Influence of alumina fixed-bed in steam reforming of glycerol for hydrogen production (7th International Conference on Renewable Energy and Conservation, ICREC 2022 November 18–20, 2022, Paris, France)
| dc.contributor.author | Maceiras, Rocío | |
| dc.contributor.author | Feijoo Conde, Jorge | |
| dc.contributor.author | Alfonsín, Víctor | |
| dc.contributor.author | Pérez, Leticia | |
| dc.contributor.author | Álvarez-Feijoo, Miguel A. | |
| dc.contributor.author | Falcón, Pablo | |
| dc.contributor.author | Vallejo, Javier P. | |
| dc.date.accessioned | 2024-11-26T16:47:10Z | |
| dc.date.available | 2024-11-26T16:47:10Z | |
| dc.date.issued | 2023 | |
| dc.description.abstract | In this study, hydrogen production by steam reforming was carried out in a tubular fixed-bed reactor. The influence of some operating variables such as temperature, flow rate of the feeding glycerol solution and space velocity on hydrogen production under a non-catalyzed reaction was analyzed. The results showed that the hydrogen yield increased with temperature and decreased with the space velocity. As the feedstock flow rate increased, the hydrogen yield decreased rapidly. Compared with a reference experiment without fixed-bed, the use of non-porous alumina fixed-bed showed better results. Under the best reaction conditions (900 ◦C and a feedstock flow rate of 0.85 g/min), 17 L/h of syngas were obtained, with a purity of about 55% of hydrogen and a production of 2.7 moles of hydrogen by mol of glycerol. | |
| dc.identifier.issn | 2352-4847 | |
| dc.identifier.uri | http://calderon.cud.uvigo.es/handle/123456789/846 | |
| dc.language.iso | en | |
| dc.publisher | Energy Reports | |
| dc.title | Influence of alumina fixed-bed in steam reforming of glycerol for hydrogen production (7th International Conference on Renewable Energy and Conservation, ICREC 2022 November 18–20, 2022, Paris, France) | |
| dc.type | Technical Report |