The structure of the metal particles and the metal-support interface of a Pt@c-Al{2}O{3} catalyst was determined by EXAFS after low temperature reduction (LTR: 300}o{ C) and high temperature reduction (HTR: 450}o{ C). The clusters have excellent thermal stability as the particle size remains 12 atoms per cluster upon increasing the reduction temperature from 300}o{ C to 450}o{ C. However, the structure of the metal-support interface is a strong function of the reduction temperature. After LTR and in the presence of chemisorbed hydrogen the metal particles are at a distance of 2.68 a from the support oxygen ions. This long Pt-O distance is due to the presence of hydrogen between the platinum atoms and the support. Increasing the reduction te...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
The catalytic performance of supported heterogeneous catalysts is significantly affected by the part...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
The catalytic performance of supported heterogeneous catalysts is significantly affected by the part...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
The relation between the catalytic activity, electronic properties, morphology, and structure of the...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
Platinum supported on H-LTL, K-LTL, and H-MAZ was reduced at temperatures from 573 to 873 K and the ...
The catalytic performance of supported heterogeneous catalysts is significantly affected by the part...