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Optimisation of the production of fermentable monosaccharides from algal biomass grown in photobioreactors treating wastewater.
Martín-Juárez, Judit; Vega-Alegre, Marisol; Riol-Pastor, Elena; Muñoz-Torre, Raúl; Bolado-Rodríguez, Silvia.
Afiliação
  • Martín-Juárez J; Department of Chemical Engineering and Environmental Technology, University of Valladolid, Calle Doctor Mergelina s/n, 47011 Valladolid, Spain; Institute of Sustainable Processes, University of Valladolid, 47011 Valladolid, Spain. Electronic address: judit.martin@iq.uva.es.
  • Vega-Alegre M; Institute of Sustainable Processes, University of Valladolid, 47011 Valladolid, Spain; Department of Analytical Chemistry, University of Valladolid, Campus Miguel Delibes, Paseo Belén 7, 47011 Valladolid, Spain. Electronic address: solvega@qa.uva.es.
  • Riol-Pastor E; Department of Chemical Engineering and Environmental Technology, University of Valladolid, Calle Doctor Mergelina s/n, 47011 Valladolid, Spain. Electronic address: elena.riol@hotmail.es.
  • Muñoz-Torre R; Department of Chemical Engineering and Environmental Technology, University of Valladolid, Calle Doctor Mergelina s/n, 47011 Valladolid, Spain; Institute of Sustainable Processes, University of Valladolid, 47011 Valladolid, Spain. Electronic address: mutora@iq.uva.es.
  • Bolado-Rodríguez S; Department of Chemical Engineering and Environmental Technology, University of Valladolid, Calle Doctor Mergelina s/n, 47011 Valladolid, Spain; Institute of Sustainable Processes, University of Valladolid, 47011 Valladolid, Spain. Electronic address: silvia@iq.uva.es.
Bioresour Technol ; 281: 239-249, 2019 Jun.
Article em En | MEDLINE | ID: mdl-30825827
Biomass grown in wastewater treatment photobioreactors is a cheap raw material with high contents of carbohydrates, proteins and lipids. This work studies the production of fermentable monosaccharides from three biomasses grown in piggery wastewater (P), domestic wastewater (W) and synthetic medium (S) by applying chemical pretreatment and enzymatic hydrolysis, using a Taguchi design. ANOVA identified temperature, chemical reagent type and chemical reagent concentration as significant operational parameters. However, the biomass concentration, pretreatment time, enzyme dosage and enzymatic hydrolysis time had no remarkable effect. The bacterial content of the biomass had no relevant impact on carbohydrate and protein solubilisation but had a remarkable effect on the degradation of the released carbohydrates (57, 60 and 37% for P, W and S), while also affecting lipid solubilisation. Pretreatment with HCl 2 M at 120 °C resulted the optimal conditions, achieving a monosaccharide recovery of 53, 59 and 80% for P, W and S biomasses, respectively.
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Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Assunto principal: Biomassa / Fermentação / Fotobiorreatores / Águas Residuárias / Monossacarídeos Idioma: En Revista: Bioresour Technol Assunto da revista: ENGENHARIA BIOMEDICA Ano de publicação: 2019 Tipo de documento: Article

Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Assunto principal: Biomassa / Fermentação / Fotobiorreatores / Águas Residuárias / Monossacarídeos Idioma: En Revista: Bioresour Technol Assunto da revista: ENGENHARIA BIOMEDICA Ano de publicação: 2019 Tipo de documento: Article