JPH05154362A - Membrane filter - Google Patents
Membrane filterInfo
- Publication number
- JPH05154362A JPH05154362A JP3349735A JP34973591A JPH05154362A JP H05154362 A JPH05154362 A JP H05154362A JP 3349735 A JP3349735 A JP 3349735A JP 34973591 A JP34973591 A JP 34973591A JP H05154362 A JPH05154362 A JP H05154362A
- Authority
- JP
- Japan
- Prior art keywords
- pump
- filtration
- water
- valve
- membrane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 62
- 238000001914 filtration Methods 0.000 claims abstract description 38
- 238000005406 washing Methods 0.000 claims abstract description 20
- 238000005374 membrane filtration Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 96
- 238000006073 displacement reaction Methods 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 description 16
- 238000000034 method Methods 0.000 description 9
- 230000008569 process Effects 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 239000010800 human waste Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000003621 irrigation water Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000001471 micro-filtration Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000008570 general process Effects 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Landscapes
- Rotary Pumps (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は河川水、湖沼水、し尿、
用水及び廃水などの原水に含まれる懸濁物を濾過するた
めの膜濾過装置に関する。The present invention relates to river water, lake water, human waste,
The present invention relates to a membrane filtration device for filtering suspensions contained in raw water such as irrigation water and waste water.
【0002】[0002]
【従来の技術】一般に精密濾過膜と称される膜の有する
孔径は、0.01〜数μmである。これらの孔径を有す
る精密濾過膜を分類すると膜の外側から内側に液体を濾
過する外圧型とその反対に膜の内側から外側に液体を濾
過する内圧型とに分類される。2. Description of the Related Art Generally, a microfiltration membrane has a pore size of 0.01 to several μm. Microfiltration membranes having these pore sizes are classified into an external pressure type that filters liquid from the outside to the inside of the membrane and an internal pressure type that filters liquid from the inside to the outside of the membrane.
【0003】外圧型の膜モジュールでは、0.5〜2時
間濾過継続後、数分間空気を用いてあるいは/および処
理水を用いて、膜の内側から外側に、空気洗浄あるいは
/および処理水洗浄の洗浄が行われる。また内圧型の膜
モジュールでは、濾過と同一または逆の方向に空気ある
いは/および処理水でフラッシングによる洗浄が行われ
る。この時濾過に必要な洗浄媒体に与える膜差圧はポン
プによる加圧か、あるいは吸引によって与えるのが一般
的である。In the external pressure type membrane module, after the filtration is continued for 0.5 to 2 hours, air or / and treated water is washed from the inside of the membrane to the outside by using air or / and treated water for several minutes. Is washed. Further, in the internal pressure type membrane module, flushing with air and / or treated water is performed in the same or opposite direction to the filtration. At this time, the transmembrane pressure difference applied to the cleaning medium necessary for filtration is generally applied by a pump or by suction.
【0004】一般的な工程では、膜濾過を行い次いで処
理水洗浄が行われるが、その場合、原水を送水するポン
プと洗浄水を送水するポンプが必要である。また当然送
水切替えのためには弁の設置が必要となる。水温が異な
ると水の粘性が異なり、濾過膜の面積、濾過膜の種類あ
るいは濾過差圧などの濾過条件を同一にして膜濾過を行
っても得られる処理水量は一定にならず、処理水量を一
定にするためには装置中に流量調節機構が必要となる。In a general process, membrane filtration is performed and then treated water is washed. In that case, a pump for feeding raw water and a pump for feeding wash water are required. Also, of course, it is necessary to install a valve for switching the water supply. If the water temperature is different, the viscosity of the water will be different, and the amount of treated water obtained will not be constant even if membrane filtration is performed with the same filtration conditions such as the area of the filtration membrane, the type of filtration membrane or the filtration differential pressure. In order to make it constant, a flow rate adjusting mechanism is required in the device.
【0005】送水用ポンプとして、通常最も一般的に用
いられる、うず巻きポンプを使用した場合には、原水送
水に使用する場合においてもまた洗浄に際し洗浄水を送
水する場合においても、上記の通り膜の汚染状況や水温
の違いなどの理由から膜透過の圧力損失が異なるため得
られる処理水量や必要とする洗浄水量が変動する。これ
らを一定に保つにはポンプの回転数の制御や水路に定流
量弁の設置などの流量調節機構が必要である。When a whirlpool pump, which is generally most commonly used as a water-feeding pump, is used, it is possible to use a membrane pump as described above, whether it is used to feed raw water or to feed wash water during washing. Since the pressure loss of the membrane permeation is different due to the condition of contamination and the difference in water temperature, the amount of treated water obtained and the required amount of washing water vary. In order to keep these constant, it is necessary to control the number of rotations of the pump and install a flow control mechanism such as installing a constant flow valve in the water channel.
【0006】また一般的には、外圧型膜モジュールの洗
浄において必要な洗浄水量は、処理水量の1〜3倍必要
である。Further, generally, the amount of washing water required for washing the external pressure type membrane module is 1 to 3 times the amount of treated water.
【0007】図2に外圧型濾過膜を用い、加圧ポンプで
原水を濾過膜に送水し、処理水を得て、該処理水により
濾過膜を洗浄ポンプにより洗浄するシステムのフロー図
を示した。詳しくは図において、加圧ポンプ10により
原水供給管11から原水を膜モジュール12に原水弁1
3を介して送水し、原水を濾過して得られた処理水は膜
モジュール12の集水部から処理水配管14に設けた流
出弁15と定量弁16(あるいは流量調節弁)を介して
処理水槽17に送られる。FIG. 2 shows a flow chart of a system in which an external pressure type filtration membrane is used, raw water is sent to the filtration membrane by a pressure pump to obtain treated water, and the treatment membrane is used to wash the filtration membrane with a washing pump. .. Specifically, in the figure, the raw water is supplied from the raw water supply pipe 11 to the membrane module 12 by the pressure pump 10 and the raw water valve 1
The treated water obtained by filtering the raw water is treated through the outflow valve 15 and the metering valve 16 (or the flow control valve) provided in the treated water pipe 14 from the water collecting portion of the membrane module 12. It is sent to the aquarium 17.
【0008】濾過膜の目詰まりが進んで濾過抵抗が一定
値まで上昇したした時、加圧ポンプ10を停止し、流出
弁15を閉にし、処理水槽17から洗浄用配管18に設
けた洗浄弁19および膜モジュール12の排水弁21を
開き、洗浄ポンプ22を運転して膜モジュール12を洗
浄する。必要とする洗浄水量は定量弁20によって制御
される。このように図2に示したシステムでは2台のポ
ンプと6個の弁の設置が必要である。When the filtration membrane is clogged and the filtration resistance rises to a certain value, the pressurizing pump 10 is stopped, the outflow valve 15 is closed, and the cleaning valve provided from the treated water tank 17 to the cleaning pipe 18 is used. 19 and the drain valve 21 of the membrane module 12 are opened, and the washing pump 22 is operated to wash the membrane module 12. The amount of wash water required is controlled by the metering valve 20. Thus, the system shown in FIG. 2 requires the installation of two pumps and six valves.
【0009】図3には外圧型濾過膜を用い、吸引ポンプ
で原水を濾過膜に吸引し、処理水を得て、該処理水によ
り濾過膜を洗浄ポンプにより洗浄するシステムのフロー
図を示した。図において、吸引ポンプ30により原水供
給管31から原水を膜モジュール32に原水弁33を介
して送水し、原水を濾過して得られた処理水は膜モジュ
ール32の集水部から処理水配管34に設けた流出弁3
5と定量弁36(あるいは流量調節弁)を介して処理水
槽37に送られる。FIG. 3 shows a flow chart of a system in which an external pressure type filter membrane is used, raw water is sucked into the filter membrane by a suction pump to obtain treated water, and the treated membrane is washed with a washing pump. .. In the figure, raw water is sent from a raw water supply pipe 31 to a membrane module 32 via a raw water valve 33 by a suction pump 30, and treated water obtained by filtering the raw water is treated water pipe 34 from a water collecting portion of the membrane module 32. Outflow valve 3
5 and the metering valve 36 (or the flow rate control valve) to the treated water tank 37.
【0010】濾過膜の目詰まりが進んで濾過抵抗が一定
値まで上昇したした時、吸引ポンプ30を停止し、流出
弁35を閉にし、処理水槽37から洗浄用配管38に設
けた洗浄弁39および膜モジュール32の排水弁41を
開き、洗浄ポンプ42を運転して膜モジュール32を洗
浄する。必要とする洗浄水量は定量弁40によって制御
される。このように図3に示したシステムでも2台のポ
ンプと6個の弁の設置が必要である。When the filtration resistance has risen to a certain value due to the progress of clogging of the filtration membrane, the suction pump 30 is stopped, the outflow valve 35 is closed, and the washing valve 39 provided in the washing pipe 38 from the treated water tank 37. And the drain valve 41 of the membrane module 32 is opened, and the washing pump 42 is operated to wash the membrane module 32. The required amount of cleaning water is controlled by the metering valve 40. Thus, the system shown in FIG. 3 also requires the installation of two pumps and six valves.
【0011】[0011]
【発明が解決しようとする課題】本発明は、槽内に膜モ
ジュールが配備されている膜濾過装置において、膜モジ
ュールによる濾過および洗浄の工程を1台の送水ポンプ
で行い、かつ原水弁および排水弁以外の弁を不要にす
る、簡素にして効率の良い濾過および洗浄を実現するこ
とができる膜濾過装置を提供することにある。DISCLOSURE OF THE INVENTION The present invention is a membrane filtration device in which a membrane module is provided in a tank, and the steps of filtration and washing by the membrane module are performed by one water pump, and a raw water valve and drainage are provided. It is an object of the present invention to provide a membrane filtration device that does not require a valve other than a valve and can realize simple and efficient filtration and cleaning.
【0012】[0012]
【課題を解決するための手段】上記課題は、少なくとも
外圧型膜モジュールが配備されている膜濾過装置におい
て、容積ネジポンプにて該外圧型膜モジュールの濾過用
ポンプおよび洗浄用ポンプを兼用させるシステムとする
ことを特徴とする膜濾過装置によって達成される。Means for Solving the Problems The above problem is to provide a membrane filtration device in which at least an external pressure type membrane module is provided, and a system in which a volumetric screw pump is used as both a filtration pump and a cleaning pump of the external pressure type membrane module. It is achieved by a membrane filtration device characterized by:
【0013】本発明に使用する容積ネジポンプは容量式
ポンプであるため送水量が一定であり、送水量の変更は
ポンプの回転数の制御によって行える。またモータは逆
回転することが可能で、モータを逆回転することにより
送水量の定流量性を保ったまま送水方向が逆にできるの
で、濾過用および洗浄用ポンプを兼用させることができ
る。本発明に使用する容積ネジポンプとしては特に一軸
偏心ネジポンプが好ましく利用される。Since the positive displacement screw pump used in the present invention is a positive displacement pump, the amount of water supplied is constant, and the amount of water supplied can be changed by controlling the rotational speed of the pump. Further, the motor can be rotated in the reverse direction, and by rotating the motor in the reverse direction, the water supply direction can be reversed while maintaining the constant flow rate of the water supply amount, so that it can be used as both a filtering pump and a cleaning pump. A uniaxial eccentric screw pump is particularly preferably used as the positive displacement screw pump used in the present invention.
【0014】膜モジュールが配備されている膜濾過装置
とは、一般的には該膜濾過装置に内圧型膜モジュールや
外圧型膜モジュールが用いられ、これら膜濾過装置が全
体としてその濾過および洗浄工程が1台の容積ネジポン
プで稼働されてもよいことを意味する。The membrane filtration device provided with a membrane module is generally an internal pressure type membrane module or an external pressure type membrane module, and these membrane filtration devices as a whole are subjected to the filtration and washing steps. May be operated with one positive displacement screw pump.
【0015】河川水、湖沼水、し尿、用水及び廃水など
の原水に含まれる懸濁物を濾過する場合には、膜濾過装
置をこれら原水槽中に浸漬して吸引方式で原水を膜濾過
することが有利な膜濾過方法であり、従って膜モジュー
ルを原水槽中に浸漬して吸引方式で原水を膜濾過するこ
とが好ましい態様である。When filtering a suspension contained in raw water such as river water, lake water, human waste, irrigation water, waste water, etc., the raw water is subjected to membrane filtration by a suction method by immersing the membrane filtration device in these raw water tanks. It is an advantageous membrane filtration method, and therefore, it is a preferred embodiment to immerse the membrane module in a raw water tank to perform membrane filtration of raw water by a suction method.
【0016】外圧型膜モジュールに使用する膜の形式
は、中空糸膜でもセラミック膜でも構わない。また膜濾
過装置は、開放槽に浸漬させて使用するタイプでも密閉
ケースに膜を封入したタイプでもよいが、開放槽に浸漬
させて使用するタイプが好ましい。開放槽に浸漬させて
使用するタイプの場合には、多くの場合送水を吸引方式
で行うのが便利である。The type of membrane used for the external pressure type membrane module may be a hollow fiber membrane or a ceramic membrane. The membrane filtration device may be of a type that is used by being immersed in an open tank or a type in which a membrane is sealed in a closed case, but a type of being used by being immersed in an open tank is preferable. In the case of the type that is used by immersing it in an open tank, it is convenient in most cases to use a suction method for water supply.
【0017】一軸偏心ネジポンプの吸引可能圧が約−8
mAqであるので、本発明において、一軸偏心ネジポン
プを使用して行う場合には適用される膜は膜の差圧とし
て0.8kg/cm2 程度以下で透過水が得られるもの
とする。The suction pressure of the uniaxial eccentric screw pump is about -8.
Since it is mAq, in the present invention, when the uniaxial eccentric screw pump is used, the membrane to be applied is such that permeated water can be obtained at a membrane pressure difference of about 0.8 kg / cm 2 or less.
【0018】本発明の膜濾過装置は活性汚泥法による汚
水処理にも利用することができ、活性汚泥処理の沈澱池
の代わりに利用したり、処理槽に活性汚泥を存在させて
生物処理するようにすることもでき、活性汚泥処理工程
の効率化をはかることもできる。The membrane filtration device of the present invention can also be used for the treatment of sewage by the activated sludge method, and can be used in place of the settling basin for activated sludge treatment, or for biological treatment by allowing activated sludge to exist in the treatment tank. The efficiency of the activated sludge treatment process can be improved.
【0019】[0019]
【実施例】以下、本発明の具体的実施例を示すが、本発
明はこれに限定されるものではない。図1に示した、開
放槽に外圧型膜モジュールを浸漬した膜濾過装置の図を
用いて本発明を説明すると、原水は原水供給管1から原
水弁2を経由して外圧型膜モジュール3に導入される。
一軸偏心ネジポンプ4により原水は外圧型膜モジュール
3を通過して吸引され処理水配管7を通って処理槽6に
流入する。処理水の流量はポンプの回転数制御装置から
の信号で一軸偏心ネジポンプ4のモータの回転数を制御
して行う。EXAMPLES Specific examples of the present invention will be shown below, but the present invention is not limited thereto. The present invention will be described with reference to the membrane filtration device shown in FIG. 1 in which an external pressure type membrane module is immersed in an open tank. Raw water is transferred from a raw water supply pipe 1 to an external pressure type membrane module 3 via a raw water valve 2. be introduced.
Raw water passes through the external pressure type membrane module 3 and is sucked by the uniaxial eccentric screw pump 4 and flows into the treatment tank 6 through the treated water pipe 7. The flow rate of the treated water is controlled by controlling the rotation speed of the motor of the uniaxial eccentric screw pump 4 by a signal from the rotation speed control device of the pump.
【0020】濾過膜の目詰まりが進んで濾過抵抗が一定
値まで上昇したした時、処理水による濾過膜の洗浄は原
水弁2を閉に、排水弁9を開として一軸偏心ネジポンプ
4のポンプを逆回転させて行う。この時洗浄水は処理水
槽6より処理水配管7を通って外圧型膜モジュール3に
送られ、膜内部から外部へ通過し、排水弁8を通って排
水される。この洗浄水量はやはり回転数制御装置からの
信号で一軸偏心ネジポンプ4のモータの回転数を制御し
て行う。When the filtration resistance has risen to a certain value due to the progress of the clogging of the filtration membrane, the raw water valve 2 is closed and the drain valve 9 is opened to clean the filtration membrane with the treated water. Reverse rotation is performed. At this time, the wash water is sent from the treated water tank 6 to the external pressure type membrane module 3 through the treated water pipe 7, passes from the inside of the membrane to the outside, and is drained through the drain valve 8. The amount of washing water is controlled by controlling the rotation speed of the motor of the uniaxial eccentric screw pump 4 by a signal from the rotation speed control device.
【0021】必要な洗浄水量は、処理水量の1〜3倍必
要であるので洗浄時一軸偏心ネジポンプ4のモータの回
転数は濾過時よりも高くするよう制御する。Since the required amount of washing water is 1 to 3 times the amount of treated water, the number of rotations of the motor of the uniaxial eccentric screw pump 4 during washing is controlled to be higher than that during filtration.
【0022】[0022]
【発明の効果】本発明は膜濾過装置に容積ネジポンプと
その回転数の制御を行う制御器とを組み込むことによ
り、濾過と洗浄とを1台の容積ネジポンプを用いて行
い、従来の濾過装置に組み込まれていた原水送水ポンプ
や洗浄水供給ポンプの2台のポンプが1台で済み、さら
に処理水流水弁、定流量弁や洗浄弁などの4個の弁を不
要にでき、膜濾過装置と処理水槽を容積ネジポンプを介
して1本の配管で連絡できるので装置として従来方式に
比べて極めてシンプルになり、メンテナンスが大幅に軽
減された。According to the present invention, a volumetric screw pump and a controller for controlling the number of revolutions thereof are incorporated in a membrane filtration device, so that filtration and washing are performed by using one volumetric screw pump, and the conventional filtration device is realized. The two pumps, the raw water feed pump and the wash water supply pump, which were built in, can be used in one unit, and the four valves such as the treated water flow valve, the constant flow valve and the wash valve can be eliminated, and the membrane filtration device can be used. Since the treated water tank can be connected with a single pipe via a positive displacement screw pump, the device is much simpler than the conventional system and the maintenance is greatly reduced.
【図1】図1は本発明の開放槽に外圧型膜モジュールを
浸漬した膜濾過装置を一軸偏心ネジポンプとその回転制
御装置によって操作して濾過を行う工程フロー図。FIG. 1 is a process flow chart of performing filtration by operating a membrane filtration device in which an external pressure type membrane module is immersed in an open tank of the present invention by a uniaxial eccentric screw pump and its rotation control device.
【図2】図2は加圧ポンプと洗浄用ポンプを使用し、弁
により濾過や洗浄を制御する従来の膜濾過装置の工程フ
ロー図。FIG. 2 is a process flow diagram of a conventional membrane filtration device in which a pressurizing pump and a cleaning pump are used, and filtration and cleaning are controlled by a valve.
【図3】図3は吸引ポンプと洗浄用ポンプを使用し、弁
により濾過や洗浄を制御する従来の膜濾過装置の工程フ
ロー図。FIG. 3 is a process flow diagram of a conventional membrane filtration device in which a suction pump and a cleaning pump are used and a valve controls filtration and cleaning.
1 原水供給管 2 原水弁 3 膜モジュール 4 一軸偏心ネジポンプ 6 処理水槽 7 処理水配管 8 排水弁 10 加圧ポンプ 11 原水供給管 12 膜モジュール 13 原水弁 14 処理水配管 15 流出弁 16 定量弁 17 処理水槽 18 洗浄用配管 19 洗浄弁 20 定量弁 21 排水弁 22 洗浄ポンプ 30 吸引ポンプ 31 原水供給管 32 膜モジュール 33 原水弁 34 処理水配管 35 流出弁 36 定量弁 37 処理水槽 38 洗浄用配管 39 洗浄弁 40 定量弁 41 排水弁 42 洗浄ポンプ 1 Raw water supply pipe 2 Raw water valve 3 Membrane module 4 Uniaxial eccentric screw pump 6 Treated water tank 7 Treated water pipe 8 Drain valve 10 Pressurizing pump 11 Raw water supply pipe 12 Membrane module 13 Raw water valve 14 Treated water pipe 15 Outflow valve 16 Quantitative valve 17 Treatment Water tank 18 Cleaning pipe 19 Cleaning valve 20 Metering valve 21 Drain valve 22 Cleaning pump 30 Suction pump 31 Raw water supply pipe 32 Membrane module 33 Raw water valve 34 Treated water pipe 35 Outflow valve 36 Quantitative valve 37 Treated water tank 38 Cleaning pipe 39 Wash valve 40 Metering valve 41 Drain valve 42 Cleaning pump
Claims (1)
濾過装置において、容積ネジポンプにて該膜モジュール
の濾過用ポンプおよび洗浄用ポンプを兼用させるシステ
ムとすることを特徴とする膜濾過装置。1. A membrane filtration apparatus in which a membrane module is provided in a tank, wherein the volumetric screw pump serves as a filtration pump and a washing pump for the membrane module.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3349735A JP2684483B2 (en) | 1991-12-10 | 1991-12-10 | Membrane filtration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3349735A JP2684483B2 (en) | 1991-12-10 | 1991-12-10 | Membrane filtration device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05154362A true JPH05154362A (en) | 1993-06-22 |
JP2684483B2 JP2684483B2 (en) | 1997-12-03 |
Family
ID=18405753
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3349735A Expired - Fee Related JP2684483B2 (en) | 1991-12-10 | 1991-12-10 | Membrane filtration device |
Country Status (1)
Country | Link |
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JP (1) | JP2684483B2 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1063674C (en) * | 1996-08-16 | 2001-03-28 | 中国科学院生态环境研究中心 | Method and apparatus for using operating pump to negative pressure cleaning by semipermeable membrance |
US7025885B2 (en) | 1998-11-23 | 2006-04-11 | Zenon Environmental Inc. | Water filtration using immersed membranes |
US7063788B2 (en) | 1995-08-11 | 2006-06-20 | Zenon Environmental Inc. | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US7087173B2 (en) | 1995-08-11 | 2006-08-08 | Zenon Environmental Inc. | Inverted cavity aerator for membrane module |
CN1317056C (en) * | 2005-03-28 | 2007-05-23 | 天津大学 | Flushing method of hollow fiber membrane filter device |
JP2007313508A (en) * | 1995-07-25 | 2007-12-06 | Otv Omnium De Traitements & De Valorisation | Biological water treatment facility for drinking water production |
US7537701B2 (en) | 1995-08-11 | 2009-05-26 | Zenon Technology Partnership | Membrane filtration module with adjustable header spacing |
USRE42669E1 (en) | 1995-08-11 | 2011-09-06 | Zenon Technology Partnership | Vertical cylindrical skein of hollow fiber membranes and method of maintaining clean fiber surfaces |
US8852438B2 (en) | 1995-08-11 | 2014-10-07 | Zenon Technology Partnership | Membrane filtration module with adjustable header spacing |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03169309A (en) * | 1989-11-28 | 1991-07-23 | Nkk Corp | How to backwash a filter |
-
1991
- 1991-12-10 JP JP3349735A patent/JP2684483B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03169309A (en) * | 1989-11-28 | 1991-07-23 | Nkk Corp | How to backwash a filter |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007313508A (en) * | 1995-07-25 | 2007-12-06 | Otv Omnium De Traitements & De Valorisation | Biological water treatment facility for drinking water production |
US7063788B2 (en) | 1995-08-11 | 2006-06-20 | Zenon Environmental Inc. | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US7087173B2 (en) | 1995-08-11 | 2006-08-08 | Zenon Environmental Inc. | Inverted cavity aerator for membrane module |
US7534353B2 (en) | 1995-08-11 | 2009-05-19 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US7537701B2 (en) | 1995-08-11 | 2009-05-26 | Zenon Technology Partnership | Membrane filtration module with adjustable header spacing |
US7615157B2 (en) | 1995-08-11 | 2009-11-10 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
USRE42669E1 (en) | 1995-08-11 | 2011-09-06 | Zenon Technology Partnership | Vertical cylindrical skein of hollow fiber membranes and method of maintaining clean fiber surfaces |
US8075776B2 (en) | 1995-08-11 | 2011-12-13 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
US8852438B2 (en) | 1995-08-11 | 2014-10-07 | Zenon Technology Partnership | Membrane filtration module with adjustable header spacing |
CN1063674C (en) * | 1996-08-16 | 2001-03-28 | 中国科学院生态环境研究中心 | Method and apparatus for using operating pump to negative pressure cleaning by semipermeable membrance |
US7025885B2 (en) | 1998-11-23 | 2006-04-11 | Zenon Environmental Inc. | Water filtration using immersed membranes |
CN1317056C (en) * | 2005-03-28 | 2007-05-23 | 天津大学 | Flushing method of hollow fiber membrane filter device |
Also Published As
Publication number | Publication date |
---|---|
JP2684483B2 (en) | 1997-12-03 |
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