Current and fuel utilization are controlled within paralleled fuel cell assemblies, each comprising one or a string of fuel cell stacks, and a reduced number of fuel cell stacks is used should one stack fail.
An important parameter in the operation of fuel cell power plants is the efficiency, that is, the degree to which fuel supplied to the fuel cell stack (or stacks) is actually utilized. For any given current, there is a stoichiometric amount of fuel which is consumed in order to generate that current. Fluctuations in power demand are handled in part by adjusting the amount of fuel provided to the fuel cell: larger demand requires more fuel and reduced demand requires less fuel. Attempts to control fuel utilization to exactly the stoichiometric quantity (100% utilization) for maximum efficiency will always result in some parts of at least some cells in a stack suffering fuel starvation. Fuel starvation causes instantaneous performance losses, and more importantly causes permanent decay of cell performance. Typically, fuel utilizations are selected to be on the order of about 85%, to ensure that increased power transients and flow variations will not result in fuel starvation.
Because of the difficulties of controlling reactant gas flows into large numbers of fuel cells, there are practical limits to fuel cell stack sizes, which limits the power obtainable from a single stack. Therefore, assemblies of fuel cell stacks are utilized to provide adequate power. It is desirable to satisfy the need for high fuel utilization without the risk of fuel starvation, even in multiple fuel cell stack assemblies.
A simple arrangement could be to have all of the stacks in series, whereby the same current would flow through all of them. If a serial fuel cell arrangement were utilized, fuel depletion could easily result in extremely high fuel utilization at the downward end of the fuel flow, resulting in possible starvation and performance decay. Furthermore, serial fuel cell stacks could result in a higher voltage than is practicable in any particular circumstance.
As used herein, the terms “fuel cell stack assembly” and “stack assembly” mean (a) a single fuel cell stack, or (b) a string of fuel cell stacks electrically connected in serial voltage relationship.
In
When fuel cell stack assemblies 15, 16 are connected in parallel passively, such as by simply using isolation diodes 18, 19 as shown in
As illustrated in
In the manufacture of fuel cell stack assembly components, component manufacturing tolerances result in each fuel cell stack assembly having different operational and performance characteristics. The reactant flow pressure drops and therefore reactant flow distributions will vary from one stack assembly to another. Variations carry over to performance so that no two fuel cell stack assemblies have exactly the same performance curve and the same fuel utilization at any point of operation.
As the load on a fuel cell stack or string of stacks varies, the reactants are adjusted in a predetermined relative manner. If separate fuel control valves are used for each stack or string of stacks, each stack or string will have its own feedback loop, with its own time of response and gain. Although the fuel control valve of each stack or string of stacks in a stack assembly could be tuned to provide the correct fuel for any given load in steady-state operation, during transients, a change of fuel and current in one stack or string will interact with changes in fuel commands to other stacks or strings. The result is a very complex control with less than adequate results. If a single fuel control valve is used for all stacks and strings in a fuel cell assembly, trimming may be accomplished to some extent by adjusting reactant flows so as to achieve, at a design point of operation, either the same current, or the same utilization. However, operation off the design point will generally result in variations in the controlled parameter (utilization or current) from one stack or string to another.
After many hours of operation, the performance of one fuel cell may differ from another fuel cell, and reactant flow distribution in the fuel cell stacks may change non-uniformly, which may alter the amount of fuel provided to each stack as well as the thermal distribution within each stack, which in turn can vary the operating point on the performance curve as well as the utilization of fuel in the different stacks.
Controlling fuel flow as a function of measured fuel utilization requires the use of hydrogen sensors at the exit of each stack (or string of series stacks), as well as separate fuel inlet mass flow control and manifolds for each stack or string. Hydrogen detectors are not sufficiently reliable, particularly over thousands of hours of operation, to maintain a desired high utilization without likelihood of fuel starvation.
Another issue with multiple fuel cell stacks is the increased probability for a stack assembly failure. The increased probability causes a drop in power plant reliability. Therefore, what is also needed is a way to avoid this decrease in power plant reliability.
A primary predication of the improvements disclosed herein is that control over the balancing of current and therefore fuel utilization in paralleled fuel cell stack assemblies should be accomplished electrically, rather than by mechanical control over reactant flows. Another predication is that assemblies of fuel cell stacks should be configured and connected in such a way as to permit use of assemblies that remain operational, should failure of one of them occur.
A first aspect of the disclosed improvements is the provision of two electrical control philosophies which will readily provide control over fuel cell stacks so as to achieve a more nearly balanced and desired fuel utilization. In a first control philosophy, paralleled fuel cell stack assemblies having different reactant flow, thermal flow and/or performance variations are compensated for by adjusting the current of both fuel cell stack assemblies to be equal. In another control philosophy, the current of paralleled fuel cell stack assemblies is adjusted to be proportional to the fuel cell's ability to contribute to the required load.
Control schemes are provided for compensation of paralleled fuel cell stack assemblies when the assemblies are connected to a grid, and therefore must respond as current sources, as well as for when the fuel cell assemblies are independent of a grid, operating an isolated load.
Embodiments include reactant flow isolation capability and electrical isolation capability so as to permit isolating a failed fuel cell stack assembly while continuing to extract power output from a functional fuel cell stack assembly, even though the total power output is reduced.
Other improvements, features and advantages will become more apparent in the light of the following detailed description of exemplary embodiments, as illustrated in the accompanying drawings.
a is a voltage/current curve illustrating two fuel cell stack assemblies operating at the same voltage.
b is a voltage/current curve illustrating two fuel cell stack assemblies operating at the same current.
Referring to
In order to cause the current of the two fuel cell stack assemblies 15, 16 to be equal, the amount of power supplied by each is adjusted. A desired power setpoint, P*, is established by the controller 31 as represented by a signal on a line 29. The controller 31 may comprise the overall controller of the fuel cell power plant 13 or some other suitable controller. The magnitude of current supplied by each cell stack assembly 15, 16 is provided over corresponding lines 33, 34 to the controller 31, in response to which the controller provides respective power command signals P1*, P2* on corresponding lines 37, 38. These signals are provided to respective power controls 39, 40 which, with the controller 31, comprise a system power converter 41. The converter 41 causes corresponding amounts of power P1, P2, to be provided to the grid 22 (assuming switches 42, 43 are positioned as shown in
A related portion of the controller 31 is functionally diagrammed in
Operation of the controller 31 in
The power commands, P1* and P2* alter the duty cycle in the power control portions 39, 40 of the system power converter 41 in a conventional fashion.
Balancing of the currents can be achieved when the fuel cell power plant 13 is not connected to the grid, but rather is driving a load at a predetermined voltage, as illustrated in
As illustrated in
The operation in
The embodiments of
Another control scheme which provides improved utilization in paralleled fuel cell stack assemblies causes a current imbalance which is proportional to a nominal operational imbalance between two paralleled fuel cell stack assemblies, with respect to a current required from each cell stack assembly under nominal fuel flow and nominal fuel utilization, in order to meet the power demand. In this alternative form, the paralleled fuel cell assemblies are controlled so that one current may be higher or lower than the other in dependence upon whether that fuel cell assembly provides less or more power, due to reactant flow and temperature variations, and differences in the performance (voltage vs. current) of the respective fuel cell stack assemblies.
Referring to
Another improvement with respect to multiple fuel cell stack assemblies is illustrated in
When the controller senses failure of one of the cell stack assemblies, it will close a corresponding one of a pair of fuel valves 65, 66 to stop the flow of fuel from a source 27 and the related cells of the failed fuel cell stack assembly, as well as blocking the source of oxygen (not shown).
With this innovation, it is possible for a fuel cell stack assembly which has not failed to continue to provide power to the grid, even after failure of one of the fuel cell stack assemblies.
The foregoing disclosure has been presented in the form of schematic, functional block diagrams, illustrating discrete function performing units. Historically, such function performing units may have comprised discrete hardware elements, such as amplifiers, resistive elements at the inputs to amplifiers, capacitors, and the like. However, all of these functions are capable of being performed in conventional computers utilizing known programming techniques. Additionally, although amplifiers 50, 72 are shown multiplying by one-half, they could as well divide by two. Although the switches 42, 43, 52, 53 are illustrated as mechanical switches, electronic switching or computer program routing may also be used.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US06/49639 | 12/29/2006 | WO | 00 | 6/29/2009 |