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<dc:title>Biogas valorization via continuous polyhydroxybutyrate production by Methylocystis hirsuta in a bubble column bioreactor</dc:title>
<dc:creator>Rodríguez Muñoz, Yadira</dc:creator>
<dc:creator>Firmino, Paulo Igor Milen</dc:creator>
<dc:creator>Pérez, Víctor</dc:creator>
<dc:creator>Lebrero Fernández, Raquel</dc:creator>
<dc:creator>Muñoz Torre, Raúl</dc:creator>
<dc:subject>Bioplásticos</dc:subject>
<dc:subject>Biorrefinería</dc:subject>
<dc:subject>Bioplastics</dc:subject>
<dc:subject>Biorefinery</dc:subject>
<dc:subject>23 Química</dc:subject>
<dc:subject>33 Ciencias Tecnológicas</dc:subject>
<dc:description>Producción Científica</dc:description>
<dc:description>Creating additional value out of biogas during waste treatment has become a priority in past years. Biogas bioconversion into valuable bioproducts such as biopolymers has emerged as a promising strategy. This work assessed the operational feasibility of a bubble column bioreactor (BCB) implemented with gas recirculation and inoculated with a polyhydroxybutyrate (PHB)-producing strain using biogas as substrate. The BCB was initially operated at empty bed residence times (EBRTs) ranging from 30 to 120 min and gas recirculation ratios (R) from 0 to 30 to assess the gas-to-liquid mass transfer and bioconversion of CH4. Subsequently, the BCB was continuously operated at a R of 30 and an EBRT of 60 min under excess of nitrogen and nitrogen feast-famine cycles of 24 h:24 h to trigger PHB synthesis. Gas recirculation played a major role in CH4 gas–liquid transfer, providing almost fourfold higher CH4 elimination capacities (~41 g CH4 m−3 h−1) at the highest R and EBRT of 60 min. The long-term operation under N excess conditions entailed nitrite accumulation (induced by O2 limiting conditions) and concurrent methanotrophic activity inhibition above ~60 mg N-NO2− L−1. Adjusting the N-NO3− supply to match microbial N demand successfully prevented nitrite accumulation. Finally, the N feast-famine 24 h:24 h strategy supported a stable CH4 conversion with a removal efficiency of 70% along with a continuous PHB production, which yielded PHB accumulations of 14.5 ± 2.9% (mg PHB mg−1 total suspended solids × 100). These outcomes represent the first step towards the integration of biogas biorefineries into conventional anaerobic digestion plants.</dc:description>
<dc:description>Ministerio de Ciencia e Innovación (grant BES-2016-077160) y (proyecto CTM2015-70442-R)</dc:description>
<dc:description>Junta de Castilla y León y EU-FEDER (CLU 2017-09) , (UIC 526071) y (VA281P18)</dc:description>
<dc:date>2021-06-04T12:23:23Z</dc:date>
<dc:date>2021-06-04T12:23:23Z</dc:date>
<dc:date>2020</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:type>info:eu-repo/semantics/acceptedVersion</dc:type>
<dc:identifier>Waste Management, 2020, vol. 113, p. 395-403</dc:identifier>
<dc:identifier>0956-053X</dc:identifier>
<dc:identifier>https://uvadoc.uva.es/handle/10324/46752</dc:identifier>
<dc:identifier>10.1016/j.wasman.2020.06.009</dc:identifier>
<dc:identifier>395</dc:identifier>
<dc:identifier>403</dc:identifier>
<dc:identifier>Waste Management</dc:identifier>
<dc:identifier>113</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>https://www.sciencedirect.com/science/article/abs/pii/S0956053X20303196</dc:relation>
<dc:rights>Attribution-NonCommercial-NoDerivatives 4.0 Internacional</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
<dc:rights>© 2020 Elsevier</dc:rights>
<dc:format>application/pdf</dc:format>
<dc:publisher>Elsevier</dc:publisher>
<europeana:object>https://uvadoc.uva.es/bitstream/10324/46752/4/Biogas-valorization-via-continuous.pdf.jpg</europeana:object>
<europeana:provider>Hispana</europeana:provider>
<europeana:type>TEXT</europeana:type>
<europeana:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</europeana:rights>
<europeana:dataProvider>UVaDOC. Repositorio Documental de la Universidad de Valladolid</europeana:dataProvider>
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