EP3776706A1 - Fuel cell system - Google Patents
Fuel cell systemInfo
- Publication number
- EP3776706A1 EP3776706A1 EP19718267.8A EP19718267A EP3776706A1 EP 3776706 A1 EP3776706 A1 EP 3776706A1 EP 19718267 A EP19718267 A EP 19718267A EP 3776706 A1 EP3776706 A1 EP 3776706A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- compressor
- fuel cell
- cell system
- air
- ambient air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 155
- 239000003570 air Substances 0.000 claims abstract description 57
- 239000012080 ambient air Substances 0.000 claims abstract description 56
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 238000009423 ventilation Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 27
- 230000006835 compression Effects 0.000 description 15
- 238000007906 compression Methods 0.000 description 15
- 238000011161 development Methods 0.000 description 8
- 230000018109 developmental process Effects 0.000 description 8
- 238000001816 cooling Methods 0.000 description 6
- 238000005056 compaction Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04014—Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04111—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants using a compressor turbine assembly
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/65—Means for temperature control structurally associated with the cells
- H01M10/656—Means for temperature control structurally associated with the cells characterised by the type of heat-exchange fluid
- H01M10/6561—Gases
- H01M10/6563—Gases with forced flow, e.g. by blowers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/66—Heat-exchange relationships between the cells and other systems, e.g. central heating systems or fuel cells
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M16/00—Structural combinations of different types of electrochemical generators
- H01M16/003—Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers
- H01M16/006—Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers of fuel cells with rechargeable batteries
-
- 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
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04253—Means for solving freezing problems
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/60—Other road transportation technologies with climate change mitigation effect
- Y02T10/70—Energy storage systems for electromobility, e.g. batteries
Definitions
- the fuel cell system The fuel cell system
- Fuel cell systems are known from the prior art, for example from DE 10 2004 051 359 B4.
- the known fuel cell system comprises a fuel cell, an air supply line for supplying ambient air into the fuel cell and an exhaust duct for discharging the reacted ambient air from the fuel cell.
- a compressor for compressing the ambient air is arranged on.
- the object of the invention is to make the fuel cell system, in particular the compression or conveying the ambient air, more efficient. This is achieved in that the compressor is designed so that it can supply another consumer with ambient air in addition to the fuel cell.
- the fuel cell system comprises a fuel cell, a Heilzu arrangementslei device for supplying ambient air into the fuel cell and an exhaust duct for discharging the reacted ambient air from the fuel cell.
- a compressor is arranged in the air supply line. Downstream of the compressor, at least one further consumer of ambient air is arranged parallel to the fuel cell.
- the compressor allows the compressor to supply both the fuel cell and the other consumers cher with ambient air.
- Other consumers may be, for example, an air conditioner, a cooling system, a blocking air system or a dilution for the anode side of the fuel cell.
- each additional consumer is assigned a control valve, so that all consumers can be supplied with ambient air as needed.
- the compressor is arranged on a shaft which can be driven by a drive unit.
- the drive unit is advantageously an electric motor.
- the speed of the compressor which is preferably designed as a radial runner, can be controlled very dynamically, so that the mass flow of ambient air conveyed by it can be set very quickly to the respective requirements.
- an exhaust gas turbine is arranged in the exhaust air line, wherein the exhaust gas turbine is preferably arranged on the shaft.
- the compressor is driven by the exhaust gas turbine, preferably supported by the electric motor.
- the existing (exhaust) energy in the exhaust air is thus reused to promote the ambient air.
- the fuel cell is associated with a supply valve, and the at least one further consumer, a control valve.
- a supply valve and the at least one further consumer, a control valve.
- the air mass flow in the air supply line can be divided as needed to the fuel cell and the other consumers.
- the supply valve and the control valve are designed as proportional valves and arranged upstream of the fuel cell and the other consumer.
- a further compressor is arranged in the air supply line.
- the additional compressor can be connected in parallel or in series with the compressor.
- the other compressor may be connected to the compressor so that the air supply is made in the fuel cell either two stages condensed, or one of the two compressors supplied the fuel cell in one stage.
- the additional compressor can also be taken from an adjacent system, for example from the air conditioning system.
- the already existing in the vehicle further compressor is used particularly effectively.
- the further compressor is connected to the compressor in series GE and a supply valve is disposed between the compressor and the further compressor.
- a supply valve is disposed between the compressor and the further compressor.
- a compressor bypass valve is parallel to the supply valve and the other United dense arranged. This results in a parallel circuit of the other consumers on the one hand and the parallel circuit of Verêtrby pass valve and other compressor with supply valve on the other.
- the compressor bypass valve opens and thus closes a single-stage compressed flow path over the United denser to the fuel cell.
- the supply valve opens and closes the two-stage compaction flow path through the compressor and the other compressor to the fuel cell.
- the fuel cell can therefore be supplied in this embodiment with both one-stage and two-stage compressed ambient air.
- a compressor bypass valve is arranged parallel to the supply valve and the United denser. This results in a parallel circuit of the compressor bypass valve and the compressor with supply valve.
- the supply of the fuel cell can therefore be done via the path compressor bypass valve and other Ver denser, or via the path compressor, supply valve and other compressor.
- the supply of the fuel cell can thus be carried out both in one stage and two stages.
- the other consumers are supplied by the compressor in this embodiment. Downstream of the compressor there is thus a branch point to the other consumers and to the supply valve.
- the further compressor is connected in parallel to the United denser.
- the compressor is associated with a supply valve, and the other United dense a compressor bypass valve.
- the supply of the fuel cell with ambient air can be done both via the compressor with supply valve and via the other compressor with compressor bypass valve. Are both control valves open, the total mass flow of ambient air into the fuel cell results from the funded by compressor and further compressor mass flows, minus the Mas senstrom to the other consumers, which are also fed by the compressor.
- the supply of the fuel cell with ambient air can also redun dant made either by the compressor or by the other compressor who the.
- both compressors can be driven in each case with an exhaust gas turbine and / or with a drive unit, wherein at least one of the two compressors should have a drive unit.
- the further compressor is connected to the compressor by means of valves such that both the fuel cell and the at least one further consumer can be supplied with ambient air both from the compressor and from the further compressor.
- the compressor and the further compressor are arranged parallel to it. Downstream of a cross-circuit of the valves to the fuel cell fuel cell and the other consumers is arranged.
- the cross-circuit consists of the supply valve, which is associated with the compressor from another compressor bypass valve, which is associated with the further compressor, from a further to supply valve, which is associated with the fuel cell, each consisting of a control valve, which is assigned to a further consumer , And from the compressor bypass valve wel Ches is located at the intersection of these four valves.
- Both the fuel cell and the other consumers can be provided with any mass flow components of compressor and further compressor ver.
- the compressor and the further compressor are each configured redundantly for the fuel cell and for the other consumers.
- Fuel cell and far re consumers can thus be supplied from both the compressor and the other United denser and thus also jointly from both compressors with ambient air.
- the further compressor is switchable to the compressor both in series and in parallel.
- the ambient air for the fuel cell can be compressed both one-stage and two-stage, and the single-stage compression is designed to be redundant at the same time.
- the at least one further consumer can also be supplied with ambient air by the further compressor.
- the single-stage compaction is running redundant device for the other consumers.
- the fuel cell system may preferably be configured to drive a drive unit of a motor vehicle.
- the vehicle then has the fuel cell system according to one of the previous embodiments and a driver's cab on, with another consumer is designed for ventilation of the cab.
- the compressor supplies the driver's cab with ambient air, if necessary heated or cooled.
- FIG. 1 shows schematically a fuel cell system according to the invention
- FIG. 2 shows schematically another fuel cell system according to the invention
- FIG. 3 schematically shows yet another fuel cell system according to the invention
- FIG. 4 schematically shows yet another fuel cell system according to the invention
- FIG. 5 schematically shows yet another fuel cell system according to the invention
- FIG. 6 schematically shows yet another fuel cell system according to the invention
- FIG. 7 schematically shows yet another fuel cell system according to the invention.
- FIG. 1 schematically shows a fuel cell system 1 according to the invention.
- the fuel cell system 1 comprises a fuel cell 2 with a cathode and an anode, an air supply line 3 and an exhaust air line 4 in the cathode path and a compressor 5, in preferred embodiments also an exhaust gas turbine 6.
- the fuel cell 2 is a galvanic cell, the chemical reaction energy of a not shown fuel supply line fuel supplied in the anode path and an oxidant in the cathode path converts into electrical energy, wherein in the embodiment shown here ambient air 10 is used as the oxidant, which is supplied via the air supply line 3 by means of the compressor 5 of the fuel cell 2.
- the fuel may preferably be hydrogen or methane or methanol Me.
- the fuel cell 2 is preferably set up to drive a drive unit of a motor vehicle. For example, the electrical energy generated by the fuel cell 2 drives an electric motor of the motor vehicle.
- the compressor 5 is arranged in the air supply line 3.
- the exhaust gas turbine 6 is arranged in the exhaust air line 4.
- the compressor 5 and the exhaust gas turbine 6 are vorzugswei se mechanically connected via a shaft 7 and additionally driven by a drive unit 11 electrically.
- the exhaust gas turbine 6 thus serves to support the Antriebssein unit 11 for driving the shaft 7 and the compressor 5.
- the compressor 5, the shaft 7, the exhaust gas turbine 6 and designed as an electric motor drive unit 11 form together to an electric turbocompressor.
- the ambient air 10 is filtered in the air supply line 3 upstream of the compressor 5 by a filter 8 and downstream of the United poet 5 cooled by a heat exchanger 9.
- further consumers (21, 22, 23) of ambient air are connected in parallel with the fuel cell 2 downstream of the fuel cell 2.
- these consumers (21, 22, 23) can be supplied with ambient air in any desired manner by means of an associated control valve (21a, 22a, 23a).
- the supply of ambient air to the fuel cell by means of an associated supply valve (2 a) can be throttled or even interrupted.
- the Steuerventi le (2a, 21a, 22a, 23a) leads out as proportional valves or as shut-off valves out.
- Other consumers (21, 22, 23) of ambient air may be, for example: interior ventilation / air conditioning of the motor vehicle,
- Air cooling of a drive electric motor and / or the power electronics of a vehicle in particular for motorized vehicles for the low-price segment (for example in Asia),
- the compressor 5 thus supplies several consumers (2, 21, 22, 23) with ambient air.
- the compressor 5 is even the only air supply unit in the motor driving convincing and further includes an electric motor and power electronics. This results in the following advantages for the motor vehicle:
- Fuel cell systems are currently associated with high costs.
- the connection to several consumers 2, 21, 22, 23 to the compressor 5 offers a possibility to reduce costs.
- FIG. 2 schematically shows another fuel cell system 1 according to the invention.
- the differences to the embodiment according to FIG. 1 are:
- the fuel cell system 1 has a turbomachine 100 with the drive unit 11 and a two-stage compressor; the two-stage compressor comprises the compressor 5 and a further compressor 52, which are arranged in the embodiment of Figure 2 on the common shaft 7. Furthermore, the optional exhaust gas turbine 6 is arranged on the shaft 7. The compressor 5 and the further compressor 52 are connected in series in the air supply line 3 to the fuel cell 2. Between the two compressors 5, 52 branches out at a branch point 101, the parallel circuit
- the fuel cell 2 is supplied with ambient air at comparatively high pressure, since it is compressed in two stages by the two compressors 5, 52.
- the other consumers 21, 22, 23, however, ambient air is supplied at a lower pressure, since it is branched off after the 1-stage compression by the compressor 5 at the branch point 101.
- the fuel cell system 1 has a bypass valve 2 b between the air supply line 3 and the exhaust air line 4 in order to be able to bypass the cathodic path of the fuel cell 2.
- a water separator 41 may be arranged in the exhaust duct 4 upstream of the exhaust gas turbine 6 in order to protect the exhaust gas turbine 6 from droplet impact.
- FIG. 3 schematically shows yet another fuel cell system 1 according to the invention.
- the differences to the embodiment according to FIG. 2 will be discussed essentially.
- the fuel cell system 1 can supply the fuel cell 2 with both 1-stage and 2-stage compressed ambient air.
- the supply valve 2a is closed and the compressor bypass valve 2c is opened.
- the fuel cell 2 is then supplied only via the compressor 5.
- the heat exchanger 9 can be bypassed in this operating point because the tempera ture of the compressed air after the compressor 5 without further compression is less than or equal to the permissible inlet temperature of the ambient air in the fuel cell 2 and in the fuel cell stack.
- FIG. 4 schematically shows yet another fuel cell system 1 according to the invention.
- the differences to the embodiment according to FIG. 3 will be discussed essentially.
- the fuel cell system 1 can supply the fuel cell 2 with both 1-stage and 2-stage compressed ambient air.
- the single-stage compression takes place, however, by the further compressor 52, which is arranged in the embodiment of Figure 4 together with the exhaust gas turbine 6 on the shaft 7.
- the compressor bypass valve 2 c is connected in parallel to the compressor 5, but can also be omitted in alterna tive embodiments, so that the ambient air must always flow through the compressor 5. Downstream of the compressor 5 is the branch point 101 is arranged, at which the path splits into a parallel connection of the further consumers 21, 22, 23 (including the associated control valves 21a, 22a, 23a) and the supply valve 2a. The paths of compressor bypass valve 2c and supply valve 2a lead together again and open into the further compressor 52, from where the fuel cell 2 is fed.
- this circuit Ver can also be used to the exhaust gas turbine 6 and the other Compressor 52 to de-ice: If, for example, the shaft 7 can not be started due to icing of the gas turbine from 6, can on the compressor 5 ambient air, which can optionally also be preheated, on the standing further Ver denser 52 in the cathode path or in the Air supply line 3 are introduced, which warms up in the fuel cell 2 and then the exhaust gas turbine 6 enteist or makes common again. Thereafter, the unit of further compressor 52 and exhaust turbine 6, which is optionally driven by an electric motor can be started.
- the further compressor 52 which is preferably the main compressor for the fuel cell 2
- a partial load operation of the fuel cell 2 is possible, in which the compressor 5 conducts a mass air flow into the air supply line 3.
- the number of start-stop operations of the further compressor 52 can be reduced by keeping it switched off at low drive powers (for example stop-and-go traffic, congestion, slow city traffic) and operation of the fuel cell 2 in the lower part load Area is effected by an air mass flow of the compressor 5.
- low drive powers for example stop-and-go traffic, congestion, slow city traffic
- operation of the fuel cell 2 in the lower part load Area is effected by an air mass flow of the compressor 5.
- FIG. 5 shows schematically yet another fuel cell system 1 according to the invention, in which the compressor 5 and the further compressor 52 in the air supply line 3 the fuel cell 2 are connected in parallel.
- the compressor bypass valve 2c is arranged in the partial path of the further compressor 52, and the supply valve 2a in the partial path of the compressor 5 to the fuel cell 2. Downstream of the compressor 5 ver branches the flow of ambient air to the supply valve 2a on the one hand and to the other consumers 21st , 22 on the other hand.
- the further consumers 21, 22 are thus supplied by the compressor 5 with ambient air.
- the fuel cell 2 can be supplied with ambient air from the compressor 5, from the further compressor 52 or from both compressors 5, 52 simultaneously - in parallel.
- the air line 4 from the water separator 41 and / or the exhaust gas turbine 6 may be arranged.
- the exhaust gas turbine 6 may be designed to drive the compressor 5 or to drive the further compressor 52.
- the fuel cell 2 and the exhaust gas turbine 6 can also have bypasses, in particular for a start-up or de-icing operation of the fuel cell system 1.
- the control valves 21a, 22a may be designed as air dampers and used at various positions for the division of the air mass flow or for pressure division who the.
- the louvers can be passive - for example, as check valves - or active - in particular with control options - be executed.
- a heat exchanger can be used as an intercooler between the two compression stages.
- FIG. 6 schematically shows yet another fuel cell system 1 according to the invention, in which the compressor 5 and the further compressor 52 in the air supply line 3 of the fuel cell 2 are connected in parallel.
- the compressor 5 and the exhaust gas turbine 6 are arranged on the shaft 7.
- the compressor 5 and the further compressor 52 are arranged in the embodiment of Figure 6 in parallel in the air supply line 3, that they can supply fol lowing customers depending on the valve positions with ambient air:
- the compressor 5 supplies the fuel cell 2 and
- the additional compressor 52 supplies the further consumers 21, 22, 23.
- the compressor 5 supplies the other consumers 21, 22, 23, and the fuel cell 2 is switched off or runs in oxygen depletion.
- the additional compressor 52 supplies the fuel cell 2, and the other consumers 21, 22, 23 are switched off or have no need for ambient air.
- the further compressor 52 supplies the further consumers 21, 22, 23, and the fuel cell 2 is switched off or runs in oxygen depletion
- the supply valve 2a, the compressor bypass valve 2c, the control valves 21a, 22a, 23a of the further consumers 21, 22, 23, another supply valve 2d and another compressor bypass valve 2e are arranged in a crossing position:
- the supply valve 2a Downstream of the compressor 5, the supply valve 2a is arranged.
- the branch point 101 Downstream of the supply valve 2a, the branch point 101 is arranged, wherein the flow path splits in a direction to the fuel cell 2 and in a direction to the other consumers 21, 22, 23.
- the further compressor bypass valve 2e Downstream of the further compressor 52, the further compressor bypass valve 2e is arranged.
- a further branching point 101 b Downstream of the further compressor bypass valve 2 e, a further branching point 101 b is arranged, wherein the flow path splits in a direction to the fuel cell 2 and in a direction to the other consumers 21, 22, 23. Between the two branch points 101, 101 b, the compressor bypass valve 2 c is arranged, which is thus preferably in both directions (for fuel cell 2 and to the other consumers 21, 22, 23) can be flowed through.
- the further supply valve 2 d Downstream of the branching point 101 in the direction of the fuel cell 2, the further supply valve 2 d is arranged.
- FIG. 7 shows schematically yet another fuel cell system 1 according to the invention, in which the compressor 5 and the further compressor 52 in the air supply line 3 of the fuel cell 2 can be connected both in series and in parallel.
- a parallel circuit of the compaction ter 5 and the compressor bypass valve 2c is arranged, which downstream of the further downstream by means of the supply valve 2a further compressor 52 can be closed again, wherein alternatively the compressor bypass valve 2c can also be omitted, especially at approximately lossless flow the stationary compressor 5.
- the parallel circuit can also only downstream of the further compressor 52 by means of the further supply valve 2 d closed again who the.
- first compressor 5 and second compressor 52 Single-stage compression with increased mass flow through parallel connection of first compressor 5 and second compressor 52: open compressor bypass valve 2c, closed supply valve 2a, open further supply valve 2d
- the supply valve 2 a is preferably only able to flow through in the direction of the further compressor 52, and the further supply valve 2 d only in the direction of the fuel cell 2.
- the compressor 5 and the wide Ren compressor 52 drive. Any number of further consumers 21, 22, 23 can be supplied with ambient air by the compressor 5.
- Figure 6 and Flg ⁇ Z is a redundant air supply, so probably for the fuel cell 2 as well as for the other consumers 21, 22, 23,
- Rulege provides, if the supply valve 2a ( Figure 5) or the compressor bypass valve 2c (FIG. 6) or the further supply valve 2d (FIG. 7) can be flowed through correspondingly in both directions.
- the availability of the vehicle with the fuel cell system 1 can be increased, which is particularly advantageous in fully automated vehicles or commercially used vehicles. As a result, safety and legal requirements can be better met (for example, the dilution of hydrogen or the protection of the ventilation).
- the two air conveyor systems so the compressor 5 and the other compressor 52 can fall back on under different sources of energy (for example, the compressor 5 to 12 V or 48V and the other compressor 52 on high-voltage electrical system), which also has a Re dundance in the energy supply results.
- sources of energy for example, the compressor 5 to 12 V or 48V and the other compressor 52 on high-voltage electrical system
- the air supply to the fuel cell 2 via the additional compressor 52 which must be in operation anyway for other tasks (for example, as a fresh air blower for vehicle air conditioning).
- the compressor 5 can be completely switched off in such Batzustän. Examples include: stop-and-go traffic, traffic jams, slow city traffic, auxiliary heating / warm-up phase.
- the fuel cell system 1 is energetically optimized. Furthermore, this minimizes the number of start-stops of the compressor 5, so that its wear parts are less stressed bean. For example, due to the reduced demands on the bearings of the shaft 7 then correspondingly cheaper storage variants can be used.
- the dynamic requirements of the compressor 5 can be reduced if at idle or at lower part-load operation of the further compressor 52 takes over the task of air supply for the fuel cell 2.
- the drive unit 11 for the compressor 5 is not shown in Figures 4-7.
- the compressor 5 nevertheless has in each case the drive unit 11 in order, on the one hand, to be able to drive the shaft 7 independently of the exhaust gas turbine 6 and, on the other hand, to be able to cover all operating situations, in particular during the starting phase.
- both redundancy and two-stage compression can be realized, for example, when the compressor 5 and the further compressor 52 are not arranged on a common shaft. This can also be used to optimize the fuel cell system 1 (Wir kungsgrad, drive unit 11, power electronics).
- the further coupled air system - ie the system which does not hang on derglei Chen wave 7 as the exhaust gas turbine, depending on the design of the compressor 5 or the other compressor 52 - air into the air supply line 3 and into the exhaust duct 4 is turned on, there warmed up and then the exhaust gas turbine 6 are supplied, so that it is de-iced.
- the compressor 5 or the further compressor 52 can be started with the exhaust gas turbine 6 connected to it in a rotationally fixed manner. This eliminates additional measures such as heaters on the exhaust turbine. 6
- valves 2 a, 2 b, 2 c, 2 d, 2 e, 21 a, 22 a, 23 a proportional valves ge can be selected if necessary, so that the mass flows of ambient air to the fuel cell 2 and the other consumers 21, 22, 23 are set virtually arbitrarily in the ideal case can.
- shut-off valves or passive valves 2a, 2b, 2c, 2d, 2e, 21a, 22a, 23a for example non-return flaps
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- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Fuel Cell (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE102018205288.3A DE102018205288A1 (en) | 2018-04-09 | 2018-04-09 | The fuel cell system |
PCT/EP2019/058582 WO2019197278A1 (en) | 2018-04-09 | 2019-04-05 | Fuel cell system |
Publications (1)
Publication Number | Publication Date |
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EP3776706A1 true EP3776706A1 (en) | 2021-02-17 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP19718267.8A Pending EP3776706A1 (en) | 2018-04-09 | 2019-04-05 | Fuel cell system |
Country Status (5)
Country | Link |
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EP (1) | EP3776706A1 (en) |
JP (1) | JP7122387B2 (en) |
CN (1) | CN111937202A (en) |
DE (1) | DE102018205288A1 (en) |
WO (1) | WO2019197278A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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DE102021201475A1 (en) * | 2021-02-16 | 2022-08-18 | Knorr-Bremse Systeme für Nutzfahrzeuge GmbH | Pneumatic supply system |
DE102022207969A1 (en) | 2022-08-02 | 2024-02-08 | Robert Bosch Gesellschaft mit beschränkter Haftung | Fuel cell system and method for operating a fuel cell system |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7344787B2 (en) * | 2003-10-29 | 2008-03-18 | General Motors Corporation | Two-stage compression for air supply of a fuel cell system |
JP2006032205A (en) * | 2004-07-20 | 2006-02-02 | Nissan Motor Co Ltd | Fuel cell system |
JP2007040593A (en) * | 2005-08-02 | 2007-02-15 | Kansai Electric Power Co Inc:The | Hybrid system |
JP4773790B2 (en) * | 2005-09-30 | 2011-09-14 | 株式会社コロナ | Fuel cell system |
CN200959348Y (en) * | 2006-06-11 | 2007-10-10 | 顾章涵 | Fuel battery module or system |
JP2008123697A (en) * | 2006-11-08 | 2008-05-29 | Toyota Motor Corp | Fuel cell system |
CN202058810U (en) * | 2011-04-22 | 2011-11-30 | 爱科腾博(大连)科技有限公司 | Fuel cell system |
CN102201586B (en) * | 2011-04-22 | 2013-12-25 | 爱科腾博(大连)科技有限公司 | Fuel cell system |
DE102011109339A1 (en) * | 2011-08-03 | 2013-02-07 | Daimler Ag | Fuel cell device for passenger car, has fuel cell stack for generating electrical high-voltage and electrically operable auxiliary compressor supplied with oxidizing agent at low voltage by fuel cell stack |
JP5601362B2 (en) * | 2012-10-16 | 2014-10-08 | トヨタ自動車株式会社 | Internal combustion engine |
JP6071428B2 (en) * | 2012-10-31 | 2017-02-01 | 三菱日立パワーシステムズ株式会社 | Power generation system and method for starting fuel cell in power generation system |
JP2014163239A (en) * | 2013-02-21 | 2014-09-08 | Toyota Motor Corp | Internal combustion engine |
US10224556B2 (en) * | 2015-12-15 | 2019-03-05 | Hamilton Sundstrand Corporation | Integrated fuel cell aircraft pressurization and cooling system |
JP6483598B2 (en) * | 2015-12-21 | 2019-03-13 | 本田技研工業株式会社 | Fuel cell system |
DE102016009932A1 (en) * | 2016-08-16 | 2018-03-08 | Daimler Ag | Device for supplying air to a fuel cell |
JP6756196B2 (en) * | 2016-09-01 | 2020-09-16 | 日産自動車株式会社 | Fuel cell system |
-
2018
- 2018-04-09 DE DE102018205288.3A patent/DE102018205288A1/en active Pending
-
2019
- 2019-04-05 WO PCT/EP2019/058582 patent/WO2019197278A1/en unknown
- 2019-04-05 JP JP2020553582A patent/JP7122387B2/en active Active
- 2019-04-05 EP EP19718267.8A patent/EP3776706A1/en active Pending
- 2019-04-05 CN CN201980024562.0A patent/CN111937202A/en active Pending
Also Published As
Publication number | Publication date |
---|---|
JP2021517723A (en) | 2021-07-26 |
DE102018205288A1 (en) | 2019-10-10 |
CN111937202A (en) | 2020-11-13 |
JP7122387B2 (en) | 2022-08-19 |
WO2019197278A1 (en) | 2019-10-17 |
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