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    Por favor, use este identificador para citar o enlazar este ítem:http://uvadoc.uva.es/handle/10324/23480

    Título
    Integrated fractionation-hydrolysis process using sub- and supercritical water for lignocellulosic biomass valorization
    Autor
    Piqueras, Cristian Martín
    Cabeza Sánchez, ÁlvaroAutoridad UVA Orcid
    Gallina, GianlucaAutoridad UVA
    Cantero Sposetti, Danilo AlbertoAutoridad UVA Orcid
    García Serna, JuanAutoridad UVA Orcid
    Cocero Alonso, María JoséAutoridad UVA Orcid
    Año del Documento
    2017
    Editorial
    Elsevier
    Documento Fuente
    Chemical Engineering Journal, Enero 2017, vol. 308, p. 110-125
    Résumé
    A novel process coupling the fractionation and hydrolysis reactors is presented. Holm oak was used as real lignocellulosic biomass to be treated. In the fractionation reactor, hemicellulose and cellulose were solubilized and partially hydrolyzed in different stages with the aim of feeding the hydrolysis reactor with high C5 concentrations or C6 concentrations. The fractionation was performed in two stages: at 180°C optimizing the hemicellulose extraction and at 260°C extracting cellulose and hard hemicellulose remaining in the biomass structure. Three water flows were tested: 11, 17 and 26 cm³/min. Sugar yields from 71 to 75% were reached, mainly composed of xylose and glucose oligomers and lower amounts of other chemicals, like retro-aldol products, acetic acid or 5-HMF. The outlet stream from the fractionation reactor was directly mixed with sub or supercritical water at the inlet mixer of a SHR where the reaction time was precisely controlled. The temperature, pressure and reaction time were modified to get an insight of their effect on the yield of retro-aldol condensation products. Yields of 24% for glycolaldehyde, and pyruvaldehyde were found at 8.3 s, 350°C and 162 bar (hydrolysis reactor conditions). On other hand, 25% of lactic acid was found at 0.23 s, 396°C and 245 bar. A discussion based on a known reaction pathway is proposed. Moreover, a kinetic model for the hydrolysis reactor was proposed, being able to reproduce the experimental data with deviations lower than 10% for sugars and other products extracted. This combined process performs a selective valorization of real lignocellulosic biomass, avoiding the costly process of extreme grinding needed for the fluidization in a continuous hydrothermal process.
    Revisión por pares
    SI
    DOI
    10.1016/j.cej.2016.09.007
    Patrocinador
    CTQ2015-64892-R (MINECO/FEDER)
    Version del Editor
    https://www.journals.elsevier.com/chemical-engineering-journal
    Idioma
    spa
    URI
    http://uvadoc.uva.es/handle/10324/23480
    Derechos
    openAccess
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    Attribution-NonCommercial-NoDerivatives 4.0 InternationalExcepté là où spécifié autrement, la license de ce document est décrite en tant que Attribution-NonCommercial-NoDerivatives 4.0 International

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