WO2014117952A1 - Brennstoffzellensystem, welches mit kohlenwasserstoffen betreibbar ist - Google Patents
Brennstoffzellensystem, welches mit kohlenwasserstoffen betreibbar ist Download PDFInfo
- Publication number
- WO2014117952A1 WO2014117952A1 PCT/EP2014/000290 EP2014000290W WO2014117952A1 WO 2014117952 A1 WO2014117952 A1 WO 2014117952A1 EP 2014000290 W EP2014000290 W EP 2014000290W WO 2014117952 A1 WO2014117952 A1 WO 2014117952A1
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- WO
- WIPO (PCT)
- Prior art keywords
- functional unit
- power generation
- unit
- generation unit
- functional
- Prior art date
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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
- H01M8/0625—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
- H01M8/0631—Reactor construction specially adapted for combination reactor/fuel cell
-
- 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
-
- 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
-
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
-
- 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
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells
Definitions
- Fuel cell system which is operable with hydrocarbons
- the invention relates to a power generation unit, in particular for use in a vehicle containing hydrocarbons such as diesel and the like
- Such a power generation unit can be used, for example, in a motor vehicle as a compact and efficient energy source, in particular for the provision of electrical and / or thermal energy.
- Multimedia technology such as radio, television and related
- Receiving devices as well as to provide light.
- Hydrocarbons such as diesel or gasoline which are readily available in a truck, can not be processed directly by common fuel cell types.
- Hydrocarbons are first reformed to be processed by fuel cells process gases and only then processed by a fuel cell. However, these systems require a lot to reform the hydrocarbons
- DE 10 2007 039 594 A1 therefore discloses, on the one hand, the reformer and further elements which are necessary for reforming, and to arrange the stack of fuel cells in a compact construction in a common external insulation.
- this document proposes to recycle anode exhaust gas into the reformer in order to utilize the heat energy contained in the exhaust gas and to use the chemical substances contained therein for reforming.
- To the supply of such a system and for reforming the provision and preparation of a number of starting materials is needed. This requires a variety of ancillaries.
- the object of the present invention is a fuel cell system
- autonomous unit can be sold.
- a vehicle according to the invention is any type of land vehicle
- a fuel cell according to the invention is a galvanic cell, which converts the chemical reaction energy of a continuously supplied fuel and an oxidizing agent into electrical energy.
- a galvanic cell which converts the chemical reaction energy of a continuously supplied fuel and an oxidizing agent into electrical energy.
- usually several cells are stacked (engl., For
- Devices in the sense of the invention are elements which serve to carry out a sub-process of the power generation unit
- a media supply within the meaning of the invention is a provision of substances or substance mixtures which are required for the overall process of energy production.
- a reforming in the context of the invention is any kind of reforming or
- Reforming for the production of a synthesis gas which is at least hydrogen contains, in particular steam reforming or reforming, partial oxidation (CPOX) and / or autothermal reforming.
- a reformer according to the invention accordingly a device for reforming.
- Arranged in the sense of the invention means that at least two elements are held in a defined position to each other.
- One behind the other in the sense of the invention means arranged in order, each having two consecutively arranged elements have a direct connection and / or contact surface.
- a longitudinal axis in the sense of the invention is that axis of a body that corresponds to the direction of its greatest extent.
- a process temperature within the meaning of the invention is the temperature which is achieved in a device during execution of a respective sub-process in normal operation.
- Damping means according to the invention are any means which are suitable for damping a vibration and / or a force pulse.
- a frame plate according to the invention is any type of two-dimensional structure which is suitable for receiving forces.
- a fixation plate according to the invention is any type of two-dimensional structure that is suitable for receiving or fastening devices.
- a flexible fastening tab according to the invention is any type of means which are suitable for attachment and damp vibrations or pulses and / or compensate for thermal expansion or shrinkage.
- An insulation according to the invention is any type of thermal insulation to reduce the passage of heat energy.
- Autothermic in the sense of the invention means that in the overall process of the power generation unit, both exothermic and endothermic reactions take place in parallel, so that the overall process is substantially independent of external heat supply is.
- Adiabatic in the sense of the invention means that in the overall process of the power generation unit, both exothermic and endothermic reactions take place in parallel, so that the overall process in the
- Hydrocarbon-containing energy is converted into electrical energy.
- a housing according to the invention is any type of shell that protects the contents from contamination and / or external forces.
- the power generation unit By dividing the power generation unit into three functional units, the power generation unit is structured in a particularly simple manner and the respective elements are easily accessible for repair in the event of a malfunction, since devices which require similar operating temperatures are each combined in one functional unit. If there is an error in a functional unit, it can be done by removing the isolation of this functional unit
- the three functional units are in
- the result is a particularly compact arrangement with respect to the space requirements of the power generation unit.
- the "symmetrical" arrangement along the longitudinal axis of the starting burner, the afterburner and the reformer promotes the uniform conversion of the respective process gases in the afterburner.
- the process temperature of the devices of the power generation unit increases substantially from the first functional unit via the third functional unit to the second functional unit.
- this arrangement has the advantage that the air in its flow direction in the first functional unit initially compressed, then heated by the high process temperature in the fuel cell and finally on arrival in the second functional unit has the highest possible temperature for reforming to promote the combustion in the afterburner or the reforming.
- the fuel which is conveyed in the first functional unit evaporated in the second functional unit and processed to a hot process gas for reforming and as reformate in the third functional unit of the fuel cell at high temperatures with the air or the oxygen Reaction is brought.
- the isolation of the respective functional unit can be dimensioned accordingly. Further advantageously, the devices can each be arranged in that functional unit which has no damaging thermal effects on the respective device.
- the supporting structure is one
- the power generator can be further attached to a vehicle.
- Fastening means in particular for mounting on a vehicle, on.
- Power generation unit particularly easy at the respective application site assemble.
- the supporting structure holds the power generating unit in a defined position. An attachment of the individual facilities of the
- Damping means which are arranged in particular when used in the vehicle between the supporting structure and the vehicle.
- the damping means ensure that vibrations, for example when used in a vehicle, act only damped on the power generation unit. For example, immediate transmission of the vibrations could affect the function of the reformer by discontinuously providing media.
- a first fixing plate between the first and the second functional unit, a second fixing plate, in particular for fixing devices of the first and / or the second functional unit, and / or between the second and the third functional unit further arranged a third fixing plate.
- the third fixing plate as an adapter plate, consisting of upper and lower plate (14b), formed and connects the devices of the second functional unit thermally and / or fluid-communicating with the fuel cell.
- the third fixing plate is formed as an adapter plate or distributor plate, which carries out the distribution of the process gas, the air and the respective exhaust air of the fuels, a complicated and space-consuming distribution of gases through pipes can be avoided.
- the formation of the adapter plate in top and bottom plate allows by removing the bottom plate cleaning the distribution channels in the adapter or distributor plate. Furthermore, a
- Reformer catalyst after removing the lower plate optionally
- first fixing plate, the second fixing plate and / or the third fixing plate are connected to at least one flexible fastening tab with the supporting structure. Due to the flexible fastening strap thermal deformations of the individual devices can be compensated. Furthermore, the flexible fastening strap thermal deformations of the individual devices can be compensated. Furthermore, the flexible fastening strap thermal deformations of the individual devices can be compensated. Furthermore, the flexible fastening strap thermal deformations of the individual devices can be compensated. Furthermore, the
- Mounting tab have a dampening function.
- the power generation unit has an insulation, by which the power generation unit is substantially adiabatic and which in particular has three isolation areas corresponding to the functional units.
- the power generation unit has a housing, which consists in particular of housing parts, which each cover substantially one of the three functional units and which are individually disassembled.
- the housing prevents the entry of contaminants in the
- each functional unit is covered by a housing part, which are each individually disassembled. In this way, repair work in a functional area or at facilities of a functional area without disassembly of the other housing parts can be made.
- At least one device for media supply such as a blower or compressor, a valve and / or a coal hydrogen pump outside the housing and / or the insulation
- Some of the media supply facilities are sensitive to high temperatures. This is because the devices are, for example, partially equipped with ball bearings or also have controls that are not readily temperature resistant. An arrangement outside the insulation can therefore individual devices in a functional unit of the in the
- Function unit exclude prevailing temperature.
- the housing at least partially forms the supporting structure.
- a frame can be dispensed with.
- a frame can be dispensed with.
- FIG. 1 shows a partially schematic process diagram of an embodiment of the power generation unit according to the invention.
- FIG. 2 shows a partially schematic cross-section of an embodiment of the power generation unit according to the invention.
- Figure 3 shows a partially schematic perspective top view of a
- Embodiment of the power generation unit according to the invention with partially removed housing and partially removed and / or shown in cross-section insulation.
- FIG. 4 shows a further partially schematic perspective top view of an embodiment of the power generation unit according to the invention with a housing partially removed and insulation partially removed and / or shown in cross section.
- FIG. 5 shows a further partially schematic perspective external view of an embodiment of the closed-housing power generation unit according to the invention.
- Hydrocarbon pumps 21a and 21b hydrocarbons, preferably diesel, in pumped the power generator. In the starting phase this takes place
- the power generation unit 1 is preferably supplied with air, which is preferably filtered.
- the starting burner 24 is open during the starting phase, whereas a preferably existing valve 34 is closed to supply the reformer 28 with air in the starting phase.
- the air and hydrocarbons are preferably heated in the starting burner 24 and ignited.
- the starting burner 24 heats the combustion chamber 32 of the preferably arranged around the reformer 28
- Throttle is, if this is not already open, open so that air can flow to the cathode K of the fuel cell 2 and is heated in the heat exchanger 30.
- the preferably present reformer air valve 34 is opened and air is conveyed with the recirculation fan 18 in the reformer 28, where it is heated by the exhaust gas of the starting burner 24 and then through the preferably present third fixing plate or adapter plate 14 to the anode A of the fuel cell 2 is headed.
- anode exhaust gas flows via the preferably present and now open recirculation valve 20 into the evaporator 25.
- hydrocarbons are also pumped via the hydrocarbon pump 21a to the evaporator, which flows through the heated anode exhaust gas in the evaporator
- This gas mixture is preferably mixed with air in the
- This reformate is in turn passed via the third fixing plate or adapter plate 14 to the anode of the fuel cell 2, where now the implementation of substantially hydrogen and oxygen to water and electrical energy.
- the electrical energy is preferably dissipated via the electrical connection 5 to a consumer. During the implementation, heat energy is released.
- the heated cathode exhaust air is passed into the combustion chamber 32 of the afterburner 27.
- a portion of the heated anode exhaust gas is preferably returned to the evaporator 25.
- Another part of the anode exhaust gas is passed through the preferably existing, now open burner anode exhaust valve 35 into the combustion chamber 32 of the afterburner 27.
- Anode exhaust gas mixed with the cathode exhaust air and preferably reacted by means of a catalyst in an exothermic reaction On the one hand, the heat energy released here serves to heat or insulate the reformer 28 and, on the other hand, improves the heat distribution in the reformer 28.
- the starting burner 24 can preferably now be switched off. Heat losses and the energy to activate the autothermal reaction in the reformer 28 or a preferably present reformer catalyst are balanced by the heat of the exothermic reaction in the fuel cell 2 and the exothermic reaction in the afterburner 27, so that the overall system is substantially adiabatic.
- a bypass line (not shown) may be preferably provided from the starting burner 24 directly into the heat exchanger 30.
- a bypass line (not shown) may be preferably provided from the starting burner 24 directly into the heat exchanger 30.
- more thermal power can be provided regardless of the required electrical power. This is particularly advantageous in those applications in which the fuel cell 2 is exposed to extremely cold temperatures and / or the vehicle requires a lot of heat to heat or cool the interior.
- the devices of the power generation unit 1 shown on the process picture in FIG. 1 can be essentially divided into three
- a first functional unit 7 for media supply preferably has the air blower 17, the recirculation blower 18, the starting burner air valve 19, the preferably present recirculation valve 20, the hydrocarbon pumps 21a and 21b, the heat exchanger 30, the cathode air valve 33 and / or the reformer air valve 34.
- the starting burner 24 is at least partially in the first
- Functional unit 7 arranged and / or a common component of the first and second functional units 7, eighth
- the power generation unit 1 is essentially replaced by the first functional unit 7 with the media air and
- Energy generation process are supplied. Preferably, these are processed in the first functional unit 7 and then provided to the devices of the second functional unit 8 and / or the third functional unit 9.
- a second functional unit 8 preferably has the afterburner 27 with the combustion chamber 32, the reformer 28, the evaporator 25, an exhaust chamber 26 (not shown in FIG. 1) and / or the afterburner anode exhaust valve 35.
- the starting burner 24 is at least partially part of the second functional unit 8 and / or a common component of the first and second functional units 7, eighth
- the reformate is converted from the reformer 28 into a third functional unit 9
- a plurality of fuel cells 2 for example in a Stack or stack to be present in the functional unit 9, or more preferably also several stacks.
- the devices of the functional units 7, 8 and 9 are preferably arranged in the manner in the respective functional units 7, 8 and 9, that the
- Process temperature increases substantially from the first functional unit 7 via the third functional unit 9 to the second functional unit 8.
- temperatures from ambient to 450 ° C. preferably from ambient to 300 ° C., more preferably from ambient to 200 ° C., more preferably from ambient to 100 ° C., and most preferably from ambient to 60 ° C.
- temperatures are preferably substantially from 200 ° C to 1000 ° C, preferably from 300 ° C to 800 ° C, more preferably from 400 ° C to 700 ° C, more preferably 450 ° C to 650 ° C.
- temperatures of 550 ° C to 850 ° C preferably from 600 ° C to 800 ° C, more preferably from 650 ° C to 750 ° C and most preferably 700 ° C. These temperatures are achieved in particular in the retracted operating state of the power generation unit 1.
- the three functional units 7, 8, 9 are preferably substantially spatially separated. Preferably, these are also, as shown in the process picture of Figure 1, arranged one behind the other.
- the three functional units 7, 8 and 9 are arranged one behind the other with respect to the flow direction of the conveyed through the air blower 17 into the system air. This has the advantage that the air is successively warmed up on its way through the three functional units 7, 8, 9 to the fuel cell 2 in order to bring and / or maintain the fuel cell at operating temperature.
- Fig. 2 shows the structure of an embodiment of an inventive
- the power generation unit 1 is divided into three functional units 7, 8, 9.
- the first functional unit 7 has in the first instance devices that are used for media supply and / or for
- Preparation of the media for the power generation unit 1 is arranged.
- a heat exchanger 30 is present, which heats the sucked air before it is the cathode K of the fuel cell 2 is supplied.
- a compression and mixing of different media can be in the first
- Function unit 7 preferably done.
- the starting burner 24 is at least partially disposed in the first functional unit 7, as shown in the embodiment of Figure 2.
- the starting burner 24 is used in particular to the
- the elements for generating the flame are in this case preferably arranged in the first functional unit 7, for.
- the starting burner tube 29 then preferably projects into the first functional unit 7, for.
- the starting burner 24 completely in the second functional unit 8.
- the heat exchanger 30 completely in the second functional unit 8.
- the second functional unit 8 essentially comprises the devices for
- the reformer is preferably arranged in the combustion chamber 32 of the afterburner 27.
- the afterburner 27 is again preferably arranged in an exhaust gas chamber 26, in which the exhaust gas of the afterburner 27 and / or the exhaust gas of the starting burner 24 is conducted to the heat exchanger 30.
- the evaporator 25 is arranged, which hydrocarbons in the recirculated from the fuel cell 2
- Anode exhaust gas evaporates before it is introduced into the reformer 28.
- the starting burner 24 and / or the afterburner 27 serve to heat the reformer 28.
- the exhaust chamber 26 in turn heats the outer wall of the
- the reformate or process gas for the anode A and the air for the cathode K of the fuel cell 2 are finally via the third fixing plate 14 and adapter plate, which preferably consists of a top plate 14a and a bottom plate 14b, in the third functional unit 9 to the respective Conducted connections.
- the cathode exhaust air and the anode exhaust gas from the fuel cell 2 are preferably connected via the third fixing plate 14 and adapter plate to the respective terminals of the second functional unit 8.
- the reformer 28 preferably has a reforming catalyst 37 and the afterburner 27 has an afterburner catalyst 38.
- the second functional unit 8 has means which require a higher operating temperature to fulfill their respective function than those of the first functional unit 7.
- the temperature in the entire second functional unit 8 is maintained at a higher level than that in FIG the first functional unit 7.
- the third functional unit 9 has two fuel cell stacks 2 in the illustrated embodiment.
- the fixation of these two fuel cell stacks 2 and / or the distribution of the process gas and the other media or removal of the cathode exhaust air and the anode exhaust gas is preferably carried out via a distributor plate 36, which is connected to the third fixing plate or adapter plate 14.
- a fuel cell 2 with a stack or a fuel cell with more than two stacks can also be used.
- the fuel cell 2 is preferably an SOFC fuel cell, but others may be
- Fuel cell types are used, such.
- the power generation unit 1 is preferably surrounded by an insulation 16, which is not shown in FIG. Figure 3 shows a partially schematic perspective view of the power generation unit 1 in a further embodiment. in the
- this embodiment differs from that of FIG. 1 in that the fuel cell 2 has only one stack.
- the individual embodiments of this and the previous embodiment can be easily combined.
- Functional unit 8 and the third frame plate 12 for the separation between the second functional unit 8 and the third functional unit 9 define.
- the energy-generating unit 1 is preferably surrounded by an insulation 16.
- the isolation prevents one
- the insulation 16 insulation plates which can be adapted for example by milling to the shape of the respective functional unit 7, 8, 9. Further
- the insulation 16 can be realized with a foam.
- the space between the housing and the facilities of the insulation 16 can be realized with a foam.
- Energy generating unit 1 is foamed in this case.
- the use of this foam for insulation of the power generation unit according to the invention is expressly provided.
- the insulation 16 is preferably divided into three regions 16a, 16b, 16c, each of which isolates a functional region 7, 8, 9. This allows the
- Isolation areas 16a, 16b, 16c are removed individually to get to the device of the respective functional unit 7, 8, 9, without others
- the power generation unit 1 is at least partially surrounded by a housing 15.
- This housing 15 is again preferably made of housing parts 15a, 15b, 15c, which each cover the functional unit 7, 8, 9 individually.
- the housing 15 consists of several
- Shells or layers which consist in particular of a metal and / or plastic.
- the housing thus protects the power generation unit 1 from the Penetration of impurities and / or mechanical influences from outside.
- Devices which need not or should not be insulated from the environment or in which a heat energy exchange with the environment is even intended, are preferably outside the housing 15 or the insulation 16
- these are, for example, the hydrocarbon pumps 21a, 21b and the valves 19, 20, 34 and the throttle / valve 33 (not shown).
- the power generation unit 1 preferably has a supporting structure on which the devices of the functional units 7, 8, 9 are arranged.
- the supporting structure may in this case preferably be formed by a frame 6 or also the housing 15 may be formed as a self-supporting housing 15.
- the supporting structure 6, 15 consists of both frame parts and housing parts.
- the frame 6 as well as the housing 15 may in this case consist of metal, plastic or fiber composite materials.
- the frame and the housing 15 are bolted together, but any other known type of connection is also possible.
- the power generation unit 1 preferably further elements:
- the frame 6 by a first
- Frame plate 10, a second frame plate 11 and / or a third frame plate 12 are reinforced. Furthermore, a first fixing plate 23, a second fixing plate 13 and a third fixing plate 14 may be provided, which are preferably connected via fastening tabs 22 respectively to the first frame plate 10, the second frame plate 11 and / or the third frame plate 12 to the fixing plates in a defined position. Further preferably, the fastening tabs 22 are made of a flexible material, so that thermal expansions of the entire structure can be compensated. Furthermore, the fastening tabs 22 may have a vibration-damping function. On the fixing plates 13, 14, 23 and / or on the frame plates 10, 11, 12 are then preferably substantially all the facilities of
- FIG. 4 shows the embodiment according to FIG. 3 in a partially schematic perspective view, wherein the energy generating unit 1 is rotated 180 ° about the longitudinal axis L in relation to FIG.
- the further view shows the air blower 17 and the recirculation blower 18, which are preferably also arranged outside the housing 15 and the insulation 16.
- the first frame plate 10 is visible to which some of the devices of the first functional unit 7 are preferably attached.
- the frame 6 preferably has additional frame elements 6, which form a plane on the outside of the housing 15, so that the power generation unit 1 can be mounted, for example, on a vehicle. For mounting can on these
- Frame parts preferably be arranged damping means which damp vibrations of the vehicle to the power generation unit 1 out. Also visible are the heat exchanger 30 and parts of the fixing plate 13.
- FIG. 5 shows the power generation unit 1 with the housing 15 completely closed, wherein all the housing parts 15a, 15b, 15c on the
- Power generating unit 1 are mounted. Again, the view is partially schematic and perspective, and the power generating unit 1 is once again aligned as in FIG.
- the housing parts 15a, 15b, 15c are preferably screwed, in particular with the frame 6.
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- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
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Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2015555615A JP2016505200A (ja) | 2013-02-04 | 2014-02-04 | 炭化水素で動作可能な燃料電池システム |
US14/765,605 US9917318B2 (en) | 2013-02-04 | 2014-02-04 | Hydrocarbon-operable fuel cell system |
DE112014000665.3T DE112014000665A5 (de) | 2013-02-04 | 2014-02-04 | Brennstoffzellensystem, welches mit Kohlenwasserstoffen betreibbar ist |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ATA82/2013 | 2013-02-04 | ||
ATA82/2013A AT513913B1 (de) | 2013-02-04 | 2013-02-04 | Brennstoffzellensystem, welches mit Kohlenwasserstoffen betreibbar ist |
Publications (1)
Publication Number | Publication Date |
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WO2014117952A1 true WO2014117952A1 (de) | 2014-08-07 |
Family
ID=50115800
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2014/000290 WO2014117952A1 (de) | 2013-02-04 | 2014-02-04 | Brennstoffzellensystem, welches mit kohlenwasserstoffen betreibbar ist |
Country Status (5)
Country | Link |
---|---|
US (1) | US9917318B2 (de) |
JP (1) | JP2016505200A (de) |
AT (1) | AT513913B1 (de) |
DE (1) | DE112014000665A5 (de) |
WO (1) | WO2014117952A1 (de) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018146172A1 (de) * | 2017-02-09 | 2018-08-16 | Avl List Gmbh | Startbrenner für ein brennstoffzellensystem |
AT521065A1 (de) * | 2018-03-19 | 2019-10-15 | Avl List Gmbh | Brennstoffzellensystem und Verfahren zum Aufheizen eines Brennstoffzellensystems |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102017203516A1 (de) | 2017-03-03 | 2018-09-06 | Thyssenkrupp Ag | Außenintegrierte Reformer-Steuereinheit für ein Unterseeboot |
WO2019239457A1 (ja) * | 2018-06-11 | 2019-12-19 | 日産自動車株式会社 | 固体酸化物形燃料電池を有する発電ユニット |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4446841A1 (de) * | 1994-12-27 | 1996-07-04 | Mtu Friedrichshafen Gmbh | Brennstoffzellenmodul |
WO1999044252A1 (en) * | 1998-02-27 | 1999-09-02 | Hydrogen Burner Technology, Inc. | Integrated power module |
EP1414092A1 (de) * | 2002-06-24 | 2004-04-28 | Delphi Technologies, Inc. | Feststoffoxidbrennstoffzelle mit integriertem Verteilsystem bzw. integrierter Sammelleitung für Luft/Brennstoff |
WO2007136080A1 (en) * | 2006-05-18 | 2007-11-29 | Honda Motor Co., Ltd. | Fuel cell system |
DE102007039594A1 (de) * | 2006-10-03 | 2008-04-10 | Avl List Gmbh | Energieerzeugungseinheit mit zumindest einer Hochtemperaturbrennstoffzelle |
US20110269032A1 (en) * | 2010-12-10 | 2011-11-03 | Delphi Technologies, Inc. | Combustor for a fuel cell system |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
US7422812B2 (en) * | 2002-06-24 | 2008-09-09 | Delphi Technologies, Inc. | Solid-oxide fuel cell system having a thermally-regulated cathode air heat exchanger |
US20030234455A1 (en) | 2002-06-24 | 2003-12-25 | Mieney Harry R. | Non-contacting fuel vaporizer |
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 |
DE102006028699B4 (de) | 2006-06-22 | 2017-04-06 | Eberspächer Climate Control Systems GmbH & Co. KG | Verfahren zum Betreiben eines Reformersystems |
US7736399B2 (en) | 2006-11-07 | 2010-06-15 | Delphi Technologies, Inc. | Electrically-heated metal vaporizer for fuel/air preparation in a hydrocarbon reformer assembly |
DE102007018311B4 (de) | 2007-04-18 | 2008-12-04 | Enerday Gmbh | Zweistufiger Reformer und Verfahren zum Betreiben eines Reformers |
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 |
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 |
DE102011107669B4 (de) | 2011-07-12 | 2022-02-10 | Eberspächer Climate Control Systems GmbH & Co. KG | Kraftstoffbehandlungsvorrichtung |
-
2013
- 2013-02-04 AT ATA82/2013A patent/AT513913B1/de not_active IP Right Cessation
-
2014
- 2014-02-04 DE DE112014000665.3T patent/DE112014000665A5/de not_active Ceased
- 2014-02-04 JP JP2015555615A patent/JP2016505200A/ja active Pending
- 2014-02-04 US US14/765,605 patent/US9917318B2/en active Active
- 2014-02-04 WO PCT/EP2014/000290 patent/WO2014117952A1/de active Application Filing
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4446841A1 (de) * | 1994-12-27 | 1996-07-04 | Mtu Friedrichshafen Gmbh | Brennstoffzellenmodul |
WO1999044252A1 (en) * | 1998-02-27 | 1999-09-02 | Hydrogen Burner Technology, Inc. | Integrated power module |
EP1414092A1 (de) * | 2002-06-24 | 2004-04-28 | Delphi Technologies, Inc. | Feststoffoxidbrennstoffzelle mit integriertem Verteilsystem bzw. integrierter Sammelleitung für Luft/Brennstoff |
WO2007136080A1 (en) * | 2006-05-18 | 2007-11-29 | Honda Motor Co., Ltd. | Fuel cell system |
DE102007039594A1 (de) * | 2006-10-03 | 2008-04-10 | Avl List Gmbh | Energieerzeugungseinheit mit zumindest einer Hochtemperaturbrennstoffzelle |
US20110269032A1 (en) * | 2010-12-10 | 2011-11-03 | Delphi Technologies, Inc. | Combustor for a fuel cell system |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018146172A1 (de) * | 2017-02-09 | 2018-08-16 | Avl List Gmbh | Startbrenner für ein brennstoffzellensystem |
US11233255B2 (en) | 2017-02-09 | 2022-01-25 | Avl List Gmbh | Starting burner for a fuel cell system |
AT521065A1 (de) * | 2018-03-19 | 2019-10-15 | Avl List Gmbh | Brennstoffzellensystem und Verfahren zum Aufheizen eines Brennstoffzellensystems |
AT521065B1 (de) * | 2018-03-19 | 2020-03-15 | Avl List Gmbh | Brennstoffzellensystem und Verfahren zum Aufheizen eines Brennstoffzellensystems |
Also Published As
Publication number | Publication date |
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DE112014000665A5 (de) | 2015-12-10 |
US9917318B2 (en) | 2018-03-13 |
AT513913A1 (de) | 2014-08-15 |
AT513913B1 (de) | 2016-12-15 |
US20160006064A1 (en) | 2016-01-07 |
JP2016505200A (ja) | 2016-02-18 |
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