Performance of an integral methane reforming fixed bed reactor packed with an industrial catalyst
DOI:
https://doi.org/10.4025/actascitechnol.v27i2.1455Keywords:
reforma a vapor de metano, reator integral, catalisador industrialAbstract
The present work has the objective to evaluate the catalytic activity and the temperature profile inside an integral steam reforming fixed bed reactor heated by an electrical furnace and packed with an industrial catalyst. Nine temperature measures were made along nine axial positions and the composition of the products reaction were evaluated by gas chromatography. The experimental conditions were: temperatures furnace of 500ºC, 600ºC, and 700ºC, feed molar ratio [H2O/CH4] = 4, and mass flow rate of 0.2 and 0.5 kg/m2.s. The results show that the use of the nine points was enough to represent the thermal behavior of the reactor. Both the catalytic activity and the conversion depend of operational temperature. However, the fixed bed temperature is independent of mass flow rate at the used experimental conditionsDownloads
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Published
2008-03-27
How to Cite
Francisquini, D. R., Gonçalves, G., Santos, O. A. A. dos, & Jorge, L. M. de M. (2008). Performance of an integral methane reforming fixed bed reactor packed with an industrial catalyst. Acta Scientiarum. Technology, 27(2), 119–122. https://doi.org/10.4025/actascitechnol.v27i2.1455
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Chemical Engineering
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0.8
2019CiteScore
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0.8
2019CiteScore
36th percentile
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