# US 5,344,563 A · Wastewater treatment system

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 5,344,563 A
- Document ID: US5344563A
- Status: Granted
- Kind: A
- Application number: 08/068,206
- Filed: 1993-06-01
- Granted: 1994-09-06
- Earliest claimed: 1993-06-01
- Inventors: Daniel G. Noyes
- Web page: https://patentgrep.com/patent/US5344563A

## CPC

- C02F 3/1247: {comprising circular tanks with elements, e.g. decanters, aeration basins, in the form of segments, crowns or sectors}
- C02F 3/1294: {"Venturi" aeration means}
- Y02A 20/208: Off-grid powered water treatment
- Y02W 10/10: Biological treatment of water, waste water, or sewage
- C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes)
- Y02A: TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT

## Abstract

A wastewater treatment system and method is disclosed, including a circular aeration basin and a contiguous annular clarifier channel. Rotational flow of an aerated mixture of untreated wastewater and return sludge is induced in the aeration basin at its periphery with relatively less turbulent flow at the center. A clarifier inlet is fluidly connected to the aeration basin through openings provided in the aeration basin wall, the clarifier inlet including means to dissipate turbulence. A sludge removal manifold extends within the clarifier having valve-controlled suction arms. The spaced suction arms provide for precise control of sludge blanket depth and sludge age independent of rate of sludge return to the basin. Process sludge withdrawn from the clarifier is mixed with raw wastewater and returned to the aeration basin. The relatively less-turbulent flow in the central area of the basin allows process sludge to accumulate in said central area. A drain provided centrally in the aeration basin allows for draw-off of such digested sludge.

## Claims

### Claim 1

A wastewater treatment system comprising in combination:
an aeration basin;
a pump having a pump inlet and a pump outlet;
at least one mixed liquor inlet disposed in said basin near the periphery of said basin, said mixed liquor inlet having a discharge outlet oriented tangentially to the periphery of said basin;
said pump outlet in fluid communication with said mixed liquor inlet for inducing flow of wastewater through said mixed liquor inlet;
an air inlet in fluid communication with said mixed liquor inlet;
a mixed liquor outlet provided in said basin, said mixed liquor outlet in fluid communication with said pump inlet;
an untreated wastewater inlet in fluid communication with said pump inlet;
said pump providing means for inducing continuous circulation of mixed liquor through said mixed liquor inlet, said aeration basin and said mixed liquor outlet;
said mixed liquor inlet providing means for inducing turbulent, rotational flow of aerated mixed liquor in a first area near the periphery of said basin and less-turbulent flow in a second area central of said basin whereby wastewater organic solids accumulate in said second area; and
an organic solids outlet in the floor of said basin at said second area.

### Claim 2 (depends on 1)

A wastewater treatment system according to claim 1 wherein
said mixed liquor inlet includes an inlet pipe in fluid connection with said pump outlet;
said inlet pipe including a reduced-diameter nozzle;
said air inlet in fluid communication with said mixed liquor inlet downstream of said reduced-diameter nozzle;
whereby velocity of flow through said reduced-diameter nozzle induces reduced pressure downstream of said reduced-diameter nozzle results in induction of air into said mixed liquor inlet and turbulent mixing of said air with said mixed liquor.

### Claim 3 (depends on 2)

A wastewater treatment system according to claim 2 wherein
said mixed liquor inlet including a housing external of said inlet pipe said housing including a discharge aperture, said discharge aperture oriented tangentially to the periphery of said basin.

### Claim 4 (depends on 1)

A wastewater treatment system according to claim 1 wherein
a plurality of mixed liquor inlets are provided in spaced relationship around the periphery of said basin;
the discharge apertures of said mixed liquor inlets oriented in like angular direction;
said mixed liquor inlets providing means for producing consistently turbulent, rotational flow in said first area.

### Claim 5 (depends on 1)

A wastewater treatment system according to claim 1 further comprising
a mixing chamber in fluid communication with said mixed liquor outlet and in fluid communication with said untreated wastewater inlet;
a flow control valve provided on said mixed liquor outlet;
whereby relative composition of untreated wastewater and previously-aerated wastewater in the mixed liquor may be adjusted.

### Claim 6 (depends on 1)

A wastewater treatment system according to claim 1 wherein said aeration basin is generally circular.

### Claim 7

A wastewater treatment system comprising in combination:
an aeration basin for receiving a mixed liquor of previously-aerated wastewater and untreated wastewater;
a clarifier;
a pump having a pump inlet and a pump outlet;
at least one mixed liquor inlet disposed in said basin oriented tangentially to the periphery of the basin;
said pump outlet in fluid communication with said mixed liquor inlet for inducing flow of mixed liquor through said mixed liquor inlet;
said pump and said mixed liquor inlet providing means for inducing turbulent, rotational flow of mixed liquor in a first area of said basin and less-turbulent mixed liquor flow in a second area central of said basin whereby aerated suspended organic solids settle in said second area;
an organic solids outlet located in said second area;
an untreated wastewater inlet in fluid communication with said pump inlet;
said clarifier comprising a channel in fluid communication with said aeration basin at a first end of said clarifier channel;
a clarified liquor outlet at a second end of said channel;
means establishing fluid communication between said pump inlet and mixed liquor contained in said clarifier channel;
whereby said pump induces continuous circulation of mixed liquor through said aeration basin and said clarifier channel.

### Claim 8 (depends on 7)

A wastewater treatment system according to claim 7 wherein
said mixed liquor inlet includes an inlet pipe in fluid connection with said pump outlet;
said inlet pipe including a reduced-diameter nozzle;
said air inlet in fluid communication with said mixed liquor inlet downstream of said reduced-diameter nozzle;
whereby velocity of flow through said reduced-diameter nozzle induces reduced pressure downstream of said reduced-diameter nozzle resulting in induction of air into said mixed liquor inlet and turbulent mixing of said air with said mixed liquor; and
said mixed liquor inlet including a housing external of said inlet pipe said housing having a discharge aperture, said discharge aperture oriented tangentially to the periphery of said basin.

### Claim 9 (depends on 8)

A wastewater treatment system according to claim 8 wherein
a plurality of mixed liquor inlets are provided in spaced relationship around the periphery of the basin;
the discharge apertures of said inlets oriented in like angular direction;
said mixed liquor inlets providing means for producing consistently turbulent, rotational flow in said first area.

### Claim 10 (depends on 7)

A wastewater treatment system according to claim 7 wherein
said clarifier channel is contiguous with the periphery of the aeration basin.

### Claim 11 (depends on 10)

A wastewater treatment system according to claim 10 wherein
said aeration basin is generally circular.

### Claim 12 (depends on 7)

A wastewater treatment system according to claim 7 wherein said clarifier includes:
a sludge header disposed along the length of the channel;
a plurality of spaced sludge suction arms in fluid communication with said sludge header;
each of said sludge suction arms near the bottom of said channel;
said sludge header in fluid communication with suction means;
whereby mixed liquor is introduced into said channel at said first end, settled organic solids are removed from said clarifier channel through said suction arms and said suction header, and clarified liquor is removed from said channel through said clarified liquor outlet.

### Claim 13 (depends on 12)

A wastewater treatment system according to claim 12 wherein
a valve is provided on each suction arm controlling flow through the suction arm to the sludge header.

### Claim 14 (depends on 7)

A wastewater treatment system according to claim 7 wherein
fluid communication between said aeration basin and said clarifier channel first end is accomplished by at least one pipe, said pipe having a first end disposed in said aeration basin; said pipe having a pipe segment extending into said clarifier channel; said pipe having a second end disposed in said clarifier channel; said pipe being open at its first end and at its second end, and said pipe segment having a laterally-extending slot.

### Claim 15 (depends on 14)

A wastewater treatment system according to claim 14 wherein
a plurality of pipes are provided.

### Claim 16 (depends on 7)

A wastewater treatment system according to claim 7 wherein scum baffle means are provided in the clarifier channel, said scum baffle means including a baffle extending transversely across said channel, said scum baffle diverting surface scum to an opening in a channel wall, said channel wall opening in fluid communication with said aeration basin whereby surface scum is diverted from the clarifier channel to the aeration basin.

### Claim 17

A method for treatment of wastewater to reduce organic solids contents, reduce biological oxygen demand and separate clarified liquid from sludge, said method comprising the steps of:
mixing wastewater to be treated with previously-aerated wastewater to create a mixed liquor, said previously-aerated wastewater containing organic solids including bacteria, protozoa and other microorganisms;
aerating said mixed liquor;
inducing turbulent flow of said aerated mixed liquor in a first peripheral area of a basin;
providing an area of reduced turbulence of flow in a second central area of said basin to allow settling of organic solids from the aerated mixed liquor;
intermittently removing accumulated organic solids from said second area;
segregating a first flow of aerated mixed liquor;
inducing laminar flow of said first flow in a channel to allow settling of organic solids from said first flow;
removing settled organic solids from said channel; and
utilizing said removed organic solids for mixing with said wastewater to be treated; and
removing clarified liquor from said channel.

### Claim 18 (depends on 17)

The method according to claim 17 wherein
said mixing of wastewater to be treated with previously-aerated wastewater includes pumping the wastewater to be treated and the previously-treated wastewater through a common header.

### Claim 19 (depends on 17)

The method according to claim 17 wherein
aerating said mixed liquor includes inducing mixed liquor flow through at least one reduced-diameter nozzle and providing fluid communication of air with the mixed liquor at the nozzle outlet.

### Claim 20 (depends on 17)

The method according to claim 17 wherein
inducing turbulent flow of said aerated mixed liquor in a basin includes inducing flow of said aerated mixed liquor through at least one reduced-diameter nozzle.

### Claim 21 (depends on 17)

The method according to claim 17 wherein
said basin is generally circular.

### Claim 22 (depends on 17)

The method of claim 17 further comprising the steps of:
introducing said first flow into a first end of said channel;
removing settled organic solids from at least one of a plurality of locations along said channel;
removing said clarified liquor from a second distal end of said channel;
whereby said settled organic solids may be removed from said channel independently of flow quantity of aerated mixed liquor.

### Claim 23 (depends on 17)

The method of claim 17 further comprising the steps of:
introducing said first flow into a first end of said channel;
removing settled organic solids from at least one of a plurality of locations along said channel;
removing said clarified liquor from a second distal end of said channel;
whereby settled organic solids may be removed from said channel from a plurality of locations.

### Claim 24 (depends on 17)

The method of claim 17 further comprising the step of:
providing continuous fluid communication between said basin and said channel and inducing fluid flow between said basin and said channel with a single pump.
