<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-04-27T21:42:50Z</responseDate><request verb="GetRecord" identifier="oai:uvadoc.uva.es:10324/46752" metadataPrefix="etdms">https://uvadoc.uva.es/oai/request</request><GetRecord><record><header><identifier>oai:uvadoc.uva.es:10324/46752</identifier><datestamp>2022-07-18T09:33:09Z</datestamp><setSpec>com_10324_35294</setSpec><setSpec>com_10324_952</setSpec><setSpec>com_10324_894</setSpec><setSpec>col_10324_35295</setSpec></header><metadata><thesis xmlns="http://www.ndltd.org/standards/metadata/etdms/1.0/" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.ndltd.org/standards/metadata/etdms/1.0/ http://www.ndltd.org/standards/metadata/etdms/1.0/etdms.xsd">
<title>Biogas valorization via continuous polyhydroxybutyrate production by Methylocystis hirsuta in a bubble column bioreactor</title>
<creator>Rodríguez Muñoz, Yadira</creator>
<creator>Firmino, Paulo Igor Milen</creator>
<creator>Pérez, Víctor</creator>
<creator>Lebrero Fernández, Raquel</creator>
<creator>Muñoz Torre, Raúl</creator>
<description>Producción Científica</description>
<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.</description>
<date>2021-06-04</date>
<date>2021-06-04</date>
<date>2020</date>
<type>info:eu-repo/semantics/article</type>
<identifier>Waste Management, 2020, vol. 113, p. 395-403</identifier>
<identifier>0956-053X</identifier>
<identifier>https://uvadoc.uva.es/handle/10324/46752</identifier>
<identifier>10.1016/j.wasman.2020.06.009</identifier>
<identifier>395</identifier>
<identifier>403</identifier>
<identifier>Waste Management</identifier>
<identifier>113</identifier>
<language>eng</language>
<relation>https://www.sciencedirect.com/science/article/abs/pii/S0956053X20303196</relation>
<rights>info:eu-repo/semantics/openAccess</rights>
<rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</rights>
<rights>© 2020 Elsevier</rights>
<rights>Attribution-NonCommercial-NoDerivatives 4.0 Internacional</rights>
<publisher>Elsevier</publisher>
</thesis></metadata></record></GetRecord></OAI-PMH>