Aqueous high-voltage zinc anode batteries

Abstract

A high voltage zinc (Zn) anode battery includes a cathode including a cathode electroactive material, an anode including a Zn electroactive material, a catholyte in contact with the cathode but not in contact with the anode, an anolyte in contact with the anode but not in contact with the cathode, and a separator disposed between the anolyte and the catholyte, where the pH of the catholyte is less than 4 and the pH of the anolyte is greater than 10. The separator has ion-selective properties.

Description

[Technical Field]

[0001] CROSS-REFERENCE TO RELATED APPLICATIONS

[0001] This application claims the benefit of U.S. Provisional Application No. 62 / 009,271, filed April 13, 2020, entitled "An Aqueous High Voltage Zinc-Anode Battery," the entire disclosure of which is incorporated herein by reference for all purposes.

[0002] STATEMENT OF GOVERNMENT-SPONSORED RESEARCH OR DEVELOPMENT

[0002] None. [Background technology]

[0003]

[0003] Batteries are becoming increasingly important as several applications requiring portable energy sources enter the consumer market. Portable electronic devices such as smartphones, tablets, and laptops are becoming more multifunctional and require higher energy density to operate for extended periods of time. Portable ventilators for healthcare applications are also being introduced in situations where power is not provided from the grid. Electric vehicles are another major driver for higher energy and power density batteries, where long cycle life and rate capability are almost essential requirements. As batteries become more integrated into devices frequently used by consumers, these batteries must meet stringent safety requirements and must contain non-flammable and non-toxic materials.

[0004]

[0004] Lithium (Li)-ion batteries are typically proposed and used as the battery of choice for personal electronic devices due to their relatively high energy density. However, lithium-ion batteries contain flammable electrolytes and elements such as cobalt, which can catalyze exothermic reactions and are highly toxic. Furthermore, there are ethical concerns regarding the extraction of cobalt from Congolese mines, where artisanal miners are not provided with adequate protection. Unfortunately, unless suitable alternatives are available, lithium-ion batteries will continue to be used.

[0005]

[0005] Metal-aqueous batteries, such as zinc (Zn) anode batteries, are attractive because they are non-flammable, non-toxic, and offer reasonable energy density compared to non-aqueous batteries such as lithium ion, lithium metal, lithium-sulfur, and magnesium ion. The most widely used Zn anode battery is the conventional manganese dioxide (MnO2)-Zn battery, used in the primary battery industry for small-scale applications such as remote controls and home clocks. The widespread use of conventional MnO2|Zn batteries in other applications has been limited by their relatively low nominal voltage of approximately 1.2 V to 1.3 V and their non-rechargeable nature. The aqueous nature of the electrolyte and the reaction of the active materials in either alkaline, acidic, or neutral solutions limit the battery's operating potential window to less than approximately 1.5 V. The relatively limited operating potential window of conventional MnO2|Zn batteries has long been considered a drawback, leading to the development of a variety of relatively high-voltage non-aqueous batteries to replace them. There is a continuing need for batteries that exhibit a relatively wide operating potential window while being non-flammable and non-toxic. Summary of the Invention

[0006] In some embodiments, a high voltage zinc (Zn) anode battery includes a cathode including a cathode electroactive material, an anode including a Zn electroactive material, a catholyte in contact with the cathode but not in contact with the anode, an anolyte in contact with the anode but not in contact with the cathode, and a separator disposed between the anolyte and the catholyte. The catholyte has a pH less than 4 and the anolyte has a pH greater than 10. The separator has ion-selective properties.

[0007] In some embodiments, a method of forming a high voltage zinc (Zn) anode battery includes disposing a catholyte in contact with a cathode including a cathode electroactive material, disposing an anolyte in contact with an anode including a Zn electroactive material, and disposing a separator between the anolyte not in contact with the cathode and the catholyte not in contact with the anode. The catholyte has a pH less than 4 and the anolyte has a pH greater than 10. The separator has ion-selective properties.

[0008]

[0008] These and other features will be more clearly understood from the following detailed description taken in conjunction with the accompanying claims. [Brief explanation of the drawings]

[0009]

[0009] For a more complete understanding of the present disclosure and its advantages, reference is now made to the following brief description, taken in conjunction with the accompanying drawings and detailed description, in which like reference numerals indicate like parts.

[0010] [Figure 1A]

[0010] FIG. 1 shows a schematic diagram of a dual electrolyte MnO2|Zn battery according to some embodiments. [Figure 1B]

[0010] FIG. 1 shows a schematic diagram of a dual electrolyte MnO2|Zn battery according to some embodiments. [Figure 1C]

[0010] FIG. 1 shows a schematic diagram of a dual electrolyte MnO2|Zn battery according to some embodiments. [Figure 1D]

[0010] FIG. 1 shows a schematic diagram of a dual electrolyte MnO2|Zn battery according to some embodiments. [Figure 2]

[0011] The open circuit potential (OCV) and start of discharge of a high-voltage aqueous manganese dioxide (MnO2)|zinc (Zn) battery are shown. [Figure 3]

[0012] Figure 1 shows the discharge curves of a high-voltage aqueous MnO2|Zn battery. [Figure 4]

[0013] Figure 1 shows the discharge curves of a high-voltage aqueous MnO2|Zn battery. [Figure 5]

[0014] Figure 1 shows the discharge curves of a high-voltage aqueous MnO2|Zn battery. [Figure 6]

[0015] Figure 1 shows the open circuit potential of a solid-state high-voltage aqueous MnO2|Zn battery. [Figure 7]

[0016] Figure 1 shows the discharge curves of a high-voltage aqueous MnO2|Zn battery. DETAILED DESCRIPTION OF THE INVENTION

[0011]

[0017] In this disclosure, the terms "negative electrode" and "anode" are both used to mean "negative electrode." Similarly, the terms "positive electrode" and "cathode" are both used to mean "positive electrode." Reference to "electrode" alone can refer to the anode, the 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 is disposed of and replaced after a single discharge. 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 and reused one or more times. As used herein, "catholyte" refers to an electrolyte in contact with the cathode without directly contacting the anode, and "anolyte" refers to an electrolyte in contact with the anode without directly contacting the cathode. The term electrolyte alone can refer to catholyte, anolyte, or an electrolyte in direct contact with both the anode and cathode.

[0012]

[0018] Energy storage systems, such as batteries, are necessary for a variety of applications, including grid-based, electric vehicle, solar storage, and uninterruptible power supplies. Currently, lithium-ion and lead-acid batteries dominate the market; however, they are expensive, flammable, and contain toxic elements. Aqueous-based metal anode systems, such as zinc (Zn) anode batteries, can compete with lithium and lead in volumetric and gravimetric energy density when paired with a cathode made of an inexpensive and abundant material, such as manganese dioxide (MnO). These batteries can deliver >400 Wh / L in aqueous alkaline electrolytes. High energy densities are possible because the theoretical capacities of MnO and Zn, based on first- and second-electron reactions, are approximately 617 mAh / g and 820 mAh / g, respectively.

[0013]

[0019] Attempting to achieve maximum utilization results in irreversibility leading to problems such as volume expansion, breakdown of the crystal structure to form spinel, redistribution of the active material, zinc poisoning of the cathode, passivation of the metal anode, and dendrite shorting. The electrolyte, potassium hydroxide (KOH), is responsible for some of the problems mentioned. During discharge, 4 of the Mn + Status is 3 + state, leading to its increased solubility in high concentrations of KOH at high volumes. 3+ The loss of ions causes the battery to lose capacity. 3+ The ion also dissociates to Mn 4+ and Mn 2+ ions, leading to the formation of lower oxides such as spinel Mn3O4 and pyrochlorite [Mn(OH)2]. Zn can form dissolved zincate ions [Zn(OH)4 2- The reaction is more complex because the anode delivers its capacity through a dissolution reaction that forms ZnO. These dissolved zincate ions also react with dissolved manganese ions to form inert Zn spinels such as ZnMn2O4. Zn anodes can also form dendrites during charging that can penetrate the separator and short-circuit the battery.

[0014]

[0020] Another problem with Zn anodes is the vigorous redistribution of active material during the dissolution reaction, which leads to loss of active ions from the current collector and thus loss of capacity. The cathode also undergoes a large volume expansion during its discharge reaction as protons from the electrolyte are intercalated into the crystalline structure, which leads to delamination of the active material from the current collector and thus again loss of capacity.

[0015]

[0021] This disclosure discloses a high-voltage aqueous Zn anode battery, which has rechargeable properties and can also function as a primary source of power or energy. The high voltage of the battery in this disclosure refers to a battery with 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 by separating the electrolyte on the cathode side from the electrolyte on the anode side and varying the hydrogen activity and hydroxyl activity, respectively. The higher the activity (e.g., hydrogen activity, hydroxyl activity), the higher the potential or voltage of the battery. As described in more detail below, in this battery system, rechargeability is achieved by adding dopants or additives to the electrolyte and / or electrodes.

[0016]

[0022] This disclosure provides a method for creating a high-voltage Zn aqueous battery by varying the hydrogen (or proton) activity and hydroxyl activity on the cathode and anode sides of the battery. Generally, an MnO2 cathode can provide an MnO2|Zn battery for cycling between 1 V and 5 V. Specifically, an MnO2 cathode, as disclosed herein, can provide a high-voltage aqueous MnO2|Zn battery for cycling between 2 V and 5 V. By varying (e.g., increasing) the hydrogen activity on the MnO2 cathode, the discharge potential of the MnO2|Zn battery can be increased to 3-3.5 V as disclosed herein, which is the highest discharge potential achieved for this chemistry. The high-voltage aqueous MnO2|Zn battery disclosed herein can reversibly discharge the theoretical two-electron capacity of MnO2 (617 mAh / g) for thousands of cycles. The high-voltage aqueous MnO2|Zn battery disclosed herein can also be used for primary or single-use applications.

[0017]

[0023] In some embodiments, cathode electroactive materials suitable for use in the cathode of the high voltage aqueous Zn anode batteries disclosed herein include manganese dioxide (MnO), manganese oxide (MnO, MnO, MnO), manganese hydroxide (MnOOH, Mn(OH)), silver oxide (AgO, AgO), silver (Ag), nickel (Ni), nickel oxide (NiO, NiO), nickel hydroxide (NiOOH, Ni), manganese dioxide (MnO), manganese hydroxide (MnOOH, Mn(OH)), manganese dioxide (MnO), manganese oxide (MnO, MnO), manganese hydroxide (MnOOH, Mn(OH)), manganese dioxide (MnO), manganese hydroxide (MnOOH, Mn(OH)), manganese dioxide (MnO), manganese oxide (MnOOH, Mn(OH)), manganese hydroxide (MnOOH, Mn(OH)), manganese dioxide (MnO), manganese oxide (MnOOH, Mn(OH)), manganese hydroxide (MnOOH, Mn(OH)), manganese oxide (MnO ... (OH)2), cobalt oxide (Co3O4, CoO), cobalt hydroxide, lead (Pb), lead oxide (PbO, PbO2), copper oxide (Cu), 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.

[0018]

[0024] In this disclosure, a high-voltage aqueous Zn anode battery may employ an MnO2 cathode. MnO2 cathodes are most commonly paired with Zn anodes in primary alkaline batteries, and their open-circuit potential is typically about 1.5-1.7 V. The average discharge potential of this battery (MnO2|Zn) is about 1.3 V. MnO2|Zn batteries have a relatively high theoretical capacity of 617 mAh / g based on a two-electron reaction. MnO2|Zn batteries exhibit rechargeable characteristics compared to one-electron (308 mAh / g) and two-electron (617 mAh / g) capacities in alkaline electrolytes. Despite the advantageous relatively high capacity characteristics of MnO2|Zn batteries, their relatively high voltage has been considered an Achilles' heel for use in applications such as personal electronic devices. As disclosed herein, the average discharge potential of this battery system can be advantageously increased to about 3 V or greater by varying the hydrogen activity and hydroxyl activity in the catholyte and anolyte of the MnO2 and Zn electrodes, respectively. Conventional MnO2|Zn battery chemistries in aqueous or non-aqueous electrolytes do not achieve discharge potentials above about 3 V. The high-voltage aqueous MnO2|Zn batteries disclosed herein, which exhibit discharge potentials above about 3 V, may begin to be used in personal electronic devices, electric vehicles, and other important applications powering the modern green economy.

[0019]

[0025] The rechargeable properties of MnO2|Zn batteries can be achieved by adding dopants or additives to the electrodes and / or electrolyte. Anode materials 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, as well as any salts thereof, or any combination thereof, can be used in both the cathode and anode. Zn electrodes tend to gas in electrolytes with high hydroxyl activity. To suppress gassing in Zn electrodes, additives such as bismuth, bismuth oxide, indium, indium oxide, indium hydroxide, cationic surfactants such as cetyltrimethylammonium bromide, anionic surfactants such as sodium dodecyl sulfate and sodium dodecylbenzenesulfonate, polyethylene glycol, zinc oxide, carboxymethylcellulose, and polyvinyl alcohol, or any combination thereof, can be used. The electrolyte additive (e.g., catholyte additive) may 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.

[0020]

[0026] Separating electrolytes at different strengths can be important to prevent neutralization reactions. In some embodiments, electrolyte separation can be achieved by electrolyte gelation, which physically prevents electrolyte mixing. The use of crosslinkers and ionomers in the gelation process can also prevent ionic crossover, allowing for the use of cellulosic separators such as cellophane or polymeric separators such as polyvinyl alcohol or crosslinked polyvinyl alcohol. The electrolyte gelation process can be carried out using a free radical polymerization process. Acrylamide and acrylic acid can be mixed with electrolytes with high proton activity or high hydroxyl activity to form long polymer chains. Crosslinkers such as N,N'-methylenebisacrylamide (MBA) can be used to increase the strength, viscosity, and self-healing properties of the polymer. Electrolyte gelation or polymerization can be carried out using initiators such as potassium persulfate, sodium persulfate, or ammonium persulfate. In some embodiments, preventing electrolyte mixing can be achieved by using an ion-selective ceramic separator or membrane, such as LiSiCON, NaSiCON, Nafion membrane, anion exchange membrane, bipolar membrane, or any combination thereof.

[0021]

[0027] The 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 increased cell potential. Higher proton activity on the cathode side and relatively high hydroxyl activity on the anode side can increase the cell potential, which in turn can lead to a higher average discharge voltage and higher energy from the cell.

[0022]

[0028] Disclosed herein is an aqueous Zn anode battery that has both single-use and rechargeable characteristics and can deliver an average discharge capacity between 2 V and 5 V over an operating range between 0 V and 5 V. As an example, this disclosure demonstrates for the first time an average discharge potential of the MnO2|Zn system above about 3 V.

[0023]

[0029] In this disclosure, high-voltage aqueous Zn anode batteries are characterized by an average discharge potential between 2 V and 5 V. This relatively high discharge potential can be achieved by separating electrolytes with different strengths for hydrogen (or proton) activity and hydroxyl activity. High-voltage aqueous Zn anode batteries can be single-use or rechargeable. In some embodiments, long-term rechargeability of high-voltage aqueous Zn anode batteries can be achieved through the use of additives and / or dopants. Separation of the anode and cathode of high-voltage aqueous Zn anode batteries can be achieved through gelation of the electrolyte with an ion-selective ionomer embedded to prevent neutralization by ion migration. Separation of the anolyte and catholyte can also be achieved through the use of ion-selective ceramic and / or polymer membranes.

[0024]

[0030] In this disclosure, the high-voltage aqueous Zn anode battery can be of any geometric form factor as desired. To those skilled in the art, the high-voltage aqueous Zn anode battery can be cylindrical or prismatic. Furthermore, the high-voltage aqueous Zn anode battery can also be flexible as desired by gelling the electrolyte and electrodes or by using a binder in the electrodes that allows flexibility.

[0025]

[0031] 1A-1D , a battery 10 can have a housing 7, a cathode 12, which can include a cathode current collector 1 and a cathode material 2, and an anode 13. In some embodiments, the anode 13 can include an anode current collector 4 and an anode material 5. Note that the scale of the components in FIGS. 1A-1D may not be accurate because the features are drawn to clearly show the electrolyte surrounding the anode 13 and cathode 12. FIGS. 1A-1C show a prismatic battery configuration with a single anode 13 and cathode 12. In another embodiment, the battery can be a cylindrical battery (e.g., as shown in FIG. 1D ) with concentrically arranged electrodes or in a rolled configuration in which the anode and cathode are layered and then rolled to form a jellyroll configuration. The cathode current collector 1 and cathode material 2 are collectively referred to as the cathode 12 or positive electrode 12, as shown in FIG. 1D . Similarly, the anode material 5 with optional anode current collector 4 may be collectively referred to as anode 13 or negative electrode 13. An electrolyte may be in contact with cathode 12 and anode 13. As described in more detail herein, the electrolyte in contact with both cathode 12 and anode 13 may be substantially the same, with different concentrations of protons and hydroxyl ions, or different electrolyte compositions may be used with anode 13 and cathode 12 to modify the properties of battery 10 in some embodiments.

[0026]

[0032] In some embodiments, battery 10 may include one or more cathodes 12 and one or more anodes 13, which may be present in any configuration or form factor. When multiple anodes 13 and / or multiple cathodes 12 are present, the electrodes may be arranged in a layered configuration, with the electrodes alternating (e.g., anode, cathode, anode, etc.). Any number of anodes 13 and / or cathodes 12 may be present to provide a desired capacity and / or output voltage. In a jelly-roll configuration (e.g., as shown in FIG. 1D ), multiple cathodes 12 and anodes 13 may be used in a layered configuration or may be rolled to form a rolled configuration with alternating layers, although battery 10 may have only one cathode 12 and one anode 13 in a rolled configuration such that a cross-section of battery 10 includes a layered configuration of alternating electrodes.

[0027]

[0033] In one embodiment, housing 7 comprises a molded box or container that contains the electrolyte and is generally non-reactive with the electrolyte solution in battery 10. In one embodiment, housing 7 comprises a polymer (e.g., a molded polypropylene box, an acrylic polymer molded box, etc.), a coated metal, or the like.

[0028]

[0034] Cathode 12 may include a mixture of components, including an electrochemically active material (e.g., a cathode electroactive material). Additional components, such as a binder, a conductive material, and / or one or more additional components, may optionally be included that may help improve the life, rechargeability, and electrochemical properties of cathode 12. Cathode 12 may include cathode material 2 (e.g., an electroactive material, additives, etc.). The cathode may include between about 1% and about 95% active material by weight. Suitable cathode materials 2 include manganese dioxide, copper manganese oxide, hausmannite, manganese oxide, copper intercalated bismuth birnessite, birnessite, todorokite, ramsdellite, pyrolusite, pyrochlorite, silver oxide, silver dioxide, silver, nickel oxyhydroxide, nickel hydroxide, nickel, lead oxide, copper oxide, copper dioxide, lead, lead dioxide (alpha and beta), 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 Examples of suitable cathodes include, but are not limited to, nitroxide, bromine, mercury, vanadium oxide, bismuth vanadium oxide, hydroquinone, calix[4]quinone, tetrachlorobenzoquinone, 1,4-naphthoquinone, 9,10-anthraquinone, 1,2-naphthaquinone, 9,10-phenanthrenequinone, a nitroxide-oxoammonium cation redox couple such as 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 may comprise an air electrode.

[0029]

[0035] In some embodiments, the cathode material 2 may be based on one or many polymorphs of MnO, including electrolytic manganese dioxide (EMD), α-MnO, β-MnO, γ-MnO, δ-MnO, ε-MnO, or λ-MnO. Other forms of MnO may also be present, such as hydrated MnO, pyrolusite, birnessite, ramsdellite, hollandite, romanekite, todorokite, lithiophorite, chalcophanite, sodium- or potassium-enriched birnessite, cryptomelane, buserite, manganese oxyhydroxide (MnOOH), α-MnOOH, γ-MnOOH, β-MnOOH, manganese hydroxide [Mn(OH)], partially or fully protonated manganese dioxide, MnO, MnO, bixbite, MnO, lithiated manganese dioxide (LiMnO, LiMnO), CuMnO, 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. Generally, the recycled form of manganese dioxide of the cathode may have a layered structure, which in some embodiments may include δ-MnO2, which is interchangeably referred to as birnessite. When non-birnessite polymorphic forms of manganese dioxide are used, they may be converted to birnessite in situ by one or more conditioning cycles, which are described in more detail below. For example, a full or partial discharge to the end of the second electron stage of MnO2 (e.g., between about 20% and about 100% of the second electron capacity of the cathode) may be performed, followed by the recharging of the MnO2. 4+ state, resulting in birnessite phase manganese dioxide.

[0030]

[0036] In some embodiments, the cathode 12 used in the high voltage aqueous Zn anode batteries disclosed herein can include electroactive materials such as metals, metal oxides, metal salts (e.g., metal sulfides), electroactive polymers, and electroactive organic compounds that are electrochemically active in a high proton activity electrolyte, such as in the catholyte 3. Non-limiting examples of cathode materials 2 that are electrochemically active in a high proton activity electrolyte 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 include pyrolusite, birnessite, ramsdellite, hollandite, romanekite, 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, bixbite, MnO, lithiated manganese dioxide (LiMn2O4), CuMn2O4, zinc manganese dioxide, lead oxide, lead dioxide, copper, copper oxide, and 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 oxide, delithiated nickel oxide, delithiated nickel manganese oxide, delithiated nickel manganese cobalt oxide, quinone compounds such as calix[4]quinone, 1,4-naphthoquinone, 9,10-anthraquinone, or any combination thereof, may also be present in cathode 12. Combinations of electroactive materials may also be employed in cathode material 2. Electroactive cathode material 2 may be in the form of powders of various particle sizes (nanometer to micrometer) and / or in the form of metal substrates having planar, mesh, or perforated structures.

[0031]

[0037] The addition of conductive additives, such as conductive carbon, allows for higher loading of the electroactive material in the cathode material, resulting in higher volumetric and gravimetric energy densities. In some embodiments, the conductive additive may be present in cathode material 2 in an amount of about 1 to 30 weight percent, based on the total weight of cathode material 2. In some embodiments, the conductive additive may include graphite, carbon fiber, carbon black, acetylene black, single-walled carbon nanotubes, multi-walled carbon nanotubes, nickel- or copper-coated carbon nanotubes, single-walled carbon nanotube dispersions, multi-walled carbon nanotube dispersions, graphene, graphene, graphene oxide, or combinations thereof. Higher loading of the electroactive material in the cathode is desirable in some embodiments to increase 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 (e.g., KS15, KS44, KC44, MB15, MB25, MK15, MK25, MK44, MX15, MX25, BNB90, LB family), TIMREX dispersions; ENASCO 150G, 210G, 250G, 260G, 350G, 150P, 250P; SUPER P, SUPER P Li, carbon black (e.g., Ketjenblack EC-300J, Ketjenblack EC-600JD, Ketjenblack EC-600JD powder), acetylene black, carbon nanotubes (single-walled or multi-walled), Zenyatta graphite, and / or combinations thereof.

[0032]

[0038] In some embodiments, the particle size range of the conductive additive can be about 1 to about 50 microns, or between about 2 microns and about 30 microns, or between about 5 microns and about 15 microns. In one embodiment, the conductive additive can include expanded graphite having a particle size range of about 10 to about 50 microns, or between about 20 to about 30 microns. Carbon fibers and nanotubes can have various aspect ratios, with diameters ranging from tens to hundreds of nanometers. In some embodiments, the mass ratio of graphite to conductive additive can be in the range of about 5:1 to about 50:1, or about 7:1 to about 28:1. The total mass fraction of the conductive additive (e.g., the total mass fraction of carbon) in cathode material 2 can be in the range of about 5% to about 99%, or about 10% to about 80%. In some embodiments, the electroactive component of cathode material 2 can be between 1 wt% and 99 wt% of the weight of cathode material 2, and the conductive additive can be between 1 wt% and 99 wt% of the weight of cathode material 2.

[0033]

[0039] In some embodiments, dopants or additives can be added to the cathode material 2 as needed to improve rechargeability and performance. The additives can be in the form of a powder mixed with the electroactive material or in the form of a metal substrate to which electroactive and conductive carbon can be applied. Non-limiting examples of additives suitable for use in the electrode materials of the present 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 dopant or additive can be present in the cathode material 2 in an amount between 0 and 30 wt %, based on the total weight of the cathode material 2.

[0034]

[0040] In some embodiments, the cathode material 2 may also include a conductive component. The addition of a conductive component, such as a metal additive, to the cathode material 2 may be achieved by adding one or more metal powders, such as nickel powder, to the cathode material 2. The conductive metal component may be present in the cathode material 2 at a concentration of between about 0 and 30% by weight. 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 may be added as an oxide and / or a salt. For example, the conductive component may be cobalt oxide, cobalt hydroxide, lead oxide, lead hydroxide, or a combination thereof. In some embodiments, a second conductive metal component is added to serve as a supporting conductive framework for the first and second electronic reactions to occur. The second electronic reaction may involve the addition of Mn 3+ Manganese ions undergo a dissolution-precipitation reaction in which they dissolve in the electrolyte and precipitate in materials such as graphite, resulting in an electrochemical reaction and the formation of non-conductive manganese hydroxide [Mn(OH)2], which ultimately leads to capacity loss in subsequent cycles. Suitable conductive components that can help reduce the solubility of manganese ions include transition metals such as Ni, Co, Fe, and Ti, as well as metals such as Ag, Au, Al, and Ca.

[0035]

[0041] Oxides and salts of such metals are also suitable. Transition metals such as Co and Mn 3+ This can help reduce the solubility of ions. Such conductive metal components may be incorporated into the electrode by chemical or physical means (e.g., ball milling, mortar / pestle, speck mixture). An example of such an electrode contains 5-95% birnessite, 5-95% conductive carbon, 0-50% conductive component (e.g., conductive metal), and 1-10% binder.

[0036]

[0042] In some embodiments, a binder may be used with the cathode material 2. The binder may be present at a concentration between about 0 and 10 wt %, or between about 1 and 5 wt %, based on the weight of the cathode material. In some embodiments, the binder may be used as a thickener and strong binder and include a water-soluble cellulose-based hydrogel crosslinked with a conductive polymer for good mechanical strength. The binder may be a cellulose film sold as cellophane. The binder may be prepared by physically crosslinking a water-soluble cellulose-based hydrogel with a polymer through repeated cooling and thawing cycles. In some embodiments, the binder may include a 0 to 10 wt % carboxymethyl cellulose (CMC) solution crosslinked with 0 to 10 wt % polyvinyl alcohol (PVA) on an equal volume basis. The binder exhibits superior performance compared to traditionally used TEFLON® or PTFE (polytetrafluoroethylene). TEFLON® and PTFE are high-resistivity materials, but are widely used in the industry due to their excellent rollability. However, this does not preclude the use of TEFLON® or PTFE as a binder. Mixtures of TEFLON® or PTFE with aqueous binders and some conductive carbons can be used to create rollable binders. The use of aqueous binders can help achieve a significant portion of the two-electron capacity with minimal capacity loss over many cycles. In some embodiments, the binder can be water-based and have excellent water retention and adhesive properties, helping to maintain conductivity compared to the same cathode using a PTFE binder instead. Examples of suitable water-based hydrogels include, but are not limited to, methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPH), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose (HEC), and combinations thereof. Examples of cross-linked polymers include polyvinyl alcohol, polyvinyl acetate, polyaniline, polyvinylpyrrolidone, polyvinylidene fluoride, polypyrrole, and combinations thereof.In some embodiments, a 0-10 wt% solution of aqueous cellulose hydrogen can be crosslinked with a 0-10 wt% solution of a crosslinked polymer, for example, by repeated freeze / thaw cycles, radiation treatment, and / or chemicals (e.g., epichlorohydrin). The aqueous binder can be mixed with 0-5% PTFE to improve manufacturability.

[0037]

[0043] Cathode material 2 may also include additional elements. The additional elements may be included in cathode materials including bismuth compounds and / or copper / copper compounds, which together enable improved constant current battery cycling of the cathode. When present as birnessite, copper and / or bismuth may be incorporated into the layered nanostructure of birnessite. The resulting birnessite cathode material may exhibit improved cycling and long-term performance due to the copper and bismuth incorporated into the birnessite crystals and nanostructure.

[0038]

[0044] Bismuth compounds may be incorporated into cathode 12 as inorganic or organic salts of bismuth (oxidation states 5, 4, 3, 2, or 1), as bismuth oxide, or as bismuth metal (i.e., elemental bismuth). The bismuth compound may be present in the cathode material at a concentration of between about 1 and 20 weight percent 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 sulfite agar, Examples of suitable bismuth oxides include bismuth oxychloride, bismuth aluminate hydrate, bismuth tungsten oxide, bismuth lead strontium calcium copper oxide, bismuth antimonide, bismuth antimony telluride, yttria-stabilized bismuth oxide (e.g., yttria-doped bismuth oxide), bismuth-lead alloy, bismuth ammonium citrate, 2-naptol bismuth salt, dichloro(tri-o-tolyl)bismuth, dichlorodiphenyl(p-tolyl)bismuth, triphenylbismuth, and / or combinations thereof.

[0039]

[0045] The copper compound may be incorporated into the cathode 12 as an organic or inorganic salt of copper (oxidation state 1, 2, 3, or 4), as copper oxide, or as copper metal (i.e., elemental copper). The copper compound may be present in a concentration of between about 1 and 70 wt% of the weight of the cathode material 2. In some embodiments, the copper compound is present in a concentration of between about 5 and 50 wt% of the weight of the cathode material 2. In other embodiments, the copper compound is present in a concentration of between about 10 and 50 wt% of the weight of the cathode material 2. In still other embodiments, the copper compound is present in a concentration of between about 5 and 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 with oxidation states +1, +2, +3, or +4, including, but not limited to, copper nitrate, copper sulfate, copper chloride, etc. The effect of copper is to change the oxidation and reduction voltage of bismuth. This results in a cathode with complete reversibility during galvanostatic cycling, compared to bismuth-modified MnO2, which cannot even withstand galvanostatic cycling.

[0040]

[0046] Cathode 12 can be fabricated using methods that are feasible for large-scale manufacturing. In the case of an MnO2 cathode, cathode 12 can deliver the entire second electronic capacity of MnO2. In some embodiments, cathode material 2 includes 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 includes 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 is primarily composed of 2-30% by weight of conductive carbon, 0-30% by weight of a conductive metal additive, 1-70% by weight of a copper compound, 1-20% by weight of a bismuth compound, 0-10% by weight of a binder, and the remainder being birnessite or EMD. In another embodiment, the cathode material is primarily composed of 2-30% by weight of conductive carbon, 0-30% by weight of a conductive metal additive, 1-20% by weight of a bismuth compound, 0-10% by weight of a binder, and the remainder being birnessite or EMD.

[0041]

[0047] The resulting cathode may have a porosity in the range of 20% to 85% as measured by mercury intrusion porosimetry, which may be measured in accordance with ASTM D4284-12, "Standard Test Method for Determining Pore Volume Distribution of Catalysts and Catalyst Supports by Mercury Intrusion Porosimetry," using the version current as of the filing date of this application.

[0042]

[0048] The cathode material 2 can be formed on a cathode current collector 1 formed from an electrically conductive material that serves as an electrical connection between the cathode material and an external electrical connection. 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 include carbon felt, carbon foam, conductive polymer mesh, or any combination thereof. The cathode current collector can be formed into a mesh (e.g., expanded mesh, woven mesh, etc.), perforated metal, foam, foil, felt, fibrous structure, porous block structure, perforated foil, wire screen, packaging assembly, or any combination thereof. In some embodiments, the current collector can be formed into or form part of a pocket assembly, in which 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 that extends outside the cathode material 2, as shown on top of cathode 12 in FIG. 1B) can be bonded to the current collector to provide an electrical connection between an external power source and the current collector.

[0043]

[0049] 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 pressed against a pressure of, for example, between 1,000 psi and 20,000 psi (6.9×10 6 Pascal and 1.4 x 10 8 The cathode material 2 may be applied to the cathode current collector 1 by pressing it with a pressure of between 1000 and 1000 Pascals. The cathode material 2 may be applied to the cathode current collector 1 as a paste. The thickness of the resulting cathode 12 may be between about 0.1 mm and about 5 mm.

[0044]

[0050] In some embodiments, the anode material 5 can include an electroactive material, which can be Zn. The Zn can be present in the anode material 5 in powder form or as a metallic structure. The Zn powder can be of various sizes ranging from nanometers to microns. The Zn metallic structure can be a foil, mesh, perforated foil, foam, sponge type, or any combination thereof.

[0045]

[0051] While the present disclosure is specifically described in the context of Zn anodes, it should be understood that other anode electroactive materials (e.g., metals other than Zn) can be used to form high-voltage aqueous metal anode batteries. For example, the use of electrolytes with different properties as described herein can enable the use of a variety of anode materials. In some embodiments, the anode can include lithium, zinc, aluminum, magnesium, iron, calcium, strontium, lanthanum, potassium, sodium, zirconium, titanium, titanium oxide, indium, indium oxide, indium hydroxide, zinc oxide, MnO, heterolite (ZnMnO), vanadium, tin, tin oxide, barium hydroxide, barium, cesium, aluminum hydroxide, copper, bismuth, silicon, carbon, and mixtures of any of these materials. The cells described herein can be formed by pairing any of the cathode materials described herein with any of the anode materials described to the extent that the materials generate a voltage in the presence of a suitable electrolyte (e.g., a suitable anolyte and catholyte, etc.).

[0046]

[0052] In some embodiments, the anode material 5 can include zinc, which can be present as elemental zinc and / or zinc oxide. In some embodiments, the Zn anode mix includes Zn, zinc oxide (ZnO), an electronically conductive material, and a binder. The Zn can be present in the anode material 5 in an amount of about 50% to about 90% by weight, alternatively about 60% to about 80% by weight, or alternatively about 65% to about 75% by weight, based on the total weight of the anode material. Additional elements that can be present in the anode in addition to or in place of zinc include, but are not limited to, lithium, aluminum, magnesium, iron, cadmium, and combinations thereof, each of which can be present in the same or similar amounts as zinc as described herein.

[0047]

[0053] In some embodiments, anode material 5 can include zinc oxide (ZnO), which can be formed to Zn in situ by a charging step during battery operation. In some embodiments, anode material 5 can include ZnO in an amount of about 5% to about 20% by weight, alternatively about 5% to about 15% by weight, or alternatively about 5% to about 10% by weight, based on the total weight of the anode material. As will be appreciated by those skilled in the art and with the benefit of this disclosure, the purpose of ZnO in the anode mix is ​​to provide a source of Zn during the recharging step, and any zinc present can be converted between zinc and zinc oxide during the charge and discharge phases.

[0048]

[0054] In some embodiments, the electrically conductive material may optionally be present in the anode material in an amount of about 5% to about 20% by weight, alternatively about 5% to about 15% by weight, alternatively about 5% to about 10% by weight, based on the total weight of the anode material. As will be appreciated by those skilled in the art, with the benefit of this disclosure, electrically conductive materials may be used in the anode mixture as a conductive agent, for example, to increase the overall electrical conductivity of the anode mixture. Non-limiting examples of electrically conductive materials suitable for use may 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, or a combination thereof. The conductive material may also include 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, graphene, or any combination thereof. In some embodiments, the electrically conductive material used in the anode mix may include metallic conductive powders including copper, bismuth, indium, nickel, silver, tin, and the like, or any combination thereof.

[0049]

[0055] The anode material 5 may also include a binder. Generally, the binder functions in contact with the current collector to hold the electroactive material particles together. The binder may be present at a concentration of 0 to 10% by weight. The binder in the anode material 5 may also include any of the binders described herein for the cathode material. Binders may be used as thickeners and strong binders, such as methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPH), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, and hydroxyethyl cellulose (HEC). They may also include water-soluble cellulose-based hydrogels crosslinked with conductive polymers, such as polyvinyl alcohol, polyvinyl acetate, polyaniline, polyvinylpyrrolidone, polyvinylidene fluoride, and polypyrrole, to provide good mechanical strength. The binder may be a cellulose film sold as cellophane. The binder may also be PTFE, a highly resistive material widely used in the industry due to its excellent rollability. 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 %, alternatively from about 4 wt % to about 6 wt %, based on the total weight of the anode material.

[0050]

[0056] In some embodiments, the anode material 5 may be used by itself without a separate anode current collector 4, although a tab or other electrical connection may still be provided to the anode material 5. In this embodiment, the anode material may have the form or structure of a foil, mesh, perforated layer, foam, felt, or powder. For example, the anode may include a metal foil electrode, a mesh electrode, or a perforated metal foil electrode.

[0051]

[0057] In some embodiments, anode 13 can include an optional anode current collector 4. Anode current collector 4 can be used with anode 13, including any of those described with respect to cathode 12. Anode material 5 can be pressed against anode current collector 4 to form anode 13. For example, anode material 5 can be pressed against anode current collector 4 at, for example, between 1,000 psi and 20,000 psi (6.9×10 6 Pascal and 1.4 x 10 8 The anode material 5 may be applied to the anode current collector 4 by pressing it with a pressure of between 1000 and 1000 Pascals. The anode material 5 may be applied to the anode current collector 4 as a paste. The tab of the anode current collector 4, if present, may extend outside the device to form a current collector tab. The thickness of the resulting anode 13 may be between about 0.1 mm and about 5 mm.

[0052]

[0058] In some embodiments, cathode and anode materials with corresponding electroactive materials can also be formed from dissolved salts in the corresponding electrolytes (e.g., catholyte and anolyte, respectively). The process of forming cathode and anode materials from dissolved salts in the corresponding electrolytes includes a charging or forming step in which dissolved salts containing active ions are plated onto a current collector by electrons flowing from an external circuit. For example, manganese salts such as manganese sulfate, manganese triflate, etc., in a highly proton-active electrolyte electroplate MnO during the charging or forming step. Similarly, zinc oxide dissolved in the anolyte forms Zn during the charging or forming step.

[0053]

[0059] 1B, battery 10 may not include a separator. The ability to form battery 10 without a separator may allow for a reduction in the overall cost of the battery while having the same or similar performance as a battery with a separator. The use of a polymer gel electrolyte (PGE) for the catholyte and anolyte may perform the function of a separator by forming a physical barrier between anode 13 and cathode 12 to prevent short circuits.

[0054]

[0060] In some embodiments, separator 9 (e.g., as shown in FIGS. 1A and 1C) and / or buffer layer may be disposed between anode 13 and cathode 12 when the electrodes are configured into a battery. Although shown as disposed between anode 13 and cathode 12, separator 9 may be used to encase one or more of anode 13 and / or cathode 12, or one or more of anodes 13 and / or cathodes 12 when multiple anodes 13 and cathodes 12 are present.

[0055]

[0061] The separator 9 may include one or more layers. For example, if a separator is used, 1 to 5 layers of separator may be applied between adjacent electrodes. The separator may 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 may include, but are not limited to, polymer separator layers such as sintered polymer film membranes, polyolefin membranes, polyolefin nonwoven membranes, cellulose membranes, cellophane, battery-grade cellophane, hydrophilically modified polyolefin membranes, and the like, or combinations thereof. As used herein, the phrase "hydrophilically modified" refers to a material having a contact angle with water of less than 45°. In another embodiment, the material used in the separator has a contact angle with water of less than 30°. In yet another embodiment, the material used in the separator has a contact angle with water of less than 20°. The polyolefin may be modified, for example, by the addition of TRITON X-100™ or oxygen plasma treatment. In some embodiments, separator 9 may include a CELGARD® brand microporous separator. In one embodiment, separator 9 may include an FS 2192 SG membrane, a polyolefin nonwoven membrane commercially available from Freudenberg, Germany. In some embodiments, the separator may include a lithium superionic conductor (LISICON®), a sodium superionic conductor (NASICON®), a NAFION®, a bipolar membrane, a water electrolysis membrane, a composite of polyvinyl alcohol and graphene oxide, polyvinyl alcohol, cross-linked polyvinyl alcohol, or a combination thereof.

[0056]

[0062] Separator 9 can comprise a variety of materials, but if more than one separator is present, the use of a PGE for the electrolyte can allow for the use of a relatively inexpensive separator 9. For example, separator 9 can comprise CELLOPHANE®, polyvinyl alcohol, CELGARD®, a composite of polyvinyl alcohol and graphene oxide, cross-linked polyvinyl alcohol, PELLON®, and / or a carbon-polyvinyl alcohol composite. The use of separator 9 can help improve the cycle life of battery 20, but is not required in all embodiments.

[0057]

[0063] If a buffer layer is used, it can be used alone or in combination with the separator 9. The buffer layer can include a gelled solution that can have the same electrolyte formulation as the anolyte and / or catholyte. For example, the buffer layer can be a PGE as described herein. One or more additives, such as calcium hydroxide, layered double hydroxides such as hydrotalcites, quintinite, vogelite, magnesium hydroxide, or combinations thereof, can also be present in the buffer layer. For example, if the anolyte and catholyte have substantially the same formulation and differ only in proton and hydroxyl anion composition and / or viscosity, the electrolyte concentration in the buffer layer can be the same as or between the anolyte and catholyte concentrations. The buffer layer can have a higher viscosity than either the anolyte or catholyte to help prevent mixing between the anolyte and catholyte, as well as limiting ion migration between the two.

[0058]

[0064] As shown in FIGS. 1A-1D , catholyte 3 may be in contact with cathode 12, and anolyte 6 may be in contact with anode 13. As described in more detail herein, one or both of catholyte 3 and / or anolyte 6 may be polymerized or gelled to form a separate gel electrolyte to prevent mixing between the two electrolyte solutions. Catholyte 3 may be disposed within housing 10 in contact with cathode material 2. In some embodiments, anolyte 6 may be polymerized or gelled, and catholyte 3 may be a liquid. Polymerization of anolyte 6 may prevent mixing between catholyte 3 and anolyte 6, even when catholyte 3 is a liquid. In some embodiments, both catholyte 3 and anolyte 6 are gelled.

[0059]

[0065] The electrolyte on the cathode side (e.g., catholyte 3) has a relatively high proton activity, which determines the potential of the battery. The higher the proton activity in the catholyte, the higher the potential of the battery. The acid dissociation constant (K a ) is a relatively good indicator for determining the activity of protons. a Non-limiting examples of acids ranging from low to very high include hydrogen phosphate, bicarbonate, 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 acid is a highly proton-active superacid, and the use of these acids can help significantly improve battery potential.

[0060]

[0066] Catholyte 3 can be an acidic solution whose pH 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, alternatively between -1.2 and 1. Catholyte 3 can be used at temperatures ranging between 0°C and 200°C. In some embodiments, the catholyte can include an acid, such as a mineral acid (e.g., hydrochloric acid, nitric acid, sulfuric acid, etc.). For acidic catholyte compositions, the acid concentration (e.g., the concentration of the acidic electrolyte) can be between about 0.0001M and about 16M, alternatively between about 0.001M and about 16M, alternatively between about 0.01M and about 16M, alternatively between about 0.1M and about 16M, alternatively between about 1M and about 16M.

[0061]

[0067] In some embodiments, the hydrogen activity of the catholyte 3 can be varied by using acids of different strengths. a is a relatively good indicator of acid strength. a The following electrolytes or ions, ranging from low to very high, can be used: hydrogen phosphate, bicarbonate, 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 be useful for modifying the hydrogen (or proton) activity, it will be apparent to those skilled in the art of chemistry or electrochemistry that any combination of acidic electrolytes with other electrolytes can be used to vary the proton activity.

[0062]

[0068] Catholyte additives can help improve the performance of cathode materials. Non-limiting examples of catholyte additives suitable for use in the present 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 the catholyte additive can be between 0M and 5M.

[0063]

[0069] In some embodiments, the catholyte solution may comprise 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, potassium iodide ... The catholyte solution may include a solution containing sodium, 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 alcohol, carboxymethyl cellulose, xantham gum, carrageenan, acrylamide, potassium persulfate, sodium persulfate, ammonium persulfate, N,N'-methylenebisacrylamide, or any combination thereof. For example, the catholyte solution may include manganese sulfate mixed with sulfuric acid or potassium permanganate mixed with sulfuric acid. Other dopants for this solution may be zinc sulfate, lead sulfate, titanium disulfide, titanium sulfate hydrate, silver sulfate, cobalt sulfate, and nickel sulfate. In some embodiments, the catholyte solution can include manganese sulfate, ammonium chloride, ammonium sulfate, manganese acetate, potassium permanganate, and / or permanganate salts, with the additive concentration being between 0M and 10M. Depending on the type of manganese salt used, the voltage of the battery system can vary. For example, with a manganese sulfate electrolyte, the voltage of the SS-HiVAB is approximately 2.45-2.5 V, while with a potassium permanganate electrolyte, the voltage of the SS-HiVAB is approximately 2.8-2.9 V.

[0064]

[0070] In some embodiments, the catholyte may include permanganate. Permanganate has a high positive potential, which may enable an increase in the overall cell potential within the battery 10. If present, the permanganate may be present in a molar ratio of acid (e.g., mineral acid, such as hydrochloric acid or sulfuric acid) to permanganate of about 5:1 to about 1:5, or about 1:1 to about 1:6, or about 1:2 to about 1:4, or about 1:3, although the exact amount may vary based on the expected operating conditions of the battery 10. The concentration of the permanganate (e.g., potassium permanganate or a permanganate salt) may be greater than 0 and less than or equal to 5M. In some embodiments, the catholyte includes sulfuric acid, hydrochloric acid, or nitric acid at a concentration greater than 0.0001M and less than or equal to 16M. The use of permanganate can be advantageous for creating high voltage batteries, as when the use of a catholyte containing permanganate is combined with a high negative anode potential, the resulting battery voltage is about 4 V for MnO2|Zn cathode and anode, and about 2.8 V for MnO2|Al cathode and anode. When the catholyte contains permanganate, suitable permanganates can include, but are not limited to, potassium permanganate, sodium permanganate, lithium permanganate, calcium permanganate, and combinations thereof.

[0065]

[0071] The anode-side electrolyte (e.g., anolyte 6) has a relatively high hydroxyl activity that determines the potential of the battery. The higher the hydroxyl activity in the anolyte, the higher the potential of the battery. Non-limiting examples of alkaline electrolytes or ions with relatively high hydroxyl activity suitable for use in anolyte 6 include ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, or any combination thereof.

[0066]

[0072] In some embodiments, the anolyte can be an alkaline electrolyte (e.g., a relatively alkaline electrolyte), while the catholyte can be an acidic solution (e.g., a relatively 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 10 or greater, alternatively 11 or greater, alternatively 12 or greater, or alternatively 13 or greater. In some embodiments, the pH of the anolyte can be about 10 or greater and about 15.13 or less, alternatively about 11 or greater and about 15.13 or less, alternatively about 12 or greater and about 15.13 or less, alternatively about 13 or greater and about 15.13 or less. As described herein, the anolyte can be polymerized or gelled. The resulting anolyte can be in a semi-solid state that resists flow within the battery. This can help limit or prevent mixing of the anolyte and catholyte. The anolyte may be polymerized using any suitable technique, including any of those described herein. In some embodiments, the alkaline electrolyte may be present in the anolyte in an amount of 1 to 70 wt. %, alternatively 1 to 25 wt. %, alternatively 25 to 70 wt. %, alternatively 20 to 60 wt. %, alternatively 20 to 55 wt. %, alternatively 30 to 55 wt. %, alternatively 1 to 55 wt. %, based on the total weight of the anolyte. Typically, a higher concentration of alkaline electrolyte is used to increase the solubility of the gelled metal in the anolyte. For example, the higher concentration of alkaline electrolyte may be between 25 and 70 wt. % of the anolyte.

[0067]

[0073] In some embodiments, the hydroxyl activity of anolyte 6 may be altered by using bases of different strengths, from low to high, including ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, or any combination thereof. While these examples of alkaline electrolytes may be useful for altering the hydroxyl activity, it will be apparent to one skilled in the art of chemistry or electrochemistry that any combination of alkaline electrolytes with other electrolytes may be used to vary the hydroxyl activity.

[0068]

[0074] In addition to hydroxide, anolyte 6 may include additional components. In some embodiments, the alkaline electrolyte may have zinc oxide, potassium carbonate, potassium iodide, and potassium fluoride as additives. When zinc compounds are present in the anolyte, the anolyte may include 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.

[0069]

[0075] In some embodiments, anolyte 6 may include an electrolyte additive (e.g., an anolyte additive) such as vanillin, indium hydroxide, zinc acetate, zinc oxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, sodium dodecylbenzenesulfonate, polyethylene glycol, ethanol, methanol, zinc gluconate, glucose, or any combination thereof.

[0070]

[0076] In some embodiments, an organic solvent containing a suitable salt can be used as the electrolyte. Examples of suitable organic solvents include, but are not limited to, cyclic carbonates, linear carbonates, dialkyl carbonates, aliphatic carboxylic acid esters, γ-lactones, linear ethers, cyclic ethers, aprotic organic solvents, fluorinated carboxylic acid esters, and combinations thereof. Any suitable additive, including the salts described herein, can be used with the organic solvent to form the organic electrolyte for the anolyte and / or catholyte.

[0071]

[0077] In some embodiments, ionic liquids can be used to form gel electrolytes (e.g., gelled anolytes, gelled catholytes, etc.). Ionic liquids can include 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, 1-ethyl-3-methylimidazolium bromide, 1-ethyl-3-methylimidazolium tetrachloroaluminate, lithium hexafluorophosphate (LiPF), 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 being mixed with an aluminum salt to form an aluminum ion-conducting electrolyte. The aluminum salt can be aluminum chloride, aluminum acetate, aluminum nitrate, aluminum bromide, etc. The mixture of EMImCl and aluminum chloride can be prepared by slowly adding the correct amount of aluminum chloride in an inert atmosphere. The ratio of aluminum chloride to EMImCl can be between 5:1 and 1:1, or about 1.5:1.

[0072]

[0078] In some embodiments, a water-in-salt electrolyte can be gelled and used as a catholyte and / or an anolyte. A water-in-salt electrolyte can include an electrolyte in which the salt concentration exceeds the saturation point. The activity of water in an aqueous electrolyte can be further reduced by increasing the salt concentration beyond the saturation point to form a water-in-salt electrolyte. The ionic conductivity of such an electrolyte can be higher than that of a typical aqueous electrolyte. A water-in-salt electrolyte can include water with an appropriate salt above its saturation point, including any of the salts and additives described herein for aqueous anolyte and / or aqueous catholyte.

[0073]

[0079] To prevent neutralization, the anolyte and catholyte must be kept separate or isolated. Such separation can be achieved by the use of a separator, through gelation or polymerization of the electrolyte, and any combination thereof.

[0074]

[0080] One or both of the anolyte and catholyte can be gelled within the battery. The polymerization process can be carried out with any electrolyte, including any of those described herein (e.g., organic, aqueous, ionic liquid, water-in-salt, etc.). Several polymerization techniques can be used to form the gel / solid electrolyte, such as, for example, step-growth, chain-growth, emulsion polymerization, solution polymerization, suspension polymerization, precipitation polymerization, photopolymerization, etc. Once the gel / solid electrolytes are formed through the polymerization step, they can be combined into a single battery housing as described herein. The battery can use a separator or can be membraneless or separatorless.

[0075]

[0081] As described herein, the electrolyte can be polymerized or gelled to form a polymer gel electrolyte (PGE) for the catholyte and / or anolyte. The resulting PGE can be in a semi-solid state that resists flow within the battery. For example, the PGE can include an inert hydrophilic polymer matrix impregnated with an aqueous electrolyte. The electrolyte can be polymerized using any suitable technique. In one embodiment, a method for forming the PGE can begin with the selection of a monomer material for the PGE. The monomer can be a polar vinyl monomer selected from the group consisting of acrylic acid, vinyl acetate, acrylic ester, vinyl isocyanate, acrylonitrile, or any combination thereof. The components of the aqueous electrolyte can then be selected and can include any of the above components for the electrolyte. An initiator can be added to begin the polymerization process. In some embodiments, a crosslinker can be used in the electrolyte composition to further crosslink the polymer matrix to form the PGE. The monomer (e.g., polar vinyl monomer) in the composition may be present in an amount between about 5% and about 50% by weight, the initiator may be present in an amount between about 0.001% and about 0.1% by weight, and the crosslinker may be present in an amount between 0 and 5% by weight.

[0076]

[0082] In some embodiments, the PGE may be formed in situ, which refers to introducing the electrolyte into the housing as a liquid and subsequently polymerizing to form the PGE within the housing. This method may allow the electrolyte composition to soak into the voids, anode, and / or cathode before fully polymerizing to form the PGE. In some embodiments, a vacuum (e.g., a pressure less than atmospheric pressure) may be created within the housing 7 upon introduction of the electrolyte into the corresponding compartments. The vacuum may help remove air and allow the electrolyte to penetrate the anode 13, the cathode 12, and / or various voids within the battery 10. In some embodiments, the vacuum may be between about 10 and 29.9 inches of mercury, or between about 20 and 29.9 inches of mercury. The use of a vacuum may help avoid the presence of air pockets within the battery 10 prior to full polymerization of the electrolyte. In some embodiments, the electrodes may be immersed in the electrolyte solution for 1 to 120 minutes at a temperature between 0°C and 30°C prior to full polymerization of the electrolyte to allow the electrolyte to impregnate the electrodes. Once the electrolyte is polymerized, the battery may be allowed to rest before use. In some embodiments, the battery may be allowed to rest for between 5 minutes and 24 hours.

[0077]

[0083] To aid in impregnating the electrodes with electrolyte, the electrodes may be pre-soaked in a selected electrolyte solution before polymerizing the electrolyte. This may be done by immersing the electrodes in the electrolyte (e.g., catholyte or anolyte separately) outside the battery or housing, and then placing the pre-soaked electrodes in the housing to construct the battery. In some embodiments, an electrolyte without a polymer or gelling agent may be introduced into the battery to soak the electrodes in situ. This may include the use of a vacuum to assist in impregnation of the electrodes. The electrodes may be soaked for between about 1 minute and 24 hours. In some embodiments, soaking may be performed over multiple cycles, in which the battery is filled with electrolyte, allowed to soak, drained, refilled, allowed to soak, and drained as many times as desired. Once the electrodes are soaked and impregnated with the electrolyte, the electrolyte, including the polymer and polymerization agent (e.g., initiator, crosslinker, etc.), may be introduced into the housing and allowed to polymerize to form the final battery.

[0078]

[0084] The electrolyte composition, monomer material, initiator, and formation conditions (e.g., temperature, etc.) can be selected to provide a desired polymerization time that allows the electrolyte composition to adequately soak the components of the batter and absorb and penetrate the electrodes. The temperature can be controlled to control the polymerization process; a relatively low temperature can inhibit or slow polymerization, while a relatively high temperature can shorten the polymerization time or accelerate the polymerization process. Also, increasing the alkaline electrolyte component (e.g., hydroxide) can shorten the polymerization time, and increasing the initiator concentration will shorten the polymerization time. Suitable polymerization times can be between 1 minute and 24 hours, depending on the composition of the electrolyte solution and the temperature of the reaction.

[0079]

[0085] In some embodiments, the anolyte and / or catholyte may be formed via a gelation process, such as a free radical polymerization technique, in which acrylic acid may be used as a monomer. The acrylic acid may be mixed with the anolyte or catholyte until substantially dissolved. A crosslinker, such as N,N'-methylenebisacrylamide (MBA), may be used to enhance the strength of the polymer. For anolytes, the process of mixing acrylic acid and MBA is typically carried out at relatively low temperatures due to the heat generated in the reaction. However, for catholytes, the mixture of acrylic acid and MBA may be heated to 50-200°C. Polymerization may be initiated through the addition of an initiator, such as a persulfate salt, such as potassium persulfate, sodium persulfate, ammonium persulfate, or any combination thereof. An electrolyte additive (e.g., anolyte additive, catholyte additive) may be included during the gelation process. An ionomer may also be added during the gelation process. Non-limiting examples of ionomers that can be added to the electrolyte during the gelation process include perfluorosulfonic acid (PFSA) / polytetrafluoroethylene (PTFE) copolymer in its acid form, or Nafion solutions made from anion exchange ionomers with polyaromatic polymers.

[0080]

[0086] As an example of a polymerization process, a mixture of acrylic acid, N,N'-methylenebisacrylamide, and an alkaline solution can be generated at a temperature of about 0°C. Any additives can then be added to the solution (e.g., gassing inhibitors, additional additives described herein, etc.). For example, if zinc oxide is used in the electrolyte, it can be dissolved in the alkaline solution after mixing the precursor components, and the zinc oxide can be beneficial during the electrochemical cycle of the anode. To polymerize the resulting mixture, an initiator such as potassium persulfate can be added to start the polymerization process and form a solid or semi-solid polymerized electrolyte (e.g., PGE). The resulting polymerized electrolyte can be stable over time once the polymerization process occurs.

[0081]

[0087] As an example, the PGEs described herein can be prepared through a free-radical polymerization process. In certain embodiments, acrylic acid (AA) can be used as a monomer, along with N,N'-methylenebisacrylamide (MBA) as a crosslinker and potassium persulfate (KSO) as an initiator. When preparing the anolyte, an alkaline electrolyte such as KOH can be added to the process and embedded in the anolyte gel / polymer framework. The addition of alkaline electrolyte to AA reduces the concentration of alkaline electrolyte in the polymer gel, resulting in neutralization. Different concentrations of alkaline electrolyte can vary the gelation time. Higher concentrations of alkaline electrolyte typically result in faster gelation, while lower concentrations require longer times. The initiator concentration can also affect the gelation process. Furthermore, the viscosity of the gel can be adjusted by varying the concentrations of the monomer and MBA, which can also affect the ionic conductivity. Similarly, when preparing the catholyte, an acidic electrolyte such as sulfuric acid can be added to the process and embedded in the catholyte gel / polymer framework.

[0082]

[0088] In some embodiments, an ionomer gelation layer may also be created, which may separate the catholyte solution and the anolyte solution, or their gels. The gelation process for forming the ionomer gelation layer is substantially similar to the gelation process for forming the anolyte gel and / or catholyte gel described herein, with the ionomer being added to the electrolyte during the gelation process. The ionomer gel (e.g., the ionomer gelation layer) may also include additives such as potassium sulfate, sodium sulfate, ammonium sulfate, or any combination thereof. Ionomer resins may also be used in the gelation process to produce the ionomer gelation layer.

[0083]

[0089] The polymerization process can occur before construction of the battery 10 or after the cells are constructed. In some embodiments, the electrolyte can be polymerized and placed in trays to form sheets. Once polymerized, the sheets can be cut to the appropriate size and shape, and one or more layers can be used to form the electrolyte in contact with the anode 13. If a preformed PGE is used, additional liquid electrolyte can be introduced into the battery and / or the electrodes can be pre-soaked in the electrolyte before constructing the battery.

[0084]

[0090] In some embodiments, PGEs can be formed using aqueous electrolytes, organic electrolytes, ionic liquids, water-in-salt electrolytes, etc. In some embodiments, aqueous electrolytes can be used in the catholyte and / or anolyte and gelled to form aqueous hydrogels as PGEs. In some embodiments, aqueous hydrogels can be created through a free radical polymerization process. For example, when preparing the anolyte, acrylic acid (AA) can be selected as the monomer, along with N,N'-methylenebisacrylamide (MBA) as the crosslinker and potassium persulfate as the initiator. In aqueous alkaline anolyte, a suitable hydroxide (e.g., potassium hydroxide (KOH), sodium hydroxide, lithium hydroxide, etc.) can be used to form the electrolyte. By neutralizing the hydroxide with AA, the hydroxide can be encapsulated in the hydrogel network. To create the hydrogel, the monomer can be combined with an optional crosslinker until the crosslinker is dissolved. Alternatively, a certain amount of hydroxide can be cooled to slow the reaction. In some embodiments where 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 optional crosslinker can then be added dropwise to the cooled hydroxide solution as the neutralization reaction releases heat. An initiator, such as potassium persulfate, can be added to gel the resulting mixture of hydroxide, monomer, and crosslinker. The mixture can then be allowed to form a PGE. The amounts and concentrations of the components can be varied to achieve different mechanical strengths of the hydrogel. Similarly, when preparing the catholyte, an acidic electrolyte, such as sulfuric acid, can be incorporated into the hydrogel network.

[0085]

[0091] Electrolytes containing ionic liquids can also be used to form PGEs containing any of the ionic liquids described herein. To form PGEs using ionic liquids, a solution of any additives, which may be contained 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 the ionic liquid. To this solution, the ionic liquid along with the additive solution can be mixed 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 an appropriate amount, such as about 1% by weight of the polymerization agent. This final solution can then be heated to form a polymerized gel.

[0086]

[0092] Organic electrolytes containing salts dissolved in organic solvents can also be gelled to form anolytes and / or catholytes. As an example, lithium ion-conducting electrolytes can be gelled using several polymerization techniques, such as ring-opening polymerization, photoinitiated radical polymerization, UV-initiated radical polymerization, thermally initiated polymerization, in situ polymerization, UV irradiation, and electrospinning. Lithium electrolytes can include lithium hexafluorophosphate (LiPF), lithium perchlorate, lithium bis(trifluoromethanesulfonyl)imide, lithium bis(oxalato)borate, and combinations thereof, in organic solvents such as ethylene carbonate, dimethyl carbonate, propylene carbonate, diethyl carbonate, ethyl methyl carbonate, and combinations thereof. An exemplary mixture can include 1 M LiPF in a solvent mixture of ethylene carbonate and dimethyl carbonate. Other solvents can also be used as mixtures to reduce the flammability of organic electrolytes.

[0087]

[0093] The organic electrolyte can be gelled by mixing a selected salt with an 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 and about 5% by weight of the mixture, and the initiator can be added in an amount between about 0.01 and about 1% by weight of the mixture. In some embodiments, a suitable gelling agent for the organic electrolyte can include pentaerythritol tetraacrylate, and the initiator can include azodiisobutyronitrile. The resulting mixture can be gelled (e.g., polymerized) by heating the mixture to about 50 to 90°C, or about 70°C, and holding for 1 to 24 hours.

[0088]

[0094] For aqueous electrolytes that are inherently acidic, such as catholytes, polymerization can be carried out using a number of processes. In certain embodiments, a method for creating an acidic, solid-state gelled aqueous electrolyte can include adding acrylamide to a solution containing manganese sulfate, H2SO4, ammonium sulfate, potassium permanganate, and / or sulfuric acid. The gelling agent, including acrylamide, can be added to the solution and mixed at a temperature between about 70 and 90°C for at least one hour until the solution is homogeneous. After the solution is thoroughly mixed, a crosslinker and initiator can be added to the solution and mixed for 2 to 48 hours until the solution gels.

[0089]

[0095] In some embodiments, the separator comprises an ion-selective gel, which comprises an ionomer, a bipolar membrane, a cation exchange membrane, an anion exchange membrane, ion-selective grafted cellophane, ion-selective grafted polyvinyl alcohol, a ceramic separator, NaSiCON, LiSiCON, or any combination thereof.

[0090]

[0096] The anolyte PGE and catholyte PGE can be used without a separator, but the separation of the catholyte and anolyte can also be achieved through an ion-selective ceramic separator and / or polymer membrane. Cellulose-based membranes, such as cellophane, can also be used to separate the catholyte and anolyte. For example, ceramic separators, such as LiSiCON and / or NaSiCON, can be used to separate the catholyte and anolyte. As another example, polymer membranes with cation exchange properties, such as Nafion, and / or anion exchange membranes can be used to separate the catholyte and anolyte. Polyvinyl alcohol (PVA) and / or cross-linked polyvinyl alcohol (C-PVA) can also be used as polymer separators to separate the catholyte and anolyte. Cellulose-based membranes, PVA, and C-PVA can be grafted with ionomers, which can impart cation and / or anion exchange properties. Bipolar membranes can also be used as separators between the catholyte and anolyte.

[0091]

[0097] Gel or polymer membranes containing LiSiCON and NaSiCON can be made using the procedures described herein for the formation of PGE and / or ionomer gelled layers by using the raw materials used to make ceramic separators.

[0092]

[0098] The cathodes and anodes used in the high voltage aqueous Zn anode batteries disclosed herein can advantageously approach 50-100% of theoretical capacity over a wide range of current densities and material loadings.

[0093]

[0099] The final cell or battery design may use a cathode containing an acidic PGE catholyte and an anode containing an alkaline PGE anolyte, with a separator or buffer layer to prevent mixing of the two PGEs. Batteries with dual electrolytes allow for high reversibility and improved or maximized utilization of the electrodes, and therefore higher energy density. The use of significantly different alkalinities and acidities in the anolyte and catholyte further allows for the average discharge of the battery to be increased to approximately 3 V or more.

[0094]

[0100] In some embodiments, the high-voltage aqueous Zn anode battery disclosed herein can be used to generate energy. For example, a method of generating energy can include (i) discharging the high-voltage aqueous Zn anode battery disclosed herein to a discharge voltage to generate energy, wherein at least a portion of the Zn in the Zn electroactive material is oxidized to form zinc oxide (e.g., ZnO) during discharge, and (ii) charging the high-voltage Zn anode battery to a charge voltage to reduce at least a portion of the zinc oxide to zinc during charging. The discharge voltage can be about 2 V or greater, alternatively about 3 V or greater, alternatively about 3.5 V or greater, alternatively about 2 V to about 5 V, alternatively about 3 V to about 5 V, alternatively about 3.5 V to about 5 V.

[0095] Example

[0101] Having generally described the subject matter, the following examples are provided as particular embodiments of the disclosure and are included to demonstrate its practice and advantages, as well as preferred aspects and features of the invention. Those of skill in the art should appreciate that the techniques disclosed in the examples that follow represent techniques discovered by the inventors to function well in the practice of the invention, and therefore 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 embodiments disclosed and still obtain like or similar results without departing from the inventive scope of this disclosure. It should be understood that the examples are given by way of illustration and are not intended to limit the scope of the claims which follow in any way.

[0096] Example 1

[0102] A schematic diagram of a battery with a prismatic geometry is shown in Figure 1A. The battery can be of any geometric form factor and can be flexible. It can be scaled up to any size (physical and capacity (Ah)) depending on the intended application. Figure 1A shows a schematic diagram of a high-voltage aqueous Zn anode battery.

[0097]

[0103] Manganese dioxide (MnO2), more specifically electrolytic manganese dioxide (EMD), was selected as the cathode in this example. The OCV of a conventional or traditional alkaline MnO2|Zn battery is approximately 1.6 V. In the high-voltage MnO2|Zn aqueous battery disclosed herein, the MnO2 catholyte was selected to be 16 M sulfuric acid, while the Zn anolyte was selected to be 51 wt% potassium hydroxide (KOH). A Nafion 115 membrane was used as the ion-selective membrane. The cathode mixture consisted of 80 wt% MnO2, 15 wt% expanded graphite, and 5 wt% Teflon applied to a titanium current collector. The anode mixture consisted of 95 wt% metallic Zn powder, 2 wt% indium hydroxide and polyethylene glycol, and 3 wt% Teflon applied to 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 and stabilized at approximately 3.4 V for over 3 hours, as shown in Figure 2. Figure 2 displays the open circuit potential (OCV) and start of discharge of a high-voltage aqueous manganese dioxide (MnO2)|zinc (Zn) battery. The catholyte and anolyte were 16 M sulfuric acid and 50 wt.% potassium hydroxide, respectively. The OCV of this battery was approximately 3.4 V. This is the highest OCV for an MnO2|Zn battery reported to date in the patent or academic literature. Upon discharge, the high-voltage MnO2|Zn aqueous battery did not exhibit a significant ohmic potential drop, as shown in Figure 2, with an average discharge potential of over 3 V.

[0098] Example 2

[0104] Another high-voltage MnO2|Zn aqueous battery was constructed with the same cathode and anode mixture composition 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 of MnO2 (617 mAh / g based on two electrons) was calculated using the areal capacity (mAh / cm2). 2) was used to determine the areal capacity. In all examples, the reported areal capacity is based on the two-electron capacity of MnO2 and its mass applied to the titanium current collector. Nafion 115 was also used as the membrane for this battery. The discharge curve for this system is shown in Figure 3, and it can be seen that the average discharge voltage for this battery was between 3.1 V and 3.2 V. Figure 3 also displays the discharge curve for a high-voltage aqueous manganese dioxide (MnO2)|zinc (Zn) battery, where the catholyte and anolyte were 10 M sulfuric acid and 51 wt. % potassium hydroxide, respectively, and the areal capacity of the cathode was 1 mAh / cm. 2 and the average discharge voltage was between 3.1 V and 3.2 V. This example marks the first time in the patent and academic literature that a MnO2|Zn battery with an average discharge potential near 3.2 V has been shown.

[0099] Example 3

[0105] Another high-voltage MnO2|Zn aqueous battery was constructed with experimental details similar to those presented in Example 2. The catholyte and anolyte of this battery system were 14 M sulfuric acid and 35 wt. % potassium hydroxide, respectively. As shown in Figure 4, the average discharge voltage of this battery was also between 3.1 V and 3.2 V. Figure 4 displays the discharge curve of a high-voltage aqueous manganese dioxide (MnO2)|zinc (Zn) battery, except that the catholyte and anolyte were 14 M sulfuric acid and 35 wt. % potassium hydroxide, respectively, and the areal capacity of the cathode was 1.6 mAh / cm. 2 and the average discharge voltage was between 3.1V and 3.2V.

[0100] Example 4

[0106] A high-voltage MnO|Zn aqueous battery was constructed with experimental details similar to those presented in Example 2, except for a high loading of MnO in the cathode. The catholyte and anolyte for this battery system were 13.3 M sulfuric acid with 3.2 M manganese sulfate dissolved in it, and 51 wt. % potassium hydroxide, respectively. The average discharge voltage for this system was 4 mAh / cm, as shown in Figure 5. 2The areal capacity of the cathode was between 2.9 V and 3 V, except for the much higher areal capacity of the MnO2|Zn battery, and the addition of manganese salts improved the rechargeability of the system. Figure 5 displays the discharge curves of a high-voltage aqueous manganese dioxide (MnO2)|zinc (Zn) battery, where the catholyte and anolyte were 13.3 M sulfuric acid with 3.2 M manganese sulfate as an additive and 51 wt.% potassium hydroxide, respectively. The areal capacity of the cathode was 4 mAh / cm2. 2 and the average discharge voltage was between 2.9V and 3V.

[0101] Example 5

[0107] A solid-state MnO2|Zn battery was fabricated with experimental details similar to those presented in Example 2. The solid-state battery had a gelled catholyte and a gelled anolyte. Gelation, or polymerization, was achieved via a free-radical polymerization process. For the catholyte, 10 M acid containing 3.2 M manganese acetate was dissolved in a solution of acrylic acid and MBA. Potassium persulfate initiator was added to the dissolved acid solution to initiate the gelation process. After heating the solution to a temperature above approximately 50 °C to approximately 70 °C, gelation was complete. The formed gel was wet and physically robust. For the anolyte, a 51 wt% potassium hydroxide solution containing indium hydroxide was cooled to 0 °C. Acrylic acid and MBA were added to the cooled solution and stirred until the contents were dissolved. The alkaline solution was maintained at a temperature of 0 °C. Potassium persulfate initiator was then added, and the alkaline solution was allowed to reach near room temperature, resulting in gelation. The integrity and structure of the formed gels depend significantly on the heating and cooling steps of the catholyte and anolyte, respectively. The OCV of this solid-state high-voltage MnO2|Zn battery was measured and recorded at approximately 3.05 V for over 7 hours without loss, as shown in Figure 6. Figure 6 displays the open circuit potential of a solid-state high-voltage aqueous manganese dioxide (MnO2)|zinc (Zn) battery, where the catholyte and anolyte were gelled with 10 M sulfuric acid containing 3.2 M manganese acetate and 51 wt.% potassium hydroxide containing indium hydroxide, respectively. The battery was very stable for 7 hours without any potential degradation. This is the first demonstration of a solid-state MnO2|Zn aqueous battery exceeding 3 V.

[0102] Example 6

[0108] A high voltage MnO2|Zn battery was constructed with experimental details similar to those presented in Example 2. The catholyte for this battery was 1 M nitric acid with 50 wt% sodium persulfate dissolved in the electrolyte. The average discharge voltage of this battery was 4 mAh / cm, as shown in Figure 7. 2 Figure 7 displays the discharge curve of a high-voltage aqueous manganese dioxide (MnO2)|zinc (Zn) battery, where the catholyte and anolyte were 1 M nitric acid with 50 wt. % sodium persulfate as an additive and 51 wt. % potassium hydroxide, respectively, and the cathode had an areal capacity of 4 mAh / cm2. 2 and the average discharge voltage was near 2.92 V. The data in this example demonstrates that an electrolyte with lower proton activity can be used with persulfate to increase the battery potential and obtain a flatter discharge profile.

[0103] Additional Disclosures

[0109] The following is provided as additional disclosure regarding combinations of features and aspects of the subject matter of the present disclosure.

[0104]

[0110] A first embodiment is a high voltage zinc (Zn) anode battery including a cathode including a cathode electroactive material, an anode including a Zn electroactive material, a proton-rich catholyte solution, the catholyte being out of contact with the anode and in contact with the cathode, a hydroxyl-rich anolyte solution, the anolyte being out of contact with the cathode and in contact with the anode, and a separator having ion-selective properties.

[0105]

[0111] A second embodiment is the battery of the first embodiment, wherein the cathode electroactive material is selected from the group consisting of manganese dioxide (MnO2), manganese oxide (Mn2O3, Mn3O4, MnO), manganese hydroxide (MnOOH, Mn(OH)2), silver oxide (AgO, Ag2O), silver (Ag), nickel (Ni), nickel oxide (NiO, Ni2O3), nickel hydroxide (NiOOH, Ni(OH)2), cobalt oxide (Co3O4, CoO), hydroxide Cobalt, 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-naphthoquinone, 9,10-anthraquinone, or combinations thereof.

[0106]

[0112] A third embodiment is the battery of the first embodiment, wherein the anode material containing the Zn electroactive material is a powder, foil, mesh, foam, sponge, perforated foil, or combinations thereof.

[0107]

[0113] A fourth embodiment is the battery of the first embodiment, wherein the cathode comprises a conductive carbon mixed with the cathode active material, the conductive carbon comprising graphite, carbon fiber, carbon black, acetylene black, single-walled carbon nanotubes, multi-walled carbon nanotubes, nickel- or copper-coated carbon nanotubes, a dispersion of single-walled carbon nanotubes, a dispersion of multi-walled carbon nanotubes, graphene, graphene, graphene oxide, or a combination thereof.

[0108]

[0114] A fifth embodiment is the battery of the first embodiment, wherein the cathode comprises an additive or dopant including 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, quinone, or a combination thereof.

[0109]

[0115] A sixth embodiment is the battery of the first embodiment, wherein the cathode comprises a binder comprising methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPH), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON®, or a combination thereof.

[0110]

[0116] A seventh aspect is the battery of any of the first, second, fourth, fifth, and sixth aspects, wherein the cathode is pressed onto a current collector comprising carbon, lead, nickel, steel (e.g., 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, titanium, bismuth, titanium, cold-rolled steel, half nickel and half copper, carbon foam, carbon felt, polypropylene mesh, or any combination thereof.

[0111]

[0117] An eighth embodiment is the battery of the seventh embodiment, wherein the current collector is a foil, a mesh, a perforated foil, a foam, a honeycomb mesh, a sponge shape, or any combination thereof.

[0112]

[0118] A ninth aspect is the battery of any of the first, second, fourth, fifth, and sixth aspects, wherein the cathode comprises 1 to 99 wt. % electroactive material, 1 to 99 wt. % conductive carbon, 0 to 30 wt. % additive, and 0 to 10 wt. % binder.

[0113]

[0119] A tenth aspect is the battery of any of the first and third aspects, wherein the anode material comprises conductive carbon mixed with electroactive Zn, and the carbon comprises graphite, carbon fiber, carbon black, acetylene black, single-walled carbon nanotubes, multi-walled carbon nanotubes, nickel- or copper-coated carbon nanotubes, a dispersion of single-walled carbon nanotubes, a dispersion of multi-walled carbon nanotubes, graphene, graphene, graphene oxide, or a combination thereof.

[0114]

[0120] An eleventh aspect is the battery of any of the first and third aspects, wherein the anode material includes an additive or dopant that is bismuth, bismuth oxide, indium, indium oxide, indium hydroxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, calcium hydroxide, sodium dodecylbenzenesulfonate, polyethylene glycol, zinc oxide, or a combination thereof.

[0115]

[0121] A twelfth aspect is the battery of any of the first, third, tenth, and eleventh aspects, wherein the anode material comprises a binder that is methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPH), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON®, or a combination thereof.

[0116]

[0122] A thirteenth aspect is the battery of any of the first, third, tenth, eleventh, and twelfth aspects, wherein the anode material is pressed onto a current collector comprising carbon, lead, nickel, steel (e.g., 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, titanium, bismuth, titanium, cold-rolled steel, half nickel and half copper, carbon foam, carbon felt, polypropylene mesh, or any combination thereof.

[0117]

[0123] A fourteenth aspect is the battery of any of the first, third, tenth, eleventh, and twelfth aspects, wherein the anode comprises 1-100 wt. % electroactive Zn, 0-10 wt. % conductive carbon, 0-30 wt. % additive or dopant, and 0-10 wt. % binder.

[0118]

[0124] A fifteenth embodiment is the battery of the first embodiment, wherein the proton-active catholyte comprises hydrogen phosphate, bicarbonate, ammonium cation, hydrogen sulfide, acetic acid, hydrogen fluoride, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, hydrogen bromide, hydroiodic acid, triflic acid, or a combination thereof.

[0119]

[0125] A sixteenth embodiment is the battery of any of the first and fifteenth embodiments, wherein the electrolyte additive to the catholyte comprises 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 a combination thereof.

[0120]

[0126] A seventeenth embodiment is the battery of the first embodiment, wherein the high hydroxyl activity anolyte comprises ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, or a combination thereof.

[0121]

[0127] An eighteenth embodiment is the battery of the first embodiment, wherein the electrolyte additive to the anolyte comprises vanillin, indium hydroxide, zinc acetate, zinc oxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, sodium dodecylbenzenesulfonate, polyethylene glycol, ethanol, methanol, zinc gluconate, glucose, or a combination thereof.

[0122]

[0128] A nineteenth aspect is the battery of any of the first, fifteenth, sixteenth, seventeenth, and eighteenth aspects, wherein the catholyte and anolyte can be gelled or polymerized.

[0123]

[0129] A twentieth embodiment is the battery of the first embodiment, in which the separator comprises an ion-selective gel made of an ionomer, a bipolar membrane, a cation exchange membrane, an anion exchange membrane, cellophane grafted with ion-selective properties, polyvinyl alcohol grafted with ion-selective properties, a ceramic separator such as NaSiCON, LiSiCON, or a combination thereof.

[0124]

[0130] A twenty-first embodiment is a high voltage zinc (Zn) anode battery including: a cathode including a cathode electroactive material; an anode including an anode electroactive material including the Zn electroactive material; a catholyte in contact with the cathode but not in contact with the anode, the catholyte having a pH less than 4; and an anolyte in contact with the anode but not in contact with the cathode, the anolyte having a pH greater than 10.

[0125]

[0131] A twenty-second embodiment is the battery of the twenty-first embodiment, further comprising a separator disposed between the anolyte and the catholyte, the separator having ion-selective properties.

[0126]

[0132] A twenty-third aspect is the battery of either of the twenty-first and twenty-second aspects, wherein the anolyte comprises a first gel electrolyte solution and the catholyte comprises a second gel electrolyte solution.

[0127]

[0133] A twenty-fourth embodiment is the battery of any of the twenty-first through twenty-third embodiments, wherein the cathode electroactive material is selected from the group consisting of manganese oxide, manganese dioxide (MnO2), Mn2O3, Mn3O4, MnO; manganese hydroxide, MnOOH, Mn(OH)2; silver oxide, AgO, Ag2O; silver (Ag); nickel (Ni); nickel oxide, NiO, Ni2O3; nickel hydroxide, NiOOH, Ni(OH)2; cobalt oxide, Co3O4, CoO; and cobalt hydroxide. lead (Pb); lead oxide, PbO, PbO2; copper oxide; copper (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; calix[4]quinone; 1,4-naphthoquinone; 9,10-anthraquinone; and any mixture thereof.

[0128]

[0134] A twenty-fifth aspect is the battery of any of the twenty-first to twenty-fourth aspects, wherein the cathode comprises conductive carbon, the conductive carbon mixed with a cathode electroactive material comprising 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, graphene, graphene oxide, and combinations thereof.

[0129]

[0135] A 26th aspect is the battery of any of the 21st to 25th aspects, wherein the cathode includes an additive and / or dopant, and the additive and / or dopant includes 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, quinone, or a combination thereof.

[0130]

[0136] A 27th aspect is the battery of any of the 21st to 26th aspects, wherein the cathode includes a binder, and the binder includes methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPH), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON, or a combination thereof.

[0131]

[0137] A 28th aspect is the battery of any of the 21st to 27th aspects, wherein the cathode comprises a cathode material pressed onto a current collector, and 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.

[0132]

[0138] A 29th embodiment is the battery of any of the 28th embodiments, wherein the current collector is a foil, a mesh, a perforated foil, a foam, a felt, a fiber, a porous block structure, a honeycomb mesh, a sponge shape, or any combination thereof.

[0133]

[0139] A 30th aspect is the battery of any of the 21st to 29th aspects, wherein the cathode comprises, based on the total weight of the cathode, 1 to 99 wt % of the cathode electroactive material, 1 to 99 wt % of the conductive carbon, 0 to 30 wt % of the additive and / or dopant, and 0 to 10 wt % of the binder.

[0134]

[0140] A thirty-first embodiment is the battery of any of the twenty-first to thirtieth embodiments, wherein the Zn electroactive material is a powder, foil, mesh, foam, sponge, perforated foil, or a combination thereof.

[0135]

[0141] A thirty-second aspect is the battery of any of the twenty-first to thirty-first aspects, wherein the anode comprises conductive carbon, the conductive carbon mixed with Zn electroactive material, and 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, graphene, graphene oxide, and combinations thereof.

[0136]

[0142] A thirty-third aspect is the battery of any of the twenty-first to thirty-second aspects, wherein the anode includes an additive and / or dopant, and the additive and / or dopant includes bismuth, bismuth oxide, indium, indium oxide, indium hydroxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, calcium hydroxide, sodium dodecylbenzenesulfonate, polyethylene glycol, zinc oxide, or a combination thereof.

[0137]

[0143] A thirty-fourth embodiment is the battery of any of the twenty-first to thirty-third embodiments, wherein the anode comprises a binder, and the binder comprises methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPH), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, TEFLON, or a combination thereof.

[0138]

[0144] A thirty-fifth embodiment is the battery of any of the twenty-first through thirty-fourth embodiments, wherein the anode comprises an anode material pressed onto a current collector, and 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.

[0139]

[0145] A thirty-sixth aspect is the battery of any of the twenty-first to thirty-fifth aspects, wherein the anode comprises, based on the total weight of the anode, 1 to 100 wt. % Zn electroactive material, 0 to 10 wt. % conductive carbon, 0 to 30 wt. % additives and / or dopants, and 0 to 10 wt. % binder.

[0140]

[0146] A thirty-seventh aspect is the battery of any of the twenty-first to thirty-sixth aspects, wherein the catholyte includes an acidic electrolyte, and the acidic electrolyte includes at least one of hydrogen phosphate, bicarbonate, 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.

[0141]

[0147] A thirty-eighth embodiment is the battery of the thirty-seventh embodiment, wherein the acidic electrolyte is present in the catholyte at a concentration between about 0.1M and about 16M.

[0142]

[0148] A thirty-ninth aspect is the battery of any of the twenty-first to thirty-eighth aspects, wherein the catholyte comprises a catholyte additive, and 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.

[0143]

[0149] A fortieth aspect is the battery of any of the twenty-first to thirty-ninth aspects, wherein the anolyte includes an alkaline electrolyte, and the alkaline electrolyte includes at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof.

[0144]

[0150] A forty-first embodiment is the battery of the fortieth embodiment, wherein the alkaline electrolyte is present in the anolyte in an amount of 20 to 60 wt %, based on the total weight of the anolyte.

[0145]

[0151] A forty-second aspect is the battery of any of the twenty-first to forty-first aspects, wherein the anolyte comprises an anolyte additive, and the anolyte additive comprises at least one of vanillin, indium hydroxide, zinc acetate, zinc oxide, cetyltrimethylammonium bromide, sodium dodecyl sulfate, sodium dodecylbenzenesulfonate, polyethylene glycol, ethanol, methanol, zinc gluconate, glucose, and any mixture thereof.

[0146]

[0152] A forty-third aspect is the battery of any one of the twenty-first to forty-second aspects, wherein the catholyte, the anolyte, or both are gelled or polymerized.

[0147]

[0153] A forty-fourth embodiment is the battery of the second embodiment, in which the separator comprises an ion-selective gel, the ion-selective gel comprising an ionomer, a bipolar membrane, a cation exchange membrane, an anion exchange membrane, ion-selectively grafted cellophane, ion-selectively grafted polyvinyl alcohol, a ceramic separator, NaSiCON, LiSiCON, or any combination thereof.

[0148]

[0154] A forty-fifth aspect is the battery according to any one of the twenty-first to forty-fourth aspects, characterized by an average discharge potential of about 2V to about 5V.

[0149]

[0155] A 46th aspect is the battery according to any one of the 21st to 45th aspects, characterized by an average discharge potential of about 3 V or more.

[0150]

[0156] A forty-seventh embodiment is a high voltage zinc (Zn) anode battery including: a cathode including a cathode electroactive material; an anode including an anode electroactive material including the Zn electroactive material; a catholyte in contact with the cathode but not in contact with the anode, the catholyte having a pH less than 2; an anolyte in contact with the anode but not in contact with the cathode, the anolyte having a pH greater than 12; and a separator having ion-selective properties, the separator disposed between the anolyte and the catholyte.

[0151]

[0157] A forty-eighth embodiment is the battery of the forty-seventh embodiment, wherein the catholyte comprises an acidic electrolyte, the acidic electrolyte comprising at least one of hydrogen phosphate, bicarbonate, 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, present in the catholyte at a concentration of between about 1 M and about 16 M.

[0152]

[0158] A forty-ninth embodiment is the battery of either of the forty-seventh and forty-eighth embodiments, wherein the anolyte comprises an alkaline electrolyte, the alkaline electrolyte comprising at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof, present in the anolyte in an amount of 30 to 55 wt %, based on the total weight of the anolyte.

[0153]

[0159] A fiftieth aspect is the battery of any one of the forty-seventh to forty-ninth aspects, characterized by an average discharge potential of about 3V to about 5V.

[0154]

[0160] A fifty-first aspect is a method of forming a high voltage zinc (Zn) anode battery, comprising: placing a catholyte having a pH less than 4 in contact with a cathode including a cathode electroactive material; placing an anolyte having a pH greater than 10 in contact with an anode including a Zn electroactive material; and disposing at least one of a separator or a buffer layer between the anolyte not in contact with the cathode and the catholyte not in contact with the anode.

[0155]

[0161] A fifty-second embodiment is the method of the fifty-first embodiment, further comprising disposing the catholyte, anolyte, anode, cathode, and separator or buffer layer in a housing to form a high voltage Zn anode battery.

[0156]

[0162] A fifty-third embodiment is the method of either of the fifty-first and fifty-second embodiments, wherein the separator or buffer layer has ion-selective properties.

[0157]

[0163] A fifty-fourth embodiment is the method of any of the fifty-first through fifty-third embodiments, wherein the catholyte comprises an acidic electrolyte, the acidic electrolyte comprising at least one of hydrogen phosphate, bicarbonate, 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, present in the catholyte at a concentration between about 1 M and about 16 M.

[0158]

[0164] A 55th embodiment is the method of any of the 51st to 54th embodiments, wherein the anolyte comprises an alkaline electrolyte, the alkaline electrolyte comprising at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof, present in the anolyte in an amount of 30 to 55 wt. %, based on the total weight of the anolyte.

[0159]

[0165] A fifty-sixth aspect is a method of producing energy, comprising: discharging a high voltage zinc (Zn) anode battery to a discharge voltage to produce energy; the high voltage Zn anode battery comprising: a cathode comprising a cathode electroactive material; an anode comprising an anode electroactive material comprising a Zn electroactive material comprising Zn that is at least partially oxidized during discharge to form zinc oxide; a catholyte in contact with the cathode and having a pH less than 4; and an anolyte in contact with the anode and not in contact with the cathode and having a pH greater than 10; and charging the high voltage Zn anode battery to a charge voltage to reduce at least a portion of the zinc oxide to Zn during charging.

[0160]

[0166] A fifty-seventh embodiment is the method of the fifty-sixth embodiment, wherein the discharge voltage is about 3V or greater.

[0161]

[0167] A fifty-eighth embodiment is the method of either of the fifty-sixth and fifty-seventh embodiments, wherein the catholyte comprises an acidic electrolyte, the acidic electrolyte comprising at least one of hydrogen phosphate, bicarbonate, 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, present in the catholyte at a concentration of between about 1 M and about 16 M.

[0162]

[0168] A fifty-ninth embodiment is the method of any one of the fifty-sixth to fifty-eighth embodiments, wherein the anolyte comprises an alkaline electrolyte, the alkaline electrolyte comprising at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof, present in the anolyte in an amount of 30 to 55 wt.%, based on the total weight of the anolyte.

[0163]

[0169] Embodiments are described herein with reference to the figures. However, it will be apparent to those skilled in the art that the detailed descriptions provided herein with respect to those figures are for explanatory purposes, as the systems and methods go beyond those limited embodiments. For example, it will be appreciated that those skilled in the art will recognize, in light of the teachings described herein, numerous alternative and suitable approaches, depending on the needs of a particular application, to perform the functionality of any given detail described herein beyond the specific implementation choices in the following embodiments described and shown. That is, there are numerous modifications and variations, too numerous to list, but all falling within the scope of the description herein. Also, singular terms should be construed to include plural terms and vice versa, masculine terms should be construed to include feminine terms and vice versa, and suitable and alternative embodiments do not necessarily imply that the two are mutually exclusive.

[0164]

[0170] It is further understood that the specific methodologies, compounds, materials, manufacturing techniques, uses, and applications described herein may vary, and that the descriptions herein are not limited thereto. It is also understood that the terminology used herein is used only for the purpose of describing particular embodiments, and is not intended to limit the scope of the present systems and methods. As used in this specification and the appended claims (this application or any derivative thereof), it should be noted that the singular forms "a," "an," and "the" include plural references 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 should be understood in the most inclusive sense possible. Accordingly, the word "or" should be understood to have the definition of "logical or," not "exclusive or," unless the context clearly dictates otherwise. Structures described herein should also be understood to refer to functional equivalents of such structures. Language that may be interpreted as approximating should be so understood unless the context clearly dictates otherwise.

[0165]

[0171] Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this description belongs. Although any methods, techniques, devices, or materials similar or equivalent to those described herein can be used in the practice or testing of the present systems and methods, the preferred methods, techniques, devices, and materials are described. It should also be understood that structures described herein refer to functional equivalents of such structures. The present systems and methods are described in detail with reference to embodiments thereof, as illustrated in the accompanying drawings.

[0166]

[0172] Other variations and modifications will be apparent to persons skilled in the art from reading the present disclosure, and may involve equivalent and other features that are already known in the art and which may be used instead of or in addition to features already described herein.

[0167]

[0173] Although claims may be formulated to particular combinations of features in this application or any further application derived therefrom, it should be understood that the scope of the present disclosure also includes any novel feature or any novel combination of features explicitly or implicitly disclosed herein, or any generalization thereof, whether or not it relates to the same system or method as presently claimed in any claim, and whether or not it alleviates some or all of the same technical problems as the present system and method.

[0168]

[0174] Features that are described in the context of separate embodiments may also be provided in combination in a single embodiment. Conversely, various features that are, for brevity, described in the context of a single embodiment may also be provided separately or in any suitable subcombination. Applicant hereby notifies that new claims may be formulated to such features and / or combinations of such features during prosecution of this application or any further application derived therefrom.

Claims

1. a cathode comprising a cathode electroactive material; an anode comprising a Zn electroactive material; a catholyte not in contact with the anode, having a pH less than 4, and in contact with the cathode; an anolyte not in contact with the cathode, having a pH greater than 10, and in contact with the anode; 1. A high voltage zinc (Zn) anode battery comprising: the anolyte comprises a first gel electrolyte solution and the catholyte comprises a second gel electrolyte solution; A high voltage zinc (Zn) anode battery, wherein the high voltage zinc (Zn) anode battery is characterized by an average discharge potential of 2V to 5V.

2. 10. The high voltage zinc (Zn) anode battery of claim 1, further comprising a separator disposed between the anolyte and the catholyte, the separator having ion-selective properties.

3. The cathode electroactive material may be manganese oxide, manganese dioxide (MnO ２ ), Mn ２ O ３ , Mn ３ O ４ , MnO; manganese hydroxide, MnOOH, Mn(OH) ２ Silver oxide, AgO, Ag ２ O; silver (Ag); nickel (Ni); nickel oxide, NiO, Ni ２ O ３ Nickel hydroxide, NiOOH, Ni(OH) ２ Cobalt oxide, Co ３ O ４ , CoO; cobalt hydroxide; lead (Pb); lead oxide, PbO, PbO ２ Copper oxide; Copper (Cu); Copper hydroxide; Potassium iron oxide (K ２ FeO ４ ); barium iron oxide (BaFeO ４ ); copper hexacyanoferrate; lithium iron phosphate; lithium nickel manganese cobalt oxide; lithium manganese oxide, LiMn ２ O ４ , Li ２ MnO ３ 10. The high voltage zinc (Zn) anode battery of claim 1, comprising at least one of: calix[4]quinone; 1,4-naphthoquinone; 9,10-anthraquinone, and any mixture thereof.

4. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the cathode comprises conductive carbon mixed with the cathode electroactive material, the conductive carbon comprising 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, graphene oxide, and combinations thereof.

5. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the cathode comprises an additive and / or dopant, the additive and / or dopant comprising 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, quinone, or a combination thereof.

6. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the cathode comprises a binder, the binder comprising methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPC), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, polytetrafluoroethylene, or a combination thereof.

7. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the cathode comprises a cathode material pressed onto a current collector, the current collector comprising 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.

8. 8. The high voltage zinc (Zn) anode battery of claim 7, wherein the current collector is a foil, a mesh, a perforated foil, a foam, a felt, a fiber, a porous block structure, a honeycomb mesh, a sponge shape, or any combination thereof.

9. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the cathode comprises 1 to 99 wt. % cathode electroactive material, 1 to 99 wt. % conductive carbon, 0 to 30 wt. % additives and / or dopants, and 0 to 10 wt. % binder, based on a total weight of the cathode.

10. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the Zn electroactive material is a powder, a foil, a mesh, a foam, a sponge, a perforated foil, or a combination thereof.

11. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the anode comprises conductive carbon mixed with the Zn electroactive material, the conductive carbon comprising 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, graphene oxide, and combinations thereof.

12. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the anode comprises an additive and / or dopant, the additive and / or dopant comprising 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.

13. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the anode comprises a binder, the binder comprising methyl cellulose (MC), carboxymethyl cellulose (CMC), hydroxypropyl cellulose (HPC), hydroxypropyl methyl cellulose (HPMC), hydroxyethyl methyl cellulose (HEMC), carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose (HEC), polyvinyl alcohol, polytetrafluoroethylene, or a combination thereof.

14. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the anode comprises an anode material pressed onto a current collector, the current collector comprising 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.

15. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the anode comprises 1 to 100 wt. % Zn electroactive material, 0 to 10 wt. % conductive carbon, 0 to 30 wt. % additives and / or dopants, and 0 to 10 wt. % binder, based on the total weight of the anode.

16. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the catholyte comprises an acidic electrolyte comprising at least one of hydrogen phosphate, bicarbonate, 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.

17. 17. The high voltage zinc (Zn) anode battery of claim 16, wherein the acidic electrolyte is present in the catholyte at a concentration between 0.1M and 16M.

18. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the catholyte comprises a catholyte additive comprising 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.

19. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the anolyte comprises an alkaline electrolyte, the alkaline electrolyte comprising at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof.

20. 20. The high voltage zinc (Zn) anode battery of claim 19, wherein the alkaline electrolyte is present in the anolyte in an amount of 20 to 60 wt. %, based on the total weight of the anolyte.

21. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the anolyte comprises an anolyte additive, the anolyte additive comprising 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.

22. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the catholyte, the anolyte, or both are gelled or polymerized.

23. 3. The high voltage zinc (Zn) anode battery of claim 2, wherein the separator comprises an ion-selective gel, the ion-selective gel comprising an ionomer, a bipolar membrane, a cation exchange membrane, an anion exchange membrane, cellophane grafted with ion-selective properties, polyvinyl alcohol grafted with ion-selective properties, a ceramic separator, NaSiCON, LiSiCON, or any combination thereof.

24. 10. The high voltage zinc (Zn) anode battery of claim 1, wherein the high voltage zinc (Zn) anode battery is characterized by an average discharge potential of 3V or more and 5V or less.

25. a cathode comprising a cathode electroactive material; an anode comprising a Zn electroactive material; a catholyte in contact with the cathode that is not in contact with the anode and has a pH of less than 2; an anolyte not in contact with the cathode, having a pH greater than 12, and in contact with the anode; a separator having ion-selective properties and disposed between the anolyte and the catholyte; 1. A high voltage zinc (Zn) anode battery comprising: the anolyte comprises a first gel electrolyte solution and the catholyte comprises a second gel electrolyte solution; A high voltage zinc (Zn) anode battery, wherein the high voltage zinc (Zn) anode battery is characterized by an average discharge potential of 3V to 5V.

26. 26. The high voltage zinc (Zn) anode battery of claim 25, wherein the catholyte comprises an acidic electrolyte comprising at least one of hydrogen phosphate, bicarbonate, 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, present in the catholyte at a concentration of between 1 M and 16 M.

27. 26. The high voltage zinc (Zn) anode battery of claim 25, wherein the anolyte comprises an alkaline electrolyte comprising at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof, present in the anolyte in an amount of 30 to 55 wt %, based on a total weight of the anolyte.

28. 1. A method for forming a high voltage zinc (Zn) anode battery, comprising: placing a catholyte having a pH less than 4 in contact with a cathode including a cathode electroactive material; placing an anolyte having a pH greater than 10 in contact with an anode comprising a Zn electroactive material; disposing at least one of a separator or a buffer layer between the anolyte not in contact with the cathode and the catholyte not in contact with the anode; A method comprising: the anolyte comprises a first gel electrolyte solution and the catholyte comprises a second gel electrolyte solution; The method, wherein the high voltage zinc (Zn) anode battery is characterized by an average discharge potential of 3V to 5V.

29. 30. The method of claim 28, further comprising disposing the catholyte, the anolyte, the anode, the cathode, and the separator or buffer layer in a housing to form a high voltage Zn anode battery.

30. 29. The method of claim 28, wherein the separator or buffer layer has ion-selective properties.

31. 29. The method of claim 28, wherein the catholyte comprises an acidic electrolyte comprising at least one of hydrogen phosphate, bicarbonate, 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 is present in the catholyte at a concentration of between 1 M and 16 M.

32. 29. The method of claim 28, wherein the anolyte comprises an alkaline electrolyte comprising at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof, and is present in the anolyte in an amount of 30 to 55 wt. %, based on a total weight of the anolyte.

33. Discharging the high voltage Zn anode battery to a discharge voltage to generate energy; charging the high voltage Zn anode battery to a charging voltage and reducing at least a portion of the zinc oxide to Zn during charging; Including, The high voltage Zn anode battery a cathode comprising a cathode electroactive material; an anode comprising an anode electroactive material comprising Zn electroactive material, the Zn comprising Zn being at least partially oxidized during discharge to form an oxidized anode material; a catholyte not in contact with the anode, having a pH less than 4, and in contact with the cathode; an anolyte not in contact with the cathode, having a pH greater than 10, and in contact with the anode; 1. A method for generating energy, comprising: the anolyte comprises a first gel electrolyte solution and the catholyte comprises a second gel electrolyte solution; The method, wherein the high voltage zinc (Zn) anode battery is characterized by an average discharge potential of 3V to 5V.

34. 34. The method of claim 33, wherein the discharge voltage is 3 V or greater.

35. 34. The method of claim 33, wherein the catholyte comprises an acidic electrolyte comprising at least one of hydrogen phosphate, bicarbonate, 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 is present in the catholyte at a concentration of between 1 M and 16 M.

36. 34. The method of claim 33, wherein the anolyte comprises an alkaline electrolyte comprising at least one of ammonia, methylamine, glycine, lithium hydroxide, sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, and any mixture thereof, and is present in the anolyte in an amount of 30 to 55 wt. %, based on a total weight of the anolyte.

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