Aitor Arregi
University of the Basque Country
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Publication
Featured researches published by Aitor Arregi.
RSC Advances | 2016
Aitor Arregi; G. Lopez; Maider Amutio; Itsaso Barbarias; Javier Bilbao; Martin Olazar
The continuous fast pyrolysis (500 °C) of pine wood sawdust has been studied in a conical spouted bed reactor (CSBR) followed by in-line steam reforming of the pyrolysis vapours in a fluidised bed reactor on a Ni commercial catalyst. An analysis has been carried out on the effect reforming temperature in the 550–700 °C range, space time from 2.5 to 30 gcat min gvolatiles−1 and steam/biomass ratio between 2 and 5 have on the pyrolysis volatile conversion, H2 yield and gaseous stream composition. The continuous pyrolysis-reforming process has shown great potential for H2 production from biomass, with no operational problems and allowing for full conversion of pyrolysis vapours. Thus, a maximum H2 yield of 117 g per kg of biomass was obtained at 600 °C, at the highest space time studied (30 gcat min gvolatiles−1) and for a S/B ratio of 4. This yield is higher than those obtained by other alternatives, such as direct steam gasification or bio-oil reforming. Moreover, the char produced in the pyrolysis step has been continuously removed from the conical spouted bed reactor in order to be upgraded following promising valorisation alternatives.
Waste Management | 2015
Maite Artetxe; Gartzen Lopez; Maider Amutio; Itsaso Barbarias; Aitor Arregi; Roberto Aguado; Javier Bilbao; Martin Olazar
Continuous pyrolysis of polystyrene has been studied in a conical spouted bed reactor with the main aim of enhancing styrene monomer recovery. Thermal degradation in a thermogravimetric analyser was conducted as a preliminary study in order to apply this information in the pyrolysis in the conical spouted bed reactor. The effects of temperature and gas flow rate in the conical spouted bed reactor on product yield and composition have been determined in the 450-600°C range by using a spouting velocity from 1.25 to 3.5 times the minimum one. Styrene yield is strongly influenced by both temperature and gas flow rate, with the maximum yield being 70.6 wt% at 500°C and a gas velocity twice the minimum one.
Chemical Engineering Journal | 2016
Itsaso Barbarias; Gartzen Lopez; Jon Alvarez; Maite Artetxe; Aitor Arregi; Javier Bilbao; Martin Olazar
Fuel Processing Technology | 2016
Jon Alvarez; G. Lopez; Maider Amutio; Maite Artetxe; Itsaso Barbarias; Aitor Arregi; Javier Bilbao; Martin Olazar
Energy | 2016
Gartzen Lopez; Jon Alvarez; Maider Amutio; Aitor Arregi; Javier Bilbao; Martin Olazar
Energy Conversion and Management | 2017
Aitor Arregi; Maider Amutio; Gartzen Lopez; Maite Artetxe; Jon Alvarez; Javier Bilbao; Martin Olazar
Journal of Analytical and Applied Pyrolysis | 2016
Itsaso Barbarias; Gartzen Lopez; Maite Artetxe; Aitor Arregi; Laura Santamaria; Javier Bilbao; Martin Olazar
Applied Catalysis A-general | 2016
Itsaso Barbarias; Gartzen Lopez; Maider Amutio; Maite Artetxe; Jon Alvarez; Aitor Arregi; Javier Bilbao; Martin Olazar
Energy Conversion and Management | 2018
Aitor Arregi; Maider Amutio; Gartzen Lopez; Javier Bilbao; Martin Olazar
Fuel | 2018
Aitor Arregi; Gartzen Lopez; Maider Amutio; Maite Artetxe; Itsaso Barbarias; Javier Bilbao; Martin Olazar