Ammoniacal nitrogen recovery from swine slurry using a gas-permeable membrane: pH control strategies and feed-to-trapping volume ratio

dc.contributor.authorSerra Toro, Andreu
dc.contributor.authorBen Hammou Abboud, Yasmina
dc.contributor.authorCardete García, Mª Alicia
dc.contributor.authorAstals Garcia, Sergi
dc.contributor.authorValentino, Francesco
dc.contributor.authorMas i Pujadas, Francesc
dc.contributor.authorDosta Parras, Joan
dc.date.accessioned2024-04-19T15:48:41Z
dc.date.available2024-04-19T15:48:41Z
dc.date.issued2024
dc.date.updated2024-04-19T15:48:46Z
dc.description.abstractGas-permeable membrane (GPM) technology is gaining interest to recover nitrogen from residual effluents due to its effectiveness, simple operation and capacity of producing a nutrient rich product with fertilising value. In this study, a GPM contactor was used at 25 °C to recover total ammoniacal nitrogen (TAN) from swine slurry as a concentrated (NH4)2SO4 solution. Firstly, a synthetic solution was tested on a wide pH range (6–12). Results showed that the ammonia mass transfer constants (Km) increased from 7.9·10−9 to 1.2·10−6 m/s as the pH increased. The reagent consumption to control the pH per mole nitrogen recovered had a minimum at pH 9, which showed a Km value of 3.0·10−7 m/s. Secondly, various pH control strategies were tested using swine slurry, including (i) no pH control, (ii) pH control at 8.5, 9.0 and 10.0, and (iii) an initial spike of the NaOH equivalent to the required to control the pH at 9. The test without pH control reached a TAN recovery of around 60%, which could be an interesting strategy when high nitrogen recoveries or short operating times are not required. The pH control at 9 stood out as the most favourable operating condition due to its high Km and lower reagent consumption. Thirdly, several feed-to-trapping volume ratios ranging from 1:1 to 15:1 were tested using swine slurry at pH 9. These assays revealed that a GPM process with a high feed-to-trapping volume ratio fastens the recovery of 99% of TAN as a high purity (NH4)2SO4 solution containing 40 g N/L.
dc.format.extent12 p.
dc.format.mimetypeapplication/pdf
dc.identifier.idgrec744616
dc.identifier.issn0944-1344
dc.identifier.urihttps://hdl.handle.net/2445/210205
dc.language.isoeng
dc.publisherSpringer Verlag
dc.relation.isformatofReproducció del document publicat a: https://doi.org/10.1007/s11356-024-32193-5
dc.relation.ispartofEnvironmental Science and Pollution Research, 2024, p. 1-12
dc.relation.urihttps://doi.org/10.1007/s11356-024-32193-5
dc.rightscc by(c) Serra Toro, Andreu et al., 2024
dc.rights.accessRightsinfo:eu-repo/semantics/openAccess
dc.rights.urihttp://creativecommons.org/licenses/by/3.0/es/*
dc.sourceArticles publicats en revistes (Enginyeria Química i Química Analítica)
dc.subject.classificationMembranes (Tecnologia)
dc.subject.classificationNitrogen
dc.subject.classificationAmoníac
dc.subject.otherMembranes (Technology)
dc.subject.otherNitrogen
dc.subject.otherAmmonia
dc.titleAmmoniacal nitrogen recovery from swine slurry using a gas-permeable membrane: pH control strategies and feed-to-trapping volume ratio
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:eu-repo/semantics/publishedVersion

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