A rechargeable electrochemical cell assembled in a discharge state, including metal electrodes.

Abstract

A rechargeable electrochemical battery cell is disclosed. In particular, a rechargeable electrochemical cell is disclosed that is assembled in a discharged state and includes an electrically conductive anode current collector and a cathode that includes a metallic material as an active material when in a discharged state.

Description

Technical Field

[0001] The present invention relates to rechargeable electrochemical cells. In particular, the present invention relates to a rechargeable electrochemical cell assembled in a discharged state, which includes a conductive cathode current collector and a cathode containing a metal material as an active material when in the discharged state.

Background Art

[0002] High-performance and low-cost batteries are advantageous for many applications, such as electric vehicles and energy storage in power grids. The battery technology currently leading the industry is lithium-ion battery technology. The performance of lithium-ion batteries has been dramatically improved over the past few decades as a result of accumulating annual improvements little by little. At the same time, as a result of the expansion of economies of scale, their production costs have been significantly reduced. This is despite the increasing complexity of this technology. Current state-of-the-art batteries employ graphite-based anodes, metal oxide cathodes, and organic electrolytes. Commercially preferred cathode formulations are based on nickel-cobalt-manganese oxide (NCM) formulations. However, the future outlook for this cathode formulation is hampered by the limited annual supply of cobalt, which is known as an obstacle to the expected future increase in battery production. Commercially preferred electrolyte formulations are based on a mixture of LiPF6 electrolyte salt and carbonate solvents. However, the high flammability of these solvents poses a safety hazard and causes battery fire accidents. Furthermore, since the LiPF6 electrolyte salt has low chemical stability, the operating temperature range of the battery is limited, and complicated and costly thermal management of the battery pack is required. To improve cost and performance, alternative battery technologies are needed.

[0003] The present invention aims to solve the above problems related to current state-of-the-art battery cells. The energy density and rate performance of the disclosed invention can be at the same or even higher levels than the performance of currently leading battery cells in the industry, whereby these disclosed improvements do not sacrifice battery performance.

[0004] Furthermore, the disclosed manufacturing technology improvements for this new battery chemistry invention will enable easier and more cost-effective production of battery cells. Since the theoretical energy density of the disclosed electrochemical cells may be similar to that of lithium-ion technology, battery packs will consist of a similar number of cells to those currently available in lithium-ion technology. Therefore, the cell production cost per kWh is expected to be significantly lower than current cell production costs. Moreover, the inertness of the electrolytes that can be used in this invention is in contrast to the operation of lithium-ion batteries, where the electrode-electrolyte interface is stabilized by a passivation layer. In the case of lithium-ion batteries, as a result of the above, even after careful optimization, they can only operate for a few thousand cycles. In contrast, cells manufactured by certain embodiments of the disclosed invention may have cycle lives several orders of magnitude longer, similar to the cycle life of supercapacitors.

[0005] In short, the factors described above predict the high commercial and technological benefits of the battery technology described herein. As a result, the present invention is beneficial to industry and commerce. [Overview of the Initiative]

[0006] Surprisingly, it was discovered that rechargeable batteries can be constructed using metallic materials, such as metal foil as the cathode. Even more surprisingly, it was discovered that rechargeable batteries can be constructed using metallic materials, such as metal foil as both electrodes. Even more surprisingly, it was discovered that rechargeable batteries can be constructed using the same metallic material for both electrodes. Even more surprisingly, it was discovered that rechargeable batteries can be constructed using copper foil for both electrodes. Even more surprisingly, it was discovered that rechargeable batteries can be constructed using only porous metals such as copper foil for both electrodes.

[0007] The present invention discloses a rechargeable electrochemical cell. The electrochemical cell may comprise at least a cathode current collector, an anode current collector, and an electrolyte, which may be at least partially between the cathode current collectors. The electrochemical cell may further comprise a separator between the cathode current collector and the anode current collector. The electrochemical cell may further comprise one or more charge carriers or current collectors. The electrochemical cell may further comprise a housing. The electrochemical cell may be in a charged state, a discharged state, or an intermediate state.

[0008] A rechargeable electrochemical cell assembled in a discharged state is described. When in a discharged state, the cell may include a conductive cathode current collector and a cathode containing a metallic material as the active material. The metallic material may be the primary active material. The metallic material may be the sole active material. The metallic material may be a metal. The metal may be substantially pure. A substantially pure metal may be a single metal, or a mixture, alloy, or compound of substantially pure metals. A substantially pure metal may contain a metallic dopant. The cathode of the electrochemical cell may be in contact with the conductive cathode current collector, or all or part of the cathode may function as the conductive cathode current collector. Metallic deposits may form on and / or within the anode current collector during charging. The metallic deposits may be solid. Salts may form at least partially from the cathode (i.e., the cathode and / or cathode material, e.g., the active material of the cathode) during charging. The anode current collector and cathode may contain substantially the same material (this may include the same combination of material and / or ratio and / or state or form of material). The anode current collector and / or cathode may be doped. The dopant may be of any material. The dopant may be metallic. The dopant may be metallic. The dopant may be substantially pure metallic. The anode current collector and / or cathode may contain copper. The anode current collector and / or cathode may contain copper and metallic dopants. The anode current collector and / or cathode may contain metallic copper. The anode current collector and / or cathode may contain metallic copper and metallic dopants. The metallic copper may be substantially pure metallic copper. The cathode and / or anode current collector may contain zinc dopants. The cathode and / or anode current collector may contain substantially pure metallic copper and zinc dopants. The cathode and / or anode current collector may, when discharged, contain metallic copper or substantially pure metallic copper and dopant. The cathode and / or anode current collector may, when discharged, contain metallic copper and zinc dopant. The cathode and / or anode current collector may, when discharged, contain substantially pure metallic copper and dopant.The dopant may be a metal dopant. The dopant may be a metal dopant. The dopant may be a zinc dopant. An ion exchange structure (e.g., a membrane, film, or separator) may be placed between the anode current collector and the cathode. The ion exchange structure may be an anion exchange membrane. The ion exchange structure may prevent the movement of cations contained in the metal salt formed at the cathode and / or allow for the selective transport of alkali metal cations or anions. The cathode and / or anode current collector may be porous. The cathode and / or anode current collector may be porous due to the evaporation of one or more elements from a metal mixture and / or alloy. The cathode and / or anode current collector may be electrochemically active, for example, by introducing one or more electrochemically active materials into the cathode and / or anode current collector. The polarity of the cell can be reversed so that the cathode becomes the anode current collector and the anode current collector becomes the cathode. The electrochemical cell can be used in a battery pack. Electrochemical cells and / or battery packs can be used in the device.

[0009] In this specification, metallic materials are defined as materials that are approximately 1 × 10⁻⁶ at 20°C. 5This refers to materials with an electrical conductivity greater than σ(S / m). Examples of metallic materials include materials in which electrons are in a three-dimensional delocalized state. Examples of metallic materials may include metals. Examples of metals may include Hg, Dy, Eu, Ce, Er, Ho, La, Pr, Tm, Nd, Y, Sc, Lu, Po, Am, Ti, Zr, Sb, Fr, Ba, Hf, As, Yb, U, Pb, Cs, V, Pa, Re, Tl, Th, Tc, Ga, Nb, Ta, Sr, Cr, Rb, Sn, Pd, Pt, Fe, Li, Os, In, Ru, Cd, K, Ni, Zn, Co, Mo, W, Ir, Na, Rh, Mg, Ca, Be, Al, Au, Cu, Ag, and mixtures, alloys, or combinations thereof. Metallic materials may include allotropes of carbon. Allotropes of carbon include diamond, graphite, graphene, amorphous carbon, fullerene, carbon nanotubes, carbon nanobuds and glassy carbon, carbon nanoforms, lonsdaleite, calvin, or other allotropes of carbon and / or any combination thereof. Other metallic materials are also possible according to the present invention.

[0010] The electrochemical cell of the present invention may be a rechargeable electrochemical cell. The electrochemical cell may include a cathode containing a metallic material as the active material in the discharge state. When the cell is in the discharge state, the cell may contain substantially pure metallic electrodes. The cell can be assembled in the discharge state. The anode and cathode of the electrochemical cell may contain the same metal or metallic alloy, or different metals or metallic alloys. The anode and cathode of the electrochemical cell may have the same composition. The anode and / or cathode of the electrochemical cell may contain metallic copper in the discharge state. The anode and / or cathode of the electrochemical cell may contain substantially pure metallic copper in the discharge state. The anode and / or cathode of the electrochemical cell may be substantially pure copper. The electrodes of the electrochemical cell can be separated by one or more ion exchange structures. One or more ion exchange structures may also function as separators. One or more ion exchange structures may be added to the separator. Ion exchange structures can be combined with separators. The ion exchange structure may be located on the anode and / or cathode side of the separator.

[0011] The anode and / or cathode can be manufactured by any means known in the art. The anode and / or cathode can be manufactured by heat treatment of a precursor metal foil. The heat treatment may be vacuum heat treatment. The heat treatment may produce a porous metal foil and / or foamed metal. The porous foil and / or foam may have a high weight surface area. A high weight surface area is preferably 0.1 m² as specified herein. 2 Greater than / g, more preferably greater than 1, and most preferably 10m 2 This means it is greater than / g. Either or both of the cell's anode current collector and / or cathode may be heat-treated metal foil.

[0012] The foil may be made of a common industrial metal. The industrial metal foil may be brass foil as the input material for the anode current collector and / or cathode. The input brass foil can be heat-treated to produce or reduce to porous copper foil. The foil can be used for both the anode current collector and / or cathode to assemble a cell. This structure creates a simple and cost-effective rechargeable metal-metal battery.

[0013] The metal used may be structured as a microporous foam at one or both electrodes. The electrode metal may be copper or any other suitable metal. On the anode side, metal deposition may occur on the surface of the current collector metal. The deposit may be sodium metal or any other suitable metal. By using a microporous foam structure, the deposited metal, e.g., sodium, can remain within the electrode structure, avoiding variable electrodeposition growth on other electrodes and / or detachment of metal fragments, e.g., sodium fragments, during discharge. On the cathode side, the conversion from a metallic cathode material, e.g., copper, to a metallic salt, e.g., CuBF4 / CuBH4 salt, may proceed without passivating the electrode surface, depending on the surface of the cathode metal, e.g., cathode copper, and the solubility of this salt. By using a microporous foam structure, good power capacity can be ensured and / or space can be created for the deposition of cathode salts, for example, CuI, CuBF4 and / or CuBH4 salts in some embodiments of the present invention, which may have a lower density than the cathode metal, for example, copper.

[0014] The manufacture of porous electrodes can be achieved in many ways. In a preferred method, a multi-component foil, for example, brass foil in the case of manufacturing porous copper foil, can be used as the input material and placed in a heating device, such as a furnace such as a vacuum furnace. By heat treatment at a temperature that removes at least one component of the foil, for example Zn in the case of brass, by evaporation, decomposition, reaction or other means, a porous foil, such as porous copper foil, can be obtained and can be used directly as the anode current collector and / or cathode of a battery assembly. In some cases, it may be advantageous to adjust the process to retain a small amount of the removed material in order to dope the electrode, for example, in the case of brass foil, a small amount, for example, preferably less than 50% of the original Zn, more preferably 25%, more preferably less than 12%, more preferably less than 5%, and most preferably less than 2%, for doping in the electrode. These doped, for example Zn, portions can help seed the electrodeposition of a metal, for example sodium, thereby promoting a more uniform surface coating. According to the present invention, other dopants and methods for incorporating dopants into the electrode are possible. Other multi-component foils can be used as precursor foils according to the present invention. In one embodiment of the present invention, the multi-component foil comprises at least one element that is substantially not removed (e.g., not evaporated or etched) under treatment (e.g., heat treatment), and at least one element that is at least partially removed (e.g., evaporated) during treatment, for example, during heat treatment.

[0015] The electrolyte in an electrochemical cell may remain virtually completely inert throughout the entire battery cycle.

[0016] In this regard, in a preferred embodiment, the disclosed metal-metal battery technology uniquely combines several advantages. • Heat-treated metal foil represents a dramatic simplification of manufacturing compared to current electrode production processes. • All the chemicals that make up a battery cell are abundant and cost-effective. The battery technology described can be easily scaled to any production volume. • Due to the expected high battery life, the life cost of battery cells is significantly improved, and life requirements are met at a higher level.

[0017] The present invention discloses a rechargeable electrochemical cell assembled in a discharged state, which may comprise only a conductive anode current collector as the anode when in the discharged state. The electrochemical cell may comprise a cathode comprising only a metallic material as the active material when in the discharged state. During charging, solid metallic deposits may form on and / or within the anode current collector. According to the present invention, the metallic material may be a metal. The metal may be a transition metal, an alkaline earth metal, a lanthanide and / or a post-transition metal and / or an element of Group 2, Group 3, Group 4, Group 5, Group 6, Group 7, Group 8, Group 9, Group 10, Group 11, Group 12, Group 13, Group 14, Group 15 and / or Group 16.

[0018] A cathode for an electrochemical cell is described, in which the cathode is porous and contains only a metallic material and a dopant as the active material.

[0019] A method for manufacturing a porous electrode or current collector for an electrochemical cell is also disclosed, which includes the following steps: a. A multi-component metal foil is introduced into the heating device. b. Heat the foil in the heating device to a temperature that evaporates, decomposes, reacts with, or otherwise completely or partially removes at least one of the metal components of the multi-component metal foil. [Brief explanation of the drawing]

[0020] [Figure 1] A schematic cross-section of an electrochemical cell according to one embodiment of the present invention in a discharge state. [Figure 2] A schematic cross-section of an electrochemical cell according to one embodiment of the present invention in a charged state. [Figure 3] A schematic cross-sectional view of an electrochemical cell according to one embodiment of the present invention, having a multi-component anode current collector and / or cathode. [Figure 4]Schematic diagram of a metal-metal cell according to an embodiment of the present invention (the left side shows charging). [Figure 5] Operating voltages of two electrodes with respect to the Na standard according to an embodiment of the present invention. The left side shows the change in the anode voltage during sodium deposition / stripping, and the right side shows the change in the cathode voltage during two representative charge-discharge cycles. [Figure 6] Battery cycle data showing verification of an embodiment of the electrochemical cell of the present invention.

Mode for Carrying Out the Invention

[0021] Detailed embodiments of the present invention are disclosed herein with reference to the accompanying drawings.

[0022] The electrochemical cell of the present invention can be a rechargeable electrochemical cell. As used herein, rechargeable means that multiple charging and discharging are possible. The electrochemical cell can be assembled in a discharged state. As used herein, assembling in a discharged state means that when the cell is assembled, the potential or current between the anode current collector and the cathode is maintained at a state where there is no or negligible current. After charging the cell and then discharging the cell, the cell is returned to a discharged state or a state close to the discharged state, and as a result, the cell no longer maintains a non-negligible current or voltage between the anode current collector and the cathode.

[0023] When the cell is in a discharged state, it can include a conductive anode current collector and a cathode containing a metal material as an active material. The anode current collector and / or the cathode can be a metal cathode and / or an anode current collector. The anode current collector and / or the cathode can be a metal cathode and / or an anode current collector. The anode current collector and / or the cathode can be a substantially pure metal or a metal cathode and / or an anode current collector. As used herein, conductivity preferably means higher than 1×10 1 S / m, more preferably higher than 1×10 3 S / m, more preferably higher than 1×10 5Higher than S / m, most preferably 1 × 10 7 This means having a conductivity higher than S / m. In this specification, substantially pure metal means that more than 50%, more preferably more than 75%, more preferably more than 85%, more preferably more than 90%, more preferably more than 95%, more preferably more than 98%, most preferably more than 99% of the material is metal, and / or more than 50%, more preferably more than 75%, more preferably more than 85%, more preferably more than 90%, more preferably more than 95%, more preferably more than 98%, most preferably more than 99% of the atoms in the material are in an oxidation state of zero.

[0024] When charged or partially charged, some or all of the metal cathode material can be converted into metal salts.

[0025] The anode and / or cathode of an electrochemical cell may be in contact with a conductive cathode current collector. The material of the anode and / or cathode current collector can be any suitable conductive material. The material may allow the movement of electrons and / or holes through the material. The contact between the cathode and the cathode current collector may obey Ohm's law. The contact may be by bonding or compression, for example. The bonding may be chemical, mechanical, or any other form of bonding, for example. All or part of the anode and / or cathode may also function as a conductive anode and / or cathode current collector. Metallic deposits may form on and / or inside the anode current collector during charging. Metallic deposits may be formed from elements of the electrolyte or from elements in the electrolyte. Metallic deposits may be formed by electrodeposition and / or reduction, for example. Salts may be formed, at least partially, from the cathode (i.e., the cathode and / or cathode material) during charging. The cathode, in whole or in part, may be converted into a salt during charging. During charging, the salt may be formed from elements of the cathode and / or elements of the electrolyte or elements in the electrolyte. The salt may be formed, for example, by a chemical reaction. The salt may be formed by an electrochemical reaction. The salt may be formed by oxidation. During discharge, the metal may detach from the anode current collector. The detachment may be by a chemical reaction. The detachment may be by an electrochemical reaction. The detachment may be by an oxidation reaction. During discharge, the salt may be completely or partially removed from the cathode or converted within the cathode. During discharge, the salt may revert back to a metal. The removal and / or conversion may be by a chemical reaction. The removal and / or conversion may be by an electrochemical reaction. The removal and / or conversion may be by chemical reduction. In this specification, deposits (e.g., electrodeposits) and products of conversion (e.g., conversion of pure metal to a salt) are generally referred to as formations.

[0026] The cathode and / or anode current collector may be porous. Porous as used herein means that the volume of voids relative to the cathode material and / or anode current collector material is greater than 10%, more preferably greater than 20%, more preferably greater than 50%, and most preferably greater than 75%. The cathode and / or anode current collector can be made porous or manufactured to be porous by any means known in the art, including but not limited to etching or sintering. One particularly cost-effective means is by evaporation of one or more elements from a metal mixture and / or alloy. In such a case, the element to be evaporated has a lower melting point and / or boiling point or a higher vapor pressure than the material held in the foil (i.e., the anode current collector material and / or cathode material), and as a result, upon heating, the element to be evaporated is completely or partially removed from the foil, leaving the porous anode current collector material and / or cathode material.

[0027] The anode current collector and cathode may contain substantially the same material (this may include the same combination and / or ratio and / or state or form of material). The anode current collector and / or cathode may contain metallic copper. The cathode and / or anode current collector may contain substantially pure metallic copper. The cathode and / or anode current collector may contain porous copper. The cathode and / or anode current collector may contain doped copper. The dopant may be any metal. The dopant may be zinc.

[0028] A cathode and / or anode current collector can be made electrochemically active, for example, by introducing one or more electrochemically active materials into the cathode and / or anode current collector. The electrochemically active materials can be introduced by any means known in the art, including but not limited to sputtering, chemical vapor deposition, electrodeposition, alloying, chemical reaction, impact, and coating, or by any other means known in the art.

[0029] An embodiment of the electrochemical cell according to the present invention assembled in a discharge state is shown in Figure 1 (showing a schematic diagram of the cell stack in cross-section). As used herein, a discharge state electrochemical cell may comprise at least an anode current collector (1) and a cathode (2). The anode current collector (1) is also called the discharge state anode. The cathode (2) and / or the anode current collector (1) may function as a substrate and / or matrix (hereinafter referred to as the substrate) for deposition / formation / reaction. The cell may also include a cathode current collector (5). Together, the cathode (2) and the cathode current collector (5), if present, are referred to as the cathode stack (9).

[0030] All or part of the anode (1) and / or cathode (5) current collector and / or cathode (2) and / or cathode stack (9) may be conductive. The anode (1) and / or cathode (5) current collector and / or cathode (2) and / or cathode stack (9) may contain conductive materials. The anode (1) and / or cathode (5) current collector and / or cathode (2) and / or cathode stack (9) may contain non-conductive materials and coatings and / or additives. The anode (1) and / or cathode (5) current collector and / or cathode (2) and / or cathode stack (9) materials and / or coatings and / or additives may be conductive and / or electrochemically active. The anode (1) and / or cathode (5) current collector and / or cathode (2) and / or cathode stack (9) may be coated (e.g., by spraying, dipping, chemical vapor deposition or atomic layer deposition), deposited (e.g., by electrodeposition or sputtering), impregnated, reacted, or by any other means known in the art. The anode (1) and / or cathode (5) current collector and / or cathode (2) and / or cathode stack (9) may include metals, mixtures of metals, and / or alloys. The anode (1) and / or cathode (5) current collector and / or cathode (2) and / or cathode stack (9) may function as a deposition / forming substrate and / or matrix for metals and / or salts during charging and / or discharging. The anode current collector (1) may function as an electroplating substrate. The cathode current collector (5) and / or the cathode (2) and / or the cathode stack (9) may function as a substrate for salt deposition / formation. The cathode (2) and the cathode current collector (5) may be the same.

[0031] As shown in Figure 2, during charging, formations (6, 7) may form on and / or within the cathode and / or anode current collector. The formations may be, for example, metals and / or salts. The combination of the anode current collector (1) and any formation (6) is referred to herein as the anode (8). The combination of the cathode, cathode current collector (if present), and formation (7) (i.e., a charged or partially charged cathode) is also referred to herein as the cathode (2). The cathode (2) and cathode current collector (5) together constitute the cathode stack (9). In summary, the anode (8) and cathode stack (6) are the electrodes.

[0032] As shown in Figure 3, according to one embodiment of the present invention, the anode current collector (1) and / or cathode (2) may comprise a metallic material (10), for example, a pure metal and another dispersion material (11). The metallic material (10) in the anode current collector (1) and / or cathode (2) may be dispersed in a matrix, mixture, or compound (collectively referred to herein as dispersions). The dispersion may comprise an inactive dispersion (11). The inactive dispersion may be conductive. The inactive dispersion may be substantially inert to the electrolyte and / or components dissolved therein, and / or the inactive dispersion may not be electrochemically involved in the operation of the cell. The inactive dispersion may be a polymer and / or a carbonaceous material. The polymer and / or carbonaceous material may be a conductive polymer and / or a carbonaceous material. Conductive polymers may include, for example, poly(fluorene), polyp-phenylene, polypyrene, polyazulene, polynaphthalene, poly(pyrrole) (PPY), polycarbazole, polyindole, polyazepine, polyaniline (PANI), poly(thiophene) (PT), poly(3,4-ethylenedioxythiophene) (PEDOT), poly(p-phenylene sulfide) (PPS), poly(acetylene) (PAC), poly(polyp-phenylenevinylene) (PPV), polyaniline nanofibers, PEDOT:PSS, and / or other conductive polymers and / or mixtures thereof. Carbonaceous materials may be allotropes of carbon. The allotropes of carbon may be, for example, diamond, graphite, graphene, grapheneylene, amorphous carbon, fullerene, carbon nanotubes, carbon nanobuds, schwarzeit, glassy carbon, carbon nanoforms, lonsdaleite, calvin, or other allotropes of carbon or any combination thereof. The dispersion may contain a binder. The anode current collector (1) and cathode (2) may contain the same or different metallic material (10). The anode current collector (1) and cathode (2) may contain the same or different dispersion material (11).

[0033] As shown in Figures 1, 2, and 3, an electrochemical cell may include a spacer and / or separator (3), referred herein to as a spacer. The separator (3) may help prevent contact and / or short circuits between the anode (8) and / or anode current collector (1) and the cathode (2) and / or cathode current collector (5) and / or cathode stack (9). The separator (3) can physically separate the anode (8) and / or anode current collector (1) and the cathode (2) and / or cathode current collector (5) and / or cathode stack (9). The separator may help interrupt dendrite formation between the anode (8) and / or anode current collector (1) and the cathode (2) and / or cathode current collector (5) and / or cathode stack (9). The electrodes of an electrochemical cell may be separated by one or more separators. The separator may function as a substrate or support for another component of the cell. The separator can also function as an ion exchange structure or a support for an ion exchange structure.

[0034] As shown in Figure 1, the electrochemical cell may include one or more ion exchange structures (4a-f). The ion exchange structures may be positioned between the anode (8) and / or anode current collector (1) and the cathode (2) and / or cathode current collector (5) and / or cathode stack (9). The separator (3) may include one or more ion exchange structures (e.g., 4b and / or 4c). One or more ion exchange structures (4a and / or 4d) may also be mounted in and / or incorporated into the anode current collector (1), anode (8), cathode stack (9) and / or cathode (2). The ion exchange structures (4a-f) may also not be mounted in and / or incorporated into any of the anode current collector (1), anode (8), cathode stack (9), cathode (2) or separator (3). The ion exchange structures and separators can be combined as the same structure (not shown). The electrodes of an electrochemical cell can be separated by one or more ion exchange structures (4a-f). One or more ion exchange structures (4a-d) can also function as a separator (3). One or more ion exchange structures (4a-f) can be added to the separator (3). The ion exchange structures (4a-f) can be combined with the separator (3). The ion exchange structures (4a-f) can be attached to the separator (3), deposited on it, or otherwise integrated. The ion exchange structures (4a-f) may be inside and / or on the anode and / or on the cathode side of the separator (3). The ion exchange structures may be, for example, a β-alumina solid electrolyte, for example, an anion exchange membrane based on an ionomer, for example, Nafion, or any other material and / or structure that facilitates the selective transport of cations and / or anions present in the electrolyte. According to the present invention, there may be 0, 1, 2, 3, 4 or more ion exchange structures.

[0035] An electrochemical cell may contain an electrolyte. The electrolyte may be at least partially between the anode (8) and / or ionic current collector (1) and the cathode (2) and / or cathode current collector (5) and / or cathode stack (9). The electrolyte may contain anode material and / or cathode material. The electrolyte may remain substantially inert throughout the entire battery cycle. The electrolyte may contain an organic or inorganic solvent. The electrolyte may contain, for example, an SO2 solvent or an NH3 solvent. According to the present invention, other solvents are possible.

[0036] The polarity of the cell can be reversed such that the cathode (2) becomes the anode current collector (1) and the anode current collector (1) becomes the cathode (2). The cell may be substantially symmetrical or asymmetrical in the discharged state. Reversing the polarity of the cell may be used as a means of regenerating the cell. Regeneration as used herein means returning a degraded cell to a state close to its original assembly and / or performance. The polarity of the cell can be reversed while the cell is in the discharged state.

[0037] The electrochemical cell may further include a housing. The electrochemical cell can be used in a battery pack. The electrochemical cell and / or battery pack can be used in an apparatus.

[0038] The cell can be assembled in a charged, partially charged, or discharged state. Most preferably, the cell is assembled in a discharged state. The anode current collector and cathode of the electrochemical cell may contain the same or different metals or metal alloys. The anode current collector and cathode of the electrochemical cell may have the same or different compositions. The anode current collector and cathode may have the same or different porosity. The anode current collector and cathode of the electrochemical cell may contain copper. The anode and cathode of the electrochemical cell may be substantially pure copper. [Examples]

[0039] In one embodiment, in the discharge state, the metal-metal battery contains substantially pure copper metal in both the anode and cathode, but according to the present invention, mixtures or combinations of other metals, alloys, and conductive materials (e.g., metals (e.g., transition metals), conductive polymers, and conductive nanomaterials such as carbon nanomaterials (e.g., CNTs, CNBs, graphene)) are possible. In this embodiment, on the anode side, metallic sodium is deposited on the copper surface (i.e., in the pores of the copper foam) during charging, but according to the present invention, other metals (e.g., alkali metals) are possible. In one embodiment, on the cathode side, metallic copper is converted to CuBF4 and / or CuBH4 (depending on the electrolyte salt composition) during charging. In one embodiment, copper is converted to CuI. The reverse process occurs during discharge.

[0040] According to one embodiment of the present invention, an electrochemical cell contains a high concentration of sodium salt in an ammonia solvent. Three electrolyte variations have been tested: NaBH4×1.5NH3, NaBF4×2.5NH3, and NaI×3.3NH3. Other electrolytes are possible according to the present invention.

[0041] According to the present invention, other molar ratios between salt and solvent are possible. The following are properties specific to the NaBH4×1.5NH3 and NaBF4×2.5NH3 electrolytes.

[0042] • Its ionic conductivity is an order of magnitude greater than that of the electrolytes in the best organic lithium-ion batteries. • Under a given anode overpotential, the deposition / exfoliation rate of metallic sodium is an order of magnitude greater than that of known organic solvents. • Enables the deposition of non-dendritic sodium on a copper substrate. • Since the electrolyte is inert to electrodeposited sodium, there is no anode SEI. • The electrolyte potential window is approximately 3V relative to sodium, so if a charge limit of 2.5-3V is used, the cathode side will remain completely inert. Ammonia is at least an order of magnitude cheaper than the organic solvents used in lithium-ion batteries, and NaBH4 / NaBF4 salt is significantly cheaper than LiPF6 salt used in lithium-ion batteries. The NaBF4×2.5NH3 composition remains liquid down to -40°C.

[0043] While the variant of NaBH4×2.5NH3 electrolyte is more cost-effective, the variant of NaBH4×1.5NH3 electrolyte allows for the attainment of higher energy densities. Furthermore, the properties of these electrolytes form a unique basis for their use in metal-metal batteries, and the present invention is not limited to these tested electrolytes.

[0044] A 2V rechargeable battery was demonstrated using the described porous copper anode current collector, cathode, and electrolyte materials. Its theoretical energy density was found to be similar to that of current lithium-ion batteries. Figure 4 schematically illustrates the battery's operation. The battery is assembled in a discharged state with porous copper electrodes on both sides. In the case of the NaBH4 / NaBF4 salt, in the charged state, the anode pores are filled with electrolytic sodium, while in the cathode pores, copper is converted to CuBF4 and / or CuBH4. In the case of the sodium iodide salt, in the charged state, the anode pores are filled with electrodeposited sodium, while in the cathode pores, copper is converted to CuI.

[0045] Figure 5 shows the voltage change of these two electrodes in one of the ammonia-based electrolytes described, compared to a sodium baseline. This data indicates that in our electrolyte, the electrolytic copper remains in a +1 valence state during charging, and the cell obtains a flat discharge plateau at approximately 2V.

[0046] The CuBF4 or CuBH4 salts produced at the cathode during charging have some solubility in the electrolyte, so crossover must be prevented for optimal operation. Therefore, an anion exchange membrane can be used between the two electrodes. In the disclosed example, this membrane allows the passage of only BF4- or BH4- anions while blocking the passage of certain other components of the electrolyte that would counteract electrons transferred via the external circuit. In other embodiments of the invention, the anion exchange membrane needs to allow the passage of different ions while blocking the passage of other components of the electrolyte. Such modifications are within the scope of the fully disclosed invention.

[0047] In one embodiment of the present invention, a Fumatech membrane saturated with BF4- or BH4- through an anion exchange process is used. According to the present invention, it is possible to use both a membrane for filtering BF4- or BH4-, or a membrane for ions suitable for other embodiments of the present invention.

[0048] In one embodiment of the present invention, a copper foam exceeding the mass surface area size threshold required for efficient electrodeposition and oxidation on both the anode and cathode sides was produced by vacuum heat treatment of brass foil. The foam was produced by placing brass foil (63w% Cu and 37w% Zn) in a vacuum (10 Pa) oven and heating it at 500°C for 6 hours.

[0049] In one embodiment of the present invention, a separator is used between the electrodes. In another embodiment of the present invention, the separator is used between the anode current collector and the anion exchange membrane. In another embodiment of the present invention, a glass fiber separator is used. According to the present invention, other separators are possible, including, but not limited to, polymer and / or cellulose separators. In this method, the anion exchange membrane is in contact with the cathode but not with the metal anode deposit (sodium deposit in this example).

[0050] According to exemplary embodiments, the exemplary cell can withstand some degree of crossover of CuBF4 salt or CuBH4 salt. In the disclosed embodiments, the salt crossover results in a copper deposition on the anode. In other words, the anode copper electrode slowly increases in mass and the cathode copper electrode slowly decreases in mass, but the overall battery operation is not substantially hindered. In the disclosed embodiments, since the electrode composition is symmetrical in the discharge state, this mass transfer of electrodes can even be reversed by switching the polarity of the battery.

[0051] In the validation experiment, both electrodes were made from pure copper wire, and crossover of the dissolved copper salt was prevented by the difference in gravity assistance. As shown in Figure 6, the cell exhibited stable performance over 1000 cycles, and the capacity gradually increased. This increase in capacity is attributed to the gradual roughening of the copper wire surface.

Claims

1. A rechargeable electrochemical cell assembled in a discharged state, a. A conductive anode current collector that is the sole anode when in a discharge state, b. Cathode containing only metallic materials as active material, c. An anion exchange structure located between the anode current collector and the cathode, which prevents the movement of cations contained in the metal salt formed at the cathode and / or enables the selective transport of alkali metal cations or anions, and d. An electrolyte that is a separate component from the anion exchange structure and is at least partially located between the cathode and the anode current collector. Equipped with, An electrochemical cell in which solid metal deposits are formed on the surface and / or inside the anode current collector during charging.

2. A rechargeable electrochemical cell assembled in a discharged state, a. A conductive anode current collector that is the sole anode when in a discharge state, b. Cathode containing only metallic materials as active material, c. An ion exchange structure located between the anode current collector and the cathode, which prevents the movement of cations contained in the metal salt formed at the cathode and / or enables the selective transport of alkali metal cations or anions, and d. An electrolyte that is a separate component from the ion exchange structure and is at least partially located between the cathode and the anode current collector, Equipped with, An electrochemical cell in which solid metal deposits are formed on the surface and / or inside the anode current collector during charging.

3. The electrochemical cell according to claim 1 or 2, wherein the cathode is substantially a pure metal cathode and / or a cathode containing a pure metal active material in a dispersion.

4. The electrochemical cell according to claim 3, wherein the cathode is in contact with a conductive cathode current collector, or all or part of the cathode also functions as a conductive cathode current collector.

5. An electrochemical cell according to any one of claims 1 to 4, wherein a salt is formed at least partially from the cathode during charging.

6. The electrochemical cell according to any one of claims 1 to 5, wherein the anode current collector and the cathode are made of substantially the same material.

7. The electrochemical cell according to any one of claims 1 to 6, wherein the anode current collector and / or the cathode are doped with a dopant.

8. The electrochemical cell according to any one of claims 1 to 6, wherein the anode current collector and / or the cathode contains copper.

9. The electrochemical cell according to claim 8, wherein the cathode and / or anode current collector comprises substantially pure metallic copper.

10. The electrochemical cell according to claim 8, wherein the cathode and / or anode current collector comprises doped copper.

11. The electrochemical cell according to claim 7 or 10, wherein the dopant is zinc.

12. The electrochemical cell according to any one of claims 1 to 11, wherein the ion exchange structure prevents the movement of cations contained in the metal salt formed in the cathode and / or enables the selective transport of alkali metal anions.

13. The electrochemical cell according to any one of claims 1 to 12, wherein the cathode and / or the anode current collector is porous.

14. The electrochemical cell according to any one of claims 1 to 13, wherein the polarity of the cell is reversible such that the cathode becomes the anode current collector and the anode current collector becomes the cathode in order to regenerate the cell.

15. A battery pack comprising an electrochemical cell as described in any one of claims 1 to 14.

16. An apparatus comprising an electrochemical cell according to any one of claims 1 to 14 or a battery pack according to claim 15.

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