WO2018210723A1 - Verfahren zum herstellen eines trockenfilms, walzvorrichtung, sowie trockenfilm und mit dem trockenfilm beschichtetes substrat - Google Patents
Verfahren zum herstellen eines trockenfilms, walzvorrichtung, sowie trockenfilm und mit dem trockenfilm beschichtetes substrat Download PDFInfo
- Publication number
- WO2018210723A1 WO2018210723A1 PCT/EP2018/062334 EP2018062334W WO2018210723A1 WO 2018210723 A1 WO2018210723 A1 WO 2018210723A1 EP 2018062334 W EP2018062334 W EP 2018062334W WO 2018210723 A1 WO2018210723 A1 WO 2018210723A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- dry film
- roller
- substrate
- roll
- calender
- Prior art date
Links
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 239000000758 substrate Substances 0.000 title claims description 58
- 239000000843 powder Substances 0.000 claims abstract description 29
- 239000000203 mixture Substances 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims description 41
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
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- 229910052799 carbon Inorganic materials 0.000 claims description 8
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- 229910052751 metal Inorganic materials 0.000 claims description 7
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- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 5
- 238000012986 modification Methods 0.000 claims description 5
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- 229910052717 sulfur Inorganic materials 0.000 claims description 5
- 229910052782 aluminium Inorganic materials 0.000 claims description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 4
- 239000002482 conductive additive Substances 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 239000011889 copper foil Substances 0.000 claims description 3
- 238000010030 laminating Methods 0.000 claims description 3
- 239000007769 metal material Substances 0.000 claims description 3
- 230000009969 flowable effect Effects 0.000 claims description 2
- 229910000314 transition metal oxide Inorganic materials 0.000 claims description 2
- 238000000059 patterning Methods 0.000 claims 1
- 238000003860 storage Methods 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 description 10
- 238000003825 pressing Methods 0.000 description 7
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 4
- 239000011149 active material Substances 0.000 description 4
- 229910001416 lithium ion Inorganic materials 0.000 description 4
- 239000002048 multi walled nanotube Substances 0.000 description 4
- 230000006641 stabilisation Effects 0.000 description 4
- 238000011105 stabilization Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 3
- 229910002102 lithium manganese oxide Inorganic materials 0.000 description 3
- VLXXBCXTUVRROQ-UHFFFAOYSA-N lithium;oxido-oxo-(oxomanganiooxy)manganese Chemical compound [Li+].[O-][Mn](=O)O[Mn]=O VLXXBCXTUVRROQ-UHFFFAOYSA-N 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000010008 shearing Methods 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000003490 calendering Methods 0.000 description 2
- 239000002041 carbon nanotube Substances 0.000 description 2
- 229910021393 carbon nanotube Inorganic materials 0.000 description 2
- 206010061592 cardiac fibrillation Diseases 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 230000002600 fibrillogenic effect Effects 0.000 description 2
- 229910000625 lithium cobalt oxide Inorganic materials 0.000 description 2
- BFZPBUKRYWOWDV-UHFFFAOYSA-N lithium;oxido(oxo)cobalt Chemical compound [Li+].[O-][Co]=O BFZPBUKRYWOWDV-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 2
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 2
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
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- 230000008023 solidification Effects 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
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- KFDQGLPGKXUTMZ-UHFFFAOYSA-N [Mn].[Co].[Ni] Chemical compound [Mn].[Co].[Ni] KFDQGLPGKXUTMZ-UHFFFAOYSA-N 0.000 description 1
- BNOODXBBXFZASF-UHFFFAOYSA-N [Na].[S] Chemical compound [Na].[S] BNOODXBBXFZASF-UHFFFAOYSA-N 0.000 description 1
- ZYXUQEDFWHDILZ-UHFFFAOYSA-N [Ni].[Mn].[Li] Chemical compound [Ni].[Mn].[Li] ZYXUQEDFWHDILZ-UHFFFAOYSA-N 0.000 description 1
- OGCCXYAKZKSSGZ-UHFFFAOYSA-N [Ni]=O.[Mn].[Li] Chemical compound [Ni]=O.[Mn].[Li] OGCCXYAKZKSSGZ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000002318 adhesion promoter Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000000274 adsorptive effect Effects 0.000 description 1
- NDPGDHBNXZOBJS-UHFFFAOYSA-N aluminum lithium cobalt(2+) nickel(2+) oxygen(2-) Chemical compound [Li+].[O--].[O--].[O--].[O--].[Al+3].[Co++].[Ni++] NDPGDHBNXZOBJS-UHFFFAOYSA-N 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
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- 239000006229 carbon black Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 229910000428 cobalt oxide Inorganic materials 0.000 description 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 description 1
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- 229910052744 lithium Inorganic materials 0.000 description 1
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
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Classifications
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- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
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- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
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- B29C43/24—Calendering
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- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
- H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
- H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/661—Metal or alloys, e.g. alloy coatings
- H01M4/662—Alloys
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/663—Selection of materials containing carbon or carbonaceous materials as conductive part, e.g. graphite, carbon fibres
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/665—Composites
- H01M4/667—Composites in the form of layers, e.g. coatings
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- the present invention relates to a method of manufacturing a substrate, a rolling apparatus, a dry film, and a dry film-coated substrate.
- US 7352558 B2 discloses pressing to a freestanding film.
- a three-stage process is usually carried out, in which a fibrillation of a dry powder mixture by means of an air jet mill, a
- From DE 10 2014 208 145 B3 is a battery cell with a coated electrode and their preparation.
- the present invention is therefore based on the object to propose a method which avoids the disadvantages mentioned, so that dry films can be applied to a substrate in an efficient and mechanically stable manner.
- a dry powder mixture is processed by a rolling apparatus having a first roll and a second roll into the dry film.
- the first roller in this case has a higher rotational peripheral speed than the second roller and the resulting dry film is stored on the first roller.
- Roll-driven rolling apparatus achieves mechanical stabilization and film formation on the first roll which rotates faster than the second roll. Thus, formation of a free-standing film is avoided, and further processing of the dry film supported on the first roll can be carried out immediately.
- the dry film is applied to a substrate by the two rollers, preferably laminated to the substrate, but alternatively or additionally, this may already be done while the dry film is being generated.
- the substrate has a sufficient roughness, for example, configured as a metal wire mesh or carbon fiber mat
- the dry film can also be pressed with the substrate due to a successful gearing.
- it can also be provided to detach the dry film from the first roller, for example by means of a doctor blade. Due to the different roller speeds (which influence a distance in dry film forming structures) and a pressing force (which has an influence on a structural height of these structures), the dry film produced typically has a fibril structure with a roughness R a of 10 ⁇ m or less.
- a ratio of the rotational peripheral speed of the first roller to the rotational peripheral speed of the second roller is between 10: 9 to 10: 1.
- a ratio of 10: 7 to 10: 3, particularly preferably 2: 1 is maintained.
- the dry film be formed with a corrugated structure, in which due to the different roller speeds a periodicity of the structure can be seen.
- a circumference of the first roller typically corresponds to a circumference of the second roller, so that a simple construction with two rollers of the same diameter results.
- it can also be provided-for example to achieve defined rotational speeds taking into account the respective circumference-to design the first roller and the second roller with different diameters and thus different calf circumferences.
- the rolling device may be formed as a calender rolling device.
- heatable rollers By heatable rollers, a further solidification of the dry film m can be achieved.
- heatable rolls or at least one heatable roll By means of heatable rolls or at least one heatable roll, the formation of the fibril structure can be assisted.
- a temperature of the at least one heatable roll should be between 80 ° C and 120 ° C.
- the second roller having a lower rotational peripheral speed than the first roller is provided with a modification, preferably a coating on its surface, which is repellent and / or adhesion-reducing to the forming dry film, so that the dry film is lighter can be removed.
- the coating may comprise or consist of polytetrafluoroethylene (PTFE), silicone and / or diamond-like carbon.
- the first roller may have a corresponding modification which acts to promote adhesion to the forming dry film.
- the modification may also be realized by a roughened surface, for example by the first roller having a surface with a greater roughness than the second roller.
- the surface of the second roll may be polished smooth.
- the dry film is typically applied to a substrate, preferably laminated, and moved for application at a speed equal to the rotational peripheral speed of the first roller. speaks. This allows a smooth transfer of the dry film from the first roller to the substrate due to the matched speeds.
- the substrate is moved over the first roller while the dry film is formed on the substrate. As a result, a direct formation of the dry layer takes place simultaneously with the movement of the substrate. If the substrate, together with a primer film, is guided directly over the first roller, an adhesion promoter layer can be applied to the substrate.
- the dry film is formed by the first roller and the second roller with a line force between the first roller and the second roller in the nip of 100 N / cm to 10 kN / cm, preferably 400 N / cm to achieve sufficient mechanical solidification of the dry film.
- the substrate is formed from a metallic material or has this metallic material in order to serve as an electrode for an energy storage unit can.
- the substrate may be provided with a primer and / or a binder prior to laminating the dry film on a respective surface to be lamination.
- a primer and / or a binder prior to laminating the dry film on a respective surface to be lamination.
- this is a thermoplastic
- the primer layer may comprise conductive carbon black and / or a thermoplastic component, preferably polyvinylpyrrolidone (PVP).
- the substrate is formed from an expanded metal, a metal wire mesh, a nonwoven fabric, a substrate having a structured surface that allows mechanical interlocking, or a metal foil, preferably a copper foil or an aluminum foil.
- a copper foil or an aluminum foil is used, to which a carbon primer is applied.
- the dry film is typically formed with a thickness of less than 500 ⁇ m, preferably less than 300 ⁇ m, particularly preferably less than 150 ⁇ m, in order to obtain a thin and at the same time mechanically stable dry film.
- Polytetrafluoroethylene a Leitadditiv, for example, carbon nanotubes, porous carbon, a transition metal oxide and / or sulfur contains or has.
- the dry powder mixture may include porous carbon (eg, porous carbon black or carbon nanotubes), sulfur, polytetrafluoroethylene, and optionally another conductive additive.
- an active material preferably lithium iron phosphate (LFP), lithium manganese oxide (LMO), nickel-manganese-cobalt (NMC), nickel-rich lithium-nickel-manganese
- Cobalt oxide NMC 622 or NMC 811
- lithium-nickel-cobalt-aluminum oxide NCA
- lithium-cobalt-oxide LCO
- lithium-manganese-nickel oxide LMNO
- lithium titanate LTO
- a dry powder mixture is guided from a powder conveyor into the nip between a first calender roll and a second calender roll.
- the first and second calender rolls are formed or driven so that the first
- Calender roll has a higher rotational peripheral speed than the second calender roll and the first and the second calender roll each have opposite rotational direction.
- a substrate in particular a
- Foil or a net be guided through the nip.
- the coating is in regular and timely coordinated Exposed to intervals, so that uncoated stripes arise.
- This timing and accuracy of the producible shapes and the accuracy of the edges is limited possible.
- the process speed for intermittent formation of dry films and coating on a substrate can be reduced by half compared to continuous coatings ( ⁇ 30 m / min instead of ⁇ 60 m / min).
- Dry film (not transferred to the substrate surface) is removed from the first calender roll, reprocessed, and can be reused. So any geometry can be realized with good precision without reducing the process speeds.
- a further first calender roll rotating about a rotation axis may be present, on which a dry film formed between the first calender roll and the second calender roll can be wound up after leaving the nip.
- the two first calender rolls should have the same rotational peripheral speed.
- a substrate, preferably a film with the dry film can be guided through the nip between the first calender roll and the second calender roll and wound onto the further first calender roll.
- a dry film has anisotropically formed fibrils. By shearing in the nip, these fibrils are preferably anisotropic in the running direction of the first roll and the second roll. A length of the fibrils lies in the range between 0.1 ⁇ and 1000 ⁇ . Alternatively or additionally, the dry film with the fibrils can have a roughness R a of less than 10 ⁇ m.
- the dry film is typically disposed on a substrate.
- An electrochemical store or an electrochemical converter preferably has a dry film with the properties described or a substrate provided with the dry film with the properties described.
- the dry film and the dry film substrate are preferably made by the described method, so the described method is for forming the dry film and the dry film substrate.
- a non-flowable powder mixture can be used. This non-flowability can be determined under the test conditions according to the German standard EN ISO 6186: 1998 (as of August 1998).
- Fig. 1 is a side schematic view of a rolling device
- Fig. 2 is a figure 1 corresponding view of a double rolling device
- Fig. 3 is a figure 1 corresponding view of the rolling device with substrate feed.
- 1 shows a schematic side view of a rolling device is shown, in which from a powder conveyor 1 stored in the powder conveyor 1 dry powder mixture on two identical in their dimensions chromed calender rolls 2a and 2b and these by acting pressing and shearing forces in a stable Condition is transferred.
- the first calender roll 2a is hereby operated at a higher rotational speed than the second calender roll 2b, so that a drying film 3 which is formed remains on the first calender roll 2a after the combined pressing and shearing process.
- the dry powder used is pre-mixed in the illustrated embodiment and has 90 weight percent Ketjenblack / sulfur (1: 2 m / m), 3 weight percent polytetrafluoroethylene (PTFE) and
- MWCNT multi-walled carbon nanotubes
- a lithium ion electrode typically 95 weight percent lithium manganese oxide, 3 weight percent lead additive (in this case
- MWCNT multi-walled carbon nanotubes
- PTFE 2 weight percent PTFE
- the rotational speeds of the first roller 2a and the second roller 2b are in a range between 10: 9 and 10: 4, in the illustrated embodiment at 2: 1 namely either 10 mm / s: 5 mm / s or 20 mm / s: 10 mm / s.
- 80 mm / s: 40 mm / s can also be used as rotational speeds, depending on the parameter window and the powder state.
- Higher rotational speeds result here in thinner dry films with a less pronounced ripple structure or less pronounced fibrils, ie a lower surface roughness R a .
- the fibrils have in the illustrated embodiment, a length of on average 10 ⁇ and are anisotropic in the direction of the rollers 2a and 2b formed.
- the first roller 2a and the second roller 2b can each be heated in the illustrated embodiment to a temperature of 100 ° C.
- the first roller 2a may be provided with an adhesion-promoting surface to which the dry film 3 adheres, while the second roller 2b has a surface adhering to the dry film 3.
- An acting line force between the first roller 2a and the second roller 2b in the illustrated embodiment is 400 N.
- the dry film 3 can be removed from the first roller 2a and thus, for example, a solvent-free electrode can be generated.
- FIG. 2 an embodiment corresponding to FIG. 1 is reproduced, in which a symmetrical structure of two of the rolling apparatus shown in FIG. 1 is present. Recurring features are provided with identical reference numerals in this figure as well as in the following figure.
- the substrate 4 is passed in the illustrated embodiment between two rolling devices, which are arranged mirror-symmetrically to each other.
- the two first rollers 2a, on each of which one of the dry films 3 is guided, are facing each other, so that the substrate 4 can be provided on both sides with the dry film 3, since both surfaces each face one of the rollers 2a.
- the substrate 4 is this with a speed which corresponds to the rotational peripheral speed of the first two rollers 2a.
- the two rolling devices are constructed identically in the embodiment shown except for the mirror-symmetrical arrangement, so in particular have the same dimensions, and are operated at the same rotational speeds or rotational peripheral speeds.
- dry films 3 differing in their composition can also be applied to the substrate 4, but in the exemplary embodiment shown in FIG. 2, the dry films 3 are identical.
- the described method also allows the production of an electrode with alternative current conductors as a substrate 4, z. B. perforated low basis weight substrates such as perforated metal foils or conductive fabrics.
- the substrate 4 is an aluminum foil with a carbon primer as a double-sided coating.
- Lithium-ion batteries lithium-sulfur batteries, sodium-sulfur batteries, solid-state batteries,
- Supercell electrodes electrodes for fuel cells, electrodes for electrolysis cells, electrodes for other electrochemical elements, but also filter membranes or adsorptive coatings by using porous particles, decorative layers, optical layers for absorption and / or layers of moisture-sensitive or solvent-sensitive materials allows.
- FIG. 3 shows, in a schematic side view corresponding to FIG. 1, a further embodiment of the invention in which the substrate 4 is wound on a substrate roll 5 in the form of a film and introduced into the nip in film form, so that the drying film 3 forming is is laminated directly to the substrate 4 in the nip.
- the dry film 3 is no longer supported directly, ie in contact with the first roller 2a, in direct contact, but is guided only indirectly on the first roller 2a and wound on a further roller 2a. Therefore, the described method allows electrode fabrication directly from a premixed dry film powder without additional fibrillation steps, so that no freestanding film also has to be formed.
- the method can be used for a prefibrillation, in which an increase in the mechanical stability of the dry film is possible.
- the freestanding film can be realized by detachment from the carrier roll.
- a loading and density can be adjusted.
- the dry film formation is self-dosing, the resulting layer thickness results from the pressing force of the two rollers 2a and 2b.
- About a continuous entry of a specific (adapted to process parameters) amount of powder, for example via the powder conveyor 1 or a conveyor substrate is a predosing.
- the mechanical stability of the dry film 3 is adjusted by the applied pressing forces and rotational speeds (shear rates). Compared to free-standing films, which were merely pressed in the nip at the same rotational speeds of the rollers 2a and 2b, the dry films 3 produced by the proposed method have a considerably increased mechanical stability.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Power Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Cell Electrode Carriers And Collectors (AREA)
- Moulding By Coating Moulds (AREA)
- Press Drives And Press Lines (AREA)
- Inert Electrodes (AREA)
Abstract
Description
Claims
Priority Applications (13)
Application Number | Priority Date | Filing Date | Title |
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EP22192127.3A EP4119323A1 (de) | 2017-05-16 | 2018-05-14 | Verfahren zum herstellen eines trockenfilms, walzvorrichtung, sowie trockenfilm und mit dem trockenfilm beschichtetes substrat |
CN201880032871.8A CN110869179B (zh) | 2017-05-16 | 2018-05-14 | 干膜的制造方法、辊压装置、干膜以及电化学存储元件或电化学转换器 |
CN202210381330.4A CN115071025B (zh) | 2017-05-16 | 2018-05-14 | 干膜的制造方法、辊压装置、干膜以及电化学存储元件 |
EP18729874.0A EP3625018B1 (de) | 2017-05-16 | 2018-05-14 | Verfahren zum herstellen eines trockenfilms |
PL18729874.0T PL3625018T3 (pl) | 2017-05-16 | 2018-05-14 | Sposób wytwarzania suchej folii |
KR1020197037010A KR102416449B1 (ko) | 2017-05-16 | 2018-05-14 | 드라이 필름의 제조방법, 롤링 장치, 드라이 필름 및 드라이 필름으로 코팅된 기판 |
RS20231097A RS64947B1 (sr) | 2017-05-16 | 2018-05-14 | Postupak za izradu suvog filma |
US16/613,138 US11990599B2 (en) | 2017-05-16 | 2018-05-14 | Method for producing a dry film, rolling device |
JP2019563588A JP2020522090A (ja) | 2017-05-16 | 2018-05-14 | ドライフィルムの製造方法、圧延装置、ドライフィルム、およびドライフィルムで被覆された基材 |
KR1020227022326A KR102597499B1 (ko) | 2017-05-16 | 2018-05-14 | 드라이 필름의 제조방법, 롤링 장치, 드라이 필름 및 드라이 필름으로 코팅된 기판 |
ES18729874T ES2963957T3 (es) | 2017-05-16 | 2018-05-14 | Procedimiento para la producción de una película seca |
JP2022016185A JP7248835B2 (ja) | 2017-05-16 | 2022-02-04 | ドライフィルムの製造方法、圧延装置、ドライフィルム、およびドライフィルムで被覆された基材 |
US18/624,223 US20240274784A1 (en) | 2017-05-16 | 2024-04-02 | Method for producing a dry film, rolling device, dry film, and substrate coated with the dry film |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE102017208220.8A DE102017208220A1 (de) | 2017-05-16 | 2017-05-16 | Verfahren zum Herstellen eines Trockenfilms sowie Trockenfilm und mit dem Trockenfilm beschichtetes Substrat |
DE102017208220.8 | 2017-05-16 |
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US16/613,138 A-371-Of-International US11990599B2 (en) | 2017-05-16 | 2018-05-14 | Method for producing a dry film, rolling device |
US18/624,223 Continuation US20240274784A1 (en) | 2017-05-16 | 2024-04-02 | Method for producing a dry film, rolling device, dry film, and substrate coated with the dry film |
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WO2018210723A1 true WO2018210723A1 (de) | 2018-11-22 |
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PCT/EP2018/062334 WO2018210723A1 (de) | 2017-05-16 | 2018-05-14 | Verfahren zum herstellen eines trockenfilms, walzvorrichtung, sowie trockenfilm und mit dem trockenfilm beschichtetes substrat |
Country Status (11)
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US (2) | US11990599B2 (de) |
EP (2) | EP4119323A1 (de) |
JP (3) | JP2020522090A (de) |
KR (2) | KR102597499B1 (de) |
CN (2) | CN115071025B (de) |
DE (1) | DE102017208220A1 (de) |
ES (1) | ES2963957T3 (de) |
HU (1) | HUE064505T2 (de) |
PL (1) | PL3625018T3 (de) |
RS (1) | RS64947B1 (de) |
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WO2023021107A2 (de) | 2021-08-19 | 2023-02-23 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Verfahren zur lösungsmittelfreien herstellung einer elektrode und bereitgestellte elektrode |
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EP4369429A1 (de) | 2022-11-11 | 2024-05-15 | Volkswagen Ag | Verfahren und vorrichtung zur herstellung eines trockenfilms |
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EP4431191A1 (de) | 2023-03-14 | 2024-09-18 | Volkswagen Ag | Verfahren zum betrieb einer walzvorrichtung für die herstellung einer elektrodenbahn sowie walzvorrichtung |
EP4435880A1 (de) | 2023-03-21 | 2024-09-25 | Volkswagen Ag | Prozessanordnung sowie verfahren zur fertigung einer elektrode |
DE102023202929A1 (de) | 2023-03-30 | 2024-10-02 | Volkswagen Aktiengesellschaft | Verfahren zur Herstellung von trockenen Elektroden auf einem Stromsammler mittels einer Walzenanlage, Walzenanlage, trockene Elektrode, Computerprogrammprodukt sowie computerlesbares Medium |
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KR20200020702A (ko) | 2020-02-26 |
US20240274784A1 (en) | 2024-08-15 |
EP4119323A1 (de) | 2023-01-18 |
ES2963957T3 (es) | 2024-04-03 |
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KR102597499B1 (ko) | 2023-11-06 |
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CN115071025B (zh) | 2023-12-26 |
DE102017208220A1 (de) | 2018-11-22 |
HUE064505T2 (hu) | 2024-03-28 |
EP3625018B1 (de) | 2023-08-30 |
PL3625018T3 (pl) | 2024-02-26 |
CN110869179B (zh) | 2022-04-29 |
KR102416449B1 (ko) | 2022-07-04 |
JP2023103999A (ja) | 2023-07-27 |
EP3625018C0 (de) | 2023-08-30 |
JP7248835B2 (ja) | 2023-03-29 |
CN110869179A (zh) | 2020-03-06 |
JP2020522090A (ja) | 2020-07-27 |
RS64947B1 (sr) | 2024-01-31 |
CN115071025A (zh) | 2022-09-20 |
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