# US 10,873,070 B2 · Method and apparatus for liquefied gas solvent delivery for electrochemical devices > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,873,070 B2 - Document ID: US10873070B2 - Status: Granted - Kind: B2 - Application number: 16/804,207 - Filed: 2020-02-28 - Published: 2020-06-25 - Granted: 2020-12-22 - Earliest claimed: 2019-10-07 - Assignees: South 8 Technologies, Inc. - Applicants: South 8 Technologies, Inc. - Inventors: James Royer; Cyrus Sam Rustomji; Jungwoo Lee - Web page: https://patentgrep.com/patent/US10873070B2 ## CPC - H01M 6/164: {by the solvent} - H01M 6/24: Cells comprising two different electrolytes - H01M 10/486: {for measuring temperature} - H01M 10/60: Heating or cooling; Temperature control - H01M 10/63: Control systems (charging or discharging in response to temperature H01M10/44 {, H01M10/443}; measurement of temperature H01M10/48 {, H01M10/486}) - H01M 50/609: Arrangements or processes for filling with liquid, e.g. electrolytes - H01M 50/673: Containers for storing liquids; Delivery conduits therefor - H01M 2300/0042: Four or more solvents - H01M 2300/0091: in the form of mixtures - Y02E 60/10: Energy storage using batteries - H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION ## Abstract Disclosed are novel methods and techniques for introducing liquefied gas solvents into electrochemical devices. Unlike conventional electrolytes, the disclosed electrolytes are based on “liquefied gas solvents” mixed with various salts, referred to as “liquefied gas electrolytes.” The disclosed liquefied gas electrolytes can have wide electrochemical potential windows, high conductivity, low temperature capability and/or high-pressure solvent properties. Non-limiting examples of a class of liquefied gases that can be used as solvents for electrolytes include hydrofluorocarbons, and in particular include fluoromethane, difluoromethane, tetrafluoroethane, and pentafluoroethane. ## Claims ### Claim 1 A method of forming a liquefied gas electrolyte in an electrochemical device, the method comprising: providing a fill setup comprising: a liquefied gas solvent source connected to a flow meter, wherein the liquefied gas solvent has a vapor pressure above an atmospheric pressure of 100 kPa at a room temperature of 293.15 K; the flow meter connected to the electrochemical device; and a valve structure constructed to allow the liquefied gas solvent to flow from the liquefied gas solvent source to the electrochemical device; wherein the connection between the flow meter and the electrochemical device comprises: a waste volume; a pressure sensor constructed to detect the pressure of the waste volume; and a temperature sensor constructed to detect the temperature of the waste volume; a. setting a preset amount of the liquefied gas solvent to be delivered to the electrochemical device; b. adding a salt to the electrochemical device; c. actuating the valve structure to allow for the flow of the liquefied gas solvent to the electrochemical device, wherein the liquefied gas solvent mixes with the salt to form a liquefied gas electrolyte; d. determining the amount of the liquefied gas solvent in the waste volume based on the pressure and temperature sensors; e. determining the amount of the liquefied gas solvent supplied based on the flow meter; f. actuating the valve structure to stop the flow of the liquefied gas solvent to the electrochemical device based on the preset amount in step (a), the amount in step (d) and the amount in step (e). ### Claim 2 (depends on 1) The method of claim 1, wherein the flow meter is a mass flow meter and step (e) further comprises reading from the mass flow meter. ### Claim 3 (depends on 1) The method of claim 1, wherein the flow meter is a mass flow controller and the method further comprises: setting the mass flow controller to a preset flow rate; and step (e) is further based on the amount of time the liquefied gas solvent has flowed through the mass flow controller. ### Claim 4 (depends on 1) The method of claim 1, wherein step (f) is further based on a comparison of the amount in step (e) to the sum of the preset in step (a) and the amount in step (d). ### Claim 5 (depends on 1) The method of claim 1, wherein the fill setup comprises a temperature control element constructed to maintain a variance of temperature within the waste volume to within +/− 2.0 degrees Celsius during step (d). ### Claim 6 (depends on 1) The method of claim 1, wherein the fill setup comprises a temperature control element constructed to maintain the connection between the liquefied gas solvent source and the flow meter to within +/− 2.0 degrees Celsius during steps (c)-(e). ### Claim 7 (depends on 1) The method of claim 1, wherein the fill setup comprises a pressure regulator or pressure controller constructed to maintain the connection between the pressurized source and the flow meter to within +/− 25 kPA variance during steps (c)-(e). ### Claim 8 (depends on 1) The method of claim 1, wherein the fill setup comprises a second liquefied gas solvent source connected to a flow meter and a second valve structure constructed to allow the liquefied gas solvent to flow from the second liquefied gas solvent source to the electrochemical device, the method further comprising: a2. setting a second preset amount of the liquefied gas solvent from the second liquefied gas solvent source to be delivered to the electrochemical device; c2. actuating the second valve structure to allow for the flow of the second liquefied gas solvent to the electrochemical device; d2. determining the amount of the second liquefied gas solvent in the waste volume based on the pressure and temperature sensors; e2. determining the amount of the second liquefied gas solvent supplied based on the flow meter; f2. actuating the second valve structure to stop the flow of the second liquefied gas solvent to the electrochemical device based on the second preset amount in step (a2), the amount in step (d2) and the amount in step (e2). ### Claim 9 (depends on 8) The method of claim 8, wherein steps (c2)-(e2) are performed after step (f). ### Claim 10 (depends on 9) The method of claim 9, wherein the connection between the flow meter and the electrochemical device comprises a third valve structure and a pump between the third valve structure and the flow meter, the method further comprising: prior to performing steps (c2)-(e2), the third valve structure is closed, and the pump is actuated to evacuate the waste volume of the liquefied gas solvent. ### Claim 11 (depends on 1) The method of claim 1, wherein the liquefied gas solvent is selected from the group consisting of: fluoromethane, difluoromethane, trifluoromethane, fluoroethane, tetrafluoroethane, pentafluoroethane, 1,1-difluoroethane, 1,2-difluoroethane, 1,1,1-trifluoroethane, 1,1,2-trifluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, pentafluoroethane, chloromethane, chloroethane, thionyl fluoride, thionyl chloride fluoride, phosphoryl fluoride, phosphoryl chloride fluoride, sulfuryl fluoride, sulfuryl chloride fluoride, 1-fluoropropane, 2-fluoropropane, 1,1-difluoropropane, 1,2-difluoropropane, 2,2-fluoropropane, 1,1,1-trifluoropropane, 1,1,2-trifluoropropane, 1,2,2-trifluoropropane, fluoroethylene, cis-1,2-fluoroethylene, 1,1-fluoroethylene, 1-fluoropropylene, 2-propylene, chlorine, chloromethane, bromine, iodine, ammonia, molecular oxygen, molecular nitrogen, carbon monoxide, carbon dioxide, sulfur dioxide, dimethyl ether, nitrous oxide, nitrogen dioxide, nitrogen oxide, carbon disulfide, hydrogen fluoride, hydrogen chloride, combination thereof, and isomers thereof. ### Claim 12 A fill setup for forming a liquefied gas electrolyte in an electrochemical device, the setup comprising: a salt inside the electrochemical device; a liquefied gas solvent source connected to a flow meter, wherein the liquefied gas solvent has a vapor pressure above an atmospheric pressure of 100 kPa at a room temperature of 293.15 K; the flow meter connected to the electrochemical device; a valve structure constructed to allow the liquefied gas solvent to flow from the liquefied gas solvent source to the electrochemical device; wherein the connection between the flow meter and electrochemical device comprises: a waste volume; a pressure sensor constructed to detect the pressure of the waste volume; and a temperature sensor constructed to detect the temperature of the waste volume; a controller connected to the flowmeter, valve structure, pressure sensor and temperature sensor, the controller adapted to perform the following steps: a. receiving a preset amount of the liquefied gas solvent to be delivered to the electrochemical device; b. actuating the valve structure to allow for the flow of the liquefied gas solvent to the electrochemical device; c. determining the amount of the liquefied gas solvent in the waste volume based on the pressure and temperature sensors; d. determining the amount of the liquefied gas solvent supplied based on the flow meter; e. actuating the valve structure to stop the flow of the liquefied gas solvent to the electrochemical device based on the preset amount in step (a), the amount in step (c) and the amount in step (d); wherein the liquefied gas solvent mixes with the salt inside the electrochemical device to form a liquefied gas electrolyte. ### Claim 13 (depends on 12) The setup of claim 12, wherein the flow meter is a mass flow meter, and step (d) further comprises taking a reading from the mass flow meter. ### Claim 14 (depends on 12) The setup of claim 12, wherein the flow meter is a mass flow controller, and the controller is adapted to perform the steps of: setting the mass flow controller to a preset flow rate; and step (d) is further based on the amount of time the liquefied gas solvent has flowed through the mass flow controller. ### Claim 15 (depends on 12) The setup of claim 12, wherein step (e) is further based on a comparison of the amount in step (d) to the sum of the preset in step (a) and the amount in step (c). ### Claim 16 (depends on 12) The setup of claim 12, further comprising a temperature control element constructed to control the temperature of the waste volume, wherein the temperature control element is connected to the controller, and wherein the controller is adapted to perform the following step: maintain a variance of temperature within the waste volume to within +/− 2.0 degrees Celsius during step (c). ### Claim 17 (depends on 16) The setup of claim 16, wherein the temperature control element comprises a heater. ### Claim 18 (depends on 12) The setup of claim 12, further comprising a temperature control element constructed to control the temperature of the connection between the liquefied gas solvent source and the flow meter, wherein the temperature control element is connected to the controller, and wherein the controller is adapted to perform the following step: maintain the connection between the pressurized source and the flow meter to within +/− 2.0 degrees Celsius during steps (b)-(e). ### Claim 19 (depends on 18) The setup of claim 18, wherein the temperature control element comprises a heater. ### Claim 20 (depends on 12) The setup of claim 12, further comprising a pressure regulator or pressure controller constructed to maintain the connection between the pressurized source and the flow meter to within +/− 25 kPA variance during steps (b)-(e). ### Claim 21 (depends on 12) The setup of claim 12, wherein the flow meter comprises a mass flow meter or a mass flow controller. ### Claim 22 (depends on 12) The setup of claim 12, wherein the connection between the flow meter and the electrochemical device comprises a constricting flow control orifice. ### Claim 23 (depends on 12) The setup of claim 12, wherein the connection between the pressurized source and the flow meter comprises a constricting flow control orifice. ### Claim 24 (depends on 12) The setup of claim 12, further comprising: a second liquefied gas solvent source connected to a flow meter; and a second valve structure constructed to allow the liquefied gas solvent to flow from the second liquefied gas solvent source to the electrochemical device; wherein the controller is connected to the second valve structure and is adapted to perform the following steps: a2. receiving a second preset amount of the liquefied gas solvent from the second liquefied gas solvent source to be delivered to the electrochemical device; b2. actuating the second valve structure to allow for the flow of the second liquefied gas solvent to the electrochemical device; c2. determining the amount of the second liquefied gas solvent in the waste volume based on the pressure and temperature sensors; d2. determining the amount of the second liquefied gas solvent supplied based on the flow meter; e2. actuating the second valve structure to stop the flow of the second liquefied gas solvent to the electrochemical device based on the second preset amount in step (a2), the amount in step (c2) and the amount in step (d2). ### Claim 25 (depends on 24) The setup of claim 24, wherein the controller performs steps (b2)-(e2) after performing step (e). ### Claim 26 (depends on 24) The setup of claim 24, wherein the connection between the flow meter and electrochemical further comprises: a third valve structure; and a pump between the third valve structure and the flow meter; wherein the pump and the third valve structure are connected to the controller; and wherein the controller is adapted to perform the following steps: prior to performing steps (b2)-(e2), actuating the third valve structure to prevent the flow of gas therethrough; actuating the pump to evacuate the waste volume of the liquefied gas solvent; and actuating the third valve structure to allow for the flow of gas therethrough. ### Claim 27 (depends on 12) The setup of claim 12, wherein the liquefied gas solvent is selected from the group consisting of : fluoromethane, difluoromethane, trifluoromethane, fluoroethane, tetrafluoroethane, pentafluoroethane, 1,1-difluoroethane, 1,2-difluoroethane, 1,1,1-trifluoroethane, 1,1,2-trifluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, pentafluoroethane, chloromethane, chloroethane, thionyl fluoride, thionyl chloride fluoride, phosphoryl fluoride, phosphoryl chloride fluoride, sulfuryl fluoride, sulfuryl chloride fluoride, 1-fluoropropane, 2-fluoropropane, 1,1-difluoropropane, 1,2-difluoropropane, 2,2-fluoropropane, 1,1,1-trifluoropropane, 1,1,2-trifluoropropane, 1,2,2-trifluoropropane, fluoroethylene, cis-1,2-fluoroethylene, 1,1-fluoroethylene, 1-fluoropropylene, 2-propylene, chlorine, chloromethane, bromine, iodine, ammonia, molecular oxygen, molecular nitrogen, carbon monoxide, carbon dioxide, sulfur dioxide, dimethyl ether, nitrous oxide, nitrogen dioxide, nitrogen oxide, carbon disulfide, hydrogen fluoride, hydrogen chloride, combination thereof, and isomers thereof. ### Claim 28 A method of forming a liquefied gas electrolyte in an electrochemical device, the method comprising: providing a fill setup comprising: a liquefied gas solvent source connected to a flow meter, wherein the liquefied gas solvent has a vapor pressure above an atmospheric pressure of 100 kPa at a room temperature of 293.15 K; the flow meter connected to the electrochemical device; a valve structure constructed to allow the liquefied gas solvent to flow from the liquefied gas solvent source to the electrochemical device; wherein the connection between the flow meter and electrochemical device comprises: a waste volume; a pressure sensor constructed to detect the pressure of the waste volume; and a temperature control element constructed to maintain the temperature of the waste volume at preset temperature; a. setting a preset amount of the liquefied gas solvent to be delivered to the electrochemical device; b. adding salt to the electrochemical device; c. actuating the valve structure to allow for the flow of the liquefied gas solvent to the electrochemical device, wherein the liquefied gas solvent mixes with the salt to form a liquefied gas electrolyte; d. determining the amount of the liquefied gas solvent in the waste volume based on the pressure sensor and the present temperature; e. determining the amount of the liquefied gas solvent supplied based on the flow meter; f. actuating the valve structure to stop the flow of the liquefied gas solvent to the electrochemical device based on the preset amount in step (a), the amount in step (d) and the amount in step (e).