Abstract
Phosphorus recovery was combined with ammonia recovery using gas-permeable membranes. In a first step, the ammonia and alkalinity were removed from municipal side-stream wastewater using low-rate aeration and a gas-permeable membrane manifold. In a second step, the phosphorus was removed using magnesium chloride (MgCl2) and reduced amounts of alkali. The side-stream wastewater contained 730 mg N/L, 140 mg P/L and 2900 mg/L alkalinity. The process recovered approximately 79–93% of the ammonia and 80–100% of the phosphorus. Surprisingly, the phosphates produced were very-high grade (42–44% P2O5) with a composition similar to the bio-mineral newberyite. However, lower grade phosphate products (27–29% P2O5) were produced whenever the N recovery step was bypassed or carbonate alkalinity was added. Therefore, removal of ammonia and alkalinity are important considerations for production of very-high grade phosphate product.
References
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Vanotti MB, Dube PJ, Szogi AA (2017) Recovery of ammonia and phosphate minerals from swine wastewater using gas-permeable membranes. Water Res. doi:10.1016/j.watres.2017.01.045
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Vanotti, M.B., Dube, P.J., Szogi, A.A. (2017). Recovery of Ammonia and Production of High-Grade Phosphates from Side-Stream Digester Effluents Using Gas-Permeable Membranes. In: Mannina, G. (eds) Frontiers in Wastewater Treatment and Modelling. FICWTM 2017. Lecture Notes in Civil Engineering , vol 4. Springer, Cham. https://doi.org/10.1007/978-3-319-58421-8_2
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DOI: https://doi.org/10.1007/978-3-319-58421-8_2
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