In this paper, the activity of a cobalt/molybdenum (Co/Mo) industrial catalyst to water gas shift reaction for hydrogen production was investigated in a three fixed bed reactor pilot plant by using a biomass-derived tar-rich synthesis as a feed-stream. A parametric variation study was carried out to assess CO conversion and selectivity for the water gas shift reaction as function of reaction temperature (T) in the range 300-450°C.
Experimental Investigations of hydrogen production from CO catalytic conversion of Tar Rich Syngas by Biomass Gasification
Chianese, Simeone;MUSMARRA, Dino
2015
Abstract
In this paper, the activity of a cobalt/molybdenum (Co/Mo) industrial catalyst to water gas shift reaction for hydrogen production was investigated in a three fixed bed reactor pilot plant by using a biomass-derived tar-rich synthesis as a feed-stream. A parametric variation study was carried out to assess CO conversion and selectivity for the water gas shift reaction as function of reaction temperature (T) in the range 300-450°C.File in questo prodotto:
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