Cathode pressure control utilizing a capacitance model
View Patent ↗Systems and methods to control fuel cell stack pressure through a cathode backpressure valve. A flow offset value is used as a capacitance term during transient operational conditions to account for discrepancies between the stack flow setpoint and the actual stack flow. The capacitance term is based on operational parameters, including stack pressure changes, stack coolant temperature and stack volume. The additional flow produced by the capacitance terms may be fed, along with pressure drop models and a valve position model to provide a more accurate prediction of valve position.
1. A fuel cell system comprising:
a fuel cell stack;
a backpressure valve in fluid communication with an outlet of the fuel cell stack; and
a controller comprising at least one processor, an input, and output and a memory, the memory configured to store instructions related to a plurality of models comprising a plurality of pressure drop models, a stack capacitance model and a valve position model, the controller is programmed to execute the instructions in memory to generate a command signal to regulate the position of the backpressure valve, the command signal comprising a feedforward component and a feedback component where the feedforward component is determined using output from the valve position model that has been modified by the stack capacitance model and at least one of the plurality of pressure drop models, wherein the stack capacitance model modifies the output based on the Ideal Gas Law according to:
d
m
cap
=
(
p
stck
,
fd
-
p
prdtd
)
*
V
R
*
T
stck
·
M
air
where dm cap is an offset term to modify the stack flow setpoint signal, R is gas constant, T stck is the stack flow temperature, V is the volume of the fuel cell stack and M air is the airflow molecular weight.
2. The system of claim 1 , wherein the capacitance model is configured to receive as input values corresponding to a pressure change in the fuel cell stack, flow temperature in the fuel cell stack, a fuel cell stack volume and a predicted pressure in the fuel cell stack, the predicted stack pressure based on a stack pressure setpoint and maximum permissible pressure based on a compressor speed.
3. The system of claim 1 , wherein the capacitance model is configured to generate input for both the valve position model and at least one of the plurality of pressure drop models.
4. A controller for a fuel cell system comprising:
at least one processor; and
a memory in signal communication with the at least one processor to store instructions, wherein the at least one processor is programmed to execute the instructions in memory to control reactant pressure in a fuel cell stack by regulating the position of a backpressure valve connected to an outlet of the fuel cell stack through the use of a valve position model, a stack capacitance model and at least one pressure drop model that cooperate in response to an operational transient in the fuel cell stack, wherein output from the stack capacitance model modifies at least one parameter used as a stack flow control signal by at least one of the valve position model and at least one pressure drop model and the output from the stack capacitance model is based on the Ideal Gas Law according to:
d
m
cap
=
(
p
stck
,
fd
-
p
prdtd
)
*
V
R
*
T
stck
·
M
air
where dm cap is a modifying airflow setpoint signal corresponding to the modifying output, R is gas constant, T cool,out is the stack coolant outlet temperature, V is the volume of the fuel cell stack and M air is the airflow molecular weight.
5. The controller of claim 4 , wherein the at least one processor is further configured to control a compressor that is in fluid communication with an inlet of the fuel cell stack.
6. The controller of claim 4 , wherein the input into the stack capacitance model comprises values corresponding to a pressure change in the fuel cell stack, a coolant temperature in the fuel cell stack, a fuel cell stack volume and a predicted pressure in the fuel cell stack, the predicted pressure based on a compressor speed and maximum permissible pressure.
7. The controller of claim 6 , wherein output from the stack capacitance model is used as input for both the valve position model and the at least one pressure drop model.
8. The controller of claim 4 , wherein the at least one pressure drop model comprises a plurality of pressure drop models such that a first pressure drop model is configured to cooperate with the at least one processor to predict pressure at the inlet of the backpressure valve, while a second pressure drop model is configured to cooperate with the at least one processor to predict pressure at the outlet of the backpressure valve.
9. The controller of claim 4 , wherein the instructions further cause the at least one processor to determine if the operational transient in the fuel cell stack has caused a stack pressure setpoint to change, and to generate a stack flow setpoint value offset by the stack flow offset value in the event the stack pressure setpoint has changed.