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DESIGN OF ACTIVE AND STABLE Au CATALYSTS FOR H2 …fornasiero/varie/poster-GOLD... · 2015. 6....

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CO + 1/2O CO 2 2 DESIGN OF ACTIVE AND STABLE Au CATALYSTS FOR H PURIFICATION 2 a a b Matteo Cargnello, Tiziano Montini, Emiliano Fonda, a c c Cristina Gentilini, Shareghe Mehraeen, Nigel D. Browning, a a Lucia Pasquato and Paolo Fornasiero a Department of Chemistry, INSTM - Trieste Research Unit and ICCOM-CNR - Trieste Research Unit, University of Trieste, Via L. Giorgieri 1, 34127 Trieste (Italy) b Synchrotron Soleil, L’Orme des Merisiers Saint-Aubin, BP 48 91192 Gif-sur-Yvette Cedex (France) c Department of Chemical Engineering and Materials Science, University of California at Davis and Materials Science and Technology Division, Lawrence Livermore National Laboratory, Davis, CA 95616 (USA) e-mail: [email protected] Design Water-soluble Au nanoparticles [3] Au@CeO 2 Au/CeO DPU 2 Reference samples: by Deposition-Precipitation with Urea [4] Ce(IV) assembly Au loading: 1 or 3 wt. % CATALYTIC ACTIVITY Full PROX mixture: CO (1%) + O (1%) + 2 H (47.5%) + CO (17.5%) + H O (5%) in Ar 2 2 2 -1 -1 GHSV ~ 75000 mL g h 75 100 125 150 175 200 225 250 0 20 40 60 80 100 CO conversion (%) Temperature (°C) Fresh Aged150 Aged250 TPO 75 100 125 150 175 200 225 250 0 20 40 60 80 100 CO conversion (%) Temperature (°C) Fresh Aged150 Aged250 TPO Au(1%)@CeO 2 Au(1%)/CeO DPU 2 Reaction rates of fresh catalysts @ DPU CHARACTERIZATION CO Chemisorption EXAFS results Advanced Electron Microscopy (HAADF-STEM) precipitation - calcination CONCLUSIONS - highly active and thermally stable Au catalysts with low Au loading (1 wt. %) have been prepared; - the embedding approach is promising with room for improvements Sample Fresh Catalysts AIM OF THE WORK Design, preparation and characterization of highly active and thermally stable Au catalysts for PROX through the embedding approach [1,2] stabilization against sintering by embedding the active phase inside the support aging protocol + mild oxidative regeneration Aged Catalysts After TPO Catalysts Accessible Au* Au(1%)@CeO 2 Au(1%)/CeO -DPU 2 Au(3%)@CeO 2 Au(3%)/CeO -DPU 2 31% 51% 11% 41% - - - - 7% 11% 11% 34% Sample Fresh Catalysts Aged Catalysts Au particle diameter (nm)* Au(1%)@CeO 2 Au(1%)/CeO -DPU 2 Au(3%)@CeO 2 Au(3%)/CeO -DPU 2 0.9 2.0 1.3 2.4 1.0 2.3 1.6 3.0 * Determined according to the protocol described in [5]. * Determined from the fitting of the first Au-Au contribution. INTRODUCTION - H , in combination with efficient Fuel Cells (FCs), is an attractive energy vector for the 2 future - most of the H -based Fuel Cells, such as Proton-Exchange Membrane (PEM) FCs, still 2 contains catalysts which are sensitive to CO poisoning REFERENCES ACKNOWLEDGEMENTS - PReferential OXidation (PROX) of CO in the presence of H is an advantageous purification 2 process: CO + 1/2O (in H ) = CO 2 - Au/CeO systems are excellent candidates, joining 2 Au selectivity and CeO oxidation capability 2 - improvement in activity, selectivity and thermal stability are objects of today’s research 2 2 - CO chemisorption and EXAFS confirm the occurrence of sintering in DPU samples - EXAFS demonstrates that calcination does not increase the dimension of Au particles in @ samples - Advanced TEM shows some big particles also in the 3 wt. % @ sample [1] De Rogatis, L. et al. “Stabilized metal nanoparticles embedded into porous oxides: a challenging approach for robust catalysts.”, Chapter 2 in Nanorods, Nanotubes and Nanomaterials Research Progress, Wesley V. Prescott and Arnold I. Schwartz Editors, Nova Science Publishers, 2008, New York, pp. 71-123. [2] Budroni, G. and Corma, A. Angew. Chem. Int. Ed. 2006, 45, 3328. [3] Pasquato, L. et al. J. Mater. Chem. 2003, 13, 2471. [4] Zanella, R. et al. J. Phys. Chem. B 2002, 106, 7634. [5] Collins, S. E. et al. J. Phys. Chem. C 2007, 111, 14371. - @ samples at least 4 times more active than traditional DPU catalysts - activity completely restored (blue and red curves) after aging/regeneration for 1 % @ sample nd ICCOM-CNR, INSTM, PRIN 2007 “Sustainable processes of 2 generation for the production of H from renewable resources“, the 2 University of Trieste and the School of Doctorate in Nanotechnology are gratefully acknowledge for the PhD studenship and financial support. Prof. M. Graziani (Univ. Of Trieste) is acknowledge for fruitful discussions. mol / (mol h) CO conv Au exposed HMT=hexamethylenetetramine H 2 Au(3%)@CeO -FRESH 2 Au(3%)@CeO -AGED 2 5 nm 5 nm 20 nm 100 nm DPU: Deposition-Precipitation Urea catalysts 75 100 125 150 0 10 20 30 40 50 60 Temperature (°C) 1% 1% 3% 3% 20 nm 5 nm HRTEM image of Au nanoparticles HAADF-STEM image of calcined Au@CeO 2 @: embedded catalysts ] ]
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Page 1: DESIGN OF ACTIVE AND STABLE Au CATALYSTS FOR H2 …fornasiero/varie/poster-GOLD... · 2015. 6. 9. · [1] De Rogatis, L. et al. “Stabilized metal nanoparticles embedded into porous

CO + 1/2O CO 2 2

DESIGN OF ACTIVE AND STABLEAu CATALYSTS FOR H PURIFICATION2

a a bMatteo Cargnello, Tiziano Montini, Emiliano Fonda, a c cCristina Gentilini, Shareghe Mehraeen, Nigel D. Browning,

a aLucia Pasquato and Paolo Fornasieroa Department of Chemistry, INSTM - Trieste Research Unit and ICCOM-CNR - Trieste Research Unit, University of Trieste,

Via L. Giorgieri 1, 34127 Trieste (Italy)b Synchrotron Soleil, L’Orme des Merisiers Saint-Aubin, BP 48 91192 Gif-sur-Yvette Cedex (France)

c Department of Chemical Engineering and Materials Science, University of California at Davis and Materials Science and Technology Division, Lawrence Livermore National Laboratory, Davis, CA 95616 (USA)

e-mail: [email protected]

Design

Water-soluble Au nanoparticles [3]

Au@CeO2

Au/CeO DPU2Reference samples:

by Deposition-Precipitation with Urea [4]

Ce(IV) assembly

Au loading: 1 or 3 wt. %

CATALYTIC ACTIVITY

Full PROX mixture: CO (1%) + O (1%) + 2

H (47.5%) + CO (17.5%) + H O (5%) in Ar2 2 2

-1 -1GHSV ~ 75000 mL g h

75 100 125 150 175 200 225 2500

20

40

60

80

100

COco

nver

sion

(%)

Temperature (°C)

Fresh Aged150 Aged250 TPO

75 100 125 150 175 200 225 2500

20

40

60

80

100

COco

nver

sion

(%)

Temperature (°C)

Fresh Aged150 Aged250 TPO

Au(1%)@CeO2Au(1%)/CeO DPU2

Reaction rates of fresh catalysts

@

DPU

CHARACTERIZATION

CO Chemisorption EXAFS results Advanced Electron Microscopy (HAADF-STEM)

precipitation - calcination

CONCLUSIONS- highly active and thermally stable Au catalysts with low Au loading (1 wt. %) have been prepared;- the embedding approach is promising with room for improvements

SampleFresh

Catalysts

AIM OF THE WORKDesign, preparation and characterization of highly active and

thermally stable Au catalysts for PROXthrough the embedding approach [1,2]

stabilization against sintering by embedding the active phase inside the support

aging protocol + mild oxidative regeneration

Aged Catalysts

After TPO Catalysts

Accessible Au*

Au(1%)@CeO2

Au(1%)/CeO -DPU2

Au(3%)@CeO2

Au(3%)/CeO -DPU2

31%

51%

11%

41%

- -

- -

7% 11%

11% 34%

SampleFresh

CatalystsAged

Catalysts

Au particle diameter (nm)*

Au(1%)@CeO2

Au(1%)/CeO -DPU2

Au(3%)@CeO2

Au(3%)/CeO -DPU2

0.9

2.0

1.3

2.4

1.0

2.3

1.6

3.0

* Determined according to the protocol described in [5]. * Determined from the fitting of the first Au-Au contribution.

INTRODUCTION- H , in combination with efficient Fuel Cells (FCs), is an attractive energy vector for the 2

future- most of the H -based Fuel Cells, such as Proton-Exchange Membrane (PEM) FCs, still 2

contains catalysts which are sensitive to CO poisoning

REFERENCES ACKNOWLEDGEMENTS

- PReferential OXidation (PROX) of CO in the presence of H is an advantageous purification 2

process: CO + 1/2O (in H ) = CO2

- Au/CeO systems are excellent candidates, joining 2

Au selectivity and CeO oxidation capability2

- improvement in activity, selectivity and thermal stability are objects of today’s research

2 2

- CO chemisorption and EXAFS confirm the occurrence of sintering in DPU samples- EXAFS demonstrates that calcination does not increase the dimension of Au particles in @ samples- Advanced TEM shows some big particles also in the 3 wt. % @ sample

[1] De Rogatis, L. et al. “Stabilized metal nanoparticles embedded into porous oxides: a challenging approach for robust catalysts.”, Chapter 2 in Nanorods, Nanotubes and Nanomaterials Research Progress, Wesley V. Prescott and Arnold I. Schwartz Editors, Nova Science Publishers, 2008, New York, pp. 71-123.[2] Budroni, G. and Corma, A. Angew. Chem. Int. Ed. 2006, 45, 3328.[3] Pasquato, L. et al. J. Mater. Chem. 2003, 13, 2471.[4] Zanella, R. et al. J. Phys. Chem. B 2002, 106, 7634.[5] Collins, S. E. et al. J. Phys. Chem. C 2007, 111, 14371.

- @ samples at least 4 times more active than traditional DPU catalysts- activity completely restored (blue and red curves) after aging/regeneration for 1 % @ sample

ndICCOM-CNR, INSTM, PRIN 2007 “Sustainable processes of 2 generation for the production of H from renewable resources“, the 2

University of Trieste and the School of Doctorate in Nanotechnology are gratefully acknowledge for the PhD studenship and financial support. Prof. M. Graziani (Univ. Of Trieste) is acknowledge for fruitful discussions.

mo

l/

(mo

l h

)C

O c

on

v

Au

exp

ose

d

HMT=hexamethylenetetramine

H2

Au(3%)@CeO -FRESH2

Au(3%)@CeO -AGED2

5 nm 5 nm

20 nm100 nm

DPU: Deposition-Precipitation Urea catalysts

75 100 125 150

0

10

20

30

40

50

60

Temperature (°C)

1%

1%

3%

3%

20 nm

5 nm

HRTEM image of Au nanoparticles

HAADF-STEM image of calcined Au@CeO2

@: embedded catalysts

]

]

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