Patent Application
20250003099
Disclosed herein are processes comprising electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0.5. Also disclosed are processes comprising electrolyzing a first aqueous solution comprising lithium to obtain a second aqueous solution comprising lithium, and an acidic aqueous solution having a pH less than 0.5, adjusting the pH of the second aqueous solution with the acidic aqueous solution to obtain a third aqueous solution comprising lithium having a pH less than 0.5, and electrolyzing the third aqueous solution comprising lithium. Additionally disclosed are processes comprising stripping a liquid medium comprising lithium with an acidic aqueous solution to obtain an aqueous solution comprising lithium, and electrolyzing the aqueous solution comprising lithium. Further disclosed are processes for preparing a liquid medium comprising lithium.
High purity lithium is a valuable resource. Many sources of lithium, such as lithium ion batteries, lithium ion battery waste, lithium containing water, e.g. ground water, and raw lithium containing ores, are complex mixtures of various elements and compounds. It may be desirable to remove various non-lithium impurities to obtain high purity lithium. Electrolysis of an aqueous solution comprising lithium provides an exemplary means for obtaining high purity lithium. In some electrolysis processes, the current density may be limited by the pH of the aqueous solution. In some electrolysis processes, the pH may be adjusted by, e.g., adding a base to the aqueous solution comprising lithium. Adding a base may, however, form an undesirable salt and generate undesirable solid particles. Such particles may be difficult to remove, and may result in a more expensive purification process. Additionally, in some lithium purification processes, a stripping step is used to transfer lithium from a liquid medium to an aqueous solution prior to electrolysis. In some such processes, fresh acid, such as H2SO4, is added as a stripping agent.
Accordingly, there is a need for economic processes with high lithium recovery and high lithium purity. There is a need for improved electrolysis performance. There is also a need for economical generation and use of stripping agents such as H2SO4. In some embodiments, it may be desirable to perform electrolysis at different pH levels. In some embodiments, it may be desirable to avoid adjusting the pH level before performing the electrolysis. In some embodiments, it may be desirable to generate lithium from solutions that already have a low pH level.
Disclosed herein are processes comprising electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0.5. In some embodiments, the aqueous solution comprises sulfate. In some embodiments, the pH of the aqueous solution is adjusted along a gradient ranging from −1 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted up along a gradient ranging from −1 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted down along a gradient ranging from −1 to 0.5. In some embodiments, a process comprises electrolyzing a first aqueous solution comprising lithium to obtain a second aqueous solution comprising lithium, and an acidic aqueous solution having a pH less than 0.5, adjusting the pH of the second aqueous solution with the acidic aqueous solution to obtain a third aqueous solution comprising lithium having a pH less than 0.5, and electrolyzing the third aqueous solution. In some embodiments, the first aqueous solution has a pH greater than 0.5. In some embodiments, electrolyzing the first aqueous solution is performed in a different electrolysis cell than electrolyzing the third aqueous solution. In some embodiments, a process comprises stripping a liquid medium comprising lithium with an acidic aqueous solution to obtain an aqueous solution comprising lithium, and electrolyzing the aqueous solution comprising lithium to obtain a lithium-depleted aqueous solution; wherein the lithium-depleted aqueous solution is provided upstream in the process as the acidic aqueous solution, wherein the liquid medium comprises less than 50 weight % water by total weight of the liquid medium, and wherein the lithium-depleted aqueous solution has a lower concentration of lithium than the aqueous solution comprising lithium. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium greater than zero. In some embodiments, the liquid medium comprises less than 5 weight % of water by total weight of the liquid medium. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 100 g/L.] In some embodiments, a process for preparing a liquid medium comprising lithium comprises electrolyzing an aqueous solution comprising lithium at a pH less than 0.5 to obtain a lithium-depleted aqueous solution, and extracting the lithium-depleted aqueous solution with a liquid medium; wherein the liquid medium comprises less than 50 weight % of water by total weight of the liquid medium, and wherein the lithium-depleted aqueous solution has a lower concentration of lithium than the aqueous solution comprising lithium.
As used herein, “a” or “an” entity refers to one or more of that entity, e.g., “a compound” refers to one or more compounds or at least one compound unless stated otherwise. As such, the terms “a” (or “an”), “one or more”, and “at least one” are used interchangeably herein.
As used herein, the term “material” refers to the elements, constituents, and/or substances of which something is composed or can be made.
As used herein, the term “about” refers to a ±5% of the stated number. Unless otherwise stated, all numbers are assumed to be modified by “about”.
As used herein, the term “electrolysis” refers to the chemical decomposition produced by passing an electric current through a liquid or solution comprising ions.
For example, disclosed herein are processes comprising electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0.5. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0.4. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0.3. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0.2. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0.1. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH less than 0. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH ranging from −1 to 0.5. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH ranging from 0 to 0.5. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH ranging from 0 to 0.4. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH ranging from 0 to 0.3. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH ranging from 0 to 0.2. In some embodiments, the processes comprise electrolyzing an aqueous solution comprising lithium, wherein the aqueous solution has a pH ranging from 0 to 0.1.
In some embodiments, the aqueous solution comprises sulfate.
In some embodiments, the pH of the aqueous solution is adjusted along a gradient ranging from −1 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted up and/or down along a gradient ranging from −1 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted along a gradient ranging from 0 to 0.5.
In some embodiments, the pH of the aqueous solution is adjusted up along a gradient ranging from −1 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted up along a gradient ranging from 0 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted up along a gradient ranging from 0 to 0.5 by adding a base.
In some embodiments, the pH of the aqueous solution is adjusted down along a gradient ranging from −1 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted down along a gradient ranging from 0 to 0.5. In some embodiments, the pH of the aqueous solution is adjusted down along a gradient ranging from 0 to 0.5 by adding an acid.
In some embodiments, a process comprises electrolyzing a first aqueous solution comprising lithium to obtain a second aqueous solution comprising lithium, and an acidic aqueous solution having a pH less than 0.5, adjusting the pH of the second aqueous solution with the acidic aqueous solution to obtain a third aqueous solution comprising lithium having a pH less than 0.5, and electrolyzing the third aqueous solution.
In some embodiments, the first aqueous solution has a pH greater than 0.5.
In some embodiments, electrolyzing the first aqueous solution is performed in a different electrolysis cell than electrolyzing the third aqueous solution.
In some embodiments, a process comprises stripping a liquid medium comprising lithium with an acidic aqueous solution to obtain an aqueous solution comprising lithium, and electrolyzing the aqueous solution comprising lithium to obtain a lithium-depleted aqueous solution; wherein the lithium-depleted aqueous solution is provided upstream in the process as the acidic aqueous solution, wherein the liquid medium comprises less than 50 weight % water by total weight of the liquid medium, and wherein the lithium-depleted aqueous solution has a lower concentration of lithium than the aqueous solution comprising lithium.
In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium greater than zero.
In some embodiments, the liquid medium comprises less than 5 weight % of water by total weight of the liquid medium. In some embodiments, the liquid medium comprises less than 10 weight % of water by total weight of the liquid medium. In some embodiments, the liquid medium comprises less than 20 weight % of water by total weight of the liquid medium. In some embodiments, the liquid medium comprises less than 1 weight % of water by total weight of the liquid medium. In some embodiments, the liquid medium comprises less than 0.1 weight % of water by total weight of the liquid medium. In some embodiments, the liquid medium is immiscible with water. In some embodiments, the liquid medium is an organic solvent. In some embodiments, the liquid medium comprises at least one chelating agent for lithium.
In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 30 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 40 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 50 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 60 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 70 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 80 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 90 g/L to about 100 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 90 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 80 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 70 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 60 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 50 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 40 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 20 g/L to about 30 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 30 g/L to about 90 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 40 g/L to about 80 g/L. In some embodiments, the lithium-depleted aqueous solution has a concentration of lithium ranging from about 50 g/L to about 70 g/L.
In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 30 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 40 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 50 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 60 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 70 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 80 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 90 g/L to about 100 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 90 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 80 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 70 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 60 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 50 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 40 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 20 g/L to about 30 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 30 g/L to about 90 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 40 g/L to about 80 g/L. In some embodiments, the aqueous solution comprising lithium has a concentration of lithium ranging from about 50 g/L to about 70 g/L.
In some embodiments, a process for preparing a liquid medium comprising lithium comprises electrolyzing an aqueous solution comprising lithium at a pH less than 0.5 to obtain a lithium-depleted aqueous solution, and extracting the lithium-depleted aqueous solution with a liquid medium; wherein the liquid medium comprises less than 50 weight % of water by total weight of the liquid medium, and wherein the lithium-depleted aqueous solution has a lower concentration of lithium than the aqueous solution comprising lithium.
In some embodiments, an electrolysis cell comprises at least one membrane. In some embodiments, an electrolysis cell comprises at least two membranes. In some embodiments, an electrolysis cell comprises two membranes. The membranes may be any known lithium ion conducting membrane for use in electrolysis of an aqueous solution comprising lithium. In some embodiments, the at least one membrane is chosen from a ceramic membrane, a polymer membrane, and combinations thereof. In some embodiments, a polymer membrane is a sulfonated membrane. In some embodiments, a sulfonated membrane has a hydrocarbon backbone or a PTFE backbone. In some embodiments, a sulfonated membrane is a sulfonated polyaryleneether or a polyphenylsulfon e.g. a polyaryleneether Ultrason® or polyphenylsulfon Ultrason®. In some embodiments, a polymer membrane is at least one chosen from a perfluorinated membrane, a cation exchange membrane, a PEEK-reinformed membrane, a styrene/divinylbenzene membrane, and combinations thereof. In some embodiments, a membrane is a fluorinated copolymer with sulfonic acid groups. In some embodiments, a membrane is a perfluorosulfonate polymer membrane. In some embodiments, the perfluorosulfonate polymer membrane is NAFION by E.I. du Pont de Nemours.
An electro chemical cell comprises a cathode and an anode. An exemplary electro chemical cell is ICI FM01. In some embodiments, a cell may be configured in a monopolar or bipolar configuration. The cathode may be any cathode known for electrolysis of an aqueous solution comprising lithium. The anode may be any anode known for electrolysis of an aqueous solution comprising lithium. In some embodiments, an anode is at least one chosen from a metal electrode, a metal oxide electrode, an electrode coated with a platinum group metal, and an electrode coated a platinum group metal oxide. In some embodiments, the thickness of the coating on the anode ranges from 1 micron to 100 microns. In some embodiments, the anode is titanium. In some embodiments, an anode has a geometry chosen from a mesh, a plate, a wire, a foam, and a felt. In some embodiments, an anode is a sheet, a rod, flat, corrugated, rectangular, unsymmetrical, or combinations thereof. In some embodiments, an anode has iridium oxide coated on a titanium substrate. In some embodiments, an anode comprises an electrically conductive substrate with a surface coating of metal oxide doped with at least one precious metal. In some embodiments, the metal oxide is chosen from titanium, tantalum, niobium, zirconium, and combinations thereof. In some embodiments, the precious metal is chosen from platinum, ruthenium, palladium, iridium, rhodium, osmium, and combinations thereof. In some embodiments, a cathode is at least one chosen from a metal electrode, a metal oxide electrode, an electrode with a platinum group metal, and an electrode coated a platinum group metal oxide. In some embodiments, the thickness of the coating on the cathode ranges from 1 micron to 100 microns. In some embodiments, a cathode is at least one chosen from a nickel electrode and a stainless steel electrode. In some embodiments, a cathode has a geometry chosen from a mesh, a plate, a wire, a foam, and a felt.
In some embodiments, a cathode is a sheet, a rod, flat, corrugated, rectangular, unsymmetrical, or combinations thereof. In some embodiments, a cathode is a stainless steel electrode. In some embodiments, a cathode is chosen from a porous metal. In some embodiments, a cathode comprises stainless steel, nickel, cobalt, titanium, steel, lead, platinum, and combinations thereof.
In some embodiments, at least one, at least two, at least 10, at least 100, at least 500 electrolysis cells are stacked one after another in fluid communication. A stack of electrolysis cells has an inlet and an outlet. In some embodiments, a process comprises electrolyzing an aqueous solution comprising lithium in a stack of electrolysis cells having a pH gradient from inlet to outlet. In some embodiments, a process comprises electrolyzing an aqueous solution comprising lithium in a stack of electrolysis cells having a decreasing pH gradient from inlet to outlet. In some embodiments, a process comprises electrolyzing an aqueous solution comprising lithium in a stack of electrolysis cells having a decreasing pH gradient from inlet to outlet, wherein the inlet has a pH greater than 0.5 and the outlet has a pH less than 0.5. In some embodiments, a process comprises electrolyzing an aqueous solution comprising lithium in a stack of electrolysis cells having a decreasing pH gradient from inlet to outlet, wherein the inlet has a pH greater than 0.5 and the outlet has a pH less than 0.5 and wherein the stack comprises at least 100electrolysis cells serially connected in fluid communication.
“Black mass” refers to materials comprising lithium derived from, for example, a lithium ion battery, lithium ion battery waste, lithium ion battery production scrap, lithium ion cell production scrap, lithium ion cathode active material, and/or combinations thereof by mechanical processes such as mechanical comminution. For example, black mass may be derived from battery scrap by mechanically treating the battery scrap to obtain the active components of the electrodes such as graphite and cathode active material and may include impurities from the casing, electrode foils, cables, separator, and electrolyte. In some examples, the battery scrap may be subjected to a heat treatment to pyrolyze organic (e.g., electrolyte) and polymeric (e.g., separator and binder) materials. Such a heat treatment may be performed before or after mechanical comminution of the battery material.
Lithium ion batteries may be disassembled, punched, milled, for example in a hammer mill, and/or shredded, for example in an industrial shredder. From this kind of mechanical processing the active material of the battery electrodes may be obtained. A light fraction such as housing parts made from organic plastics and aluminum foil or copper foil may be removed, for example, in a forced stream of gas, air separation or classification.
Battery scraps may stem from, e.g., used batteries or from production waste such as off-spec material. In some embodiments a battery material is obtained from mechanically treated battery scraps, for example from battery scraps treated in a hammer mill or in an industrial shredder. Such material may have an average particle diameter (D50) ranging from 1 μm to 1 cm, such as from 1 to 500 μm, and further for example, from 3 to 250 μm.
Larger parts of the battery scrap like the housings, the wiring and the electrode carrier films may be separated mechanically such that the corresponding materials may be excluded from the battery material that is employed in the process.
Mechanically treated battery scrap may be subjected to a solvent treatment in order to dissolve and separate polymeric binders used to bind the transition metal oxides to current collector films, or, e.g., to bind graphite to current collector films. Suitable solvents are N-methylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, N-ethylpyrrolidone, and dimethylsulfoxide, in pure form, as mixtures of at least two of the foregoing, or as a mixture with 1% to 99% by weight of water.
Mechanically treated battery scrap may be subjected to a heat treatment in a wide range of temperatures under different atmospheres. The temperature range is usually in the range of 100° C. to 900° C. Lower temperatures below 300° C. may serve to evaporate residual solvents from the battery electrolyte, at higher temperatures the binder polymers may decompose while at temperatures above 400° C. the composition of the inorganic materials may change as some transition metal oxides may become reduced either by the carbon contained in the scarp material or by introducing reductive gases. In some embodiments, a reduction of lithium metal oxides may be avoided by keeping the temperature below 400° C. and/or by removing carbonaceous materials before the heat treatment.
In some embodiments, the battery material comprises at least one chosen from lithiated nickel cobalt manganese oxide, lithiated nickel cobalt aluminum oxide, lithium metal phosphate, lithium ion battery scrap, black mass derived from a lithium ion battery, and combinations there.
In some embodiments, the battery material comprises lithium metal phosphate of formula LixMPO4, wherein x is an integer greater than or equal to one, and M is chosen from metals, transition metals, rare earth metals, and combinations thereof.
In some embodiments, the battery material comprises lithiated nickel cobalt manganese oxide of formula Li1+x(NiaCObMncM1d)1−xO2, wherein M1 is chosen from Mg, Ca, Ba, Al, Ti, Zr, Zn, Mo, V and Fe, zero ≤x≤0.2, 0.1≤a≤0.95, zero ≤b≤0.9 (such as 0.05<b≤0.5), zero ≤c≤0.6, zero ≤d≤0.1, and a+b +c+d=1. Exemplary lithiated nickel cobalt manganese oxides include Li(1+x)[Ni0.33Co0.33Mn0.33](1−x)O2, Li(1+x)[Ni0.5Co0.2Mn0.3](1−x)O2, Li(1+x)[Ni0.6Co0.2Mn0.2](1−x)O2, Li(1+x)[Ni0.7Co0.2Mn0.3](1−x)O2, Li(1+x)[Ni0.8Co0.1Mn0.1](1−x)O2 each with x as defined above, and Li[Ni0.85Co0.13Al0.02]O2.
In some embodiments, the battery material comprises lithiated nickel-cobalt aluminum oxides of formula Li[NihCoiAlj]O2+r, wherein h ranges from 0.8 to 0.90,i ranges from 0.1 to 0.3, j ranges from 0.01 to 0.10, and r ranges from zero to 0.4
In some embodiments, the battery material comprises nickel, cobalt, manganese, copper, aluminum, iron, phosphorus, or combinations thereof.
In some embodiments, the battery material has a weight ratio ranging from 0.01to 100 of lithium to a total weight of nickel, cobalt, manganese, copper, aluminum, iron, and phosphorus. In some embodiments, wherein the battery material has a weight ratio ranging from 0.01 to 10 of lithium to a total weight of nickel, cobalt, manganese, copper, aluminum, iron, and phosphorus. In some embodiments, wherein the battery material has a weight ratio ranging from 0.01to 5 of lithium to a total weight of nickel, cobalt, manganese, copper, aluminum, iron, and phosphorus. In some embodiments, wherein the battery material has a weight ratio ranging from 0.01 to 2 of lithium to a total weight of nickel, cobalt, manganese, copper, aluminum, iron, and phosphorus. In some embodiments, wherein the battery material has a weight ratio ranging from 0.01 to 1 of lithium to a total weight of nickel, cobalt, manganese, copper, aluminum, iron, and phosphorus.
In some embodiments, the battery material comprises LixMO2 wherein x is an integer greater than or equal to one, and M is chosen from metals, transition metals, rare earth metals, and combinations thereof.
In some embodiments, a process for recycling lithium ion battery materials comprises mechanically comminuting at least one chosen from a lithium ion battery, lithium ion battery waste, lithium ion battery production scrap, lithium ion cell production scrap, lithium ion cathode active material, and combinations thereof to obtain a black mass.
Without limitation, some embodiments of the disclosure include:
Claims or descriptions that include “or” or “and/or” between at least one members of a group are considered satisfied if one, more than one, or all of the group members are present in, employed in, or otherwise relevant to a given product or process unless indicated to the contrary or otherwise evident from the context. The disclosure includes embodiments in which exactly one member of the group is present in, employed in, or otherwise relevant to a given product or process. The disclosure includes embodiments in which more than one, or all the group members are present in, employed in, or otherwise relevant to a given product or process.
Furthermore, the disclosure encompasses all variations, combinations, and permutations in which at least one limitation, element, clause, and descriptive term from at least one of the listed claims is introduced into another claim. For example, any claim that is dependent on another claim can be modified to include at least one limitation found in any other claim that is dependent on the same base claim. Where elements are presented as lists, such as, e.g., in Markush group format, each subgroup of the elements is also disclosed, and any element(s) can be removed from the group. It should be understood that, in general, where the disclosure, or aspects of the disclosure, is/are referred to as comprising particular elements and/or features, embodiments of the disclosure or aspects of the disclosure consist, or consist essentially of, such elements and/or features. For purposes of simplicity, those embodiments have not been specifically set forth in haec verba herein. Where ranges are given, endpoints are included. Furthermore, unless otherwise indicated or otherwise evident from the context and understanding of one of ordinary skill in the art, values that are expressed as ranges can assume any specific value or sub range within the stated ranges in different embodiments of the disclosure, unless the context clearly dictates otherwise.
Those of ordinary skill in the art will recognize or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the disclosure described herein. Such equivalents are intended to be encompassed by the following claims.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2022/069014 | 7/7/2022 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 63220259 | Jul 2021 | US |
