JP2005152694A - Water cleaning treatment facility - Google Patents
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- JP2005152694A JP2005152694A JP2003390934A JP2003390934A JP2005152694A JP 2005152694 A JP2005152694 A JP 2005152694A JP 2003390934 A JP2003390934 A JP 2003390934A JP 2003390934 A JP2003390934 A JP 2003390934A JP 2005152694 A JP2005152694 A JP 2005152694A
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本発明は、原水を膜濾過処理して浄水を得る浄水処理設備に係り、特に、浄水系膜濾過装置の逆洗排水を膜濾過処理して透過水を原水又は浄水として回収するための槽浸漬型膜濾過装置を備えた浄水処理設備に関する。 The present invention relates to a water purification treatment facility that obtains purified water by subjecting raw water to membrane filtration, and in particular, tank immersion for recovering permeate as raw water or purified water by membrane filtration treatment of backwash wastewater of a water purification system membrane filtration device. The present invention relates to water purification equipment equipped with a mold membrane filtration device.
近年、浄水処理技術としては、凝集沈殿・砂濾過といった、広大な設置面積を必要とする旧来の浄水処理設備に代わるコンパクトな処理設備として、膜濾過装置が採用されるようになってきている。そして、水源の有効利用のために、浄水系膜濾過装置の逆洗排水を別途設けた膜濾過装置で膜濾過処理し、透過水を浄水又は膜濾過処理原水として回収することが行われている。 In recent years, membrane filtration devices have come to be adopted as water treatment technology as compact treatment equipment that replaces conventional water treatment equipment that requires a large installation area, such as coagulation sedimentation and sand filtration. And, in order to effectively use the water source, membrane filtration treatment is performed with a membrane filtration device separately provided with backwash drainage of the water purification membrane filtration device, and the permeate is recovered as purified water or membrane filtration treatment raw water. .
例えば、越生町浄水処理施設では、主系統(浄水処理系統)のケーシング収納型UF(限外濾過)膜濾過装置(分画分子量13000Da)の逆洗排水を回収系統のケーシング収納型MF(精密濾過)膜濾過装置(細孔径0.1μm)で膜濾過処理して透過水を浄水として回収することにより、回収率99%を得ている(非特許文献1)。また、回転円盤型膜濾過装置(半浸漬型膜濾過装置)により主系統の膜濾過装置の逆洗排水を膜濾過処理し、透過水を浄水として回収することも提案されている(特許文献1)。その他、逆洗排水を沈殿処理によって回収することも行われている。
しかし、主系統の浄水系膜濾過装置の逆洗排水を処理して回収する場合、沈殿処理では、沈殿槽の設置に大面積を必要とし、しかも、病原性原虫であるクリプトスポリジウムやジアルジア等の除去性が低く、その結果、これらの原虫が系内に濃縮されてしまう恐れがあった。 However, when the backwash wastewater from the main system water purification system membrane filtration device is treated and collected, the sedimentation process requires a large area for the installation of the sedimentation tank, and the pathogenic protozoa such as Cryptosporidium and Giardia The removability was low, and as a result, these protozoa could be concentrated in the system.
膜濾過装置であれば、クリプトスポリジウム等の除去性に優れ、処理水質が良好であるが、従来用いられているケーシング収納型膜濾過装置は、地上に設置する必要があり、主系統の膜濾過装置とは別に、そのための設置面積を確保する必要がある上に、SS濃縮率を上げるためにクロスフロー流速を大きく設定すると、そのための維持管理費(動力費)が高騰するという欠点がある。 If it is a membrane filtration device, Cryptosporidium, etc. is excellent in removability and the quality of treated water is good, but the conventionally used casing storage type membrane filtration device needs to be installed on the ground, and the membrane filtration of the main system In addition to the apparatus, it is necessary to secure an installation area for this purpose, and when the cross flow flow rate is set large in order to increase the SS concentration rate, there are disadvantages that the maintenance cost (power cost) for that rises.
回転円盤型膜濾過装置(半浸漬型膜濾過装置)であっても、動力設備が大きく、また、単位設置面積当たりの膜面積が大きいため、上記設置面積の問題は解決されず、更に機械設備は地上設置となる。 Even in the case of a rotating disk type membrane filtration device (semi-immersed membrane filtration device), the power equipment is large and the membrane area per unit installation area is large, so the problem of the installation area is not solved. Will be installed on the ground.
本発明は上記従来の問題点を解決し、浄水系膜濾過装置の逆洗排水を膜濾過処理して透過水を原水又は浄水として回収するための回収系膜濾過装置を設けた浄水処理設備において、回収系膜濾過装置のフラックスを高く維持すると共に設置面積、動力費を削減し、設備全体の小型化、省エネルギー化を図ることができる浄水処理設備を提供することを目的とする。 The present invention solves the above-mentioned conventional problems, and in a water purification treatment facility provided with a recovery system membrane filtration device for recovering permeate as raw water or purified water by subjecting the backwash wastewater of the water purification membrane filtration device to membrane filtration treatment An object of the present invention is to provide a water purification treatment facility capable of maintaining a high flux of the recovery system membrane filtration device and reducing the installation area and power cost, thereby reducing the size of the entire facility and saving energy.
本発明の浄水処理設備は、原水を膜濾過処理して浄水を得る浄水系膜濾過装置と、該浄水系膜濾過装置の逆洗排水を膜濾過処理する回収系膜濾過装置と、該回収系膜濾過装置の透過水を原水又は浄水として回収する手段とを備える浄水処理設備において、該回収系膜濾過装置が逆洗排水受槽内に外圧型膜モジュールを浸漬した槽浸漬型膜濾過装置であることを特徴とする。 The water purification treatment facility of the present invention includes a water purification membrane filtration device that obtains purified water by subjecting raw water to membrane filtration, a recovery system membrane filtration device that performs membrane filtration treatment of backwash waste water of the water purification membrane filtration device, and the recovery system In a water purification treatment facility comprising means for collecting permeated water of a membrane filtration device as raw water or purified water, the recovery system membrane filtration device is a tank immersion type membrane filtration device in which an external pressure type membrane module is immersed in a backwash drainage tank. It is characterized by being.
槽浸漬型膜濾過装置であれば、逆洗排水中のSS(濁質成分)が高濃度であっても十分に対応可能であり、長期に亘り、フラックスを安定に維持することができる。また、有機物濃度が高い場合にも高回収率で安定した運転維持が可能となる。なお、膜濾過装置であるため、クリプトスポリジウム、ジアルジア等の原虫を確実に除去することができる。 If it is a tank immersion type membrane filtration apparatus, even if SS (turbidity component) in backwash wastewater is high concentration, it can respond enough, and can maintain flux stably over a long period of time. Further, even when the organic matter concentration is high, it is possible to maintain stable operation with a high recovery rate. In addition, since it is a membrane filtration apparatus, protozoa such as Cryptosporidium and Giardia can be reliably removed.
また、逆洗排水を地下水槽で受けることにより、地下に設置することができることから、主系統の浄水系膜濾過装置に対して平面配置ではなく竪型配置とすることもできるため、設置面積の省スペース化が可能である。更に、膜の細孔径の選択により、フラックスをより大きく設定することもでき、小型化、省エネルギー化を図ることが可能である。 In addition, since it can be installed underground by receiving backwash wastewater in a groundwater tank, it can be a vertical arrangement instead of a planar arrangement for the main system water purification membrane filtration device. Space saving is possible. Furthermore, the flux can be set larger by selecting the pore diameter of the membrane, and it is possible to achieve downsizing and energy saving.
本発明においては、回収系膜濾過装置の膜の細孔径を浄水系膜濾過装置の膜の細孔径よりも大きくすることにより、回収系膜濾過装置のフラックスを大きく設定して設備の小型化、省エネルギー化を図ることができる。また、浄水系膜濾過装置は、浸漬膜に比較して高圧処理が可能でフラックスを高くとることができるケーシング収納型UF膜濾過装置又はケーシング収納型MF膜濾過装置であることが好ましく、これにより浄水処理に必要な膜濾過装置数の低減を図ることができる。特に、浄水系膜濾過装置はUF膜濾過装置で、回収系膜濾過装置はMF膜濾過装置であることが好ましい。 In the present invention, by making the pore size of the membrane of the recovery system membrane filtration device larger than the pore size of the membrane of the water purification system membrane filtration device, the flux of the recovery system membrane filtration device is set to be large and the equipment is downsized, Energy saving can be achieved. Further, the water purification system membrane filtration device is preferably a casing storage type UF membrane filtration device or a casing storage type MF membrane filtration device capable of high pressure treatment and high flux compared to the submerged membrane. It is possible to reduce the number of membrane filtration devices necessary for water purification treatment. In particular, it is preferable that the water purification system membrane filtration device is a UF membrane filtration device and the recovery system membrane filtration device is an MF membrane filtration device.
また、回収系膜濾過装置の槽浸漬型膜濾過装置の透過水側を吸引する吸引手段を設けることが好ましく、これにより膜濾過処理効率を高めることができる。この回収系膜濾過装置の外圧型膜モジュールは、単位設置面積当たりの膜面積を大きく確保することができ、省スペース化に有利な外圧型中空糸膜モジュールであることが好ましい。 Moreover, it is preferable to provide a suction means for sucking the permeated water side of the tank-immersion type membrane filtration device of the recovery system membrane filtration device, whereby the membrane filtration treatment efficiency can be increased. The external pressure membrane module of the recovery membrane filtration device is preferably an external pressure hollow fiber membrane module that can secure a large membrane area per unit installation area and is advantageous for space saving.
また、逆洗排水受槽内の外圧型膜モジュールの下方に散気手段を設けることにより、膜面の洗浄効果と共に、次のような効果を得ることができる。 Moreover, the following effects can be acquired with the washing | cleaning effect of a membrane surface by providing an aeration means under the external pressure type | mold membrane module in a backwash drainage tank.
即ち、浄水系統の原水に鉄やマンガンが含まれていると回収系の膜濾過装置において、鉄やマンガンのコロイドが濃縮されることによるフラックスの低下の問題が起こる。この問題を防止するためには、逆洗排水中の鉄やマンガンを十分に酸化する必要があるが、回収系の膜モジュールの下方に散気手段を設けることにより、この散気手段からの曝気が、膜洗浄のみならず、鉄、マンガンの酸化にも作用し、鉄、マンガンのコロイドによる膜の目詰まりを抑制することができる。なお、次亜塩素酸ナトリウム等の酸化剤を添加することにより、鉄やマンガンのコロイドに起因する膜の目詰まりを防止することも可能であるが、この場合であっても、曝気を併用することにより酸化剤の必要量を低減することができる。 That is, if iron or manganese is contained in the raw water of the water purification system, there arises a problem of flux reduction due to concentration of iron or manganese colloids in the recovery membrane filtration device. In order to prevent this problem, it is necessary to sufficiently oxidize iron and manganese in the backwash wastewater. However, by providing a diffuser below the membrane module of the recovery system, aeration from this diffuser However, it acts not only on the membrane cleaning but also on the oxidation of iron and manganese, and the clogging of the membrane by the colloid of iron and manganese can be suppressed. It is also possible to prevent clogging of the film due to iron or manganese colloid by adding an oxidizing agent such as sodium hypochlorite, but even in this case, aeration is used in combination. As a result, the required amount of the oxidizing agent can be reduced.
また、回収系膜濾過装置の逆洗排水受槽は、浄水系膜濾過装置の下方に設け、例えば、逆洗排水受槽を地下に設け、その上に浄水系膜濾過装置を設けた二階建て構造とすることにより、浄水処理設備全体の設置面積を小さくすることができる。 Moreover, the backwash drainage tank of the recovery system membrane filtration device is provided below the water purification system membrane filtration device, for example, a two-story structure in which a backwash drainage tank is provided in the basement and a water purification system membrane filtration device is provided thereon. By doing, the installation area of the whole water purification processing equipment can be made small.
本発明によれば、浄水系膜濾過装置の逆洗排水を膜濾過処理して透過水を原水又は浄水として回収するための回収系膜濾過装置を設けた浄水処理設備において、回収系膜濾過装置のフラックスを高く維持すると共に設置面積、動力費を削減し、設備全体の小型化、省エネルギー化を図ることができる。 According to the present invention, in a water purification treatment facility provided with a recovery system membrane filtration device for performing membrane filtration treatment of backwash wastewater of a water purification system membrane filtration device and recovering permeate as raw water or purified water, a recovery system membrane filtration device In addition to maintaining a high flux, the installation area and power cost can be reduced, and the entire equipment can be reduced in size and energy can be saved.
以下に図面を参照して本発明の浄水処理設備の実施の形態を詳細に説明する。 Embodiments of the water purification treatment facility of the present invention will be described in detail below with reference to the drawings.
図1は本発明の浄水処理設備の実施の形態を示す系統図である。 FIG. 1 is a system diagram showing an embodiment of the water purification treatment facility of the present invention.
河川水、湧水等を必要に応じて砂濾過等の前処理を施して得られる原水は、配管11、着水井1及び配管12を経て浄水系膜濾過装置2に導入され、透過水が浄水として配管14より取り出される。なお、配管12には必要に応じて塩素剤が添加される。
Raw water obtained by subjecting river water, spring water, etc. to pretreatment such as sand filtration is introduced into the water purification system membrane filtration device 2 through the
この浄水系膜濾過装置2では、原水の水質に応じてクロスフロー型又はデッドエンド型の膜濾過処理が行われる。一般に、原水が例えば凝集沈殿処理及び砂濾過処理を経た十分に清浄な水である場合にはデッドエンド型が採用され、原水が十分に清浄な水ではない場合にはクロスフロー型が採用される。 In this water purification system membrane filtration apparatus 2, a cross-flow type or a dead end type membrane filtration process is performed according to the quality of raw water. Generally, when the raw water is sufficiently clean water that has undergone, for example, coagulation sedimentation treatment and sand filtration treatment, a dead end type is adopted, and when the raw water is not sufficiently clean water, a cross flow type is adopted. .
この浄水系膜濾過装置2は、前述の如く、高圧処理が可能である点からケーシング収納型膜濾過装置が好ましく、特に膜種としてはUF膜が好ましい。 As described above, the water purification system membrane filtration device 2 is preferably a casing storage type membrane filtration device from the viewpoint that high-pressure treatment is possible, and a membrane type is particularly preferably a UF membrane.
この浄水系膜濾過装置2は所定の間隔で透過水(浄水)を逆流させることにより逆洗が行われ、逆洗排水は、配管15より回収系膜濾過装置3に送給されて膜濾過処理され、回収系膜濾過装置3の透過水は回収水として配管16より原水導入側に返送され、濃縮水は配管17より排水として系外へ排出される。なお、回収水は配管18より浄水として使用に供しても良い。
The water purification system membrane filtration device 2 is backwashed by allowing permeate (purified water) to flow backward at a predetermined interval, and the backwash wastewater is fed from the
本発明において、この回収系膜濾過装置3としては、逆洗排水受槽4に外圧型膜モジュール5を浸漬した槽浸漬型膜濾過装置を用いる。 In the present invention, as the recovery system membrane filtration device 3, a bath immersion type membrane filtration device in which an external pressure membrane module 5 is immersed in a backwash drainage receiving tank 4 is used.
この回収系膜濾過装置3の膜モジュール5の膜は低圧で膜濾過処理可能なMF膜が好ましく、その細孔径は浄水系膜濾過装置2の膜の細孔径よりも大きいことが回収系膜濾過装置5のフラックスを大きく設定して設備の小型化、省エネルギー化を図ることができる点で好ましい。例えば、浄水系膜濾過装置2が細孔径0.01μm程度のMF膜濾過装置で、回収系膜濾過装置5が細孔径0.02μm程度のMF膜濾過装置であることが好ましい。ただし、回収系膜濾過装置5の膜はクリプトスポリジウム等の原虫を十分に除去できるものであることが好ましい。膜の材質としては特に制限はないが、物理・化学的に安定なポリスルホン系又はPVDF(ポリフッ化ビニリデン)系の膜が好ましい。 The membrane of the membrane module 5 of the recovery system membrane filtration device 3 is preferably an MF membrane that can be subjected to membrane filtration at a low pressure. The pore size of the membrane of the water purification system membrane filtration device 2 is larger than the pore size of the membrane of the water purification system membrane filtration device 2. This is preferable in that the flux of the apparatus 5 can be set large to reduce the size and energy of the equipment. For example, it is preferable that the water purification system membrane filtration apparatus 2 is an MF membrane filtration apparatus having a pore diameter of about 0.01 μm, and the recovery system membrane filtration apparatus 5 is an MF membrane filtration apparatus having a pore diameter of about 0.02 μm. However, the membrane of the recovery membrane filtration device 5 is preferably one that can sufficiently remove protozoa such as Cryptosporidium. The material of the membrane is not particularly limited, but a physically and chemically stable polysulfone or PVDF (polyvinylidene fluoride) membrane is preferable.
なお、図示はされていないが、この膜モジュール5は透過水側を吸引する吸引手段を設けることが好ましく、例えば、吸引ポンプを配管16(又は配管18)に設けることにより膜濾過処理効率を高めることができ、好ましい。また、この膜モジュール5は、特に単位設置面積当たりの膜面積を大きく確保することができる外圧型中空糸膜モジュールであることが好ましい。 Although not shown, this membrane module 5 is preferably provided with a suction means for sucking the permeate side. For example, by providing a suction pump in the pipe 16 (or the pipe 18), the membrane filtration processing efficiency is increased. Can be preferred. The membrane module 5 is preferably an external pressure type hollow fiber membrane module that can secure a large membrane area per unit installation area.
この回収系膜濾過装置5では逆洗排水受槽4内の膜モジュール5の下方に散気管6が設けられており、これにより、曝気による膜の洗浄効果と、前述の鉄、マンガンのコロイドによる膜の目詰まりの抑制を図ることができる。 In this recovery system membrane filtration device 5, a diffuser tube 6 is provided below the membrane module 5 in the backwash waste water receiving tank 4, whereby the membrane cleaning effect by aeration and the aforementioned membrane of iron and manganese colloids are provided. Can be suppressed.
特に、本発明においては、この回収系膜濾過装置3の逆洗排水受槽4は、浄水系膜濾過装置2の下方に設け、例えば、逆洗排水受槽4を地下に設け、その上に浄水系膜濾過装置2を設けた二階建て構造とすることにより、浄水処理設備全体の設置面積を小さくすることができ、好ましい。 In particular, in the present invention, the backwash wastewater receiving tank 4 of the recovery system membrane filtration device 3 is provided below the water purification system membrane filtration device 2, for example, the backwash drainage receiving tank 4 is provided in the basement, and the water purification system is provided thereon. By setting it as the two-story structure which provided the membrane filtration apparatus 2, the installation area of the whole water purification processing equipment can be made small, and it is preferable.
このような本発明の浄水処理設備において、浄水系膜濾過装置及び回収系膜濾過装置の膜仕様、細孔径、水回収率、浄水系膜濾過装置の逆洗頻度、その他の運転条件等には特に制限はないが、例えば下記のような条件を採用することができる。 In such a water purification treatment facility of the present invention, the membrane specifications of the water purification system membrane filtration device and the recovery system membrane filtration device, the pore diameter, the water recovery rate, the backwash frequency of the water purification system membrane filtration device, other operating conditions, etc. Although there is no restriction | limiting in particular, For example, the following conditions are employable.
<浄水系膜濾過装置:ケーシング収納型UF膜濾過装置>
膜種:ポリスルホン製UF膜(耐塩素性)
分画分子量=13〜150kDa
膜フラックス:0.5〜8.0m3/m2/day
水回収率:90〜99%
逆洗間隔:30〜180分
逆洗フラックス:5〜16m/day
逆洗排水量:透過水量の0.02〜0.2倍
<Water purification system membrane filtration device: casing storage type UF membrane filtration device>
Membrane type: Polysulfone UF membrane (chlorine resistance)
Molecular weight cut off = 13 to 150 kDa
Membrane flux: 0.5 to 8.0 m 3 / m 2 / day
Water recovery rate: 90-99%
Backwash interval: 30 to 180 minutes Backwash flux: 5 to 16 m / day
Backwash drainage: 0.02-0.2 times the amount of permeate
<回収系膜濾過装置:浸漬型MF膜濾過装置>
膜種:PVDF製又ポリスルホン製MF膜(耐塩素性)
細孔径=0.02〜0.1μm
水回収率:90〜95%
膜フラックス:0.3〜2.0m3/m2/day
濃縮排水量:原水(逆洗排水)量の0.05〜0.1倍
上記条件で浄水処理を行った場合、浄水処理設備全体の水回収率は、
最小 90+10×0.9=99%
最大 99+1×0.95=99.95%
となる。
<Recovery system membrane filtration device: Submerged MF membrane filtration device>
Membrane type: PVDF or polysulfone MF membrane (chlorine resistance)
Pore diameter = 0.02 to 0.1 μm
Water recovery rate: 90-95%
Membrane flux: 0.3 to 2.0 m 3 / m 2 / day
Concentrated wastewater amount: 0.05 to 0.1 times the amount of raw water (backwash wastewater) When water purification treatment is performed under the above conditions, the water recovery rate of the whole water purification treatment facility is:
Minimum 90 + 10 × 0.9 = 99%
99 + 1 × 0.95 = 99.95%
It becomes.
水回収率は原水水質、特に原水濁度によって適宜設定することが好ましく、例えば原水濁度1度の場合には回収率99.95%に設定し、原水濁度10度の場合には回収率99%に設定する。この時の排水濁度はそれぞれ次のようになるが、槽浸漬型膜分離装置であれば、濁度2000度であっても十分に対応可能であり、上記条件であっても十分安定な運転が可能である。
原水濁度1度の場合(回収率99.95%で運転)
排水濁度=1×2000=2000度
原水濁度10度の場合(回収率99%で運転)
排水濁度=10×100=1000度
The water recovery rate is preferably set appropriately depending on the raw water quality, particularly the raw water turbidity. For example, when the raw water turbidity is 1 degree, the recovery rate is set to 99.95%, and when the raw water turbidity is 10 degrees, the recovery rate is set. Set to 99%. Drainage turbidity at this time is as follows, but if it is a tank immersion type membrane separator, even if the turbidity is 2000 degrees, it can sufficiently cope, and even under the above conditions, it is sufficiently stable operation. Is possible.
When the raw water turbidity is 1 degree (operation at a recovery rate of 99.95%)
Wastewater turbidity = 1 x 2000 = 2000 degrees When the raw water turbidity is 10 degrees (operation at a recovery rate of 99%)
Wastewater turbidity = 10 x 100 = 1000 degrees
1 着水井
2 浄水系膜濾過装置
3 回収系膜濾過装置
4 逆洗排水受槽
5 膜モジュール
6 散気管
DESCRIPTION OF SYMBOLS 1 Landing well 2 Water purification system membrane filtration apparatus 3 Recovery system membrane filtration apparatus 4 Backwash drainage tank 5 Membrane module 6 Aeration pipe
Claims (9)
該浄水系膜濾過装置の逆洗排水を膜濾過処理する回収系膜濾過装置と、
該回収系膜濾過装置の透過水を原水又は浄水として回収する手段とを備える浄水処理設備において、
該回収系膜濾過装置が、逆洗排水受槽内に外圧型膜モジュールを浸漬した槽浸漬型膜濾過装置であることを特徴とする浄水処理設備。 A purified water membrane filtration device that obtains purified water by subjecting raw water to membrane filtration,
A recovery membrane filtration device for membrane filtration treatment of the backwash waste water of the water purification membrane filtration device;
In the purified water treatment facility provided with means for collecting the permeated water of the recovery system membrane filtration device as raw water or purified water,
A water purification treatment facility, wherein the recovery system membrane filtration apparatus is a tank immersion type membrane filtration apparatus in which an external pressure type membrane module is immersed in a backwash drainage receiving tank.
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007245049A (en) * | 2006-03-17 | 2007-09-27 | Fuji Electric Holdings Co Ltd | Water treatment process |
JP2007268359A (en) * | 2006-03-30 | 2007-10-18 | Kurita Water Ind Ltd | Membrane separation method |
JP2007307469A (en) * | 2006-05-17 | 2007-11-29 | Fuji Electric Holdings Co Ltd | Method for treating water |
KR100949579B1 (en) | 2008-07-03 | 2010-03-25 | (주)라텍환경기술 | Equipment and Method of thickening and reuse for the Sand Filters Backwashing Water by using Submerged Hollow Fiber Membrane |
WO2017200221A1 (en) * | 2016-05-16 | 2017-11-23 | (주)글로벌엔필텍 | Sewage treatment system using multistage long-fiber filtering device, and treatment method thereof |
JP2020075218A (en) * | 2018-11-08 | 2020-05-21 | オルガノ株式会社 | Iron/manganese-containing water treatment apparatus and treatment method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04305288A (en) * | 1991-04-01 | 1992-10-28 | Kubota Corp | Water treating equipment |
JPH04310204A (en) * | 1991-04-08 | 1992-11-02 | Kubota Corp | Water treating equipment |
JPH10290926A (en) * | 1997-04-21 | 1998-11-04 | Toto Ltd | Membrane immersion type filter |
JP2000218138A (en) * | 1999-01-28 | 2000-08-08 | Hitachi Plant Eng & Constr Co Ltd | Heating type membrane filter equipment |
JP2003047961A (en) * | 2001-08-07 | 2003-02-18 | Maezawa Ind Inc | Method for concentrating wastewater from physical cleaning of membrane |
JP2003103297A (en) * | 2001-09-28 | 2003-04-08 | Toray Ind Inc | Water treatment plant |
-
2003
- 2003-11-20 JP JP2003390934A patent/JP2005152694A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04305288A (en) * | 1991-04-01 | 1992-10-28 | Kubota Corp | Water treating equipment |
JPH04310204A (en) * | 1991-04-08 | 1992-11-02 | Kubota Corp | Water treating equipment |
JPH10290926A (en) * | 1997-04-21 | 1998-11-04 | Toto Ltd | Membrane immersion type filter |
JP2000218138A (en) * | 1999-01-28 | 2000-08-08 | Hitachi Plant Eng & Constr Co Ltd | Heating type membrane filter equipment |
JP2003047961A (en) * | 2001-08-07 | 2003-02-18 | Maezawa Ind Inc | Method for concentrating wastewater from physical cleaning of membrane |
JP2003103297A (en) * | 2001-09-28 | 2003-04-08 | Toray Ind Inc | Water treatment plant |
Non-Patent Citations (1)
Title |
---|
"越生町浄水場におけるクリプトスポリジウム対策", 環境浄化技術, vol. 2, no. 10, JPN6008035332, October 2003 (2003-10-01), JP, pages 33 - 37, ISSN: 0001089185 * |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007245049A (en) * | 2006-03-17 | 2007-09-27 | Fuji Electric Holdings Co Ltd | Water treatment process |
JP2007268359A (en) * | 2006-03-30 | 2007-10-18 | Kurita Water Ind Ltd | Membrane separation method |
JP2007307469A (en) * | 2006-05-17 | 2007-11-29 | Fuji Electric Holdings Co Ltd | Method for treating water |
KR100949579B1 (en) | 2008-07-03 | 2010-03-25 | (주)라텍환경기술 | Equipment and Method of thickening and reuse for the Sand Filters Backwashing Water by using Submerged Hollow Fiber Membrane |
WO2017200221A1 (en) * | 2016-05-16 | 2017-11-23 | (주)글로벌엔필텍 | Sewage treatment system using multistage long-fiber filtering device, and treatment method thereof |
KR101879845B1 (en) * | 2016-05-16 | 2018-07-18 | (주)글로벌엔필텍 | Sewage disposal system using long fiber filter of multistage and method for treating thereof |
CN109562969A (en) * | 2016-05-16 | 2019-04-02 | 全球恩福科技股份有限公司 | Utilize the sewage disposal system and its processing method of the long fibre filter of multistage |
JP2020075218A (en) * | 2018-11-08 | 2020-05-21 | オルガノ株式会社 | Iron/manganese-containing water treatment apparatus and treatment method |
JP7090015B2 (en) | 2018-11-08 | 2022-06-23 | オルガノ株式会社 | Iron / manganese-containing water treatment equipment and treatment method |
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