Title of article :
CO removal from realistic methanol reformate via preferential oxidation—performance of a Rh/MgO catalyst and comparison to Ru/γ-Al2O3, and Pt/γ-Al2O3
Author/Authors :
Han، نويسنده , , Y.-F. and Kahlich، نويسنده , , M.J. and Kinne، نويسنده , , M. and Behm، نويسنده , , R.J.، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2004
Pages :
10
From page :
209
To page :
218
Abstract :
The performance of a 0.5 wt.% Rh/MgO catalyst for the oxidative removal of CO from H2-rich methanol reformate (1% CO, 65% H2, 10% H2O, rest CO2) was investigated and compared to that of a conventional 0.5 wt.% Pt/γ-Al2O3 catalyst and a 5 wt.% Ru/γ-Al2O3 catalyst. Temperature screening experiments and 10–30 h activity measurements reveal a high activity and selectivity in the temperature region between 175 and 300 °C, in combination with a relatively low deactivation. Water vapor in the feed gas (≤10%) has little effect on the reaction characteristics. The low activity for the reverse water gas shift (RWGS) reaction, whose rate is more than four orders of magnitude lower than the rate for CO oxidation, and for the methanation reaction at temperatures below 300 °C allow to operate Rh/MgO at higher temperatures, around 250 °C, while for Pt/γ-Al2O3 and Ru/γ-Al2O3 the reaction temperatures are limited to 200 and 150 °C, respectively, due to the decrease in selectivity (Pt/γ-Al2O3) and the onset of the methanation reaction (Ru/γ-Al2O3) at higher temperatures. calculations, using kinetic data measured in realistic reformate, predict that the minimum amount of noble metal required for the complete removal of CO from the feed gas (≤10 ppm) is by two orders of magnitude lower for Rh/MgO operated at 250 °C than for Pt/γ-Al2O3 and Ru/γ-Al2O3 catalysts at 200 and 150 °C, respectively, at a comparable O2 excess. Due to the low RWGS activity the CO exit concentration does not increase significantly above the tolerance limit of state-of-the-art Pt–Ru fuel cell anodes of 100 ppm under dynamic load conditions, down to 1% load. For the other two catalysts the CO exit concentration are significantly higher under these conditions, reaching values above 500 ppm for Ru/γ-Al2O3 at 1% load and the WGS equilibrium value of 2000 ppm for Pt/γ-Al2O3. The predictions are verified by measurements in a microreactor under similar reaction conditions. action characteristics make Rh/MgO an ideal PROX catalyst for reaction at higher temperatures (250 °C), in particular for applications requiring highly dynamic operation under variable load conditions.
Keywords :
Ru/?-Al2O3 , Water gas shift reaction , Kinetics , Selective CO oxidation , MODELING , Fuel cells , Pt/?-Al2O3 , Rh/MgO , Methanation reaction , Dynamic operation
Journal title :
Applied Catalysis B: Environmental
Serial Year :
2004
Journal title :
Applied Catalysis B: Environmental
Record number :
1446859
Link To Document :
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