Author/Authors :
Smorygo، نويسنده , , Oleg and Mikutski، نويسنده , , Vitali and Marukovich، نويسنده , , Alexander and Vialiuha، نويسنده , , Yuri and Ilyushchanka، نويسنده , , Alexander and Mezentseva، نويسنده , , Natalia and Alikina، نويسنده , , Galina and Vostrikov، نويسنده , , Zakhar and Fedorova، نويسنده , , Yulia and Pelipenko، نويسنده , , Vladimir and Bunina، نويسنده , , Rimma and Sadykov، نويسنده , , Vladis Kosse، نويسنده ,
Abstract :
Open cell metal foams made from Ni, Fe–Cr steel and Ni–Al intermetallic were studied as candidate catalyst supports for the internal indirect methane steam reforming. All the samples exhibited good corrosive resistance during 500–1000 h testing in H2–H2O–Ar environment at 600 °C. NiO/8YSZ composite based catalysts doped with fluorite-like (Pr0.3Ce0.35Zr0.35O2) or perovskite-like (La0.8Pr0.2Mn0.2Cr0.8O3) complex oxides with high lattice oxygen mobility and promoted with Pt or Ru were prepared and deposited on the foam-structure supports. Both good catalyst adhesion and stable catalyst performance were achieved in the case of the Ni–Al foam supported catalysts. The Fe–Cr support reacted with the catalytic active components resulting in fast catalyst deactivation. The foam supported catalyst performance was compared with the same catalyst prepared in a form of 0.25 mm fraction. Porous supports with different porosities were prepared by the metal foam deformation and the catalyst performance depending on the support porosity (75–95%) was studied.
Keywords :
composite catalyst , Metal foam , SOFC , Methane steam reforming , Catalyst support