Subcyclonic jet recirculation grit removal system

Claim 1

Apparatus for removing grit from a wastewater stream such as municipal sewage while maintaining the wastewater in an aerobic condition, comprising a subcyclonic sedimentation tank which is substantially radially symmetrical about a central axis and having a lower sediment accumulation surface projecting inward from the outer tank wall toward the central axis, a lower sediment accumulation tank beneath and in axial alignment with the sedimentation tank and in fluid communication therewith along the central vertical axis, inlet means for tangentially introducing the wastewater inlet stream to be degritted into the subcyclonic sedimentation tank at its periphery, outlet means for discharging a degritted wastewater stream, air lift pump means for withdrawing a portion of the wastewater from said sedimentation tank adjacent said sediment accumulation surface at the central vertical axis at a rate of at least about 0.02 of the volume of the wastewater in the sedimentation tank per minute, for introducing into the withdrawn stream at least about 0.1 standard cubic feet of air per gallon of said withdrawn stream for aeration of said withdrawn stream, and for lifting said withdrawn stream within an enclosed conduit under turbulent conditions to an elevation of at least about one foot above the surface of the wastewater in the sedimentation tank to provide an aerated, turbulently mixed recirculation stream, said air lift pump means comprising an airlift conduit having an intake opening adjacent said sediment accumulation surface, and an air-liquid separation chamber in fluid communication with said airlift conduit above the surface of wastewater in said subcyclonic sedimentation tank for separating said air from said withdrawn stream to provide said aerated recirculation stream, and discharge means for discharging said aerated turbulently mixed recirculation stream at a velocity of at least about 5 feet per second into the wastewater in the sedimentation tank in the direction of the tangential wastewater influent flow, at one or more locations radially displaced from the central axis.

Claim 4

A method for removing grit from a wastewater stream while maintaining the wastewater in an aerobic condition, comprising the steps of introducing the wastewater stream tangentially into an upper separation treatment zone which is substantially radially symmetrical about a central vertical axis and having a lower grit accumulation surface projecting inward toward the central axis, and communicating at the center thereof with a lower sediment accumulation zone at a central vertical axis, withdrawing wastewater containing suspended organic solids from the separation treatment zone adjacent the grit accumulation surface at a location generally adjacent the central vertical axis at a rate of at least about 0.02 of the volume of the wastewater in the separation treatment zone per minute to provide a recirculation wastewater stream, aerating the withdrawn wastewater recirculation stream by introducing into the withdrawn wastewater recirculation stream at least about 0.1 standard cubic feet of air per gallon of the recirculation stream, collecting grit in the lower sediment accumulation zone, lifting the recirculation stream under turbulent aeration conditions in a confined conduit zone to an elevation of at least about one foot above the surface of the wastewater in the separation treatment zone, separating at least a portion of the introduced air from the recirculation stream at an elevation above the surface of the wastewater to provide an aerated recirculation stream, conducting said aerated recirculation stream beneath the surface of the wastewater in the separation treatment zone to provide an aerated, pressurized recirculation stream, and discharging a degritted wastewater stream containing suspended organic solids from said upper separation treatment zone, discharging said aerated, pressurized recirculation stream as at least one jet into the wastewater in the separation zone at one or more locations radially displaced from the central axis in the direction of the tangential wastewater influent flow and beneath the surface of the wastewater in said upper separation treatment zone at a discharge velocity of at least about 5 feet per second.

Claim 5

A method for removing grit from a wastewater stream while maintaining the wastewater in an aerobic condition, comprising the steps of introducing the wastewater stream tangentially into an upper separation treatment zone which is substantially radially symmetrical about a central vertical axis and having a lower grit accumulation surface projecting inward toward the central axis, and communicating at the center thereof with a lower sediment accumulation zone at a central vertical axis, withdrawing wastewater containing suspended organic solids from the separation treatment zone adjacent the grit accumulation surface at a location generally adjacent the central vertical axis at a rate of at least about 0.02 of the volume of the wastewater in the separation treatment zone per minute to provide a recirculation wastewater stream, aerating the withdrawn wastewater recirculation stream by introducing into the withdrawn wastewater recirculation stream at least about 0.1 standard cubic feet of air per gallon of the recirculation stream, collecting grit in the lower sediment accumulation zone, lifting the recirculation stream under turbulent aeration conditions in a confined conduit zone to an elevation of at least about one foot above the surface of the wastewater in the separation treatment zone, separating at least a portion of the introduced air from the recirculation stream at an elevation above the surface of the wastewater to provide an aerated recirculation stream, conducting said aerated recirculation stream beneath the surface of the wastewater in the separation treatment zone to provide an aerated, pressurized recirculation stream, and discharging a degritted wastewater stream containing suspended organic solids from said upper separation treatment zone, discharging said aerated, pressurized recirculation stream as at least one jet into the wastewater in the separation zone at one or more locations radially displaced from the central axis in the direction of the tangential wastewater influent flow and beneath the surface of the wastewater in said upper separation treatment zone at a discharge velocity of at least about 5 feet per second.