US20050189281A1 - Cellular microbead filter for use in water recirculating system - Google Patents

Cellular microbead filter for use in water recirculating system Download PDF

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Publication number
US20050189281A1
US20050189281A1 US10/672,140 US67214003A US2005189281A1 US 20050189281 A1 US20050189281 A1 US 20050189281A1 US 67214003 A US67214003 A US 67214003A US 2005189281 A1 US2005189281 A1 US 2005189281A1
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Prior art keywords
microbeads
water
filtration system
chamber
cell
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US10/672,140
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Michael Timmons
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Cornell Research Foundation Inc
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Cornell Research Foundation Inc
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    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01KANIMAL HUSBANDRY; CARE OF BIRDS, FISHES, INSECTS; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
    • A01K63/00Receptacles for live fish, e.g. aquaria; Terraria
    • A01K63/04Arrangements for treating water specially adapted to receptacles for live fish
    • A01K63/045Filters for aquaria

Definitions

  • This application relates generally to filtration systems and, more particularly, to a water recirculating system for use in producing fish.
  • Raising fish in water recirculating systems requires nitrification treatment systems that maintain acceptable levels of ammonia and nitrite within a water supply.
  • a water recirculating system needs to be able to oxidize an ammonia load that is generated by fish as a result of daily fish feedings.
  • FIG. 1 illustrates one type of prior art filtration system 10 that may be used in a water recirculating system.
  • the filtration system 10 includes a chamber 12 that contains microbeads 14 .
  • Microbeads 14 are sufficiently buoyant such that they float on top of filtered water 16 that collects in the bottom of chamber 12 .
  • the microbeads 14 on the bottom are partially submerged in filtered water 16 because they support the weight of the microbeads 14 located above them.
  • Contaminated water 18 is delivered to filtration system 10 from a number of potential sources, including fish raising tanks where the water supply is contaminated with unsatisfactorily high ammonia loads.
  • Contaminated water 18 is supplied to chamber 12 from above microbeads 14 using any method that uniformly distributes contaminated water 18 over microbeads 14 , such as nozzles 13 arranged in a uniform pattern.
  • Gravity forces contaminated water 18 downward through microbeads 14 where it collects in the bottom of chamber 12 .
  • Contaminated water 18 applies a force to microbeads 14 as it impacts microbeads 14 such that contaminated water 18 submerges some additional microbeads 14 .
  • An exit pipe 20 circulates filtered water 16 back to the contaminated water source.
  • Microbeads 14 provide a substrate for bacterial growth during operation of filtration system 10 .
  • the bacteria on microbeads 14 utilize the ammonia and nitrite as nutrients for even further bacterial growth.
  • the bacterial growth on microbeads 14 also tends to reduce the buoyancy of microbeads 14 .
  • Heterotropic bacteria living on the same beads utilize fine organic solids as nutrients for growth resulting in water polishing and general improvement in water quality.
  • microbeads 14 One disadvantage of using a system 10 that includes microbeads 14 is that such systems are limited in size. In systems with large chambers, the strong buoyancy of microbeads 14 causes microbeads 14 to short circuit the flow of water through microbeads 14 in some areas of the chamber. Short circuiting the flow of water through microbeads 14 inhibits the ability of the bacteria on microbeads 14 to oxidize ammonia loads in the water passing through microbeads 14 .
  • microbeads make it necessary to utilize several chambers when oxidizing commercial ammonia loads (e.g., 9 kilograms TAN per day) that are generated from commercial fish feedings (e.g., 300 kilograms per day).
  • commercial ammonia loads e.g. 9 kilograms TAN per day
  • commercial fish feedings e.g. 300 kilograms per day.
  • the large number of chambers that are required to handle commercial ammonia loads adds unwanted expense to systems that include microbeads 14 .
  • a filtration system having a chamber with a hydraulic loading area that is divided into a plurality of cells such that each cell has a hydraulic loading area less than 2.3 square meters.
  • the system further includes a filter media, such as microbeads, positioned in each cell to filter water passing through the chamber.
  • the microbeads are spherical and have diameters between 1 mm and 3 mm.
  • the size limitation of conventional microbead filter systems is addressed by dividing the hydraulic loading area in a large chamber into cells with smaller hydraulic loading areas.
  • the smaller hydraulic loading area through each cell promotes efficient filtering by bacteria that grows on the microbeads in each cell.
  • the water recirculating system includes a fish raising tank that provides an environment for fish to grow.
  • a supply system such as a pumping system, delivers water from the tank to a filtration system.
  • the filtration system includes a chamber with a hydraulic loading area that is divided into a plurality of cells with smaller hydraulic loading areas. Filter media, such as microbeads, are positioned in each cell to filter the water received from the supply system.
  • a delivery system returns the filtered water back to the tank.
  • FIG. 1 illustrates a prior art filtration system that includes microbeads.
  • FIG. 2 illustrates a water recirculating system
  • FIG. 3 is a section view of a chamber in the water recirculating system of FIG. 2 taken along line 3 - 3 .
  • FIG. 2 illustrates one embodiment of a water recirculating system 50 that includes a filtration system 52 .
  • Filtration system 52 includes a chamber 54 having a hydraulic loading area that is divided into a plurality of cells 56 A-H (see FIG. 3 ) with smaller hydraulic loading areas.
  • a filter media, such as microbeads 58 is positioned in each of the cells 56 A-H to filter water that passes through the cells 56 A-H.
  • hydraulic loading area is a cross-sectional area of a particular portion of the filtration system 52 that is transverse to the flow of water through that particular portion. As shown in FIG. 3 , the hydraulic loading area in chamber 54 is equal to dimension A multiplied by dimension B. In the sample embodiment shown in FIG. 3 , the hydraulic loading area of each cell is dimension X multiplied by dimension Y (shown for cell 56 H only). The size of cells 56 A-H may be the same, or varied, depending on the application where filtration system 52 is being used.
  • Filtration system 52 may further include a plurality of nozzles 60 positioned above microbeads 58 within chamber 54 .
  • a supply system 57 may be used to transport contaminated water from a water source, such as a fish raising tank 55 . The contaminated water is supplied to nozzles 60 for uniform distribution above each cell 56 A-H in chamber 54 .
  • the supply system is a pumping system.
  • Chamber 54 is at least partially immersed in a receiving tank 62 that holds filtered water after it passes through microbeads 58 .
  • a delivery system 64 circulates the water back to fish raising tank 55 .
  • delivery system 64 is a pumping system and fish raising tank 55 is a pond.
  • the water in each cell 56 A-H is isolated from the water in the other cells 56 A-H as the water flows through microbeads 58 .
  • the water is unable to flow between cells 56 A-H as the water passes through microbeads 58 .
  • microbeads may be polystyrene, or any other material that adequately filters a particular contaminated water supply.
  • microbeads 58 are spherical and have a diameter between 1 mm and 3 mm.
  • the density of each microbead may be between 8 kg/cubic meter and 48 kg/cubic meter.
  • microbeads 58 are positioned within each cell 56 A-H such that microbeads 58 have a depth D between 15 cm and 60 cm.
  • the depth D of microbeads 58 will depend on such factors as the size of microbeads 58 and each cell 56 A-H in addition to the flow rate of the water through microbeads 58 .
  • chamber 54 has a rectangularly-shaped hydraulic loading area as water passes through microbeads 58 and cells 56 A-H have either a square or rectangularly-shaped hydraulic loading area.
  • Each cell 56 A-H may have a hydraulic loading area less than 2.3 square meters and/or a perimeter greater than 6 meters.
  • chamber 54 has a hydraulic loading area greater than 4.6 square meters while each cell 56 A-H has a hydraulic loading area less than 2.3 square meters.
  • specific shapes and sizes are shown and described for chamber 54 and cells 56 A-H, it will be appreciated by those of ordinary skill in the art that chamber 54 and cells 56 A-H may have any shape and size that adequately functions in filtration system 52 .
  • the number of cells may vary to suit particular applications.
  • Filtration system 52 may also include an air passage 64 positioned above microbeads 58 .
  • a fluid source 65 forces a fluid, such as air, to pass by the water before it drops onto microbeads 58 . Passing air by the water strips undesirable carbon dioxide from the water before the water passes through microbeads 58 . Carbon dioxide is extremely soluble in water such the carbon dioxide stripping may be necessary in some recirculating applications.
  • fluid source 65 may be integrated with a ventilation system of the building where filtration system 52 is located.

Abstract

A water recirculating system for use in producing fish. The water recirculating system includes a fish raising tank that provides an environment for fish to grow and a supply system to deliver contaminated water from the fish raising tank to a filtration system. The filtration system includes a chamber with a hydraulic loading area that is divided into a plurality of cells with smaller hydraulic loading areas. Filter media is positioned in each cell to filter the contaminated water received from the fish raising tank. A delivery system returns the filtered water back to the fish raising tank.

Description

    TECHNICAL FIELD
  • This application relates generally to filtration systems and, more particularly, to a water recirculating system for use in producing fish.
  • BACKGROUND
  • Raising fish in water recirculating systems requires nitrification treatment systems that maintain acceptable levels of ammonia and nitrite within a water supply. A water recirculating system needs to be able to oxidize an ammonia load that is generated by fish as a result of daily fish feedings.
  • FIG. 1 illustrates one type of prior art filtration system 10 that may be used in a water recirculating system. The filtration system 10 includes a chamber 12 that contains microbeads 14. Microbeads 14 are sufficiently buoyant such that they float on top of filtered water 16 that collects in the bottom of chamber 12. The microbeads 14 on the bottom are partially submerged in filtered water 16 because they support the weight of the microbeads 14 located above them.
  • Contaminated water 18 is delivered to filtration system 10 from a number of potential sources, including fish raising tanks where the water supply is contaminated with unsatisfactorily high ammonia loads. Contaminated water 18 is supplied to chamber 12 from above microbeads 14 using any method that uniformly distributes contaminated water 18 over microbeads 14, such as nozzles 13 arranged in a uniform pattern. Gravity forces contaminated water 18 downward through microbeads 14 where it collects in the bottom of chamber 12. Contaminated water 18 applies a force to microbeads 14 as it impacts microbeads 14 such that contaminated water 18 submerges some additional microbeads 14. An exit pipe 20 circulates filtered water 16 back to the contaminated water source.
  • Microbeads 14 provide a substrate for bacterial growth during operation of filtration system 10. The bacteria on microbeads 14 utilize the ammonia and nitrite as nutrients for even further bacterial growth. The bacterial growth on microbeads 14 also tends to reduce the buoyancy of microbeads 14. Heterotropic bacteria living on the same beads utilize fine organic solids as nutrients for growth resulting in water polishing and general improvement in water quality.
  • One disadvantage of using a system 10 that includes microbeads 14 is that such systems are limited in size. In systems with large chambers, the strong buoyancy of microbeads 14 causes microbeads 14 to short circuit the flow of water through microbeads 14 in some areas of the chamber. Short circuiting the flow of water through microbeads 14 inhibits the ability of the bacteria on microbeads 14 to oxidize ammonia loads in the water passing through microbeads 14.
  • The size limitations associated with conventional filtration systems that include microbeads makes it necessary to utilize several chambers when oxidizing commercial ammonia loads (e.g., 9 kilograms TAN per day) that are generated from commercial fish feedings (e.g., 300 kilograms per day). The large number of chambers that are required to handle commercial ammonia loads adds unwanted expense to systems that include microbeads 14.
  • SUMMARY
  • A filtration system having a chamber with a hydraulic loading area that is divided into a plurality of cells such that each cell has a hydraulic loading area less than 2.3 square meters. The system further includes a filter media, such as microbeads, positioned in each cell to filter water passing through the chamber. In some embodiments, the microbeads are spherical and have diameters between 1 mm and 3 mm.
  • The size limitation of conventional microbead filter systems is addressed by dividing the hydraulic loading area in a large chamber into cells with smaller hydraulic loading areas. The smaller hydraulic loading area through each cell promotes efficient filtering by bacteria that grows on the microbeads in each cell.
  • Another aspect relates to a water recirculating system for use in producing fish. The water recirculating system includes a fish raising tank that provides an environment for fish to grow. A supply system, such as a pumping system, delivers water from the tank to a filtration system. The filtration system includes a chamber with a hydraulic loading area that is divided into a plurality of cells with smaller hydraulic loading areas. Filter media, such as microbeads, are positioned in each cell to filter the water received from the supply system. A delivery system returns the filtered water back to the tank.
  • These and other aspects, embodiments and features will become apparent from the following description and the referenced drawings.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 illustrates a prior art filtration system that includes microbeads.
  • FIG. 2 illustrates a water recirculating system.
  • FIG. 3 is a section view of a chamber in the water recirculating system of FIG. 2 taken along line 3-3.
  • DETAILED DESCRIPTION
  • The following detailed description refers to the accompanying drawings. In the drawings, like numerals describe substantially similar components throughout the several views. These embodiments are described in sufficient detail to enable those skilled in the art to practice the present subject matter. Other embodiments may be utilized and changes may be made. The scope of the present subject matter is defined only by the appended claims, along with the full scope of equivalents to which such claims are entitled.
  • FIG. 2 illustrates one embodiment of a water recirculating system 50 that includes a filtration system 52. Filtration system 52 includes a chamber 54 having a hydraulic loading area that is divided into a plurality of cells 56A-H (see FIG. 3) with smaller hydraulic loading areas. A filter media, such as microbeads 58, is positioned in each of the cells 56A-H to filter water that passes through the cells 56A-H.
  • As used herein, hydraulic loading area is a cross-sectional area of a particular portion of the filtration system 52 that is transverse to the flow of water through that particular portion. As shown in FIG. 3, the hydraulic loading area in chamber 54 is equal to dimension A multiplied by dimension B. In the sample embodiment shown in FIG. 3, the hydraulic loading area of each cell is dimension X multiplied by dimension Y (shown for cell 56H only). The size of cells 56A-H may be the same, or varied, depending on the application where filtration system 52 is being used.
  • Filtration system 52 may further include a plurality of nozzles 60 positioned above microbeads 58 within chamber 54. A supply system 57 may be used to transport contaminated water from a water source, such as a fish raising tank 55. The contaminated water is supplied to nozzles 60 for uniform distribution above each cell 56A-H in chamber 54. In some embodiments, the supply system is a pumping system.
  • Chamber 54 is at least partially immersed in a receiving tank 62 that holds filtered water after it passes through microbeads 58. A delivery system 64 circulates the water back to fish raising tank 55. In some embodiments, delivery system 64 is a pumping system and fish raising tank 55 is a pond.
  • In one example embodiment, the water in each cell 56A-H is isolated from the water in the other cells 56A-H as the water flows through microbeads 58. In such example embodiments, the water is unable to flow between cells 56A-H as the water passes through microbeads 58.
  • The microbeads may be polystyrene, or any other material that adequately filters a particular contaminated water supply. In some embodiments, microbeads 58 are spherical and have a diameter between 1 mm and 3 mm. The density of each microbead may be between 8 kg/cubic meter and 48 kg/cubic meter. Although specific shapes, sizes and properties are described for microbeads 58, it will be appreciated by those of ordinary skill in the art that any microbeads which are calculated to achieve the same purpose may be substituted for the specific microbeads described herein.
  • In some embodiments, microbeads 58 are positioned within each cell 56A-H such that microbeads 58 have a depth D between 15 cm and 60 cm. The depth D of microbeads 58 will depend on such factors as the size of microbeads 58 and each cell 56A-H in addition to the flow rate of the water through microbeads 58.
  • In the example embodiment shown in FIG. 3, chamber 54 has a rectangularly-shaped hydraulic loading area as water passes through microbeads 58 and cells 56A-H have either a square or rectangularly-shaped hydraulic loading area. Each cell 56A-H may have a hydraulic loading area less than 2.3 square meters and/or a perimeter greater than 6 meters. In some embodiments, chamber 54 has a hydraulic loading area greater than 4.6 square meters while each cell 56A-H has a hydraulic loading area less than 2.3 square meters. Although specific shapes and sizes are shown and described for chamber 54 and cells 56A-H, it will be appreciated by those of ordinary skill in the art that chamber 54 and cells 56A-H may have any shape and size that adequately functions in filtration system 52. In addition, the number of cells may vary to suit particular applications.
  • Filtration system 52 may also include an air passage 64 positioned above microbeads 58. A fluid source 65 forces a fluid, such as air, to pass by the water before it drops onto microbeads 58. Passing air by the water strips undesirable carbon dioxide from the water before the water passes through microbeads 58. Carbon dioxide is extremely soluble in water such the carbon dioxide stripping may be necessary in some recirculating applications. In some embodiments, fluid source 65 may be integrated with a ventilation system of the building where filtration system 52 is located.
  • Although specific embodiments have been illustrated and described herein, it will be appreciated by those of ordinary skill in the art that any arrangement which is calculated to achieve the same purpose may be substituted for the specific embodiments shown. This application is intended to cover a water recirculating system in applications other than those related to fish raising, including mining, municpal and home wastewater treatment, car washes, laundry mats and other similar applications.
  • It is to be understood that the above description is intended to be illustrative, and not restrictive. Combinations of the above embodiments, and other embodiments will be apparent to those of skill in the art upon reviewing the above description. The scope of the present subject matter should be determined with reference to the appended claims, along with the full scope of equivalents to which such claims are entitled.

Claims (14)

1. A filtration system comprising:
a chamber that includes a hydraulic loading area divided into a plurality of cells with smaller hydraulic loading areas; and
filter media positioned in each of the cells to filter water passing through the cells.
2. The filtration system of claim 1 wherein the water is unable to flow between cells as the water passes through the microbeads.
3. The filtration system of claim 1 wherein the filter media is spherical microbeads with diameters between 1 mm and 3 mm.
4. The filtration system of claim 3 wherein the microbeads have a density that is between 8 kg/cubic meter and 48 kg/cubic meter.
5. The filtration system of claim 1 wherein the microbeads within each cell have a depth between 15 cm and 60 cm.
6. The filtration system of claim 1 wherein the chamber has a rectangularly-shaped hydraulic loading area as water passes through the filer media and each cell has a square-shaped hydraulic loading area.
7. The filtration system of claim 1 wherein each cell has a hydraulic loading area less than 2.3 square meters.
8. A filtration system comprising:
a chamber that includes a hydraulic loading area divided into a plurality of cells such that each cell has a hydraulic loading area less than 2.3 square meters; and
microbeads positioned in each cell to filter water passing through the chamber, the microbeads being spherical and having diameters between 1 mm and 3 mm.
9. The filtration system of claim 8 further comprising a plurality of nozzles positioned above the filter media within the chamber to supply water to each cell in the chamber.
10. The filtration system of claim 8 wherein the microbeads have a density that is between 8 kg/cubic meter and 48 kg/cubic meter and the microbeads within each cell have a depth that is between 15 cm and 60 cm.
11. The filtration system of claim 8 wherein the hydraulic loading area of the chamber is rectangularly-shaped and the hydraulic loading area of each cell is square-shaped.
12. The filtration system of claim 8 further comprising a receiving tank to receive water from the chamber.
13. The filtration system of claim 12 wherein the chamber is at least partially immersed in the receiving tank.
14. The filtration system of claim 8 wherein the water in each cell is isolated from the water in the other cells as the water flows through the microbeads.
US10/672,140 2002-06-14 2003-09-26 Cellular microbead filter for use in water recirculating system Abandoned US20050189281A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050211644A1 (en) * 2004-03-24 2005-09-29 Aquatic Advisors, Llc Mixed bed trickling reactor using microbeads
US7785479B1 (en) * 2007-05-01 2010-08-31 Michael Hays Hosford Apparatus and method of separating
CN103663682A (en) * 2012-09-24 2014-03-26 钱阳 Split-level superimposed biological filtration and oxygenation device

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6666965B1 (en) * 2002-06-14 2003-12-23 Cornell Research Foundation, Inc. Cellular microbead filter for use in water recirculating system
IS6975A (en) * 2003-10-03 2005-04-04 Ithntæknistofnun íslands Water purification equipment and its use
US7309427B2 (en) * 2004-09-13 2007-12-18 Siemens Water Technologies Holding Corp. System for treating liquids
CN101980969A (en) 2008-03-28 2011-02-23 西门子水处理技术公司 Hybrid aerobic and anaerobic wastewater and sludge treatment systems and methods
US8894856B2 (en) 2008-03-28 2014-11-25 Evoqua Water Technologies Llc Hybrid aerobic and anaerobic wastewater and sludge treatment systems and methods
US8685247B2 (en) 2009-12-03 2014-04-01 Evoqua Water Technologies Llc Systems and methods for nutrient removal in biological treatment systems
CN103402926A (en) 2010-04-21 2013-11-20 西门子私人有限公司 Methods and systems for treating wastewater
US9359236B2 (en) 2010-08-18 2016-06-07 Evoqua Water Technologies Llc Enhanced biosorption of wastewater organics using dissolved air flotation with solids recycle
CN103068748A (en) 2010-08-18 2013-04-24 西门子工业公司 Contact-stabilization/prime-float hybrid
US8925490B2 (en) 2012-01-13 2015-01-06 JLH Consulting Inc. Recirculating aquaculture systems and biofilters therefor
GB2527989B (en) 2013-05-06 2020-04-22 Evoqua Water Tech Llc Enhanced biosorption of wastewater organics using dissolved air flotation with solids recycle
US10913667B2 (en) * 2017-12-08 2021-02-09 Westech Engineering, Inc. Multi-media clarification systems and methods

Citations (60)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2055162A (en) * 1933-01-18 1936-09-22 Weber Friedrich August Chamber or tower filled with filling material
US2071591A (en) * 1935-12-02 1937-02-23 Albert L Tholin Sewage treatment
US2088497A (en) * 1934-12-04 1937-07-27 Shell Dev Process and apparatus for contacting fluids
US2188162A (en) * 1938-02-21 1940-01-23 Henry B Schulhoff Sewage treatment
US2394133A (en) * 1944-03-08 1946-02-05 Merle A Zimmerman Apparatus for rectification, absorption, or gas scrubbing
US2405593A (en) * 1944-02-04 1946-08-13 Francis L Melvill Packing for vapor and liquid contacting apparatus
US3122594A (en) * 1958-07-29 1964-02-25 Aluminium Lab Ltd Apparatus and procedure for contact between fluids
US3134735A (en) * 1961-11-28 1964-05-26 Greenleaf Entpr Inc Open gravity filters
US3227429A (en) * 1963-02-04 1966-01-04 American Radiator & Standard Mass transfer packing
US3282432A (en) * 1963-02-18 1966-11-01 Greenleaf Entpr Inc Multiple unit backwashing filter
US3302372A (en) * 1964-04-17 1967-02-07 Armour Agricult Chem Gas scrubbing process and apparatus
US3312348A (en) * 1963-10-31 1967-04-04 Greenleaf Entpr Inc Multiple unit backwashing gravity flow filter
US3340341A (en) * 1963-07-01 1967-09-05 Dow Chemical Co Method of preparing grids
US3430935A (en) * 1965-10-23 1969-03-04 Leo Lawrence Garrett Trickling bar assembly for blow-out towers
US3543937A (en) * 1968-08-02 1970-12-01 Joseph M Choun Filter media
US3589518A (en) * 1969-03-06 1971-06-29 Ircha Inst National De Rech Ch Packing materials especially for biological filters
US3661262A (en) * 1970-08-25 1972-05-09 Oceanography Mariculture Ind Filtration and circulation system for maintaining water quality in mariculture tank
US3792571A (en) * 1971-04-02 1974-02-19 Showa Denko Kk Method and apparatus for purifying waste gas
US3810348A (en) * 1972-01-07 1974-05-14 American Air Filter Co Scrubber arrangement
US3959419A (en) * 1973-09-06 1976-05-25 Fritz W. Glitsch & Sons, Inc. Vapor-liquid contact method
US3966608A (en) * 1974-03-01 1976-06-29 Ecodyne Corporation Liquid treatment apparatus
US3969447A (en) * 1973-10-18 1976-07-13 Fritz W. Glitsch & Sons, Inc. Grids for fluid contact apparatus
US4002705A (en) * 1972-03-01 1977-01-11 Mass Transfer Limited Fluid-fluid contact apparatus
US4045344A (en) * 1974-04-29 1977-08-30 Ishigaki Kiko Co., Ltd. Apparatus for treating waste water
US4122011A (en) * 1975-05-21 1978-10-24 Norton Company Trickling filter media for biological filters
US4182268A (en) * 1976-08-26 1980-01-08 Linde Aktiengesellschaft Breeding of aquatic animals in a controlled environment
US4196079A (en) * 1978-12-29 1980-04-01 Harsco Corporation Pleated filter underdrain, method and apparatus
US4200532A (en) * 1978-06-07 1980-04-29 Ishigaki Kiko Co., Ltd. Wastewater treatment apparatus
US4231863A (en) * 1979-04-26 1980-11-04 Sutphin Eldon M Method and apparatus for treating water
US4333893A (en) * 1980-01-23 1982-06-08 Clyde Robert A High area contactor
US4382046A (en) * 1981-09-22 1983-05-03 Ceramic Cooling Tower Company Water cooling tower with layers of multi-cell tiles and spacers
US4481155A (en) * 1983-10-19 1984-11-06 Ceramic Cooling Tower Company Multi-cell tiles with openings for use in a liquid cooling tower
US4599174A (en) * 1984-02-27 1986-07-08 Polybac Corporation Submerged fixed film biological treatment system
US4793934A (en) * 1987-04-22 1988-12-27 Signal Environmental Systems, Inc. Method for enhancing the separation capacity of a multi-bed filtration system
US4863606A (en) * 1987-12-11 1989-09-05 Ryall Ronald W Waste water treating process
US4929349A (en) * 1988-08-24 1990-05-29 Beckman William J Bio-filtration apparatus and method for wastewater treatment
US4948402A (en) * 1988-12-09 1990-08-14 Davis Water & Waste Industries, Inc. Modular air scrubber system
US5030353A (en) * 1989-01-13 1991-07-09 Stuth William L Secondary sewage treatment system
US5032294A (en) * 1990-03-13 1991-07-16 Schulz Christopher R Multi-cell gravity filter with central control chamber
US5137645A (en) * 1991-06-28 1992-08-11 Infilco Degremont Inc. Declining rate filter systems and methods
US5200081A (en) * 1989-01-13 1993-04-06 Stuth William L Secondary sewage treatment system
US5204027A (en) * 1992-02-04 1993-04-20 Armstrong Charles M Fluid contact panels
US5217616A (en) * 1991-12-06 1993-06-08 Allied-Signal Inc. Process and apparatus for removal of organic pollutants from waste water
US5227055A (en) * 1992-01-15 1993-07-13 Cornell Research Foundation, Inc. Aquaculture water treatment system including combined rotating biological contactor and evaporative cooler
US5277848A (en) * 1989-03-08 1994-01-11 Glitsch, Inc. Method and apparatus for downcomer tray operation
US5308479A (en) * 1989-05-26 1994-05-03 Isamu Iwai Sewage disposal apparatus employing circulating filter media
US5326503A (en) * 1992-07-30 1994-07-05 Mitsubishi Jukogyo Kabushiki Kaisha Latticed packing member for gas-liquid contactors
US5387335A (en) * 1990-11-21 1995-02-07 Iwai; Isamu Filter circulating type sewage disposal apparatus
US5413749A (en) * 1993-06-04 1995-05-09 Wheelabrator Engineered Systems Inc. Process of making beads for a liquid purification bed
US5558763A (en) * 1993-06-24 1996-09-24 Hitachi Plant Engineering & Construction Co., Ltd. Sewage treatment system with air jetting means
US5573663A (en) * 1994-01-10 1996-11-12 Junius; John H. Fluid filter using floating media
US5766488A (en) * 1994-05-12 1998-06-16 United States Filter Corporation Method and apparatus for water treatment
US5945005A (en) * 1994-01-10 1999-08-31 Junius; John H. Fluid filter using floating media
US6080304A (en) * 1997-02-27 2000-06-27 Gex Corporation Clarifying device for use in an aquarium
US6090277A (en) * 1996-06-26 2000-07-18 Gb. Odobez S.R.L. Reactor for the depuration of polluted waste waters
US6524849B1 (en) * 2001-08-23 2003-02-25 Bio-Reaction Industries, Llc Biological filter structures
US20030230246A1 (en) * 2002-06-14 2003-12-18 Cornell Research Foundation, Inc. Cellular microbead filter for use in water recirculating system
US20030230542A1 (en) * 2002-06-13 2003-12-18 United States Filter Corporation Flow splitting weir
US6890439B2 (en) * 2000-05-22 2005-05-10 Dowmus Pty. Ltd. Biolytic filtration
US6890431B1 (en) * 2000-02-18 2005-05-10 The F. B. Leopold Co., Inc. Buoyant media flotation

Patent Citations (67)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2055162A (en) * 1933-01-18 1936-09-22 Weber Friedrich August Chamber or tower filled with filling material
US2088497A (en) * 1934-12-04 1937-07-27 Shell Dev Process and apparatus for contacting fluids
US2071591A (en) * 1935-12-02 1937-02-23 Albert L Tholin Sewage treatment
US2188162A (en) * 1938-02-21 1940-01-23 Henry B Schulhoff Sewage treatment
US2405593A (en) * 1944-02-04 1946-08-13 Francis L Melvill Packing for vapor and liquid contacting apparatus
US2394133A (en) * 1944-03-08 1946-02-05 Merle A Zimmerman Apparatus for rectification, absorption, or gas scrubbing
US3122594A (en) * 1958-07-29 1964-02-25 Aluminium Lab Ltd Apparatus and procedure for contact between fluids
US3134735A (en) * 1961-11-28 1964-05-26 Greenleaf Entpr Inc Open gravity filters
US3227429A (en) * 1963-02-04 1966-01-04 American Radiator & Standard Mass transfer packing
US3282432A (en) * 1963-02-18 1966-11-01 Greenleaf Entpr Inc Multiple unit backwashing filter
US3340341A (en) * 1963-07-01 1967-09-05 Dow Chemical Co Method of preparing grids
US3312348A (en) * 1963-10-31 1967-04-04 Greenleaf Entpr Inc Multiple unit backwashing gravity flow filter
US3302372A (en) * 1964-04-17 1967-02-07 Armour Agricult Chem Gas scrubbing process and apparatus
US3430935A (en) * 1965-10-23 1969-03-04 Leo Lawrence Garrett Trickling bar assembly for blow-out towers
US3543937A (en) * 1968-08-02 1970-12-01 Joseph M Choun Filter media
US3589518A (en) * 1969-03-06 1971-06-29 Ircha Inst National De Rech Ch Packing materials especially for biological filters
US3661262A (en) * 1970-08-25 1972-05-09 Oceanography Mariculture Ind Filtration and circulation system for maintaining water quality in mariculture tank
US3792571A (en) * 1971-04-02 1974-02-19 Showa Denko Kk Method and apparatus for purifying waste gas
US3810348A (en) * 1972-01-07 1974-05-14 American Air Filter Co Scrubber arrangement
US4002705A (en) * 1972-03-01 1977-01-11 Mass Transfer Limited Fluid-fluid contact apparatus
US3959419A (en) * 1973-09-06 1976-05-25 Fritz W. Glitsch & Sons, Inc. Vapor-liquid contact method
US3969447A (en) * 1973-10-18 1976-07-13 Fritz W. Glitsch & Sons, Inc. Grids for fluid contact apparatus
US3966608A (en) * 1974-03-01 1976-06-29 Ecodyne Corporation Liquid treatment apparatus
US4045344A (en) * 1974-04-29 1977-08-30 Ishigaki Kiko Co., Ltd. Apparatus for treating waste water
US4122011A (en) * 1975-05-21 1978-10-24 Norton Company Trickling filter media for biological filters
US4182268A (en) * 1976-08-26 1980-01-08 Linde Aktiengesellschaft Breeding of aquatic animals in a controlled environment
US4200532A (en) * 1978-06-07 1980-04-29 Ishigaki Kiko Co., Ltd. Wastewater treatment apparatus
US4196079A (en) * 1978-12-29 1980-04-01 Harsco Corporation Pleated filter underdrain, method and apparatus
US4231863A (en) * 1979-04-26 1980-11-04 Sutphin Eldon M Method and apparatus for treating water
US4333893A (en) * 1980-01-23 1982-06-08 Clyde Robert A High area contactor
US4382046A (en) * 1981-09-22 1983-05-03 Ceramic Cooling Tower Company Water cooling tower with layers of multi-cell tiles and spacers
US4481155A (en) * 1983-10-19 1984-11-06 Ceramic Cooling Tower Company Multi-cell tiles with openings for use in a liquid cooling tower
US4599174A (en) * 1984-02-27 1986-07-08 Polybac Corporation Submerged fixed film biological treatment system
US4793934A (en) * 1987-04-22 1988-12-27 Signal Environmental Systems, Inc. Method for enhancing the separation capacity of a multi-bed filtration system
US4863606A (en) * 1987-12-11 1989-09-05 Ryall Ronald W Waste water treating process
US4929349A (en) * 1988-08-24 1990-05-29 Beckman William J Bio-filtration apparatus and method for wastewater treatment
US4948402A (en) * 1988-12-09 1990-08-14 Davis Water & Waste Industries, Inc. Modular air scrubber system
USRE35234E (en) * 1988-12-09 1996-05-14 Davis Water & Waste Industries, Inc. Modular air scrubber system
US5030353A (en) * 1989-01-13 1991-07-09 Stuth William L Secondary sewage treatment system
US5200081A (en) * 1989-01-13 1993-04-06 Stuth William L Secondary sewage treatment system
US5277848A (en) * 1989-03-08 1994-01-11 Glitsch, Inc. Method and apparatus for downcomer tray operation
US5308479A (en) * 1989-05-26 1994-05-03 Isamu Iwai Sewage disposal apparatus employing circulating filter media
US5032294A (en) * 1990-03-13 1991-07-16 Schulz Christopher R Multi-cell gravity filter with central control chamber
US5387335A (en) * 1990-11-21 1995-02-07 Iwai; Isamu Filter circulating type sewage disposal apparatus
US5137645A (en) * 1991-06-28 1992-08-11 Infilco Degremont Inc. Declining rate filter systems and methods
US5217616A (en) * 1991-12-06 1993-06-08 Allied-Signal Inc. Process and apparatus for removal of organic pollutants from waste water
US5227055A (en) * 1992-01-15 1993-07-13 Cornell Research Foundation, Inc. Aquaculture water treatment system including combined rotating biological contactor and evaporative cooler
US5204027A (en) * 1992-02-04 1993-04-20 Armstrong Charles M Fluid contact panels
US5326503A (en) * 1992-07-30 1994-07-05 Mitsubishi Jukogyo Kabushiki Kaisha Latticed packing member for gas-liquid contactors
US6391448B1 (en) * 1993-06-04 2002-05-21 United States Filter Corporation Liquid purification beds and beads therefor
US5413749A (en) * 1993-06-04 1995-05-09 Wheelabrator Engineered Systems Inc. Process of making beads for a liquid purification bed
US5558763A (en) * 1993-06-24 1996-09-24 Hitachi Plant Engineering & Construction Co., Ltd. Sewage treatment system with air jetting means
US5573663A (en) * 1994-01-10 1996-11-12 Junius; John H. Fluid filter using floating media
US5945005A (en) * 1994-01-10 1999-08-31 Junius; John H. Fluid filter using floating media
US5766488A (en) * 1994-05-12 1998-06-16 United States Filter Corporation Method and apparatus for water treatment
US6090277A (en) * 1996-06-26 2000-07-18 Gb. Odobez S.R.L. Reactor for the depuration of polluted waste waters
US6080304A (en) * 1997-02-27 2000-06-27 Gex Corporation Clarifying device for use in an aquarium
US6890431B1 (en) * 2000-02-18 2005-05-10 The F. B. Leopold Co., Inc. Buoyant media flotation
US7037432B2 (en) * 2000-02-18 2006-05-02 The F.B. Leopold Co., Inc. Buoyant media flotation
US6890439B2 (en) * 2000-05-22 2005-05-10 Dowmus Pty. Ltd. Biolytic filtration
US6524849B1 (en) * 2001-08-23 2003-02-25 Bio-Reaction Industries, Llc Biological filter structures
US20030230542A1 (en) * 2002-06-13 2003-12-18 United States Filter Corporation Flow splitting weir
US6849180B2 (en) * 2002-06-13 2005-02-01 Usfilter Corporation Flow splitting weir
US20050067357A1 (en) * 2002-06-13 2005-03-31 U.S. Filter Corporation Flow splitting weir
US7014783B2 (en) * 2002-06-13 2006-03-21 Usfilter Corporation Flow splitting weir
US20030230246A1 (en) * 2002-06-14 2003-12-18 Cornell Research Foundation, Inc. Cellular microbead filter for use in water recirculating system
US6666965B1 (en) * 2002-06-14 2003-12-23 Cornell Research Foundation, Inc. Cellular microbead filter for use in water recirculating system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050211644A1 (en) * 2004-03-24 2005-09-29 Aquatic Advisors, Llc Mixed bed trickling reactor using microbeads
US7785479B1 (en) * 2007-05-01 2010-08-31 Michael Hays Hosford Apparatus and method of separating
CN103663682A (en) * 2012-09-24 2014-03-26 钱阳 Split-level superimposed biological filtration and oxygenation device

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US6666965B1 (en) 2003-12-23
CA2488211A1 (en) 2003-12-24

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