| 摘要 |
FIELD: sewage treatment facilities. ^ SUBSTANCE: invention is related to the field of biological purification of sewage from organic compounds, nitrogen and phosphorus. To realise the method, the following hydraulically communicated stages - anaerobic, anoxic, aerobic - are performed for treatment with activated sludge with membrane separation, stage of deaeration that precedes stage of anaerobic treatment, stage of powdered activated carbon (PAC) treatment with membrane separation. Method also includes recirculation of sludge mixture from the aerobic treatment stage to stage of deaeration and recirculation of sludge mixture from anoxic stage to anaerobic stage. Purified water after serial anaerobic stage at load on activated sludge by "" of 2.0-4.0 mg/ghr and anoxic stage at load on activated sludge by nitrogen of 3.5-4.5 mg/ghr, "" of 8-13 mg/ghr is supplied directly to the stage of aerobic treatment with membrane separation. At that load on activated sludge by nitrogen makes 0.8-1.2 mg/g-hr, by oil products - 0.5-0.7 mg/ghr, according to synthetic surfactants - 0.16-0.22 mg/ghr and by phenols - 0.18-0.25 mg/ghr. At the stage of anoxic treatment 80-90% of recirculated sludge mixture is supplied from deaeration stage. Water purification with PAC is carried out at concentration of dissolved oxygen to 4.0 mg/l due to supply of compressed air and PAC concentration of 20-30 g/l at its single charging. At that load on PAC by oil products makes 0.35-0.45 mg/ghr, by synthetic surfactants - 0.06-0.07 mg/ghr and by phenols - 0.02-0.024 mg/ghr. ^ EFFECT: method provides for increased degree of purification from nitrogen and phosphorus, wider range of removed organic compounds, process simplification and reduction of its duration. ^ 2 tbl, 3 ex |
