WO2005117186A2 - Electrical current measurement in a fuel cell - Google Patents
Electrical current measurement in a fuel cell Download PDFInfo
- Publication number
- WO2005117186A2 WO2005117186A2 PCT/US2005/013990 US2005013990W WO2005117186A2 WO 2005117186 A2 WO2005117186 A2 WO 2005117186A2 US 2005013990 W US2005013990 W US 2005013990W WO 2005117186 A2 WO2005117186 A2 WO 2005117186A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- electrical current
- fuel cell
- current sensors
- sensors
- sensor
- Prior art date
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04313—Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
- H01M8/04537—Electric variables
- H01M8/04574—Current
- H01M8/04582—Current of the individual fuel cell
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/2484—Details of groupings of fuel cells characterised by external manifolds
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/249—Grouping of fuel cells, e.g. stacking of fuel cells comprising two or more groupings of fuel cells, e.g. modular assemblies
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M2008/1095—Fuel cells with polymeric electrolytes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- 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
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- 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
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0662—Treatment of gaseous reactants or gaseous residues, e.g. cleaning
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- 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 present invention relates to fuel cell power systems and more particularly to methods for measuring electrical current generated by a fuel cell stack of the fuel cell power system.
- a typical fuel cell stack includes a proton exchange membrane ("PEM") with a catalytic anode layer and a catalytic cathode layer formed on opposite faces thereof. Reactant gases are directed across the catalytic faces to facilitate reaction of fuel (such as hydrogen) and oxidants (such as oxygen or air) in to electricity.
- PEM proton exchange membrane
- Effective operation of a fuel cell stack or set of fuel cell stacks requires measurement of electrical power generated from the individual cells in the fuel cell stack, a set or cluster of cells or a set of connected fuel cell stacks.
- high power fuel cell systems may use multiple fuel cell stacks to generate the necessary power requirements.
- a multiple fuel cell stack set may be a preferred approach to a single fuel cell stack arrangement having either a large active area or a substantial number of cells.
- each fuel cell stack may be of relatively standard critical mass and size as optimized over many design instances and provided as an "off-the-shelf" fuel cell stack module which is readily extended in scope by a deployment in an electrical voltage and resistance series.
- the current in each fuel cell stack in such an electrical series arrangement is equal for all fuel cell stacks in the series.
- each fuel cell stack assembly In a multiple series stack fuel cell system, it is desirable for system controls to respond to accurate measurement of the electrical current output from the fuel cell stacks.
- the most common method for measuring system electrical current is with Hall-effect sensor technology.
- each fuel cell stack assembly When using multiple fuel cell stacks electrically in series, it is beneficial for each fuel cell stack assembly to have its own electrical current sensor to facilitate system diagnostics, operation switching control, and the like.
- each module When “off-the-shelf" fuel cell stack modules (as previously discussed) are combined to achieve higher total power levels, each module conveniently has its own electrical current sensor by design to function as a stand-alone module if deployed in that manner.
- the multiple stack system has multiple redundant electrical current sensors, it is advantageous to determine system electrical current by using the average of all electrical current sensors measuring electrical current from the set of fuel cell stacks connected in the voltage (and resistance) series so that one measurement, representative of the electrical current generated by the set of fuel cell stacks as a whole, is provided to the control process logic for use in manipulation (i.e., adjustment) decisions respective to control elements to the fuel cell system.
- One disadvantage, however, in using such an averaged electrical current measurement directly is that such an approach does not account for failure in a particular electrical current sensor.
- a common failure mode for a Hall-effect electrical current sensor is that significant drift will occur which is not readily detected using common sensor fault detection methods such as short circuit analysis, open wire detection, sensor out of range evaluation, and the like.
- Another disadvantage derives from unnecessary shutdown of the fuel cell stack set if a single sensor failure halts the entire stack set in an otherwise unnecessary shutdown.
- One solution to minimizing unnecessary shutdowns is to use high cost electrical current sensors which provide high reliability; however, the high cost aspect of such a solution is not desirable in minimizing the cost for a fuel cell system.
- the present invention provides a fuel cell using a plurality of electrical current sensors to independently measure electrical current generated by the membrane electrode assembly; a real-time computer connected to each electrical current sensor; and executable comparison logic in the computer for defining an acceptability status for each electrical current sensor by independent comparison of the value of the measurement of each electrical current sensor to the individual values of the measurements of each of the other electrical current sensors in the plurality of electrical current sensors.
- the present invention also provides a method for operating a fuel cell which includes measuring electrical current generated by a fuel cell assembly with a plurality of electrical current sensors; defining an acceptability status for each electrical current sensor by computer-implemented independent comparison of the value of the measurement of each electrical current sensor to the individual values of the measurements of each of the other electrical current sensors in the plurality of electrical current sensors; and operating the fuel cell using measurements from electrical current sensors defined to have a trustworthy acceptability status.
- the present invention also provides for use of a threshold tolerance variable (preferably with a fixed value) so that each acceptability status is defined by comparison of the difference of two independent electrical current sensor values to the tolerance variable.
- the present invention further provides for an operation mode variable in the computer for designating invalid electrical current sensors.
- the present invention further provides a fuel cell system using a set of fuel cell stacks electrically connected as a voltage and resistance in series where each stack has at least one electrical current sensor.
- the present invention further provides a fuel cell system where a characteristic electrical current measurement is derived from all electrical current sensors having a trustworthy acceptability status and where the characteristic measurement is used to effect manipulation of control elements of the fuel cell, including the manipulation of control elements to shutdown operation of the fuel cell.
- the present invention further provides a fuel cell system affecting a diagnostic communication (such as an enunciator) of the sensors determined to be untrustworthy.
- the enunciator alerts an operator only if a sensor is determined to be untrustworthy (in a manner similar to an automotive 'check engine' light).
- the present invention may provide cost savings from the use of "low cost" electrical current sensors in a fuel cell system even though such "low cost” sensors have less rigorous accuracy and reliability attributes than "high cost” electrical current sensors; reliable fuel cell operation from combining electrical current measurements into a composite measurement for control; fuel cell system diagnostics; minimized shutdowns of otherwise trusted sensors and efficient fuel cell performance as drifting sensors are isolated and excluded from inducing inappropriate manipulations to fuel cell stack loading.
- Figure 1 presents a fuel cell power system block flow diagram
- Figure 2 shows a fuel cell stack portion
- Figure 3 shows a set of fuel cell stacks in an electrical series
- Figure 4 shows a flowchart for determining electrical current sensor acceptability for a particular sensor
- Figure 5 shows detail in the acceptability status definition of a set of electrical current sensors
- Figure 6 shows detail in the agreement logical block of Figure 5
- Figure 7 shows detail in the acceptability status definition block of Figure 5.
- Real-time process control is generally implemented to control the fuel cell power system described herein.
- real-time computer processing is broadly defined as a method of processing in which an event causes a given reaction within an actual time limit and wherein actions are specifically controlled within the context of and by external conditions and actual times.
- real-time controlled processing relates to the performance of associated process control logical, decision, and quantitative operations intrinsic to a process control decision algorithm functioning as part of a controlled apparatus implementing a process (such as the fuel cell benefiting from the present invention) wherein the process control decision algorithm is periodically executed with fairly high frequency usually having a period of between 20 ms and 2 sec for tactical control.
- process control decision algorithm is periodically executed with fairly high frequency usually having a period of between 20 ms and 2 sec for tactical control.
- an electrical current reading which is inappropriately low respective to verity can be the basis of manipulation of cell control elements to the point were damaging cell reversal is derived from inappropriate "starvation" of the reactant feed gases.
- Fuel cell shutdown is also stressful to the fuel cell, and unnecessary shutdowns due to electrical current sensor drift and/or failure shorten thereby the maintenance life of the fuel cell.
- a real-time computer operating the fuel cell is programmed to detect untrustworthy electrical current sensors.
- the executed logic within the real-time computer compares, for a set of electrical current sensors redundantly measuring the same electrical current, the measurement of each electrical current sensor in operation with the measurements from every other electrical current sensor in operation to see if the measured values agree within a specified tolerance level.
- each electrical current sensor therefore has a number of other electrical current sensors with which its reading "agrees.”
- the number of "agreements” associated with each electrical current sensor is compared with the "agreements" of the other electrical current sensors using combinational logic (as executed in the real-time computer) to determine if each individual electrical current sensor has either a trustworthy or an untrustworthy acceptability status.
- the trustworthy electrical current sensors are then averaged to determine a characteristic fuel cell stack system electrical current measurement. Untrustworthy electrical current sensors are excluded from use in the characteristic electrical current measurement calculation. An untrustworthy electrical current sensor may also be indicated by command or visually. Since the untrustworthy electrical current sensor is effectively "removed" from the control decision process in the fuel cell, the fuel cell power system continues to operate without shutdown.
- a hydrocarbon fuel is processed in a fuel processor, for example, by reformation and partial oxidation processes, to produce a reformate gas which has a relatively high hydrogen content on a volume or molar basis. Therefore, reference is made to hydrogen-containing as having relatively high hydrogen content.
- a fuel cell power system 100 includes a fuel processor 112 for catalytically reacting a reformable hydrocarbon fuel stream 114, and water in the form of steam from a water stream 116.
- a fuel processor 112 for catalytically reacting a reformable hydrocarbon fuel stream 114, and water in the form of steam from a water stream 116.
- air is also used in a combination partial oxidation/steam reforming reaction.
- fuel processor 112 also receives an air stream 118.
- the fuel processor 112 contains one or more reactors wherein the reformable hydrocarbon fuel in stream 114 undergoes dissociation in the presence of steam in stream 116 and air in stream 118 to produce the hydrogen-containing reformate exhausted from fuel processor 112 in reformate stream 120.
- Fuel processor 112 typically also includes one or more downstream reactors, such as water-gas shift (WGS) and/or preferential oxidizer (PrOx) reactors that are used to reduce the level of carbon monoxide in reformate stream 120 to acceptable levels, for example, below 20 ppm.
- WGS water-gas shift
- PrOx preferential oxidizer
- H 2 - containing reformate 120 is fed through block valve 174 (one control element manipulated by real-time computer 164 to control fuel cell stack system 122) into the anode chamber of fuel cell stack system 122. Concurrent with the feeding of H 2 - containing reformate 120 through block valve 174 into the anode chamber of fuel cell stack system 122, oxygen in the form of air in stream 124 is fed into the cathode chamber of fuel cell stack system 122. The hydrogen from reformate stream 120 and the oxygen from oxidant stream 124 react in fuel cell stack system 122 to produce electricity. [0032] Anode exhaust (or effluent) 126 from the anode side of fuel cell stack system 122 contains some unreacted hydrogen.
- Cathode exhaust (or effluent) 128 from the cathode side of fuel cell stack system 122 may contain some unreacted oxygen. These unreacted gases represent additional energy recovered in combustor 130, in the form of thermal energy, for various heat requirements within power system 100.
- a hydrocarbon fuel 132 and/or anode effluent 126 are combusted, catalytically or thermally, in combustor 130 with oxygen provided to combustor 130 either from air in stream 134 and/or from cathode effluent stream 128, depending on power system 100 operating conditions.
- Combustor 130 discharges exhaust stream 154 to the environment, and the heat generated thereby is directed to fuel processor 112 as needed.
- Real-time computer 164 effects control of valve 174 in response to a signal from (at least) electrical current sensors 170.
- current sensor 170 is shown in singular in Figure 1; however, as further described herein, current sensor may represent a plurality of current sensors associated with the fuel cell stack 122.
- the hydrogen feed to fuel cell stack system 122 is controlled in part through manipulation of block valve 174 by real-time computer 164 with respect to electrical current measurements from electrical current sensor 170 in enabling hydrogen-containing gas to flow to fuel cell stack system 122.
- electrical current sensor(s) 170 are Hall-effect electrical current sensors.
- Controller logic 166 is provided in real-time computer 164 for execution in real-time by computer 164.
- controller logic 166 is also denoted as “software” and/or a “program” and/or an “executable program” within real-time computer 164 as a data schema holding data and/or formulae information and/or program execution instructions which constitutes a process algorithm.
- Controller logic 166 is, in a preferred embodiment, machine code resident in the physical memory storage (e.g., "RAM” "ROM” or on a disk) of computer 164.
- Controller logic 166 is preferably derived from a source language program compiled to generate the machine code.
- the physical memory storage is in electronic data communication with a central processing unit (CPU) of computer 164 which reads data from the physical memory, computationally modifies read data into resultant data, and writes the resultant data to the physical memory.
- CPU central processing unit
- Computer 164 also receives control signals from sensor(s) 170 and sends control signals to valve 174 according to the provisions of controller logic 166.
- a partial PEM fuel cell stack 200 of fuel cell stack system 122 is schematically depicted as having a pair of membrane electrode assemblies (MEAs) 208 and 210 separated from each other by a non- porous, electrically-conductive plate 212.
- MEAs 208, 210 have a cathode face 208c, 210c and an anode face 208a, 210a.
- MEAs 208, 210 and bipolar plate 212 are stacked together between non-porous, electrically-conductive, liquid-cooled plates 212, 214 and 216.
- Plates 212, 214, 216 each include respective flow fields 218, 220, 222 established from a plurality of flow channels formed in the faces of the plates for distributing fuel and oxidant gases (i.e., H 2 & O 2 ) to the reactive faces of MEAs 208, 210.
- Nonconductive gaskets or seals 226, 228, 230, 232 provide sealing and electrical insulation between the several plates of fuel cell stack 200. It is to be noted that fuel cell stack 200 shows two fuel cells with plate 212 being shared between the two fuel cells and plates 214, 216 being shared between one of the shown fuel cells and, in each case, another fuel cell not depicted in Figure 2.
- a "fuel cell" within a fuel cell stack is not physically fully separable insofar as any particular fuel cell in the stack will share at least one side of a bipolar plate with another cell.
- Porous, gas permeable, electrically conductive sheets 234, 236, 238, 240 press up against the electrode faces of MEAs 208, 210 and serve as primary electrical current collectors for the respective electrodes.
- Primary electrical current collectors 234, 236, 238, 240 also provide mechanical supports for MEAs 208, 210, especially at locations where the MEAs are otherwise unsupported in the flow field.
- Plate 214 presses up against primary electrical current collector 234 on cathode face 208c of MEA 208
- plate 216 presses up against primary electrical current collector 240 on anode face 210a of MEA 210
- plate 212 presses up against primary electrical current collector 236 on anode face 208a of MEA 208 and against primary electrical current collector 238 on cathode face 210c of MEA 210.
- An oxidant gas such as air/oxygen is supplied to the cathode side of fuel cell stack 200 from air source 118 and line 124 via appropriate supply plumbing 248.
- a fuel such as hydrogen is supplied to the anode side of fuel cell 200 from a hydrogen source 270 via appropriate supply plumbing 244.
- Exhaust plumbing (not shown) for both the H 2 and O 2 /air sides of MEAs 208, 210 is also provided for removing anode effluent from the anode flow field and the cathode effluent from the cathode flow field.
- Coolant plumbing 250, 252 is provided for supplying and exhausting liquid coolant to bipolar plates 212, 214, and 216, as needed.
- controller logic 166 of real-time computer 164 generic fuel cell power system 100 (see Figure 1) uses block valve 174 to control hydrogen gas flow, and electrical current sensor(s) 170 are used as a feedback sensors measuring electricity generated by stack 200.
- Conductor 310 electrical current is measured by electrical current sensors 170.1, 170.2, 170.3, 170.4 (reprised as sensor 170 in Figure 1 ) where fuel cell stack 302, fuel cell stack 304, fuel cell stack 306 and fuel cell stack 308 are implemented in an electrical (voltage and resistance) series as shown with one electrical current sensor provided for each stack.
- Fuel stack set 300 uses fuel cell stacks 302, 304, 306, and 308 as a plurality of fuel cell stacks in the set of n fuel cell stacks. Stacks 302, 304, 306, 308 may be separate and distinct modules or alternatively may be separate and distinct clusters of cells within a stack. [0039] Use of multiple current sensors to confirm an electrical current measurement in fuel cell power system operation is not confined to fuel cell stack series arrangements.
- a set of fuel cell stacks 300 is, in one embodiment, provided for the power plant for a bus, such as, without limitation, a school bus, a tour bus, or a metropolitan transit passenger bus. In another embodiment, a set of fuel cell stacks 300 is provided for the power plant for an automobile. In yet another embodiment, a set of fuel cell stacks 300 is provided for a stationary power generation application.
- Computer-implemented determination of electrical current sensor acceptability is effected in controller logic 166 for a particular signal input into computer 164 from any of electrical current sensors 170.1 , 170.2, 170.3, 170.4 according to the algorithm 400 of Figure 4.
- Block 402 of Figure 4 represents the reading of the electrical current sensor data from an electrical current sensor such as sensors 170.1 , 170.2, 170.3, 170.4.
- Block 404 shows a comparison operation, followed by decision block 406 for designating (a) an untrustworthy acceptability status (block 408) or (b) further action in decision block 412.
- Decision block 412 evaluates other considerations in the status of all electrical current sensors as a set to lead to either a trustworthy designation for the particular electrical current sensor (e.g., any of electrical current sensors 170.1 , 170.2, 170.3, 170.4) in block 410 or to a shutdown decision in block 414.
- Figure 5 shows the acceptability status definition method 500 for a set of electrical current sensors.
- Figures 5-7 show a (simulated) block flow characterization of the "executable program" within real-time computer 164 as a portion of controller logic 166 and the algorithm 400 illustrated in Figure 4.
- Figure 5 shows an exemplary logic flow for 4 different sensors, designated as 170.1 , 170.2, 170.3 and 170.4 respectively in Figure 3.
- Senso , sensor_2, sensor_3, and sensor_4 represent data values from sensors 170.1, 170.2, 170.3, 170.4 which are independently addressed via multiplexing logic 510 into agreement logical blocks 502a, 502b, 502c, and 502d.
- Agreement logical blocks 502a, 502b, 502c, and 502d independently evaluate sensor_1 , sensor_2, sensor_3, and sensor_4 respectively such that, for example, agreement logical block 502a independently compares the value of the measurement of electrical current sensor sensor_1 to the individual values of the measurements of each of the other electrical current sensors (sensor_2, sensor_3, and sensor_4) in the set of electrical current sensors.
- agreement logical block 502b, 502c and 502d independently compares the data value of sensor_2, sensor_3, and sensor_4, respectively to the individual data values of the other electrical current sensors.
- agreement logical block 502 decision an operation mode variable for designating inactive stacks and their corresponding invalid electrical current sensors is read from operation mode variable block 508.
- stack_1 with corresponding sensor_1 and stack_2 with corresponding sensor_2 are "on-line” (operation mode variable value of "1") with stack_3 with corresponding sensor_3 and stack_4 with corresponding sensor_4 being “off-line” (operation mode variable value of "0").
- operation mode indicators indicate the state of a given fuel cell stacks, wherein stack 302, 304 are “on-line” and stacks 306, 308 are "off-line”.
- Acceptability status definition block 506 takes these factors into consideration and determines whether sensor one and two are trustworthy, as indicated by the corresponding outputs of "1" (see display blocks per 512). [0043] Acceptability status definition block 506 receives output from agreement logical blocks 502a, 502b, 502c, and 502d as well as output from operation mode variable block 508 to effect definition of trusted electrical current sensors. [0044] Display blocks 504 and 512 show the status of particular decision operations within acceptability status definition method 500.
- FIG. 5 shows detail 600 of agreement logical block 502 shown in Figure 5. Inputs from multiplexing logic 510 ( Figure 5) are reprised from Figure 5.
- Output as displayed in block 504 ( Figure 5) for input into block 506 is shown at 606.
- Operation mode (block 508) is brought forward into Figure 6 in data linkage 604.
- Figure 6 also shows threshold tolerance variable 602 (with an exemplary value of 10) so that the acceptability status of block 502 is defined by comparison of the difference of two independent electrical current sensor values to tolerance variable 602 (in this case as a fixed value of 10).
- the "upper limit” tolerance value is multiplied by -1 in inverter 608 to create a companion "lower limit” tolerance value.
- a threshold range is defined by the upper and lower tolerance limits.
- a skilled practitioner will recognize that the upper and lower limits, and thus the threshold range will vary depending on the particular application and the operating condition of the system for such applications.
- Figure 7 shows detail 700 in acceptability status definition block 506 as shown in Figure 5.
- Inputs 702, 704, 706, 708 and 710 are top-to-bottom inputs into block 506 from blocks 502a, 502b, 502c, 502d, and 508 shown in Figure 5 respectively.
- Table 1 presents a number of different value sets for sensoM , sensor_2, sensor_3, and sensor_4, with affiliated indications of trustworthy or untrustworthy acceptability status when processed via the executable logic depicted in Figures 4-7.
- Test No 1 2 3 Sensor 510 502 trust? 510 502 trust? 510 502 trust?
- Test No. 1, 4 and 5 of Table 1 show two bad sensors but do not define a shutdown scenario, preserving robust operation of the fuel cell system in the face of sensor failure.
- Test No. 6 of Table 1 defines a basis for a shutdown decision for lack of trust in any sensor with only two bad sensors based on the operation mode of the system. In other words, two sets of sensors are in agreement; however, there is not enough information to say which two to trust.
- certain patterns of acceptability status values patterned as a first defined set denote acceptable continued operation and other patterns of acceptability status values patterned as a second defined set denote a need to shutdown.
- the described embodiment therefore enables shutdown when an effectively predefined collective shutdown value set is equivalent to all the acceptability status values patterned as a comparably defined set.
- a characteristic current measurement from all electrical current sensors having a trustworthy acceptability status is calculated.
- the characteristic current measurement is an average value of all electrical current sensors 170 having a trustworthy acceptability status.
- Control logic 166 effects manipulation (adjustment) of control elements of the fuel cell (such as valve 174) with respect to the characteristic electrical current measurement value.
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Abstract
Description
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Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2007527243A JP2007538369A (en) | 2004-05-18 | 2005-04-25 | Current measurement method in fuel cell |
| DE112005001125T DE112005001125T5 (en) | 2004-05-18 | 2005-04-25 | Measurement of electric current in a fuel cell |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US57203104P | 2004-05-18 | 2004-05-18 | |
| US60/572,031 | 2004-05-18 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2005117186A2 true WO2005117186A2 (en) | 2005-12-08 |
| WO2005117186A3 WO2005117186A3 (en) | 2007-03-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2005/013990 Ceased WO2005117186A2 (en) | 2004-05-18 | 2005-04-25 | Electrical current measurement in a fuel cell |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20050260471A1 (en) |
| JP (1) | JP2007538369A (en) |
| DE (1) | DE112005001125T5 (en) |
| WO (1) | WO2005117186A2 (en) |
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| US7935455B2 (en) * | 2006-02-27 | 2011-05-03 | GM Global Technology Operations LLC | Balanced hydrogen feed for a fuel cell |
| US7887958B2 (en) * | 2006-05-15 | 2011-02-15 | Idatech, Llc | Hydrogen-producing fuel cell systems with load-responsive feedstock delivery systems |
| JP2008010367A (en) * | 2006-06-30 | 2008-01-17 | Toyota Motor Corp | Fuel cell diagnostic apparatus and diagnostic method |
| JP5169056B2 (en) * | 2007-07-31 | 2013-03-27 | 日産自動車株式会社 | Fuel cell system and its operation stop method |
| US8790840B2 (en) * | 2010-03-10 | 2014-07-29 | Dcns Sa | Systems and methods for fuel cell thermal management |
| MX2011009115A (en) * | 2011-08-31 | 2013-02-28 | Mexicano Inst Petrol | Modular device to measure ionic, electronic and mixed conductivity in polymeric and ceramic membranes. |
| TWI427308B (en) * | 2011-10-18 | 2014-02-21 | Iner Aec Executive Yuan | Testing device for solid oxide fuel cell |
| KR101551060B1 (en) * | 2014-02-13 | 2015-09-08 | 현대자동차주식회사 | Method for diagnosing fuel cell stack |
| JP6779949B2 (en) * | 2018-09-04 | 2020-11-04 | 本田技研工業株式会社 | Power storage system and abnormality judgment method |
| DE102019208669B3 (en) * | 2019-06-14 | 2020-11-19 | Siemens Mobility GmbH | Sensor arrangement for monitoring a technical system and method for operating a sensor arrangement |
| US11732820B2 (en) * | 2020-10-23 | 2023-08-22 | Fisher Controls International Llc | Activating trip functions of a safety valve positioner by way of a control panel to achieve a safe state |
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| US5945229A (en) * | 1997-02-28 | 1999-08-31 | General Motors Corporation | Pattern recognition monitoring of PEM fuel cell |
| JP2001095107A (en) * | 1999-09-21 | 2001-04-06 | Yamaha Motor Co Ltd | Power supply control method for hybrid drive type mobile unit |
| US6383670B1 (en) * | 1999-10-06 | 2002-05-07 | Idatech, Llc | System and method for controlling the operation of a fuel processing system |
| JP2001275205A (en) * | 2000-03-24 | 2001-10-05 | Nissan Motor Co Ltd | Control device for combined use system of secondary battery and generator |
| WO2002018879A1 (en) * | 2000-08-25 | 2002-03-07 | Battelle Memorial Institute | Method and apparatus to predict the remaining service life of an operating system |
| JP2003180080A (en) * | 2001-12-11 | 2003-06-27 | Railway Technical Res Inst | Power converter |
| JP2005526363A (en) * | 2002-05-16 | 2005-09-02 | バラード パワー システムズ インコーポレイティド | Power facility with an array of adjustable fuel cell systems |
| US20040081868A1 (en) * | 2002-10-23 | 2004-04-29 | Edlund David J. | Distributed fuel cell network |
| US7181334B2 (en) * | 2003-05-14 | 2007-02-20 | General Motors Corporation | Method and apparatus to diagnose intake airflow |
-
2005
- 2005-04-05 US US11/099,261 patent/US20050260471A1/en not_active Abandoned
- 2005-04-25 JP JP2007527243A patent/JP2007538369A/en not_active Withdrawn
- 2005-04-25 DE DE112005001125T patent/DE112005001125T5/en not_active Withdrawn
- 2005-04-25 WO PCT/US2005/013990 patent/WO2005117186A2/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| WO2005117186A3 (en) | 2007-03-08 |
| JP2007538369A (en) | 2007-12-27 |
| US20050260471A1 (en) | 2005-11-24 |
| DE112005001125T5 (en) | 2008-06-05 |
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