초록 ▼

The present invention entails a process for treating wastewater utilizing a return activated sludge process. Primary sludge is separated from the wastewater stream and conveyed into a fermentation tank and held a sufficient time to permit hydrolysis of suspended solids so as to produce soluble subst

The present invention entails a process for treating wastewater utilizing a return activated sludge process. Primary sludge is separated from the wastewater stream and conveyed into a fermentation tank and held a sufficient time to permit hydrolysis of suspended solids so as to produce soluble substrates. Part of the soluble substrates are mixed with nutrified return activated sludge and held for a selected time period to form conditioned return activated sludge. Thereafter, the conditioned return activated sludge is mixed in an initial aerobic treatment zone with pretreated wastewater. Thereafter, the mixed conditioned return activated sludge and pretreatd wastewater is conveyed through a series of treatment zones, which includes at least one anoxic treatment zone, to which part of the soluble substrates are added, where nitrogen and other pollutants are removed from the wastewater.

대표청구항 ▼

A process for removing both phosphorus and nitrogen from wastewater comprising the steps of: (a) directing raw sewage into a primary treatment area and treating the same and in the process separating the raw sewage into settled sewage and raw sludge; (b) directing the settled sewage in and through a

A process for removing both phosphorus and nitrogen from wastewater comprising the steps of: (a) directing raw sewage into a primary treatment area and treating the same and in the process separating the raw sewage into settled sewage and raw sludge; (b) directing the settled sewage in and through a main stream secondary treatment area and particularly subjecting the settled sewage to a first aerobic treatment zone, followed by an anoxic treatment zone, after which the settled sewage is subjected to a second aerobic treatment zone; (c) passing the effluent from the main stream secondary treatment area to a settling zone and separating the secondary treatment effluent into purified wastewater and settled sludge; (d) returning the settled sludge to a sidestream sludge nutrification zone that lies outside of the main stream secondary treatment area; (e) directing the separated raw sludge from the primary treatment area to a sidestream fermenter and fermenting the raw sludge to produce a fermented supernatant that includes volatile fatty acids; (f) transferring fermenter supernatant from the fermenter and splitting the fermenter supernatant into at least two streams; (g) transferring one stream of the fermenter supernatant to the sidestream nutrification zone and mixing the fermenter supernatant with the settled sludge to form conditioned activated sludge and holding the conditioned activated sludge within the nutrification zone a selected time period; (h) conveying the conditioned activated sludge to the main treatment area and particularly to the first aerobic treatment zone that precedes the anoxic treatment zone and mixing the conditioned activated sludge with the settled sewage in the first aerobic treatment zone; (i) wherein the fermenter supernatant and the volatile fatty acids associated therewith form a favorable food source for phosphorus removing microorganisms that is consumed in the nutrification zone; and (j) transferring the other stream of the fermenter supernatant to the anoxic zone in the main stream and mixing the fermenter supernatant with the settled sewage to give rise to denitrification in the anoxic zone as the volatile fatty acids associated with the fermenter supernatant provides a favorable food source that is consumed by denitrifying microorganisms in the anoxic zone.