Process performance and precipitate quality of phosphorus recovery by struvite precipitation in a fluidized bed reactor using a MgO industrial by-product

dc.contributor.authorAguilar Pozo, Verónica-Belén
dc.contributor.authorChimenos Ribera, Josep Ma.
dc.contributor.authorPeña Picola, Sergi
dc.contributor.authorOlaciregui-Arizmendi, K.
dc.contributor.authorElduayen-Echave, B.
dc.contributor.authorAyesa Iturrate, Eduardo José
dc.contributor.authorAstals Garcia, Sergi
dc.date.accessioned2024-04-19T16:38:02Z
dc.date.available2024-04-19T16:38:02Z
dc.date.issued2024-04-14
dc.date.updated2024-04-19T16:38:07Z
dc.description.abstractPhosphorus recovery through struvite precipitation has gained interest due to the potential use of struvite as a fertiliser, with fluidised bed reactors being a popular technology for carrying out the process. Struvite precipitation requires a magnesium source and an alkaline reagent. This research uses a low-grade magnesium oxide (LG-MgO) industrial by-product with a 56 wt% of MgO as magnesium source and an alkaline reagent to lower operating costs and value-add an industrial by-product. LG-MgO is poorly soluble in water, but its solubility increases significantly when dissolved in anaerobic digestion supernatants due to its circumneutral pH and high buffer capacity. Phosphorus precipitation was carried out in a laboratory-scale fluidised bed reactor where three operating variables (i.e. P:Mg molar ratio, feed inlet position, and recirculation flow rate) were studied to determine the LG-MgO impact on precipitate struvite content. Experimental results showed a high struvite content in all precipitates, close to the values reported for pure magnesium sources. The P:Mg molar ratio influenced precipitate composition. The percentage of struvite in the precipitate were 75–82 wt%, 85–88 wt%, and 75–76 wt% for the P:Mg ratio of 1:0.5, 1:1 and 1:3, respectively. The feed inlet position (side or bottom) also had an impact on precipitate struvite content when the P:Mg molar ratio was 1:3, but not for the other molar ratios. The recirculation flow rate did not have a significant impact on precipitate struvite content.
dc.format.extent9 p.
dc.format.mimetypeapplication/pdf
dc.identifier.idgrec748027
dc.identifier.issn2213-2929
dc.identifier.urihttps://hdl.handle.net/2445/210206
dc.language.isoeng
dc.publisherElsevier Ltd
dc.relation.isformatofReproducció del document publicat a: https://doi.org/10.1016/j.jece.2024.112764
dc.relation.ispartofJournal of Environmental Chemical Engineering, 2024, vol. 12, num.3, p. 1-9
dc.relation.urihttps://doi.org/10.1016/j.jece.2024.112764
dc.rightscc-by-nc-nd (c) Aguilar Pozo, Verónica Belén, et al., 2024
dc.rights.accessRightsinfo:eu-repo/semantics/openAccess
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/
dc.sourceArticles publicats en revistes (Enginyeria Química i Química Analítica)
dc.subject.classificationDigestió anaeròbia
dc.subject.classificationÒxid de magnesi
dc.subject.classificationFòsfor
dc.subject.otherAnaerobic digestion
dc.subject.otherMagnesium oxide
dc.subject.otherPhosphorus
dc.titleProcess performance and precipitate quality of phosphorus recovery by struvite precipitation in a fluidized bed reactor using a MgO industrial by-product
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:eu-repo/semantics/publishedVersion

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