CA2918178C - Method to produce a composite semi-finished product - Google Patents
Method to produce a composite semi-finished product Download PDFInfo
- Publication number
- CA2918178C CA2918178C CA2918178A CA2918178A CA2918178C CA 2918178 C CA2918178 C CA 2918178C CA 2918178 A CA2918178 A CA 2918178A CA 2918178 A CA2918178 A CA 2918178A CA 2918178 C CA2918178 C CA 2918178C
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- CA
- Canada
- Prior art keywords
- finished product
- filler
- composite semi
- thermoplastic plastic
- weight
- Prior art date
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Classifications
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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
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8803—Supports for the deposition of the catalytic active composition
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
- H01M8/188—Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0239—Organic resins; Organic polymers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0241—Composites
- H01M8/0243—Composites in the form of mixtures
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/0273—Sealing or supporting means around electrodes, matrices or membranes with sealing or supporting means in the form of a frame
-
- 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
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Sustainable Energy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Composite Materials (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Inert Electrodes (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Fuel Cell (AREA)
- Lining Or Joining Of Plastics Or The Like (AREA)
Abstract
Date recue/date received 2021-10-27
Description
Furthermore, the invention relates to a use of such a composite semi-finished product and an electrode of an electrochemical cell, produced from such a composite semi-finished product.
Composite semi-finished products of the type referred to are in particular used to produce highly electrically conductive components. Electrodes for electrochemical cells, for example for fuel cells, redox flow batteries or similar, represent an area of application. For these and other fields of application, a high proportion of filler is desirable as in many cases the filler provides an important property of the composite semi-finished product. High thermal and/or electrical conductivities are, for example, achieved by a high proportion of graphite, which typically amounts to 70% by weight of the composite semi-finished product and more. These high proportions of filler provide some features during the production of the composite semi-finished products.
A substantial feature consists in the homogenous distribution of the filler in the matrix of the thermoplastic plastic. Extruders or kneaders are used for this, to which the plastic is supplied in the form of pellets or similar and the filler is supplied in the form of fine particles. The thermoplastic plastic is melted in the extruder or kneader and the filler is mechanically incorporated into the plastic melt. This process requires a low viscosity of the mixture such that the plastic must be heated far above the actual melting temperature.
The compound material can subsequently be brought into shape by injection moulding, for which, however, an even lower viscosity is required. The plastic must therefore be very strongly heated and subjected to a high pressure.
Alternatively, the Date recue/date received 2021-10-27
The calendering process leads to a long dwell time of the compound material in the calender which correspondingly must be strongly heated for a long time.
Composite semi-finished products produced in a corresponding manner have only low thermoplastic properties which is disadvantageous for the further processing of the composite semi-finished products. The composite semi-finished products often have low mechanical strengths and can only be connected or thermally welded to other thermoplastics with difficulty.
Therefore the object of the present invention is to design and to further develop the method referred to at the beginning and previously described in more detail in such a way that composite semi-finished products having improved material properties can be obtained.
According to the present disclosure, a method is provided in which the at least one thermoplastic plastic in the form of fine particles is mixed with the at least one filler in the form of fine particles, wherein in each case at least 90% by weight of the particles of the at least one thermoplastic plastic and of the at least one filler are smaller than 1 mm, in which the mixture of the at least one thermoplastic plastic and the at least of filler is heated to a temperature greater than the melting temperature of the at least one thermoplastic plastic, and in which the heated material is cooled to a temperature below the solidification temperature of the at least one thermoplastic plastic.
The invention has therefore recognised that not, as previously assumed, the particle size of the at least one filler, but in particular the particle size of the plastic and the mixture of both components before the actual processing of the materials has a considerable influence on the material properties of the composite semi-finished product. This is surprising in so far as the at least one plastic is melted independently Date recue/date received 2021-10-27
In connection with the invention, it has been recognised that the matrix structure formed by the at least one thermoplastic plastic very much depends on the original particle size of the plastic particles, and indeed indirectly. This is ascribed to the processing times and the processing temperatures in the case of the use of plastics having very small particle sizes being able to be clearly reduced according to the invention such that no or only a low number of appearances of decomposition occur with regard to the plastic or the matrix structure thereof. This is obviously due not least to the improved heat transport processes in the case of use of smaller plastic particles and the better processing ability of the previously produced, preferably substantially homogenous, mixture of plastic and filler particles. Therefore, finally a composite material is obtained, the material properties of which, despite the very high proportions of filler, are more similar to the material properties of the at least one thermoplastic plastic than this is case for the composite materials of the same composition known from the prior art, without notably effecting the material properties provided by the filler, in particular the electrical conductivity, in a disadvantageous manner. A thermoplastic composite semi-finished product can therefore preferably be obtained using the method according to the invention, said thermoplastic composite semi-finished product being able to be further processed fundamentally as a pure thermoplastic plastic or in any case in a similar manner.
For this purpose, it is particularly preferred if at least 95% by weight, in particular substantially 100% by weight of the particle distribution of the at least one thermoplastic plastic are smaller than 1mm. Incidentally, it can be preferred for the provision of a mixture which is as homogenous as possible, before the actual processing of the same, if the maximum particle sizes of the at least one Date recue/date received 2021-10-27
Furthermore, it can be preferred if the temperature to which the mixture of at least one thermoplastic plastic and at least one electrically conductive filler is only heated to a temperature which lies above the melting temperature but below the decomposition temperature of the at least one plastic. In the case of several thermoplastic plastics, these can be brought to a temperature above the highest melting temperature and below the lowest decomposition temperature of the thermoplastic plastics. Incidentally, the temperature of the material is subsequently lowered to a temperature which lies below the lowest solidification temperature of the thermoplastic plastics used.
In a first preferred embodiment of the method, the material of the filler has an electrical conductivity of at least 1 S/m, preferably at least i0 S/m, in particular at least 106S/m. The bulk material of small filler particles can have a correspondingly lower conductivity. Therefore, a composite semi-finished product having preferred properties can be obtained. Alternatively or additionally, the electrical conductivity of the composite semi-finished product can amount to at least 1 S/m, preferably at least 100 S/m, in particular at least 1000 S/m. Fundamentally, however, it is preferred if the at least one electrically conductive filler is more electrically conductive than the at least one thermoplastic plastic, in particular all thermoplastic plastics.
The electrically conductive filler is preferably carbon, graphite, soot, titanium carbide (TiC), at least one metal and/or at least one metal compound. These fillers are particularly suitable due to their mechanical properties and their conductivity.
For example a polyolefin, in particular polyethylene (PE) and/or polypropylene (PP), polyphenylene sulphide (PPS), polyether ether ketone (PEEK), polyvinyl chloride (PVC) and/or polyamide (PA) are eligible as a thermoplastic plastic. These materials offer advantages with regard to the processing ability and the joining of the Date recue/date received 2021-10-27
So that the desired properties of the at least one filler determine the properties of the composite semi-finished product to a great extent, it is fundamentally preferred if the at least one filler forms a high proportion of the composite semi-finished product. As, additionally, however, the matrix structure of the at least one thermoplastic plastic substantially influences the material properties, the proportion of the at least one filler in the composite semi-finished product amounts, as required, to between 50% by weight and 95% by weight, preferably between 70% by weight and 92% by weight, in particular between 80% by weight and 90% by weight.
In order to improve the processing ability of the composite semi-finished product, it is expedient if 90% by weight of the particles of the at least one thermoplastic plastic and/or of the at least one filler are smaller than 750 pm, preferably smaller than 500 pm, in particular smaller than 300 pm. Favourable results were in particular achieved for particle sizes of approximately 150 pm. In this context it is also preferred if the predetermined particle size is fallen below by at least 95% by weight, in particular substantially 100% by weight, of the corresponding particles. Therein, however, it must be noted that, as a rule, low quantities of particles which are larger than the corresponding limit value can be well tolerated. Nevertheless, it is expedient to eliminate larger particles beforehand by sieving or another separating method.
In order to enable a quick and gentle processing, a rolling mill or a calender can be used to heat and/or cool the material. In this context, a rolling mill is understood to be an arrangement of two rollers and a calender is understood to be an arrangement of at least three rollers. For the previously described purpose, it is furthermore expedient if the rolling mill and/or the calender comprises a roller which is able to be heated and/or at least one roller which is able to be cooled.
Date recue/date received 2021-10-27
The material can, if necessary also be heated and cooled in an injection moulding system. This facilitates and accelerates, if necessary, the production of a composite semi-finished product, in particular of a composite semi-finished product having a complicated outer shape. It is therefore particularly preferred for the simplification of the processing that the heating occurs in an extruder and the cooling occurs in an injection mould.
Alternatively, the material can also be introduced into a matrix after heating and can be pressed into shape by means of a patrix. This method is also referred to as a hot pressing method. In this way, composite semi-finished products having a complicated outer shape and/or large dimensions can also be produced easily. Therein if necessary an extruder can likewise be used for heating.
In order to be able to ensure an easy further processing of the composite semi-finished product, it is also fundamentally preferred to produce a planar composite semi-finished product.
Date recue/date received 2021-10-27
According to the present disclosure, a composite semi-finished product produced according to the present disclosure may be used for the production of an electrode of an electrochemical cell, for example a redox flow battery, of a fuel cell or of an electrolyser, as a component of a chemical-resistant heat exchanger, as a shield against high-frequency radiation, for example in a piece of medical apparatus, as a low-friction bearing or as a heating foil.
According to the present disclosure, an electrode of an electrochemical cell, for example of a redox flow battery, of a fuel cell or of an electrolyser, may be used as a component of a chemical-resistant heat exchanger, as a shield against high-frequency radiation, for example in a piece of medical apparatus, as a low-friction bearing or as a heating foil, produced according to a method according the present disclosure.
The invention is explained in greater detail below by means of drawings depicting only one exemplary embodiment. In the drawings are shown:
Fig. 1 the course of a method according to the invention in a schematic depiction, Fig. 2 a processing step of the method according to Fig. 1 and Date recue/date received 2021-10-27
In Fig. 1, a method to produce a composite semi-finished product 1 is depicted schematically. The composite semi-finished product 1 is formed from a mixture of a thermoplastic plastic 2 in the form of polypropylene and an electrically conductive filler 3 in the form of graphite. The thermoplastic plastic 2 is initially supplied to a cryogenic milling process in the form of coarse particles. The cryogenic milling process occurs with the addition of a refrigerant, in particular in the form of liquid nitrogen (N2) in order to cool the thermoplastic plastic 2 to a temperature below at least -50 C during the milling process, such that the brittleness of the thermoplastic plastic increases. The filler 3 is also milled with the addition of liquid nitrogen (N2).
The described grinding processes are referred to in Fig. 1 as "cryogenic milling". For the milling of the thermoplastic plastic 2 and of the filler 3, suitable mills are known from the prior art. The thermoplastic plastic 2 and/or the filler 3 can, however, also be milled without particular cooling or can be used entirely without previous milling.
Both the thermoplastic plastic 2 and the electrically conductive filler 3 are sieved after milling, according to the method steps referred to in Fig. 1 as "sieving".
Particles larger than 150pm are therein guided back into the milling process and are milled again. The plastic and filler particles having a size of less than 150pm are mixed with one other as homogenously as possible. The mixers known from the prior art can be used for this. The production of the mixture 4 is referred to in Fig. 1 as a "mixing".
After the mixing of the thermoplastic plastic 2 and the filler 3, the mixture 4 is transferred to a rolling mill 5 depicted in Fig. 2. There, the thermoplastic plastic 2 is melted on a tempered roller 6, which corresponds to the method step "melting"
according to Fig. 1. The roller temperature therein lies approximately 30 C
above the melting temperature of the thermoplastic plastic 2. The particles of the filler 3 are received in this during melting of the thermoplastic plastic 2. Therein, the thermoplastic plastic 2 forms a continuous phase in the form of a matrix for the Date recue/date received 2021-10-27
The further roller 8 is cooled such that the temperature of this roller 8 lies below the solidification temperature of the thermoplastic plastic 2 in the form of polypropylene during the processing of the material. Additionally, this roller 8 has a greater peripheral speed than the heated roller 6. Therefore, the material at least partially solidifies in the roller gap 7 and is removed from the cooled roller 8. As a consequence of the solidification of the material to form the composite semi-finished product 1, this is only partially further transported by the cooled roller 8, and indeed only until a planar composite semi-finished product 1 is removed from the cooled roller 8.
If necessary, the distance between the heated roller 6 and the cooled roller 8 can be variable. Therefore, for example, the width of the roller gap 7 can be adjustable. In particular the distance between the rollers 6, 8 can initially be selected to be so large that a layer 9 made from thermoplastic plastic 2 and electrically conductive filler 3 is initially formed to circulate on the heated roller 6, said electrically conductive filler 3 being homogenised further over time. After this layer 9 has the required thickness and/or the homogeneity, the cooled roller 8 can be driven up to the heated roller 6 in order to form the roller gap 7 and to remove the composite semi-finished product 1 as described.
Date recue/date received 2021-10-27
Date recue/date received 2021-10-27
Claims (23)
Date Recue/Date Received 2023-02-27
by weight of the particles of the at least one thermoplastic plastic and/or of the at least one filler are smaller than 500 pm.
by weight of the particles of the at least one thermoplastic plastic and/or of the at least one filler are smaller than 300 pm.
by weight of the particles of the at least one thermoplastic plastic and/or of the at least one filler are smaller than 200 pm.
Date Recue/Date Received 2023-02-27
Date Recue/Date Received 2023-02-27
23. A composite semi-finished product produced according to the method according to any one of claims 1 to 16.
24. An electrode of an electrochemical cell, wherein the electrode comprises a composite semi-finished product according to claim 23.
25. The electrode of claim 24, wherein the electrochemical cell is a redox flow battery, a fuel cell, or an electrolyser.
26. A component of a chemical-resistant heat exchanger, wherein the component comprises a composite semi-finished product according to claim 23.
27. A shield against high-frequency radiation, wherein the shield comprises a composite semi-finished product according to claim 23.
28. The shield of claim 27, wherein the shield is configured for use in a piece of medical apparatus.
29. A low-friction bearing comprising a composite semi-finished product according to claim 23.
30. A heating foil comprising a composite semi-finished product according to
Date Recue/Date Received 2023-02-27
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEDE102013107514.2 | 2013-07-16 | ||
| DE201310107514 DE102013107514A1 (en) | 2013-07-16 | 2013-07-16 | Process for producing a semi-finished composite product |
| PCT/EP2014/064303 WO2015007544A1 (en) | 2013-07-16 | 2014-07-04 | Method for producing a composite semifinished product |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2918178A1 CA2918178A1 (en) | 2015-01-22 |
| CA2918178C true CA2918178C (en) | 2023-10-03 |
Family
ID=51176360
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2918178A Active CA2918178C (en) | 2013-07-16 | 2014-07-04 | Method to produce a composite semi-finished product |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US11329292B2 (en) |
| EP (1) | EP3022787B1 (en) |
| JP (2) | JP6518239B2 (en) |
| CN (1) | CN105393389B (en) |
| CA (1) | CA2918178C (en) |
| DE (1) | DE102013107514A1 (en) |
| DK (1) | DK3022787T3 (en) |
| ES (1) | ES2768626T3 (en) |
| HU (1) | HUE048568T2 (en) |
| PL (1) | PL3022787T3 (en) |
| PT (1) | PT3022787T (en) |
| WO (1) | WO2015007544A1 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102015015276B4 (en) * | 2015-08-14 | 2017-11-16 | ATP Aicher + Tröbs Produktentwicklung GmbH | Highly filled plastic composition, method of manufacture and use |
| DE102017118118A1 (en) | 2017-08-09 | 2019-02-14 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Electrode for a particular bioelectrochemical cell |
| DE102021104564A1 (en) | 2021-02-25 | 2022-08-25 | Eisenhuth Gmbh & Co. Kg | Process for the continuous production of bipolar plates from plastic mixed with electrically conductive particles |
| DE102024110345A1 (en) | 2024-04-12 | 2025-10-16 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung eingetragener Verein | Electrically conductive plastic and its use |
| DE102024127259A1 (en) | 2024-09-20 | 2026-03-26 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung eingetragener Verein | Methods for the production of composite materials |
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| NL237569A (en) * | 1956-10-16 | 1900-01-01 | ||
| DK116544B (en) * | 1964-06-10 | 1970-01-19 | Madsen E Fuglsang | Injection molding machine for non-metallic masses, such as thermoplastic plastics. |
| US3644271A (en) * | 1970-03-02 | 1972-02-22 | Ethyl Corp | Composition and process for injection molding thermoplastic material and glass fibers |
| US4588443A (en) * | 1980-05-01 | 1986-05-13 | Aktieselskabet Aalborg Pottland-Cement-Fabrik | Shaped article and composite material and method for producing same |
| JPS603990B2 (en) * | 1980-10-31 | 1985-01-31 | ロンシール工業株式会社 | Method for manufacturing floor coverings |
| JPS59155007A (en) | 1983-02-24 | 1984-09-04 | Micro Denshi Kk | Method for heating vinyl chloride resin by microwave |
| DE3543279A1 (en) | 1985-12-07 | 1987-06-11 | Roehm Gmbh | METHOD FOR PRODUCING PLASTIC PRESSING PLATES WITH ELECTRICAL CONDUCTIVITY |
| JPS62209141A (en) * | 1986-02-27 | 1987-09-14 | Nippon Kokan Kk <Nkk> | Mixture of conductive fibrous filler and thermoplastic powder |
| ZA881905B (en) * | 1987-03-17 | 1988-09-09 | Hitek Limited | Forming thermoplastic web materials |
| JPH01112606A (en) * | 1987-07-15 | 1989-05-01 | Nippon Steel Chem Co Ltd | High toughness conductive resin sheet |
| CN1041129A (en) * | 1988-09-16 | 1990-04-11 | 高技术有限公司 | The forming method of thermoplastic sheets |
| DE4018190A1 (en) * | 1990-06-07 | 1991-12-12 | Hestermann Gerhard | Moulded prods. esp. from waste thermoset material - obtd. by mixing epoxy¨ polyester plastic powder with fine- or coarse-grain or fibrous plastic fillers and heating |
| DE4443988A1 (en) * | 1994-12-12 | 1996-06-13 | Hanichl Michelle | Shaped body from plastics waste |
| EP0932644A1 (en) * | 1996-10-15 | 1999-08-04 | Albemarle Corporation | Heat stabilized, flame retardant thermoplastic polymer compositions |
| US6180275B1 (en) | 1998-11-18 | 2001-01-30 | Energy Partners, L.C. | Fuel cell collector plate and method of fabrication |
| JP2000223133A (en) * | 1999-01-28 | 2000-08-11 | Nippon Carbon Co Ltd | Gas channel plate and separator for fuel cell |
| FR2812120B1 (en) * | 2000-07-24 | 2006-11-03 | Commissariat Energie Atomique | CONDUCTIVE COMPOSITE MATERIAL AND ELECTRODE FOR FUEL CELL USING THE MATERIAL |
| FR2812119B1 (en) | 2000-07-24 | 2002-12-13 | Commissariat Energie Atomique | CONDUCTIVE COMPOSITE MATERIAL AND ELECTRODE FOR FUEL CELL USING THE THERMO-COMPRESSED MATERIAL |
| WO2002022952A2 (en) * | 2000-09-12 | 2002-03-21 | Lydall, Inc. | Electrical conductive substrate |
| DE10112394A1 (en) * | 2001-03-13 | 2002-10-02 | Ticona Gmbh | Conductive plastic molding compound, its use and molded articles made therefrom |
| DE10243592A1 (en) * | 2002-09-19 | 2004-04-01 | Basf Future Business Gmbh | Bipolar plate for PEM fuel cells |
| US20040062977A1 (en) * | 2002-10-01 | 2004-04-01 | Graftech, Inc. | Fuel cell power packs and methods of making such packs |
| DE10347701A1 (en) * | 2003-10-14 | 2005-05-19 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Conductive molding, process for its manufacture and use |
| US20070001333A1 (en) * | 2005-06-30 | 2007-01-04 | Ashwit Dias | System and method for forming textured polymeric films |
| EP1991608A4 (en) * | 2006-02-23 | 2011-07-20 | Robert N Clausi | Highly filled composite materials |
| US20080149900A1 (en) * | 2006-12-26 | 2008-06-26 | Jang Bor Z | Process for producing carbon-cladded composite bipolar plates for fuel cells |
| US9379393B2 (en) * | 2006-12-26 | 2016-06-28 | Nanotek Instruments, Inc. | Carbon cladded composite flow field plate, bipolar plate and fuel cell |
| JP4916007B2 (en) * | 2007-03-01 | 2012-04-11 | 三洋化成工業株式会社 | Slush molding resin powder composition and molded product |
| DE102008036320B4 (en) * | 2008-07-29 | 2017-04-06 | Elringklinger Ag | Method for producing a bipolar plate and bipolar plate for a bipolar battery |
| DE102009051434A1 (en) * | 2009-10-30 | 2011-05-05 | Zentrum für Brennstoffzellen-Technik GmbH | Molded body made of highly conductive molding mass that contains a plastic and a filler incorporated into the plastic, useful as sealing including ring, bracelet and rubber gasket, as bipolar plate for an electrochemical cell, and as pipe |
| JP6530191B2 (en) * | 2011-08-17 | 2019-06-12 | ソルベイ スペシャルティ ポリマーズ イタリー エス.ピー.エー. | Milling method |
-
2013
- 2013-07-16 DE DE201310107514 patent/DE102013107514A1/en not_active Ceased
-
2014
- 2014-07-04 CN CN201480040760.3A patent/CN105393389B/en active Active
- 2014-07-04 DK DK14738457.2T patent/DK3022787T3/en active
- 2014-07-04 PT PT147384572T patent/PT3022787T/en unknown
- 2014-07-04 EP EP14738457.2A patent/EP3022787B1/en active Active
- 2014-07-04 JP JP2016526520A patent/JP6518239B2/en active Active
- 2014-07-04 HU HUE14738457A patent/HUE048568T2/en unknown
- 2014-07-04 US US14/905,083 patent/US11329292B2/en active Active
- 2014-07-04 PL PL14738457T patent/PL3022787T3/en unknown
- 2014-07-04 ES ES14738457T patent/ES2768626T3/en active Active
- 2014-07-04 WO PCT/EP2014/064303 patent/WO2015007544A1/en not_active Ceased
- 2014-07-04 CA CA2918178A patent/CA2918178C/en active Active
-
2018
- 2018-12-28 JP JP2018247285A patent/JP2019089337A/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| PT3022787T (en) | 2020-02-20 |
| JP6518239B2 (en) | 2019-05-22 |
| PL3022787T3 (en) | 2020-06-29 |
| HUE048568T2 (en) | 2020-08-28 |
| CN105393389A (en) | 2016-03-09 |
| DK3022787T3 (en) | 2020-03-02 |
| ES2768626T3 (en) | 2020-06-23 |
| EP3022787B1 (en) | 2019-11-27 |
| CA2918178A1 (en) | 2015-01-22 |
| CN105393389B (en) | 2020-07-07 |
| US20160156040A1 (en) | 2016-06-02 |
| WO2015007544A1 (en) | 2015-01-22 |
| JP2019089337A (en) | 2019-06-13 |
| US11329292B2 (en) | 2022-05-10 |
| DE102013107514A1 (en) | 2015-01-22 |
| JP2016531018A (en) | 2016-10-06 |
| EP3022787A1 (en) | 2016-05-25 |
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