transition metal oxide electrocatalysts for orr and oer · 2015. 9. 21. · 20 wt.% pt/c nico 2 o 4...
TRANSCRIPT
Transition metal oxide
electrocatalysts for
ORR and OER
Andrea E. Russell
Overview
• Water electrolysers
IrxRu
1-xO
2
• XAS
Ex-situ XANES
In-situ XANES
• Air electrodes for
Zn/Air batteries
NiCo2O
4
2
2H2O
4H++ 4e
- + O
2
Water electrolysis
• Hydrogen production
O2 evolution inefficiencies
• Electrocatalysts for OER
RuO2 and IrO
2
• Limitations
Cost
Dissolution of RuO4
3
H
H
H
H
PEM
O
O
H
O
H H
O
H H
+
+
+
+
-
- -
-
Energy
grid
IrxRu
1-xO
2 catalysts
4
30 40 50 60 70 80 90 100 110
2 / o
Ir0.25
Ru0.75
O2
Ir0.50
Ru0.50
O2
Ir0.75
Ru0.25
O2
RuO2
IrO2
32 33 34 35 36 37 38
2 / o
RuO2
Ir0.25
Ru0.75
O2
Ir0.50
Ru0.50
O2
Ir0.75
Ru0.25
O2
IrO2
• XRD indicates formation of a solid solution
• Series of materials prepared by Adams Fusion method
IrxRu
1-xO
2 catalysts
5
-2.1
0.0
2.1
0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4
-1.2
0.0
1.2
A
E (vs. RHE) / V
B
Jgeom
etr
ic / m
A c
m-2
-1.8
0.0
1.8
-2.1
0.0
2.1
0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4
-1.2
0.0
1.2 C
B
j geom
etr
ic / m
A c
m-2
A
E (vs. RHE) / V
IrO2
RuO2
Ir0.75
Ru0.25
O2
Ir0.5
Ru0.5
O2
Ir0.25
Ru0.55
O2
6 0.5 M H2SO
4 on GC electrode at 295K
1.3 1.4 1.5 1.6
0
20
40
60
IrO2
Ir0.75
Ru0.25
O2
Ir0.50
Ru0.50
O2
Ir0.25
Ru0.75
O2
RuO2
J
geo
me
tric / m
A c
m-2
E (vs. RHE) / V
IrxRu
1-xO
2 catalysts
7
IrxRu
1-xO
2 catalysts
0 250 500 750 10001.35
1.40
1.45
1.50
1.55
1.60
1.65
Ce
ll p
ote
ntia
l / V
Current density / mA cm-2
IrO2
Ir0.75
Ru0.25
O2
Ir0.50
Ru0.50
O2
Ir0.25
Ru0.75
O2
RuO2
PEM water electrolysis cell running at 60 °C, 20 bar
0 100 200 300 400 500 600 7001.5
1.6
1.7
1.8
1.9
2.0
Ce
ll p
ote
ntial / V
Time / h
IrO2
Ir0.75
Ru0.25
O2
Ir0.50
Ru0.50
O2
Ir0.25
Ru0.75
O2
RuO2
1 A cm-2
X-ray absorption spectroscopy
8
Io
It
XAS measurements
Transmission: m(E) measured directly using ion chambers.
Fluoresence: refilling of core-hole detected.
I = I0e-m E( )x
m(E )x = ln I0 / I( )
m(E )xµ I f / I( )
X-ray absorption spectroscopy
• XAS
XANES
– electronic structure
EXAFS
– local structure
10 M. Newville - APS
22100 22110 22120 22130 22140 22150 22160-0.2
0.0
0.2
0.4
0.6
0.8
1.0
1.2
1.4
N
orm
alis
ed a
bsorp
tion
Energy / eV
Ru foil
Ru(acac)3
RuO2
La4.87
Ru2O
12
SrRu2O
6
KRuO4
22120 22124 22128 221320.4
0.5
0.6
Ru edge - XANES Spectra
11
Edge position shifts to higher energy with increased
oxidation state – calibration curve from reference compounds
In-situ Cell
• Stable electrochemistry
• Rapid removal of evolved gas
• Stable in 1M KOH
• Clear x-ray fluorescence path
12
13
It
Detector
Electrolyte
flow
In-situ XANES – (Ir1-x
Rux)O
2
14
Ex situ 1.0 V 1.4 V 1.7 V 1.8 V 1.0 V4.7
4.8
4.9
5.0
5.1
5.2
5.3
5.4
5.5
5.6
Ir L
3 e
dg
e e
ne
rgy s
hift
/ e
V
Applied potential (vs. RHE)
IrO2
Ir0.75
Ru0.25
O2
Ir0.50
Ru0.50
O2
• Ir stabilises the oxidation state of the RuOx
Ex situ 1.0 V 1.4 V 1.7 V 1.8 V 1.0 V6.0
6.2
6.4
6.6
6.8
7.0
7.2
7.4
7.6
Ru K
-edge s
hift / eV
Applied potential (vs. RHE)
RuO2
Ir0.50
Ru0.50
O2
Ir0.75
Ru0.25
O2
Pyrochlores - OER
• (Na0.33
Ce0.67
)2(Ir
1-xRu
x)O
7
• Ref = (Ru0.9
Ir0.1
)O2
15 (a) OER LSV in 0.5M H2SO
4 (b) DEMS of pyrochlores during OER.
R.I. Walton et al.,
Angewandte Chemie.
2014
Pyrochlore – Ex-situ XANES
16
• Ruthenium in +4 oxidation state
• Iridium in +4.05 oxidation state
*pre-edge feature from the 1s-4d transition
Pyrochlores – In-situ XANES
• (Na0.33
Ce0.67
)2(Ir
1-xRu
x)O
7
• Increase in Ru ox. state
with increase in Ru
content
• Reduction in Ir ox. state
with increase in Ru
content
17
Zinc-air battery
18
Lee. J et al., Adv. Energy Mater., 2011, 1, 1, 34 - 50.
Electrocatalysts
19
Fuel Cells:
Acid environment
PtX particles on carbon
Metal/Air batteries:
Alkaline environment
NiCo2O
4 spinel particles
PEM Electrolyser:
Acid environment
IrxRu
1-xO
2
Catalyst Screening - RDE
• Spinels - AB2O
4
e.g. NiCo2O
4
• Perovskites – ABO3
e.g. LaNiO3
• Pyrochlores – A2B
2O
7
e.g. Pb2[Ru
2-xPb
x]O
7
20
1.3 1.4 1.5 1.6 1.7
0
25
50
75
100
j /
mA
cm
-2
E vs. RHE / V
LaNiO3
20 wt.% Pt/C
NiCo2O
4
Pb2(Ru
2-xPb
x)O
7-y
ORR comparison - RDE
21
0.6 0.7 0.8 0.9 1.0 1.1 1.2
-0.7
-0.6
-0.5
-0.4
-0.3
-0.2
-0.1
0.0
0.1
j / m
A c
m-2
E vs. RHE / V
LaNiO3
20 wt.% Pt/C
NiCo2O
4
Pb2(Ru2-x
Pbx)O
7-y
NiCo2O
4
• Phase purity & crystallinity
• Surface area
22
Synthesis method BET (m2 g-1)
Co-precipitation 68.2
Citrate 51.3
Ammonia 47.5
Glycine 32.7
TD- Methanol 12.6
TD - H2 O 6.8
10 20 30 40
Inte
nsity
2 Theta / Degrees
TD-H2O
TD-methanol
Ammonia
Glycine
Citric acid
Co-precipitation
NiCo2O
4
23 10 20 30 40
Inte
nsity
2 Theta / Degrees
TD-H2O
TD-methanol
Ammonia
Glycine
Citric acid
Co-precipitation
NiCo2O
4 cycling tests
24 Price S.W.T. et al., J. Power sources, 2014, 259, 43-49
Metal nanoparticles
• Metal-oxide supported on active catalyst
RuO2 → OER
Ag → ORR
25
Ruthenium
dioxide
Silver oxide
Bulk
NiCo2O
4
RuOx Modifcation
26 2.5 mg cm-2 NiCo
2O
4 on Toray at 333K, 200 cm
-2 O
2 in 8M KOH
ORR
OER
0 500 1000 1500 2000 2500 3000 3500
0.6
0.8
1.0
1.2
1.4
1.6
1.8
E v
s. R
HE
/ V
Time /s
TD - NiCo2O
4
Co-precip - NiCo2O
4
RuOx/NiCo
2O
4
Catalyst
Composition:
RuOx 0.13 mg
NiCo2O
4 2.37 mg
10 mA cm-2 20 mA cm
-2 50 mA cm
-2
RuOx stability
27 2.5 mg cm-2 NiCo
2O
4 on Toray at 333K, 200 cm
-2 O
2 in 8M KOH
0 10 20 30 40 50 60
-0.3
-0.2
-0.1
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
E v
s H
g/H
gO
/ V
Time / minutes
RuOx/NiCo
2O
4 1
st
RuOx/NiCo
2O
4 2
nd
RuOx/NiCo
2O
4 5
th
RuOx/NiCo
2O
4 10
th
10 mA cm-2
20 mA cm-2
50 mA cm-2
Acknowledgements
28
Members of research group:
Peter Richardson (now PDRA at Southampton)
Stephen WT Price (now at Diamond)
Stephen J Thompson (HMGCC in January)
Scott Gorman (Ilika in January)
Derek Pletcher – a retired colleague who won’t
Richard Walton - Warwick
Funded by:
EPSRC DTA & Ind. Case Studentships
EU FP7 POWAIR (C-Tech Innovation)
ITM Power
Johnson Matthey
Diamond
University of Southampton