Patent classifications
C22B15/0006
Method and Facility for Preparing and Evaluating Batteries
The invention relates to a method for preparing and evaluating lithium-ion batteries, having at least one step in which the batteries (2, 10) or comminuted in the presence of an aqueous medium (12), wherein the batteries (2, 10) are comminuted with a remaining charge of maximally 30% in a comminuting device (73) while adding water (12), and the water (12) is supplied in such a quantity and at such a temperature that the mixture is not heated above a temperature of more than 40 C., preferably above 30 C., during the comminuting process. The invention also relates to a corresponding facility (71).
SEPARATING BLACK MASS FROM BROKEN BATTERIES
Disclosed are approaches for recycling LIBs where lithium is recovered before the other node metals in order to increase the amount of lithium recovered. For such approaches, the other node metals need not be further refined or recovered and, despite the small loss of these other node metals as impurities in the first-recovered lithium, the available alternative dispositions for these other node metalssuch as in the form of multi-metal-oxides (MMO)can render the recovery of lithium before the other node metals to be advantageous. Several such approaches may feature nitration, roasting, lithium trapping, and/or other innovative features to facilitate greater and purer recoveries of the target LIB components.
METHOD FOR RECOVERING VALUABLE MATERIALS FROM LITHIUM ION SECONDARY BATTERIES
There is provided a method for recovering valuable materials from lithium ion secondary batteries, which includes: a heat-treatment step of performing a heat treatment on a lithium ion secondary battery to obtain a heat-treated product; a first classification step of classifying a crushed product, which is obtained by crushing the heat-treated product, at a classification point of 600 m or greater and 2,400 m or less to obtain a coarse-particle product 1 and a small-particle product; a grinding step of grinding the small-particle product to obtain a ground product; a second classification step of classifying the ground product at one or more classification points that are smaller than the classification point of the first classification step and are 75 m or greater and 1, 200 m or less to obtain a coarse-particle product 2 and a fine-particle product 1; and a magnetic separation step of sorting the fine-particle product 1 obtained in the second classification step using magnetic force.
IMPURITY MANAGEMENT PROCESS FOR LITHIUM-ION BATTERY RECYCLING
Methods are provided for removing impurities from recycled battery black mass. The method includes mixing a delithiated black mass with a first solution to form a pre-leached delithiated black mass and a pre-leach solution, separating the pre-leached delithiated black mass from the pre-leach solution, mixing the separated pre-leached delithiated black mass and a second aqueous solution to form a mixture comprising graphite and a leachate solution, and separating the graphite and the leachate solution. The pre-leach solution is comprised of a first group of impurity ions while the leachate solution is comprised of a second group of impurity ions and cathode metal ions.
System for preparing new energy Ni—Co—Mn raw material from laterite nickel ore
The present disclosure discloses a system for preparing new energy NiCoMn raw material from laterite nickel Ore. The system includes a raw auxiliary material supply module, a leaching reaction module, a neutralization and purification module, a neutralization and purification module, a NiCoMn mixed hydroxide synthesis module, a valuable metal recovery module, a crystal manufacturing module, a ternary precursor manufacturing module, and a ternary positive material manufacturing module. The present disclosure overcomes the defects of prior art and process, and is a green technology and process for simultaneous extraction of nickel, cobalt and manganese from low-grade laterite nickel ore, which not only realizes simultaneous and efficient extraction of nickel, cobalt and manganese, but also adopts energy-saving and emission reduction green technology and clean production technology to effectively recycle and safely dispose of waste water, waste residue and waste gas.
EXTRACTION AND RECOVERY OF METALS UNDER AMBIENT CONDITIONS
Methods for extracting a target metal from a mixed metal input are described. The method includes milling the mixed metal input with ammonium bicarbonate to form a milled solid product, aging the milled solid product, and leaching the target metal from the aged solid product.
MICROBIAL-ASSISTED HEAP LEACHING
Microbial-assisted heap leaching of fragments or agglomerates of fragments of copper-containing sulfidic ores, such as chalcopyrite ores, and copper-containing sulfidic waste materials is disclosed. A heap leaching method includes controlling the sulfate concentration in a leach liquor. When heap leaching includes using agglomerates. a method of forming agglomerates includes adding the feed materials at, or close to, the inlet end, typically no more than 40%, typically no more than 30%, more typically no more than 20%, of the length from the inlet end of the agglomeration unit.
PROCESS AND SYSTEM FOR RECOVERING COPPER AND COBALT FROM SULFIDIC MATERIALS
The present disclosure is directed to a process for recovering copper and cobalt from a copper and cobalt-containing sulfide ores and concentrates, particularly relatively low grade cobalt bearing sulfide ores and concentrates.
Microbial-assisted heap leaching
Microbial-assisted heap leaching of fragments or agglomerates of fragments of copper-containing sulfidic ores, such as chalcopyrite ores, and copper-containing sulfidic waste materials is disclosed. A heap leaching method includes controlling the sulfate concentration in a leach liquor. When heap leaching includes using agglomerates, a method of forming agglomerates includes adding the feed materials at, or close to, the inlet end, typically no more than 40%, typically no more than 30%, more typically no more than 20%, of the length from the inlet end of the agglomeration unit.