JOSÉ CORELLA TUDANCA-rekin lankidetzan egindako argitalpenak (102)

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

  2. Biomass gasification with pure steam in fluidised bed: 12 variables that affect the effectiveness of the biomass gasifier

    International Journal of Oil, Gas and Coal Technology, Vol. 1, Núm. 1-2, pp. 194-207

  3. Combustion of Chlorine-Containing Biomass: V2O5-WO3-TiO2 Monoliths for Cl-VOCs Abatement in the Flue Exit Gas. Part I

    Progress in Thermochemical Biomass Conversion (Wiley Blackwell), pp. 887-895

  4. Modelling a CFB Biomass Gasifier. Part I: Model Formulation

    Progress in Thermochemical Biomass Conversion (Wiley Blackwell), pp. 333-345

  5. Performance of CaO and MgO for the hot gas clean up in gasification of a chlorine-containing (RDF) feedstock

    Bioresource Technology, Vol. 99, Núm. 16, pp. 7539-7544

  6. Steam gasification of coal at low-medium (600-800 °C) temperature with simultaneous CO2 capture in a bubbling fluidized bed at atmospheric pressure. 2. Results and recommendations for scaling up

    Industrial and Engineering Chemistry Research, Vol. 47, Núm. 6, pp. 1798-1811

2007

  1. A review on dual fluidized-bed biomass gasifiers

    Industrial and Engineering Chemistry Research

2006

  1. Calculation of the conditions to get less than 2 g tar/mn3 in a fluidized bed biomass gasifier

    Fuel Processing Technology, Vol. 87, Núm. 9, pp. 841-846

  2. Catalytic hot gas cleaning with monoliths in biomass gasification in fluidized beds. 4. Performance of an advanced, second-generation, two-layers-based monolithic reactor

    Industrial and Engineering Chemistry Research, Vol. 45, Núm. 4, pp. 1389-1396

  3. 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

  4. Modeling circulating fluidized bed biomass gasifiers. Results from a pseudo-rigorous 1-dimensional model for stationary state

    Fuel Processing Technology, Vol. 87, Núm. 3, pp. 247-258

  5. Steam gasification of coal at low-medium (600-800°C) temperature with simultaneous CO2 capture in fluidized bed at atmospheric pressure: The effect of inorganic species. 1. Literature review and comments

    Industrial and Engineering Chemistry Research, Vol. 45, Núm. 18, pp. 6137-6146

2005

  1. Catalytic hot gas cleaning with monoliths in biomass gasification in fluidized bed. Modeling of the 2nd generation two layers monolithic reactor

    AIChE Annual Meeting, Conference Proceedings

  2. Catalytic hot gas cleaning with monoliths in biomass gasification in fluidized bed. Modeling of the 2nd generation two layers monolithic reactor

    AIChE Annual Meeting Conference Proceedings

  3. Catalytic hot gas cleaning with monoliths in biomass gasification in fluidized beds. 3. Their effectiveness for ammonia elimination

    Industrial and Engineering Chemistry Research, Vol. 44, Núm. 7, pp. 2036-2045

  4. Modeling circulating fluidized bed biomass gasifiers. A pseudo-rigorous model for stationary state

    Fuel Processing Technology, Vol. 86, Núm. 9, pp. 1021-1053

  5. The partitioning of heavy metals in incineration of sludges and waste in a bubbling fluidized bed. 2. Interpretation of results with a conceptual model

    Journal of Hazardous Materials, Vol. 126, Núm. 1-3, pp. 158-168

  6. The partitioning of heavy metals in incineration of sludges and waste in a bubbling fluidized bed. Part II. Review and. its modeling

    REWAS'04 - Global Symposium on Recycling, Waste Treatment and Clean Technology

  7. Waste incineration in fluidized bed: Testing total oxidation catalysts at pilot scale for gas clean up

    AIChE Annual Meeting, Conference Proceedings

2004

  1. Catalytic Hot Gas Cleaning with Monoliths in Biomass Gasification in Fluidized Beds. 1. Their Effectiveness for Tar Elimination

    Industrial and Engineering Chemistry Research, Vol. 43, Núm. 10, pp. 2433-2445