JOSÉ
CORELLA TUDANCA
Investigador hasta 2017
Publicaciones (102) Publicaciones de JOSÉ CORELLA TUDANCA
2008
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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
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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
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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
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Modelling a CFB Biomass Gasifier. Part I: Model Formulation
Progress in Thermochemical Biomass Conversion (Wiley Blackwell), pp. 333-345
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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
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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
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A review on dual fluidized-bed biomass gasifiers
Industrial and Engineering Chemistry Research
2006
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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
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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
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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
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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
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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
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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
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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
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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
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Modeling circulating fluidized bed biomass gasifiers. A pseudo-rigorous model for stationary state
Fuel Processing Technology, Vol. 86, Núm. 9, pp. 1021-1053
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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
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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
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Waste incineration in fluidized bed: Testing total oxidation catalysts at pilot scale for gas clean up
AIChE Annual Meeting, Conference Proceedings
2004
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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