JP4529117B2 - Filtration method - Google Patents

Filtration method Download PDF

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JP4529117B2
JP4529117B2 JP2003388887A JP2003388887A JP4529117B2 JP 4529117 B2 JP4529117 B2 JP 4529117B2 JP 2003388887 A JP2003388887 A JP 2003388887A JP 2003388887 A JP2003388887 A JP 2003388887A JP 4529117 B2 JP4529117 B2 JP 4529117B2
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filter medium
water
treated
filtration
medium
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JP2005144399A (en
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昌司 大谷
淳久 本田
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Kurita Water Industries Ltd
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Description

本発明は、水処理用の屈曲変形可能な濾材を経済的に洗浄し得る、且つ、洗浄効果も良好な濾過処理方法に関するものである。 The present invention relates to a filtration method that can economically wash a bending-deformable filter medium for water treatment and also has a good washing effect .

被処理液中の懸濁物質を除去するための濾過装置として、一端が固定された屈曲変形可能な濾材を濾過室内に配設したものが知られている(特許文献1参照)。   2. Description of the Related Art As a filtration device for removing suspended substances in a liquid to be treated, one in which a bending-deformable filter medium having one end fixed is disposed in a filtration chamber is known (see Patent Document 1).

前記濾過装置においては、前記濾過室に、前記濾材の自由端側から固定端側へ向けて被処理水を供給すると、該被処理水が前記濾材を通過する過程で、前記被処理水中の懸濁物質が、水流により屈曲変形した前記濾材に捕捉されて除去される。また、前記被処理水の流通方向とは逆方向に向けて前記濾過室内に洗浄水を供給すると、前記被処理水の水圧によって屈曲又は圧縮されていた前記濾材が、前記洗浄水の流れ方向に伸張し、前記濾材に付着していた懸濁物質が洗い落とされる。   In the filtering device, when water to be treated is supplied to the filtration chamber from the free end side to the fixed end side of the filter medium, the water to be treated is suspended in the process of passing the filter medium. The turbid material is trapped and removed by the filter medium bent and deformed by the water flow. Further, when cleaning water is supplied into the filtration chamber in a direction opposite to the flow direction of the treated water, the filter medium bent or compressed by the water pressure of the treated water is moved in the flow direction of the cleaning water. The suspended matter that has stretched and adhered to the filter medium is washed away.

なお、特許文献1によれば、前記濾材の固定端を前記濾過室の下部に配設し、上方から下方へ向けて前記被処理水を流し、洗浄時には、下方から上方へ向けて洗浄水を流してもよいし、それとは逆に、前記濾材の固定端を前記濾過室の上部に配設し、下方から上方へ向けて前記被処理水を流し、洗浄時には、上方から下方へ向けて洗浄水を流すようにしてもよいとされている(特許文献1の0015段落参照)。
特許第2803041号公報
According to Patent Document 1, the fixed end of the filter medium is disposed at the lower part of the filtration chamber, and the water to be treated is flowed from the upper side to the lower side. On the contrary, the fixed end of the filter medium is disposed on the upper part of the filtration chamber, and the water to be treated is flowed from the bottom to the top, and when washing, the top is washed from the top to the bottom. It is said that water may be allowed to flow (see paragraph 0015 of Patent Document 1).
Japanese Patent No. 2803401

しかしながら、前記従来の濾過装置及び濾過方法によれば、前記濾材の洗浄工程において、洗浄効果を高めるためには、前記洗浄水を大量に圧送して前記濾材を確実に伸張状態に保持せしめることが必要であった。このため、洗浄に必要な総水量が増大し、水回収率の低下及び排水量の増大を招いていた。   However, according to the conventional filtration device and filtration method, in order to enhance the washing effect in the washing step of the filter medium, the washing medium can be pumped in a large amount to ensure that the filter medium is held in an expanded state. It was necessary. For this reason, the total amount of water required for washing | cleaning increased, and the fall of the water recovery rate and the increase in the amount of drainage were invited.

本発明は、前記の如き事情を背景としてなされたもので、濾材の洗浄に必要な総水量を低減することができ、且つ洗浄効果も良好な、濾過処理方法を提供しようとするものである。 The present invention, the above such circumstances has been made as a background, it is possible to reduce the total amount of water required for cleaning of the filter medium, and cleaning effect is also good, intended to provide Filtration process how is there.

前記課題を解決するため、本発明に係る濾過処理方法は、屈曲変形可能な濾材の上端が固定され、前記濾材の下端に接続されたウエイトによって前記濾材に前記屈曲変形からの回復力が付与された濾材に沿って下部から上部へ向けて被処理水を流通せしめる濾過工程と、前記濾材に対して洗浄用の流体を上端から下端へ接触させる濾材洗浄工程と、を備え、前記濾過工程では、前記被処理水によって、前記屈曲変形からの回復力に打ち勝って前記濾材が屈曲せしめられ、前記濾材洗浄工程では、前記屈曲変形からの回復力によって前記濾材が伸張せしめられることを特徴としている(請求項)。 In order to solve the above problems, the filtration method according to the present invention is such that the upper end of a bendable filter medium is fixed, and a weight connected to the lower end of the filter medium provides the filter medium with a recovery force from the bend deformation. A filtration process for circulating the water to be treated from the lower part to the upper part along the filter medium, and a filter medium cleaning process for bringing a cleaning fluid into contact with the filter medium from the upper end to the lower end . The filter medium is bent by overcoming the recovery force from the bending deformation by the water to be treated, and the filter medium is stretched by the recovery force from the bending deformation in the filter medium cleaning step (claim). Item 1 ).

前記濾過処理方法によれば、前記濾材にそって前記下端側から前記上端側へ向けて被処理水が流通せしめられ、該被処理水によって前記屈曲変形からの回復力に打ち勝って前記濾材が屈曲又は圧縮せしめられる。このため、前記濾材の密度が高まり、良好な濾過効果が得られる。 According to the filtration method, pre SL is water to be treated allowed to flow toward from the lower side along the filter medium to the upper side, the filter medium overcomes the recovery force from the bending deformation by該被treated water Can be bent or compressed. For this reason, the density of the said filter medium increases and the favorable filtration effect is acquired.

一方、前記濾材洗浄工程においては、前記屈曲変形からの回復力によって、前記濾材が伸張せしめられた状態で、該濾材に対して洗浄用の流体が上端から下端へ接触させられる。このため、従来のものと異なり、洗浄時に、濾材を伸張せしめるために洗浄水を大量に圧送する必要がない。よって、前記濾材の洗浄に必要な総水量を低減することができる。また、洗浄時には、前記屈曲変形からの回復力で前記濾材が伸張されているので、洗浄効果も良好となる。 On the other hand, in the filter medium cleaning step, the cleaning fluid is brought into contact with the filter medium from the upper end to the lower end in a state where the filter medium is stretched by the recovery force from the bending deformation. For this reason, unlike conventional ones, it is not necessary to pump a large amount of washing water in order to extend the filter medium during washing. Therefore, the total amount of water required for cleaning the filter medium can be reduced. Further, at the time of cleaning, since the filter medium is stretched by the recovery force from the bending deformation, the cleaning effect is also improved.

好適な実施の一形態として、前記洗浄用の流体は、前記上端側から前記下端側へ向けて前記濾材に沿って流れる液体であってよい(請求項2)。 As a form of preferred embodiment, fluid for the cleaning, toward from the upper side to the lower side have yo a liquid flowing along said filter medium (claim 2).

ところで、前記濾過処理方法の濾過工程において、前記被処理水の通水開始後、被処理水によって前記濾材が十分に屈曲するまでの間は、前記濾材の密度が未だ小さいので、懸濁物質の捕捉漏れが生じ易い。このため、好適な実施の一形態として、前記被処理水の通水開始後、前記被処理水によって前記濾材が十分に屈曲するまでの間は、前記濾材を通過した処理水を未処理水として被処理水源に戻すようにすることもできる(請求項3)。このようにすれば、前記被処理水の通水開始後、該被処理水によって前記濾材が十分に屈曲するまでの間に、懸濁物資が処理水に混入してしまうことが防止される。 By the way, in the filtration step of the filtration method, the density of the filter medium is still small until the filter medium is sufficiently bent by the process water after the start of the water to be treated. Capturing leakage is likely to occur. For this reason, as one preferred embodiment, after the start of passing the water to be treated, the treated water that has passed through the filter medium is untreated water until the filter medium is sufficiently bent by the water to be treated. It can also be made to return to a to-be-processed water source ( Claim 3 ). In this way, it is possible to prevent the suspended matter from being mixed into the treated water after the start of passing the treated water until the filter medium is sufficiently bent by the treated water.

以下、添付図面を参照して、本発明を実施するための最良の形態について説明する。   The best mode for carrying out the present invention will be described below with reference to the accompanying drawings.

図1は、本発明の一実施の形態に係る濾過処理方法を実施するために用いて好適な、濾過装置の縦断面図であり、(a)は濾過装置の停止時の状態、(b)は濾過時の状態、(c)は逆洗水による濾材の洗浄時の状態を示している。 FIG. 1 is a longitudinal sectional view of a filtration device suitable for carrying out the filtration method according to an embodiment of the present invention, (a) is a state when the filtration device is stopped, and (b). filtration time of state, and (c) shows the state at the time of filter material washing with backwash water.

図1に示すように、本実施の形態に係る濾過処理方法を実施するために好適な濾過装置100を構成する濾過塔1は、上下方向に延びる筒状体であり、その内部には、上下に間隔をおいて、上部端板2と下部端板32とが、それぞれ前記濾過塔1の内壁面1aに固定されて配設されている。これらの端板2,3は、いずれも通水性を有する多孔板で形成されている。濾過室4は、前記上部端板2と、前記下部端板3と、前記濾過塔1の前記内壁面1aと、で囲まれて、前記濾過塔1内に形成されている。 As shown in FIG. 1, a filtration tower 1 constituting a filtration apparatus 100 suitable for carrying out the filtration method according to the present embodiment is a cylindrical body extending in the vertical direction. The upper end plate 2 and the lower end plate 32 are fixedly disposed on the inner wall surface 1a of the filtration tower 1 at intervals. Each of these end plates 2 and 3 is formed of a porous plate having water permeability. The filtration chamber 4 is surrounded by the upper end plate 2, the lower end plate 3, and the inner wall surface 1 a of the filtration tower 1, and is formed in the filtration tower 1.

前記濾過室4内には、屈曲変形可能な複数の濾材5が配設されている。濾材5の配設数は、各濾材5が屈曲変形して密集した時に、必要かつ十分な濾過作用が奏されるように、個々の濾材の大きさや前記濾過室1の断面積の大きさに応じて適宜に決定すればよい。   A plurality of filter media 5 that can be bent and deformed are disposed in the filter chamber 4. The number of filter media 5 arranged is such that the size of each filter media and the size of the cross-sectional area of the filter chamber 1 are such that when each filter media 5 is bent and densely packed, a necessary and sufficient filtering action is exhibited. What is necessary is just to determine suitably according to it.

前記各濾材5は、上下方向に配設された屈曲変形可能な芯紐6と、該芯紐6から周方向に放射状に延びる繊維状の濁質捕捉材7と、を備えている。該濁質捕捉材7は、前記芯紐6の上部及び下部のそれぞれの所定長さ分を除いて、前記芯紐6の回りに稠密に配設されている。前記各濾材5の上端、すなわち、前記各濾材5の芯紐6の上端6aは、前記上部端板2に連結固定され、前記各濾材5の下端、すなわち、前記各濾材5の芯紐6の下端6bは、前記濾加室1内で垂れ下がって下方へ自然に延びている。 Each of the filter media 5 includes a core string 6 that can be bent and deformed, and a fibrous turbidity trapping material 7 that extends radially from the core string 6 in the circumferential direction. The turbidity trapping material 7 is densely arranged around the core string 6 except for a predetermined length of each of the upper and lower portions of the core string 6. The upper end of each filter medium 5, i.e., the upper end 6a of the core thread 6 of each filter medium 5 is connected and fixed to the upper end plate 2, the lower end of each filter medium 5, i.e., the core thread of the filter medium 5 The lower end 6b of 6 hangs down in the filtration chamber 1 and naturally extends downward.

前記下部端板3上には、前記各濾材5に屈曲変形から回復力を付与するための共通の引張部材として、前記濾過室4内を上下動自在なウエイト8が載置されている。該ウエイト8は、通水性を有する多孔板で形成されている。該ウエイト8には、適宜両のたるみを持たせて、前記各濾材5の下端、すなわち、前記各濾材5の芯紐6の下端6bが接続されている。したがって、前記各濾材5は、前記ウエイト8の荷重で緊張せしめられている訳ではない。しかし、該ウエイトの荷重により、前記各濾材5は、屈曲変形から回復力を付与され、自然な垂れ下がり状態で伸張されている。 On the lower end plate 3, a weight 8 that is movable up and down in the filtration chamber 4 is placed as a common tension member for applying a recovery force from the bending deformation to each filter medium 5. The weight 8 is formed of a porous plate having water permeability. To the weight 8 is to have a slack as appropriate both, the lower end of each filter medium 5, i.e., the lower end 6b of the core thread 6 of each filter medium 5 is connected. Therefore, the filter media 5 are not tensed by the load of the weight 8. However, due to the load of the weight, each filter medium 5 is given a recovery force from bending deformation and is stretched in a natural hanging state.

濾過工程時には、図1(b)に示すように、前記濾過室4内に、懸濁物質を含む被処理水が、被処理水源となる被処理水槽9から、前記濾過塔1の下部から上部へ向けて供給される。その結果、前記被処理水の水圧により、前記ウエイト8が前記濾過室4内を上方へ押し上げられ、前記各濾材5が、前記上部端板2と板状の前記ウエイト8との間で屈曲変形せしめられる。これにより、前記濾過室4内における前記各濾材5の密度が高まるので、前記被処理水中に含まれる懸濁物質が前記各濾材5によって確実に捕捉される。前記各濾材5によって懸濁物質を除去され、前記上部端板2を通過した処理水は、前記濾過塔1の上部から排出される。   At the time of the filtration step, as shown in FIG. 1 (b), the water to be treated containing suspended substances is introduced into the filtration chamber 4 from the water tank 9 to be treated, which is the source of the water to be treated. Supplied towards. As a result, the weight 8 is pushed upward in the filtration chamber 4 by the water pressure of the water to be treated, and each filter medium 5 is bent and deformed between the upper end plate 2 and the plate-like weight 8. I'm damned. Thereby, since the density of each said filter medium 5 in the said filtration chamber 4 increases, the suspended substance contained in the said to-be-processed water is capture | acquired by each said filter medium 5 reliably. Suspended substances are removed by the respective filter media 5, and the treated water that has passed through the upper end plate 2 is discharged from the upper portion of the filter tower 1.

なお、前記濾過工程において、前記被処理水の通水開始後、該被処理水によって前記ウエイト8が押し上げられて前記濾材5が十分に屈曲するまでの間は、前記濾材5の密集度が未だ小さいので、懸濁物質の捕捉漏れが生じ易い。このため、好適な実施の一形態として、前記被処理水の通水開始後、前記被処理水によって前記濾材5が十分に屈曲するまでの間は、前記濾材5を通過した処理水を未処理水としてして前記被処理水槽9に戻すようにすることもできる。このようにすれば、前記被処理水の通水開始後、該被処理水によって前記濾材5が十分に屈曲するまでの間に、懸濁物質が処理水中に混入してしまうことが防止される。   In the filtration step, after the start of the water to be treated, the density of the filter medium 5 is still high until the weight 8 is pushed up by the water to be treated and the filter medium 5 is sufficiently bent. Since it is small, it is easy to cause trapped leakage of suspended solids. For this reason, as one preferred embodiment, after the start of passing the water to be treated, the treated water that has passed through the filter medium 5 is untreated until the filter medium 5 is sufficiently bent by the water to be treated. It can also be made to return to the said to-be-processed water tank 9 as water. If it does in this way, it will prevent that a suspended substance will mix in treated water after the start of water flow of the treated water until the filter medium 5 fully bends by the treated water. .

前記濾過室4内への前記被処理水の供給を停止すると、図1(a)に示したように、前記ウエイト8が自重で自然に下降して、前記下部端板3上の元の位置へと復帰する。このため、前記各濾材5が、濾過作用時の前記屈曲状態から自然に引き伸ばされる。   When the supply of the water to be treated into the filtration chamber 4 is stopped, as shown in FIG. 1 (a), the weight 8 naturally descends by its own weight, and the original position on the lower end plate 3 is reached. Return to. For this reason, each said filter medium 5 is naturally extended from the said bending state at the time of a filtration effect | action.

前記濾過工程終了後には、前記各濾材5に、多くの懸濁物質が捕捉されて絡み付いている。そこで、前記濾材5に対して、必要に応じて、前記懸濁物質を除去するための洗浄作用が施される。前記濾材5の洗浄工程時には、前記濾材5に対して洗浄用の流体を接触させる。   After the filtration step, many suspended substances are trapped and entangled with each filter medium 5. Therefore, the filter medium 5 is subjected to a cleaning action for removing the suspended substances as necessary. During the cleaning process of the filter medium 5, a cleaning fluid is brought into contact with the filter medium 5.

前記濾材5の洗浄方法の第一の実施の形態として、図1(c)に示すように、前記被処理水の流れ方向とは逆に、前記濾材5の前記上端6a側から前記下端6b側へ向けて、前記処理水を洗浄液として逆流せしめることができる。このとき、前記濾材5の前記下端6bには、前記ウエイト8によって屈曲変形からの回復力が付与され、下向きに既に自然に引き伸ばされているので、前記濾材5を伸張せしめるために逆洗水を大量に圧送する必要がない。このため、前記濾材5の洗浄に必要な総水量を低減することができる。また、前記濾材5が伸張された状態で該濾材5に逆洗水が接触するので、洗浄効果も良好となる。   As a first embodiment of the method for cleaning the filter medium 5, as shown in FIG. 1C, the upper end 6 a side to the lower end 6 b side of the filter medium 5, contrary to the flow direction of the water to be treated. The treated water can be made to flow backward as a cleaning liquid. At this time, the lower end 6b of the filter medium 5 is given a recovery force from the bending deformation by the weight 8, and has already been naturally stretched downward, so that backwash water is used to extend the filter medium 5. There is no need to pump in large quantities. For this reason, the total amount of water required for cleaning the filter medium 5 can be reduced. In addition, since the backwash water comes into contact with the filter medium 5 in a state where the filter medium 5 is stretched, the cleaning effect is also improved.

濾材洗浄作用を終えた逆洗水は、前記濾材5から分離した懸濁物質とともに、前記被処理水源9へと戻すことが好ましいが、排水槽(図示せず)へ排出しても良い。   The backwash water that has finished the filter medium cleaning action is preferably returned to the treated water source 9 together with the suspended substance separated from the filter medium 5, but may be discharged to a drainage tank (not shown).

前記濾過処理方法を実施する前記濾過装置100は、図2に示すように、適宜に変形することもできる。すなわち、前記ウエイト8を上下に案内するウエイトガイド12を備え、前記ウエイト8には、前記ウエイトガイド12を相対移動自在に受け入れるウエイトガイド挿通孔13を備えた構成である。前記ウエイトガイド12としては細長い丸棒材を用い、その上端部12aを前記上部は端板2に、下端部12bを前記下部端板3に固定して、前記濾過室4内に垂直に配設すればよい。板状の前記ウエイト8を水平状態のままで円滑に上下に案内し得るように、前記ウエイトガイド12の配設本数は、複数本、特に、前記ウエイト8に対して均等な分布状態で三本以上とすることが望ましい。 As shown in FIG. 2, the filtration device 100 that performs the filtration method can be modified as appropriate . That is, a weight guide 12 that guides the weight 8 up and down is provided, and the weight 8 includes a weight guide insertion hole 13 that receives the weight guide 12 in a relatively movable manner. The weight guide 12 is an elongated round bar, and the upper end portion 12a is fixed to the end plate 2 at the upper portion and the lower end portion 12b is fixed to the lower end plate 3 so as to be vertically arranged in the filtration chamber 4. do it. A plurality of weight guides 12 are arranged so that the plate-like weights 8 can be smoothly guided up and down in a horizontal state, in particular, three in a uniform distribution state with respect to the weights 8. It is desirable to set it above.

また、図2に示すように、前記濾材5より前記被処理水の流れ方向の下流側、例えば、前記上部端板2の上方位置に、濾材充填部14を備えた構成とすることもできる。この濾材充填部14に、適当な形式の濾材、例えば、砂やアンスラサイト等の粒状濾材15を充填しておけば、前記濾材5を通過してしまった前記懸濁物質が、前記粒状濾材15で確実に捕捉される。よって、前記被処理水の通水開始後、該被処理水によって前記濾材5が十分に屈曲するまでの間に、懸濁物質が処理水中に混入してしまうことが防止され、濾過工程開始直後から確実な濾過機能を発揮することができる。   Moreover, as shown in FIG. 2, it can also be set as the structure provided with the filter medium filling part 14 in the downstream of the flow direction of the said to-be-processed water from the said filter medium 5, for example, the upper position of the said upper end plate 2. As shown in FIG. If the filter medium filling portion 14 is filled with a suitable type of filter medium, for example, a granular filter medium 15 such as sand or anthracite, the suspended substance that has passed through the filter medium 5 is transferred to the granular filter medium 15. Is surely captured. Therefore, it is prevented that the suspended substance is mixed into the treated water after the start of passing the treated water and before the filter medium 5 is sufficiently bent by the treated water. A reliable filtration function can be exhibited.

本発明の発明者等は、内径1m、塔の高さ1.5mの濾過塔を使用して、本発明方式による濾過処理方法と、従来方式による濾過処理方法と、を実施したところ、表1に示す実験結果が得られた。 The inventors of the present invention, where the inner diameter of 1 m, using a filtration tower height 1.5m tower, the filtration method according to the present invention method and the filtration method according to the conventional method, was carried out, Table 1 The experimental results shown in Fig. 1 were obtained.

この実験結果からも明らかなように、本発明方式によれば、従来方式のものより、逆洗水の量が少なくすみ、濾過の水回収率が高くなる。   As is apparent from the experimental results, according to the method of the present invention, the amount of backwash water is smaller than that of the conventional method, and the water recovery rate of filtration is increased.

本発明の一実施の形態に係る濾過処理方法を実施するために用いて好適な濾過装置の縦断面図であり、(a)は濾過装置停止時の状態、(b)は濾過時の状態、(c)は逆洗水による濾材の洗浄時の状態を示している。BRIEF DESCRIPTION OF THE DRAWINGS It is a longitudinal cross-sectional view of the suitable filtration apparatus used in order to implement the filtration processing method which concerns on one embodiment of this invention, (a) is the state at the time of the stop of a filtration apparatus, (b) is the state at the time of filtration , and (c) shows the state at the time of filter material washing with backwash water. 図1の変形例に係る濾過装置の縦断面図である。It is a longitudinal cross-sectional view of the filtration apparatus which concerns on the modification of FIG.

符号の説明Explanation of symbols

4 濾過室
5 濾材
6a 濾材の上端
6b 濾材の下端
8 ウエイト(引張部材)
9 被処理水源
14 濾材充填部
4 Filtration chamber 5 Filter medium 6a Upper end of filter medium 6b Lower end of filter medium 8 Weight (tensile member)
9 Water to be treated 14 Filter material filling part

Claims (3)

屈曲変形可能な濾材の上端が固定され、前記濾材の下端に接続されたウエイトによって前記濾材に前記屈曲変形からの回復力が付与された濾材に沿って下部から上部へ向けて被処理水を流通せしめる濾過工程と、前記濾材に対して洗浄用の流体を上端から下端へ接触させる濾材洗浄工程と、を備え、前記濾過工程では、前記被処理水によって前記屈曲変形からの回復力に打ち勝って前記濾材が屈曲せしめられ、前記濾材洗浄工程では、前記屈曲変形からの回復力によって前記濾材が伸張せしめられることを特徴とする、濾過処理方法。 The upper end of the filter medium that can be bent and deformed is fixed, and the water to be treated is distributed from the lower part to the upper part along the filter medium in which the filter medium is given the recovery force from the bending deformation by the weight connected to the lower end of the filter medium. A filtering step, and a filtering medium cleaning step of bringing a cleaning fluid into contact with the filtering medium from the upper end to the lower end. In the filtering step, the water to be treated overcomes the recovery force from the bending deformation and A filtering method, wherein the filtering medium is bent, and in the filtering medium cleaning step, the filtering medium is extended by a recovery force from the bending deformation. 前記洗浄用の流体が、前記上端側から下端側へ向けて前記濾材に沿って流れる液体である請求項1に記載の濾過処理方法。 The filtration method according to claim 1, wherein the cleaning fluid is a liquid that flows along the filter medium from the upper end side toward the lower end side. 前記濾過工程において、前記被処理水の通水開始後、前記被処理水によって濾材が十分に屈曲するまでの間は、前記濾材を通過した処理水を未処理水として被処理水源に戻すことを特徴とする、請求項1又は2に記載の濾過処理方法。 In the filtration step, after the start of water passage of the treated water, until the filtering medium is sufficiently bent by the treated water, the treated water that has passed through the filtering medium is returned to the treated water source as untreated water. The filtration method according to claim 1 or 2 , characterized by the above.
JP2003388887A 2003-11-19 2003-11-19 Filtration method Expired - Fee Related JP4529117B2 (en)

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JP4724688B2 (en) * 2007-05-23 2011-07-13 株式会社トーケミ Filtration device
JP2010179247A (en) * 2009-02-05 2010-08-19 Kurita Water Ind Ltd Filtration device and water treatment apparatus
JP5335157B1 (en) * 2013-02-25 2013-11-06 磯村豊水機工株式会社 Manganese removal method and water purification apparatus
CN115400474B (en) * 2022-08-29 2023-07-07 贵州达沃斯光电有限公司 Filtering device

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JPH0411906A (en) * 1990-04-27 1992-01-16 Noritz Corp Filter
JPH07171319A (en) * 1993-12-16 1995-07-11 Kenseishiya:Kk Filter for coolant and filter device containing the same
JPH10249114A (en) * 1997-03-14 1998-09-22 Chofu Seisakusho Co Ltd Filter
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JP2003024716A (en) * 2001-07-19 2003-01-28 Nippon Rensui Co Ltd Turbid substance removal apparatus
JP2003038911A (en) * 2001-05-25 2003-02-12 Nippon Rensui Co Ltd Suspended matter removing apparatus and operation method therefor
JP2003236310A (en) * 2002-02-18 2003-08-26 Nippon Rensui Co Ltd Suspended matter removing apparatus
JP2004089766A (en) * 2002-08-29 2004-03-25 Ebara Corp Ascending flow filtering method for suspension water and apparatus therefor

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0411906A (en) * 1990-04-27 1992-01-16 Noritz Corp Filter
JPH07171319A (en) * 1993-12-16 1995-07-11 Kenseishiya:Kk Filter for coolant and filter device containing the same
JPH10249114A (en) * 1997-03-14 1998-09-22 Chofu Seisakusho Co Ltd Filter
JP2002166106A (en) * 2000-11-30 2002-06-11 Tookemi:Kk Filter apparatus
JP2003038911A (en) * 2001-05-25 2003-02-12 Nippon Rensui Co Ltd Suspended matter removing apparatus and operation method therefor
JP2003024716A (en) * 2001-07-19 2003-01-28 Nippon Rensui Co Ltd Turbid substance removal apparatus
JP2003236310A (en) * 2002-02-18 2003-08-26 Nippon Rensui Co Ltd Suspended matter removing apparatus
JP2004089766A (en) * 2002-08-29 2004-03-25 Ebara Corp Ascending flow filtering method for suspension water and apparatus therefor

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