IP Library Granted Patent US 7,208,090
Granted Patent B2
US 7,208,090 · App. 10/745,446 · Granted Apr 24, 2007

Wastewater treatment control

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Quick Facts
Patent No.
US 7,208,090
App. No.
10/745,446
Granted
Apr 24, 2007
Kind
B2
Abstract

Wastewater treatment controls that maintain the ORP of a mixed liquor at a relatively stable value during a wastewater treatment process such as an aerated-anoxic wastewater treatment process. The wastewater treatment control may compare a setpoint value of ORP and a measured value of ORP of the mixed liquor, generate a control signal based at least in part on the comparison, and control a biological nutrient removal control parameter using the control signal. Values corresponding to the control signal may be acquired and utilized to adjust the setpoint value of ORP to maintain stable operating conditions of the wastewater treatment process.

Claims (65)

1. A wastewater treatment method comprising:

establishing a setpoint value of oxidation-reduction potential of a mixed liquor;

measuring a measured value of oxidation-reduction potential of the mixed liquor;

comparing the measured value of oxidation-reduction potential and the setpoint value of oxidation-reduction potential;

generating a control signal based at least in part on the step of comparing;

controlling a biological nutrient removal control parameter using the control signal;

acquiring at least one value corresponding to the control signal; and

adjusting the setpoint value of oxidation-reduction potential using the at least one value.

2. A method according to claim 1 , wherein the mixed liquor is formed by mixing wastewater and activated sludge, and further comprising treating the mixed liquor under at least one of an anoxic condition, an anaerobic condition, and a combination thereof.

3. A method according to claim 1 , wherein the wastewater treatment method comprises a continuous wastewater treatment process, and further comprising treating the mixed liquor under aerated-anoxic conditions.

4. A method according to claim 1 , wherein the step of comparing the measured value of oxidation-reduction potential and the setpoint value of oxidation-reduction potential comprises

using a control to compare the measured value of oxidation-reduction potential and the setpoint value of oxidation-reduction potential, and

using the control to generate an output corresponding to the comparison of the measured value of oxidation-reduction potential and the setpoint value of oxidation-reduction potential; and

wherein the step of acquiring at least one value corresponding to the control signal comprises acquiring at least one value corresponding to the output of the control.

5. A method according to claim 4 , wherein the step of using a control comprises using a proportional-integral-derivative control.

6. A method according to claim 1 , wherein the step of controlling a biological nutrient removal control parameter using the control signal comprises regulating a supply of oxygen in the mixed liquor using the control signal, and wherein the step of regulating a supply of oxygen comprises using the control signal to control operation of an aeration device, wherein the aeration device supplies oxygen to the mixed liquor, and wherein the step of acquiring at least one value corresponding to the control signal comprises acquiring at least one value corresponding to the operation of the aeration device.

7. A method according to claim 1 , wherein the step of adjusting the setpoint value of oxidation-reduction potential comprises adjusting the setpoint value of oxidation-reduction potential when [Q] values corresponding to the at least one value exceed a threshold value in a duration of time, [Q] being a value greater than or equal to one.

8. A method according to claim 1 , wherein the step of adjusting the setpoint value of oxidation-reduction potential comprises adjusting the setpoint value of oxidation-reduction potential when [R] values corresponding to the at least one value fail to exceed a threshold value in a duration of time, [R] being a value greater than or equal to one.

9. A method according to claim 1 , wherein the step of adjusting the setpoint value of oxidation-reduction potential comprises

raising the setpoint value of oxidation-reduction potential when [S] values corresponding to the at least one value exceed a first threshold value in a first duration of time, [S] being a value greater than or equal to one, and

lowering the setpoint value of oxidation-reduction potential when [T] values corresponding to the at least one value fail to exceed a second threshold value in a second duration of time, [T] being a value greater than or equal to one, and the second threshold value being less than the first threshold value.

10. A method according to claim 1 , wherein the step of adjusting the setpoint value of oxidation-reduction potential comprises

using a rolling average function to determine a rolling average value of [U] values corresponding to the at least one value, [U] being a value greater than or equal to one,

obtaining another value corresponding to the at least one value,

using the rolling average function to determine an updated rolling average value of [U] values corresponding to the at least one value where the value of [U] is equal to [U]+1,

determining an absolute difference value between the another value corresponding to the at least one value and the updated rolling average value,

repeating the steps of obtaining another value and determining an absolute difference value for other values corresponding to the at least one value;

adjusting the setpoint value of oxidation-reduction potential when [V] values corresponding to the determined absolute difference values exceed a first threshold value in a first duration of time, [V] being a value greater than or equal to one; and

adjusting the setpoint value of oxidation-reduction potential when [W] values corresponding to the absolute difference values exceed a second threshold value in a second duration of time, [W] being a value greater than or equal to one, and the second threshold value being less than the first threshold value.

11. A method according to claim 1 , wherein the step of controlling a biological nutrient removal control parameter using the control signal comprises at least one of

using the control signal to control a position of a valve, the valve controlling at least one of the flow of oxygen-carrying gas, the flow of a chemical, the flow of recycled activated sludge, the flow of wastewater, the flow of recycled mixed liquor, and a combination thereof,

using the control signal to control at least one of a rate at which oxygen-carrying gas is provided to an aeration device, the rate at which a chemical is provided to the mixed liquor, the rate at which recycled activated sludge is provided to a treatment tank of a wastewater treatment process, the rate at which wastewater is provided to a treatment tank of a wastewater treatment process, the rate at which recycled mixed liquor is provided to a treatment tank of a wastewater treatment process, and a combination thereof,

using the control signal to control a sequencing process of a plurality of valves that are associated with at least one of the flow of oxygen-carrying gas, the flow of a chemical, the flow of recycled activated sludge, the flow of wastewater, the flow of recycled mixed liquor, and a combination thereof,

using the control signal to control an immersion depth of an aeration device,

using the control signal to control a speed of a variable speed motor, the motor driving a device configured to regulate a biological nutrient removal control parameter,

using the control signal to control a staging process of a plurality of devices configured to regulate a biological nutrient removal control parameter,

using the control signal to control an on/off cycle of a device configured to regulate a biological nutrient removal control parameter,

using the control signal to control an actuator utilized to position a liquid level weir, and

a combination thereof.

12. A method according to claim 1 , further comprising

reducing a concentration of organic compounds in an effluent obtained the mixed liquor;

reducing a concentration of nitrogen compounds in an effluent obtained from the mixed liquor; and

reducing a concentration of phosphorous compounds in an effluent obtained from the mixed liquor.

13. A method according to claim 1 , wherein the step of controlling a biological nutrient removal control parameter comprises supplying oxygen to the mixed liquor at a rate that is less than or equal to a biological oxygen demand of the mixed liquor such that a dissolved oxygen concentration of the mixed liquor is less than approximately 1.0 mg/L.

14. A wastewater treatment method comprising:

establishing a setpoint value of oxidation-reduction potential of a mixed liquor;

determining a variation of a measured value of oxidation-reduction potential of the mixed liquor from the setpoint value of oxidation-reduction potential;

controlling a device based at least in part on the determined variation, the device regulating a biological nutrient removal control parameter; and

using data corresponding to the step of controlling a device to adjust the setpoint value of oxidation-reduction potential so at least one operating characteristic of the device is maintained substantially within an established range of variation.

15. A method according to claim 14 , wherein the step of controlling a device comprises controlling an aeration device, and wherein the biological nutrient removal control parameter includes a supply of oxygen in the mixed liquor.

16. A method according to claim 14 , wherein the step of controlling a device comprises controlling a liquid level weir.

17. A method according to claim 14 , wherein the step of controlling a device comprises controlling a valve, and wherein the biological nutrient removal control parameter includes at least one of a supply of oxygen in the mixed liquor, a supply of chemicals to the mixed liquor, a recycle rate of activated sludge, a recycle rate of mixed liquor, a supply of wastewater to the mixed liquor, and combinations thereof.

18. A method according to claim 14 , wherein the established range of variation results in a substantially constant measured value of oxidation-reduction potential of the mixed liquor.

19. A wastewater treatment method comprising:

mixing wastewater and activated sludge to form a mixed liquor;

treating the mixed liquor under aerated-anoxic conditions;

establishing a setpoint value of oxidation-reduction potential;

using an oxidation-reduction potential sensor to measure a measured value of oxidation-reduction potential of the mixed liquor;

using a control to compare the measured value of oxidation-reduction potential and the setpoint value of oxidation-reduction potential, the control generating an output corresponding to the comparison of the measured value of oxidation-reduction potential and the setpoint value of oxidation-reduction potential;

using the output to generate a control signal;

using the control signal to control operation of an oxygen supply device, the oxygen supply device regulating a supply of oxygen in the mixed liquor;

acquiring at least one value corresponding to at least one of the output, the control signal, and the operation of the oxygen supply device;

adjusting the setpoint value of oxidation-reduction potential when [X] values corresponding to the at least one value exceed a first threshold value in a first duration of time, [X] being a value greater than or equal to one; and

adjusting the setpoint value of oxidation-reduction potential when [Y] values corresponding to the at least one value fail to exceed a second predetermined threshold in a second duration of time, [Y] being a value greater than or equal to one, and the second threshold value being less than the first threshold value.

20. A method according to claim 19 , wherein the step of using the control signal to control operation of an oxygen supply device comprises using the control signal to control operation of at least one of an aeration device, a liquid level weir, a valve, and a combination thereof, wherein the aeration device is configured to supply oxygen-carrying gas to the mixed liquor, wherein the liquid level weir is configure to control a liquid level of the mixed liquor, and wherein the valve is configured to regulate the flow of at least one of the wastewater and the activated sludge into a tank for mixing.

Assignments (15)
RELEASE OF SECURITY INTEREST Recorded May 26, 2023
From: JPMORGAN CHASE BANK N.A., AS COLLATERAL AGENT
To: EVOQUA WATER TECHNOLOGIES LLC; NEPTUNE BENSON, INC.
Reel/Frame 063787/0943 →
SECURITY INTEREST Recorded Apr 7, 2021
From: EVOQUA WATER TECHNOLOGIES LLC; NEPTUNE BENSON, INC.
To: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT
Reel/Frame 055848/0689 →
RELEASE OF SECURITY INTEREST (REEL/FRAME 032126/0487) Recorded Apr 6, 2021
From: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 055845/0245 →
RELEASE OF SECURITY INTEREST (REEL/FRAME 032126/0430) Recorded Apr 6, 2021
From: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 055845/0311 →
CHANGE OF NAME Recorded Feb 7, 2014
From: SIEMENS WATER TECHNOLOGIES LLC
To: EVOQUA WATER TECHNOLOGIES LLC
Reel/Frame 032174/0282 →
INTELLECTUAL PROPERTY SECURITY AGREEMENT (FIRST LIEN) Recorded Jan 24, 2014
From: WTG HOLDINGS III CORP.; WTG HOLDINGS II CORP.; SIEMENS TREATED WATER OUTSOURCING CORP.; SIEMENS WATER TECHNOLOGIES LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
Reel/Frame 032126/0487 →
INTELLECTUAL PROPERTY SECURITY AGREEMENT (SECOND LIEN) Recorded Jan 24, 2014
From: WTG HOLDINGS III CORP.; WTG HOLDINGS II CORP.; SIEMENS TREATED WATER OUTSOURCING CORP.; SIEMENS WATER TECHNOLOGIES LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
Reel/Frame 032126/0430 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 1, 2014
From: SIEMENS INDUSTRY, INC.
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 031896/0256 →
MERGER Recorded Apr 15, 2011
From: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
To: SIEMENS INDUSTRY, INC.
Reel/Frame 026138/0593 →
MERGER Recorded Apr 11, 2011
From: SIEMENS WATER TECHNOLOGIES CORP.
To: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
Reel/Frame 026106/0467 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNMENT SHOULD BE DISREGARDED, FILED IN ERROR. THE PATENT REMAINS IN THE NAME OF SIEMENS WATER TECHNOLOGIES HOLDING CORP. PREVIOUSLY RECORDED ON REEL 018772 FRAME 0508. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Feb 5, 2007
From: SIEMENS WATER TECHNOLOGIES CORP.
To: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
Reel/Frame 018853/0670 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 18, 2007
From: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
To: SIEMENS WATER TECHNOLOGIES CORP.
Reel/Frame 018772/0508 →
CHANGE OF NAME Recorded Jan 18, 2007
From: USFILTER CORPORATION
To: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
Reel/Frame 018782/0534 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 30, 2004
From: UNITED STATES FILTER CORPORATION
To: USFILTER CORPORATION
Reel/Frame 015204/0036 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 23, 2003
From: APPLEGATE, CHARLES STARK; DUBEY, DAVID W.
To: UNITED STATES FILTER CORPORATION
Reel/Frame 014853/0774 →