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<dc:title>Nitrous Oxide Abatement Coupled with Biopolymer Production As a Model GHG Biorefinery for Cost-Effective Climate Change Mitigation</dc:title>
<dc:creator>Frutos, Osvaldo D.</dc:creator>
<dc:creator>Cortés Martín, Irene</dc:creator>
<dc:creator>Cantera Ruiz De Pellon, Sara</dc:creator>
<dc:creator>Arnáiz, Esther</dc:creator>
<dc:creator>Lebrero Fernández, Raquel</dc:creator>
<dc:creator>Muñoz Torre, Raúl</dc:creator>
<dc:description>Producción Científica</dc:description>
<dc:description>N2O represents ∼6% of the global greenhouse gas emission inventory and the most important O3-depleting substance emitted in this 21st century. Despite its environmental relevance, little attention has been given to cost-effective and environmentally friendly N2O abatement methods. Here we examined, the potential of a bubble column (BCR) and an internal loop airlift (ALR) bioreactors of 2.3 L for the abatement of N2O from a nitric acid plant emission. The process was based on the biological reduction of N2O by Paracoccus denitrificans using methanol as a carbon/electron source. Two nitrogen limiting strategies were also tested for the coproduction of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) coupled with N2O reduction. High N2O removal efficiencies (REs) (≈87%) together with a low PHBV cell accumulation were observed in both bioreactors in excess of nitrogen. However, PHBV contents of 38–64% were recorded under N limiting conditions along with N2O-REs of ≈57% and ≈84% in the ALR and BCR, respectively. Fluorescence in situ hybridization analyses showed that P. denitrificans was dominant (>50%) after 6 months of experimentation. The successful abatement of N2O concomitant with PHBV accumulation confirmed the potential of integrating biorefinery concepts into biological gas treatment for a cost-effective GHG mitigation.</dc:description>
<dc:date>2017-06-19T08:43:26Z</dc:date>
<dc:date>2017-06-19T08:43:26Z</dc:date>
<dc:date>2017</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>Environmental Science &amp; Technology, 2017, 51 (11), pp 6319–6325</dc:identifier>
<dc:identifier>http://uvadoc.uva.es/handle/10324/23524</dc:identifier>
<dc:identifier>10.1021/acs.est.7b00643</dc:identifier>
<dc:identifier>Environmental Science &amp; Technology</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>http://pubs.acs.org/doi/abs/10.1021/acs.est.7b00643</dc:relation>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
<dc:rights>Attribution-NonCommercial-NoDerivatives 4.0 International</dc:rights>
<dc:publisher>American Chemical Society</dc:publisher>
<dc:peerreviewed>SI</dc:peerreviewed>
</ow:Publication>
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