The ignition and extinction processes for total oxidation of CO, CH4 and CO + CH4 mixture in oxygen excess over Pt/Al2O3 and Pt/CeO2 catalysts with the platinum phase distributed either homogeneously or het- erogeneously (i.e., locally high platinum concentration) in the support have been studied by temperature programmed oxidation experiments. Following the preparation methods by Arnby et al. [42], the samples have the same Pt load and dispersion. Generally the catalytic activity follows the order: Pt/CeO2 (hetero- geneous) > Pt/CeO2 (homogeneous) > Pt/Al2 O3 (heterogeneous) > Pt/Al2 O3 (homogeneous) as indicated by lower ignition and/or extinction temperatures. For Pt/Al2O3, the addition of NO2 to the reactant stream increases the rate of...
The influence of pretreatment, gas composition and metal (Ce or Co) oxide promotion on the low-tempe...
The ignitionextinction processes for CO oxidation over a Pt/Al2O3 monolith catalyst have been studi...
Partial oxidation of methane to synthesis gas over platinum or ruthenium supported on Ce_(1−x)Zr_xO_...
The ignition and extinction processes for total oxidation of CO, CH4 and CO + CH4 mixture in oxygen ...
A comparative study of catalytic CO oxidation and selective CO oxidation over Pt/Al2O3 and CeO2-prom...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Oxidation of methane over Pt/Al(2)O(3) and Pt/CeO(2) catalysts was studied by transient gas-flow rea...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
1020-1023Palladium and platinum supported by CeO2, ZrO2 and AI2O3 have been prepared by conventional...
Oxidation of methane over Pt/Al(2)O(3) and Pt/CeO(2) catalysts was studied by transient gas-flow rea...
The influence of pretreatment, gas composition and metal (Ce or Co) oxide promotion on the low-tempe...
The ignitionextinction processes for CO oxidation over a Pt/Al2O3 monolith catalyst have been studi...
Partial oxidation of methane to synthesis gas over platinum or ruthenium supported on Ce_(1−x)Zr_xO_...
The ignition and extinction processes for total oxidation of CO, CH4 and CO + CH4 mixture in oxygen ...
A comparative study of catalytic CO oxidation and selective CO oxidation over Pt/Al2O3 and CeO2-prom...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
Oxidation of methane over Pt/Al(2)O(3) and Pt/CeO(2) catalysts was studied by transient gas-flow rea...
Reducing the operating temperature of oxidation catalysts is important for designing energy efficien...
1020-1023Palladium and platinum supported by CeO2, ZrO2 and AI2O3 have been prepared by conventional...
Oxidation of methane over Pt/Al(2)O(3) and Pt/CeO(2) catalysts was studied by transient gas-flow rea...
The influence of pretreatment, gas composition and metal (Ce or Co) oxide promotion on the low-tempe...
The ignitionextinction processes for CO oxidation over a Pt/Al2O3 monolith catalyst have been studi...
Partial oxidation of methane to synthesis gas over platinum or ruthenium supported on Ce_(1−x)Zr_xO_...