WO2008051546A2 - Infiltration/inflow control for membrane bioreactor - Google Patents

Infiltration/inflow control for membrane bioreactor Download PDF

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Publication number
WO2008051546A2
WO2008051546A2 PCT/US2007/022493 US2007022493W WO2008051546A2 WO 2008051546 A2 WO2008051546 A2 WO 2008051546A2 US 2007022493 W US2007022493 W US 2007022493W WO 2008051546 A2 WO2008051546 A2 WO 2008051546A2
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WIPO (PCT)
Prior art keywords
treatment
flow
zone
treatment system
membrane
Prior art date
Application number
PCT/US2007/022493
Other languages
French (fr)
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WO2008051546A3 (en
Inventor
George W. Smith
Dennis J. Barnes
Original Assignee
Siemens Water Technologies Corp.
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Filing date
Publication date
Application filed by Siemens Water Technologies Corp. filed Critical Siemens Water Technologies Corp.
Priority to US12/447,084 priority Critical patent/US8293098B2/en
Publication of WO2008051546A2 publication Critical patent/WO2008051546A2/en
Publication of WO2008051546A3 publication Critical patent/WO2008051546A3/en

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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
    • C02F3/02—Aerobic processes
    • C02F3/12—Activated sludge processes
    • C02F3/1236—Particular type of activated sludge installations
    • C02F3/1268—Membrane bioreactor systems
    • 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
    • C02F3/121—Multistep 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
    • C02F3/30—Aerobic and anaerobic processes
    • 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 present invention relates to a system and method for treating wastewater, and more particularly to a wastewater treatment system and method utilizing a membrane bioreactor.
  • membrane bioreactors combining biological and physical processes in one stage promise to be more compact, efficient and economic.
  • Membrane bioreactors are typically sized to accommodate community and large-scale sewage treatment. A need has been found for these systems to periodically handle large flows of influent caused by peak rain events during storms and the like.
  • the invention relates to a system and method of treating wastewater.
  • a wastewater treatment system includes a first treatment zone fluidly connected to one or more further treatment zones.
  • a membrane module comprising a filter membrane is positioned in or fluidly connected to the further treatment zone.
  • a gravity settling device is fluidly connected to the first treatment zone to receive overflow therefrom.
  • Another embodiment is directed to a method of treating wastewater which includes flowing a wastewater through one or more treatment zones to produce a fluid product which is passed through a filter membrane to produce a concentrated mixed liquor and a filtrate, returning at least a portion of the concentrated mixed liquor to at least one of said treatment zones, when the flow of wastewater water exceeds a predetermined level, flowing a portion of said returned mixed liquor to a gravity settling device and clarifying the mixed liquor within the gravity settling device.
  • the process may use multiple reactors in series, with the ability to maintain different food to micro-organism ratios and different dissolved oxygen concentrations in each reactor.
  • the sludge separated from the mixed liquor in the gravity settling device is returned to a reactor downstream of the reactor feeding the gravity settling device.
  • FIG. 1 illustrates a system in accordance with one embodiment of the invention
  • FIG. 2 illustrates a system in accordance with another embodiment of the invention.
  • This invention is not limited in its application to the details of construction and the arrangement of components set forth in the following description or illustrated in the drawing. The invention is capable of other embodiments and of being practiced or of being carried out in various ways. Also, the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting. The use of "including,” “comprising,” or “having,” “containing,” “involving,” and variations thereof herein, is meant to encompass the items listed thereafter and equivalents thereof as well as additional items.
  • This invention may be directed to wastewater treatment systems utilizing membrane bioreactors designed to treat wastewater flows as low as 25,000 gallons per day, or peak flows as high as about 100 million gallons per day (MGD) or greater.
  • the wastewater treatment system is designed to treat an average flow of 12 MGD and a peak wastewater flow of about 30 MGD. It will be appreciated these flow volumes are merely exemplary and in no way intended to restrict the application of the invention which may be applied over a much wider range of flow.
  • Wastewater defines a stream of waste from a residential or community source, having pollutants of biodegradable material, inorganic or organic compounds capable of being decomposed by bacteria, flowing into the wastewater treatment system.
  • a "wastewater treatment system” is a system, typically a biological treatment system, having a biomass population of bacterial microorganisms of a diversity of types of bacteria, used to digest biodegradable material.
  • the biomass requires an environment that provides the proper conditions for growth.
  • One embodiment of the present invention includes bioreactor having one or more treatment zones.
  • treatment zone is used to denote an individual treatment region. Individual treatment regions may be housed in a single vessel with one or more compartments. Alternatively, individual treatment regions may be housed in separate vessels, wherein a different treatment is carried out in separate vessels.
  • the treatment zone i.e. the vessel or compartment, may be sized and shaped according to a desired application and volume of wastewater to be treated.
  • the wastewater treatment system may include a fluidizable media housed in a first treatment zone.
  • the fluidizable media may comprise biomass carriers designed to immobilize anoxic organisms.
  • the biomass carriers may be formed of any material suitable to support organisms and to remain fluidized under operating conditions.
  • the fluidizable media has a specific gravity substantially the same as that of water.
  • the fluidizable media has a surface area adequate to allow denitrifying bacteria to grow, which may enhance the efficiency of the anoxic reaction to remove nitrogen.
  • Any volume of fluidizable media may be utilized within the first treatment zone for a particular purpose. For example, a maximum volume of fluidized media may be used to substantially fill the first treatment zone, or a lesser volume of fluidized material may be used to fill a portion of the first treatment zone.
  • one or more porous or permeable membranes may be used to treat fluid flow from treatment zones and in some embodiments may be positioned within a treatment zone.
  • the membrane may have any configuration suitable for a particular purpose, such as sheet or hollow tube.
  • the membrane may be formed of any material (natural or synthetic) suitable for a particular filtration process.
  • the membrane is formed of polymeric hollow fibers.
  • One or more membranes may be positioned in one or more membrane modules.
  • the membrane modules may have any shape and cross sectional area suitable for use in a desired application, for example, square, rectangular, or cylindrical. In one embodiment, the membrane modules are rectangular.
  • one or more membrane modules may be positioned in a treatment zone in such a way as to be completely submerged by fluid during operation.
  • the membrane module may be positioned vertically, horizontally, or at an angle within the second treatment zone.
  • Multiple membrane modules may be positioned adjacent one another, or located at predetermined positions within the second treatment zone and may, but need not, be positioned in the same plane as others or parallel to one another.
  • hollow fiber membranes may be positioned horizontally within the treatment zone.
  • One or more membrane modules may be mounted directly to the vessel or compartment which forms a treatment zone.
  • one or more membrane modules may be mounted to a module support which may be removably attached to the vessel or compartment forming the treatment zone.
  • a plurality of membrane modules are mounted to a module support rack to facilitate membrane maintenance and/or replacement.
  • membrane modules having vertical partitions may be positioned horizontally.
  • the treatment zone may include an aeration system to suspend solids in wastewater or resultant concentrated mixed liquor contained within the second treatment zone, and/or to assist water transfer through the membrane.
  • the aeration system may produce fine bubbles, coarse bubbles, a jet stream of gas, a jet of gas and fluid, and combinations thereof.
  • the aeration system may be positioned in any suitable location within the treatment zone. In one embodiment, aeration may be provided along a length of one or more membrane modules horizontally positioned.
  • the wastewater treatment system may include one or more pretreatment units, such as to collect solids and/or to remove phosphorous.
  • the pretreatment unit is a trap to remove floating solids, such as grease, and other gross organic solids until they become more soluble, and is positioned upstream of the first treatment zone.
  • the trap may be sized to provide a volume of about 1 x FF (1 forward feed).
  • the pretreatment unit is a chemical phosphorous removal unit.
  • the wastewater treatment system may further include an equalization tank and/or a reserve storage tank fluidly connected to the bioreactor.
  • the tank may be sized to accommodate fluctuations in wastewater generation to normalize flow into the bioreactor.
  • the equalization capacity may be equal to about 8 hours or about 33% of the FF.
  • the same tank may also be sized to provide reserve capacity for an emergency such as a power failure, and may have a reserve capacity of about 16 hours or about 67% of the FF.
  • the tank is sized to provide a volume of about 1 x FF to provide for equalization and a reserve.
  • FIG. 1 there is illustrated one embodiment of the present wastewater treatment system.
  • the figure shows a bioreactor 10 comprising a number of treatment tanks 11 to 14 connected in series with the same or different environments maintained in each tank and a membrane filter 16 connected thereto.
  • the tanks are fluidly coupled in series to each other. Possible environments in the tanks could include anaerobic, anoxic, aerated anoxic, or aerobic depending on the effluent water quality requirements for each specific application.
  • a clarifier 15 is fluidly connected to tanks 11 and 12 by fluid inflow line 17 and fluid outflow line 18.
  • a fluid feedback line 19 is provided from the feed side of the membrane filter 16 to tanks 11 and 12.
  • Wastewater is fed into the bioreactor 10 through influent line 20.
  • Effluent is withdrawn from the bioreactor 10 through effluent line 21 coupled to the filtrate side of the membrane filter 16. Clarifier effluent is flowed from the clarifier 15 through clarifier effluent line 22.
  • the inflow to tank 11 is the average design flow rate Q and all flow is directed through the treatment tanks to the membrane filter 16.
  • no overflow is provided to clarifier 15 from tank 11 and there is no feedback of mixed liquor to tank 12.
  • a portion of the mixed liquor flow (typically a flow equal to around 1 to 4 times the average design flow, Q) into tank 11 is diverted to the clarifier 15 through inflow line 17 with the remainder flowing from tank 11 to tank 12.
  • the mixed liquor feedback from the membrane filter 16 to tank 11 is also reduced (typically to about 0.5 to 2 times the average design flow, Q) by diverting a portion of the flow to tank 12.
  • the flow from tank 11 into the clarifier 15 is selected to allow reliable gravity settling of solids material within the clarifier 15.
  • Activated sludge is returned from the clarifier 15 through outflow line 18 to tank 12 (typically a flow equal to about 0.25 to 1 times the average design flow, Q). Clarified effluent is withdrawn from the clarifier 15 through clarifier effluent line 22.
  • FIG. 2 by way of example only, there is illustrated another embodiment of the present wastewater treatment system in the form of a bioreactor 25. It will be appreciated that this embodiment functions similarly to the embodiment disclosed in Fig. 1, although a fluid feedback line 26 is now provided from the feed side of the membrane filter 16 to tank 12 and a pump 27 with associated feedback lines 28 and 29 interconnecting tanks 11 and 12 for providing feedback therebetween.
  • the speed of the pump can control the rate of feedback from treatment tank 12 to treatment tank 1, and is used to control the concentration of mixed liquor in tank 11 such that reliable gravity settling of solids material within the clarifier 15 can be achieved.
  • this is an alternative to splitting the fluid feedback line 19 between reactors 11 and 12.
  • an automated control process can include:
  • effluent flow from one or more initial treatment tanks is split, whereby part of the flow is diverted to the clarifiers 18 and the remainder is treated by a membrane filter 16.
  • the flow to the membranes is typically controlled by pumps, and is based on the liquid level in the furthest upstream treatment tank.
  • flow to the clarifiers can be regulated by a weir in the furthest upstream treatment tank. In this example, if the influent flow rate exceeds the rate that the membranes can handle, the liquid level in the treatment tank will rise and liquid will start to flow over the weir and travel to the clarifiers.
  • the weir can be a fixed weir.
  • the weir is either manually adjustable, or automatically adjustable based on an influent flow meter signal or other process measurement.
  • the flow split between the clarifiers and the membranes can be regulated using valves, gates, or other suitable devices known to a person skilled in the art.
  • flow to the membrane tanks is caused by gravity and a return stream back to the treatment tanks uses a pump.
  • This embodiment requires a means for restricting the flow to the membrane tanks and thereby to back the liquid up into the upstream treatment tanks where it can be directed to the clarifiers. It would be appreciated that a means for restricting the flow to the membrane tanks can include an adjustable weir, gate, valve or other suitable devices known to a person skilled in the art.
  • feedback flow provided from the feed side of the membrane filter 16 is split whereby part of the flow is diverted to upstream treatment tanks that feed the clarifiers 15 and the remainder is sent to downstream treatment tanks that flow to the membrane filter 16.
  • influent flow rate and the flow rate being treated by the membranes can be measured, and the proportion of the total flow being treated by the clarifiers can be calculated.
  • the desired percentage of the fluid feedback provided from the feed side of the membrane filter to be sent to the clarifiers can be calculated by a programmable logic controller (PLC) using a mass balance equation.
  • PLC programmable logic controller
  • this flow split can be calculated for substantially maintaining a target MLSS concentration in the stream being sent to the clarifiers.
  • the mass balance equation can be a function of at least four variables, being the average TSS concentration in the mixed liquor (user input or as measured with TSS probes), the desired target concentration in the upstream treatment tanks (which may or may not be verified with a TSS probe), the influent flow to the plant, and the percentage of that flow being treated by the final clarifiers.
  • the invention provides an efficient means of dealing with large inflows without compromising the operation of the membrane bioreactor.

Abstract

A wastewater treatment system comprising: a first treatment zone (11) fluidly connected to one or more further treatment zones (12-14), a membrane module (16) comprising a filter membrane is positioned in or fluidly connected to the further treatment zone; and a gravity settling device (15) fluidly connected to the first treatment zone (11) to receive overflow therefrom. A method of treating wastewater comprising flowing wastewater through one or more treatment zones (11-14) to produce a fluid product which is passed through a filter membrane (16) to produce a concentrated mixed liquor and a filtrate; returning at least a portion of the concentrated mixed liquor to at least one of the treatment zones (11); when the flow of wastewater water exceeds a predetermined level, flowing a portion of the returned mixed liquor to a gravity settling device (15) and clarifying the mixed liquor within the gravity settling device (15).

Description

INFILTRATION/INFLOW CONTROL FOR MEMBRANE BIOREACTOR
BACKGROUND OF INVENTION
1. Field of Invention
The present invention relates to a system and method for treating wastewater, and more particularly to a wastewater treatment system and method utilizing a membrane bioreactor.
2. Discussion of Related Art
The importance of membrane for treatment of waste water is growing rapidly. With the arrival of submerged membrane processes where membrane modules are immersed in a large feed tank and filtrate is collected typically through suction applied to the filtrate side of the membrane, membrane bioreactors (MBRs) combining biological and physical processes in one stage promise to be more compact, efficient and economic. Membrane bioreactors are typically sized to accommodate community and large-scale sewage treatment. A need has been found for these systems to periodically handle large flows of influent caused by peak rain events during storms and the like.
SUMMARY OF INVENTION
In accordance with one or more embodiments, the invention relates to a system and method of treating wastewater.
In one embodiment, a wastewater treatment system includes a first treatment zone fluidly connected to one or more further treatment zones. A membrane module comprising a filter membrane is positioned in or fluidly connected to the further treatment zone. A gravity settling device is fluidly connected to the first treatment zone to receive overflow therefrom.
Another embodiment is directed to a method of treating wastewater which includes flowing a wastewater through one or more treatment zones to produce a fluid product which is passed through a filter membrane to produce a concentrated mixed liquor and a filtrate, returning at least a portion of the concentrated mixed liquor to at least one of said treatment zones, when the flow of wastewater water exceeds a predetermined level, flowing a portion of said returned mixed liquor to a gravity settling device and clarifying the mixed liquor within the gravity settling device.
Preferably, the process may use multiple reactors in series, with the ability to maintain different food to micro-organism ratios and different dissolved oxygen concentrations in each reactor. For preference, the sludge separated from the mixed liquor in the gravity settling device is returned to a reactor downstream of the reactor feeding the gravity settling device.
BRIEF DESCRIPTION OF DRAWINGS
A preferred embodiment of the invention will now be described, by way of example only, with reference to the accompanying drawing in which:
FIG. 1 illustrates a system in accordance with one embodiment of the invention; and
FIG. 2 illustrates a system in accordance with another embodiment of the invention.
The accompanying drawings are not intended to be drawn to scale.
DETAILED DESCRIPTION
This invention is not limited in its application to the details of construction and the arrangement of components set forth in the following description or illustrated in the drawing. The invention is capable of other embodiments and of being practiced or of being carried out in various ways. Also, the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting. The use of "including," "comprising," or "having," "containing," "involving," and variations thereof herein, is meant to encompass the items listed thereafter and equivalents thereof as well as additional items. This invention may be directed to wastewater treatment systems utilizing membrane bioreactors designed to treat wastewater flows as low as 25,000 gallons per day, or peak flows as high as about 100 million gallons per day (MGD) or greater. In one embodiment the wastewater treatment system is designed to treat an average flow of 12 MGD and a peak wastewater flow of about 30 MGD. It will be appreciated these flow volumes are merely exemplary and in no way intended to restrict the application of the invention which may be applied over a much wider range of flow.
"Wastewater," as used herein, defines a stream of waste from a residential or community source, having pollutants of biodegradable material, inorganic or organic compounds capable of being decomposed by bacteria, flowing into the wastewater treatment system. As used herein, a "wastewater treatment system" is a system, typically a biological treatment system, having a biomass population of bacterial microorganisms of a diversity of types of bacteria, used to digest biodegradable material. Notably, the biomass requires an environment that provides the proper conditions for growth.
One embodiment of the present invention includes bioreactor having one or more treatment zones. As used herein, the phrase "treatment zone" is used to denote an individual treatment region. Individual treatment regions may be housed in a single vessel with one or more compartments. Alternatively, individual treatment regions may be housed in separate vessels, wherein a different treatment is carried out in separate vessels. The treatment zone, i.e. the vessel or compartment, may be sized and shaped according to a desired application and volume of wastewater to be treated.
The wastewater treatment system may include a fluidizable media housed in a first treatment zone. The fluidizable media may comprise biomass carriers designed to immobilize anoxic organisms. The biomass carriers may be formed of any material suitable to support organisms and to remain fluidized under operating conditions. In one embodiment, the fluidizable media has a specific gravity substantially the same as that of water. In another embodiment the fluidizable media has a surface area adequate to allow denitrifying bacteria to grow, which may enhance the efficiency of the anoxic reaction to remove nitrogen. Any volume of fluidizable media may be utilized within the first treatment zone for a particular purpose. For example, a maximum volume of fluidized media may be used to substantially fill the first treatment zone, or a lesser volume of fluidized material may be used to fill a portion of the first treatment zone.
According to one embodiment of the invention, one or more porous or permeable membranes may be used to treat fluid flow from treatment zones and in some embodiments may be positioned within a treatment zone. The membrane may have any configuration suitable for a particular purpose, such as sheet or hollow tube. The membrane may be formed of any material (natural or synthetic) suitable for a particular filtration process. In one embodiment, the membrane is formed of polymeric hollow fibers.
One or more membranes may be positioned in one or more membrane modules. The membrane modules may have any shape and cross sectional area suitable for use in a desired application, for example, square, rectangular, or cylindrical. In one embodiment, the membrane modules are rectangular.
According to one embodiment, one or more membrane modules may be positioned in a treatment zone in such a way as to be completely submerged by fluid during operation. For example, the membrane module may be positioned vertically, horizontally, or at an angle within the second treatment zone. Multiple membrane modules may be positioned adjacent one another, or located at predetermined positions within the second treatment zone and may, but need not, be positioned in the same plane as others or parallel to one another. In one embodiment, hollow fiber membranes may be positioned horizontally within the treatment zone. One or more membrane modules may be mounted directly to the vessel or compartment which forms a treatment zone. Alternatively, one or more membrane modules may be mounted to a module support which may be removably attached to the vessel or compartment forming the treatment zone. In one embodiment, a plurality of membrane modules are mounted to a module support rack to facilitate membrane maintenance and/or replacement. In another embodiment, membrane modules having vertical partitions may be positioned horizontally. The treatment zone may include an aeration system to suspend solids in wastewater or resultant concentrated mixed liquor contained within the second treatment zone, and/or to assist water transfer through the membrane. The aeration system may produce fine bubbles, coarse bubbles, a jet stream of gas, a jet of gas and fluid, and combinations thereof. The aeration system may be positioned in any suitable location within the treatment zone. In one embodiment, aeration may be provided along a length of one or more membrane modules horizontally positioned.
According to another embodiment, the wastewater treatment system may include one or more pretreatment units, such as to collect solids and/or to remove phosphorous. In one embodiment the pretreatment unit is a trap to remove floating solids, such as grease, and other gross organic solids until they become more soluble, and is positioned upstream of the first treatment zone. The trap may be sized to provide a volume of about 1 x FF (1 forward feed). In another embodiment, the pretreatment unit is a chemical phosphorous removal unit.
According to another embodiment, the wastewater treatment system may further include an equalization tank and/or a reserve storage tank fluidly connected to the bioreactor. The tank may be sized to accommodate fluctuations in wastewater generation to normalize flow into the bioreactor. For example, the equalization capacity may be equal to about 8 hours or about 33% of the FF. The same tank may also be sized to provide reserve capacity for an emergency such as a power failure, and may have a reserve capacity of about 16 hours or about 67% of the FF. In one embodiment, the tank is sized to provide a volume of about 1 x FF to provide for equalization and a reserve.
Referring to the Fig. 1 there is illustrated one embodiment of the present wastewater treatment system. The figure shows a bioreactor 10 comprising a number of treatment tanks 11 to 14 connected in series with the same or different environments maintained in each tank and a membrane filter 16 connected thereto. The tanks are fluidly coupled in series to each other. Possible environments in the tanks could include anaerobic, anoxic, aerated anoxic, or aerobic depending on the effluent water quality requirements for each specific application. A clarifier 15 is fluidly connected to tanks 11 and 12 by fluid inflow line 17 and fluid outflow line 18. A fluid feedback line 19 is provided from the feed side of the membrane filter 16 to tanks 11 and 12. Wastewater is fed into the bioreactor 10 through influent line 20. Effluent is withdrawn from the bioreactor 10 through effluent line 21 coupled to the filtrate side of the membrane filter 16. Clarifier effluent is flowed from the clarifier 15 through clarifier effluent line 22.
In one mode of operation, during average inflow conditions, the inflow to tank 11 is the average design flow rate Q and all flow is directed through the treatment tanks to the membrane filter 16. A portion of the mixed liquor, typically a flow equal to around 2 to 8 times the average design flow, Q, is returned to treatment tank 11. In this mode of operation no overflow is provided to clarifier 15 from tank 11 and there is no feedback of mixed liquor to tank 12.
In a second mode of operation, during wet weather or high inflow conditions, a portion of the mixed liquor flow (typically a flow equal to around 1 to 4 times the average design flow, Q) into tank 11 is diverted to the clarifier 15 through inflow line 17 with the remainder flowing from tank 11 to tank 12. The mixed liquor feedback from the membrane filter 16 to tank 11 is also reduced (typically to about 0.5 to 2 times the average design flow, Q) by diverting a portion of the flow to tank 12. The flow from tank 11 into the clarifier 15 is selected to allow reliable gravity settling of solids material within the clarifier 15.
Activated sludge is returned from the clarifier 15 through outflow line 18 to tank 12 (typically a flow equal to about 0.25 to 1 times the average design flow, Q). Clarified effluent is withdrawn from the clarifier 15 through clarifier effluent line 22.
Referring to Fig. 2 by way of example only, there is illustrated another embodiment of the present wastewater treatment system in the form of a bioreactor 25. It will be appreciated that this embodiment functions similarly to the embodiment disclosed in Fig. 1, although a fluid feedback line 26 is now provided from the feed side of the membrane filter 16 to tank 12 and a pump 27 with associated feedback lines 28 and 29 interconnecting tanks 11 and 12 for providing feedback therebetween. In this embodiment the speed of the pump can control the rate of feedback from treatment tank 12 to treatment tank 1, and is used to control the concentration of mixed liquor in tank 11 such that reliable gravity settling of solids material within the clarifier 15 can be achieved. It will be appreciated that, referring Fig. 1, this is an alternative to splitting the fluid feedback line 19 between reactors 11 and 12.
It is often advantageous to include a means of automated control. By way of example, an automated control process can include:
1) Splitting Effluent flow from one or more initial treatment tanks, whereby part of the flow is diverted to the clarifiers 18 and the remainder is treated by the membrane filter 16.
2) Splitting eedback flow provided from the feed side of the membrane filter 16, whereby part of the flow is diverted to upstream treatment tanks that feed the clarifiers 15 and the remainder is sent to downstream treatment tanks that flow to the membrane filter 16.
In an embodiment, by way of example only, effluent flow from one or more initial treatment tanks is split, whereby part of the flow is diverted to the clarifiers 18 and the remainder is treated by a membrane filter 16. It will be appreciated that the flow to the membranes is typically controlled by pumps, and is based on the liquid level in the furthest upstream treatment tank. It will be further appreciated that flow to the clarifiers can be regulated by a weir in the furthest upstream treatment tank. In this example, if the influent flow rate exceeds the rate that the membranes can handle, the liquid level in the treatment tank will rise and liquid will start to flow over the weir and travel to the clarifiers. The weir can be a fixed weir. Preferably the weir is either manually adjustable, or automatically adjustable based on an influent flow meter signal or other process measurement. It will be further appreciated that, in another embodiments, the flow split between the clarifiers and the membranes can be regulated using valves, gates, or other suitable devices known to a person skilled in the art.
In another embodiment, flow to the membrane tanks is caused by gravity and a return stream back to the treatment tanks uses a pump. This embodiment requires a means for restricting the flow to the membrane tanks and thereby to back the liquid up into the upstream treatment tanks where it can be directed to the clarifiers. It would be appreciated that a means for restricting the flow to the membrane tanks can include an adjustable weir, gate, valve or other suitable devices known to a person skilled in the art.
In an embodiment, by way of example, feedback flow provided from the feed side of the membrane filter 16 is split whereby part of the flow is diverted to upstream treatment tanks that feed the clarifiers 15 and the remainder is sent to downstream treatment tanks that flow to the membrane filter 16. For example, influent flow rate and the flow rate being treated by the membranes can be measured, and the proportion of the total flow being treated by the clarifiers can be calculated. By way of example, the desired percentage of the fluid feedback provided from the feed side of the membrane filter to be sent to the clarifiers can be calculated by a programmable logic controller (PLC) using a mass balance equation. For example, this flow split can be calculated for substantially maintaining a target MLSS concentration in the stream being sent to the clarifiers. It would be appreciated that the mass balance equation can be a function of at least four variables, being the average TSS concentration in the mixed liquor (user input or as measured with TSS probes), the desired target concentration in the upstream treatment tanks (which may or may not be verified with a TSS probe), the influent flow to the plant, and the percentage of that flow being treated by the final clarifiers.
Accordingly, the invention provides an efficient means of dealing with large inflows without compromising the operation of the membrane bioreactor.
Having thus described several aspects of at least one embodiment of this invention, it should be apparent to those skilled in the art that the foregoing is merely illustrative and not limiting, having been presented by way of example only. Numerous modification and other embodiments are within the scope of the invention. In particular, although many embodiments presented herein involve specific combinations of method acts or system elements, it should be understood that those acts and those elements may be combined in other ways to accomplish the same objectives. Further, acts, elements, and features discusses only in connection with one embodiment are not intended to be excluded from a similar role in other embodiments.
It is to be appreciated that various alterations, modifications, and improvements can readily occur to those skilled in the art and that such alterations, modifications, and improvements are intended to be part of the disclosure and within the spirit and scope of the invention.
Moreover, it should also be appreciated that the invention is directed to each feature, system, subsystem, or technique described herein and any combination of two or more features, systems, subsystems, and/or method, if such features, systems, subsystems, and techniques are not mutually inconsistent, is considered to be within the scope of the invention as described.
Those skilled in the art should appreciate that the parameters and configuration described herein are exemplary and that actual parameters and/or configurations will depend on the specific application in which the systems and techniques of the invention are used. Those skilled in the art should also recognize or be able to ascertain, using no more than routing experimentation, equivalents to the specific embodiments of the invention. It is therefore to be understood that the embodiments described herein are presented by way of example only and that, within the scope of the invention described and equivalents thereto; the invention may be practice d otherwise than as specifically described.

Claims

CLAIMS:
1. A wastewater treatment system comprising: a first treatment zone fluidly connected to one or more further treatment zones; a membrane module comprising a filter membrane is positioned in or fluidly connected to the further treatment zone; and a gravity settling device fluidly connected to the first treatment zone to receive overflow therefrom.
2. A treatment system according to claim 1 comprising a plurality of treatment zones in series, with each treatment zone having the ability to maintain different food to micro-organism ratios and different dissolved oxygen concentrations.
3. A treatment system according to claim 1 further comprising an aeration system provided in one or more of the further treatment zones.
4. A treatment system according to claim 1 wherein the filter membrane comprises a porous hollow fiber membrane.
5. A treatment system according to claim 1 wherein the first treatment zone includes a fluidized media.
6. A treatment system according to claim 1 wherein the gravity settling device comprises a clarifier.
7. A treatment system according to claim 1 further comprising a equalization tank fluidly connected to the system.
8. A treatment system according to claim 1 comprising a pretreatment unit.
9. A treatment system according to claim 8 wherein the pretreatment unit comprises a floating solids trap and/or a chemical phosphorus removal unit.
10. A treatment system according to claim 1 wherein the treatment zones comprise one or more of the following: an anaerobic zone, an anoxic zone, an aerated anoxic zone or an aerobic zone.
11. A treatment system according to claim 1 further comprising a fluid feedback line from a feed side of the membrane module to the first treatment zone and at least one of the further treatment zones.
12. A treatment system according to claim 1 further comprising: a first fluid feedback line from at least one of the further treatment zones and the first treatment zone; and a second fluid feedback line from a feed side of the membrane module to the at least one of the further treatment zones.
13. A treatment system according to claim 12 wherein the first fluid feedback line has an interconnecting pump.
14. A method of treating wastewater comprising: flowing a wastewater through one or more treatment zones to produce a fluid product which is passed through a filter membrane to produce a concentrated mixed liquor and a filtrate; returning at least a portion of the concentrated mixed liquor to at least one of the treatment zones; when the flow of wastewater water exceeds a predetermined level, flowing a portion of the returned mixed liquor to a gravity settling device and clarifying the mixed liquor within the gravity settling device.
15. The method according to claim 14 comprising returning sludge separated from the mixed liquor in the gravity settling device to a treatment zone downstream of the treatment zone feeding the gravity settling device.
16. The method according to claim 14 wherein the returned portion of the concentrated mix liquor is between about 2 times to about 8 times the average design flow of the system.
17. The method according to claim 14 wherein an effluent flow from one or more treatment tanks is split such that part of the flow is diverted to a clarifier and the remainder is treated by the filter membrane.
18. The method according to claim 17 wherein flow to the filter membrane is caused by gravity and wherein this flow is restricted such that liquid backs up in the upstream treatment zones.
19. The method according to claim 14 wherein a feedback flow from the feed side of the filter membrane is split such that part of the flow is diverted to an upstream treatment zone feeding a clarifier and the remainder is sent to a downstream treatment tanks that flows to the filter membrane.
20. The method according to claim 19 wherein the desired percentage of the feedback flow diverted to the clarifier is calculated by a programmable logic controller using a mass balance equation.
PCT/US2007/022493 2006-10-24 2007-10-23 Infiltration/inflow control for membrane bioreactor WO2008051546A2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113860654A (en) * 2021-10-29 2021-12-31 段润芳 Efficient sewage treatment method based on MBR (membrane bioreactor) membrane

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110253624A1 (en) * 2010-04-14 2011-10-20 Otv Sa Anaerobic digester-membrane bioreactor for treating a waste stream
US20130146541A1 (en) 2011-12-13 2013-06-13 Nxstage Medical, Inc. Fluid purification methods, devices, and systems
MX2017005167A (en) 2014-10-20 2017-11-23 Bionest Tech Inc Water treatment reactor.

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5626755A (en) * 1995-11-08 1997-05-06 Micronair, Inc. Method and apparatus for waste digestion using multiple biological processes
US5846425A (en) * 1994-07-22 1998-12-08 Whiteman; George R. Methods for treatment of waste streams
US20020185448A1 (en) * 1999-11-19 2002-12-12 Chisholm Robert D. Process and system for treatment of aqueous environments containing water soluble polymers
US20030111412A1 (en) * 2001-10-24 2003-06-19 Samsung Engineering Co., Ltd. Batch style wastewater treatment apparatus using biological filtering process and wastewater treatment method using the same
US20040000517A1 (en) * 2002-06-17 2004-01-01 Iasis Usa, Lc Tidal vertical flow wastewater treatment system and method
US20040007523A1 (en) * 2000-10-06 2004-01-15 Premier Wastewater International, Llc Apparatus and method for wastewater treatment with enhanced solids reduction (ESR)
US6723242B1 (en) * 1999-03-26 2004-04-20 Sumitomo Heavy Industries, Ltd. Method and apparatus for processing organic chlorine compounds

Family Cites Families (715)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US511995A (en) * 1894-01-02 Air and water purifier
US256008A (en) * 1882-04-04 Posoelain and china paste boxes
US285321A (en) * 1883-09-18 Pottery mold
US1997074A (en) * 1930-01-24 1935-04-09 John Stogdell Stokes Method of and apparatus for molding synthetic resinous articles
US2080783A (en) * 1932-03-09 1937-05-18 Celluloid Corp Method of molding thermoplastic materials
US2105700A (en) * 1936-07-13 1938-01-18 William D Ramage Process for purification of beverages
US2732357A (en) 1949-11-25 1956-01-24 Suspensions of polymeric chlorotri-
US2843038A (en) * 1954-01-06 1958-07-15 Robert O Manspeaker Bakery apparatus and method
US2926086A (en) * 1957-07-30 1960-02-23 Universal Oil Prod Co Stabilization of non-distilled alcoholic beverages and the resulting product
US3068655A (en) * 1959-12-01 1962-12-18 Standard Dredging Corp Mobile pneumatic breakwater
US3183191A (en) * 1960-04-19 1965-05-11 Hach Chemical Co Stain and rust removing composition
BE608328A (en) * 1960-09-19
GB996195A (en) 1961-08-03 1965-06-23 Aero Hydraulics Ltd Improvements in methods and apparatus for mixing and dispersing substances and for maintaining dispersions and emulsions
US3139401A (en) * 1962-01-05 1964-06-30 Hach Chemical Co Method for removing rust from water softeners
US3198636A (en) * 1962-06-08 1965-08-03 Norda Essential Oil And Chemic Preservation of wine
US3191674A (en) * 1963-06-18 1965-06-29 Westinghouse Electric Corp Shell-and-tube type heat exchangers
NL137371C (en) * 1963-08-02
NL136034C (en) * 1965-12-22
US3492698A (en) * 1965-12-22 1970-02-03 Du Pont Centrifugal casting apparatus for forming a cast wall member extending transversely across an elongated bundle of substantially parallel hollow filaments of a fluid permeation separation apparatus
US3462362A (en) * 1966-07-26 1969-08-19 Paul Kollsman Method of reverse osmosis
AT284384B (en) * 1967-04-15 1970-09-10 Ennio Carraro Hand tool for cleaning vertical flat surfaces, in particular window panes, glass walls or the like.
SE320270B (en) * 1967-11-04 1970-02-02 Inoue Michiro
US3556305A (en) * 1968-03-28 1971-01-19 Amicon Corp Composite membrane and process for making same
US3591010A (en) * 1968-06-10 1971-07-06 Pall Corp Filter having a microporous layer attached thereto
US3472765A (en) * 1968-06-10 1969-10-14 Dorr Oliver Inc Membrane separation in biological-reactor systems
US3625827A (en) * 1968-09-27 1971-12-07 Monsanto Co Water-soluble polymer-enzyme products
US3505215A (en) * 1968-10-10 1970-04-07 Desalination Systems Method of treatment of liquids by reverse osmosis
CH511629A (en) * 1969-03-27 1971-08-31 Brasco Sa Device for filtering a pressurized fluid
US3700561A (en) * 1969-08-11 1972-10-24 Pabst Brewing Co Recovery of enzymes
US3693406A (en) * 1970-01-26 1972-09-26 Air Intake Renu Method for inspecting filters
US3708071A (en) * 1970-08-05 1973-01-02 Abcor Inc Hollow fiber membrane device and method of fabricating same
US3700591A (en) * 1970-09-24 1972-10-24 Us Interior Cleaning of used membrane with oxalic acid
US3654147A (en) * 1971-03-16 1972-04-04 Biospherics Inc Nitrate removal from sewage
US3728256A (en) * 1971-06-22 1973-04-17 Abcor Inc Crossflow capillary dialyzer
US3763055A (en) * 1971-07-07 1973-10-02 Us Interior Microporous support for reverse osmosis membranes
GB1412983A (en) * 1971-11-30 1975-11-05 Debell & Richardson Method of producing porous plastic materials
US3795609A (en) * 1971-12-28 1974-03-05 Administrator Environmental Pr Reverse osmosis-neutralization process for treating mineral contaminated waters
US3791631A (en) * 1972-02-17 1974-02-12 Mm Ind Inc Method and apparatus for making colored expanded foam articles
US3804258A (en) * 1972-08-08 1974-04-16 V Okuniewski Filtering device
US3843809A (en) * 1972-08-23 1974-10-22 E Luck Manufacture of alcoholic beverages
US3955998A (en) * 1973-06-21 1976-05-11 Phillips Petroleum Company Aqueous gels for plugging fractures in subterranean formation and production of said aqueous gels
FR2236537B1 (en) * 1973-07-11 1977-12-23 Rhone Poulenc Ind
US3876738A (en) * 1973-07-18 1975-04-08 Amf Inc Process for producing microporous films and products
US3992301A (en) * 1973-11-19 1976-11-16 Raypak, Inc. Automatic flushing system for membrane separation machines such as reverse osmosis machines
US3968192A (en) * 1974-04-19 1976-07-06 The Dow Chemical Company Method of repairing leaky hollow fiber permeability separatory devices
US4105731A (en) * 1975-05-02 1978-08-08 Nippon Zeon Co., Ltd. Method of embedding an end of a bundle of thread-like bodies in a molding material and controlling capillary action by said material
JPS51128880A (en) * 1975-05-02 1976-11-10 Nippon Zeon Co Method of securing yarn bundle end to case
IT1040274B (en) * 1975-07-30 1979-12-20 Consiglio Nazionale Ricerche PROCEDURE FOR PREPARATION OF ANISOTROPIC MEMBRANES SUPPORTED FOR REVERSE OSMOSIS BASED ON SYNTHETIC POLYAMIDES
GB1496805A (en) * 1975-09-19 1978-01-05 Unilever Ltd Dithionite composition
US4105556A (en) * 1976-02-18 1978-08-08 Combustion Engineering, Inc. Liquid waste processing system
US4192750A (en) * 1976-08-09 1980-03-11 Massey-Ferguson Inc. Stackable filter head unit
US4247498A (en) * 1976-08-30 1981-01-27 Akzona Incorporated Methods for making microporous products
US4107043A (en) * 1977-03-03 1978-08-15 Creative Dispensing Systems, Inc. Inlet conduit fluid filter
JPS53108882A (en) 1977-03-04 1978-09-22 Kuraray Co Ltd Back washing method for hollow filament membrane
US4203848A (en) * 1977-05-25 1980-05-20 Millipore Corporation Processes of making a porous membrane material from polyvinylidene fluoride, and products
US4138460A (en) * 1977-06-10 1979-02-06 Cordis Dow Corp. Method for forming tubesheets on hollow fiber tows and forming hollow fiber bundle assemblies containing same
US4519909A (en) 1977-07-11 1985-05-28 Akzona Incorporated Microporous products
JPS6025194B2 (en) * 1977-08-04 1985-06-17 株式会社クラレ centrifugal gluing device
US4157899A (en) * 1977-10-11 1979-06-12 Cea Carter-Day Company Pulsed backflush air filter
US4183890A (en) * 1977-11-30 1980-01-15 Monsanto Company Method of cutting hollow filaments embedded in resinous mass
US4204961A (en) * 1978-03-15 1980-05-27 Cusato John Jr Filter apparatus with cleaning function
US4193780A (en) * 1978-03-20 1980-03-18 Industrial Air, Inc. Air filter construction
US4227295A (en) * 1978-07-27 1980-10-14 Baxter Travenol Laboratories, Inc. Method of potting the ends of a bundle of hollow fibers positioned in a casing
FR2420548A1 (en) * 1978-03-25 1979-10-19 Akzo Nv POLYURETHANES COATING MASS, ITS PREPARATION PROCESS AND ITS USE
MX152562A (en) * 1978-05-15 1985-08-29 Pall Corp IMPROVEMENTS TO THE PROCEDURE FOR PREPARING ALCOHOL INSOLUBLE, HYDROPHILIC AND UNCOATED POLYAMIDE RESIN MEMBRANES
US4315819A (en) * 1978-06-12 1982-02-16 Monsanto Company Hollow fiber permeator apparatus
JPS54162684A (en) 1978-06-14 1979-12-24 Ebara Infilco Co Ltd Preliminary treating method for contaminated membrane
JPS5535910A (en) * 1978-09-06 1980-03-13 Teijin Ltd Permselectivity composite membrane and preparation thereof
US4190419A (en) * 1978-09-22 1980-02-26 Miles Laboratories, Inc. Device for detecting serum bilirubin
DE7829409U1 (en) 1978-10-02 1986-07-31 Akzo Gmbh, 5600 Wuppertal Dialysis membrane hollow thread with a larger exchange surface
US4188817A (en) * 1978-10-04 1980-02-19 Standard Oil Company (Indiana) Method for detecting membrane leakage
JPS5554004A (en) * 1978-10-18 1980-04-21 Teijin Ltd Selective permeable membrane and its manufacturing
US4367139A (en) * 1978-11-16 1983-01-04 Monsanto Company Hollow fiber permeator
JPS5599703A (en) 1979-01-26 1980-07-30 Matsushita Electric Ind Co Ltd Preparation of anisotropic resin magnet
BE874961A (en) * 1979-03-20 1979-09-20 Studiecentrum Kernenergi PROCESS FOR PREPARING A MEMBRANE, THEREFORE PREPARED MEMBRANE, ELECTROCHEMICAL CELL WITH SUCH MEMBRANE AND USING SUCH ELECTROchemical cell
JPS55129107A (en) 1979-03-28 1980-10-06 Nitto Electric Ind Co Ltd Washing method of selective permeable membrane
JPS55129155A (en) 1979-03-28 1980-10-06 Sakai Chem Ind Co Ltd Production of catalyst
US4243525A (en) * 1979-03-29 1981-01-06 Fmc Corporation Method for reducing the formation of trihalomethanes in drinking water
DE2915730A1 (en) * 1979-04-19 1980-10-30 Kronsbein Dirk Gustav CARTRIDGE FILTER
US4218324A (en) * 1979-05-03 1980-08-19 Textron, Inc. Filter element having removable filter media member
US4226921A (en) * 1979-07-16 1980-10-07 The Dow Chemical Company Selective plugging of broken fibers in tubesheet-hollow fiber assemblies
US4248648A (en) * 1979-07-18 1981-02-03 Baxter Travenol Laboratories, Inc. Method of repairing leaks in a hollow capillary fiber diffusion device
JPS5621604A (en) 1979-07-27 1981-02-28 Toray Ind Inc Separation of liquid by semipermeable composite membrane
US4271026A (en) * 1979-10-09 1981-06-02 Air Products And Chemicals, Inc. Control of activated sludge wastewater treating process for enhanced phosphorous removal
CA1115433A (en) * 1979-10-26 1981-12-29 David C.I. Pollock Method for protecting a bioreactor pressurized head tank against extreme surges of influent waste water
US4367140A (en) * 1979-11-05 1983-01-04 Sykes Ocean Water Ltd. Reverse osmosis liquid purification apparatus
JPS5695304A (en) * 1979-12-28 1981-08-01 Teijin Ltd Perm selective composite membrane and its production
US4323453A (en) * 1980-01-03 1982-04-06 Monsanto Company Tube sheets for permeators
JPS5944884B2 (en) 1980-02-26 1984-11-01 株式会社クラレ Hollow fiber end sealing method and device
JPS56121685A (en) 1980-02-29 1981-09-24 Ebara Infilco Co Ltd Treatment of liquid containing iron ion and manganese ion
US4629563B1 (en) 1980-03-14 1997-06-03 Memtec North America Asymmetric membranes
US4369605A (en) * 1980-07-11 1983-01-25 Monsanto Company Methods for preparing tube sheets for permeators having hollow fiber membranes
DE3026718A1 (en) 1980-07-15 1982-02-04 Akzo Gmbh, 5600 Wuppertal HOLLOW FIBER MEMBRANE FOR PLASMA SEPARATION
JPS5735907A (en) 1980-07-15 1982-02-26 Toyobo Co Ltd Fluid separating element
JPS5770144A (en) * 1980-10-17 1982-04-30 Asahi Glass Co Ltd Organic solution of fluorinated copolymer containing carboxyl group
US4384474A (en) * 1980-10-30 1983-05-24 Amf Incorporated Method and apparatus for testing and using membrane filters in an on site of use housing
US4389363A (en) * 1980-11-03 1983-06-21 Baxter Travenol Laboratories, Inc. Method of potting microporous hollow fiber bundles
JPS57102202A (en) * 1980-12-18 1982-06-25 Toyobo Co Ltd Fluid separator
US4496470A (en) 1981-01-12 1985-01-29 The B. F. Goodrich Company Cleaning composition
JPS57190697A (en) 1981-05-18 1982-11-24 Serupoole Kogyo Kk Air diffusion apparatus
JPS6059933B2 (en) * 1981-05-22 1985-12-27 工業技術院長 Polymer membrane with maleic anhydride residues
JPS5888007A (en) 1981-11-20 1983-05-26 Asahi Glass Co Ltd Separation of liquid mixture
US4707266A (en) 1982-02-05 1987-11-17 Pall Corporation Polyamide membrane with controlled surface properties
US4702840A (en) 1982-02-05 1987-10-27 Pall Corporation Charge modified polyamide membrane
US4405688A (en) * 1982-02-18 1983-09-20 Celanese Corporation Microporous hollow fiber and process and apparatus for preparing such fiber
US4415452A (en) * 1982-03-18 1983-11-15 Heil Richard W Method and apparatus for treating organic wastewater
US4812235A (en) 1982-03-29 1989-03-14 Hr Textron, Inc. Filter element assembly replaceable mesh pack
US4540490A (en) 1982-04-23 1985-09-10 Jgc Corporation Apparatus for filtration of a suspension
US4431545A (en) * 1982-05-07 1984-02-14 Pall Corporation Microporous filter system and process
US4476112A (en) 1982-05-10 1984-10-09 Stay Fresh, Inc. Food preservative composition
WO1983003984A1 (en) 1982-05-13 1983-11-24 Gerhard Kunz Method for the treatment of a liquid phase, particularly method for desalting aqueous solutions, as well as device for its implementation
US4414172A (en) * 1982-05-21 1983-11-08 Filtertek, Inc. Process and apparatus for sealing a plurality of filter elements
JPS5952507A (en) 1982-06-03 1984-03-27 デ−・エル・エム・ドクトル・ミユラ−・アクチエンゲゼルシヤフト Apparatus for continuously concentrating suspension
US4462855A (en) 1982-06-28 1984-07-31 Celanese Corporation Process for bonding polyester reinforcement elements to rubber
JPS5928971A (en) 1982-08-06 1984-02-15 川澄化学工業株式会社 Hollow yarn type mass transfer apparatus and production thereof
US4414113A (en) * 1982-09-29 1983-11-08 Ecodyne Corporation Liquid purification using reverse osmosis hollow fibers
US4476015A (en) 1982-11-02 1984-10-09 V. J. Ciccone & Associates, Inc. Multiple element fluid separation device
JPS5992094A (en) 1982-11-18 1984-05-28 Agency Of Ind Science & Technol Anaerobic digestion of organic waste matter
GB2132366B (en) 1982-12-27 1987-04-08 Brunswick Corp Method and device for testing the permeability of membrane filters
US4467001A (en) 1982-12-27 1984-08-21 Albany International Corp. Process and device for applying, drying and curing a coating on filaments
CA1221645A (en) 1983-02-28 1987-05-12 Yoshihiro Okano Filtration apparatus using hollow fiber-membrane
DE3317396A1 (en) 1983-05-13 1984-11-15 Henkel KGaA, 4000 Düsseldorf USE OF COLOYERS FROM ESTERS AND AMIDES OF ACRYLIC AND / OR METHACRYLIC ACIDS AS STOCK POINTS LOW FOR PARAFFIN SOLUTIONS
GB8313635D0 (en) 1983-05-17 1983-06-22 Whatman Reeve Angel Plc Porosimeter
JPH0657302B2 (en) 1983-07-13 1994-08-03 株式会社東芝 Backwashing method for hollow fiber membrane filters
US4636296A (en) 1983-08-18 1987-01-13 Gerhard Kunz Process and apparatus for treatment of fluids, particularly desalinization of aqueous solutions
US4650586A (en) 1983-09-26 1987-03-17 Kinetico, Inc. Fluid treatment system
US4756875A (en) 1983-09-29 1988-07-12 Kabushiki Kaisha Toshiba Apparatus for filtering water containing radioactive substances in nuclear power plants
AU563321B2 (en) 1983-09-30 1987-07-02 U.S. Filter Wastewater Group, Inc. Cleaning of filters
EP0160014B1 (en) 1983-09-30 1993-01-07 Memtec Limited Cleaning of filters
US4888115A (en) 1983-12-29 1989-12-19 Cuno, Incorporated Cross-flow filtration
JPS61501830A (en) 1984-04-11 1986-08-28 シリンクス　リサ−チ　プロプライエタリイ　リミテツド high flux membrane
US4539940A (en) 1984-04-26 1985-09-10 Young Richard K Tube and shell heat exchanger with annular distributor
US4609465A (en) 1984-05-21 1986-09-02 Pall Corporation Filter cartridge with a connector seal
JPS60260628A (en) 1984-06-08 1985-12-23 Idemitsu Petrochem Co Ltd Thermoplastic resin molding coated with plasma polymer film
SE441236B (en) 1984-06-18 1985-09-23 Gambro Dialysatoren PROCEDURE FOR MANUFACTURING A DEVICE CONTAINING A HALFIBER BUNCH
DE3568946D1 (en) 1984-07-09 1989-04-27 Millipore Corp Improved electrodeionization apparatus and method
JPS6125903U (en) 1984-07-24 1986-02-15 株式会社 伊藤鉄工所 filtration equipment
DE3428307A1 (en) 1984-08-01 1986-02-13 Filterwerk Mann & Hummel Gmbh, 7140 Ludwigsburg DISPLAY DEVICE FOR THE POLLUTION LEVEL OF SUCTION AIR FILTERS
JPS6197006A (en) 1984-10-18 1986-05-15 Daicel Chem Ind Ltd Repairing method of hollow yarn type module
JPS6197005A (en) 1984-10-18 1986-05-15 Mitsubishi Rayon Co Ltd Manufacture of hollow yarn membrane module
US5192478A (en) 1984-10-22 1993-03-09 The Dow Chemical Company Method of forming tubesheet for hollow fibers
JPS61107905A (en) 1984-10-30 1986-05-26 Toshiba Corp Filter
JPS6338884Y2 (en) 1984-12-15 1988-10-13
US5198162A (en) 1984-12-19 1993-03-30 Scimat Limited Microporous films
GB2168981B (en) 1984-12-27 1988-07-06 Asahi Chemical Ind Porous fluorine resin membrane and process for preparation thereof
JPS61167407A (en) 1985-01-19 1986-07-29 Sumitomo Bakelite Co Ltd Preparation of hollow yarn filtration membrane module
JPS61167406A (en) 1985-01-19 1986-07-29 Sumitomo Bakelite Co Ltd Process for bundling and fixing separation membrane
JPS61171504A (en) 1985-01-25 1986-08-02 Agency Of Ind Science & Technol Apparatus for centrifugal molding of yarn bundle
JPS61192309A (en) 1985-02-21 1986-08-26 Asahi Chem Ind Co Ltd Hollow yarn type module
US4931186A (en) 1985-03-05 1990-06-05 Memtec Limited Concentration of solids in a suspension
US5024762A (en) 1985-03-05 1991-06-18 Memtec Limited Concentration of solids in a suspension
AU576424B2 (en) 1985-03-05 1988-08-25 U.S. Filter Wastewater Group, Inc. Concentration of solids in a suspension
US4642182A (en) 1985-03-07 1987-02-10 Mordeki Drori Multiple-disc type filter with extensible support
JPS61222510A (en) 1985-03-28 1986-10-03 Nitto Electric Ind Co Ltd Hollow yarn membrane module and its preparation
WO1986005705A1 (en) 1985-03-28 1986-10-09 Memtec Limited Cooling hollow fibre cross-flow separators
US4704324A (en) 1985-04-03 1987-11-03 The Dow Chemical Company Semi-permeable membranes prepared via reaction of cationic groups with nucleophilic groups
ATE53510T1 (en) 1985-04-10 1990-06-15 Memtec Ltd VARIABLE VOLUME FILTER OR CONCENTRATOR.
US4610789A (en) 1985-04-22 1986-09-09 Ppg Industries, Inc. Filtration cartridge and reactor
JPS61242607A (en) 1985-04-22 1986-10-28 Asahi Chem Ind Co Ltd Preparation of hollow yarn type module having slit
JPS61249505A (en) 1985-04-27 1986-11-06 Toyobo Co Ltd Method for preserving fluid separator
CA1247329A (en) 1985-05-06 1988-12-28 Craig J. Brown Fluid treatment process and apparatus
JPS61257203A (en) 1985-05-10 1986-11-14 Terumo Corp Hydrophilic porous membrane and its preparation
JPS61263605A (en) 1985-05-17 1986-11-21 Toshiba Corp Hollow yarn membrane device
JPS61274709A (en) 1985-05-29 1986-12-04 Ebara Corp Hollow yarn membrane filter apparatus
US4660411A (en) 1985-05-31 1987-04-28 Reid Philip L Apparatus for measuring transmission of volatile substances through films
JPS61291007A (en) 1985-06-17 1986-12-20 Toyobo Co Ltd Hollow yarn type separation membrane element
JPS61293504A (en) 1985-06-24 1986-12-24 Kurita Water Ind Ltd Separation device utilizing hollow yarn membrane
JPS624408A (en) 1985-06-28 1987-01-10 Toshiba Corp Filtration device using hollow yarn membrane
US4656865A (en) 1985-09-09 1987-04-14 The Dow Chemical Company System for analyzing permeation of a gas or vapor through a film or membrane
JPS6268828A (en) 1985-09-19 1987-03-28 Youbea Le-Ron Kogyo Kk Transparent cassette liner
US4876006A (en) 1985-10-08 1989-10-24 Ebara Corporation Hollow fiber filter device
JPS62114609A (en) 1985-11-15 1987-05-26 Ebara Corp Hollow yarn membrane filter
US4824563A (en) 1985-12-04 1989-04-25 Kabushiki Kaisha Meidensha Equipment for treating waste water
US4687578A (en) 1985-12-12 1987-08-18 Monsanto Company Fluid separation membranes
JPH0613088B2 (en) 1985-12-13 1994-02-23 ダイセル化学工業株式会社 Aseptic leak detection method for hollow fiber type modules
JPS62144708A (en) 1985-12-19 1987-06-27 Daicel Chem Ind Ltd Hollow yarn mold membrane module
DE3546091A1 (en) 1985-12-24 1987-07-02 Kernforschungsz Karlsruhe CROSS-CURRENT MICROFILTER
JPS62163708A (en) 1986-01-13 1987-07-20 Ebara Corp Method for backwashing hollow yarn filter
US4779448A (en) 1986-01-28 1988-10-25 Donaldson Company, Inc. Photoelectric bubble detector apparatus and method
JPH06104753B2 (en) 1986-02-04 1994-12-21 旭化成工業株式会社 Non-adsorbing hydrophilic hollow fiber porous membrane
JPH0742861B2 (en) 1986-03-10 1995-05-15 ヤマハ発動機株式会社 Internal combustion engine intake system
JPS62237908A (en) 1986-04-07 1987-10-17 Kurita Water Ind Ltd Filter module for hollow yarn type membrane separation equipment
JPS62250908A (en) 1986-04-24 1987-10-31 Asahi Chem Ind Co Ltd Hollow yarn type filter
US4774132A (en) 1986-05-01 1988-09-27 Pall Corporation Polyvinylidene difluoride structure
JPH0741147B2 (en) 1986-05-09 1995-05-10 株式会社東芝 Hollow fiber membrane filtration device
DE3617724A1 (en) 1986-05-27 1987-12-03 Akzo Gmbh METHOD FOR DETERMINING THE BLOW POINT OR THE BIGGEST PORE OF MEMBRANES OR FILTER MATERIALS
FR2600265B1 (en) 1986-06-20 1991-09-06 Rhone Poulenc Rech DRY AND HYDROPHILIC SEMI-PERMEABLE MEMBRANES BASED ON VINYLIDENE POLYFLUORIDE
US4839048A (en) 1986-07-08 1989-06-13 Pall Corporation Container for pressurized fluid
US4670145A (en) 1986-07-08 1987-06-02 E. I. Du Pont De Nemours And Company Multiple bundle fluid separation apparatus
ES2014516A6 (en) 1986-07-11 1990-07-16 Mentec Ltd Cleaning of filters.
JPH01501046A (en) 1986-09-04 1989-04-13 メムテック・リミテッド How to clean hollow fiber filters
US5094750A (en) 1986-09-12 1992-03-10 Memtec Limited Hollow fibre filter cartridge and header
US4876012A (en) 1986-09-12 1989-10-24 Memtec Limited Hollow fibre filter cartridge and header
JPH089668B2 (en) 1986-10-14 1996-01-31 東レ株式会社 Hydrophilized film and method for producing the same
DE3636583A1 (en) 1986-10-28 1988-05-05 Draegerwerk Ag METHOD FOR PRODUCING A HOLLOW FIBER FABRIC EXCHANGE MODULE AND MODULE PRODUCED BY THIS METHOD
JPS63143905A (en) 1986-12-08 1988-06-16 Toshiba Corp Hollow yarn membrane filter
US4781831A (en) 1986-12-19 1988-11-01 Goldsmith Robert L Cross-flow filtration device with filtrate flow conduits and method of forming same
US4834998A (en) 1986-12-22 1989-05-30 Heublein, Inc. Ultrafiltration of red wines
JPS63171607A (en) 1986-12-30 1988-07-15 Sumitomo Electric Ind Ltd Method for sealing end of hollow yarn membrane
US5139529A (en) 1987-01-20 1992-08-18 Terumo Kabushiki Kaisha Porous polypropylene membrane and methods for production thereof
JPS63180254A (en) 1987-01-21 1988-07-25 Matsushita Electric Ind Co Ltd Private branch exchange
GB8704142D0 (en) 1987-02-23 1987-04-01 Whitford Plastics Ltd Protective surface treatment
US4867883A (en) 1987-04-21 1989-09-19 Hampton Roads Sanitation District Of The Commonwealth Of Virginia High-rate biological waste water treatment process using activated sludge recycle
US4846970A (en) 1987-06-22 1989-07-11 Osmonics, Inc. Cross-flow filtration membrane test unit
WO1989000880A1 (en) 1987-07-28 1989-02-09 Minntech Corporation Filter cartridge
WO1989000879A1 (en) 1987-07-30 1989-02-09 Toray Industries, Inc. Porous polymetrafluoroethylene membrane, separating apparatus using same, and process for their production
JPS6438197A (en) 1987-07-31 1989-02-08 Nishihara Env San Res Co Ltd Treatment of sewage
US4784771A (en) 1987-08-03 1988-11-15 Environmental Water Technology, Inc. Method and apparatus for purifying fluids
JPH01144409A (en) 1987-09-18 1989-06-06 Pennwalt Corp Hydrophylic sequence copolymer of vinylidene fluoride and n-alkylacrylamide and its production
JPH0610277B2 (en) 1987-09-28 1994-02-09 ジャパンゴアテックス株式会社 Membrane material
JPH01111494A (en) 1987-10-23 1989-04-28 Shinko Pfaudler Co Ltd Continuously connected type intermittent air water lifting cylinder
DE3803341A1 (en) 1988-02-04 1989-08-10 Sartorius Gmbh FLUID-OPEN-ENDING SITES HAVING POROESE MEMBRANE FILTERS AND THEIR USE
US5221478A (en) 1988-02-05 1993-06-22 The Dow Chemical Company Chromatographic separation using ion-exchange resins
US4904426A (en) 1988-03-31 1990-02-27 The Dow Chemical Company Process for the production of fibers from poly(etheretherketone)-type polymers
DE3824359A1 (en) 1988-04-07 1989-10-19 Bayer Ag COMPOSITE MEMBRANES, METHOD FOR THEIR PRODUCTION AND THEIR USE
US4800019A (en) 1988-04-22 1989-01-24 Union Carbide Corporation Tubesheet for semipermeable membrane devices
US5147553A (en) 1988-05-04 1992-09-15 Ionics, Incorporated Selectively permeable barriers
US4966699A (en) 1988-05-25 1990-10-30 Terumo Kabushiki Kaisha Hollow fiber membrane fluid processor
US4886601A (en) 1988-05-31 1989-12-12 Japan Organo Co., Ltd. Column filter using bundles of long fibers
GB8816216D0 (en) 1988-07-07 1988-08-10 Fairey Arlon Ltd Filters
JP2830080B2 (en) 1988-07-08 1998-12-02 株式会社デンソー Filter element and manufacturing method thereof
US5075065A (en) 1988-08-01 1991-12-24 Chemical Fabrics Corporation Method for manufacturing of cast films at high productivity
US5043113A (en) 1988-08-05 1991-08-27 Hoechst Celanese Corp. Process for formation of halogenated polymeric microporous membranes having improved strength properties
DE3829766A1 (en) 1988-09-01 1990-03-22 Akzo Gmbh METHOD FOR PRODUCING MEMBRANES
US4963304A (en) 1988-09-26 1990-10-16 The Dow Chemical Company Process for preparing microporous membranes
FR2639248B1 (en) 1988-11-21 1990-12-28 Lyonnaise Eaux HOUSING FOR FILTER MODULES WITH FIBER BEAMS
US4919815A (en) 1989-02-06 1990-04-24 Zimpro/Passavant Inc. Two-stage anaerobic/aerobic treatment process
US4999038A (en) 1989-02-07 1991-03-12 Lundberg Bo E H Filter unit
DE3904544A1 (en) 1989-02-15 1990-08-16 Fraunhofer Ges Forschung POLYMINE MEMBRANES BASED ON POLYVINYLIDENE FLUORIDE, METHOD FOR THE PRODUCTION AND USE THEREOF
US4952317A (en) 1989-03-10 1990-08-28 Bradley Culkin Device and method for filtering a colloidal suspension
NL8901090A (en) 1989-04-28 1990-11-16 X Flow Bv METHOD FOR MANUFACTURING A MICROPOROUS MEMBRANE AND SUCH MEMBRANE
US4988444A (en) 1989-05-12 1991-01-29 E. I. Du Pont De Nemours And Company Prevention of biofouling of reverse osmosis membranes
US5005430A (en) 1989-05-16 1991-04-09 Electric Power Research Institute, Inc. Automated membrane filter sampler
DE3916511A1 (en) 1989-05-20 1990-12-13 Seitz Filter Werke MEMBRANE FILTER DEVICE FOR MICRO AND ULTRAFILTRATION OF FLUIDS IN THE CROSSFLOW PROCESS
US5138870A (en) 1989-07-10 1992-08-18 Lyssy Georges H Apparatus for measuring water vapor permeability through sheet materials
DE3923128A1 (en) 1989-07-13 1991-01-24 Akzo Gmbh FLAX OR CAPILLARY MEMBRANE BASED ON A HOMOGENEOUS MIXTURE OF POLYVINYLIDE FLUORIDE AND OF A SECOND, BY CHEMICAL IMPROVEMENT, HYDROPHILIBLABLE POLYMERS
US5015275A (en) 1989-07-14 1991-05-14 The Dow Chemical Company Isotropic microporous syndiotactic polystyrene membranes and processes for preparing the same
DE3926059C2 (en) 1989-08-07 1998-01-29 Basf Ag Phosphonomethylated polyvinylamines, process for their preparation and their use
DE69029850D1 (en) 1989-09-29 1997-03-13 Memtec Ltd COLLECTION LINE FOR FILTER CARTRIDGES
US5059317A (en) 1989-10-02 1991-10-22 Dietrich Marius Transportable apparatus for producing drinking water
US5227063A (en) 1989-10-03 1993-07-13 Zenon Environmental Inc. Tubular membrane module
EP0519132A1 (en) 1989-10-18 1992-12-23 Exxon Research And Engineering Company Hollow fiber module
US5079272A (en) 1989-11-30 1992-01-07 Millipore Corporation Porous membrane formed from interpenetrating polymer network having hydrophilic surface
US5158721A (en) 1989-11-30 1992-10-27 Millipore Corporation Porous membrane formed from interpenetrating polymer network having hydrophilic surface
FR2655642B1 (en) 1989-12-11 1992-02-28 Anjou Rech WATER TREATMENT PLANT BY A TANGENTIAL FILTER LOOP.
DE3943249C2 (en) 1989-12-29 1993-11-18 Seitz Filter Werke Closed filter element
DE4000978A1 (en) 1990-01-16 1991-07-18 Basf Ag METHOD FOR REMOVING HEAVY METALIONS FROM WINE AND WINE-BASED BEVERAGES
DE69104629D1 (en) 1990-01-23 1994-11-17 Kaldnes Miljoteknologi As METHOD AND REACTOR FOR PURIFYING WATER.
US5066375A (en) 1990-03-19 1991-11-19 Ionics, Incorporated Introducing and removing ion-exchange and other particulates from an assembled electrodeionization stack
ES2126571T3 (en) 1990-04-20 1999-04-01 Usf Filtration Limited MICROPOROUS MODULAR FILTER ASSEMBLIES.
US5364527A (en) 1990-06-20 1994-11-15 Heinz Zimmermann Apparatus and process for treating water
IT1242864B (en) 1990-06-26 1994-05-18 Perdomini Spa AUTOMATIC CONTROL AND OPTIMIZATION SYSTEM OF ULTRAFILTRATION PROCEDURES IN INDUSTRIAL FOOD AND / OR CHEMICAL AND / OR CHEMICAL-PHARMACEUTICAL PLANTS AND ULTRAFILTRATION PROCEDURE USING SUCH SYSTEM.
DE4117281C2 (en) 1990-06-29 1996-02-22 Gore Enterprise Holdings Inc Hydrophilized, microporous membrane made of polytetrafluoroethylene and process for its production
US5104546A (en) 1990-07-03 1992-04-14 Aluminum Company Of America Pyrogens separations by ceramic ultrafiltration
US5639373A (en) 1995-08-11 1997-06-17 Zenon Environmental Inc. Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
US5248424A (en) 1990-08-17 1993-09-28 Zenon Environmental Inc. Frameless array of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
US5182019A (en) 1990-08-17 1993-01-26 Zenon Environmental Inc. Cartridge of hybrid frameless arrays of hollow fiber membranes and module containing an assembly of cartridges
US5104535A (en) 1990-08-17 1992-04-14 Zenon Environmental, Inc. Frameless array of hollow fiber membranes and module containing a stack of arrays
JP2904564B2 (en) 1990-08-31 1999-06-14 オルガノ株式会社 Method of scrubbing filtration tower using hollow fiber membrane
FR2666245B1 (en) 1990-08-31 1992-10-23 Lyonnaise Eaux METHOD FOR CONTROLLING THE OPERATING MODES OF AN AUTOMATIC WATER FILTRATION APPARATUS ON TUBULAR MEMBRANES.
JP2858913B2 (en) 1990-09-26 1999-02-17 オルガノ株式会社 Filtration method using hollow fiber membrane
USH1045H (en) 1990-11-19 1992-05-05 The United States Of America As Represented By The Secretary Of The Army Air bubble leak detection test device
US5069065A (en) 1991-01-16 1991-12-03 Mobil Oil Corporation Method for measuring wettability of porous rock
GB2253572B (en) 1991-02-11 1994-12-14 Aljac Engineering Limited Flow device in fluid circuits
US5677360A (en) 1991-02-13 1997-10-14 Mitsubishi Rayon Co., Ltd. Hydrophilic polymer alloy, fiber and porous membrane comprising this polymer alloy, and methods for preparing them
DK0510328T3 (en) 1991-03-07 1996-02-05 Kubota Kk Apparatus for treating activated sludge
FR2674448B1 (en) 1991-03-26 1994-03-25 Dumez Lyonnaise Eaux METHOD FOR CLEANING MESOPOROUS TUBULAR MEMBRANES OF ULTRAFILTRATION.
EP0509152A1 (en) 1991-04-17 1992-10-21 Ecotechniek B.V. Method and apparatus for processing manure
DE4113420A1 (en) 1991-04-25 1992-10-29 Bayer Ag Hollow polyacrylonitrile fibres, useful for membrane processes - mfd. by dry-wet or wet spinning from special spinning solns. contg. PAN and non-solvent etc., with simultaneous extrusion of core fluid
CA2109436C (en) 1991-05-01 2002-02-05 Level Valley Dairy Company Wastewater treatment system
DE4117422C1 (en) 1991-05-28 1992-11-12 Willi Prof. Dr.-Ing. 7432 Bad Urach De Dettinger Monitoring contamination level of filter, partic. for hydraulic fluids - in which signal is produced which correlates with quotient of two pressure differences and evaluating device produces signal to change filter when quotient reaches given value
DE4119040C2 (en) 1991-06-10 1997-01-02 Pall Corp Method and device for testing the operating state of filter elements
US5211823A (en) 1991-06-19 1993-05-18 Millipore Corporation Process for purifying resins utilizing bipolar interface
AU671803B2 (en) 1991-08-07 1996-09-12 Siemens Industry, Inc. Concentration of solids in a suspension using hollow fibre membranes
US5186821A (en) 1991-09-03 1993-02-16 D. Thomas Murphy Wastewater treatment process with cooperating velocity equalization, aeration and decanting means
US5135663A (en) 1991-10-18 1992-08-04 Loctite Corporation Method of treating (meth)acrylic monomer-containing wastewater
US5137631A (en) 1991-10-22 1992-08-11 E. I. Du Pont De Nemours And Company Multiple bundle permeator
US5192442A (en) 1991-12-02 1993-03-09 Zimpro Passavant Environmental Systems, Inc. Multiple zone batch treatment process
WO1993013489A1 (en) 1991-12-24 1993-07-08 Sierra Semiconductor Corporation An anti-aliasing method for polynomial curves using integer arithmetics
US5269919A (en) 1992-01-17 1993-12-14 Von Medlin Wallace Self-contained water treatment system
US5556591A (en) 1992-01-21 1996-09-17 Millipore S.A. Membrane sealing techniques using thermoplastic polymers
US5203405A (en) 1992-02-03 1993-04-20 Phillips Petroleum Company Two pass shell and tube heat exchanger with return annular distributor
US5198116A (en) 1992-02-10 1993-03-30 D.W. Walker & Associates Method and apparatus for measuring the fouling potential of membrane system feeds
DE69316325T2 (en) 1992-02-12 1998-05-28 Mitsubishi Rayon Co HOLLOW FIBER MEMBRANE MODULE
FR2697446B1 (en) 1992-11-03 1994-12-02 Aquasource Process for the treatment of a fluid containing suspended and dissolved materials, using separation membranes.
US5411663A (en) 1992-03-20 1995-05-02 Micron Separations, Inc. Alcohol-insoluble nylon microporous membranes
EP0592066B1 (en) 1992-05-01 1997-09-03 Memtec Japan Limited Apparatus for testing membrane filter integrity
DE69305742T2 (en) 1992-05-18 1997-04-10 Minntech Corp HOLLOW FIBER FILTER CARTRIDGE AND METHOD FOR THE PRODUCTION THEREOF
CA2100643A1 (en) 1992-08-14 1994-02-15 Guido Sartori Fluorinated polyolefin membranes for aromatics/saturates separation
RU95105413A (en) 1992-09-14 1997-03-20 Даумас Пти Лтд. (AU) Method and device for removal and reworking organic wastes
US5275766A (en) 1992-10-30 1994-01-04 Corning Incorporate Method for making semi-permeable polymer membranes
ES2149218T3 (en) 1992-11-02 2000-11-01 Usf Filtration Ltd TEST SYSTEM FOR HOLLOW FIBER MODULES.
US5320760A (en) 1992-12-07 1994-06-14 E. I. Du Pont De Nemours And Company Method of determining filter pluggage by measuring pressures
FR2699424B1 (en) 1992-12-21 1995-02-03 Dumez Lyonnaise Eaux Hollow fiber filtration module and its manufacturing process.
US5262054A (en) 1992-12-30 1993-11-16 E. I. Du Pont De Nemours And Company Process for opening reverse osmosis membranes
US5401401A (en) 1993-01-13 1995-03-28 Aquaria Inc. Hang on tank canister filter
US5316671A (en) 1993-01-21 1994-05-31 Murphy D Thomas Submersible aeration train and aeration apparatus for biological purification of sewage
US5374353A (en) 1993-01-21 1994-12-20 Murphy; D. Thomas Aeration train and aeration apparatus for biological purification of wastewater
US5468397A (en) 1993-03-16 1995-11-21 Memtec America Corporation Gas backwash of pleated filters
US5389260A (en) 1993-04-02 1995-02-14 Clack Corporation Brine seal for tubular filter
US5514278A (en) 1993-04-12 1996-05-07 Khudenko; Boris M. Counterflow microbiological processes
US5361625A (en) 1993-04-29 1994-11-08 Ylvisaker Jon A Method and device for the measurement of barrier properties of films against gases
US5297420A (en) 1993-05-19 1994-03-29 Mobil Oil Corporation Apparatus and method for measuring relative permeability and capillary pressure of porous rock
US5401405A (en) 1993-05-24 1995-03-28 Davis Water & Waste Industries, Inc. Combined air/water backwash in a travelling bridge filter
FR2705734B1 (en) 1993-05-25 1995-06-30 Snecma Method and device for improving the safety of fluid filters.
IL105875A (en) 1993-06-01 1998-04-05 Aga Ab Selective clogging of failed fibers
US5425415A (en) 1993-06-15 1995-06-20 Abb Lummus Crest Inc. Vertical heat exchanger
DE4326603C2 (en) 1993-08-07 1995-11-02 Kummer Karl Dankwart Dipl Ing Sewage treatment plant with aeration tank, process for wastewater treatment
US5358732A (en) 1993-08-10 1994-10-25 Albert Einstein College Of Medicine Of Yeshiva University Method and system for removing impurities from aliments
JPH07112185A (en) 1993-08-26 1995-05-02 Nitto Denko Corp Waste water treating device and washing method therefor
JP3342928B2 (en) 1993-09-13 2002-11-11 オルガノ株式会社 Hanging equipment for filtration equipment using hollow fiber modules
US5419816A (en) 1993-10-27 1995-05-30 Halox Technologies Corporation Electrolytic process and apparatus for the controlled oxidation of inorganic and organic species in aqueous solutions
FR2713220B1 (en) 1993-11-30 1996-03-08 Omnium Traitement Valorisa Installation of water purification with submerged filter membranes.
US5403479A (en) 1993-12-20 1995-04-04 Zenon Environmental Inc. In situ cleaning system for fouled membranes
JP3160140B2 (en) 1993-12-22 2001-04-23 オルガノ株式会社 Filtration device using hollow fiber module
TW255835B (en) 1994-01-07 1995-09-01 Kubota Kk Filtration membrane module
US6036030A (en) 1994-02-02 2000-03-14 Bechtel Bwxt Idaho Llc Method for producing a selectively permeable separation module
DK175061B1 (en) 1994-03-02 2004-05-10 Apv Pasilac As Membrane filtration Event
DE4406952A1 (en) 1994-03-03 1995-09-07 Bayer Ag Process for concentrating paint overspray
US5501798A (en) 1994-04-06 1996-03-26 Zenon Environmental, Inc. Microfiltration enhanced reverse osmosis for water treatment
US5556541A (en) 1994-04-26 1996-09-17 Filtertek, Inc. Process for making hermetically sealed filter units and filters made thereby
JP3396085B2 (en) 1994-05-24 2003-04-14 テルモ株式会社 Hollow fiber membrane type blood processor
JPH07313850A (en) 1994-05-30 1995-12-05 Kubota Corp Method for backward washing immersion-type ceramic membrane separator
US5491023A (en) 1994-06-10 1996-02-13 Mobil Oil Corporation Film composition
CN2204898Y (en) 1994-06-29 1995-08-09 鹿乔 Proportional flow controlling valve
US5531900A (en) 1994-07-07 1996-07-02 University Of Arizona Modification of polyvinylidene fluoride membrane and method of filtering
CN1077804C (en) 1994-07-28 2002-01-16 米利波尔公司 Porous composite membrane and making process
JPH0839089A (en) 1994-08-02 1996-02-13 Toto Ltd Purifying tank and operation thereof
US5451317A (en) 1994-09-08 1995-09-19 Kubota Corporation Solid-liquid separator
AUPM800694A0 (en) 1994-09-09 1994-10-06 Memtec Limited Cleaning of hollow fibre membranes
US5470469A (en) 1994-09-16 1995-11-28 E. I. Du Pont De Nemours And Company Hollow fiber cartridge
FR2726568B1 (en) 1994-11-08 1996-12-06 Atochem Elf Sa POLYMER MIXTURES COMPRISING A HALOGEN POLYMER AND COMPATIBILIZED BY A GRAFT ALIPHATIC POLYESTER
AUPM957194A0 (en) 1994-11-18 1994-12-15 Act Electricity & Water Wastewater treatment method and plant
CN2236049Y (en) 1994-12-01 1996-09-25 张利军 Three-way stop valve
DE19503060A1 (en) 1995-02-01 1996-08-08 Henkel Ecolab Gmbh & Co Ohg Cleaning procedure for membrane filters
EP1300186B1 (en) 1995-03-15 2007-02-21 U.S. Filter Wastewater Group, Inc. Filtration monitoring and control system
CN1094066C (en) 1995-03-22 2002-11-13 株式会社机械化学研究所 Method of desalinating saline water and apparatus thereof
US5597732A (en) 1995-04-14 1997-01-28 Bryan-Brown; Michael Composting apparatus
EP0820344B1 (en) 1995-04-14 1999-11-03 Aquasource Method for operating and controlling a bank of filtration membrane modules, and bank of modules therefor
JPH10503964A (en) 1995-06-07 1998-04-14 ゴア ハイブリッド テクノロジーズ，インコーポレイティド Implantable containment device for a therapeutic device and method for loading and reloading the device therein
GB9511842D0 (en) 1995-06-10 1995-08-09 North West Water Group Plc Filter
US5906742A (en) 1995-07-05 1999-05-25 Usf Filtration And Separations Group Inc. Microfiltration membranes having high pore density and mixed isotropic and anisotropic structure
US5766479A (en) 1995-08-07 1998-06-16 Zenon Environmental Inc. Production of high purity water using reverse osmosis
US5670053A (en) 1995-08-07 1997-09-23 Zenon Environmental, Inc. Purification of gases from water using reverse osmosis
US6863823B2 (en) 2001-03-23 2005-03-08 Zenon Environmental Inc. Inverted air box aerator and aeration method for immersed membrane
US6685832B2 (en) 1995-08-11 2004-02-03 Zenon Environmental Inc. Method of potting hollow fiber membranes
KR20050046718A (en) 1995-08-11 2005-05-18 제논 인바이런멘탈 인코포레이티드 Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces
US5944997A (en) 1995-08-11 1999-08-31 Zenon Environmental Inc. System for maintaining a clean skein of hollow fibers while filtering suspended solids
US6656356B2 (en) 1998-10-09 2003-12-02 Zenon Environmental Inc. Aerated immersed membrane system
US7087173B2 (en) 1995-08-11 2006-08-08 Zenon Environmental Inc. Inverted cavity aerator for membrane module
US6193890B1 (en) 1995-08-11 2001-02-27 Zenon Environmental Inc. System for maintaining a clean skein of hollow fibers while filtering suspended solids
JP3431166B2 (en) 1995-09-21 2003-07-28 旭化成株式会社 Hollow membrane module
JP3671477B2 (en) 1995-10-12 2005-07-13 栗田工業株式会社 Cleaning method for submerged membrane separator
RU2119817C1 (en) 1995-10-23 1998-10-10 Акционерное общество открытого типа "Полимерсинтез" Porous fluorocarbon membrane, method of its preparation, and cartridge filter based on this membrane
JPH09138298A (en) 1995-11-16 1997-05-27 Hitachi Ltd Filter using hollow-fiber membrane and method for backwashing it
FR2741280B1 (en) 1995-11-22 1997-12-19 Omnium Traitement Valorisa METHOD FOR CLEANING A FILTER SYSTEM OF THE SUBMERSIBLE MEMBRANE TYPE
US5744037A (en) 1995-11-28 1998-04-28 Ebara Corporation Method of treating foul water
US6074718A (en) 1996-02-06 2000-06-13 Koch Membrane Systems, Inc. Self supporting hollow fiber membrane and method of construction
US5895570A (en) 1996-02-09 1999-04-20 United States Filter Corporation Modular filtering system
US6077435A (en) 1996-03-15 2000-06-20 Usf Filtration And Separations Group Inc. Filtration monitoring and control system
EP0814116A1 (en) 1996-06-19 1997-12-29 Hüls Aktiengesellschaft Hydrophilic coating of polymeric substrate surfaces
US5989428A (en) 1996-06-21 1999-11-23 Goronszy; Mervyn Charles Controlling wastewater treatment by monitoring oxygen utilization rates
EP0813897A3 (en) 1996-06-21 1998-06-24 Japan Pionics Co., Ltd. Dust removing apparatus and dust removing method
US5958243A (en) 1996-07-11 1999-09-28 Zenon Environmental Inc. Apparatus and method for membrane filtration with enhanced net flux
JP3248611B2 (en) 1996-07-12 2002-01-21 日立プラント建設株式会社 Solid-liquid separation device
JPH1033955A (en) 1996-07-23 1998-02-10 Hitachi Zosen Corp Membrane separation apparatus
JP3278577B2 (en) 1996-07-31 2002-04-30 セイコーインスツルメンツ株式会社 Adhesive for optical connector and ferrule and optical connector using the same
US5814234A (en) * 1996-08-14 1998-09-29 Prosys Corporation Integrated soil and fluid decontamination system
JPH10110657A (en) 1996-08-22 1998-04-28 Stanadyne Automot Corp Filter assembly having matching cartridge support structure
JPH1076144A (en) 1996-09-05 1998-03-24 Kurita Water Ind Ltd Membrane separator by hollow tubular membranes
JPH1076264A (en) 1996-09-05 1998-03-24 Kubota Corp Sewage treatment apparatus using immersion type membrane separator
JPH1085566A (en) 1996-09-11 1998-04-07 Hitachi Ltd Pleated type filter
US5888401A (en) 1996-09-16 1999-03-30 Union Camp Corporation Method and apparatus for reducing membrane fouling
JPH1085562A (en) 1996-09-17 1998-04-07 Asahi Chem Ind Co Ltd Union restricting orifice and filtration device
JPH1085565A (en) 1996-09-19 1998-04-07 Yamada Kogyo Kk Membrane separator
JP3686918B2 (en) 1996-10-16 2005-08-24 森村興産株式会社 Filtration device for solid-liquid separation of sewage, wastewater, etc.
USD396046S (en) 1996-10-24 1998-07-14 Allen Scheel Steer device for an outboard motor
AUPO377796A0 (en) 1996-11-21 1996-12-19 Memtec America Corporation Microporous membrane filtration and backwashing process
JP3436026B2 (en) 1996-12-02 2003-08-11 エヌオーケー株式会社 Hollow fiber membrane module
WO1999067013A1 (en) 1996-12-10 1999-12-29 Asahi Kasei Kogyo Kabushiki Kaisha Porous polyvinylidene fluoride resin film and process for producing the same
AUPO412596A0 (en) 1996-12-10 1997-01-09 Memtec America Corporation Improved microporous membrane filtration assembly
US6045899A (en) 1996-12-12 2000-04-04 Usf Filtration & Separations Group, Inc. Highly assymetric, hydrophilic, microfiltration membranes having large pore diameters
US20040232076A1 (en) 1996-12-20 2004-11-25 Fufang Zha Scouring method
NZ336455A (en) 1996-12-20 2001-04-27 Usf Filtration & Separations A method for cleaning porous membranes using a gas bubble system
WO1998028064A1 (en) 1996-12-21 1998-07-02 Akzo Nobel Nv Membrane module with hollow fibre membranes arranged in layers
JPH10180048A (en) 1996-12-27 1998-07-07 Kurita Water Ind Ltd Immersion type membrane separator
DE19700493A1 (en) 1997-01-09 1998-07-16 Bayer Ag Methods for cleaning surfaces
US6146747A (en) 1997-01-22 2000-11-14 Usf Filtration And Separations Group Inc. Highly porous polyvinylidene difluoride membranes
USD396726S (en) 1997-02-06 1998-08-04 Abc Group Combined air intake manifold and filter
JP3887072B2 (en) 1997-02-12 2007-02-28 株式会社クラレ Method for cleaning hollow fiber membrane module and filtration device used in the method
JPH10225685A (en) 1997-02-17 1998-08-25 Hitachi Ltd Water purifying treatment device
JPH10235168A (en) 1997-02-24 1998-09-08 Mitsubishi Rayon Co Ltd Filter cleaning method
US6120688A (en) 1997-02-25 2000-09-19 Zenon Environmental, Inc. Portable reverse osmosis unit for producing drinking water
US6007712A (en) 1997-02-28 1999-12-28 Kuraray Co., Ltd. Waste water treatment apparatus
US6048454A (en) 1997-03-18 2000-04-11 Jenkins; Dan Oil filter pack and assembly
US5733456A (en) 1997-03-31 1998-03-31 Okey; Robert W. Environmental control for biological nutrient removal in water/wastewater treatment
FR2762834B1 (en) 1997-05-05 1999-06-04 Ete Europ De Traitement Des Ea PROCESS AND PLANT FOR THE TREATMENT OF WASTEWATER AND THEIR APPLICATION TO WINE EFFLUENTS
JPH10328538A (en) 1997-05-29 1998-12-15 Japan Organo Co Ltd Method for cleaning hollow yarn membrane filtration tower
AUPO709797A0 (en) 1997-05-30 1997-06-26 Usf Filtration And Separations Group Inc. Predicting logarithmic reduction values
JP3859816B2 (en) 1997-06-16 2006-12-20 三菱レイヨン株式会社 Hollow fiber membrane filtration device
US5914039A (en) 1997-07-01 1999-06-22 Zenon Environmental Inc. Filtration membrane with calcined α-alumina particles therein
US6354444B1 (en) 1997-07-01 2002-03-12 Zenon Environmental Inc. Hollow fiber membrane and braided tubular support therefor
JPH1128467A (en) 1997-07-08 1999-02-02 Nkk Corp Immersion type membrane separation device
JPH1131025A (en) 1997-07-11 1999-02-02 Ricoh Co Ltd Pc card slot
JPH1133365A (en) 1997-07-17 1999-02-09 Asahi Chem Ind Co Ltd Method and apparatus for two-layer centrifugal bonding of hollow yarn membrane module
JPH1133367A (en) 1997-07-24 1999-02-09 Mitsubishi Rayon Co Ltd Hollow yarn membrane module
US5997745A (en) 1998-04-08 1999-12-07 Zenon Environmental Inc. Method for producing high purity water using triple pass reverse osmosis (TPRO)
JPH1176769A (en) 1997-09-01 1999-03-23 Daicel Chem Ind Ltd Cleaning method of filter membrane module
US6641733B2 (en) 1998-09-25 2003-11-04 U. S. Filter Wastewater Group, Inc. Apparatus and method for cleaning membrane filtration modules
US6017451A (en) 1997-10-01 2000-01-25 Kopf; Henry B. Spider fitting for multi-module filter system, and motive cart assembly comprising same
US6039872A (en) 1997-10-27 2000-03-21 Pall Corporation Hydrophilic membrane
US6083393A (en) 1997-10-27 2000-07-04 Pall Corporation Hydrophilic membrane
US6723758B2 (en) 1997-11-12 2004-04-20 Ballard Power Systems Inc. Graft polymeric membranes and ion-exchange membranes formed therefrom
JPH11156360A (en) 1997-11-25 1999-06-15 Kubota Corp Method for operation of water treatment plant
JPH11156166A (en) 1997-11-28 1999-06-15 Mitsubishi Heavy Ind Ltd Cleaning method for hollow fiber membrane module
US6290756B1 (en) 1997-12-03 2001-09-18 Praxair Technology, Inc. Hollow fiber membrane tubesheets of variable epoxy composition and hardness
USD400890S (en) 1997-12-03 1998-11-10 Gambardella C Bruce Automotive manifold
JPH11165200A (en) 1997-12-05 1999-06-22 Mitsubishi Rayon Co Ltd Method for treating sludge
JP3866399B2 (en) 1997-12-16 2007-01-10 住友重機械工業株式会社 Membrane filtration device and operation method thereof
US6066401A (en) 1998-02-25 2000-05-23 National Research Council Of Canada Wide-band two-layer antireflection coating for optical surfaces
CN1294622A (en) 1998-02-27 2001-05-09 三菱丽阳株式会社 Device and method for processing crude oil
US6126819A (en) 1998-03-13 2000-10-03 Rochem Ro-Wasserbehandlung Gmbh Apparatus for the treatment of liquids contaminated by foreign substances
DE19811945A1 (en) 1998-03-13 1999-09-16 Rochem Ro Wasserbehandlung Gmbh Cross-flow membrane filter for municipal water treatment plant
US5951878A (en) 1998-03-20 1999-09-14 Aqua-Aerobic Systems, Inc. Method and apparatus for cleaning filter material in a filter apparatus utilizing a suction generating nozzle
ES2253878T3 (en) 1998-03-31 2006-06-01 Samsung Engineering Co., Ltd. METHOD OF WASTEWATER TREATMENT TO SEPARATE ORGANIC AND NITROGEN MATTER.
JP3682897B2 (en) 1998-04-24 2005-08-17 東洋濾紙株式会社 High strength hydrophilic polyvinylidene fluoride porous membrane and method for producing the same
US6074551A (en) 1998-04-30 2000-06-13 Culligan Water Conditioning Of Fairfield County Automatic cleaning system for a reverse osmosis unit in a high purity water treatment system
DE29906389U1 (en) 1998-04-30 1999-06-17 Cramer Weberei Heek Nienborg G Multi-layer textile building material
JPH11319501A (en) 1998-05-08 1999-11-24 Toray Ind Inc Hollow fiber membrane module and use applications thereof
JPH11319507A (en) 1998-05-22 1999-11-24 Toray Ind Inc Hollow fiber membrane module
JPH11333265A (en) 1998-05-26 1999-12-07 Nitto Denko Corp Membrane module
JP3924926B2 (en) 1998-06-15 2007-06-06 東レ株式会社 Hollow fiber membrane filtration membrane module
FR2781168B1 (en) 1998-07-17 2000-09-15 Polymem WATER TREATMENT PROCESS AND INSTALLATION
WO2000004986A1 (en) 1998-07-21 2000-02-03 Toray Industries, Inc. Method for inhibiting growth of bacteria or sterilizing around separating membrane
US6113782A (en) 1998-07-28 2000-09-05 Terumo Cardiovascular Systems Corporation Potting of tubular bundles in housing
JP2000051669A (en) 1998-08-05 2000-02-22 Hitachi Ltd Hollow fiber membrane module fitted with lower cap
US6280626B1 (en) 1998-08-12 2001-08-28 Mitsubishi Rayon Co., Ltd. Membrane separator assembly and method of cleaning the assembly utilizing gas diffuser underneath the assembly
US6096213A (en) 1998-08-14 2000-08-01 3M Innovative Properties Company Puncture-resistant polyolefin membranes
JP2000061466A (en) 1998-08-20 2000-02-29 Nkk Corp Device for treating membrane-filtration waste water and its operation
US5968357A (en) 1998-08-27 1999-10-19 Voith Sulzer Paper Technology North America, Inc. Screen basket having a removable and replaceable cylindrical mesh liner
JP2000070684A (en) 1998-08-27 2000-03-07 Japan Organo Co Ltd Backwashing of pleated membrane filter
US6071404A (en) 1998-08-31 2000-06-06 Tsui; Tommy Water treating device
UA72220C2 (en) 1998-09-08 2005-02-15 Байоенджініерінг Рісорсиз, Інк. Water-immiscible mixture solvent/cosolvent for extracting acetic acid, a method for producing acetic acid (variants), a method for anaerobic microbial fermentation for obtaining acetic acid (variants), modified solvent and a method for obtaining thereof
TWI222895B (en) 1998-09-25 2004-11-01 Usf Filtration & Separations Apparatus and method for cleaning membrane filtration modules
JP4435421B2 (en) 1998-09-28 2010-03-17 グレン・ディー・リンドボウ Wastewater treatment tank with inflow gate and pre-reaction zone with outwardly spreading part
JP4069226B2 (en) 1998-09-28 2008-04-02 旭化成ケミカルズ株式会社 Method for fixing cartridge type module and tank type filtration device
US7014173B2 (en) 1998-10-09 2006-03-21 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
BR9914376A (en) 1998-10-09 2001-08-07 Zenon Environmental Inc Cycling aeration system for submerged membrane modules
US6706189B2 (en) 1998-10-09 2004-03-16 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6550747B2 (en) 1998-10-09 2003-04-22 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6319411B1 (en) 1998-10-09 2001-11-20 Zenon Environmental Inc. Method of maintaining clean vertical skeins of hollow fiber membranes and system therefor
NL1010544C2 (en) 1998-11-13 2000-05-16 Stork Friesland Bv Method and device for removing suspended matter and salts from a liquid by means of membrane filtration.
CA2290053C (en) 1999-11-18 2009-10-20 Zenon Environmental Inc. Immersed membrane module and process
JP2002530188A (en) 1998-11-23 2002-09-17 ゼノン、エンバイロンメンタル、インコーポレーテッド Filtration of water using immersion membrane
JP2000157845A (en) 1998-11-26 2000-06-13 Asahi Chem Ind Co Ltd Hollow fiber membrane cartridge and its fixing structure
JP4107453B2 (en) 1998-11-26 2008-06-25 旭化成ケミカルズ株式会社 Hollow fiber membrane cartridge
JP2000157850A (en) 1998-11-27 2000-06-13 Nitto Denko Corp Separating membrane preservation liquid and separating membrane module
GB9826575D0 (en) 1998-12-04 1999-01-27 Oladpa Tox
US6156200A (en) 1998-12-08 2000-12-05 Usf Filtration & Separations Group, Inc. Gas-scrubbed hollow fiber membrane module
JP4012640B2 (en) 1998-12-24 2007-11-21 旭化成ケミカルズ株式会社 Hollow fiber membrane module
JP2000189958A (en) 1998-12-28 2000-07-11 Maezawa Ind Inc Immersion type membrane filter device
DE19959916A1 (en) 1998-12-30 2000-07-20 Henkel Chile Sa Aqueous polymer dispersion, useful for adhesives and coatings, contains organic and/or inorganic filler particles and organic polymer particles that are formed in presence of at least one filler
US6432310B1 (en) 1999-01-22 2002-08-13 Nitto Denko Corporation Methods of running and washing spiral wound membrane module
JP2000233020A (en) 1999-02-15 2000-08-29 Nikkiso Co Ltd Washing method and washing device for blood treating device
JP2000237548A (en) 1999-02-17 2000-09-05 Tokyo Denki Komusho Co Ltd Hollow fiber membrane type heat storage tank water purifying device
JP4200576B2 (en) 1999-02-23 2008-12-24 トヨタ自動車株式会社 Fuel cell system
JP2000254459A (en) 1999-03-05 2000-09-19 Sumitomo Heavy Ind Ltd Method for washing solid-liquid separation element and solid-liquid separator
US6149817A (en) 1999-03-08 2000-11-21 Celgard Inc. Shell-less hollow fiber membrane fluid contactor
US6770202B1 (en) 1999-04-14 2004-08-03 Pall Corporation Porous membrane
AUPP985099A0 (en) 1999-04-20 1999-05-13 Usf Filtration And Separations Group Inc. Membrane filtration manifold system
AU762091B2 (en) 1999-04-20 2003-06-19 Evoqua Water Technologies Llc Membrane filtration manifold system
US6322703B1 (en) 1999-04-20 2001-11-27 Asahi Kasei Kabushiki Kaisha Method for purifying aqueous suspension
JP3572992B2 (en) 1999-04-21 2004-10-06 日立プラント建設株式会社 Operating method of membrane filtration device
JP2000317276A (en) 1999-05-12 2000-11-21 Zenken:Kk Filtering device
JP2000334276A (en) 1999-05-25 2000-12-05 Mitsubishi Rayon Co Ltd Operation of filtration device
US6221247B1 (en) 1999-06-03 2001-04-24 Cms Technology Holdings, Inc. Dioxole coated membrane module for ultrafiltration or microfiltration of aqueous suspensions
JP2000342932A (en) 1999-06-04 2000-12-12 Mitsubishi Rayon Co Ltd Potting method for separation membrane
US6627082B2 (en) 1999-06-10 2003-09-30 Envirogen, Inc. System and method for withdrawing permeate through a filter and for cleaning the filter in situ
US6277512B1 (en) 1999-06-18 2001-08-21 3M Innovative Properties Company Polymer electrolyte membranes from mixed dispersions
US6755970B1 (en) 1999-06-22 2004-06-29 Trisep Corporation Back-flushable spiral wound filter and methods of making and using same
GB9914854D0 (en) 1999-06-25 1999-08-25 Wilkes Ian P Self cleaning membrane device for filtration used in submerged operation
JP3617378B2 (en) 1999-06-25 2005-02-02 日立プラント建設株式会社 Immersion flat membrane filtration device
US6485645B1 (en) 1999-07-20 2002-11-26 Zenon Environmental Inc Biological process for removing phosphorus involving a membrane filter
AU6144600A (en) 1999-07-20 2001-02-05 Zenon Environmental Inc. Biological process for removing phosphorus involving a membrane filter
US6303035B1 (en) 1999-07-30 2001-10-16 Zenon Environmental Inc. Immersed membrane filtration process
AU6257000A (en) 1999-07-29 2001-02-19 Zenon Environmental Inc. Chemical cleaning backwash for immersed filtering membranes
US20010052494A1 (en) 1999-10-25 2001-12-20 Pierre Cote Chemical cleaning backwash for normally immersed membranes
US20040007525A1 (en) 1999-07-30 2004-01-15 Rabie Hamid R. Maintenance cleaning for membranes
FR2797198B1 (en) 1999-08-04 2002-05-03 Tami Ind MEMBRANE FOR TANGENTIAL FILTRATION AND ITS MANUFACTURING METHOD
DE19940994B4 (en) 1999-08-28 2004-02-26 Clausthaler Umwelttechnikinstitut Gmbh, (Cutec-Institut) Process for the removal of sewage sludge
US6214231B1 (en) 1999-08-27 2001-04-10 Zenon Environmental Inc. System for operation of multiple membrane filtration assemblies
JP2001070967A (en) 1999-09-02 2001-03-21 Asahi Kasei Corp Cleaning system for laundry waste water
JP2001079366A (en) 1999-09-10 2001-03-27 Asahi Kasei Corp Method for washing membrane
JP3603692B2 (en) 1999-09-14 2004-12-22 日立プラント建設株式会社 Membrane separation method and apparatus
US6468472B1 (en) 1999-09-16 2002-10-22 Metrex Research Corporation Cleaning and decontaminating dialyzers by per-compound solutions
US6589426B1 (en) 1999-09-29 2003-07-08 Zenon Environmental Inc. Ultrafiltration and microfiltration module and system
US6361695B1 (en) 1999-10-02 2002-03-26 Zenon Environmental Inc. Shipboard wastewater treatment system
JP2001104760A (en) 1999-10-05 2001-04-17 Mitsubishi Heavy Ind Ltd Immersion type membrane filtration apparatus and method for washing filtration membrane
JP4384310B2 (en) 1999-10-22 2009-12-16 メタウォーター株式会社 Membrane cleaning method
NL1013465C2 (en) 1999-11-02 2001-05-03 Stork Friesland Bv Membrane filtration element with sleeve element and sleeve members.
JP4713801B2 (en) 1999-11-18 2011-06-29 ジーイー・ゼノン・ユーエルシー Immersion type thin film elements and modules
US6861001B2 (en) 1999-12-02 2005-03-01 The General Hospital Corporation Methods for removal, purification, and concentration of viruses, and methods of therapy based thereupon
US6423784B1 (en) 1999-12-15 2002-07-23 3M Innovative Properties Company Acid functional fluoropolymer membranes and method of manufacture
FR2802444B1 (en) 1999-12-16 2002-06-14 Polymen HOLLOW FIBER WATER FILTRATION MODULE
JP3780210B2 (en) 1999-12-17 2006-05-31 ミリポア・コーポレイション Potted hollow fiber potting
US6324898B1 (en) 1999-12-21 2001-12-04 Zenon Environmental Inc. Method and apparatus for testing the integrity of filtering membranes
JP2001179059A (en) 1999-12-27 2001-07-03 Japan Organo Co Ltd Filter of pathogenic microorganism
JP2001179060A (en) 1999-12-27 2001-07-03 Maezawa Ind Inc Internal pressure type membrane treatment device
KR100752245B1 (en) 1999-12-28 2007-08-29 카나자와 히토시 Method of modifying polymeric material and use thereof
US6635179B1 (en) 1999-12-30 2003-10-21 Nephros, Inc. Sterile fluid filtration cartridge and method for using same
US6315895B1 (en) 1999-12-30 2001-11-13 Nephros, Inc. Dual-stage hemodiafiltration cartridge
JP2001190937A (en) 2000-01-06 2001-07-17 Sumitomo Heavy Ind Ltd Water purification equipment and method of cleaning membrane element
JP2001190938A (en) 2000-01-11 2001-07-17 Miura Co Ltd Method of detecting breakage of water treating membrane
JP2001205055A (en) 2000-01-31 2001-07-31 Daicel Chem Ind Ltd Method for operating membrane separation apparatus and apparatus therefor
USD478913S1 (en) 2000-02-24 2003-08-26 Usf Filtration And Separations Group, Inc. Manifold header
US6440303B2 (en) 2000-03-02 2002-08-27 Chapin Manufacturing, Inc. Fluid filter
GB0004921D0 (en) 2000-03-02 2000-04-19 Waterleau Global Water Technol System for sustainable treatment of municipal and industrial wastewater
US6926829B2 (en) 2000-03-06 2005-08-09 Kvaerner Process Systems A.S. Apparatus and method for separating fluids through a membrane
WO2001066474A2 (en) 2000-03-08 2001-09-13 Zenon Environmental Inc. Membrane module for gas transfer and membrane supported biofilm process
US6875357B1 (en) 2000-03-15 2005-04-05 Aqua-Aerobic Systems, Inc. Process and apparatus for treatment of waste water
US6299775B1 (en) 2000-03-17 2001-10-09 Clint R. Elston Waste and wastewater treatment and recycling system
JP4527232B2 (en) 2000-03-28 2010-08-18 旭化成ケミカルズ株式会社 Rack type filter
AUPQ680100A0 (en) 2000-04-10 2000-05-11 Usf Filtration And Separations Group Inc. Hollow fibre restraining system
US6337018B1 (en) 2000-04-17 2002-01-08 The Dow Chemical Company Composite membrane and method for making the same
EP1156015A1 (en) 2000-05-15 2001-11-21 VA TECH WABAG ESMIL GmbH Process and plant for filtrate generation from the stream of recycled sludge
AU142387S (en) 2000-05-31 2000-11-27 Evoqua Water Tech Llc Manifold header cap
EP1166871A1 (en) 2000-06-21 2002-01-02 Fuji Photo Film B.V. Photocalytic sheet of film and its manufacturing process
US7208091B2 (en) 2000-06-29 2007-04-24 Bio Gasol Ipr Aps Assembly for withdrawing and filtering partial volumes of process fluid
US7083726B2 (en) 2000-07-10 2006-08-01 Asahi Kasei Kabushiki Kaisha Hollow thread film cartridge, hollow thread film module using the cartridge, and tank type filter
US6517723B1 (en) 2000-07-27 2003-02-11 Ch2M Hill, Inc. Method and apparatus for treating wastewater using membrane filters
EP1350555A1 (en) 2000-08-02 2003-10-08 Toray Industries, Inc. Hollow yarn membrane module, hollow yarn membrane module unit, and method of producing hollow yarn membrane modules
JP2002058968A (en) 2000-08-18 2002-02-26 Suehiro Tadashi Filter
FR2814454B1 (en) 2000-09-27 2002-12-20 Degremont PROCESS FOR THE PURIFICATION OF WASTEWATER FOR THE ELIMINATION OF NITROGEN AND PHOSPHATE POLLUTIONS
AT408955B (en) 2000-09-28 2002-04-25 Va Tech Wabag Gmbh MEMBRANE FILTER SYSTEM AND METHOD FOR FILTERING
AUPR064800A0 (en) 2000-10-09 2000-11-02 Usf Filtration And Separations Group Inc. Improved membrane filtration system
AUPR094600A0 (en) 2000-10-23 2000-11-16 Usf Filtration And Separations Group Inc. Fibre membrane arrangement
AUPR143400A0 (en) 2000-11-13 2000-12-07 Usf Filtration And Separations Group Inc. Modified membranes
FR2816851B1 (en) 2000-11-20 2003-09-26 Aquasource IMPROVEMENTS IN PROCESSES FOR REPAIRING THE BLOCKED FIBERS OF THE MEMBRANES, IN PARTICULAR OF ULTRA-, NANO- AND HYPER-FILTRATION
US6525064B1 (en) 2000-12-08 2003-02-25 3M Innovative Properties Company Sulfonamido substituted imidazopyridines
FR2817768B1 (en) 2000-12-13 2003-08-29 Lyonnaise Eaux Eclairage METHOD FOR REGULATING A MEMBRANE FILTRATION SYSTEM
JP4382275B2 (en) 2000-12-15 2009-12-09 前澤工業株式会社 Membrane module cleaning method
US20040050791A1 (en) 2001-01-23 2004-03-18 Attila Herczeg Asymmetric hollow fiber membranes
KR200232145Y1 (en) 2001-02-16 2001-07-19 (주)경동이엔씨 Air lifting pipe and waste or polluted water disposal plant
AU2002307836B2 (en) 2001-02-23 2007-11-08 V.A.I. Ltd. Methods and apparatus for biological treatment of waste waters
ITMI20010421A1 (en) 2001-03-01 2002-09-02 Ausimont Spa SEMI-PERMEABLE SEMI-CRYSTALLINE FLUOROPOLYMER Porous MEMBRANES
JP3561690B2 (en) 2001-03-05 2004-09-02 三洋電機株式会社 Filtration system
US20030052055A1 (en) 2001-03-08 2003-03-20 Hiroharu Akamatsu Hollow fiber membrane, hollow fiber membrane module, and water purifier
AUPR421501A0 (en) 2001-04-04 2001-05-03 U.S. Filter Wastewater Group, Inc. Potting method
AU2002326398A1 (en) 2001-04-18 2002-12-16 Buddy Don Gray System for recirculating tangential filter concentrate
US6757059B2 (en) 2001-04-30 2004-06-29 Therma-Wave, Inc. Wafer chuck with integrated reference sample
US6608184B2 (en) 2001-05-10 2003-08-19 David H. Blount Production of products from sewer sludge
JP4689074B2 (en) 2001-05-17 2011-05-25 オルガノ株式会社 Filtration device
US6805806B2 (en) 2001-06-12 2004-10-19 Hydrotreat, Inc. Method and apparatus for treatment of wastewater employing membrane bioreactors
AUPR584301A0 (en) 2001-06-20 2001-07-12 U.S. Filter Wastewater Group, Inc. Membrane polymer compositions
CA2351272C (en) 2001-06-22 2009-09-15 Petro Sep International Ltd. Membrane-assisted fluid separation apparatus and method
FR2827360B1 (en) 2001-07-11 2005-10-28 Valeo Thermique Moteur Sa CONTROL VALVE FOR A FLUID CIRCUIT CIRCUIT, ESPECIALLY FOR A COOLING CIRCUIT OF AN ENGINE
JP2003024751A (en) 2001-07-11 2003-01-28 Asahi Kasei Corp Hollow fiber membrane cartridge
US6702561B2 (en) 2001-07-12 2004-03-09 Nxstage Medical, Inc. Devices for potting a filter for blood processing
JP4360057B2 (en) 2001-08-06 2009-11-11 株式会社ジーエス・ユアサコーポレーション Immersion membrane filtration apparatus and immersion membrane filtration method
JP4860843B2 (en) 2001-08-09 2012-01-25 旭化成ケミカルズ株式会社 External pressure type hollow fiber membrane module
AUPR692401A0 (en) 2001-08-09 2001-08-30 U.S. Filter Wastewater Group, Inc. Method of cleaning membrane modules
JP2003053160A (en) 2001-08-14 2003-02-25 Mitsubishi Rayon Co Ltd Cleaning method for separating membrane and membrane filtrater
JP2003062436A (en) 2001-08-23 2003-03-04 Toray Ind Inc Method for manufacturing hollow fiber membrane module
US6592762B2 (en) 2001-08-29 2003-07-15 United States Filter Corporation Process for treating BOD-containing wastewater
TW536424B (en) 2001-09-05 2003-06-11 Mitsubishi Rayon Co Water-clean cartridge, water-cleaner, and washing method of water-cleaner
AUPR774201A0 (en) 2001-09-18 2001-10-11 U.S. Filter Wastewater Group, Inc. High solids module
US6721529B2 (en) 2001-09-21 2004-04-13 Nexpress Solutions Llc Release agent donor member having fluorocarbon thermoplastic random copolymer overcoat
US6673210B2 (en) 2001-09-27 2004-01-06 Voith Paper Patent Gmbh Cleaning a semipermeable membrane in a papermaking machine
JP3908939B2 (en) 2001-11-02 2007-04-25 三菱レイヨン株式会社 Method for producing hollow fiber membrane module
WO2003039720A1 (en) 2001-11-05 2003-05-15 Asahi Kasei Kabushiki Kaisha Hollow fiber membrane module
EP1312408B1 (en) 2001-11-16 2006-07-19 US Filter Wastewater Group, Inc. Method of cleaning membranes
US6761826B2 (en) 2001-11-30 2004-07-13 New Star Lasers, Inc. Pulsed blackbody radiation flux enhancement
US6790912B2 (en) 2001-12-11 2004-09-14 3M Innovative Properties Company Extrudable fluoropolymer blends
DE10161095C1 (en) 2001-12-12 2002-11-07 Klaus Vosenkaul Process for membrane filtration of liquids e.g. water, uses fiber bundle of capillary membranes having one end cast in headpiece open to permeate collecting chamber of the headpiece and a freely moving closed end
JP2003181247A (en) 2001-12-17 2003-07-02 Nitto Denko Corp Treatment system having spiral membrane element and its operating method
JP2003190976A (en) 2001-12-27 2003-07-08 Toray Ind Inc Apparatus and method for treating wastewater
US6979404B2 (en) 2002-01-02 2005-12-27 Triple I Self-manifolding sheet membrane module
EP1463687B1 (en) 2002-01-07 2011-05-11 Berliner Wasserbetriebe Biological water treatment process involving post-denitrification mechanism and a membrane filter
AU2002357338A1 (en) 2002-01-09 2003-07-30 Hydranautics Methods for improving filtration performance of hollow fiber membranes
US6712970B1 (en) 2002-01-11 2004-03-30 Enviroquip, Inc. Sewage treatment process with phosphorus removal
US6890435B2 (en) 2002-01-28 2005-05-10 Koch Membrane Systems Hollow fiber microfiltration membranes and a method of making these membranes
AUPS046602A0 (en) 2002-02-12 2002-03-07 U.S. Filter Wastewater Group, Inc. Halar membranes
US7247238B2 (en) 2002-02-12 2007-07-24 Siemens Water Technologies Corp. Poly(ethylene chlorotrifluoroethylene) membranes
DE10209170C1 (en) 2002-03-01 2003-08-07 Horst Chmiel Mechanically cleaning hollow fiber membranes comprises forming hollow fibers into bundles, vertically joining together on their opposite-lying ends, and grasping in center to set at angle
JP4173969B2 (en) 2002-03-14 2008-10-29 旭化成クラレメディカル株式会社 Hemodialysis filter and hemodiafiltration device
JP2003266072A (en) 2002-03-18 2003-09-24 Japan Organo Co Ltd Membrane filtration method
JP2003275759A (en) 2002-03-20 2003-09-30 Hitachi Plant Eng & Constr Co Ltd Water treatment device
JP3744447B2 (en) 2002-03-20 2006-02-08 日立プラント建設株式会社 Membrane separator
US6811696B2 (en) 2002-04-12 2004-11-02 Pall Corporation Hydrophobic membrane materials for filter venting applications
US7186344B2 (en) 2002-04-17 2007-03-06 Water Visions International, Inc. Membrane based fluid treatment systems
NL1020491C2 (en) 2002-04-26 2003-10-28 Norit Membraan Tech Bv Measuring integrity of filter membrane, comprises creating volume of gas on filtrate side, increasing pressure on feed side to create pressure drop and measuring increase in pressure on filtrate side
US6869534B2 (en) 2002-05-05 2005-03-22 Brentwood Industries, Inc. Sludge digestion methods and apparatus
US6706185B2 (en) 2002-05-22 2004-03-16 Kurita Water Industries Ltd. Biological method of phosphorus removal and biological phosphorus-removing apparatus
JP2003340250A (en) 2002-05-27 2003-12-02 Kurita Water Ind Ltd Membrane separation device
JP4530245B2 (en) 2002-06-10 2010-08-25 旭化成ケミカルズ株式会社 Membrane separator
US6743362B1 (en) 2002-06-17 2004-06-01 Enviroquip Inc. Sewage treatment process
AUPS300602A0 (en) 2002-06-18 2002-07-11 U.S. Filter Wastewater Group, Inc. Methods of minimising the effect of integrity loss in hollow fibre membrane modules
US6994867B1 (en) 2002-06-21 2006-02-07 Advanced Cardiovascular Systems, Inc. Biocompatible carrier containing L-arginine
EP1517741B1 (en) 2002-06-28 2009-03-04 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk Onderzoek TNO Process for cleaning filters
KR200295350Y1 (en) 2002-08-07 2002-11-21 서봉리사이클링(주) Sludge discharger using lumped air
AU2002950934A0 (en) 2002-08-21 2002-09-12 U. S. Filter Wastewater Group, Inc. Aeration method
US20040035770A1 (en) 2002-08-26 2004-02-26 Edwards Haskell L. Dynamically responsive aerobic to anoxic inter-zone flow control system for single vessel multi-zone bioreactor wastewater treatment plants
WO2004024304A2 (en) 2002-09-13 2004-03-25 Pall Corporation Systems and methods for cleaning hollow fiber membranes
ATE542593T1 (en) 2002-10-10 2012-02-15 Siemens Industry Inc MEMBRANE FILTER AND BACKWASHING METHOD THEREOF
KR100412330B1 (en) 2002-10-25 2004-01-07 주식회사 진우환경기술연구소 Membrane Coupled Activated Sludge Method Operating Anoxic/Anaerobic Zone alternatively for Removal of Nitrogen and Phosphorus
FR2847572B1 (en) 2002-11-22 2006-04-21 Omnium Traitement Valorisa METHOD OF TREATING WATER USING INORGANIC HIGH SPECIFIC SURFACE PULVERULENT REAGENT INCLUDING A RECYCLING STAGE OF SAID REAGENT
US6863817B2 (en) 2002-12-05 2005-03-08 Zenon Environmental Inc. Membrane bioreactor, process and aerator
AU2002953111A0 (en) 2002-12-05 2002-12-19 U. S. Filter Wastewater Group, Inc. Mixing chamber
ES2358668T3 (en) 2002-12-19 2011-05-12 Hydranautics PROCEDURE FOR CLEANING AND MAINTENANCE OF A MEMBRANE SURFACE DURING FILTRATION.
FR2850297B1 (en) 2003-01-29 2005-04-15 Aquasource METHOD FOR MANUFACTURING MEMBRANES FOR FILTRATION MODULES, IN PARTICULAR FOR THE TREATMENT OF WATER
JP4042967B2 (en) 2003-01-30 2008-02-06 オルガノ株式会社 Filtration device backwash method
JP2004230280A (en) 2003-01-30 2004-08-19 Toray Ind Inc Production method for hydrophilic polyvinylidene fluoride-based resin porous membrane
CA2417945A1 (en) 2003-01-31 2004-07-31 Pall Corporation Methods and system for purifying fluids and regenerating purification media
US7014763B2 (en) 2003-02-03 2006-03-21 Aqua-Aerobic Systems, Inc. Multiple barrier biological treatment systems
DE60301322T2 (en) 2003-02-28 2006-06-08 3M Innovative Properties Co., St. Paul A fluoropolymer dispersion containing no or little fluorine-containing low molecular weight wetting agent
US7087172B2 (en) 2003-03-05 2006-08-08 Usfilter Corporation Methods for reducing nitrate demands in the reduction of dissolved and/or atmospheric sulfides in wastewater
EP1603659A2 (en) 2003-03-14 2005-12-14 Zenon Environmental Inc. Nanofiltration system for water softening with internally staged spiral wound modules
EP1466658A1 (en) 2003-04-11 2004-10-13 UTISOL Technologies AG Device and method for aeration of membrane filters
KR100535301B1 (en) 2003-05-13 2005-12-08 연세대학교 산학협력단 Hollow fiber membrane module and Method for making thereof
JP2004337730A (en) 2003-05-15 2004-12-02 Suido Kiko Kaisha Ltd Method for washing membrane
CN1816384A (en) 2003-07-04 2006-08-09 阿克佐诺贝尔股份有限公司 Cleaning of filtration membranes with peroxides
AU2003903507A0 (en) 2003-07-08 2003-07-24 U. S. Filter Wastewater Group, Inc. Membrane post-treatment
US6946073B2 (en) 2003-09-02 2005-09-20 Ch2M Hill, Inc. Method for treating wastewater in a membrane bioreactor to produce a low phosphorus effluent
EP1663461A4 (en) 2003-07-30 2009-01-14 Phase Inc Filtration system with enhanced cleaning and dynamic fluid separation
FR2858609B1 (en) 2003-08-04 2006-10-13 Otv Sa METHOD AND INSTALLATION FOR BIOLOGICAL TREATMENT OF ACTIVATED SLUDGE WATER WITH AERATION CONTROL
JP4034705B2 (en) 2003-08-27 2008-01-16 株式会社神鋼環境ソリューション Novel microorganism and method for treating organic solid using the microorganism
NZ545206A (en) 2003-08-29 2009-03-31 Siemens Water Tech Corp Backwash
JP2005087887A (en) 2003-09-17 2005-04-07 Fuji Electric Systems Co Ltd Membrane washing method
SG119706A1 (en) 2003-09-19 2006-03-28 Us Filter Wastewater Group Inc Improved methods of cleaning membrane modules
CA2533505C (en) 2003-09-22 2013-02-19 U.S. Filter Wastewater Group, Inc. Backwash and cleaning method
US7282147B2 (en) 2003-10-07 2007-10-16 Phase Inc. Cleaning hollow core membrane fibers using vibration
WO2005037414A1 (en) 2003-10-20 2005-04-28 Krishnamurthi Rao C H Novel device for submerged ultrafiltration
US20050115899A1 (en) 2003-10-21 2005-06-02 Minggang Liu Membrane bioreactor having single header membrane module
US7879229B2 (en) 2003-10-29 2011-02-01 Zenon Technology Partnership Water treatment plant with immersed membranes
CN1235668C (en) 2003-11-06 2006-01-11 上海交通大学 E-Fenton oxidation technique of dirty blocking agent in reverse osmosis concentrating liquid
US7022233B2 (en) 2003-11-07 2006-04-04 Severn Trent Services, Water Purification Solutions, Inc. Biologically active reactor system and method for treating wastewater
US7083733B2 (en) 2003-11-13 2006-08-01 Usfilter Corporation Water treatment system and method
JP2005144291A (en) 2003-11-13 2005-06-09 Ngk Insulators Ltd Method for controlling aeration quantity
WO2005046849A1 (en) 2003-11-14 2005-05-26 U.S. Filter Wastewater Group, Inc. Improved module cleaning method
EP1533325B1 (en) 2003-11-17 2011-10-19 3M Innovative Properties Company Aqueous dispersions of polytetrafluoroethylene having a low amount of fluorinated surfactant
JP4533618B2 (en) 2003-11-25 2010-09-01 アムテック株式会社 Disinfectant cleaning composition
WO2005073134A1 (en) 2004-02-02 2005-08-11 Kurita Water Industries Ltd. Process for biological treatment of organic waste water and apparatus therefor
US20070056905A1 (en) 2004-02-18 2007-03-15 Beck Thomas W Continuous pressure decay test
US7220358B2 (en) 2004-02-23 2007-05-22 Ecolab Inc. Methods for treating membranes and separation facilities and membrane treatment composition
US20070051679A1 (en) 2004-02-27 2007-03-08 Adams Nicholas W H Water filtration using immersed membranes
US20050194315A1 (en) 2004-02-27 2005-09-08 Adams Nicholas W.H. Membrane batch filtration process
WO2005082498A1 (en) 2004-02-27 2005-09-09 Zenon Environmental Inc. Water filtration using immersed membranes
CA2482517A1 (en) 2004-09-24 2006-03-24 Zenon Environmental Inc. Membrane filter cleansing process
US7311833B2 (en) 2004-03-03 2007-12-25 Kazuo Yamamoto Zero excess sludge membrane bioreactor
US8758621B2 (en) 2004-03-26 2014-06-24 Evoqua Water Technologies Llc Process and apparatus for purifying impure water using microfiltration or ultrafiltration in combination with reverse osmosis
JP4508694B2 (en) 2004-03-30 2010-07-21 株式会社クボタ Water treatment method and apparatus
JP2007535398A (en) 2004-04-22 2007-12-06 シーメンス ウォーター テクノロジース コーポレイション Filtration device including membrane bioreactor and treatment tank for digesting organic substances, and waste liquid treatment method
US7122121B1 (en) 2004-05-28 2006-10-17 Jiang Ji Advanced submerged membrane modules, systems and processes
US7282146B2 (en) 2004-05-28 2007-10-16 Siemens Water Technologies Corp. Removal system for membranes in a membrane filtration system
CA2571498A1 (en) 2004-07-02 2006-01-12 U.S. Filter Wastewater Group, Inc. Gas transfer membrane
JP3807423B2 (en) 2004-08-12 2006-08-09 栗田工業株式会社 Immersion membrane separator
NZ588094A (en) 2004-08-20 2012-04-27 Siemens Water Tech Corp Potting head for hollow fibre filter module
AU2005282211B2 (en) 2004-09-07 2011-04-21 Evoqua Water Technologies Llc Reduction of backwash liquid waste
WO2006029456A1 (en) 2004-09-14 2006-03-23 Siemens Water Technologies Corp. Methods and apparatus for removing solids from a membrane module
WO2006029465A1 (en) 2004-09-15 2006-03-23 Siemens Water Technologies Corp. Continuously variable aeration
US7172699B1 (en) 2004-10-13 2007-02-06 Eimco Water Technologies Llc Energy efficient wastewater treatment for nitrogen and phosphorus removal
US20060081533A1 (en) 2004-10-16 2006-04-20 Khudenko Boris M Batch-continuous process and reactor
JP2006116495A (en) 2004-10-25 2006-05-11 Sumitomo Electric Fine Polymer Inc Filter device
CN101065177B (en) 2004-11-02 2011-07-27 西门子水技术公司 Submerged cross-flow filtration
US7591950B2 (en) 2004-11-02 2009-09-22 Siemens Water Technologies Corp. Submerged cross-flow filtration
US7329344B2 (en) 2004-12-22 2008-02-12 Siemens Water Technologies Corp. Grease and scum removal in a filtration apparatus comprising a membrane bioreactor and a treatment vessel for digesting organic materials
WO2006066350A1 (en) 2004-12-24 2006-06-29 Siemens Water Technologies Corp. Simple gas scouring method and apparatus
ATE549076T1 (en) 2004-12-24 2012-03-15 Siemens Industry Inc CLEANING IN MEMBRANE FILTRATION SYSTEMS
NZ556400A (en) 2005-01-14 2011-05-27 Siemens Water Tech Corp Cleaning of membrane filtration system
US7279100B2 (en) * 2005-01-31 2007-10-09 Ashbrook Simon-Hartley Operations, Lp Methods and apparatus for treating wastewater employing a high rate clarifier and a membrane
US7501062B2 (en) 2005-02-22 2009-03-10 Shell Oil Company Process for permeation enhanced reactive extraction of levulinic acid
US7396453B1 (en) * 2005-04-19 2008-07-08 Procorp Enterprises, Llc Hydraulically integrated solids/liquid separation system for wastewater treatment
US9675938B2 (en) 2005-04-29 2017-06-13 Evoqua Water Technologies Llc Chemical clean for membrane filter
US7326343B2 (en) 2005-05-03 2008-02-05 University Of Western Ontario Canada Treatment of wastewater containing phosphorous and nitrogen
US7147777B1 (en) 2005-05-09 2006-12-12 Eimco Water Technologies Llc Wastewater treatment system with membrane separators and provision for storm flow conditions
US20060273038A1 (en) 2005-06-02 2006-12-07 Syed Murtuza A Chemical cleaning for membranes
EP1904216A4 (en) 2005-07-12 2008-11-19 Zenon Technology Partnership Process control for an immersed membrane system
US7850851B2 (en) 2005-08-12 2010-12-14 Siemens Water Technologies Corp. Biological phosphorus removal
KR20080045231A (en) 2005-08-22 2008-05-22 지멘스 워터 테크놀로지스 코포레이션 An assembly for water filtration using a tube manifold to minimise backwash
US20070045183A1 (en) 2005-08-26 2007-03-01 Murphy Dee T Purified water reclamation process
WO2007044442A2 (en) 2005-10-05 2007-04-19 Siemens Water Technologies Corp. Method and system for treating wastewater
WO2007044345A2 (en) 2005-10-05 2007-04-19 Siemens Water Technologies Corp. Method and apparatus for treating wastewater
WO2007044415A2 (en) 2005-10-05 2007-04-19 Siemens Water Technologies Corp. Method and apparatus for treating wastewater
US20070095754A1 (en) 2005-10-28 2007-05-03 Dennis Livingston Efficient MBR operation in wastewater treatment
KR20080075160A (en) 2005-11-08 2008-08-14 지멘스 워터 테크놀로지스 코포레이션 Combination membrane/biolytic filtration
US7314563B2 (en) 2005-11-14 2008-01-01 Korea Institute Of Science And Technology Membrane coupled activated sludge method and apparatus operating anoxic/anaerobic process alternately for removal of nitrogen and phosphorous
EP2700441A1 (en) 2005-12-09 2014-02-26 Siemens Industry, Inc. Reduced backwash volume process
ATE438591T1 (en) 2005-12-09 2009-08-15 Aquafin N V METHOD AND PLANT FOR TREATING WASTE WATER
US7147778B1 (en) 2006-01-05 2006-12-12 I. Kruger Inc. Method and system for nitrifying and denitrifying wastewater
US20090001018A1 (en) 2006-01-12 2009-01-01 Fufang Zha Operating Strategies in Filtration Processes
US7455765B2 (en) 2006-01-25 2008-11-25 Siemens Water Technologies Corp. Wastewater treatment system and method
US20100025320A1 (en) 2006-03-22 2010-02-04 Warren Thomas Johnson Backwash and cleaning method
US7481933B2 (en) 2006-04-11 2009-01-27 Siemens Water Technologies Corporation Process to improve the efficiency of a membrane filter activated sludge system
US7510655B2 (en) 2006-04-11 2009-03-31 Siemens Water Technologies Corp. Process to improve the efficiency of a membrane filter activated sludge system
US7713413B2 (en) 2006-04-11 2010-05-11 Siemens Water Technologies Corp. Aerated anoxic membrane bioreactor
FR2901488B1 (en) 2006-05-23 2008-08-15 Otv Sa AERATION DEVICE FOR IMMERSION MEMBRANE-BASED WATER FILTRATION SYSTEM INCLUDING FLOOR WITH GAS INJECTION MEANS AND AT LEAST ONE PRESSURE BALANCING SYSTEM
US7761826B1 (en) 2006-07-24 2010-07-20 Cadence Design Systems, Inc. Method and system for crosstalk analysis
AU2007291946B2 (en) 2006-08-31 2012-04-12 Evoqua Water Technologies Llc Low pressure backwash
DE102006044624B4 (en) 2006-09-19 2008-07-10 Koch Membrane Systems Gmbh Apparatus for fumigating a liquid
AU2008215180A1 (en) 2007-02-16 2008-08-21 Siemens Industry, Inc. Membrane filtration process and design
EP2129629A1 (en) 2007-04-02 2009-12-09 Siemens Water Technologies Corp. Improved infiltration/inflow control for membrane bioreactor
US20100051545A1 (en) 2007-04-04 2010-03-04 Warren Thomas Johnson Membrane module protection
US7459083B1 (en) 2007-05-07 2008-12-02 I. Kruger Inc. Method for controlling fouling of a membrane filter
KR20100023920A (en) 2007-05-29 2010-03-04 지멘스 워터 테크놀로지스 코포레이션 Membrane cleaning using an airlift pump
CA3058737C (en) 2007-05-29 2022-04-26 Fufang Zha Membrane cleaning with pulsed airlift pump
WO2009000035A1 (en) 2007-06-28 2008-12-31 Siemens Water Technologies Corp. Cleaning method for simple filtration systems
DE102007041991A1 (en) 2007-09-05 2009-03-12 Fülling, Rainer, Dr. Process for the purification of substrates by oxidants and reducing agents and the use of oxidizing agents for the oxidation of extracellular polymeric substances
JP5362343B2 (en) 2008-01-11 2013-12-11 旭化成ケミカルズ株式会社 Membrane separation unit
EP2331242B1 (en) 2008-07-24 2018-09-05 Evoqua Water Technologies LLC Frame system for membrane filtration modules
US20110132826A1 (en) 2008-08-14 2011-06-09 Siemens Water Technologies Corp. Block Configuration for Large Scale Membrane Distillation
JP2012500117A (en) 2008-08-20 2012-01-05 シーメンス ウォーター テクノロジース コーポレイション Improving backwash energy efficiency of membrane filtration systems.
WO2010141560A1 (en) 2009-06-02 2010-12-09 Siemens Water Technologies Corp. Membrane cleaning with pulsed gas slugs and global aeration
AU2010101488B4 (en) 2009-06-11 2013-05-02 Evoqua Water Technologies Llc Methods for cleaning a porous polymeric membrane and a kit for cleaning a porous polymeric membrane
US9358505B2 (en) 2009-09-03 2016-06-07 General Electric Company Gas sparger for an immersed membrane
US9364805B2 (en) 2010-10-15 2016-06-14 General Electric Company Integrated gas sparger for an immersed membrane

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5846425A (en) * 1994-07-22 1998-12-08 Whiteman; George R. Methods for treatment of waste streams
US5626755A (en) * 1995-11-08 1997-05-06 Micronair, Inc. Method and apparatus for waste digestion using multiple biological processes
US6723242B1 (en) * 1999-03-26 2004-04-20 Sumitomo Heavy Industries, Ltd. Method and apparatus for processing organic chlorine compounds
US20020185448A1 (en) * 1999-11-19 2002-12-12 Chisholm Robert D. Process and system for treatment of aqueous environments containing water soluble polymers
US20040007523A1 (en) * 2000-10-06 2004-01-15 Premier Wastewater International, Llc Apparatus and method for wastewater treatment with enhanced solids reduction (ESR)
US20030111412A1 (en) * 2001-10-24 2003-06-19 Samsung Engineering Co., Ltd. Batch style wastewater treatment apparatus using biological filtering process and wastewater treatment method using the same
US20040000517A1 (en) * 2002-06-17 2004-01-01 Iasis Usa, Lc Tidal vertical flow wastewater treatment system and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113860654A (en) * 2021-10-29 2021-12-31 段润芳 Efficient sewage treatment method based on MBR (membrane bioreactor) membrane

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