WO2014117949A1 - Energieerzeugungseinheit mit einem hochtemperatur-brennstoffzellenstack und einer verdampfungseinheit - Google Patents
Energieerzeugungseinheit mit einem hochtemperatur-brennstoffzellenstack und einer verdampfungseinheit Download PDFInfo
- Publication number
- WO2014117949A1 WO2014117949A1 PCT/EP2014/000285 EP2014000285W WO2014117949A1 WO 2014117949 A1 WO2014117949 A1 WO 2014117949A1 EP 2014000285 W EP2014000285 W EP 2014000285W WO 2014117949 A1 WO2014117949 A1 WO 2014117949A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel
- gas
- evaporation unit
- housing
- evaporator
- Prior art date
Links
Classifications
-
- 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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0618—Reforming processes, e.g. autothermal, partial oxidation or steam reforming
-
- 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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0625—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1853—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines coming in direct contact with water in bulk or in sprays
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/60—Component parts or details of steam boilers specially adapted for steam boilers of instantaneous or flash type
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/066—Integration with other chemical processes with fuel cells
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1276—Mixing of different feed components
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1288—Evaporation of one or more of the different feed components
-
- 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
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M2008/1293—Fuel cells with solid oxide electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2220/00—Batteries for particular applications
- H01M2220/20—Batteries in motive systems, e.g. vehicle, ship, plane
-
- 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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
-
- 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
- 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
Definitions
- the invention relates to a power generation unit with a high-temperature fuel cell stack operated with liquid fuel and a reformer arranged upstream of the fuel cell stack for processing the fuel, a recirculation line for at least partial recycling of the fuel
- Anode exhaust gas in the reformer and means for supplying the liquid fuel into the anode exhaust gas. Furthermore, the invention relates to a
- Evaporation unit for producing a reactant gas from a hot
- Carrier gas for example, anode exhaust gas, and a liquid fuel for operating a high-temperature fuel cell stack with upstream
- auxiliary power unit can be used, for example, in motor vehicles, where it serves to provide electrical and thermal energy.
- a power generation unit with at least one high-temperature fuel cell is known in which a
- Hydrocarbon fuel such as gasoline
- a reformer for the liquid fuel is connected upstream.
- Part of the hot anode exhaust gas is transferred to the anode circuit via an anode recirculation recycled, wherein the liquid fuel is sprayed or injected upstream of an upstream of the reformer anode blower.
- an atomizer is provided with which liquid fuel is introduced via an injector. Also for this device, the disadvantages mentioned in AT 502,131 Bl apply.
- the object of the invention is to develop a power generation unit of the type mentioned in such a way that a compact unit, especially for use in an APU is given, with improvements in the accurate metering of the liquid fuel and a homogenization of the educt gas should be achieved even in partial load operation ,
- the means for supplying the fuel is designed as an evaporation device, with a housing which has a Verdampfervlies in the fuel supply line, which can be acted upon by the hot anode exhaust gas from the recirculation line.
- the evaporation unit is the liquid diesel fuel or another
- Hydrocarbon in a hot carrier gas preferably the recirculated
- Fuel / gas mixture which can be supplied as educt gas a reformer, for example, a SOFC system.
- the housing of the evaporation unit is designed substantially cylindrical and has on one side a central supply line for the fuel and on the opposite side a central gas outlet for the educt gas. Furthermore, the housing of the evaporation unit has a preferably tangentially opening gas inlet for the anode exhaust gas. Due to the tangential junction, a swirl flow in the housing of the
- the housing of the evaporation unit may preferably be in an exhaust gas chamber of the
- Energy generation unit may be arranged, in which exhaust gas chamber hot exhaust gases of the fuel cell stack and / or the starter burner
- the evaporation unit has a substantially cylindrical housing having on one side a central supply line for the fuel and an evaporator fleece and on the opposite side with a central gas outlet for the Equipped with educt gas, wherein a preferably tangentially opening gas inlet is provided for the hot carrier gas.
- Reformer catalyst arranged gas distributor housing (Reformermanifold) have an annular space in which the supply line for the reprocessed fuel / - gas mixture opens, starting from the annular space radial
- Access openings are arranged from the annular space to the inlet surface of the reforming catalyst.
- the evaporation unit can have a heating element associated with the evaporator fleece, preferably an electrically heatable glow plug.
- FIG. 1 shows the energy generating unit according to the invention in a schematic overview including installation position of the evaporation unit
- FIG. 2 is a sectional view of the evaporation unit according to the invention in the exhaust gas chamber of a power generation unit
- 3 is a three-dimensional representation of the power generation unit of FIG. 2
- Fig. 4 shows a variant of the evaporation unit according to the invention in a sectional view, as well
- the power generation unit has a high-temperature fuel cell stack 10 (for example SOFC) with an anode side A and a cathode side K, on the anode side via a recirculation line 13, a reformer 11 is connected upstream, which serves for the treatment of the liquid fuel, such as diesel.
- the fuel F is supplied by means of fuel pump 12 to an evaporation unit 20 and into the anode exhaust gas from the
- Recirculation line 13 introduced or metered, and together with the necessary oxidant, for example, air L, fed to the reformer 11 by means of compressor 14.
- the fuel F can be supplied by means of a fuel pump 15 to a starter burner 16, whose exhaust gases are conducted into an oxidation catalytic converter or afterburner 17 and heat up the catalyst of the reformer 11.
- the compressor 18 serves to supply the oxidizing agent (e.g., air L) to the cathode side K of the fuel cell stack 10, the oxidizing agent being passed through a heat exchanger 19 which is exhausted from the exhaust gases of the oxidizing agent (e.g., air L) to the cathode side K of the fuel cell stack 10, the oxidizing agent being passed through a heat exchanger 19 which is exhausted from the exhaust gases of the oxidizing agent (e.g., air L) to the cathode side K of the fuel cell stack 10, the oxidizing agent being passed through a heat exchanger 19 which is exhausted from the exhaust gases of the oxidizing agent (e.g., air L) to the cathode side K of the fuel cell stack 10, the oxidizing agent being passed through a heat exchanger 19 which is exhausted from the exhaust gases of the oxidizing agent (e.g., air L) to the cathode side K of the fuel cell stack 10, the oxidizing agent being passed through a heat exchanger 19 which is exhausted from the exhaust
- Oxidation catalyst 17 is subjected to waste heat. In the starting phase and the starter burner 16 is supplied via the compressor 18 with the required air L.
- the evaporation device 20 has a housing 21, which has an evaporator fleece 23 in the area of the fuel feed line 22, which rapidly absorbs the fuel and distributes it to a large surface area.
- the evaporator fleece 23 is acted upon by the hot anode exhaust gas from the recirculation line 13, so that the fuel evaporates.
- the housing 21 of the evaporation unit 20 is cylindrical, for example, with a top side having a central supply line 22 for the fuel and directly adjacent to it
- Evaporator nonwoven 23 and the opposite top side a central gas outlet 24 for the reactant gas, consisting of anode exhaust gas and vaporized fuel having.
- the tangentially opening gas inlet 25 for the reactant gas consisting of anode exhaust gas and vaporized fuel having.
- Anode exhaust provides a swirl flow inside the evaporator housing.
- the evaporator fleece 23 consists of a flat, preferably disc-shaped metal or ceramic fleece, which also withstands high temperatures in the range of 250 ° C. to 600 ° C. during operation of the energy generation unit, the higher temperatures being achieved, above all, during starting operation of the energy generation unit.
- the housing 21 of the evaporation unit 20 is arranged in FIG. 2 in an exhaust chamber 26 of the energy production unit, which exhaust chamber 26 collects hot exhaust gases of the fuel cell stack (not shown here) and of the starter burner 16 and via an outlet 29 to the heat exchanger 19 (see FIG. 1). supplies.
- exhaust chamber 26 collects hot exhaust gases of the fuel cell stack (not shown here) and of the starter burner 16 and via an outlet 29 to the heat exchanger 19 (see FIG. 1). supplies.
- Parting plane between the hot interior and the cold outside of the device is indicated by dash-dotted lines, wherein the housing 21 of the
- Evaporation unit 20 for example, as a cylindrical sheet metal construction
- the housing 21 may also be conical or frusto-conical in shape or have another aerodynamically optimized shape in order to increase the evaporation rate of the unit 20.
- the top surface of the housing 21 may be formed in the region of the evaporator fleece 23 through the wall 27 of the exhaust chamber 26.
- FIG. 3 shows the cutaway, three-dimensional representation of FIG. 3
- Evaporation unit 20 in the disassembled state, wherein a support ring 30 for supporting the evaporator nonwoven 23 is visible.
- the embodiment according to FIG. 4 shows an evaporation unit 20, in which an additional heater is formed.
- the evaporation unit 20 a heating element associated with the evaporator fleece 23, preferably an electrically heatable glow plug 28, on. It is also possible above and / or below the evaporator fleece 23 to arrange an electric heating mat or heating coil. Such an evaporation unit can also outside the
- Abhaust chamber 26 are arranged and brought to operating temperature quickly.
- FIG. 5 shows the preferred arrangement of the evaporation unit 20 in the exhaust gas chamber 26, into which the hot exhaust gases leaving the oxidation catalytic converter 17 through the openings 31 enter and heat the housing 21 of the evaporation unit 20.
- Oxidation catalyst 17 serves as an afterburner for also in the
- Exhaust chamber 26 arranged starter burner 16 and the exhaust gases of the
- the upper cover surface of the housing 21 is formed by the wall 27 of the exhaust chamber 26, whereby the fuel supply to the evaporation unit 20 can be advantageously arranged in the cooler outer area (outside the exhaust chamber 26).
- the fuel / gas mixture (educt gas) produced in the evaporation unit 20 is led out of the waste gas chamber 26 via the gas outlet line 24 and, after the metered addition of air L, is fed to the compressor 14 arranged in the cooler outer area. After compression, the educt gas passes through a supply line 32, which dips back into the hot exhaust gas chamber 26, in the reformer eleventh
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US14/765,616 US10374242B2 (en) | 2013-02-04 | 2014-02-04 | Energy generating unit comprising a high-temperature fuel cell stack and a vaporizing unit |
JP2015555614A JP6532827B2 (ja) | 2013-02-04 | 2014-02-04 | 高温燃料電池スタック及び蒸発装置を有するエネルギー生成装置 |
DE112014000671.8T DE112014000671A5 (de) | 2013-02-04 | 2014-02-04 | Energieerzeugungseinheit mit einem Hochtemperatur-Brennstoffzellenstack und einer Verdampfungseinheit |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ATA84/2013 | 2013-02-04 | ||
ATA84/2013A AT513912B1 (de) | 2013-02-04 | 2013-02-04 | Energieerzeugungseinheit mit einem Hochtemperatur-Brennstoffzellenstack und einer Verdampfungseinheit |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2014117949A1 true WO2014117949A1 (de) | 2014-08-07 |
WO2014117949A8 WO2014117949A8 (de) | 2014-10-09 |
Family
ID=50073142
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2014/000285 WO2014117949A1 (de) | 2013-02-04 | 2014-02-04 | Energieerzeugungseinheit mit einem hochtemperatur-brennstoffzellenstack und einer verdampfungseinheit |
Country Status (5)
Country | Link |
---|---|
US (1) | US10374242B2 (de) |
JP (1) | JP6532827B2 (de) |
AT (1) | AT513912B1 (de) |
DE (1) | DE112014000671A5 (de) |
WO (1) | WO2014117949A1 (de) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3753060B1 (de) * | 2018-02-16 | 2024-01-03 | Fischer Eco Solutions GmbH | Brennstoffzellensystem und verfahren zu dessen betrieb |
US11802312B2 (en) | 2020-08-10 | 2023-10-31 | Dimension Genomics Inc. | Devices and methods for multi-dimensional genome analysis |
Citations (2)
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DE102007018311A1 (de) * | 2007-04-18 | 2008-10-23 | Enerday Gmbh | Zweistufiger Reformer und Verfahren zum Betreiben eines Reformers |
DE102011107669A1 (de) * | 2011-07-12 | 2013-01-17 | J. Eberspächer GmbH & Co. KG | Kraftstoffbehandlungsvorrichtung |
Family Cites Families (24)
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DE4446841A1 (de) | 1994-12-27 | 1996-07-04 | Mtu Friedrichshafen Gmbh | Brennstoffzellenmodul |
US6033793A (en) | 1996-11-01 | 2000-03-07 | Hydrogen Burner Technology, Inc. | Integrated power module |
JP3614110B2 (ja) | 2001-02-21 | 2005-01-26 | 日産自動車株式会社 | 燃料電池システム |
US20030234455A1 (en) * | 2002-06-24 | 2003-12-25 | Mieney Harry R. | Non-contacting fuel vaporizer |
US7279246B2 (en) | 2002-06-24 | 2007-10-09 | Delphi Technologies, Inc. | Solid-oxide fuel cell system having an integrated air/fuel manifold |
US7422812B2 (en) | 2002-06-24 | 2008-09-09 | Delphi Technologies, Inc. | Solid-oxide fuel cell system having a thermally-regulated cathode air heat exchanger |
DE10243275A1 (de) * | 2002-09-18 | 2004-04-01 | Volkswagen Ag | Reformereinrichtung für ein Brennstoffzellensystem und Verfahren zum Erzeugen von Wasserstoff durch Reformieren eines Betriebsmediums |
DE10348637A1 (de) | 2003-10-15 | 2005-05-25 | J. Eberspächer GmbH & Co. KG | Verdampferanordnung zur Erzeugung eines in einem Reformer zur Wasserstoffgewinnung zersetzbaren Kohlenwasserstoff/Luft- oder/und Wasserdampf-Gemisches und Verfahren zum Betreiben einer derartigen Verdampferanordnung |
US20050188616A1 (en) | 2004-02-27 | 2005-09-01 | Bizjak Travis A. | Fuel processing treatment system and fuel processing systems containing the same |
KR100529079B1 (ko) | 2004-03-25 | 2005-11-15 | 삼성에스디아이 주식회사 | 연료 전지 시스템 |
DE102004055425B4 (de) | 2004-11-17 | 2007-06-14 | Forschungszentrum Jülich GmbH | Mischkammer für einen Reformer sowie Verfahren zum Betreiben derselben |
JP4899521B2 (ja) | 2006-02-17 | 2012-03-21 | 独立行政法人産業技術総合研究所 | 燃料電池システム |
JP5021238B2 (ja) | 2006-05-18 | 2012-09-05 | 本田技研工業株式会社 | 燃料電池システム |
DE102006028699B4 (de) | 2006-06-22 | 2017-04-06 | Eberspächer Climate Control Systems GmbH & Co. KG | Verfahren zum Betreiben eines Reformersystems |
AT502131B1 (de) | 2006-10-03 | 2008-02-15 | Avl List Gmbh | Energieerzeugungseinheit mit zumindest einer hochtemperaturbrennstoffzelle |
US7736399B2 (en) * | 2006-11-07 | 2010-06-15 | Delphi Technologies, Inc. | Electrically-heated metal vaporizer for fuel/air preparation in a hydrocarbon reformer assembly |
DE102008018152B4 (de) * | 2008-04-10 | 2019-03-07 | Eberspächer Climate Control Systems GmbH & Co. KG | Brennstoffzellensystem und zugehöriges Betriebsverfahren |
DE102009013598A1 (de) * | 2008-09-19 | 2010-03-25 | Mtu Onsite Energy Gmbh | Brennstoffzellenanordnung mit verbessertem katalytischen Brenner |
JP4692938B2 (ja) | 2009-05-28 | 2011-06-01 | Toto株式会社 | 固体電解質型燃料電池 |
US20110026903A1 (en) * | 2009-07-31 | 2011-02-03 | Verizon Patent And Licensing Inc. | Recording device |
JP5439266B2 (ja) | 2010-04-21 | 2014-03-12 | 本田技研工業株式会社 | 燃料電池システム |
US20110269032A1 (en) | 2010-12-10 | 2011-11-03 | Delphi Technologies, Inc. | Combustor for a fuel cell system |
US20130015301A1 (en) * | 2011-07-12 | 2013-01-17 | Radim Zvak | Apparatis for securing and stabilizing an elevated pipe |
TW201328010A (zh) * | 2011-12-16 | 2013-07-01 | Univ Nat Cheng Kung | 用於熱光電系統之燃燒裝置 |
-
2013
- 2013-02-04 AT ATA84/2013A patent/AT513912B1/de not_active IP Right Cessation
-
2014
- 2014-02-04 US US14/765,616 patent/US10374242B2/en not_active Expired - Fee Related
- 2014-02-04 WO PCT/EP2014/000285 patent/WO2014117949A1/de active Application Filing
- 2014-02-04 JP JP2015555614A patent/JP6532827B2/ja not_active Expired - Fee Related
- 2014-02-04 DE DE112014000671.8T patent/DE112014000671A5/de not_active Withdrawn
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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DE102007018311A1 (de) * | 2007-04-18 | 2008-10-23 | Enerday Gmbh | Zweistufiger Reformer und Verfahren zum Betreiben eines Reformers |
DE102011107669A1 (de) * | 2011-07-12 | 2013-01-17 | J. Eberspächer GmbH & Co. KG | Kraftstoffbehandlungsvorrichtung |
Also Published As
Publication number | Publication date |
---|---|
DE112014000671A5 (de) | 2015-10-29 |
AT513912B1 (de) | 2016-08-15 |
US20160006062A1 (en) | 2016-01-07 |
AT513912A1 (de) | 2014-08-15 |
JP2016507132A (ja) | 2016-03-07 |
WO2014117949A8 (de) | 2014-10-09 |
US10374242B2 (en) | 2019-08-06 |
JP6532827B2 (ja) | 2019-06-19 |
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