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Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Control for a Polymer
Electrolyte Membrane Fuel Cell
Donald J. Chmielewski Kevin Lauzze
Department of Chemical
and Environmental Engineering
Illinois Institute of
Technology
Presented at the Annual Meeting of the AIChE: November 2005
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Outline
PEMFC Model
• Mat. & Energy Balances and Electrochemistry
• Operating Characteristics
Controller Design
• Power Set-Point Tracking
• Temperature / Humidity Regulation
• Oxygen Regulation
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
What is a Fuel Cell?
Fuel Cell
H2
Electric Power
Air
H2O
Answer:
A device that
converts
fuel directly into
electrical power
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Polymer Electrolyte Membrane
Fuel Cell (PEMFC)
N2
N2
N2
H2
H2
H2
H2
H2
H2
O2
O2
O2
H+
e- e-
Anode
Electrolyte
Cathode
O2 N2
N2
O2
O2
H+
H+
H+
H2O
H2O
H2O
H2O
H2O
H2O
Generated power due to
enthalpy released by
the reaction:
H2 + ½ O2 H2O
(H ~ 58 kcal/mole H2)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
The Fuel Cell Stack Stack
Fuel
Flow
Air
Flow
Current
Flow
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Dynamic Model of PEMFC
Cooling
Air In
Jacket
Exhaust
MEA
Anode
H2 In
Ecell
H2
Cathode
Air in
Cathode
Exhaust
O2
H2O
N2
Solid Material Current Collector
H+
H+
H+
H+
H+
H+
H+
H+
Insulator Parameters based
on 50 kW scale.
Pure hydrogen
feed
Air cooling is
assumed.
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Material Balances in the Cathode
memOH
in
catcat
Ncat
in
N
in
cat
N
cat
memOHOcat
in
O
in
cat
O
cat
memOHOHcat
in
OH
in
cat
OH
cat
ArCFCF
CFCFdt
dCV
ArCFCFdt
dCV
ArCFCFdt
dCV
2
22
2
222
2
222
2
2
1
2
1
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Energy Balances
memgensolambeff
soljacjacsolcatcatsol
solsolp
AQTTUA
TTUATTUAdt
dTVC
)(
)()(
Cathode Chamber Gas
Cooling Jacket Gas
Solid Material
)( catsol
catp
catcat
in
cat
in
catcat
cat TTC
UATFTF
dt
dTV
)( jacsol
jacp
jacjac
in
jac
in
jaccat
jac TTC
UATFTF
dt
dTV
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Rates
F
jr OH
22
eOHOHfgen PrHQ 22
)( ,
Rate of Reaction: (production of water per area of membrane)
Heat Generation Rate: (per area of membrane)
celle EjP Power Generation: (electrical energy generation rate per area of membrane)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Current Density Depends on the Load
The fuel cell
looks like a
battery to the
electrical world.
Ecell
Eo
Rint
Load
DC
Fuel Cell I=j*Acell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Changing the Reaction Rate
Eload
Eo
-Rint
I
Eload
= Eo - R
int*I
Eload
= Rload
*I
Eload
Eo
Rint
DC
Battery I
Rload
F
/2 n
AIr mem
OH
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Electrochemistry
mtohmactnercell EEEEE
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Electrochemistry
mtohmactnercell EEEEE
OH
OHsoloner
P
PP
F
RTEE
2
22
2/1
ln2
Nernst Potential:
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Electrochemistry
mtohmactnercell EEEEE
mem
memmemohm
A
tjAIRE
Ohmic Loss:
• ~ ionic conductivity of the membrane depends on humidification levels
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Ohmic Resistance
)(2 TP
PxRH
satOH
xH2O = 0.35
humidity with increases
, ty,conductivi Ionic
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Partial PEMFC Polarization Curve
0 2000
mtohmactnercell EEEEE
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
PEMFC Polarization Curve
0 2000
mtohmactnercell EEEEE
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
PEMFC Polarization Curve
mtohmactnercell EEEEE
)/(/ln
2
122
)( o
O
s
O
o
ooosol
act CCjjjjF
RTE
Activation Loss:
22
/ln22
1 )(
O
s
Osol
mt CCF
RTE
Mass Transfer Loss:
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Surface Concentrations
222
)()2/1( O
s
OOH CCKr
Mass Transfer Rate :
/)1(1 RH
o eKK
Mass Transfer Coefficient :
(assuming O2 is the rate limiting species)
• ~ porosity coefficient
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Flooding Resistance via the MTC
0 20 40 60 80 1000
0.5
1
1.5
2x 10
-3
Relative Humidity (%)
Mass
Tra
nsf
er
Co
eff
icie
nt
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Efficient Operation
xw = 0.35
humidity with increases , ty,conductivi Ionic
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Outline
PEMFC Model
• Mat. & Energy Balances and Electrochemistry
• Operating Characteristics
Controller Design
• Power Set-Point Tracking
• Temperature / Humidity Regulation
• Oxygen Regulation
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Set-Point Tracking
Transportation Applications
PEMFCPower
Controller
Pe(sp) MV
Pe
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Selecting the Power Output
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Selecting the Power Output
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Selecting the Power Output
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Selecting the Power Output
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
PEMFCE
cell
j
+- PI
j(sp)
Pe
PI
+
-
Pe(sp)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
PEMFCE
cell
j
+- PI
j(sp)
Pe
PI
+
-
Pe(sp)
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
PEMFCE
cell
j
+- PI
j(sp)
Pe
PI
+
-
Pe(sp)
Cooling
Air In
Jacket
Exhaust
MEA
Anode
H2 In
Ecell
H2
Cathode
Air in
Cathode
Exhaust
O2
H2O
N2
Solid Material Current Collector
H+
H+
H+
H+
H+
H+
H+
H+
Insulator
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
0 5 10 15 20
0.17
0.18
0.19
Time (seconds)
Po
wer
Den
sity
(w
atts
/cm
2)
(sp) e
e P P
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
0 5 10 15 20 25
200
210
220
230
Time (seconds)
Cu
rren
t D
ensi
ty (
mA
/cm
2)
0 5 10 15 20 250.82
0.83
0.84
0.85
Time (seconds)
Cel
l V
olt
age
(V)
j
E cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
0 5 10 15 20 25
200
210
220
230
Time (seconds)
Cu
rren
t D
ensi
ty (
mA
/cm
2)
0 5 10 15 20 250.82
0.83
0.84
0.85
Time (seconds)
Cel
l V
olt
age
(V)
j
E cell
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller Flooding
0 5 10 15 20 2564
66
68
70
72
74
Time (seconds)
Tem
per
ature
(C
elsi
us)
0 5 10 15 20 2590
92
94
96
98
100
Rel
ativ
e H
um
idit
y (
%)
RH
cat T
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
0 5 10 15 20 25
0.18
0.19
0.2
0.21
0.22
Time (seconds)
Pow
er D
ensi
ty (
wat
ts/c
m2)
P e (sp) P e
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller Failure
0 5 10 15 20 25200
300
400
Time (seconds)
Cu
rren
t D
ensi
ty (
mA
/cm
2)
0 5 10 15 20 250.5
0.6
0.7
0.8
Cel
l V
olt
age
(V)
j
cell E
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller Failure
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller
0 5 10 15 20 25
0.18
0.19
0.2
0.21
0.22
Time (seconds)
Pow
er D
ensi
ty (
wat
ts/c
m2)
P e (sp) P e
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller Failure
0 5 10 15 20 2570
80
90
100
Time (seconds)
Tem
per
atu
re (
Cel
siu
s)
0 5 10 15 20 2570
80
90
100
Rel
ativ
e H
um
idit
y (
%)
cat T
RH
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Power Controller Failure
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Temperature / RH Controller
PEMFC
Fjac
Tcat
+-
PIT
cat(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
RH(sp)
+-
PI
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
PEMFC
Fjac
Tcat
+-
PIT
cat(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
RH(sp)
+-
PI
Temperature / RH Controller
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
PEMFC
Fjac
Tcat
+-
PIT
cat(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
RH(sp)
+-
PI
Temperature / RH Controller
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
PEMFC
Fjac
Tcat
+-
PIT
cat(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
RH(sp)
+-
PI
Temperature / RH Controller
Cooling
Air In
Jacket
Exhaust
MEA
Anode
H2 In
Ecell
H2
Cathode
Air in
Cathode
Exhaust
O2
H2O
N2
Solid Material Current Collector
H+
H+
H+
H+
H+
H+
H+
H+
Insulator
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Temperature / RH Controller
0 20 40 60 800.18
0.2
0.22
0.24
0.26
0.28
0.3P
ow
er D
ensi
ty (
wat
ts/c
m2)
e P (sp)
e P
Time (seconds)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Temperature / RH Controller
0 20 40 60 8065
70
75
80
85
Time (seconds)
Tem
per
atu
re (
Cel
siu
s)
0 20 40 60 8080
85
90
95
100
Rel
ativ
e H
um
idit
y (
%)
cat T
(sp)
cat T
RH
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Oxygen Controller
PEMFC
Fjac
Tcat
RH(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
ControllerRH,
+-
PIF
cat
xO2
xO2
(sp)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Oxygen Controller
PEMFC
Fjac
Tcat
RH(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
ControllerRH,
+-
PIF
cat
xO2
xO2
(sp)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Oxygen Controller
PEMFC
Fjac
Tcat
RH(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
ControllerRH,
+-
PIF
cat
xO2
xO2
(sp)
Cooling
Air In
Jacket
Exhaust
MEA
Anode
H2 In
Ecell
H2
Cathode
Air in
Cathode
Exhaust
O2
H2O
N2
Solid Material Current Collector
H+
H+
H+
H+
H+
H+
H+
H+
Insulator
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Oxygen Controller
0 100 200 300 4000
0.1
0.2
0.3
0.4
0.5
0.6
Time (seconds)
Po
wer
Den
sity
(w
atts
/cm
2)
P P
e
e
(sp)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Oxygen Controller
0 100 200 300 4000.05
0.1
0.15
0.2
0.25
Time (seconds)
Mo
le f
ract
ion o
f oxyg
en
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Oxygen Controller
0 100 200 300 40040
50
60
70
80
90
100
Time (seconds)
Temperature (Celsius)
Relative Humidity (%)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Efficient Operation
eq
cell
E
E
Definition of Efficiency:
F
HE
OHf
eq2
2,
where
0 200 400 600 800 10000
0.2
0.4
0.6
0.8
1
1.2
1.4
Current Density (mA/cm2)
Cel
l V
olt
age
(V)
0 200 400 600 800 10000
0.05
0.1
0.15
0.2
0.25
0.3
0.35
Po
wer
Den
sity
(w
atts
/cm
2)
E
eP
cell
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Available Power and Efficiency
0.17 0.18 0.19 0.2 0.21 0.22
55
60
65
70
75
Power Density (watts/cm2)
Eff
icie
ncy
(%
)
Power Control
PEMFCE
cell
j
+- PI
j(sp)
Pe
PI
+
-
Pe(sp)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Available Power and Efficiency
0 0.05 0.1 0.15 0.2 0.25 0.3
55
60
65
70
75
Power Density (watts/cm2)
Eff
icie
ncy
(%
)
Power Control
Power & Humidity Control
PEMFC
Fjac
Tcat
+-
PIT
cat(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
RH(sp)
+-
PI
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Available Power and Efficiency
0 0.1 0.2 0.3 0.4 0.5 0.6
55
60
65
70
75
Power Density (watts/cm2)
Eff
icie
ncy
(%
)
Power Control
Power & Humidity Control
Power, Humidity & Oxygen Control PEMFC
Fjac
Tcat
RH(sp)
Power
Controller
Pe(sp)
Ecell
Pe, j
RH
ControllerRH,
+-
PIF
cat
xO2
xO2
(sp)
Department of Chemical and Environmental Engineering
Illinois Institute of Technology
Acknowledgements
• Students:
Ayman Al-Qattan Yongyou Hu
Janet Ruettiger
• Collaborators:
Said Al-Hallaj J. Robert Selman
Vijay Ramani Satish Parulekar
Jai Prakash
• Funding:
Argonne National Laboratory
Graduate College, IIT
Armour College of Engineering, IIT
Department of Chemical & Environmental Engineering, IIT