Valorization of strawberry extrudate waste: Recovery of phenolic compounds by direct-hydrothermal treatment and subsequent methane production by mesophilic semi-continuous anaerobic digestion

dc.contributor.authorCubero Cardoso, Juan
dc.contributor.authorJiménez Páez, Elena
dc.contributor.authorTrujillo Reyes, Ángeles
dc.contributor.authorSerrano, Antonio
dc.contributor.authorUrbano Baena, Juan
dc.contributor.authorRodríguez Gutiérrez, Guillermo
dc.contributor.authorBorja Padilla, Rafael
dc.contributor.authorGonzález Fermoso, Fernando
dc.date.accessioned2024-02-23T12:17:41Z
dc.date.available2024-02-23T12:17:41Z
dc.date.issued2023-07
dc.description.abstractStrawberry extrudate (SE) is an underused by-product from strawberry industry. Recovery of the phenolic compounds present in SE would represent a very interesting valorisation option. Two main challenges need to be solved, firstly, the solubilisation and recovery of the phenolic compounds contained in SE, and, after that, the stabilisation of the resulted de-phenolized SE. The present research evaluates the potential of a biorefinery process combining a hydrothermal pre-treatment, followed by a phenolic extraction process and, finally, the anaerobic digestion of the remaining SE for producing energy that will contribute to compensate the energy requirements of the whole system. Following the hydrothermal pre-treatment at 170 °C for 60 min, an extraction of 0.6 ± 0.1 g of gallic acid per kilogram of SE was achieved using an adsorbent resin, representing a recovery rate of 64 %. Long-term semi-continuous anaerobic digestion of de-phenolized SE was evaluated at different organic loading rates to evaluate the stability of the process. The anaerobic digestion of pre-treated SE achieved a stable methane production value of 243 ± 34 mL CH4·g volatile solids−1·d−1 at an organic loading rate (ORL) of 1.25 g volatile solids·L−1·d−1. During the operation at this ORL, the control parameters including pH, alkalinity, soluble chemical organic demand (sCOD), and volatile fatty acid (VFA) remained stable and consistently constant. Specifically, the VFA in the reactor during this stable period achieved a value of 102 ± 128 mg O2/L. Also, an economic balance showed that the minimal price of the generated phenolic extract for having benefited from the proposed biorefinery system was 0.812 €·(g of gallic acid equivalents)−1, a price within the range of phenolic compounds used in the food industry.es_ES
dc.description.departmentQuímica "Profesor José Carlos Vílchez Martín"
dc.description.sponsorshipThis research was funded by the Spanish Ministry of Economy, Industry, and Competitiveness through Project CTM2017-83870-R. The authors are grateful to the Regional Government of Andalusia, Junta de Andalucía, Consejería de Economía y Conocimiento (Project UHU-1257728), for providing additional financial support.es_ES
dc.identifier.citationCubero-Cardoso, J., Jiménez-Páez, E., Trujillo-Reyes, Á., Serrano, A., Urbano, J., Rodríguez-Gutiérrez, G., Borja, R., & Fermoso, F. G. (2023). Valorization of strawberry extrudate waste: Recovery of phenolic compounds by direct-hydrothermal treatment and subsequent methane production by mesophilic semi-continuous anaerobic digestion. In Waste Management (Vol. 169, pp. 310–318). Elsevier BV. https://doi.org/10.1016/j.wasman.2023.07.016es_ES
dc.identifier.doi10.1016/j.wasman.2023.07.016
dc.identifier.issn0956-053X
dc.identifier.urihttps://hdl.handle.net/10272/23296
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rightsAtribución-NoComercial-SinDerivadas 3.0 España*
dc.rights.accessRightsopen accesses_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/*
dc.subject.otherAgro-wastees_ES
dc.subject.otherBiorefineryes_ES
dc.subject.otherEconomic assessmentes_ES
dc.subject.otherHydrothermal pre-treatmentes_ES
dc.subject.otherPhenolic compounds recoveryes_ES
dc.subject.unesco3309 Tecnología de Los Alimentoses_ES
dc.subject.unesco23 Químicaes_ES
dc.titleValorization of strawberry extrudate waste: Recovery of phenolic compounds by direct-hydrothermal treatment and subsequent methane production by mesophilic semi-continuous anaerobic digestiones_ES
dc.typejournal articlees_ES
dc.type.hasVersionVoR
dspace.entity.typePublication
relation.isAuthorOfPublication01a1798e-def1-41bf-9377-c01547854b10
relation.isAuthorOfPublication.latestForDiscovery01a1798e-def1-41bf-9377-c01547854b10

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