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Tesis Doctoral
Thermochemical Biorefineries and based on DME as platform chemical: conceptual design and technoeconomic assessment. Biorrefinerías Termoquímicas basadas en DME como intermediario: Diseño conceptual y análisis tecno-económico
(2013)
Esta tesis se centra en el estudio de biorrefinerías termoquímicas (instalación que procesa biomasa para la producción de una gran variedad de productos: combustibles para la producción de calor o electricidad, carburantes ...
Artículo
Technoeconomic assessment of lignocellulosic ethanol production via DME hydrocarbonylation
(Elsevier, 2012)
In this study, a new thermochemical route to produce lignocellulosic ethanol based on DME (dimethyl ether) hydrocarbonylation is proposed and economically assessed. The process is designed and evaluated using current kinetic ...
Ponencia
Gasification of Wastes in a Pilot Fluidized Bed Gasifier
(EUBCE, 2011)
A technical assessment of gasification of various wastes in fluidized bed was made by conducting test in a 100 kWth pilot plant. The reactor was operated under simulated autothermal and adiabatic conditions, thus allowing ...
Artículo
Thermochemical biorefinery based on dimethyl ether as intermediate: Technoeconomic assessment
(Elsevier, 2013)
Thermochemical biorefinery based on dimethyl ether (DME) as an intermediate is studied. DME is converted into methyl acetate, which can either be hydrogenated to ethanol or sold as a co-product. Considering this option ...
Ponencia
Devolatilization of two agricultural residues in fluidized bed: product distribution and influence of fluidization agent
(EUBCE, 2011)
Devolatilization of two agricultural residues; corn stover and a solid by-product from enzymatic hydrolysis of biomass (cake), was carried out in a fluidized bed at temperatures between 750 and 900 ºC. The distribution of ...
Ponencia
Gasification kinetics of char from olive tree pruning with CO2 and stema in fluidized bed
(EUBCE, 2013)
Kinetics of gasification of char from olive tree pruning was measured in a fluidized bed at temperatures between 760 and 900 ºC. Experiments were carried out using H2ON2 and CO2N2 mixtures to measure the rates of the ...
Ponencia
Gasification of Char from Dried Sewage Sludge with Steam and CO2 in Fluidized Bed
(EUBCE, 2010)
Kinetics of gasification of char obtained from dried sewage sludge (DSS) with steam and CO2 have been measured in a laboratory fluidized bed (FB) reactor at temperatures between 800 and 950 ºC with steam and CO2. Char was ...
Ponencia
Fluid-Dynamics of a Cold Model of a Fluidized Bed Gasification System with Reduced Tar Content
(EUBCE, 2010)
A new gasification concept for biomass/waste gasification for electricity production for small/medium application has been developed. The gasification system is aimed at improving the two major drawbacks in fluidized beds ...
Ponencia
Conversion of Olive Tree Prunings Fluidized Bed: Experiments and Gasifier Modeling
(EUBCE, 2013)
Fuel conversion measurements were conducted in a laboratory fluidized bed (FB) to characterize the most important steps taking place a FB gasifier in the range of 800.900 ºC. The main inputs for the gasifier model to be ...