JOSÉ MANUEL
TOLEDO GABRIEL
Profesor titular de universidad
Publicaciones (36) Publicaciones de JOSÉ MANUEL TOLEDO GABRIEL
2021
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Teaching chemical engineering using Jupyter notebook: Problem generators and lecturing tools
Education for Chemical Engineers, Vol. 37, pp. 1-10
2020
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Diseño de reactores
Ingeniería de procesos: diseño e integración de procesos químicos (Dextra), pp. 173-195
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Selección de las condiciones de operación y materiales de construcción de los equipos
Ingeniería de procesos: diseño e integración de procesos químicos (Dextra), pp. 69-89
2011
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Catalytic air gasification of plastic waste (polypropylene) in a fluidized bed. Part II: Effects of some operating variables on the quality of the raw gas produced using olivine as the in-bed material
Industrial and Engineering Chemistry Research, Vol. 50, Núm. 21, pp. 11815-11821
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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Catalytic air gasification of plastic waste (Polypropylene) in fluidized bed. Part I: Use of in-gasifier bed additives
Industrial and Engineering Chemistry Research, Vol. 47, Núm. 4, pp. 1005-1010
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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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Performance of a fluidized bed gasifier in catalytic air gasification of plastic waste
CHISA 2008 - 18th International Congress of Chemical and Process Engineering
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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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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