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               <dc:title>A review on the integration of mainstream P-recovery strategies with enhanced biological phosphorus removal</dc:title>
               <dc:creator>Zhang, Congcong</dc:creator>
               <dc:creator>Guisasola, Albert</dc:creator>
               <dc:creator>Baeza, Juan Antonio</dc:creator>
               <dc:subject>Configurations</dc:subject>
               <dc:subject>Enhanced biological phosphorus removal (EBPR)</dc:subject>
               <dc:subject>Mainstream</dc:subject>
               <dc:subject>Phosphorus recovery</dc:subject>
               <dc:subject>Precipitation</dc:subject>
               <dc:description>Altres ajuts: acords transformatius de la UAB</dc:description>
               <dc:description>Phosphorus (P), an essential nutrient for all organisms, urgently needs to be recovered due to the increasing demand and scarcity of this natural resource. Recovering P from wastewater is a feasible and promising way widely studied nowadays due to the need to remove P in wastewater treatment plants (WWTPs). When enhanced biological P removal (EBPR) is implemented, an innovative option is to recover P from the supernatant streams obtained in the mainstream water line, and then combine it with liquor-crystallisation recovery processes, being the final recovered product struvite, vivianite or hydroxyapatite. The basic idea of these mainstream P-recovery strategies is to take advantage of the ability of polyphosphate accumulating organisms (PAO) to increase P concentration under anaerobic conditions when some carbon source is available. This work shows the mainstream P-recovery technologies reported so far, both in continuous and sequenced batch reactors (SBR) based configurations. The amount of extraction, as a key parameter to balance the recovery efficiency and the maintenance of the EBPR of the system, should be the first design criterion. The maximum value of P-recovery efficiency for long-term operation with an adequate extraction ratio would be around 60%. Other relevant factors (e.g. COD/P ratio of the influent, need for an additional carbon source) and operational parameters (e.g. aeration, SRT, HRT) are also reported and discussed.</dc:description>
               <dc:date>2022</dc:date>
               <dc:type>Article</dc:type>
               <dc:relation>Agencia Estatal de Investigación CTQ2017-82404-R</dc:relation>
               <dc:relation>Agència de Gestió d'Ajuts Universitaris i de Recerca 2017/SGR-1175</dc:relation>
               <dc:relation>Water research ; Vol. 212 (April 2022), art. 118102</dc:relation>
               <dc:rights>open access</dc:rights>
               <dc:rights>Aquest document està subjecte a una llicència d'ús Creative Commons. Es permet la reproducció total o parcial, la distribució, i la comunicació pública de l'obra, sempre que no sigui amb finalitats comercials, i sempre que es reconegui l'autoria de l'obra original. No es permet la creació d'obres derivades.</dc:rights>
               <dc:rights>https://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
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