초록 ▼

An apparatus for wastewater treatment, includes a calorie reducer first vessel having an inlet and an outlet, the outlet adapted to control the retention time of wastewater within the first vessel. A first recycle pump is connected to the first vessel to recycle wastewater from a bottom of the first

An apparatus for wastewater treatment, includes a calorie reducer first vessel having an inlet and an outlet, the outlet adapted to control the retention time of wastewater within the first vessel. A first recycle pump is connected to the first vessel to recycle wastewater from a bottom of the first vessel to a top of the first vessel through a recycle conduit, at a high velocity. The recycle conduit provides an air gap for drawing air into the first vessel. Bacteria within the calorie reducer vessel consume biodegradable food with a minimum number of bacteria while in the log growth phase. A second bio-reducer vessel is connected to the calorie reducer vessel. The bio-reducer holds a media supported above a bottom reservoir. A bio-reducer recycle pump recycles wastewater within the reservoir to be sprayed onto a top of the bio-reducer, to wash over the media. Further bio-reducers can be arranged downstream of the first bio-reducer. In the bio-reducers, protozoa attached to the media consume the bacteria which wash over the media.

대표청구항 ▼

[ The invention claimed is:] [1.] A method of treating wastewater, comprising the steps of:delivering wastewater into a first vessel;recycling wastewater held in said first vessel and delivering the recycled wastewater in a high velocity stream back into the first vessel, said high velocity stream s

[ The invention claimed is:] [1.] A method of treating wastewater, comprising the steps of:delivering wastewater into a first vessel;recycling wastewater held in said first vessel and delivering the recycled wastewater in a high velocity stream back into the first vessel, said high velocity stream sufficient to prevent flocculation within said first vessel;adding air to said high velocity stream of recycled wastewater delivered into said first vessel;holding wastewater in said first vessel for a preselected retention time substantially corresponding to an age of maximum waste consumption per bacteria. [12.] A method of treating wastewater comprising the steps of:delivering wastewater into a first vessel having a first reservoir, said wastewater substantially free of BOD derived from waste and containing bacteria;providing media inside said first vessel, said media having attached protozoa, said media held above a surface of the wastewater contained within said first reservoir; andrecycling wastewater from said first reservoir of said first vessel to an upper region of said first vessel and onto said media held therein in order for said protozoa to consume bacteria. The method of claim 12 comprising the further steps of:delivering wastewater from said first vessel into a second vessel, the second vessel having a second reservoir;providing media inside said second vessel, said media held above a surface of the wastewater held within said second reservoir; andrecycling wastewater from said second reservoir of said second vessel to an upper region of said second vessel and onto the media held therein. The method of claim 12 wherein said wastewater is retained in said first vessel between about 2 and 6 hours. The method of claim 14 wherein said wastewater is retained in said first vessel for about 4 hours. The method of claim 13 wherein said wastewater is retained in said first and second vessels between 2 and 6 hours. The method of claim 12 wherein said wastewater is recycled at a rate of at least 10 reservoir volumes per hour. The method of claim 1, wherein said step of holding the wastewater is further defined in that the preselected retention time is selected such that the bacterial mass is between 300 and 450 mg/liter. The method of claim 1, wherein said step of holding the wastewater is further defined in that the preselected retention time is selected such that the bacterial mass is between approximately 350 and 400 mg/liter.