CA2664679A1 - System and method for eliminating sludge via ozonation - Google Patents
System and method for eliminating sludge via ozonation Download PDFInfo
- Publication number
- CA2664679A1 CA2664679A1 CA 2664679 CA2664679A CA2664679A1 CA 2664679 A1 CA2664679 A1 CA 2664679A1 CA 2664679 CA2664679 CA 2664679 CA 2664679 A CA2664679 A CA 2664679A CA 2664679 A1 CA2664679 A1 CA 2664679A1
- Authority
- CA
- Canada
- Prior art keywords
- ozone
- activated sludge
- liquid stream
- ozonation reactor
- biosolids
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/006—Regulation methods for biological treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1205—Particular type of activated sludge processes
- C02F3/1221—Particular type of activated sludge processes comprising treatment of the recirculated sludge
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
- C02F3/1273—Submerged membrane bioreactors
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/06—Treatment of sludge; Devices therefor by oxidation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
A system and method for the treatment and reduction of sludge via ozonation in a wastewater treatment process is disclosed. The sludge treatment system (10) comprises: a sludge ozonation reactor (30) coupled to an activated sludge treatment basin (20) and adapted to receive a liquid stream of sludge containing biosolids from the activated sludge treatment basin (20). The sludge treatment system (10) also includes an ozone-enriched gas injection system (40) operatively coupled to the reactor and adapted to inject ozone-enriched gas into the liquid stream at or upstream of the sludge ozonation reactor (30). The sludge ozonation reactor (30) is configured to allow effective gas-liquid contacting between the ozone-enriched gas and the liquid stream so as to oxidize the biosolids in the liquid stream and initiate bacterial cell lysis thereby reducing the biosolids. Upon reduction of the biosolids, the liquid stream is returned via a return line (50) to the activated sludge basin (20) or other discharge point (23).
Claims (19)
1. A sludge treatment system comprising:
a plug-flow type ozonation reactor fluidically coupled to an activated sludge treatment basin and adapted to receive a liquid stream containing biosolids from the activated sludge treatment basin;
a source of ozone-enriched gas;
a gas injection system coupled to the source of ozone-enriched gas and adapted to inject ozone-enriched gas into the liquid stream in the ozonation reactor;
the ozonation reactor adapted to facilitate lysis of the biosolids and reduction of sludge; and a return conduit coupled to the ozonation reactor for transporting the ozonated liquid stream to the activated sludge treatment basin.
a plug-flow type ozonation reactor fluidically coupled to an activated sludge treatment basin and adapted to receive a liquid stream containing biosolids from the activated sludge treatment basin;
a source of ozone-enriched gas;
a gas injection system coupled to the source of ozone-enriched gas and adapted to inject ozone-enriched gas into the liquid stream in the ozonation reactor;
the ozonation reactor adapted to facilitate lysis of the biosolids and reduction of sludge; and a return conduit coupled to the ozonation reactor for transporting the ozonated liquid stream to the activated sludge treatment basin.
2. The activated sludge treatment system of claim 1 wherein the source of ozone-enriched gas further comprises an ozone generator coupled to a source of oxygen and the ozone enriched gas is an ozone enriched oxygen gas.
3. The activated sludge treatment system of claim 1 wherein the source of ozone-enriched gas further comprises an ozone generator coupled to a source of ambient air and the ozone enriched gas is ozone enriched air.
4. The activated sludge treatment system of claim 1 wherein the source of ozone-enriched gas further comprises an ozone generator coupled to a source of oxygen enriched air and the ozone enriched gas is an ozone enriched air-oxygen mixture.
5. The activated sludge treatment system of claim 1 wherein the gas injection system further comprises one or more nozzles disposed in the ozonation reactor.
6. The activated sludge treatment system of claim 1 wherein the gas injection system gas further comprises a venturi device disposed in the ozonation reactor.
7. The activated sludge treatment system of claim 1 wherein the gas injection system gas further comprises a plurality of injecting devices disposed proximate the ozonation reactor.
8. The activated sludge treatment system of claim 1 wherein the sludge treatment system further includes a return activated sludge (RAS) line adapted to recycle activated sludge to the activated sludge basin and the ozonation reactor is coupled to the RAS line.
9. The activated sludge treatment system of claim 1 further comprising a pre-treatment subsystem interposed between the activated sludge basin and the ozonation reactor, the sludge pre-treatment subsystem adapted for conditioning the liquid stream to optimize the lysis of the biosolids in the ozonation reactor.
10. The activated sludge treatment system of claim 1 wherein the liquid stream is a mixed liquor stream.
11. The activated sludge treatment system of claim 1 wherein the liquid stream is a stream of sludge.
12. A method of sludge reduction comprising the steps of:
treating wastewater in an activated sludge basin;
diverting a liquid stream containing biosolids from the activated sludge basin to a high selectivity ozonation reactor;
introducing an ozone-enriched gas to the liquid stream at or upstream of the ozonation reactor to induce lysis of the biosolids through the interaction of the biosolids with ozone within the ozonation reactor; and discharging the ozonated liquid stream containing by-products resulting from the lysis to a bioreactor for further bio-oxidation of said by-products.
treating wastewater in an activated sludge basin;
diverting a liquid stream containing biosolids from the activated sludge basin to a high selectivity ozonation reactor;
introducing an ozone-enriched gas to the liquid stream at or upstream of the ozonation reactor to induce lysis of the biosolids through the interaction of the biosolids with ozone within the ozonation reactor; and discharging the ozonated liquid stream containing by-products resulting from the lysis to a bioreactor for further bio-oxidation of said by-products.
13. The method of sludge reduction according to claim 12 further comprising the step of producing an ozone-enriched gas by generating ozone and mixing the ozone with a gas, and wherein the percent of ozone is between 6 and percent by volume.
14. The method of sludge reduction according to claim 12 further comprising the step of producing an ozone-enriched gas by generating ozone and mixing the ozone with a mixture of oxygen and ambient air, and wherein the percent of ozone is between 6 and 15 percent by volume.
15. The method of sludge reduction according to claim 12 further comprising the step pre-treating the liquid stream containing biosolids.
16 The method of sludge reduction according to claim 12 wherein the step of introducing an ozone-enriched gas to the ozonation reactor further comprises injecting ozone-enriched gas at a plurality of locations within the ozonation reactor.
17. The method of sludge reduction according to claim 12 wherein the step of discharging the ozonated liquid stream further comprises discharging the ozonated liquid stream back to the activated sludge basin.
18. The method of sludge reduction according to claim 12 wherein the ozonation reactor is a plug flow reactor.
19 19. A method of reducing biosolids in a wastewater treatment process comprising the steps of:
directing a liquid stream containing biosolids within a wastewater treatment process to a high selectivity ozonation reactor; and introducing an ozone-enriched gas to the liquid stream at or upstream of the ozonation reactor to induce lysis of the biosolids through the interaction of the biosolids with ozone within the ozonation reactor; and discharging the ozonated liquid stream containing by-products resulting from the induced lysis to a bioreactor for further bio-oxidation of the by-products;
wherein the ratio of biosolids reduced in kilograms to ozone usage in kilograms is equal to or greater than 10.
directing a liquid stream containing biosolids within a wastewater treatment process to a high selectivity ozonation reactor; and introducing an ozone-enriched gas to the liquid stream at or upstream of the ozonation reactor to induce lysis of the biosolids through the interaction of the biosolids with ozone within the ozonation reactor; and discharging the ozonated liquid stream containing by-products resulting from the induced lysis to a bioreactor for further bio-oxidation of the by-products;
wherein the ratio of biosolids reduced in kilograms to ozone usage in kilograms is equal to or greater than 10.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/541,100 US7309432B1 (en) | 2006-09-29 | 2006-09-29 | System and method for eliminating sludge via ozonation |
| US11/541,100 | 2006-09-29 | ||
| PCT/US2007/079842 WO2008042751A1 (en) | 2006-09-29 | 2007-09-28 | System and method for eliminating sludge via ozonation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2664679A1 true CA2664679A1 (en) | 2008-04-10 |
| CA2664679C CA2664679C (en) | 2012-06-26 |
Family
ID=38887010
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA 2664679 Expired - Fee Related CA2664679C (en) | 2006-09-29 | 2007-09-28 | System and method for eliminating sludge via ozonation |
Country Status (12)
| Country | Link |
|---|---|
| US (2) | US7309432B1 (en) |
| EP (1) | EP1905743B1 (en) |
| JP (1) | JP2010505602A (en) |
| CN (1) | CN101516791B (en) |
| AT (1) | ATE466820T1 (en) |
| BR (1) | BRPI0717486B1 (en) |
| CA (1) | CA2664679C (en) |
| DE (1) | DE602007006260D1 (en) |
| DK (1) | DK1905743T3 (en) |
| ES (1) | ES2341370T3 (en) |
| NO (1) | NO341674B1 (en) |
| WO (1) | WO2008042751A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9145315B2 (en) | 2013-03-01 | 2015-09-29 | Paradigm Environmental Technologies Inc. | Wastewater treatment process and system |
Families Citing this family (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9248415B2 (en) | 2004-05-25 | 2016-02-02 | Board Of Trustees Of The University Of Arkansas | Systems and methods for maximizing dissolved gas concentration of a single species of gas from a mixture of multiple gases |
| US9340438B2 (en) | 2004-05-25 | 2016-05-17 | Board Of Trustees Of The University Of Arkansas | Systems and methods for delivering dissolved gases into force-main and gravity sewers |
| US9315402B2 (en) * | 2004-05-25 | 2016-04-19 | Board Of Trustees Of The University Of Arkansas | Systems and methods for wastewater treatment |
| US7309432B1 (en) * | 2006-09-29 | 2007-12-18 | Praxair Technology, Inc. | System and method for eliminating sludge via ozonation |
| DE102007060914B4 (en) * | 2007-12-14 | 2023-03-16 | Air Liquide Deutschland Gmbh | Process for treating water in a treatment plant |
| US8268174B2 (en) * | 2009-11-02 | 2012-09-18 | Ovivo Luxembourg S.a.r.l. | Wastewater treatment method and system with ozonation for microconstituent removal |
| CN103974910B (en) * | 2011-12-01 | 2016-10-19 | 普莱克斯技术有限公司 | For carrying out the method and system of sludge ozonation in Waste Water Treatment |
| US8308946B2 (en) * | 2012-01-28 | 2012-11-13 | Epcot Crenshaw Corporation | Systems and methods for anaerobic digestion of biomaterials |
| AU2014223287A1 (en) | 2013-03-01 | 2015-10-22 | Paradigm Environmental Technologies Inc. | Wastewater treatment process and system |
| CN106103361A (en) * | 2014-04-29 | 2016-11-09 | 三菱电机株式会社 | Sludge treatment equipment and method for sludge treatment |
| BR102014014539A2 (en) * | 2014-06-13 | 2016-01-05 | Biotecam Assessoria E Desenvolvimento De Tecnologia Ambiental Ltda | microbial crop enrichment equipment and process for environmental applications |
| EP3160627B1 (en) * | 2014-06-24 | 2019-02-13 | Nova Chemicals (International) S.A. | Controlling local fluid age in a stirred reactor |
| CN104291442A (en) * | 2014-10-09 | 2015-01-21 | 常州大学 | Method for inhibiting activated sludge bulking of SBR pool |
| CN104710090B (en) * | 2015-03-25 | 2016-08-17 | 刘劼 | A kind of pollution-free method for sludge treatment |
| US10077418B2 (en) | 2015-04-15 | 2018-09-18 | Board Of Trustees Of The University Of Arkansas | Method for improved rate and control of beverage carbonation with automatic shut-off |
| JP2016209800A (en) * | 2015-05-01 | 2016-12-15 | 株式会社安川電機 | Excess sludge weight loss device |
| TWI571443B (en) * | 2015-07-08 | 2017-02-21 | Lin Zhi-Yan | Biological sludge reduction method |
| CN106007256A (en) * | 2016-07-28 | 2016-10-12 | 黄霞 | Microbubble ozone catalytic oxidation-no-aeration biochemical coupling technology system and application thereof |
| JP6342029B1 (en) * | 2017-03-13 | 2018-06-13 | 株式会社御池鐵工所 | Sludge treatment equipment |
| JP6818671B2 (en) * | 2017-10-10 | 2021-01-20 | 三菱電機株式会社 | Wastewater treatment system |
| CN107721111A (en) * | 2017-11-10 | 2018-02-23 | 北京宜清源科技有限公司 | A kind of system and method for mud decrement processing |
| WO2019193646A1 (en) * | 2018-04-03 | 2019-10-10 | 三菱電機株式会社 | Sludge discharge control device, water treatment system, and sludge discharge control method |
| CN109467293A (en) * | 2018-12-25 | 2019-03-15 | 湖南智水环境工程有限公司 | Sludge reduction device and water treatment facilities |
| CN110526497A (en) * | 2019-08-22 | 2019-12-03 | 麦王环境技术股份有限公司 | A kind of wastewater treatment equipment and method based on MBR in conjunction with ozone multi-point adding |
| IT202100017066A1 (en) | 2021-06-29 | 2022-12-29 | Soc It Acetilene E Derivati S I A D S P A In Breve S I A D S P A | WASTEWATER TREATMENT PLANT WITH REDUCTION OF HARMFUL OUTFLOWS THROUGH INTEGRATION AND RECOVERY OF GAS FLOWS RICH IN OXYGEN AND OZONE WITH LOW ENERGY CONSUMPTION SYSTEMS |
Family Cites Families (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4178239A (en) * | 1974-11-13 | 1979-12-11 | Union Carbide Corporation | Biological intermediate sewage treatment with ozone pretreatment |
| JPS558835A (en) | 1978-07-04 | 1980-01-22 | Shinryo Air Conditioning Co Ltd | Treatment of surplus sludge |
| JP3351047B2 (en) | 1993-09-27 | 2002-11-25 | 栗田工業株式会社 | Treatment method of biological sludge |
| JP3697729B2 (en) * | 1994-11-14 | 2005-09-21 | 栗田工業株式会社 | Biological sludge ozone treatment equipment |
| JP3521535B2 (en) | 1995-04-11 | 2004-04-19 | 栗田工業株式会社 | Aerobic biological treatment system for organic wastewater |
| JP3322783B2 (en) | 1995-11-30 | 2002-09-09 | 株式会社荏原製作所 | Method and apparatus for treating organic sewage |
| DE69630236T2 (en) * | 1996-07-19 | 2004-08-05 | Kurita Water Industries, Ltd. | METHOD AND DEVICE FOR THE BIOLOGICAL TREATMENT OF ORGANICALLY POLLUTED WASTE WATER |
| JP4410163B2 (en) * | 1997-05-30 | 2010-02-03 | 三菱電機株式会社 | Waste water ozone treatment method and ozone treatment apparatus |
| JP3397096B2 (en) | 1997-09-19 | 2003-04-14 | 栗田工業株式会社 | Apparatus and method for ozone treatment of biological sludge |
| US6126842A (en) * | 1998-01-30 | 2000-10-03 | Decker; R. Scott | Low-concentration ozone waste water treatment |
| JP2001191097A (en) * | 1999-10-25 | 2001-07-17 | Sumitomo Precision Prod Co Ltd | Waste water treating method |
| DE10035268A1 (en) | 2000-07-20 | 2002-01-31 | Scc Special Comm Cables Gmbh | Optical cable for sewer conduit or pipe system has reinforcement elements on one half of cable sheath surrounding core element containing optical transmission elements |
| JP2005230582A (en) | 2000-10-06 | 2005-09-02 | Able:Kk | Method and apparatus for volume reduction of surplus sludge |
| WO2002088803A2 (en) | 2001-04-30 | 2002-11-07 | Sterlite Optical Technologies Limited | Dispersion shifted fiber having low dispersion slope |
| JP3744428B2 (en) | 2002-01-30 | 2006-02-08 | 栗田工業株式会社 | Apparatus and method for aerobic digestion treatment of sludge |
| DE10215413A1 (en) | 2002-04-08 | 2003-10-23 | Air Liquide Gmbh | Waste water with organic residues treated in first reactor chamber by return-feed of pre-treated water containing regulated feed of dead organisms from second chamber |
| US20040004038A1 (en) | 2002-07-03 | 2004-01-08 | Jfe Engineering Corporation | Method and apparatus for treating sludge, and method and apparatus for treating wastewater utilizing the same |
| JP4503248B2 (en) * | 2002-08-30 | 2010-07-14 | 住友重機械エンバイロメント株式会社 | Wastewater treatment method |
| FR2845682B1 (en) | 2002-10-10 | 2004-11-19 | Air Liquide | METHOD OF REDUCING SLUDGE OF BIOLOGICAL TREATMENT OF WATER USING OZONE |
| FR2864069B1 (en) | 2003-12-17 | 2006-05-05 | Air Liquide | METHOD FOR REDUCING SLURRY FROM WASTEWATER TREATMENT BY OXYGENATION AND MECHANICAL ACTION |
| US7309432B1 (en) * | 2006-09-29 | 2007-12-18 | Praxair Technology, Inc. | System and method for eliminating sludge via ozonation |
-
2006
- 2006-09-29 US US11/541,100 patent/US7309432B1/en active Active
-
2007
- 2007-03-02 DK DK07004391T patent/DK1905743T3/en active
- 2007-03-02 EP EP20070004391 patent/EP1905743B1/en not_active Not-in-force
- 2007-03-02 DE DE200760006260 patent/DE602007006260D1/en active Active
- 2007-03-02 AT AT07004391T patent/ATE466820T1/en not_active IP Right Cessation
- 2007-03-02 ES ES07004391T patent/ES2341370T3/en active Active
- 2007-09-28 CA CA 2664679 patent/CA2664679C/en not_active Expired - Fee Related
- 2007-09-28 JP JP2009530624A patent/JP2010505602A/en active Pending
- 2007-09-28 CN CN2007800360857A patent/CN101516791B/en not_active Expired - Fee Related
- 2007-09-28 WO PCT/US2007/079842 patent/WO2008042751A1/en active Application Filing
- 2007-09-28 BR BRPI0717486A patent/BRPI0717486B1/en not_active IP Right Cessation
- 2007-10-31 US US11/930,264 patent/US7695622B2/en not_active Expired - Fee Related
-
2009
- 2009-04-28 NO NO20091686A patent/NO341674B1/en not_active IP Right Cessation
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9145315B2 (en) | 2013-03-01 | 2015-09-29 | Paradigm Environmental Technologies Inc. | Wastewater treatment process and system |
| US9809480B2 (en) | 2013-03-01 | 2017-11-07 | Cypress Technologies Limited | Wastewater treatment process and system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101516791B (en) | 2012-11-28 |
| ES2341370T3 (en) | 2010-06-18 |
| BRPI0717486B1 (en) | 2018-07-17 |
| BRPI0717486A2 (en) | 2013-10-15 |
| US7309432B1 (en) | 2007-12-18 |
| WO2008042751A1 (en) | 2008-04-10 |
| DK1905743T3 (en) | 2010-08-16 |
| EP1905743A1 (en) | 2008-04-02 |
| NO20091686L (en) | 2009-06-23 |
| US20080128352A1 (en) | 2008-06-05 |
| CN101516791A (en) | 2009-08-26 |
| EP1905743B1 (en) | 2010-05-05 |
| ATE466820T1 (en) | 2010-05-15 |
| NO341674B1 (en) | 2017-12-18 |
| US7695622B2 (en) | 2010-04-13 |
| DE602007006260D1 (en) | 2010-06-17 |
| JP2010505602A (en) | 2010-02-25 |
| CA2664679C (en) | 2012-06-26 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKLA | Lapsed |
Effective date: 20200928 |