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dc.contributor.authorMiranda, Diego A.
dc.contributor.authorMarín, Katherine
dc.contributor.authorSundman, Ola
dc.contributor.authorHedenström, Mattias
dc.contributor.authorQuillaguaman, Jorge
dc.contributor.authorGorzsás, András
dc.contributor.authorBroström, Markus
dc.contributor.authorCarlborg, Markus
dc.contributor.authorLundqvist, Jenny
dc.contributor.authorRomero-Soto, Luis
dc.contributor.authorJönsson, Leif J.
dc.contributor.authorCarrasco, Cristhian
dc.contributor.authorMartín, Carlos
dc.date.accessioned2024-02-01T17:13:22Z
dc.date.available2024-02-01T17:13:22Z
dc.date.created2023-08-30T08:37:54Z
dc.date.issued2023
dc.identifier.citationFermentation. 2023, 9 (6), .en_US
dc.identifier.issn2311-5637
dc.identifier.urihttps://hdl.handle.net/11250/3115139
dc.description.abstractThe global production of fossil-based plastics has reached critical levels, and their substitution with bio-based polymers is an urgent requirement. Poly(3-hydroxybutyrate) (PHB) is a biopolymer that can be produced via microbial cultivation, but efficient microorganisms and low-cost substrates are required. Halomonas boliviensis LC1, a moderately halophilic bacterium, is an effective PHB producer, and hydrolysates of the residual stalks of quinoa (Chenopodium quinoa Willd.) can be considered a cheap source of sugars for microbial fermentation processes in quinoa-producing countries. In this study, H. boliviensis LC1 was adapted to a cellulosic hydrolysate of quinoa stalks obtained via acid-catalyzed hydrothermal pretreatment and enzymatic saccharification. The adapted strain was cultivated in hydrolysates and synthetic media, each of them with two different initial concentrations of glucose. Cell growth, glucose consumption, and PHB formation during cultivation were assessed. The cultivation results showed an initial lag in microbial growth and glucose consumption in the quinoa hydrolysates compared to cultivation in synthetic medium, but after 33 h, the values were comparable for all media. Cultivation in hydrolysates with an initial glucose concentration of 15 g/L resulted in a higher glucose consumption rate (0.15 g/(L h) vs. 0.14 g/(L h)) and volumetric productivity of PHB (14.02 mg/(L h) vs. 10.89 mg/(L h)) than cultivation in hydrolysates with 20 g/L as the initial glucose concentration. During most of the cultivation time, the PHB yield on initial glucose was higher for cultivation in synthetic medium than in hydrolysates. The produced PHBs were characterized using advanced analytical techniques, such as high-performance size-exclusion chromatography (HPSEC), Fourier transform infrared (FTIR) spectroscopy, 1H nuclear magnetic resonance (NMR) spectroscopy, scanning electron microscopy (SEM), X-ray diffraction (XRD), and thermogravimetric analysis (TGA). HPSEC revealed that the molecular weight of PHB produced in the cellulosic hydrolysate was lower than that of PHB produced in synthetic medium. TGA showed higher thermal stability for PHB produced in synthetic medium than for that produced in the hydrolysate. The results of the other characterization techniques displayed comparable features for both PHB samples. The presented results show the feasibility of producing PHB from quinoa stalks with H. boliviensis.en_US
dc.language.isoengen_US
dc.rightsNavngivelse 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/deed.no*
dc.subjectpolyhydroxybutyrateen_US
dc.subjectagricultural residuesen_US
dc.subjectlignocellulosic materialsen_US
dc.subjectquinoaen_US
dc.subjectHalomonas boliviensisen_US
dc.subjecthalophilic bacteriaen_US
dc.subjectbiopolymersen_US
dc.subjectadaptationen_US
dc.titleProduction and Characterization of Poly(3-hydroxybutyrate) from Halomonas boliviensis LC1 Cultivated in Hydrolysates of Quinoa Stalksen_US
dc.title.alternativeProduction and Characterization of Poly(3-hydroxybutyrate) from Halomonas boliviensis LC1 Cultivated in Hydrolysates of Quinoa Stalksen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.rights.holder© 2023 by the authors.en_US
dc.subject.nsiVDP::Teknologi: 500::Bioteknologi: 590en_US
dc.source.pagenumber0en_US
dc.source.volume9en_US
dc.source.journalFermentationen_US
dc.source.issue6en_US
dc.identifier.doi10.3390/fermentation9060556
dc.identifier.cristin2170702
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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Navngivelse 4.0 Internasjonal
Except where otherwise noted, this item's license is described as Navngivelse 4.0 Internasjonal