Efficient Dry Process for Superior Electrodes

Introduction

This dry process method for producing electrodes offers a game-changing solution for manufacturing high-performance electrodes in electrochemical devices, including batteries, fuel cells, and supercapacitors. The dry process eliminates the need for solvent-based production methods, reducing environmental impact and lowering production costs. For companies in the energy storage and battery manufacturing industries, this technology offers a unique opportunity to improve both sustainability and product performance while positioning themselves at the forefront of next-generation energy solutions.

The Challenge: High Costs and Environmental Impact of Wet Processes

Traditional electrode production processes rely heavily on solvents and wet chemistry, which not only contribute to high manufacturing costs but also raise environmental concerns. These processes require significant energy input for drying and solvent recovery, leading to inefficiencies in both cost and time. Moreover, the environmental regulations surrounding solvent use are becoming stricter, increasing the pressure on manufacturers to find more sustainable alternatives. Companies in energy storage and battery manufacturing are seeking innovative methods that reduce environmental impact while improving production efficiency and product quality.

Dry Process: A Sustainable, Cost-Effective Alternative

This efficient dry process method for producing electrodes addresses these challenges by eliminating the need for solvents and wet processing. By using a dry technique, the method significantly reduces energy consumption, shortens production times, and lowers overall manufacturing costs. The result is a more sustainable production process that not only aligns with stricter environmental regulations but also improves the performance of the electrodes. The electrodes produced by this method exhibit enhanced energy density, longer cycle life, and greater reliability, making them ideal for applications in electric vehicles, renewable energy storage, and portable electronics.

Key Benefits for Energy and Electronics Sectors

For battery manufacturers, this technology offers a way to reduce costs while producing high-quality electrodes that meet the growing demand for efficient, long-lasting batteries. Companies in the electric vehicle (EV) industry will benefit from the enhanced energy storage capacity of these electrodes, enabling longer driving ranges and improved battery performance. Renewable energy companies can integrate these advanced electrodes into energy storage systems, providing more efficient and sustainable solutions for solar and wind power. Electronics manufacturers will also find value in using these electrodes to improve the performance of portable devices, such as smartphones and laptops, with longer battery life and faster charging capabilities.

Invest in Next-Generation Energy Solutions

Licensing this efficient dry process electrode technology positions your organization at the cutting edge of sustainable and high-performance energy storage solutions. By offering a cost-effective and environmentally friendly alternative to traditional electrode production methods, your company can meet the growing demand for clean energy technologies while improving product performance and reliability. This innovative method provides a strategic advantage in the competitive energy storage market, supporting the transition to a more sustainable, energy-efficient future.

A method of making an electrode for an electrochemical cell includes the step of providing an electrode composite comprising from 70 – 98 % active material , from 0 – 10 % conductive material additives , and from 2 – 20 % polymer binder , based on the total weight of the electrode composite . The electrode composite is mixed and then compressed the electrode composite into an electrode composite sheet . The electrode composite sheet is applied to a current collector with pressure to form an electrode , wherein the electrode possesses positive characteristics for adhesion according to ASTM standard test D3359 – 09e2 , entitled Standard Test Methods for Measuring Adhesion by Tape Test , and wherein the electrode composite sheet and the electrode possess positive characteristics for flexibility according to the Mandrel Test . The binder can be a single nonfluoropolymer binder . Dry process electrodes are also disclosed .

We claim : 1 . A method of making an electrode for an electrochemi cal cell , comprising the steps of : providing an electrode composite comprising from 70 – 98 % active material , from 0 – 10 % conductive mate rial additives , and from 2 – 20 % polymer binder , based on the total weight of the electrode composite ; mixing the electrode composite ; compressing the electrode composite into an electrode composite sheet ; applying the electrode composite sheet to a current col lector with pressure to form an electrode , wherein the electrode possesses positive characteristics for adhe sion according to ASTM standard test D3359 – 09e2 , entitled Standard Test Methods for Measuring Adhe sion by Tape Test , and wherein the electrode composite sheet and the electrode possess positive characteristics for flexibility according to the Mandrel Test . 2 . The method of claim 1 , wherein the binder is a single nonfluoropolymer binder . 3 . The method of claim 1 , wherein the active material comprises at least 80 % by weight of the electrode compos ite . 4 . The method of claim 1 , wherein the active material is a positive electrode active material comprising at least one selected from the group consisting of LiCo02 , LiNi1 , 3Cou 3M11 / 302 , LiNio . 8C00 . 15Al2 . 05O2 , Lii + xNi1 / 3C01 / 3M11 / 302 , where 0 < x < 0 . 8 , LiMn204 , LiFePO4 , LizMn204 , LiNi CoA102 , LiNi , Co _ M _ O , where M = Mn , Al , Sn , In , Ga or Ti and 0 . 15 < x < 0 . 5 , 0 . 5 < y < 0 . 8 and ( < z < 0 . 15 , Li [ Li ( 1 – 2v ) / 3Ni „ Mn ( 2 – y ) / 3 ] O2 , Li [ Li ( 1 – x ) / 3 Co , . Mn ( 2 – 2y ) 3 ] 0 , and Li [ Ni , Coi 2yMn , 102 , 0 < y < 0 . 5 , LiNiC002 . MnO2 , lithium rich com pounds Li1 + y ( Ni1 / 3C01 / 3M11 / 3 ) 1 – 102 , where y = x / ( 2 + x ) and X = 0 – 0 . 33 , and xLi MnO3 ( 1 – x ) Li ( NiCoMn ) O2 and Li ( 1 + y ) ( Ni . . . Coo2Mno . 3 ) 1 – 102 , where y = x / ( 2 + x ) and x = 0 – 0 . 33 , and LIMPO4 , where M is at least one selected from the group consisting of V , Cr , Mn , Fe , Co , and Ni . 5 . The method of claim 1 , wherein the active material is an anode active material comprising at least one selected from the group consisting of carbon , hard carbon , soft carbon , synthetic graphite , natural graphite , mesophase car bon microbeads , SnO2 , SnO , TiO2 , Li Tis012 , LiTi204 , SiO , and silicon . 6 . The method of claim 1 , wherein the conductive material additive comprises at least one selected from the group consisting of carbon black , acetylene black , carbon nano tube , carbon nanofiber , carbon fibers , coke , high surface area carbon , graphite , metal particles , and conducting polymer . 7 . The method of claim 1 , wherein the binder material is a soft polymer comprising at least one selected from the group consisting of acrylic – based soft polymers , isobuty lene – based soft polymers , diene – based soft polymers , sili con – containing soft polymers , olefin – based soft polymers , vinyl – based soft polymers , epoxy – based soft polymers , fluo rine – containing soft polymers , natural rubbers , polypeptides , proteins , polyester – based thermoplastic elastomers , vinyl chloride – based thermoplastic elastomers , and polyamide based thermoplastic elastomers . 8 . The method of claim 1 , wherein the binder material is a soft polymer comprising at least one selected from the group consisting of homopolymers or copolymers of acrylic acid or methacrylic acid derivatives , polybutyl acrylate , polybutyl methacrylate , polyhydroxyethyl methacrylate , polyacrylamide , polyacrylonitrile , butyl acrylate – styrene copolymers , butyl acrylate – acrylonitrile copolymers , butyl acrylate – acrylonitrile – glycidyl methacrylate copolymers , polyisobutylene , isobutylene – isoprene rubber , isobutylene styrene copolymers , polybutadiene , polyisoprene , butadi ene – styrene random copolymers , isoprene – styrene random copolymers , acrylonitrile – butadiene copolymers , acryloni trile – butadiene – styrene copolymers , butadiene – styrene block copolymers , styrene – butadiene – styrene – block copoly mers , isoprene – styrene – block copolymers , styrene – isoprene styrene – block copolymers , dimethylpolysiloxane , diphenylpolysiloxane , dihydroxypolysiloxane , liquid poly ethylene , polypropylene , poly – 1 – butene , ethylene – a – olefin copolymers , propylene – a – olefin copolymers , ethylene – pro pylene – diene copolymers ( EPDM ) , ethylene – propylene – sty rene copolymers , polyvinyl alcohol , polyvinyl acetate , poly vinyl stearate , vinyl acetate – styrene copolymers , polyethylene oxide , polypropylene oxide , epichlorohydrin rubbers , vinylidene fluoride – based rubbers , tetrafluoroethyl ene – propylene rubbers , poly ( 2 – methoxyethoxyethoxyethyl ene ) , styrene butadiene rubber ( SBR ) , butadiene – acryloni trile , rubber ( NBR ) , hydrogenated NBR ( HNBR ) , epichlorhydrin rubber ( CHR ) and acrylate rubber ( ACM ) . 9 . The method of claim 1 , wherein the binder material comprises asoft polymer comprising at least one selected from the group consisting of soft polymers having a cross linked structure , and soft polymers having a functional group in the range of about 3 – 12 % by weight of the soft polymer , wherein the functional group is at least one selected from the group consisting of an unsaturated group , a carboxyl group , a hydroxy group , an amino group , and an epoxy group 10 . The method of claim 1 , wherein the mixing step comprises at least one selected from the group consisting of rubber kneading , two roll milling , tumbling mixing , air jet mixing , mixture grinding , high – shear mixing , V – blender mixing , mixing by a screw – driven mass mixer , double – cone mixing , drum mixing , conical mixing , two – dimensional mixing , double Z – arm blending , ball – milling , and fluidized bed blending 11 . The method of claim 1 , wherein the mixing step further comprises the step of providing a solvent and mixing the solvent with the binder at a binder to solvent ratio of from 100 : 1 to 1 : 100 by weight , and adding the active material particles and carbonaceous conductors to binder solution in a ratio of from 10 : 1 to 1 : 5 , by weight . 12 . The method of claim 11 , wherein the solvent com prises at least one selected from the group consisting of a hydrocarbon , ketone , naphtha , acetate , acrylonitrile , toluene , xylene , alcohol , or esters . 13 . The method of claim 1 , wherein said electrode com posite sheet has a thickness of less than 200 microns . 14 . The method of claim 1 , wherein said electrode com posite sheet has a thickness of from 50 – 150 microns . 15 . The method of claim 1 , wherein the electrode com posite sheet comprises less than 50 % solvent , by weight of the electrode composite sheet . 16 . The method of claim 1 , wherein the binder material comprises at least two binder materials . 17 . The method of claim 1 , further comprising the step of forming a binder coating of a Li ion transporting material on the surface of the active materials . 18 . The method of claim 17 , wherein the binder materials comprise at least one selected from the group consisting of homopolymers and copolymers of polyvinylidenefluoride ( PVDF ) , polyolefinic materials with electron withdrawing substituents , and water soluble binders . 19 . The method of claim 17 , wherein the binders comprise at least one selected from the group consisting of copoly mers of vinylidene fluoride and hexafluoropropylene , poly ( methyl methacrylate ) ( PMMA ) , polyacrylic acids , poly acrylronitrile ( PAN ) , polyvinyl chloride ( PVC ) , poly vinylalcohols ( PVA ) , polyvinyl pyrrolidone , polyethylene oxides ( PEO ) , polyethylene glycols , polyacrylamide ( PAAm ) , poly – N – isopropylearylamide , poly – N , N – dimethyl acrylamide , polyethyleneimine , polyoxyethylene , polyvi nylsulfonic acid , polyactic acid ( PLA ) , polyacrylic acid ( PAA ) , polysuccinic acid , poly maleic acid and anhydride , poly furoic ( pyromucic acid ) , poly fumaric acid , poly sorbic acid , poly linoleic acid , poly linolenic acid , poly glutamic acid , poly methacrylic acid , poly licanic acid , poly glycolic acid , polyaspartic acid , poly amic acid , poly formic acid , poly acetic acid , poly propionic acid , poly butyric acid , poly sebacic acid , acrylic acid – type water – soluble polymers , maleicanhydride – type water – soluble polymers , poly ( N – vinyl amides ) , polyacrylamides , N – methylacrylamide , N – ethyl acrylamide , N , N – dimethyl acrylamide , and N , Ndiethylacry lamide , poly ( hydroxy – ethyl methacrylate ) , polyesters , poly ( ethyl oxazolines ) , poly ( oxymethylene ) , poly ( vinyl methyl ether ) , poly ( styrene sulfonic acid ) , poly ( ethylenesulfonic acid ) , poly ( vinyl phosphoric ) acid , poly ( maleic acid ) , starch , cellulose , protein , polysaccharide , dextrans , tannin , lignin , polyethylene – polypropylene copolymer , copolymers of poly ( acrylonitrile – co – acrylamide ) , co – polymer of polystyreneb utadiene rubber and poly ( acrylonitrile – co – acrylamide ) , or mixtures or co – polymers thereof , carboxymethyl cellulose ( CMC ) , poly vinylalcohols ( PVA ) , polyacrylic acids ( PAA ) , polystyrenebutadiene rubber ( SBR ) , PEO , or co – polymers of polyacrylonitrile , polyethylene oxides ( PEO ) and polyacry lamide ( PAAm ) , poly vinylalcohols ( PVA ) and polyacryl amide ( PAAm ) , or PEO and polyacrylronitrile ( PAN ) , or co – polymers or mixtures thereof . 20 . The method of claim 17 , wherein the second binder material is a soft polymer comprising at least one selected from the group consisting of homopolymers or copolymers of acrylic acid or methacrylic acid derivatives , polybutyl acrylate , polybutyl methacrylate , polyhydroxyethyl meth acrylate , polyacrylamide , polyacrylonitrile , butyl acrylate styrene copolymers , butyl acrylate – acrylonitrile copolymers , butyl acrylate – acrylonitrile – glycidyl methacrylate copoly mers , polyisobutylene , isobutylene – isoprene rubber , isobu tylene – styrene copolymers , polybutadiene , polyisoprene , butadiene – styrene random copolymers , isoprene – styrene random copolymers , acrylonitrile – butadiene copolymers , acrylonitrile – butadiene – styrene copolymers , butadiene – sty rene – block copolymers , styrene – butadiene – styrene – block copolymers , isoprene – styrene – block copolymers , styrene isoprene – styrene – block copolymers , dimethylpolysiloxane , diphenylpolysiloxane , dihydroxypolysiloxane , liquid poly ethylene , polypropylene , poly – 1 – butene , ethylene – a – olefin copolymers , propylene – d – olefin copolymers , ethylene – pro pylene – diene copolymers ( EPDM ) , ethylene – propylene – sty rene copolymers , polyvinyl alcohol , polyvinyl acetate , poly vinyl stearate , vinyl acetate – styrene copolymers , polyethylene oxide , polypropylene oxide , epichlorohydrin rubbers , vinylidene fluoride – based rubbers , tetrafluoroethyl ene – propylene rubbers , poly ( 2 – methoxyethoxyethoxyethyl ene ) , styrene butadiene rubber ( SBR ) , butadiene – acryloni trile , rubber ( NBR ) , hydrogenated NBR ( HNBR ) , epichlorhydrin rubber ( CHR ) and acrylate rubber ( ACM ) . 21 . The method of claim 1 , wherein the compressing step comprises passing the electrode composite through a pair of opposing rollers . 22 . The method of claim 21 , wherein the electrode com posite sheet is passed through a plurality of pairs of rollers , the spacing between the rollers decreasing for each subse quent pair of rollers . 23 . A binder system for the fabrication of an electrode comprising active materials and a current collector , the binder comprising : a first lithium ion transporting polymeric coating binder material coating the active materials to produce a first binder coated active material composite ; and , a second polymeric binder material binding the coated first binder coated active material composites together and to the current collector ; wherein when formed the electrode possesses positive characteristics for adhesion according to ASTM stan dard test D3359 – 09e2 , entitled Standard Test Methods for Measuring Adhesion by Tape Test , and wherein the electrode composite sheet and the electrode possess positive characteristics for flexibility according to the Mandrel Test . 24 . The binder of claim 23 , wherein the ratio of the first polymeric coating binder material to the second polymeric binder material is between 1 : 20 and 20 : 1 by weight . 25 . An electrode , comprising : electrode active materials ; a first lithium ion transporting polymeric binder material for coating the active materials to produce a first binder coated active material composite ; a second polymeric binder material binding the first binder coated active material composites together and to the current collector ; wherein when formed the electrode possesses positive characteristics for adhesion according to ASTM stan dard test D3359 – 09e2 , entitled Standard Test Methods for Measuring Adhesion by Tape Test , and wherein the electrode composite sheet and the electrode possess positive characteristics for flexibility according to the Mandrel Test . 26 . An electrode , comprising : a current collector ; an electrode composite comprising from 70 – 98 % active material , from 0 – 10 % conductive material additives , and from 2 – 20 % polymer binder , based on the total weight of the electrode composite ; the electrode composite being formed into an electrode composite sheet ; the electrode composite sheet being adhered to the current collector to form the electrode , wherein the electrode possesses positive characteristics for adhesion accord ing to ASTM standard test D3359 – 09e2 , entitled Stan dard Test Methods for Measuring Adhesion by Tape Test , and wherein the electrode composite sheet and the electrode possess positive characteristics for flexibility according to the Mandrel Test . 27 . The electrode of claim 26 , wherein the polymer binder is a single nonfluoropolymer binder . 28 . A process for making an electrode , comprising the steps of : coating electrode active materials with a first lithium ion transporting polymeric coating binder material to pro duce a first binder coated active material composite ; mixing the coated electrode active materials with a second polymeric binder material for binding the first binder coated active material composite together and to a current collector ; compressing the electrode composite into an electrode composite sheet ; and , applying the electrode composite sheet to a current col lector with pressure to form an electrode , wherein the electrode possesses positive characteristics for adhe sion according to ASTM standard test D3359 – 09e2 , entitled Standard Test Methods for Measuring Adhe sion by Tape Test , and wherein the electrode composite sheet and the electrode possess positive characteristics for flexibility according to the Mandrel Test .

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Title

DRY PROCESS METHOD FOR PRODUCING ELECTRODES FOR ELECTROCHEMICAL DEVICES AND ELECTRODES FOR ELECTROCHEMICAL DEVICES

Inventor(s)

Jian-ping Zheng, Qiang Wu

Assignee(s)

Florida State University Research Foundation Inc

Patent #

20180175366

Patent Date

June 21, 2018

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