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JPH09290261A - Purified water manufacturing equipment - Google Patents

Purified water manufacturing equipment

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Publication number
JPH09290261A
JPH09290261A JP13085296A JP13085296A JPH09290261A JP H09290261 A JPH09290261 A JP H09290261A JP 13085296 A JP13085296 A JP 13085296A JP 13085296 A JP13085296 A JP 13085296A JP H09290261 A JPH09290261 A JP H09290261A
Authority
JP
Japan
Prior art keywords
reverse osmosis
membrane module
osmosis membrane
pump
outlet
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.)
Pending
Application number
JP13085296A
Other languages
Japanese (ja)
Inventor
Yuji Nishida
祐二 西田
Hajime Hisada
肇 久田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nitto Denko Corp
Original Assignee
Nitto Denko Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nitto Denko Corp filed Critical Nitto Denko Corp
Priority to JP13085296A priority Critical patent/JPH09290261A/en
Publication of JPH09290261A publication Critical patent/JPH09290261A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

(57)【要約】 【課題】河川水等の濁質原水を精密濾過膜または限外濾
過膜で前処理のうえ、逆浸透膜モジュ−ルにより浄水と
する場合、装置の全体構造の簡易化、運転の簡易化及び
逆浸透膜モジュ−ルの塩素類やバクテリヤ等による劣化
の確実な排除を保証し得る浄水の製造装置を提供する。 【解決手段】原水タンク1内に全量濾過式の精密濾過ま
たは限外濾過膜エレメント2を浸漬設置し、該濾過膜エ
レメント2の濾過液出口810をポンプ4を介してクロ
スフロ−方式の逆浸透膜モジュ−ル3の原液供給口31
に連通し、該逆浸透膜モジュ−ル3の濃縮原液出口32
を上記ポンプ4の入口側に連通した。
(57) [Abstract] [Problem] Simplification of the overall structure of an apparatus when raw turbid water such as river water is pretreated with a microfiltration membrane or an ultrafiltration membrane and purified by a reverse osmosis membrane module. Provided is an apparatus for producing purified water which can guarantee the simplification of operation and the reliable elimination of deterioration of a reverse osmosis membrane module due to chlorine and bacteria. SOLUTION: A full-volume filtration type microfiltration or ultrafiltration membrane element 2 is immersed in a raw water tank 1 and a filtrate outlet 810 of the filtration membrane element 2 is passed through a pump 4 to a cross flow type reverse osmosis membrane. Undiluted solution supply port 31 of module 3
And a concentrated stock solution outlet 32 of the reverse osmosis membrane module 3.
Was communicated with the inlet side of the pump 4.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、河川水等を原水と
して浄水を製造する場合に使用する浄水製造装置に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a purified water producing apparatus used when producing purified water using river water or the like as raw water.

【0002】[0002]

【従来の技術】河川水、湖水、地下水等を原水として浄
水を得る場合、伝統的に凝集沈殿砂濾過法が使用されて
きたが、近来、維持管理の簡易化、ランニングコストの
軽減、設置スペ−スの低減等を図るために、膜分離法が
重視されている。膜分離法に使用される膜には、精密濾
過膜、限外濾過膜及び逆浸透膜等が存在するが、精密濾
過膜や限外濾過膜等では除去が困難なトリハロメタン等
の有害物質をも完全に除去するために、逆浸透膜モジュ
−ルの使用が要求されている。
2. Description of the Related Art When obtaining purified water from river water, lake water, groundwater, etc. as raw water, the coagulation sedimentation sand filtration method has been traditionally used, but recently, maintenance and management is simplified, running cost is reduced, and installation space is reduced. -The membrane separation method is emphasized in order to reduce the amount of waste. Membranes used in the membrane separation method include microfiltration membranes, ultrafiltration membranes and reverse osmosis membranes, but they also contain harmful substances such as trihalomethane that are difficult to remove with microfiltration membranes or ultrafiltration membranes. The use of reverse osmosis membrane modules is required for complete removal.

【0003】この逆浸透膜モジュ−ルの主流は、スパイ
ラル型膜モジュ−ルである。このスパイラル型膜モジュ
−ルにおいては、内部に透過液流路保持材(例えば、不
織布、プラスチックネット)を納めた膜封筒を集液管の
周囲に原液流路保持材(例えば、プラスチックネット)
と共にスパイラル状に巻回し、この膜封筒の開口を集液
管内に連通した膜エレメントを筒状ケ−ス内に収納し、
筒状ケ−スの一端に原液供給口を、胴ケ−スの他端に濃
縮原液出口をそれぞれ設け、上記スパイラル巻回層間に
原水を流通させ、集液管から透過液を取り出している。
このスパイラル型膜モジュ−ルでは、外径を抑え、かつ
膜面積を広くするために、上記スパイラル巻回層間の原
液流路の間隙をかなり狭くしており、濁質の原水を直接
流すと、原水通路の閉塞が避けられないので、原水を汚
水指数 4以下に前処理することが必要であり、その前
処理に精密濾過膜モジュ−ルまたは限外濾過膜モジュ−
ルを使用することが公知である。
The mainstream of this reverse osmosis membrane module is a spiral wound type membrane module. In this spiral type membrane module, a membrane envelope containing a permeated liquid flow path holding material (for example, non-woven fabric, plastic net) inside is provided with a raw liquid flow path holding material (for example, plastic net) around a liquid collection tube.
A spiral wound with the membrane element, the membrane element having the opening of the membrane envelope communicated with the liquid collection tube is housed in the tubular case,
A stock solution supply port is provided at one end of the cylindrical case, and a concentrated stock solution outlet is provided at the other end of the barrel case. The raw water is circulated between the spirally wound layers, and the permeate is taken out from the liquid collection tube.
In this spiral type membrane module, in order to suppress the outer diameter and widen the membrane area, the gap of the raw solution flow path between the spiral winding layers is considerably narrowed, and when the raw water of turbidity is directly flowed, Since clogging of the raw water passage is unavoidable, it is necessary to pretreat the raw water to a sewage index of 4 or less. For the pretreatment, a microfiltration membrane module or an ultrafiltration membrane module is required.
It is known to use

【0004】図5は精密濾過膜モジュ−ルまたは限外濾
過膜モジュ−ルで前処理したうえで、逆浸透膜モジュ−
ルで本処理する公知の浄水ラインを示し、原水を原水供
給配管11’で原水タンク1’に溜め、この原水をポン
プ41’で前処理膜モジュ−ル2’に加圧送入してクロ
スフロ−方式で濾過し濃縮液を原水タンク1’に戻すと
共に濾過液を一旦一次処理水タンク10’に溜め、更に
この一次処理水をポンプ42’で逆浸透膜モジュ−ル
3’に加圧送入してクロスフロ−方式で透過処理し濃縮
液を一次処理水タンク10’に戻すと共に濾過液を浄水
タンク7’に溜め、浄水として使用している。
FIG. 5 shows a reverse osmosis membrane module after pretreatment with a microfiltration membrane module or an ultrafiltration membrane module.
A well-known water purification line for main treatment is shown in FIG. 1 in which raw water is stored in a raw water tank 1 ′ through a raw water supply pipe 11 ′, and the raw water is pumped into a pretreatment membrane module 2 ′ by a pump 41 ′ to cross flow. The concentrated solution is filtered by the method and returned to the raw water tank 1 ', the filtrate is once stored in the primary treated water tank 10', and this primary treated water is pumped into the reverse osmosis membrane module 3'by the pump 42 '. Then, the concentrated liquid is returned to the primary treated water tank 10 'by permeation treatment by a cross flow method and the filtrate is stored in the purified water tank 7'and used as purified water.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記の
浄水製造設備では、前処理工程で精密濾過膜モジュ−ル
または限外濾過膜モジュ−ル2’により菌体が除去され
るにもかかわらず、一次処理水タンク10’での貯水時
にバクテリヤが繁殖し易く、非衛生的であり、逆浸透膜
モジュ−ル3’の膜の種類によっては膜がバリテリヤで
分解される畏れもあり、また、殺菌用の塩素類を注入す
れば、膜酸化・劣化の危険性が生じる。更に、タンクを
三基も必要とし、設置スペ−スの広大化が避けられず、
ポンプも二基必要とし、ランニングコストのアップや全
体を連動させるための制御装置が複雑化も免れ得ない。
However, in the above-mentioned purified water production equipment, although the bacterial cells are removed by the microfiltration membrane module or the ultrafiltration membrane module 2'in the pretreatment step, Bacteria easily proliferate during water storage in the primary treated water tank 10 ', which is unsanitary, and depending on the type of membrane of the reverse osmosis membrane module 3', there is a fear that the membrane will be decomposed by variteria, and sterilization is also possible. If chlorine for injection is injected, there is a risk of film oxidation and deterioration. Furthermore, three tanks are required, and the expansion of the installation space is inevitable,
It requires two pumps, which increases running costs and complicates the control device for interlocking the entire system.

【0006】本発明の目的は、河川水等の濁質原水を精
密濾過膜または限外濾過膜で前処理のうえ、逆浸透膜モ
ジュ−ルにより浄水とする場合、装置の全体構造の簡易
化、運転の簡易化及び逆浸透膜モジュ−ルの塩素類やバ
クテリヤ等による劣化の確実な排除を保証し得る浄水の
製造装置を提供することにある。
The object of the present invention is to simplify the overall structure of the apparatus when raw turbid water such as river water is pretreated with a microfiltration membrane or an ultrafiltration membrane and then purified with a reverse osmosis membrane module. Another object of the present invention is to provide an apparatus for producing purified water which can guarantee the simplification of operation and the reliable elimination of deterioration of the reverse osmosis membrane module due to chlorine and bacteria.

【0007】[0007]

【課題を解決するための手段】本発明に係る浄水の一の
製造装置は、原水タンク内に全量濾過式の精密濾過また
は限外濾過膜エレメントを浸漬設置し、該濾過膜エレメ
ントの濾過液出口をポンプを介してクロスフロ−方式の
逆浸透膜モジュ−ルの原液供給口に連通し、該逆浸透膜
モジュ−ルの濃縮原液出口を上記ポンプの入口側に連通
したことを特徴とする構成である。本発明に係る浄水の
他の製造装置は、原水タンク内に全量濾過式の精密濾過
または限外濾過膜エレメントを浸漬設置し、逆浸透膜モ
ジュ−ルの濃縮原液出口にポンプを、該ポンプの出口に
エゼクタをそれぞれ連通し、エゼクタの吸入口に前記濾
過膜エレメントの濾過液出口を連通したことを特徴とす
る構成である。
One of the apparatus for producing purified water according to the present invention is a raw water tank in which a total filtration type microfiltration or ultrafiltration membrane element is immersed and installed, and a filtrate outlet of the filtration membrane element. Is connected to a stock solution supply port of a cross flow type reverse osmosis membrane module via a pump, and a concentrated stock solution outlet of the reverse osmosis membrane module is connected to an inlet side of the pump. is there. Another apparatus for producing purified water according to the present invention is a total water filtration type microfiltration or ultrafiltration membrane element immersed in a raw water tank, and a pump is installed at the concentrated stock solution outlet of a reverse osmosis membrane module. The ejector is communicated with the outlet, and the filtrate outlet of the filtration membrane element is communicated with the intake of the ejector.

【0008】[0008]

【発明の実施の形態】以下、図面を参照しつつ本発明の
実施の形態について説明する。図1は本発明に係る浄水
の一の製造装置の実施例を示す説明図である。図1にお
いて、1は原水タンク、11は原水供給配管である。2
は原水タンク1内に浸漬設置した精密濾過または限外濾
過膜エレメントであり、濾過液側の吸引・減圧で発生さ
れる膜間差圧によって全量濾過方式で操作される構成で
ある。この精密濾過または限外濾過膜エレメントの膜に
は、平膜や中空糸膜を使用できる。例えば、図2の
(イ)及び図2の(ロ)〔図2の(イ)におけるロ−ロ
断面図〕に示すように、両端にダクト811を有する枠
縁81に平膜82を融着または接着剤により貼着すると
共に膜82,82間に濾過液流路保持材83(不織布、
プラスチックネット等)を介在させ、ダクト811に濾
過液取出し管812を取り付けた膜エレメント部材aを
図3に示すように、ラック84に装着したものを使用で
きる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is an explanatory diagram showing an embodiment of an apparatus for producing purified water according to the present invention. In FIG. 1, 1 is a raw water tank, and 11 is a raw water supply pipe. Two
Is a microfiltration or ultrafiltration membrane element immersed in the raw water tank 1 and operated by a total volume filtration method by the transmembrane pressure difference generated by suction / decompression on the filtrate side. A flat membrane or a hollow fiber membrane can be used as the membrane of the microfiltration or ultrafiltration membrane element. For example, as shown in (a) of FIG. 2 and (b) of FIG. 2 [a cross sectional view taken along line (a) of FIG. 2], a flat film 82 is fused to a frame edge 81 having ducts 811 at both ends. Alternatively, the filtered liquid flow path holding material 83 (nonwoven fabric,
As shown in FIG. 3, a membrane element member a having a filtered liquid take-out pipe 812 attached to a duct 811 via a plastic net or the like may be attached to a rack 84 as shown in FIG.

【0009】図1において、3はクロスフロ−方式で使
用される逆浸透膜モジュ−ルであり、この逆浸透膜モジ
ュ−ル3の原液供給口31に濾過膜エレメント2の濾過
液出口810をポンプ4を介して連通してある。5は逆
浸透膜モジュ−ル3の濃縮液出口32をポンプ4の入口
側に連通するリタ−ン配管、6はリタ−ン配管5中に設
けた調圧弁である。7は逆浸透膜モジュ−ル3の透過液
出口33に連通した浄水タンクである。
In FIG. 1, reference numeral 3 denotes a reverse osmosis membrane module used in a cross flow system, and a filtrate outlet 810 of a filtration membrane element 2 is pumped to a stock solution supply port 31 of the reverse osmosis membrane module 3. It communicates via 4. Reference numeral 5 is a return pipe that connects the concentrated liquid outlet 32 of the reverse osmosis membrane module 3 to the inlet side of the pump 4, and 6 is a pressure regulating valve provided in the return pipe 5. Reference numeral 7 is a water purification tank communicating with the permeate outlet 33 of the reverse osmosis membrane module 3.

【0010】本発明に係る浄水製造装置は、河川水、湖
水、地下水等を原水として浄水を得る場合に使用され、
図1において、原水タンク1に原水が溜っている。浄水
を製造するには、ポンプ4を駆動し、調圧弁6の絞り度
を調節しつつ逆浸透膜モジュ−ル3の原液室圧力を上昇
させていく。この圧力上昇により逆浸透膜モジュ−ル3
での透過が行われると共に濾過膜エレメント2の濾過液
側が減圧されて濾過膜エレメント2での濾過が行われ、
定常状態に達すると、濾過膜エレメント2の濾過流束と
逆浸透膜モジュ−ル3の透過流束とがバランスし、逆浸
透膜モジュ−ル3の透過液出口33から浄水タンク7に
ほぼ一定流量で浄水が流入されていく。上記定常濾過流
束または透過流束は、ポンプ4の回転速度や調圧弁6の
絞り度により定まり、図5に示す従来例とは異なり、ポ
ンプ間の連動といつた厄介な操作は不要である。
The purified water producing apparatus according to the present invention is used for obtaining purified water by using river water, lake water, groundwater, etc. as raw water.
In FIG. 1, raw water is stored in a raw water tank 1. To produce purified water, the pump 4 is driven to increase the stock solution chamber pressure of the reverse osmosis membrane module 3 while adjusting the degree of restriction of the pressure regulating valve 6. This pressure increase causes reverse osmosis membrane module 3
And the filtrate side of the filtration membrane element 2 is decompressed and filtration is performed by the filtration membrane element 2.
When the steady state is reached, the filtration flux of the filtration membrane element 2 and the permeation flux of the reverse osmosis membrane module 3 are balanced, and the permeate outlet 33 of the reverse osmosis membrane module 3 is almost constant in the purified water tank 7. Purified water flows in at a flow rate. The steady-state filtration flux or permeation flux is determined by the rotation speed of the pump 4 and the throttling degree of the pressure regulating valve 6, and unlike the conventional example shown in FIG. 5, interlocking between pumps and troublesome operation are unnecessary. .

【0011】図4は本発明に係る浄水の他の製造装置の
実施例を示す説明図である。図4において、9はエゼク
タであり、吸入口91に精密濾過または限外濾過膜エレ
メント2の濾過液出口810を連通し、逆浸透膜モジュ
−ル3の濃縮原液出口32をポンプ40の入口に連通
し、ポンプ40の出口をエゼクタ9の入口92に連通
し、エゼクタ9の出口93を逆浸透膜モジュ−ル3の原
液供給口31に連通してある。図4において、上記以外
の構成は図1に示した実施例に実質的に同じであり、1
は原水タンクを、11は原水供給配管を、7は浄水タン
クをそれぞれ示している。
FIG. 4 is an explanatory view showing an embodiment of another apparatus for producing purified water according to the present invention. In FIG. 4, reference numeral 9 denotes an ejector, which communicates the filtrate outlet 810 of the microfiltration or ultrafiltration membrane element 2 with the inlet 91, and the concentrated stock solution outlet 32 of the reverse osmosis membrane module 3 to the inlet of the pump 40. The outlet of the pump 40 communicates with the inlet 92 of the ejector 9, and the outlet 93 of the ejector 9 communicates with the stock solution supply port 31 of the reverse osmosis membrane module 3. 4, the configuration other than the above is substantially the same as that of the embodiment shown in FIG.
Is a raw water tank, 11 is a raw water supply pipe, and 7 is a water purification tank.

【0012】図4に示す浄水製造装置においては、エゼ
クタ9の吸引力で濾過膜エレメント2での濾過が行わ
れ、エゼクタ9の出口圧力で逆浸透膜モジュ−ル3での
透過が行われる。この場合、エゼクタ9の吸引力はエゼ
クタ9内の流速で与えられ、この流速がポンプ40の出
力とエゼクタ9の抵抗とで定まるし、また、エゼクタ出
口93の圧力もポンプ40の出力とエゼクタ9の抵抗と
で定まるから、濾過膜エレメント2の濾過流束及び逆浸
透膜モジュ−ル3の透過流束はポンプ40の出力とエゼ
クタ9の特性とで定まる定常値に到達し、逆浸透膜モジ
ュ−ル3の透過液出口33から浄水タンク7にほぼ一定
流量で浄水が流入されるに至る。
In the purified water producing apparatus shown in FIG. 4, the suction force of the ejector 9 filters the membrane element 2, and the outlet pressure of the ejector 9 causes the reverse osmosis membrane module 3 to permeate. In this case, the suction force of the ejector 9 is given by the flow velocity in the ejector 9, and this flow velocity is determined by the output of the pump 40 and the resistance of the ejector 9, and the pressure at the ejector outlet 93 is also the output of the pump 40 and the ejector 9. Therefore, the filtration flux of the filtration membrane element 2 and the permeation flux of the reverse osmosis membrane module 3 reach a steady value determined by the output of the pump 40 and the characteristics of the ejector 9, and the reverse osmosis membrane module -The purified water flows into the purified water tank 7 from the permeated liquid outlet 33 of the valve 3 at a substantially constant flow rate.

【0013】[0013]

【発明の効果】本発明に係る浄水の製造装置において
は、単一のポンプで運転されるから、複数基のポンプを
使用する場合のポンプの連動を必要とせず、運転が簡単
であり、またタンクも少ないので設置スペ−スを軽減で
きる。さらに、精密濾過または限外濾過膜エレメントの
濾過液側と逆浸透膜モジュ−ルとの間が密閉配管とされ
ており、濾過膜エレメントで除菌されたのち逆浸透膜モ
ジュ−ルに至るまでの間での菌の繁殖を排除できるか
ら、衛生的であり、逆浸透膜モジュ−ルの膜のバクテリ
ヤ分解の畏れも全くない。
Since the purified water producing apparatus according to the present invention is operated by a single pump, there is no need to interlock the pumps when using a plurality of pumps, and the operation is simple. Since there are few tanks, the installation space can be reduced. Furthermore, a closed pipe is provided between the filtrate side of the microfiltration or ultrafiltration membrane element and the reverse osmosis membrane module until the reverse osmosis membrane module is sterilized by the filtration membrane element. It is hygienic because it can eliminate the growth of bacteria between them and there is no fear of bacterial degradation of the membrane of the reverse osmosis membrane module.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明に係る浄水の製造装置の一例を示す説明
図である。
FIG. 1 is an explanatory view showing an example of an apparatus for producing purified water according to the present invention.

【図2】本発明において使用する濾過膜エレメント部材
の一例を示す説明図である。
FIG. 2 is an explanatory view showing an example of a filtration membrane element member used in the present invention.

【図3】本発明において使用する濾過膜エレメントの一
例を示す説明図である。
FIG. 3 is an explanatory diagram showing an example of a filtration membrane element used in the present invention.

【図4】本発明に係る浄水の製造装置の一例を示す説明
図である。
FIG. 4 is an explanatory view showing an example of an apparatus for producing purified water according to the present invention.

【図5】従来の浄水製造装置を示す説明図である。FIG. 5 is an explanatory view showing a conventional purified water manufacturing apparatus.

【符号の説明】[Explanation of symbols]

1 原水タンク 2 全量濾過式の精密濾過または限外濾過膜エ
レメント 3 逆浸透膜モジュ−ル 4 ポンプ 40 ポンプ 7 浄水タンク 9 エゼクタ
1 Raw water tank 2 Total filtration type microfiltration or ultrafiltration membrane element 3 Reverse osmosis membrane module 4 Pump 40 Pump 7 Water purification tank 9 Ejector

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】原水タンク内に全量濾過式の精密濾過また
は限外濾過膜エレメントを浸漬設置し、該濾過膜エレメ
ントの濾過液出口をポンプを介してクロスフロ−方式の
逆浸透膜モジュ−ルの原液供給口に連通し、該逆浸透膜
モジュ−ルの濃縮原液出口を上記ポンプの入口側に連通
したことを特徴とする浄水の製造装置。
1. A full-filtration type microfiltration or ultrafiltration membrane element is immersed in a raw water tank, and a filtrate outlet of the filtration membrane element is connected to a crossflow type reverse osmosis membrane module via a pump. An apparatus for producing purified water, characterized in that the concentrated stock solution outlet of the reverse osmosis membrane module communicates with the stock solution supply port and communicates with the inlet side of the pump.
【請求項2】原水タンク内に全量濾過式の精密濾過また
は限外濾過膜エレメントを浸漬設置し、逆浸透膜モジュ
−ルの濃縮原液出口にポンプを、該ポンプの出口にエゼ
クタをそれぞれ連通し、エゼクタの吸入口に前記濾過膜
エレメントの濾過液出口を連通したことを特徴とする浄
水の製造装置。
2. A total filtration type microfiltration or ultrafiltration membrane element is immersed in a raw water tank, and a pump is connected to the concentrated stock solution outlet of the reverse osmosis membrane module and an ejector is connected to the outlet of the pump. An apparatus for producing purified water, wherein the filtered liquid outlet of the filtration membrane element is communicated with the suction port of the ejector.
JP13085296A 1996-04-26 1996-04-26 Purified water manufacturing equipment Pending JPH09290261A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13085296A JPH09290261A (en) 1996-04-26 1996-04-26 Purified water manufacturing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13085296A JPH09290261A (en) 1996-04-26 1996-04-26 Purified water manufacturing equipment

Publications (1)

Publication Number Publication Date
JPH09290261A true JPH09290261A (en) 1997-11-11

Family

ID=15044207

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13085296A Pending JPH09290261A (en) 1996-04-26 1996-04-26 Purified water manufacturing equipment

Country Status (1)

Country Link
JP (1) JPH09290261A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
US7537701B2 (en) 1995-08-11 2009-05-26 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
JP2010162504A (en) * 2009-01-16 2010-07-29 Panasonic Electric Works Co Ltd Water treatment apparatus
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
CN102349683A (en) * 2011-07-12 2012-02-15 上海沃迪科技有限公司 Ultrafiltration/reverse osmosis composite device
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
WO2014184966A1 (en) * 2013-05-11 2014-11-20 株式会社 Permeation Reclaimed water apparatus

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
US8852438B2 (en) 1995-08-11 2014-10-07 Zenon Technology Partnership Membrane filtration module with adjustable header spacing
US7025885B2 (en) 1998-11-23 2006-04-11 Zenon Environmental Inc. Water filtration using immersed membranes
JP2010162504A (en) * 2009-01-16 2010-07-29 Panasonic Electric Works Co Ltd Water treatment apparatus
CN102349683A (en) * 2011-07-12 2012-02-15 上海沃迪科技有限公司 Ultrafiltration/reverse osmosis composite device
WO2014184966A1 (en) * 2013-05-11 2014-11-20 株式会社 Permeation Reclaimed water apparatus
CN105408259A (en) * 2013-05-11 2016-03-16 株式会社保美纯 Reclaimed water apparatus

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