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RESEARCH PRODUCT

Implementation of a global P-recovery system in urban wastewater treatment plants

S. GrauDenis ManginA. BouzasRamón BaratL. PastorN. Martí

subject

Struvite020209 energyStrategy and Managementchemistry.chemical_elementSewage02 engineering and technologyElutriationIndustrial and Manufacturing Engineeringchemistry.chemical_compoundSludge line management0202 electrical engineering electronic engineering information engineering[SPI.GPROC]Engineering Sciences [physics]/Chemical and Process EngineeringGlobal phosphorus recoveryComputingMilieux_MISCELLANEOUSTECNOLOGIA DEL MEDIO AMBIENTEMixing chamber0505 lawGeneral Environmental ScienceResource recoveryRenewable Energy Sustainability and the Environmentbusiness.industryPhosphorus05 social sciencesCrystallisationPulp and paper industry6. Clean waterAnaerobic digestionchemistryStruvite050501 criminologyEnvironmental scienceSewage treatmentUrban WWTPbusiness

description

[EN] Current wastewater treatment plants (WWTPs) paradigm is moving towards the so-called water resource recovery facilities in which sewage is considered a source of valuable resources. In particular, urban WWTPs are crucial systems to enhance phosphorus (P) recycling. This paper evaluates the implementation of a P-recovery system in Calahorra WWTP combining the operation of a new sludge line configuration coupled to a struvite crystallisation reactor at demonstration-scale. This new configuration consisted in the elutriation in the gravity thickener of the mixed sludge contained in the mixing chamber in order to reduce the phosphate load to the anaerobic digestion. The results indicated that the P available in the primary sludge overflow was nearly five times more than the obtained for the conventional configuration (1.88 vs. 0.39 gP/kg sludge treated), and the uncontrolled P precipitation inside the anaerobic digester was reduced by 43%. Regarding the total P entering the WWTP, 19% of the total P could be recovered with the new configuration proposed in comparison with 9% in the previous conventional configuration. The average recovery efficiency in the crystallisation plant was 86.9 0.4%, yielding a struvite recovery of 8.0 +/- 0.6 kg/d (0.67 +/- 0.04 kg/m(3) fed to the crystalliser). The potential struvite production with the new configuration would be around 41 kg/d (15 t/y) crystallising the thickener supernatant which could be increased up to around 103 kg/d (38 t/y) treating all the P enriched streams (thickener supernatant and centrate streams). The paper demonstrates that WWTPs can contribute to reduce P scarcity, resulting in environmental and economic benefits. (C) 2019 Elsevier Ltd. All rights reserved.

https://doi.org/10.1016/j.jclepro.2019.04.126