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Title: Carbon monoxide removal by preferential oxidation from hydrogen-rich gas streams

Technical Report ·
OSTI ID:6560605

The use of methanol as an indirect transportation fuel is currently being investigated at the Los Alamos National Laboratory. In the Los Alamos research, methanol is converted to hydrogen by catalytic steam reforming and water-gas shift reaction processes, The product hydrogen gas stream is then oxidized in a fuel cell operating at temperatures less than 200/degree/C to produce electrical power to drive a vehicle. Residual carbon monoxide contained in the hydrogen stream is a severe poison to the fuel cell electrode. In this study we examined the feasibility of removing the CO to levels of less than 0.1 mol%, while minimizing the consumption of hydrogen. This was to be accomplished by selective oxidation of the CO using a 0.5% platinum-on-alumina catalyst. Experimental results showed that approximately 90% of the CO and only 3% of the H/sub 2/ would be oxidized with an O/sub 2//CO ratio of 1, in total gas flows up to 1455 cm/sup 3//min (at 177/degree/C and 158.6 kPa (23 psia)), from a mixture that was initially 2% CO in H/sub 2/. When the O/sub 2//CO ratio was increased to 1.5, CO conversion was at or near 100%, and H/sub 2/ conversion rose to about 4%. In runs with excess CO/sub 2/ present, as would exist in an actual fuel cell, no significant effect on CO oxidation was noted. 122 refs., 16 figs., 5 tabs.

Research Organization:
Los Alamos National Lab., NM (USA); Massachusetts Inst. of Tech., Los Alamos, NM (USA). School of Chemical Engineering Practice-Los Alamos Station
DOE Contract Number:
W-7405-ENG-36
OSTI ID:
6560605
Report Number(s):
LA-11483-MS; MIT-LANL-1; ON: DE89006380
Resource Relation:
Other Information: Portions of this document are illegible in microfiche products
Country of Publication:
United States
Language:
English

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