Method and apparatus for simultaneous controlling of fuel concentration and temperature of liquid fuel by sensor-less and temperature-control based feed-back control, liquid fuel cell apparatus using the same

Patent metadata

Field	Value
Publication number	US-10079395-B2
Application number	US-201314093614-A
Country	US
Kind code	B2
Filing date	Dec 2, 2013
Priority date	Nov 30, 2012
Publication date	Sep 18, 2018
Grant date	Sep 18, 2018

Abstract

A concentration of a fuel supplied to a fuel cell and a heat exchange rate of a heat exchanger are controlled simultaneously in order to maintain a temperature of fuel cell stack and a diluted fuel concentration that is supplied to the fuel cell stack in a target level. Further, by appropriately responding to an exterior temperature changes or unexpected fuel cell performance changes, it is possible to improve a system efficiency and stability of fuel cell operation and to regulate the fuel concentration quickly and accurately compared to a prior sensor-less concentration controller.

First claim

What is claimed is:

1. A method for simultaneously controlling a fuel concentration and a temperature of liquid fuel cell by using a temperature-control based feed-back control without using a concentration sensor, comprising:
obtaining a database by measuring a fuel consumption rate or speed according to an operating condition of a liquid fuel cell, and preparing a fuel consumption equation according to operating conditions based on the database (S 1 );
determining a fuel consumption rate or speed in a given operating condition based on the fuel consumption equation determined in Step S 1 , and determining an undiluted fuel feed amount or speed corresponding to the determined fuel consumption rate or speed (S 2 );
setting a target temperature (T f ) and selecting either a target-condition control mode or a present-condition control mode, and supplying an undiluted fuel to a fuel mixer in an undiluted fuel feed amount or speed determined according to the selected mode, and then supplying thus made diluted fuel in the fuel mixer to a stack of the fuel cell to start an operation of the fuel cell (S 3 );
fixing the target-condition control mode so that the undiluted fuel is supplied accordingly if the temperature of the stack reaches a predetermined intermediate temperature (T i ) lower than the target temperature (T f ), and simultaneously performing a feed-back control to a heat removal rate of a heat exchanger comparing the present temperature of the fuel cell stack with the target temperature so that the temperature of the fuel cell stack is maintained in a normal state where the temperature of the fuel cell stack is within a preset error bound from the target temperature (T f ) (S 4 ); and
increasing or decreasing the undiluted fuel flux or flow rate fixed according to the target-condition control mode in S 4 , if the fuel cell is in an abnormal state where the temperature (T) of the fuel cell stack deviates from the preset error bound from the target temperature (T f ) although the heat exchanger operates in a maximum manner or in a minimum manner, by feed-back control comparing the present temperature of the fuel cell stack with the target temperature so that the temperature of the fuel cell stack comes back to the normal state where the temperature (T) of the fuel cell stack is within a preset error bound from the target temperature (T f ).

2. The method according to claim 1 , wherein in the step S 1 , the fuel consumption rate or speed of Step S 1 is determined as the sum of a fuel consumption rate or speed required for generating a current at the fuel cell and an inevitable fuel loss rate or speed when the fuel cell is in operation.

3. The method according to claim 2 , wherein the fuel consumption rate or speed required for generating a current is determined by a measured current value according to the operation of the fuel cell and a Faraday constant.

4. The method according to claim 2 , wherein the inevitable fuel loss rate is determined as the sum of fuel losses caused by crossover of a fuel passing from anode to cathode of the fuel cell and a fuel loss caused by evaporation at a gas-liquid separator and/or a fuel mixer.

5. The method according to claim 1 , wherein in the step S 3 , if temperature (T) of the fuel cell stack is lower than the intermediate temperature (T i ), an output power of the heat exchanger is set to be 0 (zero), and in the step S 4 , if temperature (T) of the fuel cell stack is equal to or higher than the intermediate temperature (T i ), the heat exchanger starts to perform heat exchange.

6. The method according to claim 1 , wherein in the step S 4 , the intermediate temperature (T i ) is lower than the target temperature (T f ), by 5 to 30° C.

7. The method according to claim 1 , wherein when the fuel cell is being operated, the method further comprises determining whether to stop an operation of the fuel cell based on an output voltage of the fuel cell stack and/or a temperature of the fuel cell stack, and the operation of fuel cell is stopped if the output voltage is lower than a minimum output voltage (V min ) or the temperature of the fuel cell stack exceeds an upper limit.

8. The method according to claim 7 , wherein the minimum output voltage (V min ) is 0.1˜0.2V, and the upper limit of temperature is 80 to 100° C.

9. The method according to claim 1 , wherein in the step S 3 and S 4 , the feed-back control manner is respectively one or combination of P, PI or PID.

10. The method according to claim 1 , wherein, in a startup stage, controlling an output current is further performed, and
in a region where an output current density (I) is lower than a final output current density (I st ), the output current density is increased by each increment (ΔI) of 5 to 100 mA/cm 2 , if an elapsed time (t) reaches a holding time (t h ), and
in each increasing stage, if the voltage change rate (dV/dt) reaches the first voltage change rate (P1) while the current is constantly maintained, then the output current density is not increased until the corresponding voltage change rate (dV/dt) reaches the second voltage change rate (dV/dt) (P2), wherein P2 is smaller than P1, and after reaching the second voltage change rate (dV/dt) (P2), the output current density is increased by the increment (ΔI) even before the elapsed time (t) reaches the holding time (t h ), and
the above process is repeated to reach the final target output current density.

11. An apparatus for simultaneously controlling a fuel concentration and a temperature of liquid fuel cell by using a temperature-control based feed-back control without using a concentration sensor, comprising a microprocessor, the microprocessor being programmed to perform:
determining a fuel consumption rate or consumption speed in a given operating condition based on a database of fuel consumption rates or consumption speeds of the liquid fuel cell, which database is determined according to operating condition, and determining an undiluted fuel flux or flow rate corresponding to the fuel consumption rate or consumption speed;
selecting any one of the target-condition control mode and the present-condition control mode and starts an operation of fuel cell by supplying an undiluted fuel at a flux or flow rate determined accordingly;
fixing the target-condition control mode so that the undiluted fuel is supplied accordingly if the temperature of the fuel cell stack reaches a predetermined intermediate temperature (T i ) lower than the target temperature (T f ), and performing a feed-back control to a heat removal rate of the heat exchanger comparing the present temperature of the fuel cell stack with the target temperature so that the temperature of the fuel cell stack is maintained in a normal state where the temperature of the fuel cell stack is within a preset error bound from the target temperature (T f ); and
increasing or decreasing the undiluted fuel flux or flow rate fixed according to the target-condition control mode, if the temperature of the fuel cell stack deviates from the preset error bound from the target temperature, by feed-back control comparing the present temperature of the fuel cell stack with the target temperature so that the temperature of the fuel cell stack comes back to a normal state where the temperature of the fuel cell stack is within a preset error bound from the target temperature (T f ).

12. The apparatus according to claim 11 , wherein the microprocessor comprises:
a storage unit in which a database is built with fuel consumption rates or consumption speeds of the liquid fuel cell determined according to operating conditions of the fuel cell;
a first processing unit which is programmed

Assignees

• Korea Inst Sci & Tech

Inventors

• Ha Heung Yong
• An Myunggi
• Kim Woon Jo

Classifications

• H01M8/0432

  Temperature; Ambient temperature · CPC title

• H01M8/04798

  of fuel cell reactants · CPC title

• H01M8/04753

  of fuel cell reactants · CPC title

• H01M8/04186 Primary

  of liquid-charged or electrolyte-charged reactants · CPC title

• H01M8/1009

  with one of the reactants being liquid, solid or liquid-charged (H01M8/12 takes precedence) · CPC title