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8/10/2019 Alternative Materials to Replace Platinum
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Alternative Materials to Replace Platinum inCatalytic and Electrocatalytic Applications
Jingguang Chen
Department of Chemical EngineeringUniversity of Delaware
Newark, DE 19711 [email protected]
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Abundance of Elements of Catalytic Interests
Pt-group metals (Pt, Ir, Pd, Rh, Ru) are expensive and limited in supply
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Needs of Pt in Catalysis and Electrocatalysis
- Demand in Heterogeneous Catalysis: Pt catalysts are used in many chemical and refining processes
- Demand in Emerging Clean Energy Technologies:
Pt electrocatalysts are required in low-temperature fuel cells,electrolyzers, and photoelectrochemical cells in significant amounts
- Research Efforts in Solving Pt Challenge: I. Replace Pt with alternative materials with similar activity and stability II. Reduce loading of Pt using monolayer catalysts and electrocatalysts
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I. Replace Pt with Transition Metal Carbides
Physical properties of carbides: High hardness, wear resistance High temperature stability Excellent electrical conductivity
Chemical properties of carbides: Similar catalytic activity to
Pt-group metals
IV V VI
Levy & Boudart, Science , 181 (1973) 547Oyama, Transition Metal Carbides and Nitrides, (1996)Hwu & Chen, Chemical Rev iews 105 (2005) 185Chen Research Group: Angew. Chem. Int. Ed. 49 (2010) 9859Thompson Research Group: J. Catalysis , 272 (2010) 235
Davis Research Group: J. Catalysis , 282 (2011) 83
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II. Reduce Pt Loading with Monolayer (ML) Pt
Challenge: Identify substrates with Pt-like bulk properties
Esposito & Chen, Energy & Env. Sci . (2011)
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BridgingMaterials Gap
- Thin films
- Supported catalyst
Single CrystalModel Surfaces
- UHV studies
- DFT modeling
BridgingPressure Gap
- Reactor studies
- Electrochem cells
Research Approaches
- Avoid trial-and-error, empirical approach, i.e., randomly picking elementsfrom the Periodic Table
- Use theory and model systems to obtain design principles for identifyingcatalysts with little or no Pt, while maintaining Pt-like activity and stability
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BridgingMaterials Gap
- Thin films- Supported catalyst
Single CrystalModel Surfaces
- UHV studies- DFT modeling
BridgingPressure Gap
- Reactor studies- Electrochem cells
Examples of of reducing and replacing Pt :
1. H 2 production from water electrolysis with monolayer Pt2. Conversion of biomass-derived oxygenates with Pt-free catalysts
Example 1: Reducing Pt Loading
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H2 from Water Electrolysis on ML Pt/WC
Esposito, Hunt & Chen, Angew. Chem. Int. Ed .49 (2010) 9859
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H2 is a mobile energy carrier
H2 has a high gravimetric energy density No CO 2 emission when H 2 is made from the electrolysis of
water using renewable energy such as solar
Motivation for Water Electrolysis
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Hydrogen Production from Water Electrolysis
Oxygen Evolution Reaction (OER)
Overall Reaction
Hydrogen Evolution Reaction (HER)
Eo H+/H2 =0.0 V vs. NHE
Eo H2O/O2 =+1.23 V vs. NHE
C a t
h o
d e
( H E R C a t a l y s
t )
PowerInpute- e-
(-)(+)
H2O
H2(g)
O 2(g) + 2H +
A n o
d e
( O E R C a t a l y s
t )
Schematic electrolysis cell
Challenge: HER requires relatively large Pt particles (~ 5nm)
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Questions of Using ML Pt/WC as Electrocatalysts
- What is the descriptor responsible for making Pt the optimalcatalyst for the hydrogen evolution reaction (HER)?
- Does ML Pt/WC meet such descriptor for high HER activity?
- Is ML Pt/WC stable under the relatively harsh HERconditions?
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HER Activity and Hydrogen Binding Energy (HBE)
[1] Data from: Norskov, Bligaard, Logadottir, Kitchin, Chen, Pandelov, Stimming, J.Electrochem. Soc., 152 (2005) J23-26.
Classic volcano curve observed for the HER is explained bySabatiersPrinciple [2] (Volmer Step)
(Tafel Step)
[2] P. Sabatier, Catalysis in Organic Chemistry, D. Van Nostrand Company, New York, 1922.
(Weak)(Strong)
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Surface HBE (eV)WC(001) -0.99Pt(111) -0.46
1 ML Pt-WC(001) -0.43DFT-calculated per-atom hydrogenbinding energy (HBE) for WC, Pt, and 1ML Pt-WC surfaces with a hydrogencoverage of 1/9 ML.
d-band density of states
DFT Prediction: Similar HBE Values betweenMonolayer Pt-WC and Bulk Pt
Pt WC
1 atomiclayer of Pt
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Experimental Verification: HER Activity of Pt/WC
As Pt coverage nears 1 ML, the
activity of WC electrodes reachthat of Pt foil
WC Foil
Pt Foil
Combined DFT and experimental results have identified monolayer Pt on WCas electrolysis catalyst of similar activity with significant reduction in cost
Esposito, Hunt & Chen, Angew. Chem. Int. Ed . 49 (2010) 9859
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Adhesion of ML Pt in the Pt/WC system
Use DFT to compare adhesion of Pt atoms to WC and Pt surfaces:
Pt-(Substrate) > Pt-Pt
Pt-(Substrate) < Pt-Pt
ML configurationfavored
Particlesfavored
Binding Energy OutcomePt
migration
ML surface atoms Substrate Binding energy
/ eV (M-X^) - (M-M) BE
/ eV
Pt
Pt(111) -5.43 0.00
C(0001) -4.12 1.31
WC(0001) -6.59 -1.16
W2C(0001) -6.51 -1.08
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ML Pt/WC Shows Excellent HER Stability
Physical characterization of ML Pt-WCsurface further confirms that the Pt ML isstable on WC under HER conditions.
SEM images taken before and afterextended stability tests
XPS Pt 4f spectra and atomic Pt4f/W4f signal ratiobefore and after extended stability tests
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From Model Thin Films to Catalytic Particles
Challenge: A synthesis technique to deposit ML Pt on WC particles
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Transmission Electron Microscopy ofAtomic Layer Deposition (ALD) of Pt on WC
A thin film of Pt is deposited on WC particles at 50 ALD cycles
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HER Activity of ALD Pt/WC Particles
- Similar to thin film results, low loading of Pt (10 ALD cycles) show similarHER activity as 10 wt% Pt/C catalyst
- Elemental analysis reveals Pt loading of 10 ALD cycle Pt/WC is a factor of
~10 less than 10 wt% Pt/C
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Extension to Other ML Metal/Carbide Catalysts
Volcano relationship reveals other potential catalysts: ML Pd/WC and Pd/Mo 2C
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Extension to Other Electrochemical Devices
- WC is electrochemically stable in the pH and potential range for HER- Other applications depend on pH and E range
Weidman, Esposito & Chen, J. Electrochem. Soc. 157 (2010) F179
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BridgingMaterials Gap
- Thin films- Supported catalyst
Single CrystalModel Surfaces
- UHV studies- DFT modeling
BridgingPressure Gap
- Reactor studies- Electrochem cells
Examples of of reducing and replacing Pt :
1. H 2 production from water electrolysis with monolayer Pt2. Conversion of biomass-derived oxygenates with Pt-free catalysts
Example 2: Replacing Pt
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Skoplyak, Barteau & Chen,ChemSusChem 1 (2008) 524
Pt Catalysts for Biomass-derived Oxygenates
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Ni/WC(0001)
Ni/Pt(111)
Replacing Ni/Pt with Ni/WC for Pt-free Catalysts
Advantages of replacing Ni/Pt wth Ni/WC: lower cost; higher stabilityHumbert, Menning & Chen, Journal of Catalysis , 271 (2010) 132
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Similar Reaction Pathways on Ni/WC and Ni/Pt
Glycolaldehyde
AcetaldehydeEthylene glycol Acetic Acid
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Sorbitol
HOO
HO OHOH
OH
Glucose Mannitol
Hydrolysis
isomerization
H2
Hydrogenation
OH
OH
Ethylene glycol
+other
polyols
OH
HOO O
HO OH
O
OH
n
Cellulose
O
H2O
Fructose
CH2OH
OCH2OH
OH
OH
HO
H2
Hydrogenation
OHOH
OH
OH OH
OH
OHOH
OH
OH OH
OH
-H2O
Dehydration
H2
Hydrogenation
H2
HydrogenolysisLight alkanes
CO2, etc.
H+
C-C cleavage+oxdationOrganic acids (unidentified)
OOH O
OOH OH
HMF DHM-THF
OH
Conversion of Cellulose on Pt-free Catalysts
Conversion of cellulose to ethylene glycol on Ni-WC & Ni-W 2C:Ji, Zhang 7 Chen, Catalysis Today , 147 (2009) 77
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Cellulose Conversion to Chemicals on Ni-W 2C
Results: 100% conversion, 61% EG yield, (6 MPa H 2; 518 K; 30 min)
Ji, Zhang, & Chen, Angew. Chem. Int. Ed. 47 (2008) 8510
C l i d Ch ll
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Conclusions and Challenges
- Promising results are obtained in reducing Pt loading using
monolayer Pt on carbides for electrocatalysis, achievingabout a factor of ~10 in Pt reduction
- Pt-free catalysts are demonstrated for conversion of
biomass-derivatives, using less expensive metal (Ni, Co,etc.) supported on carbides.
- Significant challenges exist for achieving large-scaleapplications in catalysis and electrocatalysis:
- synthesis of high surface area carbides ( critical for activity )- deposition of monolayer metal on carbides ( critical for saving Pt )- resistance to carbon deposition ( critical for catalysis )- long-term stability in solution ( critical for electrocatalysis )
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Acknowledgement
Collaborators: Prof. Barteau (Univ. Delaware); Prof. Willis (Univ. Conn)
Funding: Department of Energy