JP7544064B2 - Submerged flat membrane element and its manufacturing method - Google Patents
Submerged flat membrane element and its manufacturing method Download PDFInfo
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- JP7544064B2 JP7544064B2 JP2021548725A JP2021548725A JP7544064B2 JP 7544064 B2 JP7544064 B2 JP 7544064B2 JP 2021548725 A JP2021548725 A JP 2021548725A JP 2021548725 A JP2021548725 A JP 2021548725A JP 7544064 B2 JP7544064 B2 JP 7544064B2
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/06—Flat membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/08—Flat membrane modules
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/002—Organic membrane manufacture from melts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C65/00—Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor
- B29C65/02—Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor by heating, with or without pressure
- B29C65/08—Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor by heating, with or without pressure using ultrasonic vibrations
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Description
本発明は、膜分離活性汚泥法に使用される膜分離装置の浸漬型平膜エレメントに関し、特にろ板の周縁部に分離膜を接着して形成された止水部の剥離強度及び断面プロファイルを工夫することにより、止水部の透水部側からの剥離発生時に分離膜全体の破断を防止し、平膜エレメントのろ過性能を長期維持し、止水部の透水部側のみの補修による使用寿命の延命化を図ったものに関する。 The present invention relates to a submerged flat membrane element of a membrane separation device used in a membrane bioreactor activated sludge process, and in particular to an element that prevents the entire separation membrane from breaking when peeling occurs from the permeable side of the water-stopping part by devising the peel strength and cross-sectional profile of the water-stopping part formed by bonding the separation membrane to the peripheral part of the filter plate, thereby maintaining the filtration performance of the flat membrane element for a long period of time and extending the service life by repairing only the permeable side of the water-stopping part.
近年、世界的な人口増加や工業化、都市化、生活レベルの向上を背景にして、生活用水や工業用水に必要な質・量が高まっている。膜分離活性汚泥法は、活性汚泥によって処理された水を分離膜を用いてろ過するため、清澄なろ液を得ることができ、設備のコンパクト性や運転管理の容易さなどの利点もあり、近年非常に注目を集める技術となってきた。膜分離活性汚泥法に用いられる固液分離装置には、例えば図1に示すような浸漬型の膜分離装置がある。図1において、膜分離装置1は、平膜エレメント2と散気装置3とを備える。In recent years, the quality and quantity of water required for domestic and industrial use has increased against the backdrop of global population growth, industrialization, urbanization, and improved living standards. The membrane separation activated sludge process uses a separation membrane to filter water treated with activated sludge, which allows for the production of clear filtrate. It also has advantages such as compact equipment and easy operation and management, and has become a technology that has attracted a lot of attention in recent years. Solid-liquid separation equipment used in the membrane separation activated sludge process includes, for example, a submerged membrane separation equipment as shown in Figure 1. In Figure 1, the membrane separation equipment 1 comprises a flat membrane element 2 and an aeration device 3.
図2に示すように、平膜エレメント2は、熱可塑性樹脂製のろ板4の表裏に分離膜5を配置し、ろ板4の周縁部の全周に沿って接着したものである。活性汚泥によって処理された水は、分離膜5の接着部で囲まれた面によりろ過される。接着部で囲まれた面を透水部と呼ぶ。分離膜5は、基材である不織布に膜ポリマーを含浸させた構成である。平膜エレメント2は、運転時の吸引ろ過により透水部の膜面に汚泥や夾雑物が付着・堆積するが、散気装置3から噴出する気泡およびそれにより生じる上昇流によって膜面を洗浄し、膜面に付着・堆積した汚泥や夾雑物を除去することで、平膜エレメントのろ過性能の低下を防止している。As shown in Figure 2, the flat membrane element 2 has separation membranes 5 placed on the front and back of a filter plate 4 made of thermoplastic resin, which is bonded along the entire periphery of the filter plate 4. Water treated with activated sludge is filtered by the surface surrounded by the bonded parts of the separation membrane 5. The surface surrounded by the bonded parts is called the permeable part. The separation membrane 5 is composed of a nonwoven fabric base material impregnated with a membrane polymer. When the flat membrane element 2 is in operation, sludge and impurities adhere to and accumulate on the membrane surface of the permeable part due to suction filtration, but the membrane surface is washed by air bubbles sprayed from the air diffuser 3 and the resulting upward flow, removing the sludge and impurities that have adhered to and accumulated on the membrane surface, preventing a decline in the filtration performance of the flat membrane element.
しかし、この気泡との衝突や、上昇流の影響により分離膜が揺動し、ろ板と分離膜の接着部に負荷が生じ、分離膜が剥離し、透過水側へ汚泥がリークするという問題がある。ろ板と分離膜の接着法には、超音波溶着法がある。これは、超音波を発振するホーンを接着すべき部位に押圧し、超音波の振動により生じる熱により、ろ板樹脂と分離膜とを溶融させ、溶着するものである。 However, collisions with these air bubbles and the upward flow can cause the separation membrane to vibrate, placing a load on the adhesive between the filter plate and the separation membrane, causing the separation membrane to peel off and sludge to leak into the permeate side. One method for adhering the filter plate and separation membrane is ultrasonic welding. With this method, a horn that emits ultrasonic waves is pressed against the area to be bonded, and the heat generated by the ultrasonic vibrations melts and welds the filter plate resin and the separation membrane.
図3に示すように、ろ板と分離膜との溶着が弱い場合、膜面洗浄時の膜の揺動により、分離膜がろ板から剥離しやすくなる問題がある。活性汚泥処理中の分離膜の剥離による透過水側への汚泥リークの発生は、膜分離装置内の90%以上の平膜エレメントで阻止されていなければ実用的ではない。一方、溶着が強すぎると、溶着時に溶融したろ板樹脂が分離膜の内部深くまで達した状態で固化し、結果として、ろ板と分離膜の溶着部が破断しやすくなる問題がある。As shown in Figure 3, if the welding between the filter plate and the separation membrane is weak, there is a problem that the separation membrane is likely to peel off from the filter plate due to the vibration of the membrane when the membrane surface is cleaned. Sludge leakage into the permeate side due to peeling of the separation membrane during activated sludge treatment is not practical unless more than 90% of the flat membrane elements in the membrane separation device are prevented. On the other hand, if the welding is too strong, the filter plate resin that melts during welding solidifies deep inside the separation membrane, resulting in a problem that the welded part between the filter plate and the separation membrane is likely to break.
このような問題に対して、特許文献1には、ろ板外側に位置する溶融代を透水部側に位置する溶融代より高く形成することによって、ろ板と分離膜の剥離や分離膜の破断を抑制する技術が開示されている。しかし、特許文献1に記載の発明では、一度溶融代をつぶしてしまうと、部分的に剥離した分離膜を修理して再度使用することは困難である。また、平膜エレメントの同一面において複数の止水部を独立して設けなければならず、平膜エレメント作製の作業が煩雑になる。そのため溶着時に、とくに透水部側の止水部で、超音波発振ホーンの接触不良が起こりやすく、複数の止水部間で溶着強度差を大きく設けられないという問題がある。 To address these problems, Patent Document 1 discloses a technology that prevents the separation membrane from the filter plate and the rupture of the separation membrane by making the melting margin located on the outside of the filter plate higher than the melting margin located on the water permeable section side. However, with the invention described in Patent Document 1, once the melting margin is crushed, it is difficult to repair the partially peeled separation membrane and reuse it. In addition, multiple water stop parts must be provided independently on the same surface of the flat membrane element, making the work of manufacturing the flat membrane element complicated. As a result, during welding, poor contact of the ultrasonic oscillation horn is likely to occur, especially in the water stop part on the water permeable section side, and there is a problem that it is not possible to create a large difference in welding strength between multiple water stop parts.
また、特許文献2では、不織布層に達しない適度な溶着条件を設定することによって、使用時の分離膜の破断を防止するとしているが、実際には分離膜の破断を完全に防止することは難しく、分離膜の破断を防止する溶着条件では分離膜の剥離が起こりやすく、分離膜の剥離を防止する溶着条件では分離膜の破断が起こりやすいため、両者を同時に防ぐことは困難であった(図3)。 Patent Document 2 also claims that rupture of the separation membrane during use is prevented by setting appropriate welding conditions that do not reach the nonwoven fabric layer. However, in reality, it is difficult to completely prevent rupture of the separation membrane; welding conditions that prevent rupture of the separation membrane make the separation membrane more likely to peel off, while welding conditions that prevent peeling of the separation membrane make the separation membrane more likely to rupture, making it difficult to prevent both simultaneously (Figure 3).
本発明は、上記の従来技術の問題に鑑み創案されたものであり、その目的は、ろ板の周縁部に分離膜を接着して形成された単一の止水部の剥離強度及び断面プロファイルを工夫することにより、止水部の透水部側のみが部分的に剥離した際にも分離膜の破断を防止し、ろ過性能を長期間維持し、止水部の透水部側での剥離の補修による使用寿命の延命化が可能な浸漬型平膜エレメントおよびその製造方法を提供することにある。The present invention was devised in consideration of the problems of the prior art described above, and its purpose is to provide a submerged flat membrane element and its manufacturing method that can prevent rupture of the separation membrane even when only the permeable part side of the water-stopping part is partially peeled off, by devising the peel strength and cross-sectional profile of a single water-stopping part formed by bonding a separation membrane to the peripheral part of a filter plate, maintain filtration performance for a long period of time, and extend the service life by repairing peeling on the permeable part side of the water-stopping part.
本発明者は、上記目的を達成するために剥離強度と超音波ホーンの形状との関係について鋭意検討した結果、特定の断面形状を形成する超音波ホーンを用いて単一の凹状断面の連続した止水部を設け、止水部の溶着部位の強度を透水部側とろ板外側で適切に設定できるようにすることにより、止水部の耐久性と補修のしやすさを両立する浸漬型平膜エレメントを容易に製造できることを見出し、本発明の完成に至った。 In order to achieve the above-mentioned objective, the inventors conducted extensive research into the relationship between peel strength and the shape of the ultrasonic horn, and discovered that by using an ultrasonic horn that forms a specific cross-sectional shape to provide a continuous water-stopping section with a single concave cross-section and by allowing the strength of the welded parts of the water-stopping section to be appropriately set on the permeable section side and the outside of the filter plate, it is possible to easily manufacture a submerged flat membrane element that combines durability of the water-stopping section with ease of repair, thus completing the present invention.
即ち、本発明は、以下の(1)~(5)の構成を有するものである。
(1)樹脂製のろ板の周縁部の全周に沿って樹脂製の分離膜を接着して止水部を形成した浸漬型平膜エレメントであって、止水部が単一の凹状断面の連続した線で構成され、止水部の透水部側の凹状断面の肩部を形成する溶着部位1における剥離強度が、止水部のろ板外側の凹状断面の肩部を形成する溶着部位2における剥離強度の30~90%であり、止水部の溶着部位2における剥離強度が、8N以上40N以下であることを特徴とする浸漬型平膜エレメント。
(2)止水部の透水部側の凹状断面の肩部の立ち上がり部が曲線を形成し、止水部のろ板外側の凹状断面の肩部の立ち上がり部が凹状断面の両肩部間の平坦部のろ板外側の端で平坦部から明確な上向きの角度変更によって立ち上がり、その角度変更を形成するエッジ角度が80度以上135度以下であることを特徴とする(1)に記載の浸漬型平膜エレメント。
(3)上記溶着部位1の剥離強度が30N以下であることを特徴とする(1)または(2)に記載の浸漬型平膜エレメント。
(4)樹脂製のろ板に樹脂製の分離膜を重ね、重なった周縁部の全周に沿って分離膜側から超音波ホーンを押し当てて単一の凹状断面の連続した線で構成される止水部を形成することを含み、超音波ホーンの押し当てる部分が、止水部の凹状断面に対応した凸状形状を有することを特徴とする(1)~(3)のいずれかに記載の浸漬型平膜エレメントの製造方法。
(5)超音波ホーンの押し当てる部分が、止水部の凹状断面に対応した凸状形状部に続くあやめ部をさらに含むことを特徴とする(4)に記載の製造方法。
That is, the present invention has the following configurations (1) to (5).
(1) A submerged flat membrane element in which a water-stopping portion is formed by bonding a resin separation membrane along the entire peripheral portion of a resin filter plate, the water-stopping portion being composed of a continuous line with a single concave cross-section, the peel strength at welded portion 1 forming the shoulder of the concave cross-section on the water permeable portion side of the water-stopping portion being 30 to 90% of the peel strength at welded portion 2 forming the shoulder of the concave cross-section on the outer side of the filter plate of the water-stopping portion, and the peel strength at welded portion 2 of the water-stopping portion being 8 N or more and 40 N or less.
(2) A submerged flat membrane element as described in (1), characterized in that the rising portion of the shoulder of the concave cross section on the water permeable section side of the water stop section forms a curve, the rising portion of the shoulder of the concave cross section on the outer side of the filter plate of the water stop section rises from the flat section at the outer end of the filter plate of the flat section between both shoulders of the concave cross section by a clear upward angle change, and the edge angle forming the angle change is 80 degrees or more and 135 degrees or less.
(3) The submerged type flat membrane element according to (1) or (2), wherein the peel strength of the welded portion 1 is 30 N or less.
(4) A method for producing a submerged flat membrane element according to any one of (1) to (3), comprising overlapping a resin separation membrane on a resin filter plate, and pressing an ultrasonic horn from the separation membrane side along the entire circumference of the overlapped peripheral portion to form a water-stopping portion composed of a continuous line with a single concave cross-section, characterized in that the portion pressed by the ultrasonic horn has a convex shape corresponding to the concave cross-section of the water-stopping portion.
(5) A manufacturing method described in (4), characterized in that the portion pressed by the ultrasonic horn further includes an iris portion continuing to a convex shaped portion corresponding to the concave cross section of the water-stopping portion.
(1)本発明の浸漬型平膜エレメントは、単一の凹状断面の止水部の溶着部位の透水部側とろ板外側で剥離強度を適切に制御しているので、使用時に最も負荷のかかる止水部の透水部側において溶着時の熱による分離膜の劣化を抑制し、使用時に分離膜が破断することを防止でき、また、長期使用により止水部の透水部側で一部剥離が発生した際も、ろ板外側で止水機能を保持することで平膜エレメントのろ過性能を維持し、部分的な補修による使用寿命の延命化を図ることができる。
(2)本発明の浸漬型平膜エレメントは、止水部の断面形状の凹状部の内側立ち上がり部が曲線を形成し、止水部のろ板外側の凹状断面の肩部の立ち上がり部が凹状断面の両肩部間の平坦部のろ板外側の端で平坦部から明確な上向きの角度変更によって立ち上がり、その角度変更を形成するエッジ角度を特定の範囲に制御しているので、止水部の内側では、分離膜の構造をできるだけ保持しつつ、分離膜の剥離を防止する十分な溶着強度を実現でき、上記効果を容易に得ることができる。
(3)本発明の浸漬型平膜エレメントの製造方法は、特定形状を有する超音波ホーンを使用しているので、一度の溶着作業によりろ板の平滑面において上記効果を持つ単一の凹状止水部を形成させることができ、ろ板の加工費用や、溶着の工数および電源容量を軽減することができる。
(1) In the submerged flat membrane element of the present invention, the peel strength is appropriately controlled on the water permeable section side and the outside of the filter plate of the welded portion of the water stop section with a single concave cross section. This suppresses deterioration of the separation membrane due to heat during welding on the water permeable section side of the water stop section which is subjected to the greatest load during use, and prevents the separation membrane from rupturing during use. Furthermore, even if partial peeling occurs on the water permeable section side of the water stop section due to long-term use, the water stopping function is maintained on the outside of the filter plate, maintaining the filtration performance of the flat membrane element and enabling partial repairs to be performed to extend the service life.
(2) In the submerged flat membrane element of the present invention, the inner rising portion of the concave portion of the cross-sectional shape of the water-stopping portion forms a curve, and the rising portion of the shoulder portion of the concave cross-section on the outer side of the filter plate of the water-stopping portion rises from the flat portion at a clear upward angle change at the outer edge of the filter plate of the flat portion between the two shoulder portions of the concave cross-section, and the edge angle forming the angle change is controlled within a specific range. Therefore, inside the water-stopping portion, sufficient welding strength can be achieved to prevent peeling of the separation membrane while maintaining the structure of the separation membrane as much as possible, and the above-mentioned effects can be easily obtained.
(3) The manufacturing method of the submerged-type flat membrane element of the present invention uses an ultrasonic horn having a specific shape, so that a single concave water-stopping portion having the above-mentioned effects can be formed on the smooth surface of the filter plate by a single welding operation, thereby reducing the processing costs of the filter plate, the labor hours for welding, and the power supply capacity.
本発明の浸漬型平膜エレメントの実施形態について図面を参照して説明する。An embodiment of a submerged flat membrane element of the present invention will be described with reference to the drawings.
図4は、本発明の浸漬型平膜エレメントの一例の模式図である。本発明の浸漬型平膜エレメントは、図4に示されるように、ろ板4の中央部10に流路材11として樹脂メッシュを配置し、その上に緩衝材12を配置し、さらにその上にろ板4の周縁部7に沿って分離膜5を接着した構成をとることが好ましい。本発明では、吸引ろ過時に分離膜5が流路材11側に押し付けられる状態となるため、膜保護の役割を持つ緩衝材12を間に配置することが好ましい。図4では、浸漬型平膜エレメントのろ板4の片面側の構成のみが示されているが、本発明では、ろ板4の表裏両面に同様の構成を有することが好ましい。 Figure 4 is a schematic diagram of an example of a submerged flat membrane element of the present invention. As shown in Figure 4, the submerged flat membrane element of the present invention is preferably configured such that a resin mesh is placed as a flow path material 11 in the center 10 of the filter plate 4, a buffer material 12 is placed on top of that, and a separation membrane 5 is further bonded on top of that along the peripheral portion 7 of the filter plate 4. In the present invention, since the separation membrane 5 is pressed against the flow path material 11 side during suction filtration, it is preferable to place a buffer material 12 that serves to protect the membrane between them. Although Figure 4 shows only the configuration of one side of the filter plate 4 of the submerged flat membrane element, in the present invention, it is preferable that the filter plate 4 has a similar configuration on both the front and back sides.
本発明の浸漬型平膜エレメントにおける膜透過水の流れを図4を用いて説明すると、分離膜5の外表面に被処理液を接触させ、分離膜5の外側から内側へ吸引ろ過が行われ、ろ過された膜透過水は、分離膜5とろ板4との間に配置された緩衝材12、流路材11中の空隙を順に通りながら、ろ板4の端部に取り付けられた透過水取水口13の方向へ流れて行き、透過水取水口13から浸漬型平膜エレメント外へ排出されるようになっている。The flow of membrane permeate in the submerged flat membrane element of the present invention is explained using Figure 4. The liquid to be treated is brought into contact with the outer surface of the separation membrane 5, and suction filtration is performed from the outside to the inside of the separation membrane 5. The filtered membrane permeate passes through the buffer material 12 arranged between the separation membrane 5 and the filter plate 4, and the gaps in the flow path material 11, in that order, and flows in the direction of the permeate intake 13 attached to the end of the filter plate 4, and is discharged from the permeate intake 13 to the outside of the submerged flat membrane element.
本発明の浸漬型平膜エレメントは、ろ板4の周縁部7を中央部10より0.6~2mm高くすることが好ましく、それにより形成される中央部10の凹空間に流路材11及び緩衝材12が配置され、流路材11及び緩衝材12が配置された状態での中央部10と周縁部7の段差は0.5mm以下となるようにすることが好ましい。緩衝材12は、ろ板4に接着した流路材11を覆うように配置し、流路材11と接着することが好ましい。分離膜5は、流路材11、緩衝材12が配置されたろ板4を覆うように周縁部7にて接着することが好ましい。In the submerged flat membrane element of the present invention, the peripheral portion 7 of the filter plate 4 is preferably 0.6 to 2 mm higher than the central portion 10, and the flow path material 11 and the buffer material 12 are placed in the recessed space of the central portion 10 formed thereby, and it is preferable that the step between the central portion 10 and the peripheral portion 7 when the flow path material 11 and the buffer material 12 are placed is 0.5 mm or less. The buffer material 12 is preferably placed so as to cover the flow path material 11 bonded to the filter plate 4, and is bonded to the flow path material 11. The separation membrane 5 is preferably bonded at the peripheral portion 7 so as to cover the filter plate 4 on which the flow path material 11 and the buffer material 12 are placed.
本発明において、分離膜5の材質は、樹脂製であれば特に限定されないが、例えばポリ塩化ビニル、塩素化ポリ塩化ビニル、ポリエーテルスルホン、ポリフッ化ビニリデン、もしくはポリテトラフルオロエチレンなどの熱可塑性樹脂、またはこれらの混合物からなるものを適宜選択することができる。また、分離膜5は、PETまたはポリプロピレンなどの熱可塑性樹脂からなる不織布や抄紙に前記膜材質からなる分離層を含浸または積層した複合膜であってもよい。また、分離膜5の厚みは、好ましくは50μm~300μm、より好ましくは80μm~150μmである。この厚みが大き過ぎると、溶着むらが発生しやすくなるとか、ろ板から剥離しやすくなることがある。また、厚みが薄いと、分離膜の破断が発生しやすくなる。In the present invention, the material of the separation membrane 5 is not particularly limited as long as it is made of resin, but for example, a thermoplastic resin such as polyvinyl chloride, chlorinated polyvinyl chloride, polyethersulfone, polyvinylidene fluoride, or polytetrafluoroethylene, or a mixture thereof, can be appropriately selected. The separation membrane 5 may also be a composite membrane in which a separation layer made of the membrane material is impregnated or laminated on a nonwoven fabric or paper made of a thermoplastic resin such as PET or polypropylene. The thickness of the separation membrane 5 is preferably 50 μm to 300 μm, more preferably 80 μm to 150 μm. If this thickness is too large, uneven welding may occur easily or the membrane may peel off from the filter plate. If the thickness is too thin, the separation membrane is more likely to break.
ろ板4の材質は、平膜エレメント全体の形状を保持する樹脂製のものであれば特に限定されないが、例えばABS樹脂、ポリ塩化ビニル樹脂、ポリカーボネート樹脂などの熱可塑性樹脂を適宜選択することができる。ろ板の寸法は、高さ(長さ)300mm~1500mm、幅200mm~550mmの矩形形状を有し、幅10mm~20mmの周縁部7を有することが好ましい。The material of the filter plate 4 is not particularly limited as long as it is made of a resin that maintains the overall shape of the flat membrane element, but thermoplastic resins such as ABS resin, polyvinyl chloride resin, polycarbonate resin, etc. can be appropriately selected. The dimensions of the filter plate are preferably a rectangular shape with a height (length) of 300 mm to 1500 mm and a width of 200 mm to 550 mm, and a peripheral edge 7 with a width of 10 mm to 20 mm.
本発明において、ろ板と分離膜とは、ろ板の周縁部7と分離膜5を5~15mm程度の幅で重なるように配置した後、周縁部7の内側端部から0.5mm以上外側の位置において超音波溶着法により溶着されることが好ましい。図5は、ろ板4と分離膜5の溶着部分をわかりやすくするために、ろ板4と分離膜5をずらした状態での周縁部7中の止水部6及び溶着補助部8を示す説明図である。超音波溶着法としては、ロータリー溶着法やアップダウン法が挙げられるが、本発明においては、アップダウン法によりアップダウンホーンを用いて、幅0.5mm~3mm、最大深さ50μm~500μmの単一の連続した止水部6(溶着部)をろ板4の周縁部7に沿って全周にわたって一体に形成することが好ましい。また、使用時に分離膜5の外周がばたつくことを防止するために止水部6の外側にあやめ状の溶着補助部8を設けることが好ましい。In the present invention, the filter plate and the separation membrane are preferably welded by ultrasonic welding at a position 0.5 mm or more outside the inner end of the peripheral portion 7 after the peripheral portion 7 of the filter plate and the separation membrane 5 are arranged so that they overlap with a width of about 5 to 15 mm. Figure 5 is an explanatory diagram showing the water stop portion 6 and the welding auxiliary portion 8 in the peripheral portion 7 in a state in which the filter plate 4 and the separation membrane 5 are shifted in order to make the welded portion of the filter plate 4 and the separation membrane 5 easier to understand. Examples of ultrasonic welding methods include the rotary welding method and the up-down method, but in the present invention, it is preferable to use an up-down horn by the up-down method to integrally form a single continuous water stop portion 6 (welded portion) with a width of 0.5 mm to 3 mm and a maximum depth of 50 μm to 500 μm all around the peripheral portion 7 of the filter plate 4. In addition, it is preferable to provide an iris-shaped welding auxiliary portion 8 on the outside of the water stop portion 6 to prevent the outer periphery of the separation membrane 5 from flapping during use.
図6は、周縁部7の止水部6付近を幅方向に切断した断面写真である。本発明では、止水部6は、図6の両矢印Aで示される凹状断面を有した連続した一本の線で構成され、この線が周縁部7に沿って閉じた矩形を構成している。止水部6は、ろ板4と分離膜5が溶着して形成された溶着部であり、溶着部は、ろ板4と分離膜5とを引き剥がした際に、剥離強度が発現する部位である。図7は、図6において透水部側(周縁部内側)からろ板外側(周縁部外側)に向かって分離膜5を引き剥がしたときの剥離強度プロファイルである。分離膜5は、剥離試験中の引張応力により伸展するため、剥離強度を発現する引張距離は実際のAの長さより大きくなる。 Figure 6 is a cross-sectional photograph of the water-stopping portion 6 of the peripheral portion 7 cut in the width direction. In the present invention, the water-stopping portion 6 is composed of a continuous line having a concave cross section as indicated by the double-headed arrow A in Figure 6, and this line forms a closed rectangle along the peripheral portion 7. The water-stopping portion 6 is a welded portion formed by welding the filter plate 4 and the separation membrane 5, and the welded portion is a portion where peel strength is developed when the filter plate 4 and the separation membrane 5 are peeled off. Figure 7 is a peel strength profile when the separation membrane 5 is peeled off from the water-permeable portion side (inside the peripheral portion) toward the outside of the filter plate (outside the peripheral portion) in Figure 6. The separation membrane 5 stretches due to the tensile stress during the peel test, so the tensile distance at which peel strength is developed is greater than the actual length of A.
本発明の平膜エレメントでは、止水部の剥離強度プロファイルは、図7に示すように、2つのピーク(ピーク1、ピーク2)が存在する。ピーク1は、図8に示される止水部の透水部側の凹状断面の肩部を形成する溶着部位1における剥離強度であり、ピーク2は、止水部のろ板外側の凹状断面の肩部を形成する溶着部位2における剥離強度である。このような剥離強度プロファイルは、周縁部に分離膜を溶着する際のアップダウンホーンの形状に密接に関連しており、本発明の浸漬型平膜エレメントに特有の性質である。In the flat membrane element of the present invention, the peel strength profile of the water stop portion has two peaks (peak 1 and peak 2), as shown in Figure 7. Peak 1 is the peel strength at welded portion 1 that forms the shoulder of the concave cross section on the permeable portion side of the water stop portion shown in Figure 8, and peak 2 is the peel strength at welded portion 2 that forms the shoulder of the concave cross section on the outer side of the filter plate of the water stop portion. Such a peel strength profile is closely related to the shape of the up-down horn when welding the separation membrane to the peripheral portion, and is a property unique to the submerged type flat membrane element of the present invention.
本発明の平膜エレメントでは、図7に示すように、溶着部位1の剥離強度(ピーク1)は、比較的弱く設定されており、一方、溶着部位2の剥離強度(ピーク2)は、溶着部位1の剥離強度(ピーク1)より強く設定されているという特徴を有する。すなわち、溶着部位1では、後述するように溶着部位1側が特定の形状を有する超音波ホーンを用いることにより、ろ板と分離膜とが互いに広く浅く溶融して接着された状態にある。このため、溶着部位1は、溶着部位2に比較して分離膜の劣化が抑えられるとともに比較的弱い剥離強度を有することになる。これにより、活性汚泥処理時に透水部の分離膜が揺動することによるストレスにさらされた際に、最も負荷のかかる止水部と透水部の境界である溶着部位1で分離膜が破断することを効果的に防止することができる。一方、溶着部位2では、溶着部位2側が特定の形状を有する超音波ホーンを用いるため、ろ板と分離膜とが溶着部位1よりも多く溶融して強固に一体化している。このため、溶着部位2は溶着部位1に比較して比較的強い剥離強度を有することになる。これにより、仮に溶着部位1において分離膜が剥離したとしても、溶着部位2では分離膜とろ板とが容易に剥離することを防ぐことができる。このような構成を有することにより、溶着部位1で分離膜とろ板周縁部とが剥離した際にも溶着部位2により浸漬型平膜エレメントとしての機能を維持することが可能となる。In the flat membrane element of the present invention, as shown in FIG. 7, the peel strength (peak 1) of the welded portion 1 is set relatively weak, while the peel strength (peak 2) of the welded portion 2 is set stronger than the peel strength (peak 1) of the welded portion 1. That is, in the welded portion 1, the filter plate and the separation membrane are melted and bonded to each other widely and shallowly by using an ultrasonic horn having a specific shape on the welded portion 1 side as described later. Therefore, the welded portion 1 has a relatively weak peel strength and suppresses the deterioration of the separation membrane compared to the welded portion 2. This effectively prevents the separation membrane from breaking at the welded portion 1, which is the boundary between the water-stopping portion and the water-permeable portion and is subjected to the most stress when exposed to stress due to the oscillation of the separation membrane in the water-permeable portion during activated sludge treatment. On the other hand, in the welded portion 2, the welded portion 2 uses an ultrasonic horn having a specific shape on the welded portion 2 side, so the filter plate and the separation membrane are melted more than the welded portion 1 and are firmly integrated. For this reason, welded portion 2 has a relatively strong peel strength compared to welded portion 1. As a result, even if the separation membrane peels off at welded portion 1, the separation membrane and the filter plate can be prevented from easily peeling off at welded portion 2. With this configuration, even when the separation membrane peels off from the peripheral portion of the filter plate at welded portion 1, welded portion 2 makes it possible for the submerged flat membrane element to maintain its function.
本発明の平膜エレメントでは、止水部の溶着部位1における剥離強度は、溶着部位2における剥離強度の30~90%、好ましくは35~85%である。溶着部位1における剥離強度の比率が上記範囲より小さいと、溶着部位1の剥離強度が不十分となり、平膜エレメントの取扱時に容易に溶着部位1が剥離しやすくなる。また、比率が上記範囲より大きいと、本発明の目的とする効果を十分に得ることができない。In the flat membrane element of the present invention, the peel strength at welded portion 1 of the water stop portion is 30 to 90%, preferably 35 to 85%, of the peel strength at welded portion 2. If the peel strength ratio at welded portion 1 is smaller than the above range, the peel strength of welded portion 1 will be insufficient and welded portion 1 will easily peel off when the flat membrane element is handled. If the ratio is larger than the above range, the intended effect of the present invention cannot be fully obtained.
本発明において、止水部の溶着部位2の剥離強度は、8N以上40N以下、好ましくは11N以上35N以下である。溶着部位2の剥離強度が小さすぎると、溶着部位1において膜剥離等が発生した際に溶着部位2においても膜剥離が発生しやすくなる。一方、溶着部位2の剥離強度を大きくしようとして分離膜とろ板樹脂界面を過度に溶融しすぎると、溶着部の分離膜の構造が劣化して分離膜の破断強度が顕著に低下してしまい、膜破断が生じやすくなる。In the present invention, the peel strength of the welded portion 2 of the water stop portion is 8 N or more and 40 N or less, preferably 11 N or more and 35 N or less. If the peel strength of the welded portion 2 is too small, membrane peeling is likely to occur at the welded portion 2 when membrane peeling or the like occurs at the welded portion 1. On the other hand, if the interface between the separation membrane and the filter plate resin is melted too much in an attempt to increase the peel strength of the welded portion 2, the structure of the separation membrane at the welded portion will deteriorate and the rupture strength of the separation membrane will decrease significantly, making the membrane more likely to rupture.
本発明において、止水部の溶着部位1の剥離強度は、好ましくは30N以下、より好ましくは27N以下である。また、止水部の溶着部位1の剥離強度は、好ましくは4N以上、より好ましくは5N以上である。溶着部位1の剥離強度が大きすぎると、膜剥離の発生は減少するが、膜破れが生じやすくなる。一方、溶着部位1の剥離強度が小さすぎると、膜剥離が生じやすくなる。In the present invention, the peel strength of the welded portion 1 of the water-stopping portion is preferably 30 N or less, more preferably 27 N or less. Also, the peel strength of the welded portion 1 of the water-stopping portion is preferably 4 N or more, more preferably 5 N or more. If the peel strength of the welded portion 1 is too high, the occurrence of membrane peeling is reduced, but membrane rupture is more likely to occur. On the other hand, if the peel strength of the welded portion 1 is too low, membrane peeling is more likely to occur.
以上のように、止水部の透水部側に剥離強度の比較的弱い溶着部位1を設け、同一の止水部のろ板外側に剥離強度の比較的強い溶着部位2を設けることにより、止水部の透水部側で溶着時の分離膜の劣化を防止し、使用時に最も負荷のかかる透水部側で分離膜の破断を防止でき、同時に分離膜のろ板からの剥離も防止できるため、平膜エレメントのろ過性能を長期間保持することができる。また、溶着部位1でのみ分離膜とろ板が部分的に剥離した場合、点検時にこれを補修することで平膜エレメントの延命化を図ることができる。 As described above, by providing welded area 1, which has a relatively weak peel strength, on the permeable section side of the water stop section, and providing welded area 2, which has a relatively strong peel strength, on the outer side of the filter plate of the same water stop section, deterioration of the separation membrane during welding on the permeable section side of the water stop section can be prevented, and rupture of the separation membrane can be prevented on the permeable section side, which is subjected to the greatest load during use, while at the same time peeling of the separation membrane from the filter plate can be prevented, thereby maintaining the filtration performance of the flat membrane element for a long period of time. Furthermore, if partial peeling occurs between the separation membrane and the filter plate only at welded area 1, the life of the flat membrane element can be extended by repairing this during inspection.
本発明の平膜エレメントの止水部の形状は、以下に挙げるような特徴を有する。すなわち、本発明の止水部では、止水部の透水部側の凹状断面の肩部(溶着部位1)の立ち上がり部が、図10のEに示すような曲線を形成し、止水部のろ板外側の凹状断面の肩部(溶着部位2)の立ち上がり部が、前記両肩部の間の平坦部(図10のB)のろ板外側の端(図10のC)で明確な上向きの角度変更によって立ち上がっている。この溶着部位2の立ち上がり部の角度変更を形成するエッジ角度(図8のX)は、80度以上135度以下であることが好ましい。一方、溶着部位1の断面を形成するためには、溶着部位1側の断面形状が曲率半径0.3~3mm、弧長が0.4~4mmの曲線を有する超音波ホーンを用いることが好ましい。止水部がこのような形状を有することで、溶着時、凹状断面の止水部の形成により分離膜が引き伸ばされる際、止水部の溶着部位1においては分離膜の伸展程度が広範囲に分散されるので、溶着時の分離膜の劣化を効果的に防ぐことができ、さらに溶着部位1の剥離の影響を図10のCの位置で止め、より剥離強度の強い溶着部位2で分離膜とろ板の剥離の進行を完全に防止することができる。The shape of the water stop part of the flat membrane element of the present invention has the following characteristics. That is, in the water stop part of the present invention, the rising part of the shoulder part (welded part 1) of the concave cross section on the water permeable part side of the water stop part forms a curve as shown in E of FIG. 10, and the rising part of the shoulder part (welded part 2) of the concave cross section on the outer side of the filter plate of the water stop part rises with a clear upward angle change at the outer end of the filter plate (C of FIG. 10) of the flat part (B of FIG. 10) between the two shoulder parts. The edge angle (X in FIG. 8) that forms the angle change of the rising part of this welded part 2 is preferably 80 degrees or more and 135 degrees or less. On the other hand, in order to form the cross section of the welded part 1, it is preferable to use an ultrasonic horn whose cross-sectional shape on the welded part 1 side has a curve with a radius of curvature of 0.3 to 3 mm and an arc length of 0.4 to 4 mm. Because the water-stopping portion has this type of shape, when the separation membrane is stretched due to the formation of a water-stopping portion with a concave cross-section during welding, the degree of stretching of the separation membrane is distributed over a wide range at the welded portion 1 of the water-stopping portion, so that deterioration of the separation membrane during welding can be effectively prevented. Furthermore, the effect of peeling of the welded portion 1 can be stopped at position C in Figure 10, and the progression of peeling between the separation membrane and the filter plate can be completely prevented at the welded portion 2, which has a stronger peel strength.
本発明の平膜エレメントの製造方法としては、樹脂製のろ板の上に分離膜を重ね、重なった周縁部の全周に沿って超音波を発振するホーン(超音波ホーン)を一定圧で押し当てて、ろ板と分離膜との界面で摩擦熱を生じさせ、ろ板および分離膜を構成する樹脂を溶融し、単一の凹状断面の連続した線で構成される止水部(溶着部)を形成する工程を含むことが好ましい。超音波ホーン9は、ろ板4と分離膜5を重ねた部分に押し当てる部分が、図9の右側に示すような止水部6を形成する部分と、その外側に分離膜5の外周のばたつき防止のためのあやめ状の溶着補助部8を形成する部分から構成されることが好ましい。超音波ホーン9は、設定したホーン速度で図9の矢印の方向にろ板周縁部に押し込まれるようになっている。溶融したろ板周縁部の樹脂は、図10に示すように、押し込まれたホーンの両脇へ流れ、盛り上がる。このとき、図10の止水部の領域E,B,Dの剥離強度は、超音波ホーンの影響を領域D>領域E>>領域Bの順に強く受けるために、図7に示されるような剥離強度プロファイルが得られる。The manufacturing method of the flat membrane element of the present invention preferably includes a step of stacking a separation membrane on a resin filter plate, pressing a horn (ultrasonic horn) that emits ultrasonic waves along the entire circumference of the overlapped peripheral portion with a constant pressure to generate frictional heat at the interface between the filter plate and the separation membrane, melting the resin that constitutes the filter plate and the separation membrane, and forming a water-stopping portion (welded portion) composed of a continuous line with a single concave cross section. The ultrasonic horn 9 is preferably composed of a portion that presses against the overlapped portion of the filter plate 4 and the separation membrane 5, which is a portion that forms the water-stopping portion 6 as shown on the right side of Figure 9, and a portion that forms an iris-shaped welding auxiliary portion 8 on the outside of the portion that presses against the overlapped portion of the filter plate 4 and the separation membrane 5. The ultrasonic horn 9 is pressed against the peripheral portion of the filter plate in the direction of the arrow in Figure 9 at a set horn speed. The molten resin on the peripheral portion of the filter plate flows to both sides of the pressed horn and rises up, as shown in Figure 10. In this case, the peel strengths of areas E, B, and D of the waterproofing portion in Figure 10 are more strongly affected by the ultrasonic horn in the order of area D > area E >> area B, resulting in a peel strength profile such as that shown in Figure 7.
このような剥離強度プロファイルを発現するためには、前述したような形状を有する超音波ホーンを用いた上で、超音波周波数、超音波発振時間、押付圧力等を特定の好適な範囲に設定すればよい。具体的には、超音波周波数は、15~70kHzが好ましく、15~50kHzがより好ましく、15~30kHzがさらに好ましい。押付圧力は、好ましくは0.1~3.0MPa、より好ましくは0.5~2.5MPaであり、発振時間は、好ましくは0.3~1.5秒、より好ましくは0.4~1.0秒である。押付圧力が小さいと、ろ板周縁部と分離膜との密着が弱くなる(ホーンがろ板に沈み込むことができない)ため、均一な溶着が得られないことがある。押付圧力が大きいと、超音波発振機に負荷がかかり寿命を短くしてしまうことがある。発振時間が小さいと、分離膜とろ板の摩擦界面での発熱が不十分となり溶着むらが発生することがある。発振時間が大きいと、ろ板樹脂と分離膜の溶融が大きくなりすぎ、かえって剥離強度が弱くなることがある。In order to realize such a peel strength profile, an ultrasonic horn having the shape described above is used, and the ultrasonic frequency, ultrasonic oscillation time, pressing pressure, etc. are set to a specific suitable range. Specifically, the ultrasonic frequency is preferably 15 to 70 kHz, more preferably 15 to 50 kHz, and even more preferably 15 to 30 kHz. The pressing pressure is preferably 0.1 to 3.0 MPa, more preferably 0.5 to 2.5 MPa, and the oscillation time is preferably 0.3 to 1.5 seconds, more preferably 0.4 to 1.0 seconds. If the pressing pressure is small, the adhesion between the peripheral portion of the filter plate and the separation membrane is weak (the horn cannot sink into the filter plate), and uniform welding may not be obtained. If the pressing pressure is large, the ultrasonic oscillator may be loaded and its life may be shortened. If the oscillation time is small, heat generation at the friction interface between the separation membrane and the filter plate may be insufficient, resulting in uneven welding. If the oscillation time is long, the melting of the filter plate resin and the separation membrane becomes too great, which may result in a weakening of the peel strength.
本発明の平膜エレメントは、上述のように構成されているので、止水部の透水部側の溶着部位1が破断することはなく、また仮に溶着部位1が長期使用により剥離したとしてもろ板側の溶着部位2が剥離されずに保たれるので、溶着部位1の部分補修のみで延命化を図ることができる。 Because the flat membrane element of the present invention is constructed as described above, the welded portion 1 on the permeable portion side of the water-stopping portion will not break, and even if the welded portion 1 peels off due to long-term use, the welded portion 2 on the filter plate side will not peel off and will remain so. Therefore, the life of the element can be extended by only partially repairing the welded portion 1.
本発明の平膜エレメントを実施例によって示すが、本発明はこれらに限定されるものではない。本発明における剥離強度の評価は、以下の方法に依った。The flat membrane element of the present invention will be illustrated by examples, but the present invention is not limited to these. The peel strength in the present invention was evaluated according to the following method.
(剥離強度)
溶着部位1および2の剥離強度は、超音波溶着後の未使用状態の平膜エレメントを用いて、次に示す手順に基づいて測定した。止水部の長さ方向が15mm幅になるように溶着部をカットし、止水部から2cm離れた分離膜の透水部を引張試験機(島津オートグラフAGS-J、50Nロードセル)の上部のつかみ具にセットし、分離膜が溶着されているろ板を下部のつかみ具にセットした。20mm/minで180度剥離を行い、そのときの強力(N)を測定した。剥離方向は、平膜エレメントの透水部側から周縁部側に向かう方向で実施した。溶着部位1の剥離強度は、透水部側のピークトップを読み取り、溶着部位2の剥離強度は、ろ板外側のピークトップを読み取ることで測定した。
(Peel Strength)
The peel strength of the welded parts 1 and 2 was measured using an unused flat membrane element after ultrasonic welding according to the following procedure. The welded part was cut so that the length of the water-stopping part was 15 mm wide, and the water-permeable part of the separation membrane 2 cm away from the water-stopping part was set in the upper grip of a tensile tester (Shimadzu Autograph AGS-J, 50N load cell), and the filter plate to which the separation membrane was welded was set in the lower grip. 180-degree peeling was performed at 20 mm/min, and the strength (N) at that time was measured. The peeling direction was from the water-permeable part side of the flat membrane element toward the peripheral part side. The peel strength of the welded part 1 was measured by reading the peak top on the water-permeable part side, and the peel strength of the welded part 2 was measured by reading the peak top on the outer side of the filter plate.
(透過水側への汚泥リーク抑制率)
透過水側への汚泥リーク抑制率については、平膜エレメント10枚分を曝気槽にて3ヵ月間連続運転して使用し、透過水取出口13に接続した透明な吸引チューブについて使用中定期的に目視で観察して汚泥が透過水側へリークした平膜エレメントの有無を確認し、使用した平膜エレメント10枚のうち、汚泥がリークしなかった平膜エレメントの枚数の割合を透過水側への汚泥リークの抑制率(%)とした。
(Sludge leakage suppression rate to permeate side)
To determine the rate of sludge leakage inhibition to the permeate side, 10 flat membrane elements were used in continuous operation in an aeration tank for three months, and the transparent suction tube connected to the permeate outlet 13 was visually observed periodically during use to check for the presence or absence of flat membrane elements from which sludge had leaked to the permeate side. The percentage of flat membrane elements from which sludge had not leaked out of the 10 flat membrane elements used was taken as the rate of sludge leakage inhibition to the permeate side (%).
(分離膜の剥離又は破断の有無)
分離膜の剥離又は破断の有無は、使用した平膜エレメント10枚について目視で確認し、剥離又は破断が生じた場合は、その割合(%)も表示した。
(Whether or not separation membrane is peeled off or broken)
The ten flat membrane elements used were visually inspected for peeling or breakage of the separation membrane, and if peeling or breakage occurred, the percentage of peeling or breakage was also indicated.
(補修による再使用の可否)
補修による再使用の可否については、分離膜の剥離又は破断が生じた場合において、剥離または破断した溶着部位を再度溶着し、その溶着部位の剥離強度が初期強度の90%以上に回復した場合には可、90%未満の場合には不可と判断した。
(Whether or not the item can be reused after repair)
Regarding the feasibility of reuse through repair, in the case where peeling or breakage of the separation membrane occurs, if the peeled or broken welded portion is re-welded and the peel strength of the welded portion recovers to 90% or more of its initial strength, it is deemed feasible to reuse, but if it is less than 90%, it is deemed unfeasible.
(実施例1)
(分離膜)
PET抄紙を所定の大きさに切断した後、皺が入らないように注意しながら製膜用の枠に固定した。次に、塩素化ポリ塩化ビニル7.5質量%、テトラヒドロフラン63.3質量%、イソプロパノール19質量%、1-ブタノール10.2質量%からなる溶液(製膜原液)の中に、前記PET抄紙を静かに浸漬し、1分間放置した。その後、製膜原液を含浸させたPET抄紙をゆっくりと引き上げた後、相対湿度75%、温度20℃の乾燥ゾーン(恒温恒湿箱の中)で10分間放置し、分離膜を形成させた。
Example 1
(Separation membrane)
The PET paper was cut to a predetermined size and then fixed to a frame for film formation while being careful not to wrinkle. Next, the PET paper was gently immersed in a solution (film-forming stock solution) consisting of 7.5% by mass of chlorinated polyvinyl chloride, 63.3% by mass of tetrahydrofuran, 19% by mass of isopropanol, and 10.2% by mass of 1-butanol, and left for 1 minute. Thereafter, the PET paper impregnated with the film-forming stock solution was slowly pulled out and left for 10 minutes in a drying zone (in a constant temperature and humidity box) at a relative humidity of 75% and a temperature of 20°C to form a separation membrane.
(ろ板の作製)
ABS樹脂製のろ板(高さ315mm、幅225mm)の表裏面ともに、ABS樹脂製の周縁部(幅12.5mm)を隙間無く接着することにより、周縁部の厚みが6mmであり、中央部より周縁部が1mm高いろ板を作成した。
(Preparation of filter plate)
An ABS resin filter plate (height 315 mm, width 225 mm) had its peripheral portion (width 12.5 mm) glued tightly to both sides to create a filter plate with a peripheral thickness of 6 mm and a peripheral portion 1 mm higher than the center.
(平膜エレメントの作製)
ろ板の中央部に、流路材として樹脂メッシュ:日本フィルコン(株)DOP-18K(高さ290mm、幅200mm)をセットし、耐水接着剤にてろ板と接着し、膜透過水流路を形成した。ろ板と樹脂メッシュを接着し、樹脂メッシュの上面に緩衝材としてPET製の不織布:廣瀬製紙(株)05TH-60(高さ285mm、幅195mm)をセットした。さらに、不織布上部から分離膜(高さ305mm、幅215mm、厚さ0.13mm)をろ板の周縁部と重ね合わせ、図9に示すアップダウンホーンを押し当て周縁部と分離膜とを溶着した。
なお、前記アップダウンホーンは、透水部側(内側立ち上がり部)の先端の曲率半径が1mm、弧長が1.6mm、ろ板外側(外側立ち上がり部)のエッジ角度が90度のものを用いた。また、アップダウンホーンの押付圧力は0.8MPa、超音波の発振周波数は20kHz、発振時間は0.475秒とした。
裏面も同様に分離膜の接着を行い、平膜エレメントを作製した。
(Preparation of flat membrane element)
A resin mesh (Nihon Filcon Co., Ltd. DOP-18K, height 290 mm, width 200 mm) was set as a flow path material in the center of the filter plate, and was bonded to the filter plate with a water-resistant adhesive to form a membrane permeate flow path. The filter plate and the resin mesh were bonded, and a PET nonwoven fabric (Hirose Paper Co., Ltd. 05TH-60, height 285 mm, width 195 mm) was set as a cushioning material on the upper surface of the resin mesh. Furthermore, a separation membrane (height 305 mm, width 215 mm, thickness 0.13 mm) was overlapped with the peripheral portion of the filter plate from above the nonwoven fabric, and the up-down horn shown in FIG. 9 was pressed against it to weld the peripheral portion and the separation membrane.
The up-down horn had a radius of curvature of 1 mm at the tip of the water permeable portion (inner rising portion), an arc length of 1.6 mm, and an edge angle of 90 degrees on the outside of the filter plate (outer rising portion). The pressing pressure of the up-down horn was 0.8 MPa, the ultrasonic oscillation frequency was 20 kHz, and the oscillation time was 0.475 seconds.
A separation membrane was similarly adhered to the back side to prepare a flat membrane element.
(実施例2)
発振時間を0.50秒とした以外は、実施例1と同様にして平膜エレメントを作製した。
Example 2
A flat membrane element was produced in the same manner as in Example 1, except that the oscillation time was set to 0.50 seconds.
(実施例3)
発振時間を0.65秒とした以外は、実施例1と同様にして平膜エレメントを作製した。
Example 3
A flat membrane element was produced in the same manner as in Example 1, except that the oscillation time was set to 0.65 seconds.
(実施例4)
アップダウンホーンとして、実施例1で用いたものよりも透水部側(内側立ち上がり部)の先端の曲率半径が大きいもの(2mm)を用いた以外は、実施例2と同様にして平膜エレメントを作製した。
Example 4
A flat membrane element was prepared in the same manner as in Example 2, except that an up-down horn having a larger radius of curvature (2 mm) at the tip on the water permeable section side (inner rising section) than that used in Example 1 was used.
(実施例5)
アップダウンホーンとして、実施例1で用いたものよりも透水部側(内側立ち上がり部)の先端の曲率半径が小さいもの(0.6mm)を用いた以外は、実施例1と同様にして平膜エレメントを作製した。
Example 5
A flat membrane element was prepared in the same manner as in Example 1, except that an up-down horn having a smaller radius of curvature (0.6 mm) at the tip on the water permeable section side (inner rising section) than that used in Example 1 was used.
(実施例6)
発振時間を0.40秒とした以外は、実施例5と同様にして平膜エレメントを作製した。
Example 6
A flat membrane element was produced in the same manner as in Example 5, except that the oscillation time was set to 0.40 seconds.
(実施例7)
アップダウンホーンとして、実施例1で用いたものよりも透水部側(内側立ち上がり部)の先端の曲率半径が小さいもの(0.8mm)を用い、発振時間を0.80秒とした以外は、実施例1と同様にして平膜エレメントを作製した。
(Example 7)
A flat membrane element was prepared in the same manner as in Example 1, except that an up-down horn having a smaller radius of curvature (0.8 mm) at the tip on the water permeable section side (inner rising section) than that used in Example 1 was used, and the oscillation time was set to 0.80 seconds.
(比較例1)
アップダウンホーンとして、透水部側(内側立ち上がり部)のエッジ角度が90度、ろ板外側(外側立ち上がり部)のエッジ角度が90度のものを用い、発振時間を0.40秒とした以外は、実施例1と同様にして平膜エレメントを作製した。
(Comparative Example 1)
A flat membrane element was prepared in the same manner as in Example 1, except that an up-down horn with an edge angle of 90 degrees on the water permeable section side (inner rising section) and an edge angle of 90 degrees on the outside of the filter plate (outer rising section) was used, and the oscillation time was set to 0.40 seconds.
(比較例2)
アップダウンホーンとして、透水部側(内側立ち上がり部)のエッジ角度が90度、ろ板外側(外側立ち上がり部)のエッジ角度が90度のものを用いた以外は、実施例3と同様にして(つまり、発振時間0.60秒)平膜エレメントを作製した。
(Comparative Example 2)
A flat membrane element was prepared in the same manner as in Example 3 (i.e., oscillation time 0.60 seconds), except that an up-down horn was used in which the edge angle on the water permeable section side (inner rising section) was 90 degrees and the edge angle on the outside of the filter plate (outer rising section) was 90 degrees.
(比較例3)
アップダウンホーンとして、透水部側(内側立ち上がり部)のエッジ角度が90度、ろ板外側(外側立ち上がり部)のエッジ角度が160度のものを用いた以外は、実施例3と同様にして平膜エレメントを作製した。
(Comparative Example 3)
A flat membrane element was prepared in the same manner as in Example 3, except that the up-down horn had an edge angle of 90 degrees on the water permeable section side (inner rising section) and an edge angle of 160 degrees on the outside of the filter plate (outer rising section).
実施例1~7及び比較例1~3の平膜エレメントの詳細と評価結果を表1に示す。Details and evaluation results of the flat membrane elements of Examples 1 to 7 and Comparative Examples 1 to 3 are shown in Table 1.
表1の結果から明らかなように、実施例1~7では、優れた耐久性を有しかつ補修の容易な平膜エレメントが得られている。なお、実施例1、2、4では、運転中に溶着部位1の一部において分離膜がろ板から剥離したが、透過水側に被処理液がリークすることはなく、溶着部位1の再溶着による補修により平膜エレメントの再使用が可能であった。実施例6では、汚泥リーク抑制率は90%と高かったものの、溶着部位1および2がともに剥離を生じたが、補修により平膜エレメントの再使用が可能であった。一方、溶着部位1および2の剥離強度が低い比較例1では、60%の平膜エレメントで溶着部位1および2がともに膜剥離を生じており、しかも汚泥リーク抑制率は40%と低かった。また、比較例2では、使用時の揺動による負荷を受ける溶着部位1において、溶着時の分離膜の劣化が強すぎたためか、30%の平膜エレメントで溶着部位1の破断(膜破れ)が生じており、補修による再使用も不可能であった。また、比較例3では、溶着部位1と溶着部位2の溶着形状を入れ替えたが、比較例2と同様に使用時の揺動の影響か、20%の平膜エレメントで溶着部位1の破断(膜破れ)が観察され、補修による再使用も不可能であった。As is clear from the results in Table 1, in Examples 1 to 7, flat membrane elements with excellent durability and easy repair were obtained. In Examples 1, 2, and 4, the separation membrane peeled off from the filter plate at part of welded portion 1 during operation, but the treated liquid did not leak to the permeate side, and the flat membrane element could be reused by repairing it by re-welding welded portion 1. In Example 6, the sludge leakage suppression rate was high at 90%, but both welded portions 1 and 2 peeled off, but the flat membrane element could be reused by repairing it. On the other hand, in Comparative Example 1, in which the peel strength of welded portions 1 and 2 was low, membrane peeling occurred at both welded portions 1 and 2 in 60% of the flat membrane elements, and the sludge leakage suppression rate was low at 40%. In Comparative Example 2, rupture (membrane rupture) occurred at welded portion 1 in 30% of the flat membrane elements, possibly because the separation membrane deteriorated too much during welding at welded portion 1, which receives a load from rocking during use, and reuse by repair was impossible. In Comparative Example 3, the welded shapes of welded portion 1 and welded portion 2 were switched, but rupture (membrane rupture) was observed at welded portion 1 in 20% of the flat membrane elements, possibly because of rocking during use, as in Comparative Example 2, and reuse by repair was impossible.
本発明の浸漬型平膜エレメントは、ろ板の周縁部に分離膜を接着して形成された単一の連続した凹状断面の止水部の剥離強度及び断面プロファイルを工夫しているので、耐久性と補修のしやすさを両立することができ、使用寿命の延命化を図ることができる。従って、本発明の浸漬型平膜エレメントは、水処理分野、特に排水処理に用いるのに好適である。The submerged flat membrane element of the present invention has an improved peel strength and cross-sectional profile for the water-stopping section with a single continuous concave cross-section formed by bonding the separation membrane to the peripheral portion of the filter plate, which allows for both durability and ease of repair, thereby extending the service life. Therefore, the submerged flat membrane element of the present invention is suitable for use in the water treatment field, particularly wastewater treatment.
1 膜分離装置
2 平膜エレメント
3 散気装置
4 ろ板
5 分離膜
6 止水部
7 周縁部
8 溶着補助部
9 超音波ホーン
10 中央部
11 流路材
12 緩衝材
13 透過水取出口
REFERENCE SIGNS LIST 1 Membrane separation device 2 Flat membrane element 3 Air diffuser 4 Filter plate 5 Separation membrane 6 Water stopper 7 Periphery 8 Welding auxiliary 9 Ultrasonic horn 10 Center 11 Flow path material 12 Cushioning material 13 Permeate outlet
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| PCT/JP2020/033015 WO2021059885A1 (en) | 2019-09-26 | 2020-09-01 | Immersion type flat membrane element and manufacturing method thereof |
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| JP2002113338A (en) * | 2000-10-04 | 2002-04-16 | Mitsubishi Rayon Co Ltd | Separation membrane element and module using the same |
| JP5066810B2 (en) * | 2005-02-04 | 2012-11-07 | 東レ株式会社 | Polymer separation membrane and production method thereof |
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| JP4969079B2 (en) * | 2005-09-26 | 2012-07-04 | 株式会社クボタ | Membrane periphery fixing structure of submerged membrane cartridge |
| JP2008049239A (en) * | 2006-08-23 | 2008-03-06 | Gs Yuasa Corporation:Kk | Membrane element |
| JP5603111B2 (en) * | 2010-03-17 | 2014-10-08 | 志摩環境事業協業組合 | Flat membrane element and submerged membrane separation apparatus using the same |
| WO2013146838A1 (en) * | 2012-03-30 | 2013-10-03 | 東レ株式会社 | Separation membrane element having surface fastener, and membrane module |
| JP5966733B2 (en) * | 2012-07-31 | 2016-08-10 | 東レ株式会社 | Separation membrane element and membrane module |
| JP6097151B2 (en) * | 2013-05-27 | 2017-03-15 | 住友化学株式会社 | Method for producing gas separation membrane |
| JP6300602B2 (en) * | 2014-03-31 | 2018-03-28 | 株式会社クボタ | Method for producing flat membrane element and flat membrane element |
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| JP2001212436A (en) | 2000-02-04 | 2001-08-07 | Kubota Corp | Immersion type membrane cartridge and method of manufacturing the same |
| JP2014008728A (en) | 2012-07-02 | 2014-01-20 | Kojima Press Industry Co Ltd | Ultrasonic horn, ultrasonic machining device and ultrasonic machining method |
| JP2014188446A (en) | 2013-03-27 | 2014-10-06 | Kubota Corp | Membrane cartridge |
| JP2014188445A (en) | 2013-03-27 | 2014-10-06 | Kubota Corp | Membrane cartridge and method of manufacturing the same |
| JP2015205420A (en) | 2014-04-18 | 2015-11-19 | 日東電工株式会社 | Gas permeable member and manufacturing method thereof |
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