US20080152959A1 - Methods for fuel cell system optimization - Google Patents

Methods for fuel cell system optimization Download PDF

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Publication number
US20080152959A1
US20080152959A1 US11/641,942 US64194206A US2008152959A1 US 20080152959 A1 US20080152959 A1 US 20080152959A1 US 64194206 A US64194206 A US 64194206A US 2008152959 A1 US2008152959 A1 US 2008152959A1
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maximum
mode
fuel cell
operational
cell system
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US7393603B1 (en
Inventor
Steven Edward Schumer
Arne Watson Ballantine
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Bloom Energy Corp
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Bloom Energy Corp
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Assigned to BLOOM ENERGY CORPORATION reassignment BLOOM ENERGY CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SCHUMER, STEVEN EDWARD, BALLANTINE, ARNE WATSON
Priority to PCT/US2007/025727 priority patent/WO2008079207A1/en
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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes 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
    • H01M8/04537Electric variables
    • H01M8/04604Power, energy, capacity or load
    • H01M8/04619Power, energy, capacity or load of fuel cell stacks
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04701Temperature
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04746Pressure; Flow
    • H01M8/04753Pressure; Flow of fuel cell reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04828Humidity; Water content
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04858Electric variables
    • H01M8/04925Power, energy, capacity or load
    • H01M8/0494Power, energy, capacity or load of fuel cell stacks
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the present invention is directed to fuel cell systems and operation thereof.
  • Fuel cells are electrochemical devices which can convert energy stored in fuels to electrical energy with high efficiencies.
  • High temperature fuel cells include solid oxide and molten carbonate fuel cells. These fuel cells may operate using hydrogen and/or hydrocarbon fuels.
  • Embodiments of the present invention describe methods of operating a fuel cell system comprising: operating a fuel cell system at one or more operational modes, wherein said fuel cell system is configured to operate at a plurality of operational modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • a fuel cell system comprises: a computer system for directing the operation of said fuel cell system, said computer system comprising: a processor; and a memory, coupled to the processor, the memory comprising a plurality of instructions executed by the processor, the plurality of instructions configured to: operate the fuel cell system in a first operational mode; and switch the fuel cell system to a second operational mode; wherein said first and second operational modes are each selected from an array of operational modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • the embodiments of the present invention overcome the aforementioned problems by providing a flexible approach to operating a fuel cell system. Namely they provide the ability operate at one or more different operational modes. For instance, all settings are adjusted to optimize to an operational mode of the fuel cell system such as maximum return on investment.
  • embodiments of the present invention enable optimization of system output to a number of key variables. For example, this system allows the optimization of the system output to maximum return on investment. This ensures that the fuel cell generator equipment purchased is best utilized for return on investment.
  • a fuel cell system is configured to operate at one or more different operational modes.
  • a fuel cell system is configured to switch between at least two different operational modes.
  • a fuel cell system is operated at a mode selected from an available list of modes.
  • a fuel cell system is operated at a mode based on data provided to the system.
  • a fuel cell system is configured to automatically switch from one operational mode to another different mode based on data provided thereto.
  • a fuel cell system is configured with a control system for automatically selecting between operational modes.
  • a fuel cell system is configured with a computer system for automatically selecting between operational modes.
  • Embodiments of the present invention describe a fuel cell system control method whereby it is possible to select from multiple criteria for system operation.
  • the controller of the fuel cell system will optimize system operation against these criteria, to achieve the following operational modes: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • Maximum output power generally describes a state of the fuel cell system wherein the system outputs the maximum possible output power without damage. For instance, system controls are adjusted to make changes, such as increasing the fuel cell temperature and/or increasing the fuel flow rate to the upper end of their allowed range.
  • the fuel system operates at the maximum possible overall efficiency.
  • the control system constantly monitors stack voltages, inverter power losses and auxiliary component loads and selects both thermal and electric conversion levels to be at the level where system efficiency is optimized.
  • This output power will almost always be less than the maximum output power of the system and it will also be less than the minimum output power of the system because of the shape of the curve of fuel cell efficiency, electric power conversion efficiency curve, and auxiliary component power losses.
  • fuel cell efficiency decreases with increased power, at the higher limits.
  • Fixed power auxiliary devices have a decreasing negative impact on efficiency the higher the output power of the system is. Losses such as pump, blower, and resistive heating losses will increase continuously as the output power of the system is increased.
  • this mode the fuel cell system is operated in a mode where age-related and thermal effects are minimized while maintaining and acceptable load for the customer.
  • the controller will isolate outputs which, for example, are paralleled to increase load-sharing of 25 KW modules. Thus, an efficiency loss may be incurred. However, by isolating outputs, the reliability of each individual output is increased.
  • the maximum lifetime mode optimizes control parameters, such as stack temperature, reformer temperature, power level, humidity, and gas fuel flow in order to achieve the longest lifetime of components, such as the fuel cell stacks, hot box metal components, and auxiliary components such as the inverter or air blowers.
  • control parameters such as stack temperature, reformer temperature, power level, humidity, and gas fuel flow in order to achieve the longest lifetime of components, such as the fuel cell stacks, hot box metal components, and auxiliary components such as the inverter or air blowers.
  • the temperature parameter in particular would be minimized to the lowest possible value for sustained operation in order to minimize the degradation rate of fuel cell components.
  • the fuel cell system adjusts its output in order to obtain a maximum return on system investment.
  • One or more of several key inputs based on the customer installation are maintained through system lifetime: cost of fuel; opportunity and lost-business costs; grid stability or fraction of capacity; cost or credit of CO 2 (or other) system emissions; cost of system hardware; and cost of replacement electricity from the grid (as a function of yearly season and time of day).
  • the system is then configured with upper and lower limits on key system parameters such as output power and stack temperatures.
  • the system is also configured with limits on key external factors such as grid power cost, grid stability, and loss of power risk.
  • the control system optimizes system parameters to minimize the cost of power generation throughout the projected lifetime of the system.
  • a combined mode is used wherein two or more of said operational modes coincide via the same system settings. For example, maximum efficiency and maximum lifetime are both optimized with the same settings. This might involve operating at a temperature which maximizes lifetime, but at a power level which maximizes efficiency.
  • a method of operating a fuel cell system involves the steps of operating the fuel cell system at a first operational mode and switching from said first operational mode to a second operational mode.
  • Said first and second operational modes are different from one another and each independently selected from a list of modes comprising maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • a benefit of the present invention is a flexible approach to operating a fuel cell system.
  • the fuel cell system is flexibly operated based on the desired benefits to the end user and/or supplier of power. This method will permit automatic, permissive switching among the modes discussed above.
  • the control system can be so configured as to automatically respond to such events as, but not limited to, time-of-day electric rate changes by changing to maximum return on investment mode.
  • These events, provided as data to said fuel cell system, or controller for the system may further include other externally supplied market signals such as price of spot-market such as natural gas, for systems which operate on natural gas.
  • user definable control modes might be included.
  • the matrix of parameters limits, the matrix of costs, and the matrix of system responses could be manipulated by the customer in order to obtain an optimization which the customer's circumstances dictate.
  • the user settings could be triggered to change on a time of day basis for use in peak-shaving. This might be particularly appropriate in installations where billing rates change at discrete times and cost of power is unacceptably high.
  • the control system could be configured to recognize and diagnose situations where a change in system configuration may lead to, for example, an improved return on investment condition. For instance, if three 25 KW hot box modules were installed, but base load exceeds 100 KW and CO 2 emissions costs are great, the control system could flag for the user the advantage of installing a fourth 25 KW hot box module.
  • Operation of the fuel cell system may be carried out manually or automatically. Both types of operation are further described below.
  • a particular group of settings may be associated with one of the operational modes wherein activation of said settings can be carried out in one step.
  • the settings are constantly monitored and adjusted to achieve the optimal state of the system, be it maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • a human operator may change the operational mode of the fuel cell system by using a control system such as a computer or a control panel, based on the desired benefits as previously discussed.
  • a control system such as a computer or a control panel
  • displayed or printed data pertaining to events such as fuel cost, or electricity cost may be used by the human operator in selecting the most appropriate mode.
  • control system such as a computer or a dedicated logic chip (or circuit) is configured to store operational mode parameters and execute an operational mode from of list of: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding. Data pertaining to events previously described would be received by the control system and positively (switch to new mode) or negatively (stay at the same mode) acted upon.
  • another method involves operating a fuel cell system equipped with a control system by activating said control system to switch the operational mode of the fuel cell from a first mode to a second mode.
  • any combination can result. That is, the first, second, third, etc. modes are each independently chosen from the list of operational modes previously described. This obviously can result in a very large number of combinations or permutations.
  • a fuel cell system in another embodiment, includes a fuel cell stack and a computer system for directing the operation of said fuel cell system.
  • Said computer system preferably comprises a processor, and a memory coupled to the processor.
  • the memory stores a plurality of instructions (corresponding to operational modes) executed by the processor, to operate the fuel cell system in a first operational mode. If need be, the computer system can switch the fuel cell system to a second operational mode.
  • Said first and second operational modes are each selected from maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • the computer system may be equipped to receive data pertaining to, but not limited by, time-of-day electric rate changes or fuel cost. Upon receipt of the data, the computer system may select to switch or not switch modes based on how it is programmed.
  • the data may be provided from the internet, entered manually by the operator provided from other data sources.

Abstract

A method of operating a fuel cell system which includes operating a fuel cell system at one or more operational modes, wherein said fuel cell system is configured to operate at a plurality of operational modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.

Description

    BACKGROUND OF THE INVENTION
  • The present invention is directed to fuel cell systems and operation thereof.
  • Fuel cells are electrochemical devices which can convert energy stored in fuels to electrical energy with high efficiencies. High temperature fuel cells include solid oxide and molten carbonate fuel cells. These fuel cells may operate using hydrogen and/or hydrocarbon fuels. There are classes of fuel cells, such as the solid oxide regenerative fuel cells, that also allow reversed operation, such that oxidized fuel can be reduced back to unoxidized fuel using electrical energy as an input.
  • SUMMARY OF THE INVENTION
  • Embodiments of the present invention describe methods of operating a fuel cell system comprising: operating a fuel cell system at one or more operational modes, wherein said fuel cell system is configured to operate at a plurality of operational modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding. In a specific embodiment, a fuel cell system comprises: a computer system for directing the operation of said fuel cell system, said computer system comprising: a processor; and a memory, coupled to the processor, the memory comprising a plurality of instructions executed by the processor, the plurality of instructions configured to: operate the fuel cell system in a first operational mode; and switch the fuel cell system to a second operational mode; wherein said first and second operational modes are each selected from an array of operational modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • Currently available fuel cell systems are typically optimized for performance based on one or possibly two parameters. The most typical parameters being maximum output power and customer load. Several problems accompany such performance optimizations.
  • First, when fuel costs are high, operation at a maximum power setting (or operating to meet all customer load demands) may be a poor choice economically, thereby reducing the economic benefits expected of the system.
  • Second, given the typical shape of the efficiency curve of a fuel cell system, operating at a maximum power setting when the need for reduced CO2 emissions is in effect, is an inappropriate choice, particularly when in violation of the conditions under which the system has been licensed for operation.
  • Finally, if it is desired to maintain the longest possible economic lifetime or reliability of the equipment (of the fuel cell system), then operating at a maximum output power or following a load profile will not be satisfactory.
  • The embodiments of the present invention overcome the aforementioned problems by providing a flexible approach to operating a fuel cell system. Namely they provide the ability operate at one or more different operational modes. For instance, all settings are adjusted to optimize to an operational mode of the fuel cell system such as maximum return on investment.
  • Whereas previous fuel cell generator systems operate strictly to generate power at a specified output level or to generate power following a varying load profile, embodiments of the present invention enable optimization of system output to a number of key variables. For example, this system allows the optimization of the system output to maximum return on investment. This ensures that the fuel cell generator equipment purchased is best utilized for return on investment.
  • Accordingly, in one aspect of the present invention a fuel cell system is configured to operate at one or more different operational modes.
  • In another aspect, a fuel cell system is configured to switch between at least two different operational modes.
  • In another aspect, a fuel cell system is operated at a mode selected from an available list of modes.
  • In another aspect, a fuel cell system is operated at a mode based on data provided to the system.
  • In yet aspect, a fuel cell system is configured to automatically switch from one operational mode to another different mode based on data provided thereto.
  • In yet another aspect, a fuel cell system is configured with a control system for automatically selecting between operational modes.
  • In still another aspect, a fuel cell system is configured with a computer system for automatically selecting between operational modes.
  • Embodiments of the present invention describe a fuel cell system control method whereby it is possible to select from multiple criteria for system operation. The controller of the fuel cell system will optimize system operation against these criteria, to achieve the following operational modes: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • Maximum output power generally describes a state of the fuel cell system wherein the system outputs the maximum possible output power without damage. For instance, system controls are adjusted to make changes, such as increasing the fuel cell temperature and/or increasing the fuel flow rate to the upper end of their allowed range.
  • In the maximum efficiency mode, the fuel system operates at the maximum possible overall efficiency. For example, the control system constantly monitors stack voltages, inverter power losses and auxiliary component loads and selects both thermal and electric conversion levels to be at the level where system efficiency is optimized. This output power will almost always be less than the maximum output power of the system and it will also be less than the minimum output power of the system because of the shape of the curve of fuel cell efficiency, electric power conversion efficiency curve, and auxiliary component power losses. Typically, fuel cell efficiency decreases with increased power, at the higher limits. Fixed power auxiliary devices have a decreasing negative impact on efficiency the higher the output power of the system is. Losses such as pump, blower, and resistive heating losses will increase continuously as the output power of the system is increased.
  • In the maximum reliability this mode, the fuel cell system is operated in a mode where age-related and thermal effects are minimized while maintaining and acceptable load for the customer. In this mode, the controller will isolate outputs which, for example, are paralleled to increase load-sharing of 25 KW modules. Thus, an efficiency loss may be incurred. However, by isolating outputs, the reliability of each individual output is increased.
  • Similar to maximum reliability mode, the maximum lifetime mode optimizes control parameters, such as stack temperature, reformer temperature, power level, humidity, and gas fuel flow in order to achieve the longest lifetime of components, such as the fuel cell stacks, hot box metal components, and auxiliary components such as the inverter or air blowers. In this mode, the temperature parameter in particular would be minimized to the lowest possible value for sustained operation in order to minimize the degradation rate of fuel cell components.
  • In maximum return on investment mode, the fuel cell system adjusts its output in order to obtain a maximum return on system investment. One or more of several key inputs based on the customer installation are maintained through system lifetime: cost of fuel; opportunity and lost-business costs; grid stability or fraction of capacity; cost or credit of CO2 (or other) system emissions; cost of system hardware; and cost of replacement electricity from the grid (as a function of yearly season and time of day). The system is then configured with upper and lower limits on key system parameters such as output power and stack temperatures. The system is also configured with limits on key external factors such as grid power cost, grid stability, and loss of power risk. The control system optimizes system parameters to minimize the cost of power generation throughout the projected lifetime of the system.
  • In one embodiment, a combined mode is used wherein two or more of said operational modes coincide via the same system settings. For example, maximum efficiency and maximum lifetime are both optimized with the same settings. This might involve operating at a temperature which maximizes lifetime, but at a power level which maximizes efficiency.
  • In another embodiment, a method of operating a fuel cell system involves the steps of operating the fuel cell system at a first operational mode and switching from said first operational mode to a second operational mode. Said first and second operational modes are different from one another and each independently selected from a list of modes comprising maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • As previously noted, a benefit of the present invention is a flexible approach to operating a fuel cell system. In sequential or multiple mode operation methods, the fuel cell system is flexibly operated based on the desired benefits to the end user and/or supplier of power. This method will permit automatic, permissive switching among the modes discussed above. If, for example, the fuel cell system is operating in the maximum output power mode, the control system can be so configured as to automatically respond to such events as, but not limited to, time-of-day electric rate changes by changing to maximum return on investment mode. These events, provided as data to said fuel cell system, or controller for the system, may further include other externally supplied market signals such as price of spot-market such as natural gas, for systems which operate on natural gas.
  • In some cases, user definable control modes might be included. In these modes, the matrix of parameters limits, the matrix of costs, and the matrix of system responses could be manipulated by the customer in order to obtain an optimization which the customer's circumstances dictate.
  • The user settings could be triggered to change on a time of day basis for use in peak-shaving. This might be particularly appropriate in installations where billing rates change at discrete times and cost of power is unacceptably high.
  • The control system could be configured to recognize and diagnose situations where a change in system configuration may lead to, for example, an improved return on investment condition. For instance, if three 25 KW hot box modules were installed, but base load exceeds 100 KW and CO2 emissions costs are great, the control system could flag for the user the advantage of installing a fourth 25 KW hot box module.
  • Operation of the fuel cell system may be carried out manually or automatically. Both types of operation are further described below. For instance, a particular group of settings may be associated with one of the operational modes wherein activation of said settings can be carried out in one step. Preferably, the settings are constantly monitored and adjusted to achieve the optimal state of the system, be it maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • In manual operation, a human operator may change the operational mode of the fuel cell system by using a control system such as a computer or a control panel, based on the desired benefits as previously discussed. As in some embodiments, displayed or printed data pertaining to events such as fuel cost, or electricity cost may be used by the human operator in selecting the most appropriate mode.
  • In automatic operation, the control system such as a computer or a dedicated logic chip (or circuit) is configured to store operational mode parameters and execute an operational mode from of list of: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding. Data pertaining to events previously described would be received by the control system and positively (switch to new mode) or negatively (stay at the same mode) acted upon.
  • Therefore, another method involves operating a fuel cell system equipped with a control system by activating said control system to switch the operational mode of the fuel cell from a first mode to a second mode.
  • In embodiments of the present invention wherein operational modes are switched between two or more different ones, any combination can result. That is, the first, second, third, etc. modes are each independently chosen from the list of operational modes previously described. This obviously can result in a very large number of combinations or permutations.
  • In another embodiment, a fuel cell system includes a fuel cell stack and a computer system for directing the operation of said fuel cell system. Said computer system preferably comprises a processor, and a memory coupled to the processor. The memory stores a plurality of instructions (corresponding to operational modes) executed by the processor, to operate the fuel cell system in a first operational mode. If need be, the computer system can switch the fuel cell system to a second operational mode. Of course the number of times the switching occurs is potentially limitless. Said first and second operational modes are each selected from maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
  • The computer system may be equipped to receive data pertaining to, but not limited by, time-of-day electric rate changes or fuel cost. Upon receipt of the data, the computer system may select to switch or not switch modes based on how it is programmed. The data may be provided from the internet, entered manually by the operator provided from other data sources.
  • The foregoing description of the invention has been presented for purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise form disclosed, and modifications and variations are possible in light of the above teachings or may be acquired from practice of the invention. The description was chosen in order to explain the principles of the invention and its practical application. It is intended that the scope of the invention be defined by the claims appended hereto, and their equivalents.

Claims (24)

1. A method of operating a ftiel cell system compri sing:
operating the fuel cell system at a first operational mode; and
switching from said first operational mode to a second operational mode,
wherein said first and second operational modes are different from one another and each independently selected from a list of modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
2. The method of claim 1 wherein switching between the first and second operational modes is carried out manually.
3. The method of claim 1 wherein switching between the first and second operational modes is carried out automatically.
4. The method of claim 3 wherein the switching is carried out based on data provided to the system.
5. The method of claim 4 further comprising the step of providing data to the system.
6. The method of claim 4 wherein the data comprises: time-of-day electric rate changes, fuel cost or CO2 emission levels.
7. The method of claim 1 wherein the system further comprises a control system for storage and execution of settings for each operational mode.
8. The method of claim 7 further comprising the step of activating the control system to switch the operational mode of the fuel cell from the first mode to the second mode.
9. The method of claim 1 wherein the first mode is maximum power output.
10. The method of claim 1 wherein the second mode is maximum power output.
11. The method of claim 1 wherein the first mode is maximum system efficiency.
12. The method of claim 1 wherein the second mode is maximum system efficiency.
13. The method of claim 1 wherein the first mode is maximum reliability.
14. The method of claim 1 wherein the second mode is maximum reliability.
15. The method of claim 1 wherein the first mode is maximum lifetime.
16. The method of claim 1 wherein the second mode is maximum lifetime.
17. The method of claim 1 wherein the first mode is maximum return on investment.
18. The method of claim 1 wherein the second mode is maximum return on investment.
19. The method of claim 1 wherein the first mode is a mode combining two or more of maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment.
20. The method of claim 1 wherein the second mode is a mode combining two or more of maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment.
21. A fuel cell system comprising:
a computer system for directing the operation of said fuel cell system, said computer system comprising:
a fuel cell stack;
a processor; and
a memory, coupled to the processor, the memory comprising a plurality of instructions executable by the processor, the plurality of instructions configured to:
operate the fuel cell system in a first operational mode; and
switch the fuel cell system to a second operational mode;
wherein said first and second operational modes are each selected from an array of operational modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
22. A fuel cell system comprising:
a fuel cell stack; and
a means for:
operating the fuel cell system at a first operational mode; and
switching from said first operational mode to a second operational mode,
wherein said first and second operational modes are different from one another and each independently selected from a list of modes comprising: maximum power output, maximum system efficiency, maximum reliability, maximum lifetime, maximum return on investment or a mode combining any two or more of the preceding.
23. A method of operating a fuel cell system comprising:
providing a fuel cell system comprising a fuel cell stack and a control system;
storing in the control system a list of operational mode parameters which correspond to a maximum power output mode, a maximum system efficiency mode, a maximum reliability mode, a maximum lifetime mode, a maximum return on investment mode and a mode combining any two or more of the preceding; and
executing a first operational mode from the list of operational mode parameters stored in the control system to operate the fuel cell system in the first operational mode.
24. The method of claim 23, further comprising executing a second operational mode different from the first operational mode from the list of operational mode parameters stored in the control system to operate the fuel cell system in the second operational mode.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009051698A1 (en) 2009-11-03 2011-05-05 Daimler Ag Fuel cell system operating method for drive of e.g. electric vehicle, involves regulating relationship between cathode air supply quantity or rate determined by air supply device and current or power output of fuel cell
WO2022187456A1 (en) * 2021-03-05 2022-09-09 Toyota Motor Engineering & Manufacturing, Inc. Fuel cell power unbalancing to control degradation and improve performance

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8163158B2 (en) * 2008-05-12 2012-04-24 Enrg, Inc. Operation of an electrolysis cell
US8892264B2 (en) 2009-10-23 2014-11-18 Viridity Energy, Inc. Methods, apparatus and systems for managing energy assets
US9159108B2 (en) 2009-10-23 2015-10-13 Viridity Energy, Inc. Facilitating revenue generation from wholesale electricity markets
US8457802B1 (en) 2009-10-23 2013-06-04 Viridity Energy, Inc. System and method for energy management
US9159042B2 (en) 2009-10-23 2015-10-13 Viridity Energy, Inc. Facilitating revenue generation from data shifting by data centers
US9367825B2 (en) 2009-10-23 2016-06-14 Viridity Energy, Inc. Facilitating revenue generation from wholesale electricity markets based on a self-tuning energy asset model
WO2012167093A2 (en) * 2011-06-01 2012-12-06 Enerfuel, Inc. Fuel cell-coupled heating and refrigeration system
WO2013067213A1 (en) * 2011-11-01 2013-05-10 Viridity Energy, Inc. Facilitating revenue generation from wholesale electricity markets
US9171276B2 (en) * 2013-05-06 2015-10-27 Viridity Energy, Inc. Facilitating revenue generation from wholesale electricity markets using an engineering-based model
US9098876B2 (en) 2013-05-06 2015-08-04 Viridity Energy, Inc. Facilitating revenue generation from wholesale electricity markets based on a self-tuning energy asset model
US10199669B2 (en) 2016-01-25 2019-02-05 Micrsoft Technology Licensing, LLC Power modulation for fuel cell powered datacenters

Citations (67)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3488266A (en) * 1967-12-12 1970-01-06 Continental Oil Co Electrochemical reduction of benzene using a carbon anode
US4041210A (en) * 1976-08-30 1977-08-09 United Technologies Corporation Pressurized high temperature fuel cell power plant with bottoming cycle
US4532192A (en) * 1984-11-06 1985-07-30 Energy Research Corporation Fuel cell system
US4792502A (en) * 1986-11-14 1988-12-20 International Fuel Cells Corporation Apparatus for producing nitrogen
US4898792A (en) * 1988-12-07 1990-02-06 Westinghouse Electric Corp. Electrochemical generator apparatus containing modified high temperature insulation and coated surfaces for use with hydrocarbon fuels
US4917971A (en) * 1989-03-03 1990-04-17 Energy Research Corporation Internal reforming fuel cell system requiring no recirculated cooling and providing a high fuel process gas utilization
US4983471A (en) * 1989-12-28 1991-01-08 Westinghouse Electric Corp. Electrochemical cell apparatus having axially distributed entry of a fuel-spent fuel mixture transverse to the cell lengths
US5034287A (en) * 1990-04-23 1991-07-23 International Fuel Cells Corporation Fuel cell cooling using heat of reaction
US5047299A (en) * 1990-07-25 1991-09-10 Westinghouse Electric Corp. Electrochemical cell apparatus having an integrated reformer-mixer nozzle-mixer diffuser
US5084362A (en) * 1990-08-29 1992-01-28 Energy Research Corporation Internal reforming molten carbonate fuel cell system with methane feed
US5143800A (en) * 1990-07-25 1992-09-01 Westinghouse Electric Corp. Electrochemical cell apparatus having combusted exhaust gas heat exchange and valving to control the reformable feed fuel composition
US5170124A (en) * 1990-06-08 1992-12-08 Minister Of National Defence Of Her Majesty's Canadian Government Method and apparatus for monitoring fuel cell performance
US5169730A (en) * 1990-07-25 1992-12-08 Westinghouse Electric Corp. Electrochemical cell apparatus having an exterior fuel mixer nozzle
US5302470A (en) * 1989-05-16 1994-04-12 Osaka Gas Co., Ltd. Fuel cell power generation system
US5441821A (en) * 1994-12-23 1995-08-15 Ballard Power Systems Inc. Electrochemical fuel cell system with a regulated vacuum ejector for recirculation of the fluid fuel stream
US5498487A (en) * 1994-08-11 1996-03-12 Westinghouse Electric Corporation Oxygen sensor for monitoring gas mixtures containing hydrocarbons
US5501914A (en) * 1993-09-01 1996-03-26 Mitsubishi Jukogyo Kabushiki Kaisha Solid oxide electrolyte fuel cell
US5505824A (en) * 1995-01-06 1996-04-09 United Technologies Corporation Propellant generator and method of generating propellants
US5527631A (en) * 1994-02-18 1996-06-18 Westinghouse Electric Corporation Hydrocarbon reforming catalyst material and configuration of the same
US5573867A (en) * 1996-01-31 1996-11-12 Westinghouse Electric Corporation Purge gas protected transportable pressurized fuel cell modules and their operation in a power plant
US5601937A (en) * 1995-01-25 1997-02-11 Westinghouse Electric Corporation Hydrocarbon reformer for electrochemical cells
US5629103A (en) * 1993-04-30 1997-05-13 Siemens Aktiengesellschaft High-temperature fuel cell with improved solid-electrolyte/electrode interface and method of producing the interface
US5686196A (en) * 1996-10-09 1997-11-11 Westinghouse Electric Corporation System for operating solid oxide fuel cell generator on diesel fuel
US5733675A (en) * 1995-08-23 1998-03-31 Westinghouse Electric Corporation Electrochemical fuel cell generator having an internal and leak tight hydrocarbon fuel reformer
US5741605A (en) * 1996-03-08 1998-04-21 Westinghouse Electric Corporation Solid oxide fuel cell generator with removable modular fuel cell stack configurations
US5955039A (en) * 1996-12-19 1999-09-21 Siemens Westinghouse Power Corporation Coal gasification and hydrogen production system and method
US6013385A (en) * 1997-07-25 2000-01-11 Emprise Corporation Fuel cell gas management system
US6033794A (en) * 1997-12-10 2000-03-07 The United States Of America As Represented By The United States Department Of Energy Multi-stage fuel cell system method and apparatus
US6051125A (en) * 1998-09-21 2000-04-18 The Regents Of The University Of California Natural gas-assisted steam electrolyzer
US6280865B1 (en) * 1999-09-24 2001-08-28 Plug Power Inc. Fuel cell system with hydrogen purification subsystem
US20010049035A1 (en) * 2000-05-01 2001-12-06 Haltiner Karl Jacob Solid oxide fuel cell process gas sampling for analysis
US6329090B1 (en) * 1999-09-03 2001-12-11 Plug Power Llc Enthalpy recovery fuel cell system
US20020028362A1 (en) * 2000-09-01 2002-03-07 Dennis Prediger Anode oxidation protection in a high-temperature fuel cell
US20020051898A1 (en) * 2000-09-28 2002-05-02 Moulthrop Lawrence C. Regenerative electrochemical cell system and method for use thereof
US20020058175A1 (en) * 2000-11-15 2002-05-16 Technology Management, Inc. Multipurpose reversible electrochemical system
US6403245B1 (en) * 1999-05-21 2002-06-11 Microcoating Technologies, Inc. Materials and processes for providing fuel cells and active membranes
US20020106544A1 (en) * 2001-02-07 2002-08-08 Noetzel John G. Solid oxide auxiliary power unit reformate control
US6451466B1 (en) * 2000-04-06 2002-09-17 Utc Fuel Cells, Llc Functional integration of multiple components for a fuel cell power plant
US20020142208A1 (en) * 2000-10-30 2002-10-03 Keefer Bowie G. Energy efficient gas separation for fuel cells
US6531243B2 (en) * 1998-09-14 2003-03-11 Forschungszentrum Jülich GmbH Solid oxide fuel operating with an excess of fuel
US6569298B2 (en) * 2000-06-05 2003-05-27 Walter Roberto Merida-Donis Apparatus for integrated water deionization, electrolytic hydrogen production, and electrochemical power generation
US6569549B1 (en) * 2000-11-02 2003-05-27 Utc Fuel Cells, Llc Method for increasing the operational efficiency of a fuel cell power plant
US20030157386A1 (en) * 2002-02-20 2003-08-21 Ion America Corporation Load matched power generation system including a solid oxide fuel cell and a heat pump and an optional turbine
US20030167105A1 (en) * 2000-07-28 2003-09-04 Colborn Jeffrey A. System of and method for power management
US6623880B1 (en) * 2001-05-29 2003-09-23 The United States Of America As Represented By The Department Of Energy Fuel cell-fuel cell hybrid system
US20030196893A1 (en) * 2002-04-23 2003-10-23 Mcelroy James Frederick High-temperature low-hydration ion exchange membrane electrochemical cell
US20030205641A1 (en) * 2002-05-03 2003-11-06 Ion America Corporation Solid oxide regenerative fuel cell for airplane power generation and storage
US20040013923A1 (en) * 2002-02-19 2004-01-22 Trent Molter System for storing and recoving energy and method for use thereof
US20040081859A1 (en) * 2002-10-23 2004-04-29 Ion America Solid oxide regenerative fuel cell
US20040115489A1 (en) * 2002-12-12 2004-06-17 Manish Goel Water and energy management system for a fuel cell
US20040137300A1 (en) * 2002-11-07 2004-07-15 Randall Gemmen Piezoelectric axial flow microvalve
US20040146761A1 (en) * 2002-09-23 2004-07-29 Hydrogenics Corporation Fuel cell system and method of operating the same
US20040191597A1 (en) * 2003-03-24 2004-09-30 Ion America Corporation Solid oxide regenerative fuel cell with selective anode tail gas circulation
US20040191595A1 (en) * 2003-03-24 2004-09-30 Ion America Corporation SORFC system and method with an exothermic net electrolysis reaction
US20040202914A1 (en) * 2003-04-09 2004-10-14 Ion America Corporation Co-production of hydrogen and electricity in a high temperature electrochemical system
US20040219398A1 (en) * 2003-05-02 2004-11-04 Calhoon John C. Fuel cell control and data reporting
US20040224193A1 (en) * 2003-04-09 2004-11-11 Ion America Corporation Method of optimizing operating efficiency of fuel cells
US20050031922A1 (en) * 2003-08-08 2005-02-10 Clingerman Bruce J. Method and apparatus for venting and purging of a fuel cell
US20050048334A1 (en) * 2003-09-03 2005-03-03 Ion America Corporation Combined energy storage and fuel generation with reversible fuel cells
US6887608B2 (en) * 2002-09-06 2005-05-03 Nissan Motor Co., Ltd. Fuel cell system and related operating method
US20050242588A1 (en) * 2004-04-30 2005-11-03 Washington Krik B Integrated fuel cell and additive gas supply system for a power generation system including a combustion engine
US7014932B2 (en) * 2003-03-19 2006-03-21 Proton Energy Systems, Inc. Drainage system and process for operating a regenerative electrochemical cell system
US20060102397A1 (en) * 2002-07-25 2006-05-18 Daimlerchrysler Ag Method and arrangement for controlling the energy supply of a mobile device comprising at least one electric driving motor and a hybrid energy system containing a fuel cell system and a dynamic energy system
US7129674B2 (en) * 2003-08-19 2006-10-31 Matsushita Electric Industrial Co., Ltd. Power supply apparatus having control section for controlling quantity of fuel to be supplied to fuel cell
US20070141416A1 (en) * 2005-12-20 2007-06-21 Peter Kilian Floating base load hybrid strategy for a hybrid fuel cell vehicle to increase the durability of the fuel cell system
US20070199746A1 (en) * 2001-02-16 2007-08-30 Cellex Power Products, Inc. Hybrid power supply apparatus for battery replacement applications
US20080070073A1 (en) * 2006-09-19 2008-03-20 Mark Petersen Fuel cell module power delivery control system

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4052784B2 (en) 2000-08-15 2008-02-27 三洋電機株式会社 Combined heat and power fuel cell power generator and method of operating the same
KR20060093539A (en) 2005-02-22 2006-08-25 삼성에스디아이 주식회사 Fuel cell system and driving method thereof

Patent Citations (73)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3488266A (en) * 1967-12-12 1970-01-06 Continental Oil Co Electrochemical reduction of benzene using a carbon anode
US4041210A (en) * 1976-08-30 1977-08-09 United Technologies Corporation Pressurized high temperature fuel cell power plant with bottoming cycle
US4532192A (en) * 1984-11-06 1985-07-30 Energy Research Corporation Fuel cell system
US4792502A (en) * 1986-11-14 1988-12-20 International Fuel Cells Corporation Apparatus for producing nitrogen
US4898792A (en) * 1988-12-07 1990-02-06 Westinghouse Electric Corp. Electrochemical generator apparatus containing modified high temperature insulation and coated surfaces for use with hydrocarbon fuels
US4917971A (en) * 1989-03-03 1990-04-17 Energy Research Corporation Internal reforming fuel cell system requiring no recirculated cooling and providing a high fuel process gas utilization
US5302470A (en) * 1989-05-16 1994-04-12 Osaka Gas Co., Ltd. Fuel cell power generation system
US4983471A (en) * 1989-12-28 1991-01-08 Westinghouse Electric Corp. Electrochemical cell apparatus having axially distributed entry of a fuel-spent fuel mixture transverse to the cell lengths
US5034287A (en) * 1990-04-23 1991-07-23 International Fuel Cells Corporation Fuel cell cooling using heat of reaction
US5170124A (en) * 1990-06-08 1992-12-08 Minister Of National Defence Of Her Majesty's Canadian Government Method and apparatus for monitoring fuel cell performance
US5047299A (en) * 1990-07-25 1991-09-10 Westinghouse Electric Corp. Electrochemical cell apparatus having an integrated reformer-mixer nozzle-mixer diffuser
US5143800A (en) * 1990-07-25 1992-09-01 Westinghouse Electric Corp. Electrochemical cell apparatus having combusted exhaust gas heat exchange and valving to control the reformable feed fuel composition
US5169730A (en) * 1990-07-25 1992-12-08 Westinghouse Electric Corp. Electrochemical cell apparatus having an exterior fuel mixer nozzle
US5084362A (en) * 1990-08-29 1992-01-28 Energy Research Corporation Internal reforming molten carbonate fuel cell system with methane feed
US5629103A (en) * 1993-04-30 1997-05-13 Siemens Aktiengesellschaft High-temperature fuel cell with improved solid-electrolyte/electrode interface and method of producing the interface
US5501914A (en) * 1993-09-01 1996-03-26 Mitsubishi Jukogyo Kabushiki Kaisha Solid oxide electrolyte fuel cell
US5527631A (en) * 1994-02-18 1996-06-18 Westinghouse Electric Corporation Hydrocarbon reforming catalyst material and configuration of the same
US5498487A (en) * 1994-08-11 1996-03-12 Westinghouse Electric Corporation Oxygen sensor for monitoring gas mixtures containing hydrocarbons
US5441821A (en) * 1994-12-23 1995-08-15 Ballard Power Systems Inc. Electrochemical fuel cell system with a regulated vacuum ejector for recirculation of the fluid fuel stream
US5505824A (en) * 1995-01-06 1996-04-09 United Technologies Corporation Propellant generator and method of generating propellants
US5601937A (en) * 1995-01-25 1997-02-11 Westinghouse Electric Corporation Hydrocarbon reformer for electrochemical cells
US5733675A (en) * 1995-08-23 1998-03-31 Westinghouse Electric Corporation Electrochemical fuel cell generator having an internal and leak tight hydrocarbon fuel reformer
US5573867A (en) * 1996-01-31 1996-11-12 Westinghouse Electric Corporation Purge gas protected transportable pressurized fuel cell modules and their operation in a power plant
US5741605A (en) * 1996-03-08 1998-04-21 Westinghouse Electric Corporation Solid oxide fuel cell generator with removable modular fuel cell stack configurations
US5686196A (en) * 1996-10-09 1997-11-11 Westinghouse Electric Corporation System for operating solid oxide fuel cell generator on diesel fuel
US5955039A (en) * 1996-12-19 1999-09-21 Siemens Westinghouse Power Corporation Coal gasification and hydrogen production system and method
US6013385A (en) * 1997-07-25 2000-01-11 Emprise Corporation Fuel cell gas management system
US6436562B1 (en) * 1997-07-25 2002-08-20 Emprise Technology Associates Corp. Fuel-cell engine stream conditioning system
US6033794A (en) * 1997-12-10 2000-03-07 The United States Of America As Represented By The United States Department Of Energy Multi-stage fuel cell system method and apparatus
US6531243B2 (en) * 1998-09-14 2003-03-11 Forschungszentrum Jülich GmbH Solid oxide fuel operating with an excess of fuel
US6051125A (en) * 1998-09-21 2000-04-18 The Regents Of The University Of California Natural gas-assisted steam electrolyzer
US6403245B1 (en) * 1999-05-21 2002-06-11 Microcoating Technologies, Inc. Materials and processes for providing fuel cells and active membranes
US6329090B1 (en) * 1999-09-03 2001-12-11 Plug Power Llc Enthalpy recovery fuel cell system
US6280865B1 (en) * 1999-09-24 2001-08-28 Plug Power Inc. Fuel cell system with hydrogen purification subsystem
US6451466B1 (en) * 2000-04-06 2002-09-17 Utc Fuel Cells, Llc Functional integration of multiple components for a fuel cell power plant
US20010049035A1 (en) * 2000-05-01 2001-12-06 Haltiner Karl Jacob Solid oxide fuel cell process gas sampling for analysis
US6569298B2 (en) * 2000-06-05 2003-05-27 Walter Roberto Merida-Donis Apparatus for integrated water deionization, electrolytic hydrogen production, and electrochemical power generation
US20030167105A1 (en) * 2000-07-28 2003-09-04 Colborn Jeffrey A. System of and method for power management
US20020028362A1 (en) * 2000-09-01 2002-03-07 Dennis Prediger Anode oxidation protection in a high-temperature fuel cell
US20020051898A1 (en) * 2000-09-28 2002-05-02 Moulthrop Lawrence C. Regenerative electrochemical cell system and method for use thereof
US20020142208A1 (en) * 2000-10-30 2002-10-03 Keefer Bowie G. Energy efficient gas separation for fuel cells
US6569549B1 (en) * 2000-11-02 2003-05-27 Utc Fuel Cells, Llc Method for increasing the operational efficiency of a fuel cell power plant
US20020058175A1 (en) * 2000-11-15 2002-05-16 Technology Management, Inc. Multipurpose reversible electrochemical system
US20020106544A1 (en) * 2001-02-07 2002-08-08 Noetzel John G. Solid oxide auxiliary power unit reformate control
US20070199746A1 (en) * 2001-02-16 2007-08-30 Cellex Power Products, Inc. Hybrid power supply apparatus for battery replacement applications
US6623880B1 (en) * 2001-05-29 2003-09-23 The United States Of America As Represented By The Department Of Energy Fuel cell-fuel cell hybrid system
US20040013923A1 (en) * 2002-02-19 2004-01-22 Trent Molter System for storing and recoving energy and method for use thereof
US20030162067A1 (en) * 2002-02-20 2003-08-28 Ion America Corporation Fuel water vapor replenishment system for a fuel cell
US20030157386A1 (en) * 2002-02-20 2003-08-21 Ion America Corporation Load matched power generation system including a solid oxide fuel cell and a heat pump and an optional turbine
US20030196893A1 (en) * 2002-04-23 2003-10-23 Mcelroy James Frederick High-temperature low-hydration ion exchange membrane electrochemical cell
US20030205641A1 (en) * 2002-05-03 2003-11-06 Ion America Corporation Solid oxide regenerative fuel cell for airplane power generation and storage
US20060102397A1 (en) * 2002-07-25 2006-05-18 Daimlerchrysler Ag Method and arrangement for controlling the energy supply of a mobile device comprising at least one electric driving motor and a hybrid energy system containing a fuel cell system and a dynamic energy system
US6887608B2 (en) * 2002-09-06 2005-05-03 Nissan Motor Co., Ltd. Fuel cell system and related operating method
US20040146761A1 (en) * 2002-09-23 2004-07-29 Hydrogenics Corporation Fuel cell system and method of operating the same
US20040081859A1 (en) * 2002-10-23 2004-04-29 Ion America Solid oxide regenerative fuel cell
US6821663B2 (en) * 2002-10-23 2004-11-23 Ion America Corporation Solid oxide regenerative fuel cell
US20040137300A1 (en) * 2002-11-07 2004-07-15 Randall Gemmen Piezoelectric axial flow microvalve
US20040115489A1 (en) * 2002-12-12 2004-06-17 Manish Goel Water and energy management system for a fuel cell
US7014932B2 (en) * 2003-03-19 2006-03-21 Proton Energy Systems, Inc. Drainage system and process for operating a regenerative electrochemical cell system
US7201979B2 (en) * 2003-03-24 2007-04-10 Bloom Energy Corporation SORFC system and method with an exothermic net electrolysis reaction
US20040191597A1 (en) * 2003-03-24 2004-09-30 Ion America Corporation Solid oxide regenerative fuel cell with selective anode tail gas circulation
US20040191598A1 (en) * 2003-03-24 2004-09-30 Ion America Corporation SORFC power and oxygen generation method and system
US20040191595A1 (en) * 2003-03-24 2004-09-30 Ion America Corporation SORFC system and method with an exothermic net electrolysis reaction
US20040224193A1 (en) * 2003-04-09 2004-11-11 Ion America Corporation Method of optimizing operating efficiency of fuel cells
US20040202914A1 (en) * 2003-04-09 2004-10-14 Ion America Corporation Co-production of hydrogen and electricity in a high temperature electrochemical system
US20060177711A1 (en) * 2003-05-02 2006-08-10 Microsoft Corporation Fuell cell control and data reporting
US20040219398A1 (en) * 2003-05-02 2004-11-04 Calhoon John C. Fuel cell control and data reporting
US20050031922A1 (en) * 2003-08-08 2005-02-10 Clingerman Bruce J. Method and apparatus for venting and purging of a fuel cell
US7129674B2 (en) * 2003-08-19 2006-10-31 Matsushita Electric Industrial Co., Ltd. Power supply apparatus having control section for controlling quantity of fuel to be supplied to fuel cell
US20050048334A1 (en) * 2003-09-03 2005-03-03 Ion America Corporation Combined energy storage and fuel generation with reversible fuel cells
US20050242588A1 (en) * 2004-04-30 2005-11-03 Washington Krik B Integrated fuel cell and additive gas supply system for a power generation system including a combustion engine
US20070141416A1 (en) * 2005-12-20 2007-06-21 Peter Kilian Floating base load hybrid strategy for a hybrid fuel cell vehicle to increase the durability of the fuel cell system
US20080070073A1 (en) * 2006-09-19 2008-03-20 Mark Petersen Fuel cell module power delivery control system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009051698A1 (en) 2009-11-03 2011-05-05 Daimler Ag Fuel cell system operating method for drive of e.g. electric vehicle, involves regulating relationship between cathode air supply quantity or rate determined by air supply device and current or power output of fuel cell
WO2022187456A1 (en) * 2021-03-05 2022-09-09 Toyota Motor Engineering & Manufacturing, Inc. Fuel cell power unbalancing to control degradation and improve performance
US11876262B2 (en) 2021-03-05 2024-01-16 Toyota Motor Engineering & Manufacturing North America, Inc. Fuel cell power unbalancing to control degradation and improve performance

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