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7/27/2019 YGShul
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Nano Material Applicationsin Fuel Cell
Dept. of Chemical Eng. Yonsei Univ.
Prof. Y.G. Shul, H.S. Kim
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Nano Materials in Fuel Cell
Hydrogen
Release Catalyst Novel Anode Catalyst
Organic-Inorganic
Membrane
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Fuel Cell Applications
Heteropolyacid(HPA)-SiO2 nanoparticles for high
temperature operation of a direct methanol fuelcell
Preparation and characterization of new carbon
for fuel cell application Pulse Electrodeposition for Preparing PEM Fuel
Cell Electrode
Investigation of alloy catalyst for acceleratinghydrogen release from NaBH4
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In this study
SiO2
Heteropoly acid
Nano scale. .. .
..... .
...
. ... .
. .
..... .
.... .
.
. .. ...... .
.... .
.. .. ...... .
.... .
.. .. ...... .
.... .
.. .. ...... .
.... .
.
. .. ...... .
.... .
.. .. ...... .
.... .
.. .. ...... .
.... .
.. .. ...... .
.... .
.
Preparation nanohybride particle (HPA/SiO2)By micro emulsion technique
Characterization :
TEM, Solid state NMR, TMP adsorption, N2 adsorption, FT-IR
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Heteropolyacid-SiO2 nanoparticles
TEM image of heteropolyacid-SiO2 nanoparticle(R=2, HPA 30%, 24hr)
TEM image of heteropolyacid-SiO2 nanoparticle(R=2, X=30%, 12hr)
100 nm 100nm
R= [H2O]/[AOT]X=[Heteropolyacid]
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31P MAS NMR
Chemical shift (, ppm)
-20-18-16-14-12-10
Heteropolyacid
100nm
500nm
Bulk
Dehydration
Fig. 31P MAS NMR spectra of heteropolyacid and HPA/SiO2
H3PW12O406H2O
-15.6ppm
-15.3ppm
-15.1ppm
-15.0ppm
Referenced from
- M.Misono et al., J.Phys.Chem.B., 104 (2000) 8108
- F.Lefebvre et al., J.Chem.Soc.Chem.Commun, (1992) 756
Dehydration of heteropolyacidHeteropolyacid < nanoparticle < Bulk powder
Trapping of acidic proton to OH group
Si
OHH+
Si
OHH+
Si
OHH+
34012 ][ OPW
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13C CP MAS NMR
13C CP MAS NMR spectra(a) thiol- and (b) sulfonic-functionalized heteropolyacid-SiO2 nanoparticle.
Chemical shift (, ppm)
0102030405060
(a)
(b)
27.9 ppm
11.4 ppm18.2 ppm
54.0 ppm
Chemical shift (, ppm)
0102030405060
(a)
(b)
27.9 ppm
11.4 ppm18.2 ppm
54.0 ppm
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Preparation of inorganic particlesin microemulsion
H2O
HPA
Cyclohexane
TEOS
Si(OR)4
+ 4H2O Si(OH)
4+ 4ROH
Si-OH + HO-Si Si-O-Si + H2O
Sol-gel process
O
O
O
O
SO3
-Na
+
Aerosol-OT
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Surface area vs. nano HPA/SiO2
Pore size (A)
0 20 40 60 80
DV/D
R(cm
3/g)
0.00
0.01
0.02
0.03
0.04
0.05
100nm HPA/SiO2
500nm HPA/SiO2Bulk HPA/SiO2
1 2 3
Porefraction
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1 2 3 4
BETSurfacearea
(m2/g)
0
100
200
300
400
500
600
Surface area Pore size distribution
HPA 100nm00nmulk
Pore ratio
R > 3nm
100nm00nmulk
R < 1nm
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Application to DMFC
Pressure gauge
Methanol
2M solution.
Fuel pump
Fuel heater
Cell
Needlevalve
flowmeter
2way
valve
O2
Tank
G.C
6 way
valve
Pressure gauge
Methanol
2M solution.
Fuel pump
Fuel heater
Cell
Needlevalve
flowmeter
2way
valve
O2
Tank
G.C
6 way
valve
Heteropolyacid Proton conductivity
Silica particle Methanol blocker
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Polysulfone/nanoparticle compositemembrane
45 50 55 60 65 70 75 80 85 90 95 100 105 1100
20
40
60
80
100
Z''(o
hm)
Z'(ohm)Cell temperature (
oC)
20 40 60 80 100 120 140
Methanolc
rossoverrate
(mol/cm
2m
in)
0
2
4
6
8
10
12
14
16
18
Sulfonated polysulfone membraneComposite membrane
Heteropolyacid-SiO2 nanoparticleHeteropolyacid-SiO2 nanoparticle
1.4 10-3 S/cm 6.510-5 S/cm
Complex impedance response(a) and methanol crossover rate(b) of the sulfonated polysulfone
and sulfonated polysulfone / heteropolyacid SiO2 nanoparticle composite membrane.
(a) (b)
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Nafion/nanoparticle composite membrane
Content of nanoparticles (%)
0 5 10 15 20 25
condu
ctivityx10
2(
S/cm)
0
2
4
6
8
10
Temperature (oC)
0 20 40 60 80 100 120 140 160
Crossove
rrate(mol/cm
2*min)
0
20
40
60
80
100
Nafion membrane
Composite membrane
Proton conductivity(a) and methanol crossover rate(b) of the sulfonated polysulfoneand sulfonated polysulfone / heteropolyacid SiO2 nanoparticle composite membrane.
(a) (b)
Reduction of methanol crossover
A little decrease of proton conductivity
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Nafion-HPA/SiO2 composite membrane
Current density (mA/cm2)
0 50 100 150 200 250 300
Ce
llvo
ltage
(V)
0.0
0.2
0.4
0.6
0.8
80oC
160oC
200oC
Power
dens
ity
(mW/cm
2)
0
10
20
30
40
50
60
Wavenumber (cm-1
)
1000150020002500300035004000
Transmi
ttance
(%)
0
20
40
60
80
100
Heteropolyacid - SiO2
nanoparticle
Sulfonated heteropolyacid - SiO2
nanoparticle
FT-IR spectra of sulfonated heteropolyacid-SiO2 nanoparticle
(Nafion / sulfonated heteropolyacid-SiO2 nanoparticle composite membrane)
H2O H3O+
DMFC performance of composite membrane
Improvement of DMFC performance by increasing the cell temperature
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Research of carbon material application
Caronstructure
FCapplication
Performance remark Reference
Pt/CNT PEMFC 0.7V,
0.7 mA/cm2
(50oC)
high electrocatalytic activity for oxygen reduction
3.60.3nm
J.of powersources
139(2005) 73
Pt/mesoporous carbon
(SBA-15)
DMFC 0.4V,
135 mA/cm2 (65oC)
Great potentiality for DMFC support
Johnson Mattheyat
0.4V, 135 mA/cm2 (80oC)
J.Of powersources
130 (2005)
PtSn/
MWNT
DEFC 0.4V,
100 mA/cm2Improvement in liquid mass transfer for catalyst-
3nm
PtSn/XC-72
0.4V, 80 mA/cm2
Carbon 42
(2004)
Carbon
fiber
Mg-H2O2
Semi-fuelcell
1.5V,
300mA/cm2
Similar reference with Pt-Ir on carbon paper
Mg: anode
Microfiber carbon :cathode
cathode side: 0.20M H2O2
J.Of power
sources 96(2001) 240
Carbonnanocoil
DMFC 0.4V ,
170mA/cm2
(60oC)
Great potentiality for DMFC support material Angew. Chem
2003,115,
4488
Carbonnanohorn
DMFC 0.4V ,
130mA/cm2NEC
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I-V curve for electrodes with commercialPt/C and Pt/C+ Pt/ACF (900)
Current density ( A/cm2
)
0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4
Vo
ltage(V)
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
1.1
Commercial Pt/C
Commertial Pt/C (70%)+ Pt/ACF(30%.400oC)
Commertial Pt/C (70%)+ Pt/ACF(30%.900
o
C)
Performance increasing
Commercial Pt/C Pt/C+Pt/ACF (400) Pt/C+Pt/ACF (900)Current density ( mA/cm2 ) 710 807 960
Cell Temp. : 80, Humidify condition : RH% 100 anode and cathode, Flow rate: Stoichiometry 1.5(Anode):2.0(Cathode)
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Impedance for the electrodes manufacturedwith Pt/C, Pt/ACF(900) catalysts
Z' / Ohm
0.06 0.08 0.10 0.12 0.14 0.16 0.18 0.20 0.22 0.24 0.26
-Z''/O
hm
0.00
0.02
0.04
0.06
0.08
0.10
Pt/ACF ( 400oC )
Pt/ACF ( 900oC )
Z' / Ohm
0.0 0.1 0.2 0.3 0.4 0.5
-Z''/O
hm
0.00
0.05
0.10
0.15
0.20
0.25
0.30
Pt/ACF ( 400oC )
Pt/ACF ( 900oC )
Impedance spectra at 0.8VImpedance spectra at 0.7V
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Specific surface area and average porediameter of the CNF treated by KOH
58.01303.54950-1h
62.37341.87900-3h
54.41375.52Modified method
44.33460.10900-2h
48.0645.53900-1h48.80509.95800-1h
46.07444.18750-1h
62.21107.60No activation
5H
Avg. Pore diameter( )
Surf. area(m2 /g)ctivation conditionNF
58.01303.54950-1h
62.37341.87900-3h
54.41375.52Modified method
44.33460.10900-2h
48.0645.53900-1h48.80509.95800-1h
46.07444.18750-1h
62.21107.60No activation
5H
Avg. Pore diameter( )
Surf. area(m2 /g)ctivation conditionNF
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SEM - CNFs named 5H
pristine
MDF(900-2h)
800-1h
900-2h
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TEM - 60wt% Pt-Ru/CNF
50 nm 50 nm 50 nm
(a) (b) (c)A/(900-2h) B/(900-2h) B/MDF(900-2h)
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Growth of nanofiber on ACF
micropores
Surface and Pores of
Activated Carbon Fiber
Reduction in He/H2
Synthesis from C2H
4/H2
a
b a, b
c
inactive
H2 C2H4
Impregnation of metal salt solution
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Preparation of various carbon substrates
CNF/ACF
Fig. SEM images of carbon nano fibers grown on ACFFig. SEM images of carbon nano fibers grown on ACFFig. SEM images of carbon nano fibers grown on ACF
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Preparation of platinum on ACF-CNFs
TEM Image of Pt/ACF-CNFs
Fig. TEM images of Platinum oncarbon nanofibers grown on ACF
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Preparation of platinum on ACF-CNFs
XRD patterns of Pt/ACF-CNFs
Fig. XRD pattern of Pt/ACF-CNFs
2 th e ta
3 0 4 0 5 0 6 0 7 0 8 0
Intensity(a.u.)
P t / A C F - C N F s
P t / C ( C o m m e r c ia l )
Pt(1 1 1)
Pt(2 0 0)Pt(2 2 0)
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Single cell performance
Fig. The performance of Pt/ACF-CNFs used in anode catalyst
Cell Temp. : 80, Humidify condition : RH% 100 anode and cathode, Stoichiometry anode: cathode = 1.5: 2.0Membrane : nafion 112:, anode : 20%Pt/C, cathode : 20%Pt/C and 20%Pt/ACF-CNFs+20%Pt/C, Back pressure : 1bar
Current density(A/cm2)
0.0 0.5 1.0 1.5 2.0 2.5 3.0
Vo
ltage
(V)
0.4
0.5
0.6
0.7
0.8
0.9
1.0
Pt/ACF-CNFs 30%
Pt/C
Pt/ACF-CNFs 20%
Pt/ACF-CNFs 100%
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Schematic Diagram of The ElectrodePrepared by Pulse Electrodeposition
Ion exchange
membrane
Carbon clothe Hydrophobic
carbon layer
Catalystparticle
Reactant gas
Hydrophilic
carbon layer
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Back-Scattered Electron Image and Pt LineScan of The Cross Section of MEA using
EPMA
PC deposition Pt/C layer
membrane
E-TEK Pt/C layer
E-TEK GDL
100.0
0.0
0.0
200.0
161.0Microne
Pt
Distance (m)
PC layer
membraneGDL GDLETEK layer
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ESEM Image and Pt Concentration Profile ofthe Cross Section of MEA Using EDX Spot
Analysis
Distance from membrane (m)
0 2 4 6 8 10 12 14
Ptw
t%
0
20
40
60
80
E-TEK electrode
PC deposition electrode
E-TEK electrode
PC deposition electrode
Membrane
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Comparison of MEA performance betweenpulse electrodeposited electrode and TKK
Current density (A/cm
2
)
0.0 0.3 0.6 0.9 1.2 1.5 1.8 2.1 2.4 2.7
Potential(V)
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
TKK (0.4mg/cm2
)PC (0.32mg/cm
2)
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High Throughput Screening (HTS) test
Hydrogen release rate of metal catalysts can bemeasured without catalyst synthesis procedure
To apply metal alloy catalyst, amounts of precursorsolutions can be mixed to accurate ratios.
Schematic diagram of simplified HTS test microreactors
Coolant
Coolant
H2
NaBH4Reduction Hydrolysis
H2Mixed
Precursor
SolutionRuCl3
Co(NO3)2
FeCl2
..
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Hydrogen release test (Ternary alloy)
0
5
10
15
20
25
30
Hydrogen
Ge
nerationRate(Lmin-1g-1)
Ru
Co Ni
0
5
10
15
20
25
30
Hydrogen
GenerationRate(Lmin-1g-1)
Ru
Co Fe
Ru:Co:Fe = 60:20:20
(wt%)
Hydrogen release rate of (a) Ru-Co-Ni, (b) Ru-Co-Fefrom 10 wt% NaBH4 solution with 4 wt% NaOH
(Temperature fixed to 25C)
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XRD Patterns
XRD Patterns of (a) Ru/ACF; (b) NaBH4-reduced
Ru0.6Co0.2Fe0.2/ACF; (c) NaBH4 and H2-reducedRu0.6Co0.2Fe0.2/ACF catalyst
2 theta
30 40 50 60 70
Intensity
RuCoFe
CoFe2O
4
(a)
(b)
(c)
Co and Fe were notreduced completely
when NaBH4 only wasused for reduction. After the additional
reduction by usinghydrogen, CoFe alloywere shown
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RuCoFe/ACF nanocatalyst
1000 / T
3.20 3.25 3.30 3.35 3.40 3.45 3.50
lnk
1.0
1.5
2.0
2.5
3.0
3.5
(a)
(b)
(d)
(e)
(c)
T / oC
10 15 20 25 30 35 40
H2ReleaseRate/Lm
in-1gRu
-1
0
20
40
60
80
100
(a)
(b)
(d)
(e)
(c)
catalyst Reduction
Agent
hydrogen release rate
at 25 C (Lmin-1gRu-1)
Activation Energy
(kJmol-1)
(a)
10 wt% Ru/ACF H2 14.21 59.23
(b)
16 wt% Ru0.6Co0.2Fe0.2/ACF H2 22.63 47.91
(c) 16 wt% Ru0.6Co0.2Fe0.2/ACF NaBH4 34.37 50.54
(d)
13 wt% Ru0.75Co0.25/ACF NaBH4 + H2 37.12 45.44
(e 16 wt% Ru0.6Co0.2Fe0.2/ACF NaBH4 + H2 41.73 44.01
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Conclusions
Nano materials may lead to drastic improvement in fuel cellapplication
1)Nanohybride electrolyte (HPA-SiO2+Nafion) waseffective for the high temperature operating of DMFC
2)New nano carbons are promising to enhance the catalytic
activity in fuel cell3) Nano alloy will be effective to release control of the H2from chemical hydride (NaBH4, NH3BH3)
4) Electrodeposition is effective to reduce the amount of Ptloading
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Acknowledgement
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Backup slides
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Impedance spectra
Fig. Impedance spectra of single cell
Z'/Ohm
0.05 0.10 0.15 0.20 0.25
-Z''/Ohm
0.00
0.02
0.04
0.06
0.08
0.10
Pt/ACF-CNFs 30%
Pt/C
Pt/ACF-CNFs 20%
Pt/ACF-CNFs 100% Membrane resistance 0.063
Interfacial resistance
(Mixture ratio 20%Pt/C:20%Pt/ACF-CNFs)
Only 20% Pt/C 0.069
Only 20% Pt/ACF-CNFs 0.175
2:8 0.096
3:7 0.065
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Cyclic voltammogram
E /V
-0.2 0.0 0.2 0.4 0.6 0 .8 1.0 1.2
i/A
-1.0
-0.8
-0.6
-0.4
-0.2
0.0
0.2
0.4
Pt/C
Pt /ACF -CNT s 30%
Fig. Cyclic voltammograms of Pt/ACF-CNFs used oxygen
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Technical Barriers of Electrodes for PEMFuel Cells
Electrode performance 400 mA/cm2 at 0.8V with H
2
/Air and 1atm
Novel method of pulse electrodeposition
Pt-X alloy
Material Cost 0.2 g (Pt loading)/peak kW Non-precious catalyst (Pt-free)
Durability 40,000 hours operation with
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Why Pulse Electrodeposition(Dependence of Nucleation Rate on
Overpotential)
2
1 expbs
J KzekT
=
log i = +
K1 - rate constant
S - surface area occupied by oneatom on the surface of the nucleus
e - the charge of the electron
z - the electronic charge of the ion
k - the Boltzmann constant
T- the temperature b=P2/4S, where P is the perimeter and
S is the surface area
i current applied
, Tafel constants Overpotential 1: on time 2: off time Ip: peak current density
Ia: average current density
Duty cycle: 1/
Rate of 2D-nucleation * Tafel expression for overpotential
1 2
t5t4t3t2t1
Current
density
time
ip
ia
Pulse electrodeposition
Off time
Concentration of electrolyte is recoveredElectrodeposition at high current density
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Comparison of the Limiting Current Densitybetween Pulse and Direct Electrodeposition
diffusion model by H. Y. Cheh,
( )( )
l
dc l
i
i
a
0.4
1 0.2
=
0.6
0.8
1.0
a( )( )
( )( )( )( )( )
2
2
22 21
1
exp 2 1 18 11
2 1 exp 2 1 1
p l
dc l
j
i
i j a
j j a
=
=
2 2 1/ 4 (sec )D a =
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TEM and SEM image of Pt electrodepositedelectrodes
Pulse DC
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Polarization Curves of MEAs Prepared byDirect Current and Pulse Electrodeposition
Current density (A/cm2)
0.0 0.3 0.6 0.9 1.2 1.5 1.8 2.1 2.4
Po
ten
tia
l(V)
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
50mA/cm2
DC
200mA/cm2
PC
The conditions of pulse electrodeposition: 200mA/cm2 of peak current density,
5.2ms on time and 70ms off time. Total charge is fixed at 6C/cm
2
on both cases.
Nafion 112
Cell Temperature: 75 oC
H2/O2 (flow rate: 1.5/2 stoichiometric)
Pressure: 1atm
SEM Images of Pt Electrodeposited
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SEM Images of Pt ElectrodepositedElectrodes by D.C or P.C mode. (Total
charge is fixed at 6C/cm2 on both cases)
50mA/cm2
of D.C. electrodeposition 200mA/cm2
of peak current density,5.2ms on time and 70ms off time
Effect of the peak current density of pulse
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Effect of the peak current density of pulseelectrodeposition on the performance of the
PEM fuel cell
Current density (A/cm2)
0.0 0.3 0.6 0.9 1.2 1.5 1.8 2.1 2.4 2.7
Po
ten
tia
l(V)
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
10 mA/cm2
DC
30 mA/cm2
PC
100 mA/cm2 PC
200 mA/cm2
PC
400 mA/cm2
PC
600 mA/cm2
PC
Cyclic Voltammograms of the Electrodes
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Cyclic Voltammograms of the ElectrodesPrepared at Different Peak Current
Densities in Pulse Electrodeposition
Potential (V. Hg/Hg2SO
4)
-0.8 -0.6 -0.4 -0.2 0.0 0.2 0.4 0.6 0.8
Curren
tdens
ity
(mA/cm
2)
-1.5
-1.0
-0.5
0.0
0.5
1.0
200mA/cm2
100mA/cm2
400mA/cm2
30mA/cm2
600mA/cm2
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Effect of Charge Density on thePerformance of PEM Fuel Cell
Current density (A/cm2)
0.0 0.3 0.6 0.9 1.2 1.5 1.8 2.1 2.4 2.7 3.0
Potential(V)
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
6C/cm2
8C/cm2
13C/cm2
16C/cm2
Comparison of Pt line scan image in the
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Comparison of Pt line scan image in thecross section of the MEA
(A) 8C/cm2 and (B) 20C/cm2
Microns (m)
Cps Cps
300 300
0
0 0
0
40 40
Microns (m)
(A) (B)
Microns (m)
Cps Cps
300 300
0
0 0
0
40 40
Microns (m)
(A) (B)