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1.
Environ Technol ; 36(9-12): 1398-404, 2015.
Artículo en Inglés | MEDLINE | ID: mdl-25420588

RESUMEN

Phosphorus was recovered from dairy manure via a microwave-enhanced advanced oxidation process (MW/H2O2-AOP) followed by struvite crystallization in a pilot-scale continuous flow operation. Soluble phosphorus in dairy manure increased by over 50% after the MW/H2O2-AOP, and the settleability of suspended solids was greatly improved. More than 50% of clear supernatant was obtained after microwave treatment, and the maximum volume of supernatant was obtained at a hydrogen peroxide dosage of 0.3% and pH 3.5. By adding oxalic acid into the supernatant, about 90% of calcium was removed, while more than 90% of magnesium was retained. As a result, the resulting solution was well suited for struvite crystallization. Nearly 95% of phosphorus in the treated supernatant was removed and recovered as struvite.


Asunto(s)
Estiércol , Fósforo/aislamiento & purificación , Calcio/aislamiento & purificación , Industria Lechera , Peróxido de Hidrógeno/química , Compuestos de Magnesio/química , Microondas , Oxidación-Reducción , Fosfatos/química , Proyectos Piloto , Estruvita
2.
Artículo en Inglés | MEDLINE | ID: mdl-18444078

RESUMEN

In this study, the workability of a pilot-scale, fluidized reactor was examined to determine effectiveness in removing, and recovering, phosphorus as struvite, from centrate at Lulu Island Wastewater Treatment Plant (LIWWTP), Richmond, British Columbia. The crystallization process was run continuously over a period of 5 months in two runs (Run 1 for 4 months and Run 2 for a month). In addition to efficient recovery of phosphorus as struvite, the study also investigated factors that affect the growth of struvite. Chemical analyses were conducted on the harvested struvite to determine its purity. Results showed that the reactor was capable of removing over 90% of phosphate and 4% of ammonia-nitrogen, with greater than 85% of the phosphate removed being recovered as harvestable struvite crystals. It was possible to achieve over 90% P-removal at a pH of 7.5; this is contrary to the information found in literature, which recommends that a higher pH (8.2-9.0) is required. Factors that affected phosphate removal were the operating pH, the reactor supersaturation ratio (SSR), the N:P and Mg:P molar ratios. Analysis of the harvested product showed that the crystals were composed of nearly pure struvite (96% by weight), with small amounts of calcium and traces of other metals. High resolution SEM pictures were taken of the inside of the crystals to determine the influence of Mg:P molar ratio on the compactness of the crystals.


Asunto(s)
Compuestos de Magnesio/aislamiento & purificación , Fosfatos/aislamiento & purificación , Fósforo/aislamiento & purificación , Eliminación de Residuos Líquidos/métodos , Cristalización , Estudios de Factibilidad , Filtración/métodos , Concentración de Iones de Hidrógeno , Compuestos de Magnesio/química , Fosfatos/química , Fósforo/química , Estruvita , Eliminación de Residuos Líquidos/instrumentación
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