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dc.contributor.authorVecino Bello, Xanel
dc.contributor.authorReig i Amat, Mònica
dc.contributor.authorBhushan, Brij
dc.contributor.authorGibert Agulló, Oriol
dc.contributor.authorValderrama Angel, César Alberto
dc.contributor.authorCortina Pallás, José Luís
dc.contributor.otherUniversitat Politècnica de Catalunya. Departament d'Enginyeria Química
dc.date.accessioned2019-02-01T14:40:36Z
dc.date.issued2019-03-15
dc.identifier.citationVecino, X. [et al.]. Liquid fertilizer production by ammonia recovery from treated ammonia-rich regenerated streams using liquid-liquid membrane contactors. "Chemical engineering journal", 15 Març 2019, vol. 360, p. 890-899.
dc.identifier.issn1385-8947
dc.identifier.urihttp://hdl.handle.net/2117/128152
dc.description.abstractThe nitrogen load on urban wastewater should be considered as a secondary resource for nitrogen-based fertilizers. From this point of view, ammonia-rich streams obtained from a regeneration step with zeolites using 70-80 g NaOH/L could contain up to 3.5-4.5 g NH3/L as well as other ionic species (Na+, K+, Ca2+, Mg2+) and dissolved organic matter (DOM). Thus, they could be treated to obtain a valuable product composed by ammonia for fertilizing applications. A sorption pre-treatment process was carried out to remove the residual amount of DOM and to reduce membrane fouling before processing with hollow fibres liquid-liquid membrane contactors (HF-LLMC). Polypropylene HF-LLMC was used to selectively extract ammonia in single or two-step configurations using different acid stripping solutions (H3PO4, HNO3 or a mixture of HNO3/H3PO4). For ammonia recovery, the ammonia mass transfer coefficient (Km(NH3)) and water transport by HF-LLMC were determined. H3PO4 was found to be the best acid stripping solution by one-step HF-LLMC; the ammonia removal was 76% with a Km(NH3) of 8.8x10-7 m/s. Additionally, the ammonia was concentrated 26 times, and it was recovered as multi-nutrient liquid fertilizer (NP) composed of 7.8% N and 21.6% P2O5. Furthermore, ammonia recovery was increased, reaching values up to 94%, through two-step HF-LLMC, and again H3PO4 was used as stripping solution. Finally, water transport from the feed to the stripping phase was estimated to be 0.022 L/m2·h for one-step HF-LLMC with H3PO4. Finally, the use of UV-Vis and 2D-Fluorescence was shown to be a successful approach for monitoring pore wetting events.
dc.format.extent10 p.
dc.language.isoeng
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Spain
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/
dc.subjectÀrees temàtiques de la UPC::Enginyeria química
dc.subject.lcshMunicipal water supply
dc.subject.lcshAmmonium salts
dc.subject.lcshHydrophobic surfaces
dc.titleLiquid fertilizer production by ammonia recovery from treated ammonia-rich regenerated streams using liquid-liquid membrane contactors
dc.typeArticle
dc.subject.lemacAigües residuals
dc.contributor.groupUniversitat Politècnica de Catalunya. R2EM - Resource Recovery and Environmental Management
dc.identifier.doi10.1016/j.cej.2018.12.004
dc.description.peerreviewedPeer Reviewed
dc.rights.accessRestricted access - publisher's policy
drac.iddocument23617328
dc.description.versionPostprint (author's final draft)
dc.date.lift2023-03-15
upcommons.citation.authorVecino, X.; Reig, M.; Bhushan, B.; Gibert, O.; Valderrama, C.; Cortina, J.
upcommons.citation.publishedtrue
upcommons.citation.publicationNameChemical engineering journal
upcommons.citation.volume360
upcommons.citation.startingPage890
upcommons.citation.endingPage899


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Except where otherwise noted, content on this work is licensed under a Creative Commons license: Attribution-NonCommercial-NoDerivs 3.0 Spain