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Phenomenological Model of Electrochemically Active Surface Area Loss Mechanisms in the Cathode Catalyst Layer
Steven G. Rinaldo,a,b Wendy Lee,b Jürgen Stumper,b and Michael Eikerling.a
Department of Chemistry, Simon Fraser University,a and the Automotive Fuel Cell Cooperation Corporation,b Burnaby, BC, Canada.
1. Introduction Durability and lifetime continue to be foremost issues in polymer electrolyte fuel cell (PEFC) development. Performance issues arise due to the instability of functional materials found in the fuel cell. These include, but are not limited to, the catalyst support, polymer electrolyte membrane (PEM) and dispersed nanoparticle catalyst. Platinum, the hitherto irreplaceable catalyst is thermodynamically unstable at high potential and low pH as suggested by the potential-pH diagrams developed by Pourbaix; it is also well known that potential cycling exacerbates this instability. Mechanisms of Pt mass loss and redistribution in the cathode catalyst layer (CCL) are sensitive to materials properties, CCL structure as well as conditions such as pH, temperature and potential. The primary effect of Pt mass loss and redistribution is the loss of electrochemically active surface area. The cartoon below illustrates the relative importance of various ECSA loss mechanisms under normal operating conditions
decreasing influence on ECSA loss under normal conditions
dissolution redeposition agglomeration detachment
2. General Degradation Model (illustrative) particle radius distribution (PRD)
in the cathode catalyst layer
degradation stressor1
PRD temporal evolution (imaging)ECSA temporal evolution(voltammetry)decoupling mechanisms is difficult
3. General Degradation Model (mathematical) spatially invariant PRD continuity equation (PRD temporal evolution)2,3,4
0 0
, 1, ', d ' , ', d ' ,
2 agg agg det
d- ', ' , '
d
rK r r r K r r K t
t
rf r t
f r t f r t r f r t f r t r f r tt r
Pt mass balance (closed CCL) and ECSA temporal evolution
particles interact via mean-field concentration
3Pt Pt Pt CCL
0
4, d
3
M C t r f r t r
2ECSA
0
4 , d
S r f r t r
4. Simplifications (minor support corrosion)
(i) PRD/ECSA temporal evolution determined by dissolution and redeposition
(ii) particle radius change controlled by Gibbs-Thomson interfacial kinetics
dep diss flat 0Pt Pt Pt Pt exp
d
d
r
t R
k C t k Cr
diss flat
dep dissPt Pt0 Pt Pt Ptflat
0 0 Pt
k Crt T t C t k k
R R C
flat 4Pt Pt Pt 0
CCL CCL
4
3
M C R
, 1, exp 0
ff 3
0
, d 1
f
(iii) dimensionless governing equations
5. Main Effective Parameters
6. Dissolution Limit (Potentiostatic)5 1
7. Dissolution Limit (Potential Cycling)6
model evaluation via an in-situ transmission electron microscopy study extracted surface tension and dissolution rate suggest cathodic dissolution mechanism of dissolution changes; potentiostatic vs. potential cycling
8. Redeposition (Parametric Study) 1
9. Conclusions and Outlook • good agreement with experimental data (potentiostatic and cycling)• predict PRD evolution based on ECSA loss and vice-versa• relate observable phenomena (PRD, ECSA) to material properties (surface tension)• fundamental link between Pt oxide formation/reduction and Pt mass balance• key aspect is the relation between oxide mediated Pt dissolution and ECSA loss
outlook• evaluate surface tension of nanoparticles under electrochemical conditions• deconvolution of ECSA loss curves insight into mechanism(s)• refine sub-model of particle radius change dissolution mechanism
effPt
0
2RRT
(A) surface tension ( ) strong function of oxide coverage (PtO)
(B) extended surface dissolution rate ( ) Pt/PtO dissolution mechanisms
(C) redeposition coefficient ( ), Pt mass/electrode volume ( )
dissPtk
effPt
CCL
3322
33
main factors:• particle size • electrode potential• oxide growth/reductionagglomeration
dissolution/redeposition
detachment
main factors: • temperature• support properties• particle movement
main factors: • support corrosion
22
11
11
11 22 33
1. K.J.J. Mayrhofer, Electrochem. Commun., 10, 1144 (2008).2. M. Smoluchowski, Physik. Zeitschr., 17 (1916), pp. 557–599.3. I. M. Lifshitz and V. V. Slyozov, J. Phys. Chem. Solids., 19, 35 (1961).4. C. Wagner, Z. Elektrochem., 65, 581 (1961).5. S.G. Rinaldo, J. Stumper, and M. Eikerling, J. Phys. Chem. C., 114, 5773 (2010).6. S.G. Rinaldo, W. Lee, J. Stumper and M. Eikerling, ESL, 14, B47 (2011).
inte
rrela
ted
mech
an
ism
s
,, 0d
d
r
t
f r tf r t
t r 3
Pt Pt Pt CCL
0
4, d
3
M C t r f r t r 2ECSA
0
4 , d
S r f r t r
small particles dissolve faster effective dissolution rate
analytical parametric solution via method of characteristics parametric study revealed strong influence of surface tension on ECSA loss dissolution rate dispersion could result in mean radius increases with ECSA loss
1.0 0.8 0.6 0.4 0.2 0.01.0
1.5
2.0
2.5
mean r
adiu
s (n
m)
normalized ECSA
Pt = 0.2 J m-2
Pt = 0.7 J m-2
Pt = 1.2 J m-2
Pt = 1.7 J m-2
0 1 2 30.0
0.4
0.8
1.2
1.6
0 1 2 30.0
0.4
0.8
1.2
1.6
0 1 2 30.0
0.4
0.8
1.2
1.6
0 1 2 30.0
0.4
0.8
1.2
1.6
0 h 60 h 200 h 400 h 800 h
Pt = 0.2 J m-2
(d)(c)
(b)
(a) 0 h 0.6 h 1.6 h 16 h 40 h
Pt = 0.7 J m-2
0 h 0.1 h 0.5 h 1.4 h 4 h
Pt = 1.2 J m-2
Pt particle radius (nm)
num
ber
of p
art
icle
s (a
rb. u
nits
)
0 h 0.01 h 0.04 h 0.2 h 1 h
Pt = 1.7 J m-2
10-410-310-210-1100 101 102 1030.00
0.25
0.50
0.75
1.00
Pt = 0.2 J m-2
Pt = 0.7 J m-2
Pt = 1.2 J m-2
Pt = 1.7 J m-2n
orm
aliz
ed E
CS
A
time (h)
0 1 2 3 4 50.00
0.25
0.50
0.75
1.00
0 1 2 3 4 5 60.00
0.25
0.50
0.75
1.00 TEM, Shao et al. 0 h model, 0 h
num
ber
of par
ticl
es (ar
b. units) TEM, Shao et al. 192 h
model, 192 h
Pt particle radius (nm)
0 50 100 150 2000.4
0.5
0.6
0.7
0.8
0.9
1.0 model Shao et al.
norm
aliz
ed E
CS
A
time (h)
comparison with potentiostatic experiments in high/low potential regions fitted surface tension values indicate dissolution occurs at a PtO interface ratio of surface tension (high/low potential) agree with experimental ratios extended surface dissolution rate trends follow experiment
0 2 4
0.5
0.6
0.7
0.8
0.9
1.0(b)(a)
Ref. 25, CO-stripping 0 h Ref. 25, CO-stripping 2 h Ref. 25, CO-stripping 4 h this work, Eq. 4
norm
aliz
ed E
CS
A
potential cycling treatment time (h)
1 2 3 4 5 6
0
20
40
60
80
100
120 this work, 0 h Ref. 25, IL-TEM, 0 h this work, 2 h Ref. 25, IL-TEM, 2 h this work, 4 h Ref. 25, IL-TEM, 4 h
num
ber
of p
artic
les
per
dr in
terv
al
particle radius (nm)
0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.40
1
2
3
4
effective dissolution region
Ref. 8, potentiostatic ECSA Ref. 32, anodic DST Ref. 32, cathodic DST Ref. 33, Pt CV
this work, potential cycling ECSA
Ref. 30, PtO DFT
Ref. 29, Pt DFT
Ref. 31, Pt ZCM
surf
ace
tens
ion (
J m
-2)
potential (V vs. SHE)
Ref. 28, Pt DFT
-100
-80
-60
-40
-20
0
20
40
60
80
cur
rent de
nsi
ty (A
cm
-2)
1 2 3 4 5 6 7 80
20
40
60
80
100
120
1 2 3 4 5 6 7 80
20
40
60
80
100
120
1 2 3 4 5 6 7 80
20
40
60
80
100
120
1 2 3 4 5 6 7 80
20
40
60
80
100
120
= 1 x 10-4
= 10-1 = 2 x 10-4
= 1 x 10-6
num
ber
of par
ticl
es (ar
b. units)
particle radius (nm)
0.0 5.0x10-3 1.0x10-2
0.0
0.2
0.4
0.6
0.8
1.0 = 10-1
= 2 x 10-4
= 1 x 10-4
= 1 x 10-6
analytical, = 0
norm
aliz
ed E
CS
A
dimensionless time
0.0 5.0x10-3 1.0x10-20
25
50
75
100
125
150
175
= 10-1
= 2 x 10-4
= 1 x 10-4
= 1 x 10-6
dim
ensio
nle
ss c
oncentr
ation
dimensionless time
10-6 10-4 10-2 100 1020.0
0.2
0.4
0.6
0.8
1.0 R
0 = 13.2; = 0.0001
norm
aliz
ed E
CSA
log
transition
dissolution
redeposition
parametric study on the effect of redeposition loss of small particles and growth of large particles mean-field concentration approaches asymptotic value two ECSA loss mechanisms identified
• dissolution induced ECSA loss• redeposition induced ECSA loss