WO1992002465A1 - Treatment of a trickling-percolating filter - Google Patents
Treatment of a trickling-percolating filter Download PDFInfo
- Publication number
- WO1992002465A1 WO1992002465A1 PCT/GB1991/001271 GB9101271W WO9202465A1 WO 1992002465 A1 WO1992002465 A1 WO 1992002465A1 GB 9101271 W GB9101271 W GB 9101271W WO 9202465 A1 WO9202465 A1 WO 9202465A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- filter
- medium
- treatment
- trickling
- pipes
- Prior art date
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
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
-
- 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
- C02F3/04—Aerobic processes using trickle filters
-
- 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
- C02F3/28—Anaerobic digestion processes
- C02F3/2806—Anaerobic processes using solid supports for microorganisms
-
- 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
Definitions
- the invention relates to a method of treatment for the restoration and maintenance of the function of a trickling-percolating filter for wastewater and provides a specially developed application system used with the process equipment available on-site at the wastewater treatment plant.
- This system provides an extremely economic restoration process for existing trickling-percolating filters which have restricted flow and would, under the circumstances, require disassembly, cleaning and reassembling for rectification.
- the method can be utilised while the filter is operating or after the filter has become blocked and is no longer operational.
- the system described also provides for on-line maintenance while the trickling-percolating filter continues to function.
- a trickling-percolating filter is a fixed medium secondary system.
- the medium is composed of tightly packed material, usually stones, sheets of Neoprene rubber or plastic shapes of various types, usually contained in a cylindrical tank.
- the medium provides a surface on which a microbial mass develops as a result of the utilisation of the food e - ⁇ nutrients present in the influent wastewater by microorganisms.
- the wastewater is distributed over the surface of the medium usually by means of rotating arms. Thus the wastewater is allowed to trickle over and percolate through the medium. It is therefore cleaned by the action of the microbial mass growing on the medium.
- the process of cleaning the wastewater is usually aerobic, requiring oxygen from the air present in the interstitial spaces in the medium.
- the oxygen provides the oxidizing potential to the growing microbial mass, or biomass, growing there.
- solids are produced which must exit the filter.
- these solids are sloughed from the medium and collected in the secondary clarifier of the treatment plant.
- a method of treatment of a trickling- percolating filter which consists in applying, in a distributed manner within the body of the filter medium, a liquid solution of one or more electron acceptor substances.
- the application of the electron acceptor solution is followed by the application of a liquid suspension of microorganisms (bacteria) capable of using the said electron acceptor substance or substances.
- bacteria microorganisms
- the soluble electron acceptor substitutes for oxygen which is no longer available to the biomass while a "puddling/ponding" condition remains.
- This technique allows an on-site and in place bio-remediation of the trickling-percolating filter. It is, in fact, a bacterial and biochemical process which restores function to the filter during the course of the treatment process itself. The technique can be continued after the filter returns to effective operation as a preventive maintenance process and to improve process treatment and capacity.
- Injection of a concentrated solution of sodium or potassium nitrate salts having a concentration of 50% weight/volume or greater, for example, into the trickling-percolating filter can be accomplished by pouring the solution into porous pipes, made of plastic or other material and placed vertically into the medium symmetrically over its surface.
- the bacterial suspension can, as well, D ⁇ poured into these same pipes. If the pipes are driven deeply enough into the medium they will not interfere with the rotation of the arms of the trickling-percolating filter. They may be left in place in the medium and used as a part of the regular maintenance program of the trickling-percolating filter.
- the restoration of the filter by the biochemical bacterial system described herein involves, among the basic biochemical functions provided by the bacteria as they grow, several processes produced by the hydraulics of the newly introduced pipes and the products of the utilisation of nitrate as an electron acceptor. Normally the hydraulic pressure provided by the influent is downward. The hydraulic pressure provided by the pipes is horizontal as the liquid exits these pipes from their sides. In addition, nitrogen gas is produced from the denitrification of the nitrate by the bacteria of the system. This nitrogen gas provides an additional turbulence as it will rise vertically out of the media present in the percolating-trickling filter. Thus there are now three pressures and flows provided during the use of the described system: hydraulic, downward and lateral and gaseous upward.
- a trickling-percolating filter comprising a container which holds a filter medium; a rotary arm structure arranged above the filter medium to trickle-feed wastewater on to the medium; and a plurality of spaced porous pipes embedded in the medium and adapted to be fed with liquids for remedial and/or preventative blockage treatment of the medium, the pipes being effective to feed the liquids in distimped fashion throughout the medium.
- Figure 1 is a top view of a filter incorporating the invention
- Figure 2 is a cross-sectional view of the filter of Figure 1.
- Figure 3 is a diagram illustrating the manner in which the perforated pipes are inserted into the filter medium.
- the filter 1 comprises a medium which is a bed of granular material 2 comprising stones, plastic shapes etc. which fills a cylindrical tank 3.
- a set of rotating perforated arms dispenses wastewater onto the top of the bed. The wastewater trickles through the medium and is aerobically treated by bacteria therein.
- the invention provides a set of vertical perforated pipes 5 plunged into the material which can be connectedto a fluid supply system (not shown) .
- fluid comprising a solution of sodium or potassium nitrate salts is fed to the pipes 5 bypassing and removing blockages which may cause "puddling/ponding" .
- the pipes 5 are also used for the distribution of liquid containing specific microorganisms which are prescribed to provide the biological activity needed to release blockage of the medium material by utilising the nitrate salts and to enhance the action of the filter.
- the time interval between the application of the nitrate solution and the bacterial suspension is approximately 1 to 2 hours.
- FIG. 3 shows a system for the installation of the feed pipes into a filter medium of the filter.
- the filter medium In situations where the filter medium is tightly packed or compacted it is necessary to create open vertical shafts into the filter medium by means of a mechanical device which can penetrate to the base of the medium for the purpose of inserting the feed pipes.
- An example of such a system is one that includes three 3 parts.
- the pneumatic hammer then drives the hollow driving shaft with the inserted drill tip/pipe anchor into the filter medium to the desired depth.
- Several different lengths of hollow driving shafts may be required depending on the depths of the filter medium encountered.
- the pneumatic hammer Upon reaching the desired depth, the pneumatic hammer is withdrawn from the hollow driving shaft. A feed pipe is then inserted into the hollow driving shaft until it contacts the drill tip/pipe anchor. The hollow driving shaft is then withdrawn leaving the feed pipe in place at the desired d -»th.
- the feed pipes do not extend above the level of the medium sufficiently far to impede the rotation of the feed arms. The top of the feed pipes may be marked for easier location and identification.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Compounds Of Unknown Constitution (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9016505.1 | 1990-07-27 | ||
GB9016505A GB9016505D0 (en) | 1990-07-27 | 1990-07-27 | Restoration and maintenance of the function of a trickling-percolating-filter |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1992002465A1 true WO1992002465A1 (en) | 1992-02-20 |
Family
ID=10679749
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB1991/001271 WO1992002465A1 (en) | 1990-07-27 | 1991-07-26 | Treatment of a trickling-percolating filter |
Country Status (4)
Country | Link |
---|---|
AU (1) | AU8301991A (en) |
CA (1) | CA2066231A1 (en) |
GB (1) | GB9016505D0 (en) |
WO (1) | WO1992002465A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4410271C1 (en) * | 1994-03-24 | 1995-09-21 | Lumos Trading & Investments Co | Process for reducing slime and deposit formation in plants in which water from paper and pulp machines is circulated, and in plants in which cooling water is circulated |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2524459A1 (en) * | 1982-04-06 | 1983-10-07 | Ceskoslovenska Akademie Ved | PROCESS FOR THE CONCENTRATION OF A BIOLOGICAL SLUDGE, PARTICULARLY AN ACTIVE SLUDGE |
DE3205452C1 (en) * | 1982-02-16 | 1983-10-27 | Grabowski Tropfkörper-Technik GmbH, 6352 Ober-Mörlen | Device for in situ washing of a packing usable for biological waste water treatment |
FR2553751A1 (en) * | 1983-10-24 | 1985-04-26 | British Petroleum Co | Process for biological purification of waste water by trickling over bacterial beds and device employed. |
-
1990
- 1990-07-27 GB GB9016505A patent/GB9016505D0/en active Pending
-
1991
- 1991-07-26 AU AU83019/91A patent/AU8301991A/en not_active Abandoned
- 1991-07-26 CA CA002066231A patent/CA2066231A1/en not_active Abandoned
- 1991-07-26 WO PCT/GB1991/001271 patent/WO1992002465A1/en not_active Application Discontinuation
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3205452C1 (en) * | 1982-02-16 | 1983-10-27 | Grabowski Tropfkörper-Technik GmbH, 6352 Ober-Mörlen | Device for in situ washing of a packing usable for biological waste water treatment |
FR2524459A1 (en) * | 1982-04-06 | 1983-10-07 | Ceskoslovenska Akademie Ved | PROCESS FOR THE CONCENTRATION OF A BIOLOGICAL SLUDGE, PARTICULARLY AN ACTIVE SLUDGE |
FR2553751A1 (en) * | 1983-10-24 | 1985-04-26 | British Petroleum Co | Process for biological purification of waste water by trickling over bacterial beds and device employed. |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4410271C1 (en) * | 1994-03-24 | 1995-09-21 | Lumos Trading & Investments Co | Process for reducing slime and deposit formation in plants in which water from paper and pulp machines is circulated, and in plants in which cooling water is circulated |
DE4410271C2 (en) * | 1994-03-24 | 1999-02-25 | Lumos Trading & Investments Co | Process for reducing the formation of slime and deposits in systems in which water from paper and pulp machines is circulated, as well as in systems in which cooling water is circulated |
Also Published As
Publication number | Publication date |
---|---|
GB9016505D0 (en) | 1990-09-12 |
CA2066231A1 (en) | 1992-01-28 |
AU8301991A (en) | 1992-03-02 |
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