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Title: Gas phase oxidation downstream of a catalytic combustor

Conference ·
OSTI ID:5185775

The objective of the experiments reported here was to determine what effect the length available for gas-phase reactions downstream of the catalytic reactor has on the emissions of CO and unburned hydrocarbons. A premixed, prevaporized propane/air feed to a 12-cm-dia catalytic-reactor test section was used. The catalytic reactor was made of four 2.5-cm-long monolithic catalyst elements. Four water-cooled gas-sampling probes were located at positions between 0 and 22 cm downstream of the catalytic reactor. Measurements of unburned hydrocarbons, CO, and CO/sub 2/ were made. Tests were performed with an inlet-air temperature of 800/sup 0/K, a reference velocity of 10 m/s, pressures of 3 and 6 x 10/sup 5/ Pa, and fuel-air equivalence ratios of 0.14 to 0.24. For very lean mixtures, hydrocarbon emissons were high and CO continued to be formed downstream of the catalytic reactor. At the highest equivalence ratios tested, hydrocarbon levels were much lower and CO was oxidized to CO/sub 2/ in the gas-phase downstream. To achieve acceptable emissions, a downstream region several times longer than the catalytic reactor could be required.

Research Organization:
Case Western Reserve Univ., Cleveland, OH (USA); National Aeronautics and Space Administration, Cleveland, OH (USA). Lewis Research Center
DOE Contract Number:
AI01-77CS51040
OSTI ID:
5185775
Report Number(s):
DOE/NASA/1040-16; NASA-TM-81551; CONF-7903134-1
Resource Relation:
Conference: 13. middle atlantic regional meeting of the American Chemical Society, West Long Branch, NJ, USA, 19 Mar 1979
Country of Publication:
United States
Language:
English