Method of controlling operation of fuel cell power supply

• US 5,290,641 A
• Filed: 05/21/1992
• Issued: 03/01/1994
• Est. Priority Date: 10/06/1989
• Status: Expired due to Term

• Current Assignee: Fuji Electric Company Limited (Fuji Electric Systems Company Limited)
• Original Assignee: Fuji Electric Company Limited (Fuji Electric Systems Company Limited)
• Inventors: Harashima, Kouichi
• Primary Examiner(s): Willis, Jr., Prince
• Assistant Examiner(s): NUZZOLILLO, MARIA
• Application Number:
  US07/886,607
• Time in Patent Office: 649 Days
• Field of Search: 429/17, 429/20, 429/24
• US Class Current: 429/431
• CPC Class Codes: H01M 8/04089 of gaseous reactants
• CPC Class Codes: H01M 8/0612 from carbon-containing material
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

A fuel cell power supply in which the flow rates of reactant gases are set at flow rates required for a steady state operation plus predetermined extra amounts when an output power increase command is issued. This increase in the flow rates of the reactant gases reduces the consumption ratios of the hydrogen and oxygen to values different from those employed in the steady state operation. This makes it possible to compensate an output voltage drop due to a low temperature of the fuel cell during some time period after the command is issued, thus preventing an overload of the fuel cell.

Claims

1. A method of controlling the operation of a fuel cell power supply having a fuel cell, a reformed gas supply system for supplying the fuel cell with reformed gas at a flow rate Q, an air system for supplying the fuel cell with reactant air at a flow rate Q'"'"', a power inverting system for inverting the output of the fuel cell and supplying the inverted output power to an external load, and a control system for controlling these systems in response to a command externally applied to increase or decrease the output power of said fuel cell, said method comprising the steps of:

calculating a reference current and a reference voltage in accordance with a reference power designated by said command to increase the output power on the basis of I-V characteristic curves of said fuel cell store in said control system;

calculating a first reference flow rate Q₂ of said reformed gas and a first reference flow rate Q₂ '"'"' of said reactant air to be supplied to said fuel cell in accordance with said reference current;

adding to said first reference flow rates Q₂ and Q₂ '"'"' a predetermined amount q of said reformed gas and a predetermined amount g'"'"' of said reactant air, respectively, to obtain a second reference flow rate Q₃ of said reformed gas and a second reference flow rate Q₃ '"'"' of said reactant air to be supplied to said fuel cell;

increasing said flow rates Q and Q'"'"' of said reformed gas and said reactant air by controlling said reformed gas supply system and said air system in accordance with said second reference flow rates Q₃ and Q₃ '"'"';

detecting the flow rates Q and Q'"'"' of said reformed gas and said reactant air respectively to find a first timing when said detected flow rates reach said second reference flow rates Q₃ and Q₃ '"'"' respectively;

detecting an output current, an output voltage and a temperature of said fuel cell;

controlling said fuel cell, said reformed gas supply system, said air system, and said power inverting system in accordance with said second reference flow rates Q₃ and Q₃ '"'"' and said reference power provided by said command from said first timing to a second timing when the temperature of said fuel cell reaches a predetermined steady state operation temperature corresponding to said reference current; and

controlling said fuel cell, said reformed gas supply system, said air system, and said power inverting system in accordance with said first reference flow rates Q₂ and Q₂ '"'"', said reference current, and the output current of said fuel cell after said second timing.

2. A method of controlling the operation of a fuel cell power supply having a fuel cell, a reformed gas supply system for supplying the fuel cell with reformed gas at a flow rate Q, an air system for supplying the fuel cell with reactant air at a flow rate Q'"'"', a power inverting system for inverting the output of the fuel cell and supplying the inverted output power to an external load, and a control system for controlling these systems in response to a command externally applied to increase or decrease the output power of said fuel cell, said method comprising the steps of:

calculating a reference current and a reference voltage in accordance with a reference power designated by said command to increase the output power on the basis of I-V characteristic curves of said fuel cell stored in said control system;

calculating a first reference flow rate Q₂ of said reformed gas and said reactant air to be supplied to said fuel cell in accordance with said reference current;

adding to said first reference flow rates Q₂ and Q₂ '"'"' a predetermined amount q of said reformed gas and a predetermined amount q'"'"' of said reactant air, respectively, to obtain a second reference flow rate Q₃ of said reformed gas and a second reference flow rate Q₃ '"'"' of said reactant air to be supplied to said fuel cell;

increasing said flow rates Q and Q'"'"' of said reformed gas and said reactant air respectively by controlling said reformed gas supply system and said air system in accordance with said second reference flow rates Q₃ and Q₃ '"'"' respectively;

detecting the flow rates Q and Q'"'"' of said reformed gas and said reactant air respectively to find a first timing when said detected flow rates reach said second reference flow rates Q₃ and Q₃ '"'"';

detecting an output current, an output voltage and a temperature of said fuel cell;

controlling said fuel cell, said reformed gas supply system, said air system, and said power inverting system in accordance with said second reference flow rates Q₃ and Q₃ '"'"' and said reference voltage from said first timing to a second timing when the temperature of said fuel cell reaches a predetermined steady state operation temperature corresponding to said reference current, so that said output voltage is maintained at said reference voltage; and

controlling said fuel cell, said reformed gas supply system, said air system, and said power inverting system in accordance with said first reference flow rates Q₂ and Q₂ '"'"', said reference current, and the output current of said fuel cell after said second timing.