Behaviour of dolomite, olivine and alumina as primary catalysts in air–steam gasification of sewage sludge

• Published in: Fuel (Guildford) Vol. 90; no. 2; pp. 521 - 527
• Main Authors: de Andrés, Juan Manuel, Narros, Adolfo, Rodríguez, María Encarnación
• Format: Journal Article
• Language: English
• Published: Kidlington Elsevier Ltd 01.02.2011; Elsevier
• Subjects: Aluminum oxide; Applied sciences; Assaying; Biomass; Bubbling fluidised bed; Catalysis; Catalysts; Dolomite; Energy; Energy. Thermal use of fuels; Exact sciences and technology; Fuels; Gasification; Natural energy; Olivine; Primary catalyst; Sewage sludge; Sewage sludge gasification; Tar content; Sewage sludge gasification; Bubbling fluidised bed; Tar content; Primary catalyst; Tar; Dolomite; Biomass; Water vapor; Sewage sludge; Bubbling; Gasification; Performance; Alumina; Catalyst
• ISSN: 0016-2361; 1873-7153
• DOI: 10.1016/j.fuel.2010.09.043

Sewage sludge gasification assays were performed in an atmospheric fluidised bed reactor using air and air–steam mixtures as the gasifying agents. Dolomite, olivine and alumina are three well known tar removal catalysts used in biomass gasification processing. However, little information is available regarding their performance in sewage sludge gasification. The aim of the current study was to learn about the influence of these three catalysts in the product distribution and tar production during sewage sludge gasification. To this end, a set of assays was performed in which the temperature (750–850 °C), the in-bed catalyst content (0, 10 and 15 wt.%) and the steam–biomass ratio (SB) in the range of 0–1 were varied with a constant equivalence ratio (ER) of 0.3. The results were compared to the results from gasification without a catalyst. We show that dolomite has the highest activity in tar elimination, followed by alumina and olivine. In addition to improving tar removal, the presence of water vapour and the catalysts increased the content of H 2 in the gases by nearly 60%.