conductive material, and/or one or more additional components can also be optionally included that can serve to improve the lifespan, rechargeability, and electrochemical properties of the cathode 12. The cathode 12 can comprise a cathode material 2 (e.g., an electroactive material, additives, etc.). The cathode can comprise between about 1 wt. % and about 95 wt. % active material. Suitable cathode materials 2 can include, but are not limited to, manganese dioxide, copper manganese oxide, hausmannite, manganese oxide, copper intercalated bismuth birnessite, birnessite, todokorite, ramsdellite, pyrolusite, pyrochroite, silver oxide, silver dioxide, silver, nickel oxyhydroxide, nickel hydroxide, nickel, lead oxide, copper oxide, copper dioxide, lead, lead dioxide (α and β), potassium persulfate, sodium persulfate, ammonium persulfate, potassium permanganate, calcium permanganate, barium permanganate, silver permanganate, ammonium permanganate, peroxide, gold, perchlorate, cobalt oxide (CoO, CoO2, Co3O4), lithium cobalt oxide, sodium cobalt oxide, perchlorate, nickel oxide, bromine, mercury, vanadium oxide, bismuth vanadium oxide, hydroquinone, calix[4]quinone, tetrachlorobenzoquinone, 1,4-naphthoquinone, 9,10-anthraquinone, 1,2-napthaquinone, 9,10-phenanthrenequinone, nitroxide-oxammonium cation redox pair like 2,2,6,6-tetramethylpiperidin-1-yl)oxyl (TEMPO), carbon, 2,3-dicyano-5,6-dichlorodicyanoquinone, tetracyanoethylene, sulfur trioxide, ozone, oxygen, air, lithium nickel manganese cobalt oxide, sulfur, lithium iron phosphate, lithium copper oxide, lithium copper oxyphosphate, or any combination thereof. In some embodiments, the cathode can comprise an air electrode.
In some embodiments, the cathode material 2 can be based on one or many polymorphs of MnO2, including electrolytic manganese dioxide (EMD), α-MnO2, β-MnO2, γ-MnO2, δ-MnO2, ε-MnO2, or λ-MnO2. Other forms of MnO2 can also be present such as hydrated MnO2, pyrolusite, birnessite, ramsdellite, hollandite, romanechite, todorokite, lithiophorite, chalcophanite, sodium or potassium rich birnessite, cryptomelane, buserite, manganese oxyhydroxide (MnOOH), α-MnOOH, γ-MnOOH, β-MnOOH, manganese hydroxide [Mn(OH)2], partially or fully protonated manganese dioxide, Mn3O4, Mn2O3, bixbyite, MnO, lithiated manganese dioxide (LiMn2O4, Li2MnO3), CuMn2O4, aluminum manganese oxide, zinc manganese dioxide, bismuth manganese oxide, copper intercalated birnessite, copper intercalated bismuth birnessite, tin doped manganese oxide, magnesium manganese oxide, or any combination thereof. In general, the cycled form of manganese dioxide in the cathode can have a layered configuration, which in some embodiment can comprise δ-MnO2 that is interchangeably referred to as birnessite. If non-birnessite polymorphic forms of manganese dioxide are used, these can be converted to birnessite in-situ by one or more conditioning cycles as described in more details below. For example, a full or partial discharge to the end of the MnO2 second electron stage (e.g., between about 20% to about 100% of the 2nd electron capacity of the cathode) may be performed and subsequently recharging back to its Mn4+ state, resulting in birnessite-phase manganese dioxide.
In some embodiments, the cathode 12 used in the high voltage aqueous Zn-anode battery as disclosed herein can contain electroactive materials like metal, metal oxides, metal salts (e.g., metal sulfides), electroactive polymers, electroactive organic compounds, etc. that have electrochemical activity in electrolytes of high proton activity, such as in the catholyte 3. Nonlimiting examples of cathode materials 2 that have electrochemical activity in electrolytes of high proton activity include electrolytic manganese dioxide (EMD), α-MnO2, β-MnO2, γ-MnO2, δ-MnO2, ε-MnO2, λ-MnO2, or any combination thereof. Other forms of MnO2 can also be present in the cathode 12, such as pyrolusite, birnessite, ramsdellite, hollandite, romanechite, todorokite, lithiophorite, chalcophanite, sodium rich birnessite, potassium rich birnessite, cryptomelane, buserite, manganese oxyhydroxide (MnOOH), α-MnOOH, γ-MnOOH, β-MnOOH, manganese hydroxide [Mn(OH)2], partially or fully protonated manganese dioxide, Mn3O4, Mn2O3, bixbyite, MnO, lithiated manganese dioxide (LiMn2O4), CuMn2O4, zinc manganese dioxide, lead oxide, lead, lead dioxide, copper, copper oxide, copper hydroxide, silver, silver oxide, nickel, nickel oxide, nickel hydroxide, nickel oxyhydroxide, cobalt oxide, cobalt, cobalt hydroxide, lithium nickel manganese cobalt oxide, lithium nickel oxide, lithium manganese oxide, lithium cobalt oxide, lithium iron phosphate, potassium iron oxide, barium iron oxide, copper hexacyanoferrate, delithiated manganese oxides, delithiated nickel oxides, delithiated nickel manganese oxides, delithiated nickel manganese cobalt oxides, quinone compounds like calix[4]quinone, 1,4-napththoquinone, 9,10-anthraquinone, or any combination thereof. Combinations of electroactive materials can also be employed in the cathode materials 2. The electroactive cathode materials 2 can be in the form of powders of varying particle sizes (nanometers to micrometers) and/or in the form of metallic substrates with planar, mesh or perforated-type architecture.
The addition of a conductive additive such as conductive carbon enables high loadings of an electroactive material in the cathode material, resulting in high volumetric and gravimetric energy density. In some embodiments, the conductive additive can be present in the cathode material 2 in an amount of about 1-30 wt. %, based on the total weight of the cathode material 2. In some embodiments, the conductive additive can comprise graphite, carbon fiber, carbon black, acetylene black, single walled carbon nanotubes, multi-walled carbon nanotubes, nickel or copper coated carbon nanotubes, dispersions of single walled carbon nanotubes, dispersions of multi-walled carbon nanotubes, graphene, graphyne, graphene oxide, or a combination thereof. Higher loadings of the electroactive material in the cathode are, in some embodiments, desirable to increase the energy density. Other examples of conductive carbon include TIMREX Primary Synthetic Graphite (all types), TIMREX Natural Flake Graphite (all types), TIMREX MB, MK, MX, KC, B, LB Grades (examples, KS15, KS44, KC44, MB15, MB25, MK15, MK25, MK44, MX15, MX25, BNB90, LB family) TIMREX Dispersions; ENASCO 150 G, 210 G, 250 G, 260 G, 350 G, 150 P, 250 P; SUPER P , SUPER P Li, carbon black (examples include Ketjenblack EC-300J, Ketjenblack EC-600JD, Ketjenblack EC-600JD powder), acetylene black, carbon nanotubes (single or multi-walled), Zenyatta graphite, and/or combinations thereof.
In some embodiments, the conductive additive can have a particle size range from about 1 to about 50 microns, or between about 2 and about 30 microns, or between about 5 and about 15 microns. In an embodiment, the conductive additive can include expanded graphite having a particle size range from about 10 to about 50 microns, or from about 20 to about 30 microns. Carbon fibers and nanotubes can have varying aspect ratios where their diameters can be in the tens to hundreds of nanometers. In some embodiments, the mass ratio of graphite to the conductive additive can range from about 5:1 to about 50:1, or from about 7:1 to about 28:1. The total conductive additive mass percentage (e.g., total carbon mass percentage) in the cathode material 2 can range from about 5% to about 99%, or from about 10% to about 80%. In some embodiments, the electroactive component in the cathode material 2 can be between 1 and 99 wt. % of the weight of the cathode material 2, and the conductive additive can be between 1 and 99 wt. % of the weight of the cathode material 2.
In some embodiments, dopants or additives can be added to the cathode material 2, as necessary to enhance rechargeability and performance. The additives can be in the form of powders mixed with the electroactive material or in the form of metallic substrates onto which the electroactive and conductive carbon can be pasted onto. Nonlimiting examples of additives suitable for use in the electrode materials of this disclosure include bismuth, bismuth oxide, copper oxide, copper, indium, indium hydroxide, indium oxide, aluminum, aluminum oxide, nickel, nickel hydroxide, nickel oxide, silver, silver oxide, cobalt, cobalt oxide, cobalt hydroxide, lead, lead oxide, lead dioxide, quinones, salts thereof, derivatives thereof, or any combination thereof. In some embodiments, the dopants or additives can be present in the cathode material 2 in an amount between 0 to 30 wt. %, based on the total weight of the cathode material 2.
In some embodiments, the cathode material 2 can also comprise a conductive component. The addition of a conductive component such as metal additives to the cathode material 2 may be accomplished by addition of one or more metal powders such as nickel powder to the cathode material 2. The conductive metal component can be present in a concentration of between about 0-30 wt. % in the cathode material 2. The conductive metal component may be, for example, nickel, copper, silver, gold, tin, cobalt, antimony, brass, bronze, aluminum, calcium, iron, or platinum. In one embodiment, the conductive metal component is a powder. In some embodiments, the conductive component can be added as an oxide and/or salt. For example, the conductive component can be cobalt oxide, cobalt hydroxide, lead oxide, lead hydroxide, or a combination thereof In some embodiments, a second conductive metal component is added to act as a supportive conductive backbone for the first and second electron reactions to take place. The second electron reaction has a dissolution-precipitation reaction where Mn3+ ions become soluble in the electrolyte and precipitate out on the materials such as graphite resulting in an electrochemical reaction and the formation of manganese hydroxide [Mn(OH)2] which is non-conductive. This ultimately results in a capacity fade in subsequent cycles. Suitable conductive components that can help to reduce the solubility of the manganese ions include transition metals like Ni, Co, Fe, T
i and metals like Ag, Au, Al, Ca. Oxides and salts of such metals are also suitable. Transition metals like Co can also help in reducing the solubility of Mn3+ ions. Such conductive metal components may be incorporated into the electrode by chemical means or by physical means (e.g. ball milling, mortar/pestle, spex mixture). An example of such an electrode comprises 5-95% birnessite, 5-95% conductive carbon, 0-50% conductive component (e.g., a conductive metal), and 1-10% binder.
In some embodiments, a binder can be used with the cathode material 2. The binder can be present in a concentration of between about 0-10 wt. %, or alternatively between about 1-5 wt. % by weight of the cathode material. In some embodiments, the binder comprises water-soluble cellulose-based hydrogels, which can be used as thickeners and strong binders, and have been cross-linked with good mechanical strength and with conductive polymers. The binder may also be a cellulose film sold as cellophane. The binders can be made by physically cross-linking the water-soluble cellulose-based hydrogels with a polymer through repeated cooling and thawing cycles. In some embodiments, the binder can comprise a 0-10 wt. % carboxymethyl cellulose (CMC) solution cross-linked with 0-10 wt. % polyvinyl alcohol (PVA) on an equal volume basis. The binder, compared to the traditionally-used TEFLON® or PTFE (polytetrafluoroethylene), shows superior performance. TEFLON® or PTFE is a very resistive material, but its use in the industry has been widespread due to its good rollable properties. This, however, does not rule out using TEFLON® or PTFE as a binder. Mixtures of TEFLON® or PTFE with the aqueous binder and some conductive carbon can be used to create rollable binders. Using the aqueous-based binder can help in achieving a significant fraction of the two-electron capacity with minimal capacity loss over many cycles. In some embodiments, the binder can be water-based, have superior water retention capabilities, adhesion properties, and help to maintain the conductivity relative to an identical cathode using a PTFE binder instead. Examples of suitable water-based hydrogels can include, but are not limited to, methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroypropyl cellulose (HPH), hydroypropylmethyl cellulose (HPMC), hydroxethylmethyl cellulose (HEMC), carboxymethylhydroxyethyl cellulose, hydroxyethyl cellulose (HEC), and combinations thereof. Examples of crosslinking polymers include polyvinyl alcohol, polyvinylacetate, polyaniline, polyvinylpyrrolidone, polyvinylidene fluoride, polypyrrole, and combinations thereof. In some embodiments, a 0-10 wt. % solution of water-cased cellulose hydrogen can be cross-linked with a 0-10 wt. % solution of crosslinking polymers by, for example, repeated freeze/thaw cycles, radiation treatment, and/or chemical agents (e.g., epichlorohydrin). The aqueous binder may be mixed with 0-5% PTFE to improve manufacturability.
The cathode material 2 can also comprise additional elements. The additional elements can be included in the cathode material including a bismuth compound and/or copper/copper compounds, which together allow improved galvanostatic battery cycling of the cathode. When present as birnessite, the copper and/or bismuth can be incorporated into the layered nanostructure of the birnessite. The resulting birnessite cathode material can exhibit improved cycling and long-term performance with the copper and bismuth incorporated into the crystal and nanostructure of the birnessite.
The bismuth compound can be incorporated into the cathode 12 as an inorganic or organic salt of bismuth (oxidation states 5, 4, 3, 2, or 1), as a bismuth oxide, or as bismuth metal (i.e., elemental bismuth). The bismuth compound can be present in the cathode material at a concentration between about 1-20 wt. % of the weight of the cathode material 2. Examples of bismuth compounds include bismuth chloride, bismuth bromide, bismuth fluoride, bismuth iodide, bismuth sulfate, bismuth nitrate, bismuth trichloride, bismuth citrate, bismuth telluride, bismuth selenide, bismuth subsalicylate, bismuth neodecanoate, bismuth carbonate, bismuth subgallate, bismuth strontium calcium copper oxide, bismuth acetate, bismuth trifluoromethanesulfonate, bismuth nitrate oxide, bismuth gallate hydrate, bismuth phosphate, bismuth cobalt zinc oxide, bismuth sulphite agar, bismuth oxychloride, bismuth aluminate hydrate, bismuth tungsten oxide, bismuth lead strontium calcium copper oxide, bismuth antimonide, bismuth antimony telluride, bismuth oxide yttria stabilized (e.g., yttria doped bismuth oxide), bismuth-lead alloy, ammonium bismuth citrate, 2-napthol bismuth salt, dichloritri(o-tolyl)bismuth, dichlorodiphenyl(p-tolyl)bismuth, triphenylbismuth, and/or combinations thereof.
The copper compound can be incorporated into the cathode 12 as an organic or inorganic salt of copper (oxidation states 1, 2, 3, or 4), as a copper oxide, or as copper metal (i.e., elemental copper). The copper compound can be present in a concentration between about 1-70 wt. % of the weight of the cathode material 2. In some embodiments, the copper compound is present in a concentration between about 5-50 wt. % of the weight of the cathode material 2. In other embodiments, the copper compound is present in a concentration between about 10-50 wt. % of the weight of the cathode material 2. In yet other embodiments, the copper compound is present in a concentration between about 5-20 wt. % of the weight of the cathode material 2. Examples of copper compounds include copper and copper salts such as copper aluminum oxide, copper (I) oxide, copper (II) oxide and/or copper salts in a +1, +2, +3, or +4 oxidation state including, but not limited to, copper nitrate, copper sulfate, copper chloride, etc. The effect of copper is to alter the oxidation and reduction voltages of bismuth. This results in a cathode with full reversibility during galvanostatic cycling, as compared to a bismuth-modified MnO2 which cannot withstand galvanostatic cycling as well.
The cathodes 12 can be produced using methods implementable in large-scale manufacturing. For a MnO2 cathode, the cathode 12 can be capable of delivering the full second electron capacity of the MnO2. In some embodiments, the cathode material 2 can comprises 2-30 wt. % conductive carbon, 0-30 wt. % conductive metal additive, 1-70 wt. % copper compound, 1-20 wt. % bismuth compound, 0-10 wt. % binder and birnessite or EMD. In another embodiment, the cathode material comprises 2-30 wt. % conductive carbon, 0-30 wt. % conductive metal additive, 1-20%wt. bismuth compound, 0-10 wt. % binder and birnessite or EMD. In one embodiment, the cathode material consists essentially of 2-30 wt. % conductive carbon, 0-30 wt. % conductive metal additive, 1-70 wt. % copper compound, 1-20 wt. % bismuth compound, 0-10 wt. % binder, and the balance is birnessite or EMD. In another embodiment, the cathode material consists essentially of 2-30 wt. % conductive carbon, 0-30 wt. % conductive metal additive, 1-20 wt. % bismuth compound, 0-10 wt. % binder, and the balance is birnessite or EMD.
The resulting cathode may have a porosity in the range of 20%-85% as determined by mercury infiltration porosimetry. The porosity can be measured according to ASTM D4284-12 “Standard Test Method for Determining Pore Volume Distribution of Catalysts and Catalyst Carriers by Mercury Intrusion Porosimetry” using the version as of the date of the filing of this application.
The cathode material 2 can be formed on a cathode current collector 1 formed from a conductive material that serves as an electrical connection between the cathode material and an external electrical connection or connections. In some embodiments, the cathode current collector 1 can be, for example, carbon, lead, nickel, steel (e.g., stainless steel, etc.), nickel-coated steel, nickel plated copper, tin-coated steel, copper plated nickel, silver coated copper, copper, magnesium, aluminum, tin, iron, platinum, silver, gold, titanium, bismuth, half nickel and half copper, or any combination thereof. In some embodiments, the current collector 1 can comprise a carbon felt, carbon foam, a conductive polymer mesh, or any combination thereof. The cathode current collector may be formed into a mesh (e.g., an expanded mesh, woven mesh, etc.), perforated metal, foam, foil, felt, fibrous architecture, porous block architecture, perforated foil, wire screen, a wrapped assembly, or any combination thereof. In some embodiments, the current collector can be formed into or form a part of a pocket assembly, where the pocket can hold the cathode material 2 within the current collector 1. A tab (e.g., a portion of the cathode current collector 1 extending outside of the cathode material 2 as shown at the top of the cathode 12 in
The cathode material 2 can be pressed onto the cathode current collector 1 to form the cathode 12. For example, the cathode material 2 can be adhered to the cathode current collector 1 by pressing at, for example, a pressure between 1,000 psi and 20,000 psi (between 6.9×106 and 1.4×108 Pascals). The cathode material 2 may be adhered to the cathode current collector 1 as a paste. The resulting cathode 12 can have a thickness of between about 0.1 mm to about 5 mm.
In some embodiments, the anode material 5 can comprise an electroactive material, which can be Zn. Zn can exist in powder form or as a metallic structure in the anode material 5. The Zn powder can be of varying sizes ranging from nanometers to microns. The Zn metallic structure can be a foil, mesh, perforated foil, foam, sponge-type, or any combination thereof.
While the current disclosure is discussed in detail in the context of a Zn anode, it should be understood that other anode electroactive materials (e.g., metals other than Zn) can be used to form a high voltage aqueous metal-anode battery. For example, the use of the electrolytes having different properties as described herein can allow for a variety of anode materials to be used. In some embodiments, the anode can comprise lithium, zinc, aluminum, magnesium, iron, calcium, strontium, lanthanum, potassium, sodium, zirconium, titanium, titanium oxide, indium, indium oxide, indium hydroxide, zinc oxide, Mn3O4, hetaerolite (ZnMn2O4), vanadium, tin, tin oxide, barium hydroxide, barium, cesium, aluminum hydroxide, copper, bismuth, silicon, carbon and a mixture of any of these materials. The cells as described herein can be formed by pairing of any of the cathode materials described herein and any of the anode materials as described to the extent that the materials mentioned above to generate a voltage in the presence of suitable electrolytes (e.g., a suitable anolyte and catholyte, etc.).
In some embodiments, the anode material 5 can comprise zinc, which can be present as elemental zinc and/or zinc oxide. In some embodiments, the Zn anode mixture comprises Zn, zinc oxide (ZnO), an electronically conductive material, and a binder. The Zn may be present in the anode material 5 in an amount of from about 50 wt. % to about 90 wt. %, alternatively from about 60 wt. % to about 80 wt. %, or alternatively from about 65 wt. % to about 75 wt. %, based on the total weight of the anode material. Additional elements that can be in the anode in addition to the zinc or in place of the zinc include, but are not limited to, lithium, aluminum, magnesium, iron, cadmium and a combination thereof, where each element can be present in amounts that are the same or similar to that of the zinc described herein.
In some embodiments, the anode material 5 can comprise zinc oxide (ZnO), which can be formed into Zn by a charging step in situ during battery operation. In some embodiments, the anode material 5 can comprise ZnO in an amount of from about 5 wt. % to about 20 wt. %, alternatively from about 5 wt. % to about 15 wt. %, or alternatively from about 5 wt. % to about 10 wt. %, based on the total weight of anode material. As will be appreciated by one of skill in the art, and with the help of this disclosure, the purpose of the ZnO in the anode mixture is to provide a source of Zn during the recharging steps, and the zinc present can be converted between zinc and zinc oxide during charging and discharging phases.
In an embodiment, an electrically conductive material may be optionally present in the anode material in an amount of from about 5 wt. % to about 20 wt. %, alternatively from about 5 wt. % to about 15 wt. %, or alternatively from about 5 wt. % to about 10 wt. %, based on the total weight of the anode material. As will be appreciated by one of skill in the art, and with the help of this disclosure, the electrically conductive material can be used in the anode mixture as a conducting agent, e.g., to enhance the overall electric conductivity of the anode mixture. Non-limiting examples of electrically conductive material suitable for use can include any of the conductive carbons described herein such as carbon, graphite, graphite powder, graphite powder flakes, graphite powder spheroids, carbon black, activated carbon, conductive carbon, amorphous carbon, glassy carbon, and the like, or combinations thereof. The conductive material can also comprise any of the conductive carbon materials described with respect to the cathode material including, but not limited to, acetylene black, single walled carbon nanotubes, multi-walled carbon nanotubes, graphene, graphyne, or any combinations thereof. In some embodiments, the electrically conductive material used in the anode mixture can comprise a metallic conductive powder, wherein the metallic conductive powder comprises copper, bismuth, indium, nickel, silver, tin, etc., or any combination thereof.
The anode material 5 may also comprise a binder. Generally, a binder functions to hold the electroactive material particles together and in contact with the current collector. The binder can be present in a concentration of 0-10 wt. %. The binders in the anode material 5 can also comprise any of the binders described herein with respect to the cathode material. The binders may comprise water-soluble cellulose-based hydrogels like methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroypropyl cellulose (HPH), hydroypropylmethyl cellulose (HPMC), hydroxethylmethyl cellulose (HEMC), carboxymethylhydroxyethyl cellulose and hydroxyethyl cellulose (HEC), which can be used as thickeners and strong binders, and have been cross-linked with good mechanical strength and with conductive polymers like polyvinyl alcohol, polyvinylacetate, polyaniline, polyvinylpyrrolidone, polyvinylidene fluoride and polypyrrole. The binder may also be a cellulose film sold as cellophane. The binder may also be PTFE, which is a very resistive material, but its use in the industry has been widespread due to its good rollable properties. In some embodiments, the binder may be present in the anode material in an amount of from about 2 wt. % to about 10 wt. %, alternatively from about 2 wt. % to about 7 wt. %, or alternatively from about 4 wt. % to about 6 wt. %, based on the total weight of the anode material.
In some embodiments, the anode material 5 can be used by itself without a separate anode current collector 4, though a tab or other electrical connection can still be provided to the anode material 5. In this embodiment, the anode material may have the form or architecture of a foil, a mesh, a perforated layer, a foam, a felt, or a powder. For example, the anode can comprise a metal foil electrode, a mesh electrode, or a perforated metal foil electrode.
In some embodiments, the anode 13 can comprise an optional anode current collector 4. The anode current collector 4 can be used with an anode 13, including any of those described with respect to the cathode 12. The anode material 5 can be pressed onto the anode current collector 4 to form the anode 13. For example, the anode material 5 can be adhered to the anode current collector 4 by pressing at, for example, a pressure between 1,000 psi and 20,000 psi (between 6.9×106 and 1.4×108 Pascals). The anode material 5 may be adhered to the anode current collector 4 as a paste. A tab of the anode current collector 4, when present, can extend outside of the device to form the current collector tab. The resulting anode 13 can have a thickness of between about 0.1 mm to about 5 mm.
In some embodiments, the cathode material and the anode material with their corresponding electroactive materials can also be formed from dissolved salts in the corresponding electrolytes (e.g., catholyte and anolyte, respectively). The process of forming the cathode material and the anode material from dissolved salts in the corresponding electrolytes would involve a charging step or a formation step, where the dissolved salts containing the active ions are plated onto the current collector by electrons flowing from an outside circuit. For example, manganese salts like manganese sulfate, manganese triflate, etc. in electrolytes with high proton activity will electroplate MnO2 during the charging or formation step. Similarly, zinc oxide dissolved into the anolyte will form Zn during the charging or formation step.
As shown in
In some embodiments, a separator 9 (e.g., as shown in
The separator 9 may comprise one or more layers. For example, when the separator is used, between 1 to 5 layers of the separator can be applied between adjacent electrodes. The separator can be formed from a suitable material such as nylon, polyester, polyethylene, polypropylene, poly(tetrafluoroethylene) (PTFE), poly(vinyl chloride) (PVC), polyvinyl alcohol, cellulose, or any combination thereof. Suitable layers and separator forms can include, but are not limited to, a polymeric separator layer such as a sintered polymer film membrane, polyolefin membrane, a polyolefin nonwoven membrane, a cellulose membrane, a cellophane, a battery-grade cellophane, a hydrophilically modified polyolefin membrane, and the like, or combinations thereof. As used herein, the phrase “hydrophilically modified” refers to a material whose contact angle with water is less than 45°. In another embodiment, the contact angle with water of the material used in the separator is less than 30°. In yet another embodiment, the contact angle with water of the material used in the separator is less than 20°. The polyolefin may be modified by, for example, the addition of TRITON X-100™ or oxygen plasma treatment. In some embodiments, the separator 9 can comprise a CELGARD® brand microporous separator. In an embodiment, the separator 9 can comprise a FS 2192 SG membrane, which is a polyolefin nonwoven membrane commercially available from Freudenberg, Germany. In some embodiments, the separator can comprise a lithium super ionic conductor (LISICON®), sodium super ionic conductions (NASICON), NAFION®, a bipolar membrane, a water electrolysis membrane, a composite of polyvinyl alcohol and graphene oxide, polyvinyl alcohol, crosslinked polyvinyl alcohol, or a combination thereof.
While the separator 9 can comprise a variety of materials, the use of a PGE for the electrolyte can allow for a relatively inexpensive separator 9 to be used when one or more separators are present. For example, the separator 9 can comprise CELLOPHANE®, polyvinyl alcohol, CELGARD®, a composite of polyvinyl alcohol and graphene oxide, crosslinked polyvinyl alcohol, PELLON®, and/or a composite of carbon-polyvinyl alcohol. Use of the separator 9 may help in improving the cycle life of the battery 20, but is not necessary in all embodiments.
When a buffer layer is used, the buffer layer can be used alone or in combination with a separator 9. The buffer layer can comprise a gelled solution that can comprise the same electrolyte formulation as the anolyte and/or the catholyte. For example, the buffer layer can be a PGE as described herein. One or more additives can also be present in the buffer layer such as calcium hydroxide, layered double hydroxides like hydrotalcites, quintinite, fougerite, magnesium hydroxide, or combinations thereof. For example, when the anolyte and catholyte have substantially the same formulation, only with different proton and hydroxyl anion compositions and/or viscosities, the buffer layer can have a concentration of the electrolyte that is the same as the anolyte or catholyte, or have a concentration that is between that of the anolyte and the catholyte. The buffer layer can have a viscosity greater than that of either the anolyte or catholyte to help prevent mixing between the anolyte and catholyte as well as limiting the migration of ions between the anolyte and catholyte.
As shown in
The electrolyte on the cathode side (e.g., catholyte 3) has a relatively high proton activity, which dictates the potential of the battery. The higher the activity of the protons in the catholyte, the higher the potential of the battery. An acid dissociation constant (Ka) is a relatively good indicator for judging proton activity. Nonlimiting examples of acidic electrolytes or ions having low to very large Ka's suitable for use in the catholyte 3 include hydrogen phosphate, bicarbonates, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, or any combination thereof. Triflic acids are superacids with high proton activity and use of these acids can help boost battery potential significantly.
The catholyte 3 can be an acidic solution, wherein the pH of the catholyte can be less than about 4, alternatively less than about 3, alternatively less than about 2, alternatively less than about 1, alternatively between −1.2 and 4, alternatively between −1.2 and 3, alternatively between −1.2 and 2, or alternatively between −1.2 and 1. The catholyte 3 can be used in conditions having temperatures ranging between 0 and 200° C. In some embodiments, the catholyte can comprise an acid such as a mineral acid (e.g., hydrochloric acid, nitric acid, sulfuric acid, etc.). For acid catholyte compositions, the acid concentration (e.g., concentration of the acidic electrolyte) can be between about 0.0001 M and about 16 M, alternatively from about 0.001 M to about 16 M, alternatively from about 0.01 M to about 16 M, alternatively from about 0.1 M to about 16 M, or alternatively from about 1 M to about 16 M.
In some embodiments, the hydrogen activity of the catholyte 3 can be altered by using acids of different strengths. Ka is a relatively good indicator for judging acid strengths. The following electrolytes or ions having low to very large Ka's can be used in the catholyte solution: hydrogen phosphate, bicarbonates, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, or any combination thereof. While these examples of acidic electrolytes can help alter hydrogen (or proton) activity, it should be apparent to anyone skilled in chemistry or electrochemistry that any combination of acidic electrolytes and other electrolytes can be used to alter proton activity.
Catholyte additives can help with boosting the performance of the cathode material. Nonlimiting examples of catholyte additives suitable for use in this disclosure include manganese sulfate, nickel sulfate, potassium permanganate, manganese chloride, manganese acetate, manganese triflate, bismuth chloride, bismuth nitrate, manganese nitrate, nickel sulfate, nickel nitrate, zinc sulfate, zinc chloride, zinc acetate, zinc triflate, indium chloride, copper sulfate, copper chloride, lead sulfate, sodium persulfate, potassium persulfate, ammonium persulfate, ammonium chloride, vanillin, potassium chloride, sodium chloride, lithium nitrate, lithium chloride, lithium carbonate, lithium acetate, lithium triflate, aluminum trifluoromethanesulfonate, aluminum chloride, aluminum nitrate, potassium sulfate, sodium sulfate, ammonium sulfate, or any combination thereof. The concentration of catholyte additives can be between 0 and 5 M.
In some embodiments, the catholyte solution can comprise a solution comprising potassium permanganate, sodium permanganate, lithium permanganate, calcium permanganate, manganese sulfate, manganese chloride, manganese nitrate, manganese perchlorate, manganese acetate, manganese bis(trifluoromethanesulfonate), manganese triflate, manganese carbonate, manganese oxalate, manganese fluorosilicate, manganese ferrocyanide, manganese bromide, magnesium sulfate, ammonium chloride, ammonium sulfate, ammonium hydroxide, zinc sulfate, zinc triflate, zinc acetate, zinc nitrate, bismuth chloride, bismuth nitrate, nitric acid, sulfuric acid, hydrochloric acid, sodium sulfate, potassium sulfate, cobalt sulfate, lead sulfate, sodium hydroxide, potassium hydroxide, titanium sulfate, titanium chloride, lithium nitrate, lithium chloride, lithium bromide, lithium bicarbonate, lithium acetate, lithium sulfate, lithium nitrate, lithium nitrite, lithium hydroxide, lithium perchlorate, lithium oxalate, lithium fluoride, lithium carbonate, lithium sulfate, lithium bromate, polyvinyl alchohol, carboxymethyl cellulose, xanthum gum, carrageenan, acrylamide, potassium persulfate, sodium persulfate, ammonium persulfate, N,N′-methylenebisacrylamide, or any combination thereof. For example, the catholyte solution can comprise manganese sulfate mixed with sulfuric acid or potassium permanganate mixed with sulfuric acid. Other dopants to this solution can be zinc sulfate, lead sulfate, titanium disulfide, titanium sulfate hydrate, silver sulfate, cobalt sulfate, and nickel sulfate. In some embodiments, the catholyte solution can comprise manganese sulfate, ammonium chloride, ammonium sulfate, manganese acetate, potassium permanganate, and/or a salt of permanganate, where the additives can have a concentration between 0 and 10 M. Depending on the type of manganese salts used voltage of the battery system can be different. For example, in manganese sulfate electrolyte the voltage of the SS-HiVAB is around 2.45-2.5V, while in potassium permanganate electrolyte the voltage of the SS-HiVAB is around 2.8-2.9V.
In some embodiments, the catholyte can comprise a permanganate. Permanganates have a high positive potential. This can allow the overall cell potential to be increased within the battery 10. When present, the permanganate can be present in a molar ratio of an acid (e.g., a mineral acid such a hydrochloric acid, sulfuric acid, etc.) to permanganate of between about 5:1 to about 1:5, or about 1:1 to about 1:6, or between about 1:2 to about 1:4, or about 1:3, though the exact amount can vary based on the expected operation conditions of the battery 10. The concentration of the permanganate (e.g., potassium permanganate or a salt of permanganate, etc.) can be greater than 0 and less than or equal to 5 M. In some embodiments, the catholyte solution comprises sulfuric acid, hydrochloric acid or nitric acid at a concentration greater than 0.0001 M and less than or equal to 16 M. The use of a permanganate can be advantageous for creating a high voltage battery such that when the use of a catholyte with permanganates is combined with a very negative anode potential, the resulting battery can have a voltage of approximately 2.8 V when the cathode and anode are MnO2|Zn and a voltage of approximately 4 V when the cathode and anode are MnO2|Al. When the catholyte comprises a permanganate, suitable permanganates can include, but are not limited to, potassium permanganate, sodium permanganate, lithium permanganate, calcium permanganate, and combinations thereof.
The electrolyte on the anode side (e.g., anolyte 6) has a relatively high hydroxyl activity, which dictates the potential of the battery. The higher the activity of the hydroxyl in the anolyte, the higher the potential of the battery. Nonlimiting examples of alkaline electrolytes or ions having relatively high hydroxyl activity suitable for use in the anolyte 6 include ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, caesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, or any combination thereof.
In some embodiments, the anolyte can be an alkaline electrolyte (e.g., a relatively highly alkaline electrolyte), while the catholyte can be an acidic solution (e.g., a relatively highly acidic solution). The alkaline electrolyte in the anolyte can be a hydroxide such as potassium hydroxide, sodium hydroxide, lithium hydroxide, ammonium hydroxide, cesium hydroxide, or any combination thereof. The resulting anolyte can have a pH of equal to or greater than 10, alternatively equal to or greater than 11, or alternatively equal to or greater than 12, or alternatively equal to or greater than 13. In some embodiments, the pH of the anolyte can be greater than or equal to about 10 and less than or equal to about 15.13, alternatively greater than or equal to about 11 and less than or equal to about 15.13 alternatively greater than or equal to about 12 and less than or equal to about 15.13, or alternatively greater than or equal to about 13 and less than or equal to about 15.13. As described herein, the anolyte can be polymerized or gelled. The resulting anolyte can be in a semi-solid state that resists flowing within the battery. This can serve to limit or prevent any mixing between the anolyte and the catholyte. The anolyte can be polymerized using any suitable techniques, including any of those described herein. In some embodiments, the alkaline electrolyte can be present in the anolyte in an amount of 1-70 wt. %, alternatively 1-25 wt. %, alternatively 25-70 wt. %, alternatively 20-60 wt. %, alternatively 20-55 wt. %, alternatively 30-55 wt. %, or alternatively 1-55 wt. %, based on the total weight of the anolyte. Usually a higher concentration of alkaline electrolyte is used to increase the solubility of any metals in the gelled state in the anolyte. For example, the higher concentration of alkaline electrolyte can be between 25-70 wt. % of the anolyte.
In some embodiments, the hydroxyl activity of the anolyte 6 can be altered by using bases of different strengths, where the following from low to high strength can be used: ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, caesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, or any combination thereof. While these examples of alkaline electrolytes can help alter hydroxyl activity, it should be apparent to anyone skilled in chemistry or electrochemistry that any combination of alkaline electrolytes and other electrolytes can be used to alter hydroxyl activity.
In addition to a hydroxide, the anolyte 6 can comprise additional components. In some embodiments, the alkaline electrolyte can have zinc oxide, potassium carbonate, potassium iodide and potassium fluoride as additives. When zinc compounds are present in the anolyte, the anolyte can comprise zinc sulfate, zinc chloride, zinc acetate, zinc carbonate, zinc chlorate, zinc fluoride, zinc formate, zinc nitrate, zinc oxalate, zinc sulfite, zinc tartrate, zinc cyanide, zinc oxide, sodium hydroxide, potassium hydroxide, lithium hydroxide, potassium chloride, sodium chloride, potassium fluoride, lithium nitrate, lithium chloride, lithium bromide, lithium bicarbonate, lithium acetate, lithium sulfate, lithium permanganate, lithium nitrate, lithium nitrite, lithium perchlorate, lithium oxalate, lithium fluoride, lithium carbonate, lithium bromate, acrylic acid, N,N′-methylenebisacrylamide, potassium persulfate, ammonium persulfate, sodium persulfate, or a combination thereof.
In some embodiments, the anolyte 6 can comprise electrolyte additives (e.g., anolyte additives), such as vanillin, indium hydroxide, zinc acetate, zinc oxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, sodium dodecylbenzene sulfonate, polyethylene glycol, ethanol, methanol, zinc gluconate, glucose, or any combination thereof.
In some embodiments, an organic solvent containing a suitable salt can be used as an electrolyte. Examples of suitable organic solvents include, but are not limited to, cyclic carbonates, linear carbonates, dialkyl carbonates, aliphatic carboxylate esters, γ-lactones, linear ethers, cyclic ethers, aprotic organic solvents, fluorinated carboxylate esters, and combinations thereof. Any suitable additives including salts as described herein can be used with the organic solvents to form an organic electrolyte for the anolyte and/or catholyte.
In some embodiments, an ionic liquid can be used to form a gelled electrolyte (e.g., a gelled anolyte, a gelled catholyte, etc.). The ionic liquids can comprise 1-ethyl-3-methylimidazolium chloride (EMImCl), 1-allyl-3-methylimidazolium bromide, 1-allyl-3-methylimidazolium chloride, 1-butyl-2,3-dimethylimidazolium chloride, 1-ethyl-3-methylimidazolium acetate, -ethyl-3-methylimidazolium bromide, 1-ethyl-3-methylimidazolium tetrachloroaluminate, lithium hexafluorophosphate (LiPF6), lithium perchlorate, lithium bis(trifluoromethanesulfonyl)imide, lithium bis(oxalato)borate, and combinations thereof. Other ionic liquids are known and can also be used. In some embodiments, EMImCl can be used as the ionic liquid and can be purified before mixing with an aluminum salt to form an aluminum-ion conducting electrolytes. The aluminum salt can be aluminum chloride, aluminum acetate, aluminum nitrate, aluminum bromide, and others. The mixture of EMImCl with aluminum chloride can be made by slowly adding a precise amount of aluminum chloride in an inert atmosphere. The mixing ratio of aluminum chloride with EMImCl can be between 5:1 to 1:1, or about 1.5:1.
In some embodiments, a water in salt electrolyte can be gelled and used as the catholyte and/or anolyte. A water in salt electrolyte can include an electrolyte in which the salt concentration is above the saturation point. The activity of water in an aqueous electrolyte can be further reduced by increasing the salt concentration above the saturation point in order to form a water in salt electrolyte. The ionic conductivity of such electrolytes can be higher than those in a regular aqueous electrolyte. A water in salt electrolyte can comprise water along with a suitable salt above its saturation point, including any of the salts and additives described herein with regard to the aqueous anolyte and/or catholyte.
The anolyte and the catholyte need to be kept separated or decoupled so that neutralization does not take place. Such separation can be achieved by using a separator, through gelation or polymerization of the electrolytes, and any combination thereof.
One or both of the anolyte and the catholyte can be gelled in the battery. The polymerization process can be performed with any electrolyte, including any of those described herein (e.g., organic, aqueous, ionic liquid, water in salt, etc.). A number of polymerization techniques can be used to form the gelled/solid electrolyte—for example, step-growth, chain-growth, emulsion polymerization, solution polymerization, suspension polymerization, precipitation polymerization, photopolymerization and others. Once the gelled/solid electrolytes are formed through the polymerization step, they can be combined in a single battery housing as described herein. The battery can use separators or be membrane-less or separator-less.
As described herein, the electrolyte can be polymerized or gelled to form a polymer gel electrolyte (PGE) for the catholyte and/or the anolyte. The resulting PGE can be in a semi-solid state that resists flowing within the battery. For example, the PGE can comprise an inert hydrophilic polymer matrix impregnated with aqueous electrolyte. The electrolyte can be polymerized using any suitable techniques. In an embodiment, a method of forming a PGE can begin with selecting a monomer material for the PGE. The monomer can be polar vinyl monomer selected from the group consisting of acrylic acid, vinyl acetate, acrylate esters, vinyl isocyanate, acrylonitrile, or any combinations thereof. The aqueous electrolyte component can then be selected, and can include any of the components described above with respect to the electrolyte. An initiator can be added to start the polymerization process. In some embodiments, a cross-linker can be used in the electrolyte composition to further cross-link the polymer matrix in order to form the PGE. The monomer in the composition (e.g., a polar vinyl monomer) can be present in an amount of between about 5% to about 50% by weight, the initiator can be present in an amount of between about 0.001 wt. % to about 0.1 wt. %, and the cross-linker can be present in an amount of between 0 to 5 wt. %.
In some embodiments, the PGE can be formed in-situ, which refers to the introduction of the electrolyte as a liquid into the housing followed by subsequent polymerization to form the PGE within the housing. This method can allow the electrolyte composition to soak into the void spaces, the anode, and/or the cathode prior to fully polymerizing to form the PGE. In some embodiments, a vacuum (e.g., a pressure less than atmospheric pressure) can be created within the housing 7 upon introduction of the electrolyte into the corresponding compartment. The vacuum can serve to remove air and allow the electrolyte to penetrate the anode 13, the cathode 12, and/or the various void spaces within the battery 10. In some embodiments, the vacuum can be between about 10 and 29.9 inches of mercury or between about 20 and about 29.9 inches of mercury vacuum. The use of the vacuum can help to avoid the presence of air pockets within the battery 10 prior to the full polymerization of the electrolyte. In some embodiments, the electrodes can be soaked in the electrolyte solution for between 1-120 minutes at a temperature of between 0° C. to 30° C. prior to full polymerization of the electrolyte to allow the electrolyte to impregnate the electrodes. Once the electrolyte is polymerized, the battery can be allowed to rest prior to use. In some embodiments, the battery can be allowed to rest for between 5 minutes and 24 hours.
In order to help impregnate the electrodes with the electrolyte, the electrodes can be pre-soaked with the selected electrolyte solution prior to polymerizing the electrolyte. This can be performed by soaking the electrodes in the electrolyte (e.g., in a catholyte or anolyte separately) outside of the battery or housing, and then placing the pre-soaked electrodes into the housing to construct the battery. In some embodiments, an electrolyte that does not contain a polymer or gelling agent can be introduced into the battery to soak the electrodes in-situ. This can include the use of a vacuum to assist in impregnating the electrodes. The electrodes can be soaked for between about 1 minute and 24 hours. In some embodiments, the soaking can be carried out over a plurality of cycles in which the battery is filled with the electrolyte and allowed to soak, drained, refilled and allowed to soak, followed by draining a desired number of times. Once the electrodes are soaked and impregnated with the electrolyte, the electrolyte containing the polymer and polymerization agents (e.g., an initiator, cross-linking agent, etc.) can be introduced into the housing and allowed to polymerize to form the final battery.
The composition of the electrolyte, the monomer material, the initiator, and the conditions of the formation (e.g., temperature, etc.) can be selected to provide a desired polymerization time to allow the electrolyte composition to properly soak the components of the batter to absorb and penetrate into the electrodes. The temperature can be controlled to control the polymerization process, where relatively colder temperatures can inhibit or slow the polymerization, and relatively warmer temperatures can decrease the polymerization time or accelerate the polymerization process. In addition, an increase in an alkaline electrolyte component (e.g., a hydroxide) can decrease the polymerization time, and an increase in the initiator concentration will decrease the polymerization time. Suitable polymerization times can be between 1 minute and 24 hours, based on the composition of the electrolyte solution and the temperature of the reaction.
In some embodiments, the anolyte and/or the catholyte can be formed via a gelation process, such as a free radical polymerization technique, wherein acrylic acid can be used as the monomer, for example. Acrylic acid can be mixed with either the anolyte or catholyte until it is substantially dissolved. A cross-linker like N,N′-methylenebisacrylamide (MBA) can be used to increase the strength of the polymer. For the anolyte, the process of mixing the acrylic acid with the MBA can be usually done at relatively cold temperatures because of the heat generated in the reaction. However, for the catholyte, the mixture of acrylic acid and MBA can be heated between 50-200° C. The polymerization can be initiated through the addition of an initiator like a persulfate salt, such as potassium persulfate, sodium persulfate, ammonium persulfate, or any combination thereof. The electrolyte additives (e.g., anolyte additive, catholyte additive) can be included during the gelation process. Ionomers can also be added during the gelation process. Nonlimiting examples of ionomers that can be added to the electrolyte during the gelation process include Nafion solutions which are made from perfluorosulfonic acid (PFSA)/polytetrafluoroethylene (PTFE) copolymer in the acid form or anion exchange ionomers with polyaromatic polymer.
As an example of a polymerization process, a mixture of acrylic acid, N,N′-methylenebisacrylamide, and alkaline solution can be created at a temperature of around 0° C. Any additives can then be added to the solution (e.g., gassing inhibitors, additional additives as described herein, etc.). For example, zinc oxide, when used in the electrolyte, can be dissolved in the alkaline solution after mixing the precursor components, where the zinc oxide can beneficial during the electrochemical cycling of the anode. To polymerize the resulting mixture an initiator such as potassium persulfate can be added to initiate the polymerization process and form a solid or semi-solid polymerized electrolyte (e.g., a PGE). The resulting polymerized electrolyte can be stable over time once the polymerization process has occurred.
As an example, a PGE described herein can be made through a free radical polymerization process. In an embodiment, acrylic acid (AA) can be used as a monomer with N,N′-methylenebisacrylamide (MBA) as the cross-linker and potassium persulfate (K2S2O8) as the initiator. When preparing the anolyte, an alkaline electrolyte such as KOH can be added to this process, which can be embedded in the anolyte gel/polymer framework. The addition of alkaline electrolyte to AA results in neutralization, which reduces the concentration of the alkaline electrolyte in the polymeric gel. Differing alkaline electrolyte concentrations can alter the gelation time. Higher alkaline electrolyte concentrations usually result in faster gelation, while lower alkaline electrolyte concentrations take longer times. Further, initiator concentration can affect the gelation process. Furthermore, the viscosity of the gel can be tuned by altering the monomer and MBA concentration, which can also affect ionic conductivity. Similarly, when preparing the catholyte, an acidic electrolyte such as sulfuric acid can be added to this process, which can be embedded in the catholyte gel/polymer framework.
In some embodiments, an ionomer gelation layer can also be made, wherein the ionomer gelation layer can separate the catholyte and anolyte solutions or gels. The gelation process for forming the ionomer gelation layer is substantially similar to the gelation process of forming the anolyte and/or catholyte gels as described herein, wherein the ionomers are added to the electrolyte during the gelation process. The ionomer gels (e.g., ionomer gelation layers) can also contain additives such as potassium sulfate, sodium sulfate, ammonium sulfate, or any combination thereof. Ionomer resins can also be used in the gelation process to produce an ionomer gelation layer.
The polymerization process can occur prior to the construction of the battery 10 or after the cell is constructed. In some embodiments, the electrolyte can be polymerized and placed into a tray to form a sheet. Once polymerized, the sheet can be cut into a suitable size and shape and one or more layers can be used to form the electrolyte in contact with the anode 13. When a pre-formed PGE is used, additional liquid electrolyte can be introduced into the battery and/or the electrodes can be pre-soaked with the electrolyte prior to constructing the battery.
In some embodiments, the PGE can be formed using an aqueous electrolyte, organic electrolyte, ionic liquid, water in salt electrolyte, and the like. In some embodiments, an aqueous electrolyte can be used for the catholyte and/or anolyte and gelled to form an aqueous hydrogel as the PGE. In some embodiments, aqueous hydrogels can be made through a free radical polymerization process. For example, when preparing the anolyte, acrylic acid (AA) can be selected as the monomer with N,N′-methylenebisacrylamide (MBA) as the cross-linker and potassium persulfate as the initiator. In aqueous alkaline anolytes, a suitable hydroxide (e.g., potassium hydroxide (KOH), sodium hydroxide, lithium hydroxide, etc.) can be used to form the electrolyte. The hydroxide can be encapsulated in a hydrogel network by neutralizing the hydroxide with the AA. To create a hydrogel, the monomer can be combined with any cross-linker until the cross-linker is dissolved. Separately, an amount of the hydroxide can be cooled to slow the reaction. In some embodiments in which the anolyte is an aqueous electrolyte, the hydroxide can be cooled to a temperature below about 10° C., below about 5° C., or below about 0° C. The mixed solution of the monomer and any cross-linker can then be added drop-wise to the chilled solution of the hydroxide as the neutralization reaction releases heat. To gel the resulting mixture of the hydroxide, monomer, and cross-linker, an initiator such as potassium persulfate can be added. The mixture can then be allowed to form a PGE. The amounts and concentrations of the ingredients can be varied to obtain varying mechanical strengths of the hydrogels. Similarly, when preparing the catholyte, an acidic electrolyte such as sulfuric acid can be encapsulated in a hydrogel network.
Electrolytes comprising ionic liquids can also be used to form PGEs, including any of the ionic liquid described herein. To form a PGE using an ionic liquid, a solution of any additives, which can be in a suitable solvent, can be prepared and a monomer can be added. The monomer can be any suitable monomer. For example, acrylamide can be used as a polymerization agent for ionic liquids. To this solution, the ionic liquid along with the additive solution can be mixed along with an initiator. Any suitable initiator for use with the polymerization agent can be used. For example, azobisisobutyronitrile can be used with acrylamide. The initiator can be added in a suitable amount such about 1 wt. % of the polymerization agent. This final solution can then be heated to form a polymerized gel.
Organic electrolytes comprising a salt dissolved in an organic solvent can also be gelled to form an anolyte and/or catholyte. As an example, lithium-ion conducting electrolytes can be gelled using a number of polymerization techniques such as ring-opening polymerization, photo-initiated radical polymerization, UV-initiated radical polymerization, thermal-initiated polymerization, in-situ polymerization, UV-irradiation, electrospinning, and others. The lithium electrolyte can comprise lithium hexafluorophosphate (LiPF6), lithium perchlorate, lithium bis(trifluoromethanesulfonyl)imide, lithium bis(oxalato)borate, and combinations thereof in an organic solvent such as ethylene carbonate, dimethyl carbonate, propylene carbonate, diethyl carbonate, ethyl methyl carbonate, and combinations thereof. An exemplary mixture can include 1 M LiPF6 mixed in a solvent mixture of ethylene carbonate and dimethyl carbonate. Other solvents also exist that can be used as a mixture to reduce the flammability of the organic electrolyte.
The organic electrolyte can be gelled by mixing the selected salts with the organic solvent. A gelling agent can then be added along with an initiator. The gelling agent can be added in an amount between about 0.1 to about 5 wt. % of the mixture, and the initiator can be added in an amount of between about 0.01 to about 1 wt. % of the mixture. In some embodiments, a suitable gelling agent for an organic electrolyte can comprise pentaerythritol tetraacrylate and the initiator can comprise azodiisobutyronitrile. The resulting mixture can be gelled (e.g., polymerized) by heating the mixture to about 50-90° C., or to about 70° C. and holding for 1-24 hours.
For an aqueous electrolyte which is acidic in nature, such as the catholyte, the polymerization can be carried out using a number of processes. In an embodiment, a method for making a solid state gelled aqueous acid electrolyte can comprise the addition of acrylamide to a solution comprising manganese sulfate, H2SO4, ammonium sulfate, potassium permanganate, and/or sulfuric acid. A gelling agent comprising acrylamide can be added to the solution and mixed at a temperature between about 70-90° C. for at least an hour until the solution is homogenous. After the solution is mixed well, then a cross-linker and initiator can be added to the solution and mixed between 2-48 hours until the solution gels.
In some embodiments, the separator comprises an ion-selective gel; wherein the ion-selective gel comprises an ionomer, a bipolar membrane, a cation-exchange membrane, an anion-exchange membrane, a cellophane grafted with ion-selective properties, a polyvinyl alcohol grafted with ion-selective properties, a ceramic separator, NaSiCON, LiSiCON, or any combination thereof.
While an anolyte PGE and a catholyte PGE can be used without a separator, separation of the catholytes and anolytes can also be done through ion-selective ceramic separators and/or polymeric membranes. Cellulose-based membranes like cellophane can also be used to separate the catholytes and anolytes. For example, ceramic separators like LiSiCON and/or NaSiCON can be used to separate the catholytes and anolytes. As another example, polymeric membranes having cation-exchange properties like Nafion and/or anion-exchange membranes can be used to separate the catholytes and anolytes. Polyvinyl alcohol (PVA) and/or cross-linked polyvinyl alcohol (C-PVA) can also be used as polymeric separators to separate the catholytes and anolytes. The cellulose-based membranes, PVA, and C-PVA can be grafted with ionomers that may impart cation and/or anion exchange properties. Bipolar membranes can also be used as separators between catholytes and anolytes.
Gels or polymeric membranes containing LiSiCON and NaSiCON can be made using the procedures described herein for the formation of PGEs and/or ionomer gelation layers, by using raw materials used in making ceramic separators.
The cathodes and anodes used in the high voltage aqueous Zn-anode battery as disclosed herein can advantageously access 50-100% of the theoretical capacity at wide range of current densities and material loading.
The final cell or battery design could have a cathode with an acidic PGE catholyte and an anode with an alkaline PGE anolyte with a separator or buffering layer that prevents the intermixing of the two PGE's. A battery with dual electrolytes allows for high reversibility and improved or maximum utilization of the electrodes and thus, a higher energy density. The use of vastly different alkalinity and acidity in the anolyte and catholyte further allows for increasing the average discharge of the battery to equal to or greater than about 3 V.
In some embodiments, the high voltage aqueous Zn-anode battery as disclosed herein can be used for producing energy. For example, a method for producing energy may comprise (i) discharging the high voltage aqueous Zn-anode battery as disclosed herein to a discharge voltage to produce energy, wherein at least a portion of the Zn of the Zn electroactive material is oxidized during the discharging to form oxidized zinc (e.g., ZnO); and (ii) charging the high voltage Zn-anode battery to a charge voltage, wherein at least a portion of the oxidized zinc is reduced to Zn during the charging. The discharge voltage can be equal to or greater than about 2 V, alternatively equal to or greater than about 3 V, alternatively equal to or greater than about 3.5 V, alternatively from about 2 V to about 5 V, alternatively from about 3 V to about 5 V, or alternatively from about 3.5 V to about 5 V.
The subject matter having been generally described, the following examples are given as particular aspects of the disclosure and are included to demonstrate the practice and advantages thereof, as well as preferred aspects and features of the inventions. It should be appreciated by those of skill in the art that the techniques disclosed in the examples which follow represent techniques discovered by the inventors to function well in the practice of the inventions, and thus can be considered to constitute preferred modes for its practice. However, those of skill in the art should, in light of the present disclosure, appreciate that many changes can be made in the specific aspects which are disclosed and still obtain a like or similar result without departing from the scope of the inventions of the instant disclosure. It is understood that the examples are given by way of illustration and are not intended to limit the specification of the claims to follow in any manner.
A schematic drawing of the battery with prismatic geometry is shown in
Manganese dioxide (MnO2), more specifically electrolytic manganese dioxide (EMD), was chosen as the cathode in this example. Traditional or conventional alkaline MnO2|Zn batteries have an OCV of about 1.6V. In the high voltage MnO2|Zn aqueous battery disclosed herein, the catholyte for the MnO2 was chosen to be 16 M sulfuric acid, while the anolyte for the Zn was chosen to be 51 wt. % potassium hydroxide (KOH). A Nafion 115 membrane was used as the ion-selective membrane. The cathode mix was comprised of 80 wt. % MnO2, 15 wt. % expanded graphite, and 5 wt. % Teflon pasted on a titanium current collector. The anode mix was comprised of 95 wt. % metallic Zn powder, 2 wt. % indium hydroxide and polyethylene glycol, and 3 wt. % Teflon pasted on a copper current collector. The OCV of this MnO2|Zn battery with high proton activity in the catholyte and high hydroxyl activity in the anolyte initially showed 3.45 V with it being stabilized at about 3.4 V for over 3 hours as shown in
Another high voltage MnO2|Zn aqueous battery was created with similar cathode and anode mix compositions as described in Example 1. The catholyte and anolyte in the battery system of Example 2 were 10 M sulfuric acid and 51 wt. % potassium hydroxide. The theoretical capacity (617 mAh/g based on two electrons) of the MnO2 was used to determine the areal capacity (mAh/cm2). The areal capacities reported in all of the examples are based on the two electron capacity of MnO2 and its mass pasted onto the titanium current collector. Nafion 115 was used as the membrane for this battery as well. The discharge curve of this system is shown in
Another high voltage MnO2|Zn aqueous battery with similar experimental details as presented in Example 2 was made. The catholyte and anolyte in this battery system were 14 M sulfuric acid and 35 wt. % potassium hydroxide, respectively. The average discharge voltage of this battery was also between 3.1 and 3.2 V, as shown in
A high voltage MnO2|Zn aqueous battery with similar experimental details as presented in Example 2 was made, except with higher loadings of MnO2 on the cathode. The catholyte and anolyte in this battery system were 13.3 M sulfuric acid with 3.2 M manganese sulfate dissolved, and 51 wt. % potassium hydroxide, respectively. The average discharge voltage for this system was between 2.9 and 3 V, but at much higher areal capacities of 4 mAh/cm2 as shown in
A solid state MnO2|Zn battery with similar experimental details as presented in Example 2 was made. The solid state battery had gelled catholyte and anolytes. The gelling or polymerization was done through a free radical polymerization process. For the catholytes, a 10 M acid with 3.2 M manganese acetate was dissolved in a solution of acrylic acid and MBA. To this dissolved acidic solution, a potassium persulfate initiator was added to begin the gelation process. The gelation was complete after heating the solution at a temperature of greater than about 50 to about 70° C. The formed gel was moist and physically sturdy. For the anolyte, a 51 wt. % potassium hydroxide solution with indium hydroxide dissolved in it was cooled at 0° C. To this cooled solution acrylic acid and MBA were added and stirred till the contents were dissolved. The alkaline solution was maintained at a temperature of 0° C. Afterwards, the potassium persulfate initiator was added to it and allowed to gel by letting the alkaline solution reach near room temperature. The integrity and structure of the gels formed highly depend on the heating and cooling steps for the catholytes and anolytes, respectively. The OCV of this solid state high voltage MnO2|Zn battery was measured, and as shown in
A high voltage MnO2|Zn battery with similar experimental details as presented in Example 2 was made. The catholyte in this battery was 1 M nitric acid with 50 wt. % sodium persulfate dissolved in the electrolyte. The average discharge voltage of this battery was around 2.92 V and at a high areal capacity of 4 mAh/cm2, as shown in
The following is provided as additional disclosure for combinations of features and aspects of the presently disclosed subject matter.
A first aspect, which is a high voltage Zinc (Zn)-anode battery comprising a cathode comprising a cathode electroactive material; an anode comprising a Zn electroactive material; a catholyte solution with high proton activity in contact with the cathode, wherein the catholyte is not in contact with the anode; an anolyte solution with high hydroxyl activity in contact with the anode, wherein the anolyte is not in contact with the cathode; and a separator with ion-selective properties.
A second aspect, which is the battery of the first aspect, wherein the cathode electroactive material comprises manganese dioxide (MnO2), manganese oxides (Mn2O3, Mn3O4, MnO), manganese hydroxides (MnOOH, Mn(OH)2), silver oxides (AgO, Ag2O), silver (Ag), nickel (Ni), nickel oxide (NiO, Ni2O3), nickel hydroxides (NiOOH, Ni(OH)2), cobalt oxide (Co3O4, CoO), cobalt hydroxides, lead (Pb), lead oxide (PbO, PbO2), copper oxide, copper, copper hydroxide, potassium iron oxide (K2FeO4), barium iron oxide (BaFeO4), copper hexacyanoferrate, lithium iron phosphate, lithium nickel manganese cobalt oxide, lithium manganese oxide (LiMn2O4, Li2MnO3), calix[4]quinone, 1,4-napththoquinone, 9,10-anthraquinone, or a combination thereof.
A third aspect, which is the battery of the first aspect, wherein the anode material containing the Zn electroactive material is a powder, foil, mesh, foam, sponge, perforated foil, or a combination thereof.
A fourth aspect, which is the battery of the first aspect, wherein the cathode contains conductive carbon mixed with the cathode active material where the conductive carbon comprises of graphite, carbon fiber, carbon black, acetylene black, single walled carbon nanotubes, multi-walled carbon nanotubes, nickel or copper coated carbon nanotubes, dispersions of single walled carbon nanotubes, dispersions of multi-walled carbon nanotubes, graphene, graphyne, graphene oxide, or a combination thereof.
A fifth aspect, which is the battery of the first aspect, wherein the cathode contains additives or dopants which comprises of bismuth, bismuth oxide, copper oxide, copper, indium, indium hydroxide, indium oxide, aluminum, aluminum oxide, nickel, nickel hydroxide, nickel oxide, silver, silver oxide, cobalt, cobalt oxide, cobalt hydroxide, lead, lead oxide, lead dioxide, quinones, or a combination thereof.
A sixth aspect, which is the battery of the first aspect, wherein the cathode contains binders comprising of methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroypropyl cellulose (HPH), hydroypropylmethyl cellulose (HPMC), hydroxethylmethyl cellulose (HEMC), carboxymethylhydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON®, or combinations thereof.
A seventh aspect, which is the battery of any of the first, second, fourth, fifth and sixth aspects, wherein the cathode is pressed onto a current collector comprising of carbon, lead, nickel, steel (e.g., stainless steel, etc.), nickel-coated steel, nickel plated copper, tin-coated steel, copper plated nickel, silver coated copper, copper, magnesium, aluminum, tin, iron, platinum, silver, gold, titanium, bismuth, titanium, cold rolled steel, half nickel and half copper, carbon foam, carbon felt, polypropylene mesh, or any combination thereof.
An eighth aspect, which is the battery of the seventh aspect, wherein the current collector is a foil, mesh, perforated foil, foam, honey-combed mesh, sponge-shaped, or any combinations thereof.
A ninth aspect, which is the battery of any of the first, second, fourth, fifth and sixth aspects, wherein the cathode comprises of 1 to 99 wt. % electroactive material, conductive carbon 1 to 99 wt. %, additives 0 to 30 wt. %, and binder 0 to 10 wt. %.
A tenth aspect, which is the battery of any of the first and third aspects, wherein the anode material comprises of conductive carbon mixed with electroactive Zn, where the carbon comprises of graphite, carbon fiber, carbon black, acetylene black, single walled carbon nanotubes, multi-walled carbon nanotubes, nickel or copper coated carbon nanotubes, dispersions of single walled carbon nanotubes, dispersions of multi-walled carbon nanotubes, graphene, graphyne, graphene oxide, or a combination thereof.
An eleventh aspect, which is the battery of any of the first and third aspects, wherein the anode material comprises of additives or dopants, which are bismuth, bismuth oxide, indium, indium oxide, indium hydroxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, calcium hydroxide, sodium dodecylbenzene sulfonate, polyethylene glycol, zinc oxide, or combinations thereof.
A twelfth aspect, which is the battery of any of the first, third, tenth and eleventh aspects, wherein the anode material comprises of binders, which are methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroypropyl cellulose (HPH), hydroypropylmethyl cellulose (HPMC), hydroxethylmethyl cellulose (HEMC), carboxymethylhydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON®, or combinations thereof.
A thirteenth aspect, which is the battery of any of the first, third, tenth, eleventh and twelfth aspects, wherein the anode material is pressed on a current collector comprising of carbon, lead, nickel, steel (e.g., stainless steel, etc.), nickel-coated steel, nickel plated copper, tin-coated steel, copper plated nickel, silver coated copper, copper, magnesium, aluminum, tin, iron, platinum, silver, gold, titanium, bismuth, titanium, cold rolled steel, half nickel and half copper, carbon foam, carbon felt, polypropylene mesh, or any combination thereof.
A fourteenth aspect, which is the battery of any of the first, third, tenth, eleventh and twelfth aspects, wherein the anode comprises of 1-100 wt. % of electroactive Zn, 0-10 wt. % of conductive carbon, 0-30 wt. % additives or dopants, and 0-10 wt. % binders.
A fifteenth aspect, which is the battery of first aspect, wherein the catholyte of high proton activity comprises of hydrogen phosphate, bicarbonates, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, or combinations thereof.
A sixteenth aspect, which is the battery of any of the first and fifteenth aspects, wherein the electrolyte additives to the catholyte comprises of manganese sulfate, nickel sulfate, potassium permanganate, manganese chloride, manganese acetate, manganese triflate, bismuth chloride, bismuth nitrate, manganese nitrate, nickel sulfate, nickel nitrate, zinc sulfate, zinc chloride, zinc acetate, zinc triflate, indium chloride, copper sulfate, copper chloride, lead sulfate, sodium persulfate, potassium persulfate, ammonium persulfate, ammonium chloride, vanillin, potassium chloride, sodium chloride, lithium nitrate, lithium chloride, lithium carbonate, lithium acetate, lithium triflate, aluminum trifluoromethanesulfonate, aluminum chloride, aluminum nitrate, potassium sulfate, sodium sulfate, ammonium sulfate, or combinations thereof.
A seventeenth aspect, which is the battery of the first aspect, wherein the anolyte with high hydroxyl activity comprises of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, caesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, or combinations thereof.
An eighteenth aspect, which is the battery of the first aspect, wherein the electrolyte additives to the anolyte comprise of vanillin, indium hydroxide, zinc acetate, zinc oxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, sodium dodecylbenzene sulfonate, polyethylene glycol, ethanol, methanol, zinc gluconate, glucose, or combinations thereof.
A nineteenth aspect, which is the battery of any of the first, fifteenth, sixteenth, seventeenth and eighteenth aspects, wherein the catholyte and anolyte can be gelled or polymerized.
A twentieth aspect, which is the battery of the first aspect, wherein the separator comprises of ion-selective gel comprising of ionomers, bipolar membrane, cation-exchange membrane, anion-exchange membrane, cellophane grafted with ion-selective properties, polyvinyl alcohol grafted with ion-selective properties, ceramic separators like NaSiCON, LiSiCON, or combinations thereof.
A twenty-first aspect, which is a high voltage zinc (Zn)-anode battery comprising a cathode comprising a cathode electroactive material; an anode comprising an anode electroactive material, wherein the anode electroactive material comprises a Zn electroactive material; a catholyte in contact with the cathode, wherein the catholyte is not in contact with the anode, and wherein the catholyte has a pH of less than 4; and an anolyte in contact with the anode, wherein the anolyte is not in contact with the cathode, and wherein the anolyte has a pH of greater than 10.
A twenty-second aspect, which is the battery of the twenty-first aspect, further comprising a separator disposed between the anolyte and the catholyte, wherein the separator has ion-selective properties.
A twenty-third aspect, which is the battery of any of the twenty-first and twenty-second aspects, wherein the anolyte comprises a first gelled electrolyte solution, and wherein the catholyte comprises a second gelled electrolyte solution.
A twenty-fourth aspect, which is the battery of any of the twenty-first through twenty-third aspects, wherein the cathode electroactive material comprises at least one of a manganese oxide, manganese dioxide (MnO2), Mn2O3, Mn3O4, MnO; a manganese hydroxide, MnOOH, Mn(OH)2; a silver oxide, AgO, Ag2O; silver (Ag); nickel (Ni); a nickel oxide, NiO, Ni2O3; a nickel hydroxide, NiOOH, Ni(OH)2; a cobalt oxide, Co3O4, CoO; a cobalt hydroxide; lead (Pb); a lead oxide, PbO, Pb02; a copper oxide; copper (Cu); a copper hydroxide; potassium iron oxide (K2FeO4); barium iron oxide (BaFeO4); copper hexacyanoferrate; lithium iron phosphate; lithium nickel manganese cobalt oxide; a lithium manganese oxide, LiMn2O4, Li2MnO3; calix[4]quinone; 1,4-napththoquinone; 9,10-anthraquinone; and any mixture thereof.
A twenty-fifth aspect, which is the battery of any of the twenty-first through twenty-fourth aspects, wherein the cathode comprises a conductive carbon, wherein the conductive carbon is mixed with the cathode electroactive material, and wherein the conductive carbon comprises graphite, carbon fiber, carbon black, acetylene black, single walled carbon nanotubes, multi-walled carbon nanotubes, nickel coated carbon nanotubes, copper coated carbon nanotubes, dispersions of single walled carbon nanotubes, dispersions of multi-walled carbon nanotubes, graphene, graphyne, graphene oxide, and combinations thereof.
A twenty-sixth aspect, which is the battery of any of the twenty-first through twenty-fifth aspects, wherein the cathode comprises an additive and/or dopant, and wherein the additive and/or dopant comprises bismuth, bismuth oxide, copper oxide, copper, indium, indium hydroxide, indium oxide, aluminum, aluminum oxide, nickel, nickel hydroxide, nickel oxide, silver, silver oxide, cobalt, cobalt oxide, cobalt hydroxide, lead, lead oxide, lead dioxide, quinones, or a combination thereof.
A twenty-seventh aspect, which is the battery of any of the twenty-first through twenty-sixth aspects, wherein the cathode comprises a binder, and wherein the binder comprises methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroypropyl cellulose (HPH), hydroypropylmethyl cellulose (HPMC), hydroxethylmethyl cellulose (HEMC), carboxymethylhydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON, or a combination thereof.
A twenty-eighth aspect, which is the battery of any of the twenty-first through twenty-seventh aspects, wherein the cathode comprises a pressed cathode material on a current collector, wherein the current collector comprises carbon, lead, nickel, steel, stainless steel, nickel-coated steel, nickel plated copper, tin-coated steel, copper plated nickel, silver coated copper, copper, magnesium, aluminum, tin, iron, platinum, silver, gold, bismuth, titanium, cold rolled steel, half nickel and half copper, polypropylene, or any combination thereof.
A twenty-ninth aspect, which is the battery of any of the twenty-eighth aspect, wherein the current collector is a foil, mesh, perforated foil, foam, felt, fibrous, porous block architecture, honey-combed mesh, sponge-shaped, or any combinations thereof.
A thirtieth aspect, which is the battery of any of the twenty-first through twenty-ninth aspects, wherein the cathode comprises 1-99 wt. % of a cathode electroactive material, 1-99 wt. % of a conductive carbon, 0-30 wt. % of an additive and/or dopant, and 0-10 wt. % of a binder, based on a total weight of the cathode.
A thirty-first aspect, which is the battery of any of the twenty-first through thirtieth aspects, wherein the Zn electroactive material is a powder, foil, mesh, foam, sponge, perforated foil, or a combination thereof.
A thirty-second aspect, which is the battery of any of the twenty-first through thirty-first aspects, wherein the anode comprises conductive carbon, wherein the conductive carbon is mixed with the Zn electroactive material, and wherein the carbon comprises graphite, carbon fiber, carbon black, acetylene black, single walled carbon nanotubes, multi-walled carbon nanotubes, nickel coated carbon nanotubes, copper coated carbon nanotubes, dispersions of single walled carbon nanotubes, dispersions of multi-walled carbon nanotubes, graphene, graphyne, graphene oxide, and combinations thereof.
A thirty-third aspect, which is the battery of any of the twenty-first through thirty-second aspects, wherein the anode comprises an additive and/or dopant, and wherein the additive and/or dopant comprises bismuth, bismuth oxide, indium, indium oxide, indium hydroxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, calcium hydroxide, sodium dodecylbenzene sulfonate, polyethylene glycol, zinc oxide, or a combination thereof.
A thirty-fourth aspect, which is the battery of any of the twenty-first through thirty-third aspects, wherein the anode comprises a binder, and wherein the binder comprises methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroypropyl cellulose (HPH), hydroypropylmethyl cellulose (HPMC), hydroxethylmethyl cellulose (HEMC), carboxymethylhydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON, or a combination thereof.
A thirty-fifth aspect, which is the battery of any of the twenty-first through thirty-fourth aspects, wherein the anode comprises a pressed anode material on a current collector, wherein the current collector comprises carbon, lead, nickel, steel, stainless steel, nickel-coated steel, nickel plated copper, tin-coated steel, copper plated nickel, silver coated copper, copper, magnesium, aluminum, tin, iron, platinum, silver, gold, bismuth, titanium, cold rolled steel, half nickel and half copper, polypropylene, or any combination thereof.
A thirty-sixth aspect, which is the battery of any of the twenty-first through thirty-fifth aspects, wherein the anode comprises 1-100 wt. % of a Zn electroactive material, 0-10 wt. % of a conductive carbon, 0-30 wt. % of an additive and/or dopant, and 0-10 wt. % of a binder, based on a total weight of the anode.
A thirty-seventh aspect, which is the battery of any of the twenty-first through thirty-sixth aspects, wherein the catholyte comprises an acidic electrolyte; and wherein the acidic electrolyte comprises at least one of hydrogen phosphate, bicarbonates, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, and any mixture thereof.
A thirty-eighth aspect, which is the battery of the thirty-seventh aspect, wherein the acidic electrolyte is present in the catholyte in a concentration of between about 0.1 M and about 16 M.
A thirty-ninth aspect, which is the battery of any of the twenty-first through thirty-eighth aspects, wherein the catholyte comprises a catholyte additive; and wherein the catholyte additive comprises at least one of manganese sulfate, nickel sulfate, potassium permanganate, manganese chloride, manganese acetate, manganese triflate, bismuth chloride, bismuth nitrate, manganese nitrate, nickel sulfate, nickel nitrate, zinc sulfate, zinc chloride, zinc acetate, zinc triflate, indium chloride, copper sulfate, copper chloride, lead sulfate, sodium persulfate, potassium persulfate, ammonium persulfate, ammonium chloride, vanillin, potassium chloride, sodium chloride, lithium nitrate, lithium chloride, lithium carbonate, lithium acetate, lithium triflate, aluminum trifluoromethanesulfonate, aluminum chloride, aluminum nitrate, potassium sulfate, sodium sulfate, ammonium sulfate, and any mixture thereof.
A fortieth aspect, which is the battery of any of the twenty-first through thirty-ninth aspects, wherein the anolyte comprises an alkaline electrolyte; and wherein the alkaline electrolyte comprises at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, caesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof.
A forty-first aspect, which is the battery of the fortieth aspect, wherein the alkaline electrolyte is present in the anolyte in an amount of 20-60 wt. %, based on the total weight of the anolyte.
A forty-second aspect, which is the battery of any of the twenty-first through forty-first aspects, wherein the anolyte comprises an anolyte additive; and wherein the anolyte additive comprises at least one of vanillin, indium hydroxide, zinc acetate, zinc oxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, sodium dodecylbenzene sulfonate, polyethylene glycol, ethanol, methanol, zinc gluconate, glucose, and any mixture thereof.
A forty-third aspect, which is the battery of any of the twenty-first through forty-second aspects, wherein the catholyte, the anolyte, or both are gelled or polymerized.
A forty-fourth aspect, which is the battery of the second aspect, wherein the separator comprises an ion-selective gel; and wherein the ion-selective gel comprises an ionomer, a bipolar membrane, a cation-exchange membrane, an anion-exchange membrane, a cellophane grafted with ion-selective properties, a polyvinyl alcohol grafted with ion-selective properties, a ceramic separator, NaSiCON, LiSiCON, or any combination thereof.
A forty-fifth aspect, which is the battery of any of the twenty-first through forty-fourth aspects, wherein the battery is characterized by an average discharge potential of from about 2 V to about 5 V.
A forty-sixth aspect, which is the battery of any of the twenty-first through forty-fifth aspects, wherein the battery is characterized by an average discharge potential of equal to or greater than about 3 V.
A forty-seventh aspect, which is a high voltage zinc (Zn)-anode battery comprising a cathode comprising a cathode electroactive material; an anode comprising an anode electroactive material, wherein the anode electroactive material comprises a Zn electroactive material; a catholyte in contact with the cathode, wherein the catholyte is not in contact with the anode, and wherein the catholyte has a pH of less than 2; an anolyte in contact with the anode, wherein the anolyte is not in contact with the cathode, and wherein the anolyte has a pH of greater than 12; and a separator disposed between the anolyte and the catholyte, wherein the separator has ion-selective properties.
A forty-eighth aspect, which is the battery of the forty-seventh aspect, wherein the catholyte comprises an acidic electrolyte; wherein the acidic electrolyte comprises at least one of hydrogen phosphate, bicarbonates, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, and any mixture thereof; and wherein the acidic electrolyte is present in the catholyte in a concentration of between about 1 M and about 16 M.
A forty-ninth aspect, which is the battery of any of the forty-seventh and forty-eighth aspects, wherein the anolyte comprises an alkaline electrolyte; wherein the alkaline electrolyte comprises at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, caesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof; and wherein the alkaline electrolyte is present in the anolyte in an amount of 30-55 wt. %, based on the total weight of the anolyte.
A fiftieth aspect, which is the battery of any of the forty-seventh through forty-ninth aspects, wherein the battery is characterized by an average discharge potential of from about 3 V to about 5 V.
A fifty-first aspect, which is a method of forming a high voltage zinc (Zn)-anode battery, the method comprising disposing a catholyte in contact with a cathode, wherein the cathode comprises a cathode electroactive material, and wherein the catholyte has a pH of less than 4; disposing an anolyte in contact with an anode, wherein the anode comprises a Zn electroactive material, and wherein the anolyte has a pH of greater than 10; and disposing at least one of a separator or a buffer layer between the anolyte and the catholyte, wherein the catholyte is not in contact with the anode, and wherein the anolyte is not in contact with the cathode.
A fifty-second aspect, which is the method of the fifty-first aspect, further comprising disposing the catholyte, the anolyte, the anode, the cathode, and the separator or buffer layer in a housing to form the high voltage Zn-anode battery.
A fifty-third aspect, which is the method of any of the fifty-first and fifty-second aspects, wherein the separator or buffer layer has ion-selective properties.
A fifty-fourth aspect, which is the method of any of the fifty-first through fifty-third aspects, wherein the catholyte comprises an acidic electrolyte; wherein the acidic electrolyte comprises at least one of hydrogen phosphate, bicarbonates, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, and any mixture thereof; and wherein the acidic electrolyte is present in the catholyte in a concentration of between about 1 M and about 16 M.
A fifty-fifth aspect, which is the method of any of the fifty-first through fifty-fourth aspects, wherein the anolyte comprises an alkaline electrolyte; wherein the alkaline electrolyte comprises at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, caesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof; and wherein the alkaline electrolyte is present in the anolyte in an amount of 30-55 wt. %, based on the total weight of the anolyte.
A fifty-sixth aspect, which is a method for producing energy comprising discharging a high voltage zinc (Zn)-anode battery to a discharge voltage to produce energy, wherein the high voltage Zn-anode battery comprises a cathode comprising a cathode electroactive material; an anode comprising an anode electroactive material, wherein the anode electroactive material comprises a Zn electroactive material comprising Zn, and wherein at least a portion of the Zn of the Zn electroactive material is oxidized during the discharging to form oxidized zinc; a catholyte in contact with the cathode, wherein the catholyte is not in contact with the anode, and wherein the catholyte has a pH of less than 4; and an anolyte in contact with the anode, wherein the anolyte is not in contact with the cathode, and wherein the anolyte has a pH of greater than 10; and charging the high voltage Zn-anode battery to a charge voltage, wherein at least a portion of the oxidized zinc is reduced to Zn during the charging.
A fifty-seventh aspect, which is the method of the fifty-sixth aspect, wherein the discharge voltage is equal to or greater than about 3 V.
A fifty-eighth aspect, which is the method of any one of the fifty-sixth and fifty-seventh aspects, wherein the catholyte comprises an acidic electrolyte; wherein the acidic electrolyte comprises at least one of hydrogen phosphate, bicarbonates, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, and any mixture thereof; and wherein the acidic electrolyte is present in the catholyte in a concentration of between about 1 M and about 16 M.
A fifty-ninth aspect, which is the method of any one of the fifty-sixth through fifty-eighth aspects, wherein the anolyte comprises an alkaline electrolyte; wherein the alkaline electrolyte comprises at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, caesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof; and wherein the alkaline electrolyte is present in the anolyte in an amount of 30-55 wt. %, based on the total weight of the anolyte.
Embodiments are discussed herein with reference to the Figures. However, those skilled in the art will readily appreciate that the detailed description given herein with respect to these figures is for explanatory purposes as the systems and methods extend beyond these limited embodiments. For example, it should be appreciated that those skilled in the art will, in light of the teachings of the present description, recognize a multiplicity of alternate and suitable approaches, depending upon the needs of the particular application, to implement the functionality of any given detail described herein, beyond the particular implementation choices in the following embodiments described and shown. That is, there are numerous modifications and variations that are too numerous to be listed but that all fit within the scope of the present description. Also, singular words should be read as plural and vice versa and masculine as feminine and vice versa, where appropriate, and alternative embodiments do not necessarily imply that the two are mutually exclusive.
It is to be further understood that the present description is not limited to the particular methodology, compounds, materials, manufacturing techniques, uses, and applications, described herein, as these may vary. It is also to be understood that the terminology used herein is used for the purpose of describing particular embodiments only, and is not intended to limit the scope of the present systems and methods. It must be noted that as used herein and in the appended claims (in this application, or any derived applications thereof), the singular forms “a,” “an,” and “the” include the plural reference unless the context clearly dictates otherwise. Thus, for example, a reference to “an element” is a reference to one or more elements and includes equivalents thereof known to those skilled in the art. All conjunctions used are to be understood in the most inclusive sense possible. Thus, the word “or” should be understood as having the definition of a logical “or” rather than that of a logical “exclusive or” unless the context clearly necessitates otherwise. Structures described herein are to be understood also to refer to functional equivalents of such structures. Language that may be construed to express approximation should be so understood unless the context clearly dictates otherwise.
Unless defined otherwise, all technical and scientific terms used herein have the same meanings as commonly understood by one of ordinary skill in the art to which this description belongs. Preferred methods, techniques, devices, and materials are described, although any methods, techniques, devices, or materials similar or equivalent to those described herein may be used in the practice or testing of the present systems and methods. Structures described herein are to be understood also to refer to functional equivalents of such structures. The present systems and methods will now be described in detail with reference to embodiments thereof as illustrated in the accompanying drawings.
From reading the present disclosure, other variations and modifications will be apparent to persons skilled in the art. Such variations and modifications may involve equivalent and other features which are already known in the art, and which may be used instead of or in addition to features already described herein.
Although Claims may be formulated in this Application or of any further Application derived therefrom, to particular combinations of features, it should be understood that the scope of the disclosure also includes any novel feature or any novel combination of features disclosed herein either explicitly or implicitly or any generalization thereof, whether or not it relates to the same systems or methods as presently claimed in any Claim and whether or not it mitigates any or all of the same technical problems as do the present systems and methods.
Features which are described in the context of separate embodiments may also be provided in combination in a single embodiment. Conversely, various features which are, for brevity, described in the context of a single embodiment, may also be provided separately or in any suitable sub-combination. The Applicants hereby give notice that new claims may be formulated to such features and/or combinations of such features during the prosecution of the present Application or of any further Application derived therefrom.
This application claims the benefit of U.S. Provisional Application No. 62/009,271 filed on Apr. 13, 2020 and entitled, “An Aqueous High Voltage Zinc-Anode Battery,” which is incorporated herein by reference in its entirety for all purposes.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2021/026875 | 4/12/2021 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 63009271 | Apr 2020 | US |
