Anode loop observer for fuel cell systems
View Patent ↗A system and method for controlling the bleed valve in an anode recirculation loop of a fuel cell system. The system uses a model to determine the concentration of hydrogen in the recirculated gas by calculating the volume flow of the recirculated gas through a fuel cell stack, a pressure drop across the anode inlet and outlet of the stack, and the density of the recirculated gas, and using a measured temperature of the recirculated gas and a measured pressure drop across a recirculation pump.
1. A method for determining the concentration of hydrogen in an anode recirculation loop of a fuel cell stack, said method comprising:
measuring the pressure drop across a recirculation pump;
measuring the temperature of the anode recirculation gas flowing through the recirculation loop;
setting an arbitrary value for the percentage of hydrogen in the recirculation gas;
calculating the pressure drop across the anode side of the stack;
calculating the volume flow of the recirculation gas flowing through the anode side of the stack as a function of the calculated pressure drop across the anode side of the stack, the percentage of hydrogen in the recirculation gas, the measured temperature and the measured pressure drop;
calculating the density of the recirculation gas flowing through the recirculation loop using the calculated volume flow, the measured pressure drop and the speed of the recirculation pump; and
using the calculated density, the measured temperature and the measured pressure drop to calculate a new percentage of hydrogen in the recirculation gas.
2. The method according to claim 1 wherein calculating the pressure drop across the anode side of the stack includes using the measured pressure.
3. The method according to claim 2 wherein calculating the pressure drop across the anode side of the stack includes determining and using the pressure drop across a water separator in the recirculation loop that removes water from the recirculation gas.
4. The method according to claim 3 wherein calculating the pressure drop across the anode side of the stack includes determining and using the pressure drop across piping in the recirculation loop.
5. The method according to claim 4 wherein calculating the pressure drop across the anode side of the stack includes using the equation:
Δ p anode =(1 −c piping )·(Δ p pump −Δp separator )
where Δp anode is the pressure drop across the anode side of the stack, c piping is the pressure drop across the piping in the recirculation loop, Δp pump is the measured pressure drop across the pump and Δp separator is the pressure drop across the water separator.
6. The method according to claim 1 wherein the density of the recirculation gas is calculated by the equation:
ρ
=
p
·
∑
n
i
·
M
W
i
nRT
=
p
·
∑
n
i
n
·
M
W
i
RT
where x is the speed of the pump, ρ is the density, p is a measured pressure, T is the measured temperature, MW is the molecular weight of the gas,
n
i
n
is the fractions of specific gases and n is moles of the gas.
7. The method according to claim 1 wherein an accurate value for the percentage of hydrogen in the recirculation gas is provided after a few cycles of calculating the pressure drop across the anode side of the stack, calculating the volume flow of the recirculation gas of the anode side of the stack and calculating the density of the recirculation gas.
8. The method according to claim 1 further comprising opening a bleed valve in the recirculation loop for bleeding the recirculation gas if the percentage of hydrogen falls below a predetermined percentage.