| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 7065586 | Biomass and Bioenergy | 2013 | 11 Pages |
Abstract
⺠Fermentation residue of a biogas plant could be successfully liquefied with a low rate of coke formation. ⺠Liquefaction resulted in an incomplete removal of biomass-bound sulfur. ⺠Low catalyst loadings result in incomplete conversion, implicating catalyst deactivation. ⺠At 400 °C the observed conversion to methane was highest. ⺠A residence time dependent biomass to catalyst ratio of 0.45 g gâ1 hâ1 was determined to yield nearly complete conversion.
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Physical Sciences and Engineering
Chemical Engineering
Process Chemistry and Technology
Authors
Hemma Zöhrer, Frédéric Vogel,