Publicaciones en colaboración con investigadores/as de Universidad de Zaragoza (45)

2008

  1. 140 g H2/kg biomass d.a.f. by a CO-shift reactor downstream from a FB biomass gasifier and a catalytic steam reformer

    International Journal of Hydrogen Energy, Vol. 33, Núm. 7, pp. 1820-1826

2006

  1. Hydrogen production by biomass gasification with steam-O2 mixtures followed by a catalytic steam reformer and a CO-shift system

    Energy and Fuels, Vol. 20, Núm. 3, pp. 1305-1309

2003

  1. Two advanced models for the kinetics of the variation of the tar composition in its catalytic elimination in biomass gasification

    Industrial and Engineering Chemistry Research, Vol. 42, Núm. 13, pp. 3001-3011

2002

  1. Improving the modeling of the kinetics of the catalytic tar elimination in biomass gasification

    Industrial and Engineering Chemistry Research, Vol. 41, Núm. 14, pp. 3351-3356

  2. Improving the modelling of the kinetics of the catalytic tar elimination in biomass gasification

    VTT Symposium (Valtion Teknillinen Tutkimuskeskus)

2000

  1. Biomass gasification with air in fluidized bed. Hot gas cleanup with selected commercial and full-size nickel-based catalysts

    Industrial and Engineering Chemistry Research, Vol. 39, Núm. 5, pp. 1143-1154

1999

  1. Biomass gasification in atmospheric and bubbling fluidized bed: Effect of the type of gasifying agent on the product distribution

    Biomass and Bioenergy, Vol. 17, Núm. 5, pp. 389-403

  2. Biomass gasification in fluidized bed: Where to locate the dolomite to improve gasification?

    Energy and Fuels, Vol. 13, Núm. 6, pp. 1122-1127

  3. Producer gas cleaning from tars in a vortex bubbling device

    Heat Transfer Research, Vol. 30, Núm. 1, pp. 50-58

1998

  1. Commercial steam reforming catalysts to improve biomass gasification with steam-oxygen mixtures. 2. Catalytic tar removal

    Industrial and Engineering Chemistry Research, Vol. 37, Núm. 7, pp. 2668-2680

1997

  1. Biomass Gasification with Steam in Fluidized Bed: Effectiveness of CaO, MgO, and CaO-MgO for Hot Raw Gas Cleaning

    Industrial and Engineering Chemistry Research, Vol. 36, Núm. 5, pp. 1535-1543

  2. Biomass Gasification: Produced Gas Upgrading by In-Bed Use of Dolomite

    Industrial and Engineering Chemistry Research, Vol. 36, Núm. 12, pp. 5220-5226

  3. Biomass gasification in fluidized bed at pilot scale with steam-oxygen mixtures. Product distribution for very different operating conditions

    Energy and Fuels, Vol. 11, Núm. 6

  4. Commercial Steam Reforming Catalysts to Improve Biomass Gasification with Steam-Oxygen Mixtures. 1. Hot Gas Upgrading by the Catalytic Reactor

    Industrial and Engineering Chemistry Research, Vol. 36, Núm. 12, pp. 5227-5239

  5. Hot gas cleaning and upgrading with a calcined dolomite located downstream a biomass fluidized bed gasifier operating with steam-oxygen mixtures

    Energy and Fuels, Vol. 11, Núm. 6, pp. 1194-1197

1996

  1. Biomass gasification with air in an atmospheric bubbling fluidized bed. Effect of six operational variables on the quality of the produced raw gas

    Industrial and Engineering Chemistry Research, Vol. 35, Núm. 7, pp. 2110-2120

  2. Calcined dolomite, magnesite, and calcite for cleaning hot gas from a fluidized bed biomass gasifier with steam: Life and usefulness

    Industrial and Engineering Chemistry Research, Vol. 35, Núm. 10, pp. 3637-3643

1993

  1. Improved Steam Gasification of Lignocellulosic Residues in a Fluidized Bed with Commercial Steam Reforming Catalysts

    Industrial and Engineering Chemistry Research, Vol. 32, Núm. 1, pp. 1-10

1992

  1. Minimum and maximum velocities for fluidization for mixtures of agricultural and forest residues with a second fluidized solid. I. Preliminary data and results with sand-sawdust mixtures

    International chemical engineering, Vol. 32, Núm. 1, pp. 95-102

  2. Minimum and maximum velocities for fluidization for mixtures of agricultural and forest residues with a second fluidized solid. II. Experimental results for different mixtures

    International chemical engineering, Vol. 32, Núm. 1, pp. 103-113