| 1 |
Kinetic model considering catalyst deactivation for the steam reforming of bio-oil over Ni/La2O3-alpha Al2O3
Gayubo AG, Valle B, Aramburu B, Montero C, Bilbao J
Chemical Engineering Journal, 332, 192, 2018 |
| 2 |
Biomass to hydrogen-rich gas via steam reforming of raw bio-oil over Ni/La2O3-alpha Al2O3 catalyst: Effect of space-time and steam-to-carbon ratio
Valle B, Aramburu B, Benito PL, Bilbao J, Gayubo AG
Fuel, 216, 445, 2018 |
| 3 |
Steam reforming of raw bio-oil over Ni/La2O3-alpha Al2O3: Influence of temperature on product yields and catalyst deactivation
Valle B, Aramburu B, Olazar M, Bilbao J, Gayubo AG
Fuel, 216, 463, 2018 |
| 4 |
Effect of calcination/reduction conditions of Ni/La2O3-alpha Al2O3 catalyst on its activity and stability for hydrogen production by steam reforming of raw bio-oil/ethanol
Valle B, Aramburu B, Remiro A, Bilbao J, Gayubo AG
Applied Catalysis B: Environmental, 147, 402, 2014 |
| 5 |
Upgrading of Bio-Oil in a Continuous Process with Dolomite Catalyst
Valle B, Aramburu B, Santiviago C, Bilbao J, Gayubo AG
Energy & Fuels, 28(10), 6419, 2014 |
| 6 |
Steam Reforming of the Bio-Oil Aqueous Fraction in a Fluidized Bed Reactor with in Situ CO2 Capture
Remiro A, Valle B, Aramburu B, Aguayo AT, Bilbao J, Gayubo AG
Industrial & Engineering Chemistry Research, 52(48), 17087, 2013 |
