Patent Document

This application claims priority from Japanese Patent Application No. 2004-342966, filed Nov. 26, 2004, the entire contents of which is incorporated herein by reference. 
     TECHNICAL FIELD 
     The present disclosure relates to fuel cell systems, more particularly, controlling fuel cell system operation. 
     BACKGROUND 
     In a fuel cell system, a fuel gas such as hydrogen and an oxidizer gas containing oxygen are electrochemically reacted across an electrolyte to produce electrical energy. Conventional fuel cell systems contain one or more unit fuel cells including generally a fuel electrode coated with a redox catalyst layer, an oxidizing electrode coated with a redox catalyst layer, and an electrolyte film separating the electrodes and having a gas passage formed to supply oxidizer gas (e.g. air) to the oxidizing electrode (e.g. cathode) in an oxidizer electrode chamber, and fuel gas (e.g. hydrogen) to the fuel electrode (e.g. anode) in a fuel electrode chamber. 
     Conventional fuel cell systems may include pipes for supplying and exhausting oxidizing gas and fuel gas to and from the fuel cell stack. However, since only a portion of the oxidizing gas and the fuel gas supplied to the fuel cell generally reacts within the respective oxidizing electrode chamber and fuel electrode chamber, the gas exhausted from a fuel cell stack may be rich in unreacted fuel gas and/or oxidizer gas. This leads to fuel cell operating inefficiency and waste of expensive fuel gas. 
     Although various methods have been developed to monitor the exit concentration of the exhaust gas from an operating fuel cell and adjust the operating parameters of the fuel cell system to achieve higher fuel gas conversion, these methods generally require expensive gas concentration detection instrumentation that adds substantially to the cost of a fuel cell system. Moreover, the existing gas concentration monitoring systems may suffer from operating instability and gas detection interferences. For example, gas detection monitors which operate by monitoring the thermal conductivity or infrared absorbance of the exhaust gas may respond non-selectively to gases other than the fuel gas, for example, water vapor or carbon dioxide. This may provide a false indication of the fuel gas concentration in the fuel cell system exhaust and lead to selection of improper fuel cell operating parameters. Selection of improper fuel cell operating parameters can seriously degrade fuel cell operating efficiency, long term cycling performance and fuel cell life. 
     SUMMARY 
     In general, the invention relates to techniques for controlling fuel cell systems during start-up. In certain embodiments, a fuel cell system includes a fuel cell stack having multiple unit fuel cells, a voltage sensor electrically connected to the fuel cell stack, a fuel gas supply conduit, a fuel gas exhaust conduit, a fuel gas recirculation conduit connecting between the fuel gas exhaust conduit and the fuel gas supply conduit at a diversion point, and a fuel gas vent valve positioned in the fuel gas exhaust conduit downstream from the diversion point. The fuel gas vent valve vents at least a portion of the fuel gas within the fuel gas exhaust conduit to an atmosphere external to the fuel cell stack in response to a fuel gas control process executed by a controller in response to a fuel cell operating voltage detected by the voltage sensor. 
     In some exemplary embodiments, the fuel cell system includes a fuel gas recirculation valve positioned to divert a portion of the fuel gas from the fuel gas exhaust conduit and recirculate the diverted portion of the fuel gas to the fuel gas supply conduit. In other exemplary embodiments, the fuel cell system includes a compressor in flow communication with the fuel gas recirculation conduit. In additional exemplary embodiments, a first check valve is positioned in the fuel gas exhaust conduit upstream of the fuel exhaust valve and downstream of the diversion point to allow irreversible flow of fuel gas through the fuel gas exhaust valve. In other additional embodiments, a second check valve is positioned in the fuel recirculation conduit upstream of the first check valve and downstream of the diversion point to allow irreversible flow of fuel gas to the fuel gas supply conduit. 
     In certain other embodiments, a method includes supplying fuel gas to the fuel cell chamber at a fuel cell start-up time with the fuel gas vent valve in an open position, maintaining the fuel gas vent valve in an open position for a time period corresponding to an estimated gas replacement completion time, and closing the fuel gas vent valve after the estimated gas replacement completion time has elapsed. 
     In one exemplary embodiment, the estimated gas replacement completion time is determined as a summation T of a first replacement estimation time T 1  estimating a time from the fuel cell start-up time to the time when the contents of the fuel gas supply conduit are replaced with fuel gas, a second replacement estimation time T 2  estimating a time from the time when the contents of the fuel gas supply conduit are replaced with fuel gas to the time when the contents of the fuel chamber are replaced with fuel gas, and a third replacement estimation time T 3  estimating a time from the time when the contents of the fuel chamber are replaced with fuel gas to the time when the contents of the fuel gas exhaust conduit are replaced with fuel gas. 
     In other exemplary embodiments, the second replacement estimation time T 2  is calculated according to the equation (Vstack/Vin)×T 1 , wherein Vstack is the volume defined by the fuel electrode chamber, Vin is the volume defined by the fuel gas supply conduit, and T 1  is the first replacement estimation time T 1 . The third replacement estimation time T 3  is calculated according to the equation (Vout/Vin)×T 1 , wherein Vout is the volume of the fuel gas exhaust conduit, Vin is the volume of the fuel gas supply conduit, and T 1  is the first replacement estimation time T 1 . In still other exemplary embodiments, the third replacement estimation time T 3  is calculated according to the equation (Vout/Vin)×T 1 , wherein Vout is the volume of the fuel gas exhaust conduit, Vin is the volume of the fuel gas supply conduit, and T 1  is the first replacement estimation time. 
     According to certain additional embodiments, the gas replacement completion time may be estimated based on the voltage information determined by the voltage sensor electrically connected to the fuel cell stack. In certain exemplary embodiments, the second replacement estimation time T 2  may be determined by dividing the voltage sensed by the voltage sensor by the number of unit fuel cells in the fuel cell stack to obtain a voltage per unit fuel cell of the fuel cell stack, performing a linear approximation to the variation in voltage per unit fuel cell as a function of time from start-up to determine initial slope values, and comparing the initial slope values to a target slope value and setting replacement estimation time T 2  to the elapsed time from fuel cell start-up required for the initial slope values to equal the target slope value. In other exemplary embodiments, the target voltage may be changed according to the slope of the linear approximation to the variation in voltage per unit fuel cell as a function of time from start-up when the second replacement estimation time T 2  is determined. 
     In certain embodiments, the fuel cell control methods include supplying fuel gas to the fuel cell chamber of at a fuel cell start-up time with the fuel gas vent valve in an open position, maintaining the fuel gas vent valve in an open position for a time period corresponding to the estimated gas replacement completion time, and closing the fuel gas vent valve after the estimated gas replacement completion time has elapsed. 
     According to the present disclosure, the gas replacement completion time is estimated based on the voltage information determined by a voltage detection means (e.g. a voltage sensor) connected to and monitoring the electric power generation of the fuel cell stack. Therefore, without using a gas concentration sensor, the deterioration of the catalyst layer resulting from exposure to a mixture of fuel gas and oxidizer gas during fuel cell start-up can be controlled, and the reliability and durability of the fuel cell system improved. 
     Certain aspects of the invention may provide fuel cell systems exhibiting improved operating efficiency. Other aspects of the invention may provide lower cost fuel cell systems that may not require gas concentration sensors to monitor fuel conversion efficiency. In other aspects, the invention may provide improved fuel cell system operating and control methods that reduce deterioration of the fuel cell electrode catalyst layers resulting from exposure to the mixture of fuel gas and oxidizer gas during fuel cell start-up. 
     The above summary of the invention is not intended to describe each embodiment or every implementation of the invention. Exemplary embodiments of the invention are described below and illustrated by the following drawings. In particular, each embodiment described below is not limited to fuel cell systems suitable for use in fuel cell powered vehicles. Rather, the invention may also be applied to fuel cell systems for use in other applications. The details of one or more embodiments of the invention are set forth in the accompanying drawings and the description below. Other features, objects, and advantages of the invention will be apparent from the description and drawings, and from the claims. 
    
    
     
       BRIEF DESCRIPTION OF DRAWINGS 
         FIG. 1  is a schematic diagram illustrating a fuel cell system according to a first embodiment. 
         FIG. 2  is a diagram illustrating a characteristic graphical relationship between the fuel cell operating voltage as a function of time measured using a voltage sensor during fuel cell start-up, and describing one embodiment of the estimation procedure for determining the gas replacement completion time. 
         FIG. 3  is a diagram illustrating a characteristic graphical relationship between the fuel cell operating voltage as a function of time measured using a voltage sensor during fuel cell start-up, and describing another embodiment of the estimation procedure for determining the gas replacement completion time. 
         FIG. 4  is a diagram illustrating a characteristic graphical relationship between the fuel cell operating voltage as a function of time measured using a voltage sensor during fuel cell start-up, and describing a further embodiment of the estimation procedure for determining the gas replacement completion time. 
         FIG. 5  is a schematic diagram illustrating a fuel cell system according to another embodiment. 
         FIG. 6  is a schematic diagram illustrating a fuel cell system according to an additional embodiment. 
     
    
    
     DETAILED DESCRIPTION 
       FIG. 1  is a schematic diagram of a first embodiment of a fuel cell system  1 A.  FIG. 2  is a characteristic line graph showing voltage of fuel cell stack  2  upon start of the fuel cell and illustrates an estimation procedure of the gas replacement completion time. 
     In  FIG. 1 , fuel cell system  1 A is equipped with fuel cell stack  2 . Fuel cell stack  2  is equipped with fuel electrode  3  facing the fuel chamber and oxidizer electrode  4  facing the oxidizer gas chamber. In fuel cell stack  2 , the voltage detection means  30  (for example, a voltage sensor) is electrically connected to the fuel cell system  1 A and detects a voltage produced by the electric power generation of fuel electrode  3  and oxidizer electrode  4 . The voltage detected by the voltage detection means  30  is output to a controller  40 . 
     With respect to fuel gas supply conduit (e.g. fuel gas supply means)  5 , one end is connected to fuel tank  6 , and the other end is connected to the entry of the fuel chamber of the fuel cell stack  2 . Fuel gas (e.g. hydrogen gas) is used to fill fuel tank  6 . The fuel gas supply valve  7  is positioned in fuel gas supply conduit  5 . The fuel gas supply valve  7  can adjust the flow volume and pressure of fuel gas supplied from fuel tank  6  to fuel cell stack  2  under process control by controller  40 . 
     With respect to fuel gas exhaust conduit (fuel gas exhaust means)  8 , one end is connected to the exit of the fuel chamber of fuel cell stack  2 , and the other end is open to the outside air. Return check valve  9  and fuel gas vent valve  10  are positioned in flow communication with fuel gas exhaust conduit  8 , close to the vent to the outer atmosphere. Return check valve  9  prevents the outside air from flowing back into fuel gas exhaust conduit  8 . The fuel gas vent valve  10  opens and closes fuel gas exhaust conduit  8  and is controlled by controller  40 . 
     With respect to fuel gas recirculation conduit (fuel gas recirculation means)  11 , one end is connected at an upstream position relative to the fuel gas vent valve  10  and return check valve  9  of fuel gas exhaust conduit  8 . The other end is connected to the fuel gas supply conduit  5  at a downstream position relative to the fuel gas supply valve  7  of fuel gas supply conduit  5 . More specifically, fuel gas recirculation conduit  11  diverges from fuel gas exhaust conduit  8  at a diversion point and recirculates fuel gas to fuel gas supply conduit  5 . 
     In some embodiments, the length of fuel gas recirculation conduit  11  may be set, at least, to be shorter than the length of fuel gas exhaust conduit  8 . Return check valve  12  may be positioned in fuel gas recirculation conduit  11 . Return check valve  12  prevents fuel gas from flowing out to fuel gas exhaust conduit  8  without passing through fuel cell stack  2  from fuel gas supply conduit  5  during steady-state fuel cell operation. 
     With respect to oxidizer gas supply conduit (oxidizer gas charging means)  13 , one end is open to the outside environment (e.g. the external air), and the other end is connected to the entry of the oxidizer gas chamber of fuel cell stack  2 , Oxidizer gas compressor  14  is connected to oxidizer gas supply conduit  13 . With this oxidizer gas compressor  14 , an oxidizer gas (e.g. the ambient air from an external environment) may be supplied to fuel cell stack  2  through oxidizer gas supply conduit  13 . The operation of oxidizer gas compressor  14  may be controlled by controller  40 . 
     With respect to oxidizer gas exhaust conduit (oxidizer gas exhaust means)  15 , one end is connected to the exit of the oxidizer gas chamber of fuel cell stack  2 , and the other end is open to the outside environment (e.g. the external air) In the above fuel cell system  1 A, oxidizer gas exhausted through the oxidizer gas conduit  15  from the oxidizer electrode  4  may be recirculated for reuse in the oxidizer chamber of the fuel cell (not shown in  FIG. 1 ) provided that the water generated by reaction of oxidizer and fuel in the fuel cell system  1 A is removed. Alternatively, the oxidizer exhaust gas may be combined with the fuel gas exhaust downstream of the fuel gas vent valve  10  (not shown in  FIG. 1 ) in order to dilute unreacted fuel in the fuel gas exhaust. 
     The controller  40  controls fuel cell system  1 A as described above. For example, the controller  40  executes a fuel gas control process in response to a voltage detected by the voltage sensor (voltage detection means)  30  during fuel cell start-up. In one embodiment, the fuel gas control process includes supplying fuel gas to the fuel cell chamber at a fuel cell start-up time with the fuel gas vent valve in an open position, maintaining the fuel gas vent valve in an open position for a time period corresponding to the estimated gas replacement completion time, and closing the fuel gas vent valve after the estimated gas replacement completion time has elapsed. 
     In addition, controller  40  estimates a gas replacement completion time T (i.e., the time elapsed from the time when the fuel supply to fuel gas supply conduit  5  to fuel cell stack  2  starts to the time when the oxidizer gas is substantially completely replaced with fuel gas in fuel gas supply conduit  5 , the fuel chamber of fuel cell stack  2 , and fuel gas exhaust conduit  8 ) based on the voltage detection information of the voltage detection means  30 . The gas replacement operation and the estimation procedure of the gas replacement completion time are described in further detail below. 
     Operation of the above fuel cell system  1 A upon fuel cell start-up will now be described. When the fuel cell start mode is initiated by the controller  40 , the controller  40  opens the valve  10  for the fuel gas exhaust conduit  8  and starts to supply fuel gas from fuel tank  6 . The valve  7  for the fuel gas supply volume adjustment remains closed until the pressure of this fuel gas reaches a higher pressure than normal operation. When the pressure of fuel gas reaches a set high pressure, controller  40  opens the valve  7  for the fuel gas supply volume adjustment to start the fuel supply. The high pressure fuel gas flows into fuel gas supply conduit  5 , the fuel chamber of fuel cell stack  2  and the fuel gas exhaust conduit  8  in that order. The oxidizer gas is replaced with fuel gas in this manner. 
     The controller  40  estimates the gas replacement completion time T, that is the elapsed time from fuel cell start-up to the time when the contents of fuel gas supply conduit  5 , the fuel chamber of fuel cell stack  2 , and fuel gas exhaust conduit  8  are replaced with fuel gas. As illustrated in  FIG. 2 , in one embodiment the controller  40  determines and stores a fuel supply start time (time a), and monitors the detected voltage of the voltage detection means  30  after the fuel supply starts. In addition, the controller  40  detects and stores the point in time where the detected voltage of the voltage detection means  30  starts to rise from zero (time b). The controller  40  then estimates the gas replacement completion time T, e.g., by using one of the following exemplary estimation methods. 
     As shown in  FIG. 2 , controller  40  may compute the estimated gas replacement completion time T as a summation of the first replacement estimation time T 1 , which is measured from the time when the fuel supply starts to the time when the contents of the fuel gas supply conduit  5  are replaced with fuel gas; the second replacement estimation time T 2 , which is measured from the time when the contents of the fuel gas supply conduit  5  are replaced with fuel gas to the time when the contents of the fuel chamber of fuel cell stack  2  are replaced with fuel gas; and the third replacement estimation time T 3 , which is measured from the time when the contents of the fuel chamber of fuel cell stack  2  are replaced with fuel gas to the time when the contents of the fuel gas exhaust conduit  8  are replaced with fuel gas. 
     The first replacement estimation time T 1  may be determined by time point “b” in  FIG. 2 , which is measured from time point “a” in  FIG. 2  when the fuel supply is started, to the time when the detected voltage of the voltage detection means  30  first starts to rise. The second replacement estimation time T 2  may be determined by the following calculation: the volume of the fuel chamber of fuel cell stack  2 , Vstack, is divided by the volume of fuel gas supply conduit  5 , Vin, and the divided value is multiplied by first replacement estimation time T 1 , that is, T 2 =(Vstack/Vin)×T 1 . The third replacement estimation time T 3  may be determined by the following calculation: the volume of fuel gas exhaust conduit  8 , Vout, divided by the volume of fuel gas supply conduit  5 , Vin, and the resultant value multiplied by first replacement estimation time T 1 , that is T 3 =(Vout/Vin)×T 1 . 
     When the controller  40  reaches the estimated gas replacement completion time T, the controller closes fuel gas vent valve  10 . As a result, the controller  40  prevents fuel gas from being exhausted to the outside air upon determining that the replacement of oxidizer gas by fuel gas in the fuel gas supply conduit  5  is completed. If the fuel gas vent valve  10  is closed, fuel gas in fuel gas exhaust conduit  8  returns to fuel gas supply conduit  5  through fuel gas recirculation conduit  11  and is re-supplied to fuel cell stack  2 . 
     In addition, the controller  40  starts to drive oxidizer gas compressor  14  after fuel gas vent valve  10  is closed. An oxidizer gas (e.g. air) is thus supplied to fuel cell stack  2  soon after the contents of fuel gas supply conduit  5 , the fuel chamber of fuel cell stack  2 , and fuel gas exhaust conduit  8  are replaced with fuel gas, and the electric power generation starts. Also, the controller  40  checks the detected voltage of the voltage detection means  30  upon expiration of the estimated gas replacement completion time. Controller  40  then adjusts the drive power of oxidizer gas compressor  14  so that the amount of oxidizer gas supplied is increased as this detected voltage is reduced. 
     In one embodiment, the gas replacement completion time can be estimated based on the voltage information obtained from the voltage detection means  30  electrically connected to the fuel cell stack  2  and positioned to detect voltage produced by the electric power generation of fuel cell stack  2 . Fuel gas is supplied to fuel cell stack  2  by opening fuel gas vent valve  10  when the fuel cell is started up; the gas replacement completion time (that is, the elapsed time from the time when the fuel supply to fuel cell stack  2  starts to the time when an oxidizer gas is replaced with fuel gas in fuel gas supply conduit  5 , fuel chamber of fuel cell stack  2 , and fuel gas exhaust conduit  8 ) is estimated using the voltage provided by the voltage detection means  30 ; and fuel gas vent valve  10  is set to the closing position upon passage of the estimated gas replacement completion time relative to the start-up time. 
     Thus, the deterioration of the catalyst layer by exposure to a mixture of fuel gas and an oxidizer gas upon fuel cell start-up may be controlled without using an expensive and potentially unreliable gas concentration sensor, and the reliability and durability of fuel cell system  1 A may be improved. Since process control of fuel cell system  1 A is performed by controller  40  based on voltage information from the voltage detection means  30 , accurate recognition of the gas replacement time can be improved, and it may be possible to prevent unnecessary waste of expensive fuel gas in the fuel gas exhaust, thereby improving fuel cell operating efficiency and reducing operating cost. 
     In this first embodiment, the estimated gas replacement completion time may be determined as a summation T of the first replacement estimation time T 1 , which is the elapsed time period from the time when the fuel supply starts to the time when the contents of fuel gas supply conduit  5  are replaced with fuel gas; the second replacement estimation time T 2 , which is the elapsed time period from the time when the contents of fuel gas supply conduit  5  are replaced with fuel gas to the time when the contents of the fuel chamber of fuel cell stack  2  are replaced with fuel gas; and third replacement estimation time T 3 , which is the elapsed time period from the time when the contents of the fuel chamber of fuel cell stack  2  are replaced with fuel gas to the time when the contents of fuel gas exhaust conduit  8  are replaced with fuel gas. 
     The first replacement estimation time T 1  may be determined by the elapsed time from the time when the fuel supply starts to the time when the detected voltage of the voltage detection means  30  starts to rise. The second replacement estimation time T 2  may be determined by the following formula: the volume of the fuel chamber of fuel cell stack  2 , Vstack, is divided by the volume of fuel gas supply conduit  5 , Yin, and the divided value is multiplied by first replacement estimation time T 1 , that is, T 2 =(Vstack/Vin)×T 1 . The third replacement estimation time T 3  may be determined by the following formula: the volume of fuel gas exhaust conduit  8 , Vout, is divided by the volume of fuel gas supply conduit  5 , Vin, and the divided value is multiplied by the first replacement estimation time T 1 , that is T 3 =(Vout/Vin)×T 1 . 
     This estimation procedure can perform accurate estimations because the replacement speed of fuel gas can be determined by detecting the time point where fuel gas reaches the inside of fuel cell stack  2 , using the fuel cell system operating voltage information determined by the voltage detection means  30 . Thus, the estimated gas replacement completion time T can be simply estimated using the measured gas replacement speed and the known conduit volumes. 
     In this first embodiment, since the length of fuel gas recirculation conduit  11  is set to be shorter in comparison with the length of fuel gas exhaust conduit  8 , components that potentially need replacing due to deterioration can be reduced as much as possible. Therefore, the amount of a gas mixture of fuel gas and an oxidizer gas in the fuel electrode chamber upon start of the fuel cell may be reduced, and the deterioration of the catalyst layer resulting from exposure to the mixture of fuel gas and oxidizer gas on fuel cell system start-up may be reduced or prevented. As for the length of fuel gas recirculation conduit  11 , a shorter length may be preferable. 
     In another related embodiment, the pressure of fuel gas supplied to the fuel cell stack upon fuel cell start-up may be increased above the normal supply pressure (e.g. the steady state supply pressure) when the fuel cell is started-up. Consequently, the rate that fuel is supplied to the fuel cells can be increased. As a result, the gas replacement process may be performed quickly and accurately. Preferably, the initial setting pressure of valve for the fuel gas supply volume adjustment  7  upon start of the fuel cell is set to as high a pressure as possible in consideration of resist pressure of the fuel cell system (e.g. a plurality of unit fuel cells), so as to carry out fast fuel gas replacement. 
     In yet another related embodiment, the supply of oxidizer gas to the oxidizer gas chamber of fuel cell stack  2  may be started soon after the estimated gas replacement completion time has elapsed, so that electric power generation by the fuel cell system  1 A can be achieved sooner, without facilitating the deterioration of the catalyst layer by exposure to a mixture of fuel gas and oxidizer gas upon start of the fuel cell. Thus, the fuel cell system start-up performance may be improved. Because the voltage of the voltage detection means  30  may be detected upon reaching the estimated gas replacement completion time point, and the amount of oxidizer gas supplied gets larger as this detected voltage is lower, electric power generation can be achieved more rapidly, regardless of the voltage level upon completion of the gas replacement completion time. 
     Another exemplary estimation procedure for gas replacement completion time T will now be described with respect to  FIG. 3 . In  FIG. 3 , the estimated gas replacement completion time T is a summation of first replacement estimation time T 1 , a second replacement estimation time T 2  and a third replacement estimation time T 3 . The first replacement estimation time T 1  is measured from the time point a when the fuel supply starts to the time when the contents of fuel gas supply conduit  5  are replaced with fuel gas at time point b. The second replacement estimation time T 2  is measured from the time point b up to the time when the contents of the fuel chamber of fuel cell stack  2  are replaced with fuel gas. The third replacement estimation time T 3  is measured from the time when the contents of the fuel chamber of fuel cell stack  2  are replaced with fuel gas up to the time when the contents of fuel gas exhaust conduit  8  are replaced with fuel gas. 
     The first replacement estimation time T 1  may be determined by the time elapsed from when the fuel supply starts (point a in  FIG. 3 ), to the time when the detected voltage of the voltage detection means  30  starts to rise (point b in  FIG. 3 ). The second replacement estimation time T 2  may be determined by the time elapsed from when the contents of the fuel gas supply to the time when the detected voltage value reaches a target voltage, which may be determined in the following manner: (1) dividing the voltage sensed by the voltage sensor  30  by the number of unit fuel cells in the fuel cell stack  1 A to obtain a voltage per unit fuel cell of the fuel cell stack  1 A; performing a linear approximation to the variation in voltage per unit fuel cell as a function of time from start-up to determine initial slope values (e.g. in the voltage zone of 0.2V-0.3 V in  FIG. 3 ); and (2) comparing the initial slope values to a target slope value and setting replacement estimation time T 2  to the elapsed time from fuel cell start-up required for the linear approximation based on the initial slope values to reaches a set target voltage (e.g. 0.9V in  FIG. 3 ). The third replacement estimation time T 3  may be determined by the following formula: the volume of fuel gas exhaust conduit  8 , Vout, is divided by the volume of fuel gas supply conduit  5 , Vin, and the resultant value is multiplied by the first replacement estimation time T 1 , i.e., T 3 =(Vout/Vin)×T 1 . 
     The gas replacement completion time T may thus be estimated more certainly and accurately regardless of the operational state of fuel cell stack  2  (e.g. immediately after starting the fuel cell system) when determined based on the measured operating voltage change of fuel cell stack  2 . The target voltage may generally be selected to be a voltage corresponding to steady state operation of the fuel cell stack after oxidizer gas is provided to the oxidizer electrode chamber in quantities sufficient to achieve a steady measured fuel cell system operating voltage. 
     Yet another example estimation procedure for determining gas replacement completion time T will now be described. This estimation procedure is similar to the other estimation procedures described above, with the primary difference that the target voltage is determined from the slope of the linear approximation to the variation in voltage per unit fuel cell as a function of time from start-up to the second replacement estimation time T 2 . 
     As shown in  FIG. 4 , the slope of the approximate line may generally be determined by prior experimentation, and the target voltage may be determined according to the slope of the approximate line calculated. The target voltage may then be set to be lower as the initial slope of the approximate line decreases (e.g. in the order of Example 1&gt;Example 2&gt;Example 3 in  FIG. 4 ). With this method, even in the case in which, for example, an oxidizer gas is not provided to the oxidizer electrode, the gas replacement completion time can be appropriately estimated, and an appropriate fuel cell system start-up can be performed. 
       FIG. 5  is a schematic diagram of a fuel cell system relating to a second embodiment. In  FIG. 5 , fuel cell system  1 B of this second embodiment differs from that of  FIG. 1  in that a circulation compressor  20  is positioned in the fuel gas exhaust conduit  8 . Other components are the same with respect to  FIG. 1 , so the detailed description of  FIG. 5  has been omitted to avoid duplication. The reference numerals in  FIG. 5  refer to the same elements and structures as referenced in  FIG. 1 . 
     Start-up operations of the fuel cell in fuel cell system  18  of this second embodiment are similar to the first embodiment ( FIG. 1 ), and the same influences and effects as the first embodiment can be obtained. The difference in operation upon start-up of the fuel cell is that circulation compressor (fuel gas circulation means)  20  is put in action before opening the fuel gas supply valve  7 . More specifically, since circulation compressor  20  is put in action when fuel gas is supplied to fuel cell stack  2 , fuel gas from fuel tank  6  fast and certainly reaches fuel gas supply conduit  5 , the fuel chamber of fuel cell stack  2  and fuel gas exhaust conduit  8  to perform the gas replacement. Therefore, the deterioration of the catalyst layer by the mixture of fuel gas and an oxidizer gas when the fuel cell is started can be further controlled. In this second embodiment, circulation compressor (fuel gas circulation means)  20  is positioned in fuel gas exhaust conduit  8 , but the same influences and effects can be obtained even by setting it upstream of the valve  12  for fuel gas recirculation conduit  11 . 
       FIG. 6  is a schematic diagram of fuel cell system  1 C relating to the third embodiment. In  FIG. 6 , fuel cell system  1 C of this third embodiment differs in the point that valve  21  for the fuel gas recirculation conduit  11  is positioned by changing fuel gas recirculation conduit  11  to a return check valve comparable with the one  10  in the second embodiment. Since other components are the same, the explanations have been omitted to avoid duplication. In addition, the same codes point to the same structure items in  FIG. 6 . 
     Start-up operations of the fuel cell in fuel cell system  1 C of this third embodiment are similar to the second embodiment described in  FIG. 5 , and the same influences and effects as the second embodiment can be obtained. The difference in operation upon start-up of the fuel cell is that fuel gas is also supplied to fuel gas recirculation conduit  11  by opening the valve  21  for the fuel gas recirculation conduit  11  as well, when the fuel gas vent valve  10  is opened. Fuel gas flows through the valve  21  for the fuel gas recirculation conduit  11 , and the gas replacement of all fuel conduits may thereby be performed. Therefore, the mixture gas of fuel gas and an oxidizer gas can be prevented from being supplied to the fuel cell stack, and the deterioration by the mixture gas can be certainly controlled. 
     Also, since circulation compressor  20  utilized as in the second embodiment, the fuel gas is more effectively circulated in fuel gas recirculation conduit  11 . The fuel gas vent valve  10  is closed at the estimated gas replacement completion time T, but the valve  21  for the fuel gas recirculation conduit  11  is closed sooner. 
     Various embodiments of the invention have been described. These and other embodiments are within the scope of the following claims.

Technology Category: 5