# US 12,119,463 B2 · Recycling method for treating used batteries, in particular rechargeable batteries, and battery processing installation > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 12,119,463 B2 - Document ID: US12119463B2 - Status: Granted - Kind: B2 - Application number: 16/343,224 - Filed: 2017-10-12 - Published: 2019-08-22 - Granted: 2024-10-15 - Earliest claimed: 2016-10-20 - Assignees: Duesenfeld GmbH - Applicants: Duesenfeld GmbH - Inventors: Christian Hanisch - Web page: https://patentgrep.com/patent/US12119463B2 ## CPC - H01M 10/54: Reclaiming serviceable parts of waste accumulators - C22B 1/005: {Preliminary treatment of scrap (C22B1/02 - C22B1/26 take precedence)} - C22B 7/00: Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; {Methods of a general interest or applied to the winning of more than two metals (briquetting of scrap C22B1/248; preliminary treatment of scrap C22B1/005)} - C22B 7/001: {Dry processes} - H01M 6/52: Reclaiming serviceable parts of waste cells or batteries {, e.g. recycling} - Y02P 10/20: Recycling - Y02W 30/84: Recycling of batteries or fuel cells - H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY - C22B: PRODUCTION AND REFINING OF METALS (electrolytic C25); PRETREATMENT OF RAW MATERIALS - Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS - Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT ## Abstract The invention relates to a method for treating used lithium batteries (10) containing the steps: comminuting the batteries (10) such that comminuted material (24) is obtained, and (b) inactivating of the comminuted material (24) such that an inactive comminuted material (42) is obtained. According to the invention, the drying is conducted at a maximum pressure of 300 hPa and a maximum temperature of 80° C. and the deactivated comminuted material (42) is not filled into a transport container and/or said deactivated comminuted material is immediately further processed after the drying process. ## Claims ### Claim 1 A method for treating used lithium batteries , comprising: receiving, into a comminuting device, used lithium batteries that include a cathode, anode, separator, and electrolyte comprising a fluorine salt and a solvent, the solvent including an organic carbonate; comminuting the used lithium batteries, by the comminuting device, and obtaining comminuted material as a result; and inactivating the comminuted material and obtaining inactivated comminuted material as a result, wherein the inactivating includes a drying process, comprising drying the comminuted material by removal of organic carbonate from the electrolyte by vaporizing the organic carbonate at a pressure-temperature above a boiling point of the organic carbonate, the pressure being not more than 300 hPa, and the temperature being not more than 80° C. and lower than a decomposition temperature of the fluorine salt. ### Claim 2 (depends on 1) The method according to claim 1, wherein: the organic solvent comprises dimethyl carbonate, or ethyl methylcarbonate, or both; and the drying process further continues the drying until the vaporizing removes at least 90 percent by weight of the dimethyl carbonate, or ethyl methylcarbonate, or both, from the electrolyte. ### Claim 3 (depends on 1) The method according to claim 1, further comprising: capturing and condensing gases created from the vaporizing of organic carbonate in the electrolyte during the drying process. ### Claim 4 (depends on 1) The method according to claim 1, further comprising: performing the drying within an interior of a drying device; continuous monitoring, by a controller, of at least one progress parameter that is indicative of a progress of the drying, the at least one progress parameter comprising a pressure in the interior of the drying device or a pressure of a gas flow out of the interior of the drying device drying process, and not terminating the drying process until the progress parameter reaches a pre-determined progress parameter threshold value. ### Claim 5 (depends on 1) The method according to claim 1, wherein the the pressure is not more than 30 hPa for at least 50% of a duration of the drying, or the pressure does not exceed 50 hPa during the drying, or both. ### Claim 6 (depends on 1) The method according to claim 1, further comprising: feeding the comminuted material, through an airlock, into an interior of a drying device; and performing the drying within the interior of the drying device. ### Claim 7 (depends on 6) The method according to claim 6, further comprising: vacuum sucking away of gases created from vaporized organic carbonate during the drying process and/or wherein the batteries comprise current collector foils having a coating material and movement using the agitator is conducted such that at least 50% by weight of the coating material of comminuted material is sucked away. ### Claim 8 (depends on 1) The method according to claim 1 wherein: comminuting the used lithium batteries is performed within a container; and the drying is performed within the container. ### Claim 9 (depends on 3) The method according to claim 3 wherein condensing is performed at an ambient pressure, or condensing is performed at a temperature within a temperature range that extends from 0° C. to 50° C., or both. ### Claim 10 (depends on 1) The method according to claim 1, wherein comminuting of the used lithium batteries is configured such that the comminuted material includes components of comminuted material, and at least 90% by weight of the components of the comminuted material have a sieve size that is not more than 50 mm. ### Claim 11 (depends on 1) The method according to claim 1, wherein receiving the used lithium-ion batteries further includes receiving used lithium-ion batteries that further comprise carrier foil and binder that binds active material to the carrier foil, and the temperature of the vaporizing pressure-temperature being not more than 80° C., lower than a decomposition temperature of the binder, and lower than the decomposition temperature of the fluorine salt. ### Claim 12 (depends on 11) The method according to claim 11, further comprising a high temperature drying of the inactivated comminuted material, the high temperature drying being configured to decompose binder. ### Claim 13 (depends on 1) The method according to claim 1, further comprising: moving by an agitator, over a duration of the drying, a not yet inactivated comminuted material among the comminuted material, or a mixture of inactivated comminuted material and not yet inactivated comminuted material, or both; and supplying, during the drying, a vaporization heat to the comminuted material, wherein the supplying includes the agitator supplying at least 35% of said vaporization heat. ### Claim 14 (depends on 1) The method according to claim 1, further comprising: performing the drying within an interior of a drying device; and agitating, by an agitator, the inactivated comminuted material when removing the inactivated comminuted material from the drying device.