In the present work we studied the thermophilic biological treatability of high strength liquid wastes from a pharmaceutical industry (rich in organic matter e COD: Chemical Oxygen Demand, nutrients and salinity). Different mixtures (with concentrations of COD, phosphorus and chloride up to 57,000 mg L-1, 2000 mg L-1 and 9000 mg L-1, respectively) were tested. The pilot plant used in this work was designed and built with dimensions comparable to a semi-industrial unit. The results are therefore representative for full-scale applications. During four months of experimentation, the pilot plant (TAMR e Thermophilic Aerobic Membrane Reactor) was operated at 49 ± 1 C and the organic loading rate was 1.5-5.5 kgCOD m-3 d-1 with a hydraulic retention time of 5-10 days. Main results are the following: a) extremely high COD removal rate (up to 98%); b) very low sludge production (~0.016 kgVSS produced kgCOD removed-1 ); c) suitability as a pre-treatment to a conventional (e.g. activated sludge) biological treatment (the studied pharmaceutical industrial wastewaters are discharged into the sewer system for final polishing in a centralized municipal wastewater treatment plant) and d) high phosphorus removal (up to 99%).

Treatment of high strength pharmaceutical wastewaters in a Thermophilic Aerobic Membrane Reactor (TAMR)

COLLIVIGNARELLI, MARIA CRISTINA;ABBA', ALESSANDRO;BERTANZA, GIORGIO
2014-01-01

Abstract

In the present work we studied the thermophilic biological treatability of high strength liquid wastes from a pharmaceutical industry (rich in organic matter e COD: Chemical Oxygen Demand, nutrients and salinity). Different mixtures (with concentrations of COD, phosphorus and chloride up to 57,000 mg L-1, 2000 mg L-1 and 9000 mg L-1, respectively) were tested. The pilot plant used in this work was designed and built with dimensions comparable to a semi-industrial unit. The results are therefore representative for full-scale applications. During four months of experimentation, the pilot plant (TAMR e Thermophilic Aerobic Membrane Reactor) was operated at 49 ± 1 C and the organic loading rate was 1.5-5.5 kgCOD m-3 d-1 with a hydraulic retention time of 5-10 days. Main results are the following: a) extremely high COD removal rate (up to 98%); b) very low sludge production (~0.016 kgVSS produced kgCOD removed-1 ); c) suitability as a pre-treatment to a conventional (e.g. activated sludge) biological treatment (the studied pharmaceutical industrial wastewaters are discharged into the sewer system for final polishing in a centralized municipal wastewater treatment plant) and d) high phosphorus removal (up to 99%).
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11571/911434
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