Patent Application
20130183600
The present invention pertains to a fuel cell device, and more particularly to a fuel cell device capable of adjusting the fuel cell stack temperature using generating air.
In conventional fuel cell devices if a fuel cell stack temperature temporarily rose due to a load following operation of a fluctuating power load, a control was implemented to increase the supplied amount of generating air, which is an oxygen-containing gas, in order to maintain the cell stack temperature in an appropriate temperature range (for example, see Patent Citation 1). In the device described in Patent Citation 1, operation of the device is stopped when an elevated cell stack temperature fails to return to an appropriate temperature range, regardless of any increase in the amount of generating air supplied. Patent Citation 1: Published Unexamined Application 2007-287633
Cell stack temperatures do rise temporarily due to power load increases as described above, but they also rise due to degradation of fuel cells. For example, if the effective electrode surface area usable to implement generating reactions is reduced due to a degradation of the fuel cell unit such as peeling of the electrode layer, a portion of the fuel gas intended to be supplied for generation would normally be combusted as exhaust gas without being supplied for electrical generation, and the amount of heat emitted due to combustion would increase. This causes the cell stack temperature to rise. Also, this degradation-induced temperature rise would be permanent, not temporary.
Therefore a control was conventionally implemented to simply increase the generating air supply amount so as to maintain cell stack temperatures in an appropriate temperature range, without distinguishing between temporary cell stack temperature rises caused by power load following and cell stack temperature rises caused by degradation. I.e., if there is not a large power load, the amount of rise in the stack temperature is primarily due to degradation, but in the past the appropriate temperature range was maintained by increasing the generating air supply amount even in cases where the appropriate temperature range was exceeded due to the rise amounts caused by degradation.
However the problem was that to return a cell stack temperature to the appropriate temperature range when its rise is caused by degradation always required increasing the amount of generating air supplied. There was an additional problem in that if fuel cell stack degradation occurred, it was advantageous from the standpoint of maintaining output power performance to maintain a somewhat higher temperature, but if the cell stack temperature was forcibly returned to the appropriate temperature range by increasing the generating air supply amount, only a degraded output power performance could be achieved, and if an attempt was made to force power output as normal in that state, an extra generating load was imposed on the remaining effective portion, further promoting degradation.
The present invention was undertaken to resolve this type of issue, and has the object of providing a fuel cell device capable of executing appropriate stack temperature control both before and after fuel cell stack degradation.
In order to accomplish the above objectives, the present invention is a fuel cell device comprising a fuel cell stack for generating power by reacting fuel gas and oxygen-containing gas; a fuel gas supply means for supplying fuel gas to the fuel cell stack; an oxygen-containing gas supply means for supplying oxygen-containing gas to the fuel cell stack; a temperature detection means for detecting the temperature of the fuel cell stack; and a control device for controlling a supply flow rate of oxygen-containing gas, wherein the control device controls the supply flow rate of oxygen-containing fuel gas so that the cell stack is within an appropriate temperature range; wherein the control device is constituted to determine degradation of the fuel cell stack, and to execute control to increase the supply flow rate of oxygen-containing gas so as to return the stack temperature to the appropriate temperature range when the fuel cell stack is not in a degraded state, and to execute control of the supply flow rate of oxygen-containing gas so as not to increase the supply flow rate of oxygen-containing gas until reaching the supply flow rate required to return the cell stack temperature to the appropriate temperature range when the fuel cell stack is in a degraded state.
If the stack temperature rise is a temporary one caused by power load following or the like, it is desirable to return the stack temperature quickly to the appropriate temperature range by increasing the supply flow rate of oxygen-containing gas. On the other hand, if the rise in stack temperature is caused by degradation, it is desirable to maintain the stack temperature at some degree of high temperature, not returning it to the appropriate temperature range, since fuel cell output power performance can be maintained. I.e., maintaining some degree of high temperature in the cell stack works as a degradation correction relative to power output performance.
In the present invention if the stack temperature departs from the appropriate temperature range due to a temporary temperature rise in a non-degraded state, the supply flow rate of oxygen-containing gas is increased in order to return it quickly to the appropriate temperature range. However in the present invention if the stack temperature departs from the appropriate temperature range due to a permanent temperature rise caused by degradation, the stack temperature can be stabilized at a thermally balanced temperature somewhat above the appropriate temperature range by not attempting to force the stack temperature back to the appropriate temperature range, and not increasing the supply flow rate of oxygen-containing gas up to the supply flow rate required to return the stack temperature to the appropriate temperature range. Thus in the present invention a quick return to the appropriate temperature range relative to temporary rises in stack temperature can be accomplished, while on the other hand for permanent temperature rises caused by degradation, output power performance of the degraded cell stack can be compensated by holding at a temperature higher than the appropriate temperature range, thereby obtaining the rated output performance.
In the present invention the control device makes a determination that the fuel cell has degraded if the cell stack temperature continues to be outside the appropriate temperature range for a predetermined time period, and when fuel cell degradation is determined, it suppresses increases in the supply flow rate of oxygen-containing gas.
In the present invention thus constituted, a judgment of whether a stack temperature rise is temporary or permanent can be made by a simple control, without creating a complicated judgment processing process for the purpose, by measuring the length of the continuous period over which the cell stack temperature is outside the appropriate temperature range, so that for both temporary and permanent temperature rises, stack temperature can be maintained at temperatures respectively appropriate to each.
In the present invention there is preferably an upper limit value set for the supply flow rate of oxygen-containing gas, and the control device does permit increases after the supply flow rate of oxygen-containing gas reaches the upper limit value.
In the present invention thus constituted, once the supply flow rate of oxygen-containing gas reaches the upper limit value, the supply flow rate will be fixed thereafter, so the stack temperature can be stably maintained at the appropriate temperature in a degraded state.
In the present invention, the upper limit value for the supply flow rate of oxygen-containing gas is fixed, regardless of the size of the deviation of the stack temperature from the appropriate temperature range.
In the present invention thus constituted, because the greater the degree of degradation of the cell stack, the more the cell stack temperature settles at a high temperature, the level of the cell stack temperature is effective for maintaining power output performance. Therefore a stack temperature appropriate for maintaining power output performance can be achieved in proportion to the extent of degradation at the time of degradation.
In the present invention the speed of increase in supply flow rate of oxygen-containing gas is set high in proportion to the size of the deviation of the stack temperature from the appropriate temperature range.
In the present invention thus constituted, temporary rises in stack temperature can be quickly returned to the appropriate temperature range, whereas for temperature rises caused by degradation, the supply flow rate of oxygen-containing gas is limited by the upper limit value even if deviation is large and the speed of increase in the supply flow rate of oxygen-containing gas is set high, so excessive rises in the supply flow rate of oxygen-containing gas can be suppressed.
In the present invention if the stack temperature is equal to or greater than a predetermined temperature, and is within the appropriate temperature range, the supply flow rate of oxygen-containing gas is preferably not changed.
In the present invention thus constituted, the temperature band in which the stack temperature is equal to or greater than a predetermined temperature and also within the appropriate temperature range becomes the deadband region in which fluctuations in the supply flow rate of oxygen-containing gas is not allowed. Providing this type of deadband region results in waiting period for a stack temperature following delay, so the stack temperature is prevented from continuing to fluctuate without settling on a specific value.
The fuel cell system of the present invention is able to prevent the occurrence of carbon deposits, reforming catalyst degradation and the like which can occur at restart, and can thereby enable long operating life.
Next, referring to the attached drawings, a solid oxide fuel cell (SOFC) device according to an embodiment of the present invention will be explained.
The fuel cell module 2 is furnished with a housing 6; within this housing 6, a sealed space 8 is formed, mediated by thermal insulation (not shown; thermal insulation is not a mandatory structure, and may be omitted). Note that it is acceptable not to provide thermal insulation. A fuel cell assembly 12 for carrying out the electrical power generating reaction using fuel gas and oxidizer (air) is disposed in a generating chamber 10, which is the lower part of this sealed space 8. This fuel cell assembly 12 is furnished with ten fuel cell stacks 14 (see
A combustion chamber 18 is formed above the aforementioned power generating chamber 10 in the sealed space 8 of the fuel cell module 2; residual fuel gas and residual oxidant (air) not used in the electrical generation reaction are burned in this combustion chamber 18 to producing exhaust gas.
A reformer 20 for reforming fuel gas is disposed at the top of the combustion chamber 18; the reformer 20 is heated by the heat of residual gas combustion to a temperature at which the reforming reaction can take place. An air heat exchanger 22 for receiving the heat of combustion and heating the air is further disposed above this reformer 20.
Next, the auxiliary unit 4 is furnished with a pure water tank 26 for holding water from a municipal or other water supply source 24 and filtering it into pure water, and a water flow rate regulator unit 28 (a “water pump” or the like driven by a motor) for regulating the flow rate of water supplied from the reservoir tank. The auxiliary tank 4 is further furnished with a gas shutoff valve 32 for shutting off the fuel gas supplied from a fuel supply source 30 such as municipal gas or the like, a desulfurizer 36 for desulfurizing the fuel gas, and a fuel flow rate regulator unit 38 (a “fuel pump” or the like driven by a motor) for regulating the flow rate of fuel gas. Furthermore, the auxiliary unit 4 is furnished with an electromagnetic valve 42 for shutting off air serving as an oxidant and supplied from an air supply source 40, a reforming air flow rate regulator unit 44 and generating air flow rate regulator unit 45 (“air blower” or the like driven by a motor) for regulating air flow rate, a first heater 46 for heating reforming air supplied to the reformer 20, and a second heater 48 for heating a generating air supplied to the power generating chamber. This first heater 46 and second heater 48 are provided in order to efficiently raise the temperature at startup, but may be omitted.
Next, a hot-water producing device 50 supplied with exhaust gas is connected to the fuel cell module 2. Municipal water from a water supply source 24 is supplied to this hot-water producing device 50; this water is turned into hot water by the heat of the exhaust gas, and is supplied to a hot water reservoir tank in an external water heater (not shown).
The fuel cell module 2 is provided with a control box 52 for controlling the supply flow rate of fuel gas and the like.
Furthermore, an inverter 54 serving as an electrical power extraction unit (electrical power conversion unit) for supplying electrical power generated by the fuel cell module to the outside is connected to fuel cell module 2.
The internal structure of the solid oxide fuel cell (SOFC) device according to this embodiment of the present invention is explained using
As shown in
A pure water guide pipe 60 for introducing pure water on the upstream end of the reformer 20, and a reform gas guide pipe 62 for introducing the fuel gas and reforming air to be reformed, are attached to the reformer 20; a vaporizing section 20a and a reforming section 20b are formed in sequence starting from the upstream side within the reformer 20, and the reforming section 20b is filled with a reforming catalyst. Fuel gas and air blended with the steam (pure water) introduced into the reformer 20 is reformed by the reforming catalyst used to fill in the reformer 20. Appropriate reforming catalysts are used, such as those in which nickel is imparted to the surface of alumina spheres, or ruthenium is imparted to the surface of alumina spheres.
A fuel gas supply line 64 is connected to the downstream end of the reformer 20; this fuel gas supply line 64 extends downward, then further extends horizontally within a manifold 66 formed under fuel cell assembly 12. Multiple fuel supply holes 64b are formed on the bottom surface of a horizontal portion 64a of the fuel gas supply line 64; reformed fuel gas is supplied into manifold 66 from these fuel supply holes 64b.
A lower support plate 68 provided with through holes for supporting the above-described fuel cell stack 14 is attached at the top of manifold 66, and fuel gas in the manifold 66 is supplied into the fuel cell units 16.
Next, the air heat exchanger 22 is provided over the reformer 20. This air heat exchanger 22 is furnished with an air concentration chamber 70 on the upstream side and two air distribution chambers 72 on the downstream side; the air concentration chamber 70 and the distribution chambers 72 are connected using six air flow conduits 74. Here, as shown in
Air flowing in the six air flow conduits 74 of the air heat exchanger 22 is pre-heated by rising combustion exhaust gas from combustion chamber 18.
Air guide pipes 76 are connected to each of the respective air distribution chambers 72; these air guide pipes 76 extend downward, communicating at the bottom end side with the lower space in the generating chamber 10, and introducing preheated air into the generating chamber 10.
Next, an exhaust gas chamber 78 is formed below the manifold 66. As shown in
As shown in
Next, referring to
As shown in
The fuel cell 84 is a tubular structure extending in the vertical direction, furnished with a cylindrical internal electrode layer 90, on the inside of which is formed a fuel gas flow path 88, a cylindrical external electrode layer 92, and an electrolyte layer 94 between the internal electrode layer 90 and the external electrode layer 92. This internal electrode layer 90 is a fuel electrode through which fuel gas passes, and is a (−) pole, while the external electrode layer 92 is an air electrode for contacting the air, and is a (+) pole.
The internal electrode terminals 86 attached at the top end and bottom end of the fuel cell unit 16 have the same structure, therefore the internal electrode terminal 86 attached at the top end side will be specifically explained. The top portion 90a of the inside electrode layer 90 is furnished with an outside perimeter surface 90b and top end surface 90c, exposed to the electrolyte layer 94 and the outside electrode layer 92. The inside electrode terminal 86 is connected to the outer perimeter surface 90b of the inside electrode layer 90 through a conductive seal material 96, and is electrically connected to the inside electrode layer 19 by making direct contact with the top end surface 90e of the inside electrode layer 90. A fuel gas flow path 98 communicating with a fuel gas flow path 88 in the inside electrode layer 90 is formed at the center portion of the inside electrode terminal 86.
The inside electrode layer 90 is formed, for example, from at least one of a mixture of Ni and zirconia doped with at least one type of rare earth element selected from Ca, Y, Sc, or the like; or a mixture of Ni and ceria doped with at least one type of rare earth element; or any mixture of Ni with lanthanum gallate doped with at least one element selected from Sr, Mg, Co, Fe, or Cu.
The electrolyte layer 94 is formed, for example, from at least one of the following: zirconia doped with at least one type of rare earth element selected from among Y, Sc, or the like; ceria doped with at least one type of selected rare earth element; or lanthanum gallate doped with at least one element selected from among Sr or Mg.
The outside electrode layer 92 is formed, for example, from at least one of the following: lanthanum manganite doped with at least one element selected from among Sr or Ca; lanthanum ferrite doped with at least one element selected from among Sr, Co, Ni, or Cu; lanthanum cobaltite doped with at least one element selected from among Sr, Fe, Ni, or Cu; silver, or the like.
Next, referring to
As shown in
In addition, a current collector 102 and an external terminal 104 are attached to the fuel cell unit 16. The current collector 102 is integrally formed by a fuel electrode connecting portion 102a, which is electrically connected to the inside electrode terminal 86 attached to the inside electrode layer 90 serving as the fuel electrode, and by an air electrode connecting portion 102b, which is electrically connected to the entire external perimeter of the outside electrode layer 92 serving as the air electrode. The air electrode connecting portion 102b is formed of a vertical portion 102c extending vertically along the surface of the outside electrode layer 92, and multiple horizontal portions 102d extending in the horizontal direction from the vertical portion 102c along the surface of the outside electrode layer 92. The fuel electrode connecting portion 102a extends linearly in an upward or downward diagonal direction from the vertical portion 102c of the air electrode connecting portion 102b toward the inside electrode terminals 86 positioned in the upper and lower directions on the fuel cell unit 16.
Furthermore, inside electrode terminals 86 at the top and bottom ends of the two fuel cell units 16 positioned at the end of the fuel cell stack 14 (at the front and back sides on the left edge in
Next, referring to
As shown in
Next, signals from the various sensors described below are input to the control unit 110.
First, flammable gas detection sensor 120 detects gas leaks and is attached to the fuel cell module 2 and the auxiliary unit 4.
The purpose of a CO detection sensor 122 is to detect leakage of CO in the exhaust gas, which is supposed to be exhausted to the outside via the exhaust gas conduit 80 and the like, into the external housing (not shown) which covers the fuel cell module 2 and the auxiliary unit 4.
A water reservoir state detection sensor 124 detects the temperature and amount of hot water in a water heater (not shown).
An electrical power state detection sensor 126 detects current, voltage, and the like in the inverter 54 and in a distribution panel (not shown).
A power generator air flow rate detection sensor 128 detects the flow rate of power generator air supplied to the generating chamber 10.
A reforming air flow rate sensor 130 detects the flow rate of reforming air supplied to the reformer 20.
A fuel flow rate sensor 132 detects the flow rate of fuel gas supplied to the reformer 20.
A water flow rate sensor 134 detects the flow rate of pure water (steam) supplied to the reformer 20.
A water level sensor 136 detects the water level in pure water tank 26.
A pressure sensor 138 detects pressure on the upstream side outside the reformer 20.
An exhaust temperature sensor 140 detects the temperature of exhaust gas flowing into the hot water producing device 50.
As shown in
A combustion chamber temperature sensor 144 detects the temperature in combustion chamber 18.
An exhaust gas chamber temperature sensor 146 detects the temperature of exhaust gases in the exhaust gas chamber 78.
A reformer temperature sensor 148 detects the temperature of the reformer 20 and calculates the temperature of the reformer 20 from the intake and exit temperatures on the reformer 20.
If the solid oxide fuel cell (SOFC) device is placed outdoors, the outside temperature sensor 150 detects the temperature of the outside atmosphere. Sensors to detect outside atmospheric humidity and the like may also be provided.
Signals from these various sensors are sent to the control unit 110; the control unit 110 sends control signals to the water flow rate regulator unit 28, the fuel flow rate regulator unit 38, the reforming air flow rate regulator unit 44, and the power generating air flow rate regulator unit 45 based on data from the sensors, and controls the flow rate in each of these units.
The control unit 110 sends control signals to the inverter 54 to control the supplied electrical power.
Next, referring to
At the beginning, in order to warm up the fuel cell module 2, the operation starts in a no-load state, i.e., with the circuit which includes the fuel cell module 2 in an open state. At this point current does not flow in the circuit, therefore the fuel cell module 2 does not generate electricity.
First, reforming air is supplied from the reforming air flow rate regulator unit 44 to the reformer 20 on the fuel cell module 2 via the first heater 46. At the same time, power generating air is supplied from the generating air flow rate regulator unit 45 to the air heat exchanger 22 of the fuel cell module 2 via the second heater 48, and the power generating air reaches the generating chamber 10 and the combustion chamber 18.
Immediately thereafter, fuel gas is also supplied from the fuel flow rate regulator unit 38, and fuel gas into which reforming air is blended passes through the reformer 20, the fuel cell stack 14, and the fuel cell units 16 to reach the combustion chamber 18.
Next, ignition is brought about by the ignition device 83, and fuel gas and air (reforming air and power generating air) supplied to the combustion chamber 18 is combusted. This combustion of fuel gas and air produces exhaust gas; the generating chamber 10 is warmed by this exhaust gas, and when the exhaust gas rises in the sealed space 8 of the fuel cell module 2, the fuel gas, which includes the reforming air in the reformer 20 is warm, as is the power generating air inside the air heat exchanger 22.
At this point, fuel gas into which reforming air is blended is supplied to the reformer 20 by the fuel flow rate regulator unit 38 and the reforming air flow rate regulator unit 44, therefore the partial oxidation reforming reaction PDX given by Expression (1) proceeds in the reformer 20. This partial oxidation reforming reaction PDX is an exothermic reaction, and therefore has favorable starting characteristics. This elevated-temperature fuel gas is supplied from the fuel gas supply line 64 to the bottom of the fuel cell stack 14, and by this means the fuel cell stack 14 is heated from the bottom; and the combustion chamber 18 is also heated by the combustion of the fuel gas and air, so that the fuel cell stack 14 is also heated from above, thereby enabling an essentially uniform rise in temperature in the vertical direction of the fuel cell stack 14. Even though the partial oxidation reforming reaction PDX is progressing, the ongoing combustion reaction between fuel gas and air is continued in the combustion chamber 18.
CmHn+xO2→aCO2+bCO+cH2 (1)
After the start of the partial oxidation reforming PDX, when the reformer temperature sensor 148 senses that the reformer 20 has reached a predetermined temperature (e.g., 600° C.), a premixed gas of fuel gas, reforming air and steam is supplied to the reformer 20 by the water flow rate regulator unit 28, the fuel flow rate regulator unit 38, and the reforming air flow rate regulator unit 44. At this point, an auto-thermal reforming reaction ATR, which makes use of both the aforementioned partial oxidation reforming reaction PDX and the steam reforming reaction SR described below, proceeds in the reformer 20. This auto-thermal reforming reaction ATR can be internally thermally balanced, therefore the reaction proceeds in a thermally independent fashion inside the reformer 20. In other words, if oxygen (air) is abundant, heat emission by the partial oxidation reforming reaction PDX dominates, and if steam is abundant, the endothermic steam reforming reaction SR dominates. At this stage, the initial stage of startup has passed and some degree of elevated temperature has been achieved within the generating chamber 10, therefore even if the endothermic reaction is dominant, no major drop in temperature will be caused. Also, the combustion reaction continues within the combustion chamber 18 even as the auto-thermal reforming reaction ATR proceeds.
When the reformer temperature sensor 146 senses that the reformer 20 has reached a predetermined temperature (e.g., 700° C.) after starting auto-thermal reforming reaction ATR shown in Equation (2), the supply of reforming air by the reforming air flow rate regulator unit 44 is stopped and the supply of steam by water flow rate regulator unit 28 is increased. A gas containing no air and only containing fuel gas and steam is thus supplied to the reformer 20, where the steam reforming reaction SR of Expression (3) proceeds.
CmHn+xO2+yH2O→aCO2+bCO+cH2 (2)
CmHn+xH2O→aCO2+bCO+cH2 (3)
This steam reforming reaction SR is an endothermic reaction, therefore the reaction proceeds as a thermal balance is maintained with the combustion heat from the combustion chamber 18. At this stage, the fuel cell module is in the final stages of startup, therefore the temperature has risen to a sufficiently high level within the generating chamber 10 so that no major temperature drop is induced in the power generating chamber 10 even though an endothermic reaction is proceeding. Also, the combustion reaction continues to proceed in the combustion chamber 18 even as the steam reforming reaction SR is proceeding.
Thus, after the fuel cell module 2 has been ignited by the ignition device 83, the temperature inside the generating chamber 10 gradually rises as a result of the partial oxidation reforming reaction PDX, the auto-thermal reforming reaction ATR, and the steam reforming reaction SR proceeding in sequence. Next, when the temperatures of interior of the generating chamber 10 and individual fuel cells 84 reach a predetermined generating temperature below the rated temperature at which the fuel cell module 2 can be stably operated, the circuit including the fuel cell module 2 is closed and electrical generation by the fuel cell module 2 begins, such that current flows in the circuit. Generation of electricity by the fuel cell module 2 causes the fuel cell 84 itself to emit heat, such that the temperature of the fuel cell 84 rises. As a result, the rated temperature for operating the fuel cell module 2, for example 600° C. to 800° C., is reached.
Thereafter, in order to maintain the rated temperature, fuel gas and air are supplied in a quantity greater than the fuel gas and air consumed by individual fuel cells 84 to continue combustion inside the combustion chamber 18. During electrical generation, generation of electricity by the high reforming efficiency steam reforming reaction SR proceeds.
Next, referring to
As shown in
When stopping the operation of the fuel cell module 2, the flow rate of power generating air supplied by the power generating air flow rate regulator unit 45 into the fuel cell module 2 is being increased at the same time that the flow rate of fuel gas and steam being supplied to the reformer 20 is being reduced; the fuel cell assembly 12 and the reformer 20 are air cooled to reduce their temperatures. Thereafter when the temperature in the generating chamber gets down to a predetermined temperature, for example 400° C., the supply of fuel gas and steam to the reformer 20 is stopped and the steam reforming reaction SR in the reformer 20 ends. Supply of power generating air continues until the temperature in the reformer 20 drops to a predetermined temperature, e.g. 200° C.; when the predetermined temperature is reached, the supply of power generating air from the power generating air flow rate regulator unit 45 is stopped.
Thus in the present embodiment the steam reforming reaction SR by the reformer 20 and cooling by power generating air are used in combination, therefore when the operation of the fuel cell module 2 is stopped, that operation can be stopped relatively quickly.
Next, referring to
In this embodiment the generating chamber temperature sensor 142, which is a temperature detection means, measures the temperature close to the fuel cell stack 14 (i.e. individual fuel cells 84 themselves) as a stack temperature Ts. The control unit 110 acquires the measured stack temperature Ts, and as a basic processing control it controls the generating air flow rate regulator unit 45, which is an oxygen-containing gas supply means for supplying air as an oxygen-containing gas, so as to maintain the stack temperature Ts in the appropriate temperature range A (temperature T1 to T2) during operation.
The fuel cell stack 14 generates electrical power by a generating reaction between gas reformed for generation (in this example hydrogen gas) and oxygen-containing gas for generation (in this example air).
In operations following completion of startup, the control unit 110 normally sets a supply flow rate AF of power generating air supplied to the fuel cell stack 14 at a specified supply flow rate AF0 and controls the generating air flow rate regulator unit 45 to supply power generating air at the flow rate AF0. Therefore if not in a state of following high load electrical power demands, and if the fuel cell stack 14 is not in a degraded state, the measured cell stack temperature Ts is maintained within the appropriate temperature range A.
However, if the stack temperature Ts rises and exceeds the appropriate temperature range A due to a power load following operation or degradation of the fuel cell stack 14 or the like, the control unit 110 controls the generating air flow rate regulator unit 45 and adjusts the generating air supply flow rate AF so as to return the stack temperature Ts to within the appropriate temperature range A.
In
At this point, the control unit 110 gradually increases the supply flow rate AF over time at a predetermined speed of increase or rate of increase. When supply flow rate AF is increased, cooling capacity to the fuel cell stack 14 is increased and stack temperature Ts begins to drop after the temperature rise caused by power load following operation thermally balances with cooling capacity. Note that the speed of increase or rate of increase means a rate of increase in the amount supplied per unit time.
In
Note that in the present embodiment a maximum supply flow rate AFmax, which is a maximum set value, is set for the supply flow rate AF, and the supply flow rate AF is not increased past the maximum supply flow rate AFmax. In the present embodiment, the maximum supply flow rate AFmax is set at a size equal to a 10% increase in the supply flow rate AF0.
Once the supply flow rate AF returns to the supply flow rate AF0 at time t3, the supply flow rate AF is thereafter maintained at the supply flow rate AF0. That is, in
Note that in the present embodiment the supply flow rate AF is varied linearly relative to elapsed time, but without such limitation, it may also be varied stepwise in predetermined temperature steps.
Next,
In
At this point, the control unit 110, as in
The control unit 110 activates a timer starting from the time t10 at which the increase of the supply flow rate AF is started. In
At this point, stack temperature Ts can be returned to within the appropriate temperature range A by further increasing the supply flow rate AF from the supply flow rate AF2, however the control unit 110 controls stack temperature Ts to a temperature above the appropriate temperature range A (i.e., the temperature at which the temperature rise caused by degradation is thermally balanced by the cooling capacity from the supply flow rate AF2).
After the degradation determination, once the supply flow rate AF is fixed at the supply flow rate AF2, the supply flow rate AF2 is thereafter replaced by a specified or normal supply flow rate (i.e., corresponding to the supply flow rate AF0 before degradation).
Note that after the degradation has occurred in the fuel cell stack 14, if the power load is small, stack temperature Ts may return to within the appropriate temperature range A, even if generating air is now being supplied at the newly specified supply flow rate AF2.
Thus in the present embodiment, even if the supply flow rate AF continues to be increased during the predetermined degradation determination period C, and the stack temperature Ts has not returned to within the appropriate temperature range A, the rise in stack temperature Ts will be determined to be not temporary but permanent, resulting from the degradation of the fuel cell stack 14. If the fuel cell stack 14 has degraded, maintenance of a somewhat high stack temperature Ts functions as degradation compensation for maintaining output power performance as a fuel cell.
Therefore if a degradation determination is made, the control unit 110 does not further increase the supply flow rate AF from the supply flow rate AF2 to force stack temperature Ts back into the appropriate temperature range A, but rather prohibits an increase in the supply flow rate AF up to the amount required to return stack temperature Ts to within the appropriate temperature range A, thereby fixing the supply flow rate AF at the supply flow rate AF2. Stack temperature Ts is by this means held at a temperature responsive to the relationship between degradation and the supply flow rate AF2, at or below the service limit temperature of the fuel cell stack 14, and stack temperature Ts is maintained at a somewhat high level to assure power output performance.
Note that when the supply flow rate AF is held at the supply flow rate AF2, if stack temperature Ts seems likely to reach the service limit temperature, the control unit 110 may further increase the supply flow rate AF within a range at or below the maximum supply flow rate AFmax.
In the present embodiment a determination of degradation was made using degradation determination time C, but without such limitation, degradation can also be determined to occur if the supply flow rate AF reaches a particular supply flow rate (e.g., the supply flow rate AF2) when the supply flow rate AF is increased at a predetermined speed of increase in amount without stack temperature Ts returning to within the appropriate temperature range A. Therefore a determination of degradation is made if stack temperature Ts does not return to within the appropriate temperature range A despite an increase in the supply flow rate during a predetermined time interval and/or up to a predetermined flow rate.
Also, in the above embodiment the supply flow rate AF is fixed at the supply flow rate AF2 when a degradation determination is made, but without such limitation, the speed of increase in the supply flow rate AF after the determination of degradation (time t11) can also be suppressed to a low level (see the dot-and-dash line in
In such cases, the increase of the supply flow rate AF is stopped when it reaches a particular supply flow rate (e.g., the maximum supply flow rate AFmax) (time t12), and the supply flow rate AF is maintained at that supply flow rate (the maximum supply flow rate AFmax).
In the embodiment above the degradation determination is made using the stack temperature, but the method for judging degradation determination is not limited thereto. For example, degradation can be judged based on whether the generating efficiency at the time when the generated current value reaches a specified value has fallen to a predetermined value or below.
Next, referring to
The control unit 110 executes the processing flow shown in
First, the control unit 110 determines whether stack temperature Ts is above 670° C. (decrease start temperature T3 within the appropriate temperature range A) (step S1).
If stack temperature Ts is at or below 670° C. (step S1; No), the control unit 110 transitions to processing to return the supply flow rate AF to the normal supply flow rate AF0 (step S9) and terminates processing. Therefore if stack temperature Ts is at 670° C. or below, the supply flow rate AF is maintained at the supply flow rate AF0. Note that as shown in
On the other hand if stack temperature Ts is higher than 670° C. (step S1; Yes), the control unit 110 determines whether the supply flow rate AF is less than the maximum supply flow rate AFmax (step S2).
If the supply flow rate AF is the maximum supply flow rate AFmax (step S2; No), the supply flow rate AF cannot be increased any further, so the control unit 110 terminates processing. Therefore when the supply flow rate AF reaches the maximum supply flow rate AFmax, the supply flow rate AF will be maintained at the maximum supply flow rate AFmax so long as stack temperature Ts does not go to 670° C. or below.
On the other hand if the supply flow rate AF is less than the maximum supply flow rate AFmax (step S2; Yes), then there is margin to increase the supply flow rate AF, so the control unit 110 determines whether stack temperature Ts is above 680° C. (the upper limit temperature T2 of the appropriate temperature range A).
If stack temperature Ts is not above 680° C. (step S3; No), the control unit 110 does not yet change the supply flow rate AF at this point. I.e., the current supply flow rate is maintained since the control unit 110 terminates processing.
On the other hand, if stack temperature Ts is above 680° C. (step S3; Yes), the control unit 110 determines whether stack temperature Ts is greater than 700° C.) (step S4).
If stack temperature Ts is not above 700° C. (step S4; No), stack temperature Ts is above 680° C. and equal to or less than 700° C., and the deviation from the appropriate temperature range A (the temperature gap from the appropriate temperature range A; in this case the temperature difference relative to the upper limit temperature T2) is small, so the control unit 110 sets the speed of increase in supply flow rate AF to a minimum value ΔAFmin (step S8) and terminates processing. The supply flow rate AF is thus increased at the minimum value ΔAFmin (rate of increase per unit time), so that cooling performance relative to the fuel cell stack 14 is increased.
In this case, however, the temperature deviation is small, so if the speed of increase in the supply flow rate AF is too large and the amount of generating air supplied compared to the speed of increase in stack temperature Ts is too large, there is a risk that stack temperature Ts will be too low, and fluctuation in the stack temperature Ts will become unstable, etc. Therefore in the present embodiment if the temperature difference is small, the speed of increase in the supply flow rate AF is suppressed and the above-described problem does not occur.
On the other hand, if stack temperature Ts is above 700° C. (step S4; Yes), the control unit 110 determines whether stack temperature Ts is greater than 710° C. (step 5).
If stack temperature Ts is not above 700° C. (step S5; No), stack temperature Ts is above 700° C. but at or below 710° C., with a medium deviation from the appropriate temperature range A, therefore the control unit 110 sets the speed of increase in the supply flow rate AF at a mid-value ΔAFmid which is larger than the minimum value ΔAFmin (step S7) and terminates processing.
In this case when stack temperature Ts exceeds 700° C., the temperature deviation is mid-level, so the control unit 110 increases the speed of increase in cooling performance by increasing the speed of increase in the supply flow rate AF more, so as to bring stack temperature Ts quickly into the appropriate temperature range A.
On the other hand if stack temperature Ts is above 710° C. (step S5; Yes), deviation from the appropriate temperature range A is large, so the control unit 110 sets the speed of increase in the supply flow rate AF at the maximum value ΔAFmax (step S6), which is larger than the mid-value ΔAFmid, and terminates processing.
In this case when stack temperature Ts exceeds 710° C., the temperature deviation is large, so the control unit 110 quickly increases the speed of increase in cooling performance by further increasing the speed of increase in the supply flow rate AF more so as to bring stack temperature Ts quickly into the appropriate temperature range A.
Thus in the present embodiment stack temperature Ts can be returned quickly to the appropriate temperature range A in response to temporary rises in stack temperature Ts by setting the speed of increase in the supply flow rate AF to be faster in proportion to the temperature deviation of stack temperature Ts relative to the appropriate temperature range A.
However, even if the temperature deviation is large, the supply flow rate AF is limited to the maximum supply flow rate AFmax (see step S2), therefore the amount of generating air supplied can be prevented from becoming excessive. Also, even if the temperature deviation is large, the supply flow rate AF is limited to the maximum supply flow rate AFmax, therefore the higher the temperature deviation, the higher is the temperature at which stack temperature Ts is held, so the degradation compensation amount for maintaining power output performance can be increased.
In this embodiment it is also conceivable that degradation could advance further with the supply flow rate AF having reached the maximum supply flow rate AFmax, so that stack temperature Ts rises too far. When the stack temperature exceeds 820° C. the system is stopped for safety reasons, therefore no safety problems arise due to the supply flow rate AF not exceeding the maximum supply flow rate.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2010-220433 | Sep 2010 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2011/072223 | 9/28/2011 | WO | 00 | 3/15/2013 |
