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Atomic Layer Deposition of Zirconium Oxide for Fuel Cell Applications
UIC REU – Summer 2011AMReL Lab, UIC
Department of Bioengineering andDepartment of Chemical Engineering
Christine JamesUniversity of Michigan, Department of Chemical Engineering
Overview
• Background• Atomic Layer Deposition• Data Collected• Future Work
Fuel Cell Advantages
• Provides clean energy– Hydrogen fuel cells – only emit water
• Very efficient– Fuel Values
• Hydrogen: 141.8 kJ/g• Gasoline: 48 kJ/g • Coal: 15-27 kJ/g
Santhanam et al., Introduction to Hydrogen Technology, 2009, Hoboken, NJ: J. Wiley.
Fossil fuel
2007
Environmentally friendly
Coal 23 %
Nuclear Power 8 %
Renewable Energy 6 %
Petroleum 40 %
Natural Gas 23 %
Source: US Energy Information Agency
Sections of the Fuel Cell
• Cathode– Oxygen is reduced
• Anode– Hydrogen is oxidized
• Electrolyte– Transports the oxygen ions
www1.eere.energy.gov
SOFC FUEL CELL
Fuel In Air In
Unused Gases Out
Excess Fuel and
Water
Electrical Current
Solid Oxide Fuel Cells (SOFCs)• Current SOFCs are high temperature– Temperature: about 1000 °C
• Intermediate Temperature Fuel Cells– Temperature: 600-800°C– Smaller scale applications– Allows use of alternate materials– Starts and stops faster– Reduces corrosion – Offers a wide range of possibilities
Problem with Reducing Temperature• High temperatures needed to transport O2- ions – Requirement can be as high as 1200° C– Low temperatures cause ionic resistance
• Deposit electrolytes and analyze– Samples from atomic to bulk-like thickness– Method to be used:
• Atomic Layer Deposition
• Deposit oxide layers on silicon then platinum (Pt)
Approach
Atomic Layer Deposition (ALD)
www.cambridgenanotech.com/ald
H2O
Tri-methyl aluminumAl(CH3)3(g)
Methyl group(CH3)3(g)
Hydroxyl (OH) from surface absorbed H2O
Reaction of TMA with OH
Methane reaction product CH4
Chosen Precursor
www.aloha.airliquide.com
Niinistö, et al., Advanced Engineering Materials, 2009, 11, No.4, 223.
Precursors Growth Temperature ImpuritiesMetal Precursor O source Range (°C) Preferred (°C) Saturation verified C [-at%] H [-at%]
at 300 °C ZyALD Ozone 250-400 300 Yes <1 N.R.
ALD System
ZyALD
ZyALD
Pulse and Purge times requiredReactor Temperature: 300°CBubbler Temperature: 50°CBubbler Pressure: 10 torrPrecursor: ZyALDPrecursor Pulse Time:
Precursor Purge Time:Oxidizer Pulse Time:Oxidizer Purge Time:Run for 40 cycles
Varied6 s
20 sVaried1.5 s
Varied
2 2.5 3 3.5 4 4.5 5 5.5 6 6.50.4
0.5
0.6
0.7
0.8
0.9
1
Precursor Pulse Time (s)
Gro
wth
Rat
e (Å
/cyc
le)
2 4 6 8 10 12 140.700000000000001
0.750000000000001
0.800000000000001
0.850000000000001
0.900000000000001
0.950000000000001
1
Precursor Purge Time (s)
Grow
th R
ate
(Å/c
ycle
)
10 s
0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.80.600000000000001
0.650000000000001
0.700000000000001
0.750000000000001
0.800000000000001
0.850000000000001
0.900000000000001
0.950000000000001
1
Oxidizer Pulse Time (s)
Gro
wth
Rat
e (Å
/cyc
le)
12 13 14 15 16 17 180.600000000000001
0.650000000000001
0.700000000000001
0.750000000000001
0.800000000000001
0.850000000000001
0.900000000000001
0.950000000000001
1
Oxidizer Purge Time (s)
Gro
wth
Rat
e (Å
/cyc
le)
17 s
1 s
Varied
Zr
www.cambridgenanotech.com/ald
Temperature WindowReactor Temperature: VariedBubbler Temperature: 50°C
Bubbler Pressure: 10 torrPrecursor: ZyALD
50 100 150 200 250 300 350 4000
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
2
Temperature (°C)
Gro
wth
Rat
e (Å
/cyc
le)
Precursor Condensation Precursor Decomposition
Temperature Window
Comparison to Work from another group
225 250 275 300 325 3500
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
Temperature (°C)
Gro
wth
Rat
e (Å
/cyc
le)
Niinistö, et al., J. Mater. Chem. 18, 5243 (2008).
Thickness vs. Cycles RunReactor Temperature: 300°CBubbler Temperature: 50°C
Bubbler Pressure: 10 torrPrecursor: ZyALD
0 20 40 60 80 100 120 140 160 1800
20
40
60
80
100
120
140
160
Number of Cycles Run
Thic
knes
s (Å
) Slope: .87R² = 0.9973
Future Work
1. Deposit the zirconium oxide on Platinum2. Run electrochemical analysis
Silicon Substrate
Electrolyte: Zirconium Oxide
Platinum
Summary• Goal is to lower operating temperature of the fuel cell– By decreasing electrolyte layer thickness
• Atomic Layer Deposition (ALD) is being used• Have determined some necessary parameters:– Pulse and Purge times– Temperature Window for ALD
• Have compared cycles and thickness– Proved linear relationship
• Next Steps: – Deposit on Platinum – Run Electrochemical analysis
Acknowledgements
• National Science Foundation– EEC-NSF Grant # 1062943
• Graduate Mentor: Runshen Xu• Professor Takoudis and Professor Jursich