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Featured researches published by Aitor Arregi.


RSC Advances | 2016

Hydrogen production from biomass by continuous fast pyrolysis and in-line steam reforming

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

Styrene recovery from polystyrene by flash pyrolysis in a conical spouted bed reactor.

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

A sequential process for hydrogen production based on continuous HDPE fast pyrolysis and in-line steam reforming

Itsaso Barbarias; Gartzen Lopez; Jon Alvarez; Maite Artetxe; Aitor Arregi; Javier Bilbao; Martin Olazar


Fuel Processing Technology | 2016

Characterization of the bio-oil obtained by fast pyrolysis of sewage sludge in a conical spouted bed reactor

Jon Alvarez; G. Lopez; Maider Amutio; Maite Artetxe; Itsaso Barbarias; Aitor Arregi; Javier Bilbao; Martin Olazar


Energy | 2016

Assessment of steam gasification kinetics of the char from lignocellulosic biomass in a conical spouted bed reactor

Gartzen Lopez; Jon Alvarez; Maider Amutio; Aitor Arregi; Javier Bilbao; Martin Olazar


Energy Conversion and Management | 2017

Hydrogen-rich gas production by continuous pyrolysis and in-line catalytic reforming of pine wood waste and HDPE mixtures

Aitor Arregi; Maider Amutio; Gartzen Lopez; Maite Artetxe; Jon Alvarez; Javier Bilbao; Martin Olazar


Journal of Analytical and Applied Pyrolysis | 2016

Pyrolysis and in-line catalytic steam reforming of polystyrene through a two-step reaction system

Itsaso Barbarias; Gartzen Lopez; Maite Artetxe; Aitor Arregi; Laura Santamaria; Javier Bilbao; Martin Olazar


Applied Catalysis A-general | 2016

Steam reforming of plastic pyrolysis model hydrocarbons and catalyst deactivation

Itsaso Barbarias; Gartzen Lopez; Maider Amutio; Maite Artetxe; Jon Alvarez; Aitor Arregi; Javier Bilbao; Martin Olazar


Energy Conversion and Management | 2018

Evaluation of thermochemical routes for hydrogen production from biomass: A review

Aitor Arregi; Maider Amutio; Gartzen Lopez; Javier Bilbao; Martin Olazar


Fuel | 2018

Role of operating conditions in the catalyst deactivation in the in-line steam reforming of volatiles from biomass fast pyrolysis

Aitor Arregi; Gartzen Lopez; Maider Amutio; Maite Artetxe; Itsaso Barbarias; Javier Bilbao; Martin Olazar

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Javier Bilbao

University of the Basque Country

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Martin Olazar

University of the Basque Country

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Gartzen Lopez

University of the Basque Country

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Maider Amutio

University of the Basque Country

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Maite Artetxe

University of the Basque Country

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Itsaso Barbarias

University of the Basque Country

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Jon Alvarez

University of the Basque Country

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Laura Santamaria

University of the Basque Country

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G. Lopez

University of the Basque Country

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Aitor Ochoa

University of the Basque Country

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