TW553765B - Ceramic membrane module and the operation method thereof - Google Patents

Ceramic membrane module and the operation method thereof Download PDF

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Publication number
TW553765B
TW553765B TW091121964A TW91121964A TW553765B TW 553765 B TW553765 B TW 553765B TW 091121964 A TW091121964 A TW 091121964A TW 91121964 A TW91121964 A TW 91121964A TW 553765 B TW553765 B TW 553765B
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Taiwan
Prior art keywords
membrane
tube
water
casing
housing
Prior art date
Application number
TW091121964A
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Chinese (zh)
Inventor
Tsunehisa Tanaka
Ken Yoshizaki
Motoshi Tajima
Yoshihisa Narukami
Mitsuo Tazaki
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Kubota Kk
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Priority claimed from JP2002267472A external-priority patent/JP2004098031A/en
Priority claimed from JP2002267471A external-priority patent/JP2003170028A/en
Priority claimed from JP2002269315A external-priority patent/JP2004105815A/en
Priority claimed from JP2002270830A external-priority patent/JP2004105838A/en
Application filed by Kubota Kk filed Critical Kubota Kk
Application granted granted Critical
Publication of TW553765B publication Critical patent/TW553765B/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06Tubular membrane modules
    • B01D63/061Manufacturing thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06Tubular membrane modules

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A membrane element 10 is formed by parallelly arranging a plurality of membrane tubes 13 made of a ceramic tiny straight pipe of which the foreend is blocked, and collecting and fixing water-tightly with a binding plate 16 the root end of membrane tubes 13 which pass through the binding plate 16. The membrane element 10 is installed within a casing 11 through insertion opening 11 a, and the binding plate 16 is water-tightly mounted on the insertion opening 11a. The casing 11 is provided with a source water supply port 14 connecting to the outside space of membrane tubes 13 on one side of binding plate 16, and a water collector 19 covering the opening 13a on the root end of membrane tubes 13 on the other side of binding plate16. The water collector 19 has a draining port 20 for running away the filtered water.

Description

553765 五、發明說明(1) [發明所屬之技術領域] 本發明係關於一種陶瓷膜組件,係關於潔淨水(淨水 )處理、污水•廢水處理、氣體分離、灰塵分離之技術。 [先前技術] 一般所知之膜體,如第3 2圖所示一般,係將複數個中 空線膜2平行填充於殼體1之内部,並於殼體兩側裝設蓋罩 3。複數個中空線膜2係在兩側端部,以不滲水方式使中空 線膜2相互間及與殼體1之間集束固定。 如上述一般,藉由以平行方式將複數個中空線膜2填 充於殼體1内部之構造,具有能以高密度方式將中空線膜2 配置於有限之殼體1内部領域之優點,而另一方面,由於 係在殼體兩端藉由黏接等方式將中空線膜2之束體以不滲 水方式固定於殼體1,因此將中空線膜2之束體從殼體1中 取出時,必須破壞並分解殼體1與中空線膜2之束體間的密 封構造,而導致無法維修。 此外,將中空線膜2彎曲成U字狀,並利用凸緣等集束 固定時,雖可由殼體1之一側之開口部取出放入,但因殼 體1内部存在有中空線膜2之U字狀彎曲部,因此乃產生無 法以高密度方式將中空線膜2配置於有限之殼體1内部領域 的問題。 本發明係為解決上述課題而創作者,其目的在提供一 種陶瓷膜組件及其運轉方法,不僅能以高密度方式配置膜 管,同時亦易於將膜元件放入或取出於殼體。 [發明内容]553765 V. Description of the invention (1) [Technical field to which the invention belongs] The present invention relates to a ceramic membrane module, and relates to technologies for clean water (purified water) treatment, sewage and wastewater treatment, gas separation, and dust separation. [Prior Art] Generally, as shown in FIG. 32, a generally known film body is a plurality of hollow wire films 2 filled in parallel to the inside of the casing 1, and covers 3 are provided on both sides of the casing. A plurality of hollow wire membranes 2 are attached to the ends of both sides, and the hollow wire membranes 2 are fixed to each other and to the casing 1 in a water-tight manner. As described above, the structure in which a plurality of hollow wire membranes 2 are filled in the housing 1 in a parallel manner has the advantage of being able to arrange the hollow wire membranes 2 in a limited inner area of the housing 1 in a high-density manner. On the one hand, because the bundle of the hollow wire membrane 2 is fixed to the shell 1 in a water-tight manner at the two ends of the shell by means of adhesion or the like, when the bundle of the hollow wire membrane 2 is taken out of the shell 1 , The sealing structure between the casing 1 and the bundle of the hollow wire membrane 2 must be broken and broken, resulting in failure to repair. In addition, when the hollow wire membrane 2 is bent into a U-shape and fixed with a bundle such as a flange, although it can be taken out from the opening on one side of the housing 1, the hollow wire membrane 2 The U-shaped curved portion causes a problem that the hollow wire film 2 cannot be arranged in a limited area inside the housing 1 in a high-density manner. The present invention was created by the creators to solve the above-mentioned problems, and an object thereof is to provide a ceramic membrane module and a method for operating the same, which can not only arrange a membrane tube in a high-density manner, but also easily put a membrane element into or out of a casing. [Inventive Content]

314039.ptd 第12頁 553765 五、發明說明(2) 為達成上述目的,本發明申請專利範圍第1項之陶瓷 膜組件,係以平行方式配置前端閉塞之呈細直管狀之陶瓷 製之複數膜管,並藉由集束板以不滲水方式將貫通集束板 之各膜管之基端予以集束固定以構成膜元件,再將該膜元 件從膜元件插入口填充於殼體内,並以不滲水方式將集束 板配置於膜元件插入口,並且在上述殼體設置有:在上述 集束板之一側與各膜管外側相連通之第1供排部;在上述 集束板之另一側與各膜管之基端開口相連通之第2供排 部。 根據上述申請專利範圍第1項之構成,膜管具有來自 陶瓷材質之剛性,故可以懸臂支撐,不會因本身重量而導 致破損,可懸臂支撐之長度,係隨著縮小管外徑及管壁厚 度使其形成細管狀並降低本身重量而變長。 因此,利用陶瓷材將膜管作成前端閉塞之細直管狀, 藉此,沿著預定長度呈直線配置之複數膜管可以平行且高 密度方式配置,並藉由集束板進行懸臂式支撐,同時能以 高密度方式將膜管填充於殼體内,而增加相當於殼體之單 位容積的膜面積。藉由集束板僅於一側之基端集束固定各 膜管,可使膜元件更容易裝卸於殼體。藉由懸臂式支撐具 剛性之膜管,可使膜管閉塞之前端側形成非固定狀態,而 不會如同習知集束固定膜管兩側的情形一般,使殼體形狀 受到限定,而得以在槽體等任意形狀之殼體中配置膜管。 此外,如申請專利第2項之陶瓷膜組件,係在殼體中 裝設用以覆蓋插通於集束板之各膜管之基端開口側的蓋314039.ptd Page 12 553765 V. Description of the invention (2) In order to achieve the above purpose, the ceramic membrane module of the first patent application scope of the present invention is a plurality of thin straight tubular ceramic membranes arranged in parallel in a closed front end Tube, and the base end of each membrane tube passing through the bundle plate is bundled and fixed by the bundle plate to form a membrane element, and then the membrane element is filled into the housing from the membrane element insertion opening, and is impervious to water. The cluster plate is arranged at the membrane element insertion port, and the housing is provided with a first supply and discharge section connected to one side of the cluster plate and the outside of each membrane tube; and the other side of the cluster plate is connected to each The second supply and discharge part of the membrane tube is opened at the base end and communicates with it. According to the constitution of item 1 of the above patent application scope, the membrane tube has rigidity from ceramic material, so it can be supported by cantilever without damage due to its own weight. The thickness makes it long and thin, and reduces its weight. Therefore, the ceramic tube is made into a thin straight tube with a closed front end by using a ceramic material, whereby a plurality of film tubes arranged in a straight line along a predetermined length can be arranged in a parallel and high-density manner, and cantilevered by a bundle plate, and can simultaneously support The membrane tube is filled in the casing in a high-density manner, and the membrane area equivalent to the unit volume of the casing is increased. By bundling and fixing each membrane tube at the base end of only one side of the bundling plate, the membrane element can be more easily attached to and detached from the housing. With the cantilevered support rigid membrane tube, the end of the membrane tube can be formed into a non-fixed state before closing, instead of limiting the shape of the casing, as in the conventional case of fixing the two sides of the membrane tube. Membrane tubes are arranged in casings of arbitrary shapes such as tanks. In addition, if the ceramic membrane module of the patent application No. 2 is applied, a cover is installed in the housing to cover the open side of the base end of each membrane tube inserted in the cluster plate.

314039.ptd 第13頁 553765 五、發明說明(3) 罩,在設置於膜元件插入口之外周緣之殼體側凸緣,以及 設置於上述蓋罩之開口端之外周緣之蓋罩側凸緣之間,挾 持上述集束板之外周部的狀態下,藉由連結上述殼體側凸 緣與蓋罩側凸緣,使膜元件固定於殼體内,並於上述集束 板之表裡兩面,黏接用以密封集束板與殼體側凸緣之間之 環狀之一側的襯墊,及用以密封集束板與蓋罩側凸緣之間 之環狀之另一側的襯塾,在由上述一側之襯墊内周面與集 束板表裡之其中一面所形成之一側的凹部,及另一側之襯 墊之内周面與集束板之表裡之另一面所形成之另一側的凹 部間,填充用以將上述各膜管黏接於集束板之黏合劑。 根據上述說明,係在集束板之表裡兩面連接一側之襯 墊與另一側之襯墊後,使各膜管之基端開口側插通於集束 板。然後,在一側之凹部與另一側之凹部填充黏合劑,以 將各膜管黏接於集束板。藉此,無須經由機械加工(切削 加工)即可形成上述一側及另一側之凹部,因此,無須在 集束板側進行機械加工,即可輕易地將膜管安裝於集束板 上。 此外,因各膜管係藉由填充於一側及另一側之凹部之 黏合劑,黏接於集束板上,因此可使膜管穩固且確實地安 裝於集束板上,以避免產生膜管從集束板上脫落之問題。 此外,襯墊除了具有可密封集束板與凸緣之間的功能 外,尚兼具有形成凹部之作用,因此可縮減零件數,而作 成簡單的構造。 此外,申請專利範圍第3項之陶瓷膜組件,係在殼體314039.ptd Page 13 553765 V. Description of the invention (3) The cover is provided with a housing-side flange provided on the outer periphery of the membrane element insertion opening and a cover-side protrusion provided on the outer periphery of the cover end. Between the edges, the outer peripheral portion of the cluster plate is held, and the membrane element is fixed in the housing by connecting the casing-side flange and the cover-side flange, and on both surfaces of the cluster plate. A gasket for sealing one side of the ring between the cluster plate and the casing-side flange, and a gasket for sealing the other side of the ring between the cluster plate and the cover-side flange, The recess on one side is formed by the inner peripheral surface of the pad on one side and one of the front and back surfaces of the cluster plate, and the inner peripheral surface of the pad on the other side and the other surface on the front and back surfaces of the cluster plate Between the recesses on the other side, an adhesive is used for adhering each of the film tubes to the bundle plate. According to the above description, after the pad on one side and the pad on the other side are connected on both sides of the surface of the cluster plate, the open end of each membrane tube is inserted into the cluster plate. Then, the concave portion on one side and the concave portion on the other side are filled with an adhesive to adhere each membrane tube to the bundle plate. As a result, the recesses on one side and the other side can be formed without machining (cutting). Therefore, the membrane tube can be easily mounted on the cluster plate without performing machining on the cluster plate side. In addition, since each membrane tube is adhered to the cluster plate by an adhesive filled in the concave portions on one side and the other side, the membrane tube can be stably and surely installed on the cluster plate to avoid the generation of the membrane tube. The problem of falling off the cluster board. Furthermore, in addition to the function of sealing between the concentrating plate and the flange, the gasket also has a function of forming a recessed portion, so that the number of parts can be reduced and a simple structure can be formed. In addition, the ceramic membrane module of the third patent application scope is attached to the housing

314039.ptd 第14頁 553765 五、發明說明(4) 側設有流體分散器,可使供給於殼體内之流體分散以平均 流入上述各膜管。 精此’流體供給到殼體時’措由流體分散is削弱流力 而平均地流入各膜管。如上所述,由於係在減弱流體之流 力強度並使其均一化之狀態下使上述流體流入各膜管中, 因此可避免膜管振動並產生損傷。 此外,申請專利範圍第4項之陶瓷膜組件,係由可使 流體分散器安裝於殼體側之安裝板及裝設於該安裝板上而 突入於殼體内之管體所構成,而在上述管體内形成流路, 並有複數個流通孔沿著管體軸心方向排列形成於管體周壁 部,上述各流通孔之朝向,係與膜管之軸心方向垂直,且 面向殼體之内周面。 根據所述,供給至殼體内的流體,係流經流體分散器 之管體内之流路,通過各流通孔而流出至管體外側。此 時,由各流通孔所流出之流體,一旦接觸到殼體之内周面 後,即朝著膜管軸心方向變更流向而朝各膜管流出。藉 此,流體可藉由流體分散器削弱流力,而平均地流入各膜 管。如此一來,由於係在減弱上述流體之流力強弱並使其 均一化的狀態下,使上述流體流入各膜管,因此可避免膜 管振動並產生損傷。 此外,申請專利範圍第5項之陶瓷膜組件,係將用以 覆蓋殼體内之膜元件之各膜管之基端開口側的蓋罩,以可 自由裝卸之方式安裝在膜元件插入口 ,而將用以保護由複 數個膜管所形成之膜管群之前端部的前端保護框安裝在上314039.ptd Page 14 553765 V. Description of the invention (4) A fluid disperser is provided on the side, which can disperse the fluid supplied into the casing and evenly flow into the above membrane tubes. Therefore, when the fluid is supplied to the casing, the fluid dispersion force weakens the flow force and flows evenly into each membrane tube. As described above, since the fluid is caused to flow into each membrane tube in a state where the flow strength of the fluid is weakened and uniformized, the membrane tube can be prevented from vibrating and being damaged. In addition, the ceramic membrane module in the scope of patent application No. 4 is composed of a mounting plate on which the fluid disperser can be installed on the housing side and a pipe body installed on the mounting plate and protruding into the housing. A flow path is formed in the tube body, and a plurality of flow holes are arranged along the axis direction of the tube body and formed on the peripheral wall of the tube body. The directions of the flow holes are perpendicular to the axis direction of the membrane tube and face the casing. Within the perimeter. According to the above, the fluid supplied into the casing flows through the flow path in the tube body of the fluid disperser, and flows out to the outside of the tube body through the respective flow holes. At this time, once the fluid flowing out of each of the flow holes comes into contact with the inner peripheral surface of the housing, it changes its flow direction toward the axis of the membrane tube and flows out to each membrane tube. As a result, the fluid can weaken the flow force through the fluid disperser and flow into the membrane tubes evenly. In this way, since the fluid flows into each membrane tube in a state where the flow force of the fluid is weakened and uniformized, the membrane tube can be prevented from vibrating and being damaged. In addition, the ceramic membrane module in the scope of the patent application No. 5 is a cover for covering the open end of the base end of each membrane tube of the membrane element in the casing, and is detachably installed at the membrane element insertion port. A front end protection frame for protecting the front end of a membrane tube group formed by a plurality of membrane tubes is mounted on the

314039.ptd 第15頁 553765 五、發明說明(5) 述膜元件上。 根據該種構成,從殼體内取出膜元件時,係先將蓋罩 由膜元件插入口取下,然後,再由膜元件插入口將膜元件 拉出至殼體外側。 此外,將膜元件填充於殼體内時,係由膜元件插入口 將膜元件插入至殼體内,然後,再將蓋罩安裝於膜元件插 入σ 。 藉此,由於可輕易地將膜元件取出放入殼體,因此以 全新之膜元件更換老舊之膜元件的維修處理較容易進行。 此外,如上述一般,將膜元件由膜元件插入口插入至 殼體内時,當膜管群之前端部即將接觸到膜元件插入口之 周邊部或殼體之内周面等時,由於膜管群之前端部係由前 端保護框所保護,而形成上述前端保護框與膜元件插入口 之周邊部或殼體之内周面等相接觸。藉此,可避免產生膜 管群之前端部直接接觸到膜元件插入口之周邊部或殼體之 内周面等而損傷膜管之問題。 此外,申請專利範圍第6項之陶兗膜組件,係在集束 板上,安裝可將膜元件引導至可取出插入於膜元件插入口 之方向之複數個引導構件,前端保護框則形成包圍膜管群 前端部之外側周圍的環狀,並由上述引導構件所支撐,上 述引導構件係與膜管平行配置,並位於膜管群之外側周 圍。 藉此,將膜元件取出放入於殼體時,引導構件與殼體 内周面接觸並產生滑動,藉此,將膜元件朝取出放入方向314039.ptd Page 15 553765 V. Description of the invention (5) On the membrane element. According to this configuration, when the membrane element is taken out of the casing, the cover is first removed from the membrane element insertion opening, and then the membrane element is pulled out of the casing through the membrane element insertion opening. In addition, when the membrane element is filled in the casing, the membrane element is inserted into the casing through the membrane element insertion port, and then the cover is mounted on the membrane element insertion σ. Therefore, since the membrane element can be easily taken out and put into the case, the maintenance process of replacing the old membrane element with a completely new membrane element is easier. In addition, as described above, when the membrane element is inserted into the housing from the membrane element insertion opening, when the front end of the membrane tube group is about to contact the peripheral portion of the membrane element insertion opening or the inner peripheral surface of the housing, etc., The front end of the tube group is protected by a front-end protection frame, and the front-end protection frame is formed to be in contact with the peripheral portion of the membrane element insertion opening or the inner peripheral surface of the housing. This can avoid the problem that the front end of the membrane tube group directly contacts the peripheral portion of the membrane element insertion opening or the inner peripheral surface of the casing, etc., and damages the membrane tube. In addition, the ceramic membrane module of the 6th patent application is attached to the cluster board, and a plurality of guide members can be installed to guide the membrane element to the direction where the membrane element can be inserted and inserted, and the front protective frame forms a surrounding membrane. The front end of the tube group is ring-shaped around the outer side and supported by the guide member, and the guide member is arranged in parallel with the membrane tube and is located around the outer side of the membrane tube group. Thereby, when the membrane element is taken out and put into the case, the guide member comes into contact with the inner peripheral surface of the case and slides, thereby pulling the membrane element in the direction of taking out and putting in.

314039.ptd 第16頁 553765 五、發明說明(6) 引導。如此一來,可順利地進行上述膜元件之取出放入。 此外,申請專利範圍第7項之陶瓷膜組件,其膜管係 僅以膜形成材形成管壁,並作成管外徑為1至6mmp ,管壁 厚度為0.2至0.8m m之形狀。 根據前述,膜管可藉由以膜形成材形成管壁而形成具 備預定強度之直管狀,並藉由作成管外徑為1至6mmp ,管 壁厚度為0. 2至0 . 8mm之形狀,可控制膜滲透阻力而獲得預 定的流通量。此外,一般的陶瓷製膜管係將膜形成材塗層 於膜支撐材表面之雙重構造,因此不易實現小徑化。 此外,申請專利範圍第8項之陶瓷膜組件之運轉方 法,係在進行一般運轉時,使流體一面由第1供排部供給 至殼體内,一面由第2供排部排出,而在進行逆洗運轉 時,使流體一面由第2供排部供給至殼體内,一面由第1供 排部排出。 根據前述,在進行一般運轉時,由第1供排部供給至 殼體内的流體,由各膜管外側流入至内側並經過濾後,作 為過濾處理流體而從各膜管之基端開口通過第2供排部而 排出至外部。進行上述過濾時,包含於流體中的雜質,係 作為膜面附著物而逐漸附著於各膜管外面。在剝離去除該 膜面附著物時,係進行下述逆洗運轉。 換言之,進行逆洗運轉時,由第2供排部所供給之流 體(過濾處理流體),係由各膜管之基端開口流入至各膜 管内側,並由各膜管之内側流出至外側,再由殼體内部通 過第1供排部而排出至外部。如上述一般,藉由使流體由314039.ptd Page 16 553765 V. Description of the invention (6) Guide. In this way, the membrane element can be smoothly taken out and put in. In addition, for the ceramic membrane module of the seventh patent application range, the membrane tube is formed of a film wall only with a film forming material, and is formed into a shape with a tube outer diameter of 1 to 6 mmp and a tube wall thickness of 0.2 to 0.8 mm. According to the foregoing, the film tube may be formed into a straight tube having a predetermined strength by forming a tube wall with a film-forming material, and by forming a tube having an outer diameter of 1 to 6 mmp and a thickness of the tube wall of 0.2 to 0.8 mm, The membrane permeation resistance can be controlled to obtain a predetermined throughput. In addition, the general ceramic film-forming pipe has a dual structure in which a film-forming material is coated on the surface of a film support material, and therefore it is not easy to reduce the diameter. In addition, the operation method of the ceramic membrane module of the eighth patent application range is to carry out fluid flow from the first supply and discharge part into the casing and discharge from the second supply and discharge part during normal operation, During the backwash operation, the fluid is supplied into the housing from the second supply / discharge unit while being discharged from the first supply / discharge unit. According to the foregoing, during normal operation, the fluid supplied into the housing from the first supply and discharge unit flows from the outside to the inside of each membrane tube and is filtered, and then passes through the base end of each membrane tube as a filtering treatment fluid. The second supply and discharge unit is discharged to the outside. During the above-mentioned filtration, impurities contained in the fluid are gradually attached to the outside of each membrane tube as a film surface attachment. When peeling off this film surface attachment, the following backwash operation was performed. In other words, when the backwash operation is performed, the fluid (filtration treatment fluid) supplied from the second supply and discharge unit flows into the inside of each membrane tube through the base end opening of each membrane tube, and flows out from the inside of each membrane tube to the outside. , And then discharged from the inside to the outside through the first supply and discharge part. As mentioned above,

314039.ptd 第17頁 553765 五、發明說明(7) 各膜管内側流出至外側,可使上述膜管外面之膜面附著物 從膜管剝離並去除。 此外,申請專利範圍第9項之陶瓷膜組件之運轉方 法,係在進行一般運轉時,使流體由第2供排部供給至殼 體内,同時由第1供排部排出,而在進行逆洗運轉時,使 流體由第1供排部供給至殼體内,同時由第2供排部排出。 根據前述,在進行一般運轉時,由第2供排部所供給 之流體,係由各膜管之基端開口流入至各膜管内側,並由 各膜管内側流出至外側並經過過濾後,作為過濾處理流體 而由殼體内部通過第1供排部而排出至外部。進行上述過 濾時,包含於流體中的雜質,係作為膜面附著物逐漸附著 於各膜管内面。在剝離去除該膜面附著物時,係進行下述 逆洗運轉。 換言之,在逆洗運轉時,由第1供排部供給至殼體内 的流體(過濾處理流體),由各膜管之外側流入至内側, 而由各膜管之基端開口經過第2供排部排出至外部。如上 述一般,藉由使流體由各膜管之外側流入至内側,上述膜 管之内面之膜面附著物會從膜管剝離,並從膜管之基端開 口推出去除。 此時,由第1供排部供給至殼體内的流體(過濾處理 流體),由於係以同樣方式由膜管之外面壓入至膜管内 側,因此對附著於膜管内面之膜面附著物同樣具有使之剝 離之作用力,藉此有利於膜面附著物之剝離去除。此外, 當上述流體由膜管外側流入至内側時,因流體之流力將集314039.ptd Page 17 553765 V. Description of the invention (7) The inside of each membrane tube flows out to the outside, so that the film surface attachments on the outside of the membrane tube can be peeled off and removed from the membrane tube. In addition, the operation method of the ceramic membrane module according to item 9 of the patent application range is that during normal operation, the fluid is supplied from the second supply and discharge unit into the casing, and is discharged from the first supply and discharge unit at the same time. During the washing operation, the fluid is supplied into the housing from the first supply / discharge unit and is simultaneously discharged from the second supply / discharge unit. According to the foregoing, during normal operation, the fluid supplied from the second supply and discharge unit flows into the inside of each membrane tube through the base end opening of each membrane tube, flows out from the inside of each membrane tube to the outside, and is filtered. The filtered fluid is discharged from the inside of the casing through the first supply and discharge unit to the outside. During the filtration described above, impurities contained in the fluid are gradually attached to the inner surface of each membrane tube as a film surface attachment. When peeling off this film surface attachment, the following reverse washing operation was performed. In other words, during the backwash operation, the fluid (filtration treatment fluid) supplied into the housing by the first supply and discharge unit flows into the inside from the outside of each membrane tube, and passes through the second supply through the base end opening of each membrane tube. The discharge section is discharged to the outside. In general, as described above, by allowing the fluid to flow from the outside to the inside of each membrane tube, the film surface attachments on the inner surface of the membrane tube are peeled from the membrane tube and pushed out through the opening of the base end of the membrane tube. At this time, the fluid (filtration treatment fluid) supplied into the housing from the first supply / discharge unit is pressed into the inside of the membrane tube from the outer surface of the membrane tube in the same manner, and therefore adheres to the membrane surface attached to the inner surface of the membrane tube. The object also has the force to make it peel, thereby facilitating the peeling and removal of the adherend on the film surface. In addition, when the fluid flows from the outside to the inside of the membrane tube,

314039.ptd 第18頁 553765 五、發明說明(8) 束於膜管内,因而使膜管内流速增大,藉此可提昇推出及 剝離去除膜管内面之膜面附著物之效果。 [實施方式] 為詳細說明本發明,乃參照所附圖面進行說明。 首先,根據第1至4圖說明第1實施形態。 膜組體之殼體11,雖可採用各種形狀,但在本實施形 態中,則以直管圓筒狀進行說明。如第1、第2圖所示,殼 體1 1係在兩端形成開口以作為膜元件插入口 11 a,在膜元 件插入口 1 1 a之外周緣具有殼體側凸緣1 2。殼體1 1,係分 別由兩側之膜元件插入口 11 a裝入填充於内部之複數(2個 )膜元件1 0,在形成於兩側之膜元件1 0之間的供水空間 1 1 b所對應之位置具有用以供給被處理水之源水供給口 1 4 (第1供排部之一例),而在兩側又具有濃縮水排出口 15° 如第3、第4圖所示一般,上述膜元件1 0係由複數個膜 管1 3與集束板1 6所構成。上述各膜管1 3為陶瓷製並形成前 端閉塞之細直管狀,而僅利用膜形成材形成管壁,並作成 管外徑為1至6mmp ,孔徑為0.0 5至1 0 // m,長度約為3 0 0至 8 0 0 m m之形狀。 該等膜管1 3係以預定之間隔呈平行配置,並將基端裝 入配置在上述集束板1 6上所形成之貫穿孔,而藉由填充於 各膜管1 3之基端間的黏接材層1 7,以不滲水方式集束固定 於集束板1 6上。 上述膜元件1 0係由各膜元件插入口 1 1 a填充於殼體1 1314039.ptd Page 18 553765 V. Description of the invention (8) It is bundled in the membrane tube, thereby increasing the flow velocity in the membrane tube, thereby improving the effect of pushing out and peeling off the film surface attachments on the inner surface of the membrane tube. [Embodiment] In order to explain the present invention in detail, it will be described with reference to the attached drawings. First, the first embodiment will be described with reference to Figs. 1 to 4. Although the casing 11 of the membrane assembly can have various shapes, in this embodiment, a straight tube shape will be described. As shown in Figs. 1 and 2, the casing 11 is formed with openings at both ends as the membrane element insertion opening 11 a, and has a casing-side flange 12 at the outer periphery of the membrane element insertion opening 1 1 a. The housing 11 is filled with a plurality of (2) membrane elements 1 0 filled in from the membrane element insertion openings 11 a on both sides, and a water supply space 1 1 formed between the membrane elements 10 on both sides. The position corresponding to b has a source water supply port 1 4 (an example of the first supply and discharge unit) for supplying the treated water, and a concentrated water discharge port 15 ° on both sides, as shown in Figures 3 and 4. Generally, the membrane element 10 is composed of a plurality of membrane tubes 13 and a bundle plate 16. Each of the above film tubes 13 is a thin straight tube made of ceramic and formed with a closed front end, and only the film forming material is used to form the tube wall, and the outer diameter of the tube is 1 to 6 mmp, the hole diameter is 0.0 5 to 10 // m, and the length A shape of about 300 to 800 mm. The film tubes 13 are arranged in parallel at a predetermined interval, and the base ends are inserted into the through-holes formed in the above-mentioned bundle plate 16, and are filled between the base ends of the film tubes 13. The adhesive material layer 17 is bundled and fixed on the bundle plate 16 in a water-impermeable manner. The above-mentioned membrane element 10 is filled in the casing 1 by each membrane element insertion opening 1 1 a.

314039.ptd 第19頁 553765 五、發明說明(9) 内部,而集束板1 6則藉由一側的襯墊丨8 (密封材)以不滲 水方式配置於殼體側凸緣12。覆蓋各膜管13之基端開口 13a而配置之集水部19 ’具有過濾水排出口 2〇,係隔著另 —側之襯墊21 (密封材)以不滲水方式配置於集束板16, 並藉由固定螺栓2 2連接殼體凸緣! 2、集束板i 6、集水部i 9 並固定為一體。 此外’上述源水供給口 1 4係設在殼體1 1之外周部,而 在集束板1 6之另一側與各膜管i 3外側相連通。此外,上述 集水部1 9與過濾水排出口 2 〇,係用以構成第2供排部,而 在集束板1 6之另一側與各膜管丨3之基端開口丨3a相連通。 以下’ $兄明上述構成之作用。 進行一般運轉時,如第2圖之實線箭頭所示一般,由 源水供給口 1 4所供給之被處理水(流體),流入殼體1 1内 之供水空間1 1 b,而由與各膜管1 3之閉塞之前端相對向的 位置朝基端側進行通水。藉此,能以交叉流入方式將被處 理水均勻地供給到各膜管1 3間的流路。以交叉流入方式供 給之被處理水係由各膜管1 3之外側流入至内側時,藉由各 膜管1 3而過濾,而透過膜管1 3之被處理水則作為過濾處理 水通過膜管1 3之内部流路1 3 c而由基端開口 1 3 a流入至集水 部1 9内,再由過濾水排出口 2 〇排出至外部。此外,被處理 水係沿著膜管i 3流動,而其濃縮水則是由濃縮水排出口 1 5 排出。 在此’由於膜管1 3具有陶瓷材質之剛性,而能夠進行 懸臂式支撐,不會因本身重量而導致破損之可懸臂支撐之314039.ptd Page 19 553765 V. Description of the invention (9) The cluster plate 16 is arranged on the casing side flange 12 in a water-tight manner through a gasket 丨 8 (seal) on one side. The water collecting part 19 ′, which covers the base end opening 13 a of each membrane tube 13, has a filtered water discharge port 20, and is arranged on the cluster plate 16 in a water-impermeable manner through a gasket 21 (sealing material) on the other side. And the housing flange is connected by the fixing bolt 2 2! 2. The collecting plate i 6 and the water collecting part i 9 are fixed together. In addition, the above-mentioned source water supply port 14 is provided on the outer peripheral portion of the casing 11 and communicates with the outside of each membrane tube i 3 on the other side of the cluster plate 16. In addition, the above-mentioned water collecting part 19 and the filtered water discharge port 20 are used to constitute the second supply and discharge part, and the other side of the collecting plate 16 is connected to the base end opening 3a of each membrane tube 3 . Here's the function of the above composition. During normal operation, as indicated by the solid arrows in FIG. 2, the treated water (fluid) supplied from the source water supply port 14 flows into the water supply space 1 1 b in the housing 11, and The position where the front end of each membrane tube 13 is opposite to the occlusion is passed toward the base end side. Thereby, the to-be-processed water can be uniformly supplied to the flow path between each membrane tube 13 by a cross-flow method. When the treated water supplied by the cross-flow method flows from the outside of each membrane tube 13 to the inside, it is filtered by each membrane tube 13 and the treated water passing through the membrane tube 13 passes through the membrane as filtered treated water. The internal flow path 1 3 c of the tube 13 flows into the water collection part 19 from the base end opening 13 a, and is then discharged to the outside through the filtered water discharge port 20. In addition, the water to be treated flows along the membrane tube i 3, and the concentrated water is discharged through the concentrated water discharge port 1 5. Here ’s because the membrane tube 13 has the rigidity of ceramic material, and cantilever-type support can be carried out without being damaged due to its own weight.

314039.ptd 第20頁 553765 五、發明說明(ίο) 長度’會隨著縮小管外徑及管壁厚度,使之形成細管狀並 減輕本身重量而變得愈長。因此,膜管丨3可藉由陶竟材形 成前端閉塞之細直管狀,而在利用集束板1 6進行懸臂式支 撐之狀態下,沿著預定長度呈直線式配置。 因此’可利用集束板1 6以懸臂支樓並平行配置複數個 膜管13,其結果,可將膜管13以高密度方式填充於殼體n 之内部,並增加相當於殼體11之單位容積的膜面積·二 各膜管13係藉由僅配置於單側的集束板丨'6固定於殼體 11,因此,在進行維修時,只需拆卸固定螺栓22,即可輕 易地將殼體側凸緣1 2、集束板1 6、及集水部丨9分離,以便 於將膜元件1 0取出至殼體1 1之外部。 此外, 板1 6,可使 不會如以往 等形狀受到 膜管13。 藉由將具有 膜管1 3之閉 集束固定膜 侷限,而能 剛性之膜管 塞之前端側 管兩側的情 夠在槽體等 1 3以懸臂式 形成非固定 形一般,使 任意形狀之 支撐於集束 狀態,因此 殼體之長度 殼體中配置 一般的陶瓷製之膜管,係具有在膜支广 形成材之雙重構造,故不易實現小徑化,作H表面塗布膜 係藉由單獨以膜形成材形成管壁,而&在本發明 強度之細直管&,並形成瞢冰13形成於 中 丁 ’吓柯w干例从狀〜从仍少风耳璧,而使 具有預定強度之細直管狀,並形成管外經為、e d形成於 壁厚度為0.2至0_ 8mm之形狀,故可藉此L至^’管 獲得預定之流通量(flux)。 夢透阻力並 此外,在進行上述一般運轉時,被處王里 之外側流入至内側並過渡時’包含於被卢 各膜S 1 3 、处理水中之雜質,314039.ptd Page 20 553765 V. Description of the invention (ίο) The length will become longer as the outer diameter of the tube and the thickness of the wall are reduced to form a thin tube and reduce its own weight. Therefore, the membrane tube 3 can be formed into a thin straight tube with a closed front end by a ceramic material, and can be arranged in a straight line along a predetermined length in a state of cantilever support using a bundle plate 16. Therefore, 'the bundle plate 16 can be used as a cantilever branch and a plurality of membrane tubes 13 can be arranged in parallel. As a result, the membrane tube 13 can be filled in the casing n in a high density manner, and a unit equivalent to the casing 11 can be added. Volume membrane area · The two membrane tubes 13 are fixed to the housing 11 by a bundling plate 丨 6 arranged on only one side. Therefore, when performing maintenance, the housing can be easily removed by simply removing the fixing bolts 22 The body-side flange 12, the collecting plate 16, and the water collecting part 9 are separated to facilitate taking out the membrane element 10 to the outside of the casing 11. In addition, the plate 16 can prevent the film tube 13 from receiving the shape as in the past. By restricting the closed-bundle fixed membrane with the membrane tube 13 and the rigidity of the membrane tube plug on both sides of the front side tube, it is sufficient to form a non-fixed shape in a cantilever manner, such that any shape of It is supported in a bundled state. Therefore, the length of the shell is equipped with a general ceramic membrane tube, which has a double structure formed of a wide support on the membrane. Therefore, it is not easy to reduce the diameter. The tube wall is formed by a film forming material, and & the thin straight tube of the strength of the present invention, and formed 瞢 冰 13 is formed in Zhongding 'scared Ke w dry example from ~ still less wind ears, so that it has A thin straight tube with a predetermined strength is formed into a shape with the outer diameter of the tube and ed formed in a wall thickness of 0.2 to 0-8 mm. Therefore, the L to ^ 'tube can obtain a predetermined flux. In addition, during the normal operation described above, when the outside of the king's palace flows into the inside and transitions, the impurities contained in the membrane S 1 3 and the treated water are included.

314039.ptd 第21頁314039.ptd Page 21

553765 五、發明說明(11) 係作為膜面附著物陸續附著於各膜管1 3之外面。在剝離去 除該膜面附著物時,係進行以下逆洗運轉。換言之,逆洗 運轉係如第2圖虛線箭頭所示,將過濾處理水由過濾水排 出口 2 0供給至殼體1 1内,並由源水供給口 1 4排出至外部。 根據所述,由過濾水排出口 2 0所供給之過濾處理水,由各 膜管1 3之基端開口 1 3 a流入至各膜管1 3内側,而從各膜管 1 3之内側流出至外側,再由殼體1 1内部通過源水供給口 14 而排出至外部。如上述般,由於過濾處理水係由各膜管13 之内側流出至外側,因而使上述膜管1 3之外面之膜面附著 物從膜管1 3剝離去除。 在上述第1實施形態中,逆洗運轉係將過濾水排出口 2 0所供給之過濾處理水由源水供給口 1 4排出,但亦可由濃 縮水排出口 1 5將過濾水排出口 2 0所供給之過濾處理水排 出。或是在殼體11中,安裝逆洗水排出專用之逆洗水排出 口 (省略圖例),而由該逆洗排出口排出。 在上述第1實施形態中,進行逆洗運轉時,係由過濾 水排出口 2 0供給過濾處理水(經過濾處理之水)以進行逆 洗,但亦可供給與過濾處理水不同之逆洗專用的逆洗水。 在上述第1實施形態中,進行一般運轉時,係由源水 供給口 1 4供給被處理水而由過濾水排出口 2 0排出,但亦可 使被處理水朝相反方向流出。換言之,在以下說明之本發 明之第2實施形態中,如第5第,6圖所示,係將第1實施形 態中之源水供給口 1 4 (參照第2圖)作為過濾水排出口 3 0 (第1供排部之一例),而將第1實施形態中之過濾水排出553765 V. Description of the invention (11) It is successively attached to the outer surface of each membrane tube 13 as a film surface attachment. When peeling off the film surface attachment, the following backwash operation was performed. In other words, as shown by the dashed arrow in FIG. 2, the backwash operation supplies filtered water to the casing 11 through the filtered water discharge port 20 and discharges it to the outside through the source water supply port 14. According to the description, the filtered treated water supplied from the filtered water discharge port 20 flows into the inside of each membrane tube 13 through the base end opening 13 a of each membrane tube 13 and flows out from the inside of each membrane tube 13 To the outside, it is discharged from the inside of the casing 11 through the source water supply port 14 to the outside. As described above, since the filtered water flows out from the inside of each membrane tube 13 to the outside, the film surface attachments on the outer surface of the membrane tube 13 are peeled off and removed from the membrane tube 13. In the first embodiment described above, the backwash operation is to discharge the filtered water supplied from the filtered water discharge port 20 through the source water supply port 14, but the filtered water discharge port 20 may also be discharged from the concentrated water discharge port 15 The supplied filtered treated water is discharged. Alternatively, a backwash water discharge port (not shown in the figure) dedicated to backwash water discharge is installed in the casing 11 and discharged through the backwash discharge port. In the first embodiment described above, when the backwash operation is performed, the filtered water (filtered water) is supplied from the filtered water discharge port 20 for backwashing, but a backwash different from the filtered water may also be supplied. Dedicated backwash water. In the first embodiment described above, during normal operation, the treated water is supplied from the source water supply port 14 and discharged through the filtered water discharge port 20, but the treated water may also flow out in the opposite direction. In other words, in the second embodiment of the present invention described below, as shown in FIGS. 5 and 6, the source water supply port 14 (see FIG. 2) in the first embodiment is used as the filtered water discharge port. 3 0 (an example of the first supply and discharge unit), and the filtered water in the first embodiment is discharged

314039.ptd 第 22 頁 553765 五、發明說明(12) 口 2 0 (參照第2圖)作為源水供給口 3 1 (第1供排部之一例 )’並將第1實施形態中之集水部1 9 (參照第2圖)作為配 水部3 2。此外,上述源水供給口 3 1與集水部1 9,係用以構 成第2供排部。另外,在殼體11中尚安裝有排氣口 3 3。 以下,說明上述構成之作用。 進行一般運轉時,如第6圖之實線箭頭所示一般,係 將被處理水(流體)由兩源水供給口 3 1供給至殼體1 1内, 並由過濾水排出口 3 0排出至外部。換言之,由源水供給口 3 1供給至配水部3 2内之被處理水,由各膜管1 3之基端開口 1 3 a流入至各膜管1 3之内部流路1 3 c,再由各膜管1 3内側流 出至外側並經過過濾後,作為過濾處理水而由殼體丨丨内通 過過濾水排出口 30排出至外部。如上述一般,當被處理水 由f ΐ 1 3内側流出至外側並進行過濾時,包含於被處理水 之4貝’將作為膜面附著物,而陸續附著於各膜管1 3之内 面。剝=去除誘膜面附著物時,係進行下述之逆洗運轉。 一換言之’進行逆洗運轉時,如第6圖之實線箭頭所示 ^、曼,係將被處理水(流體)由過濾水排出口 30供給至殼 渦1内’並由兩源水供給口 3 1排出至外部。根據所述,由 水排出口 3〇供給至殼體内的過濾處理水,係由各膜管 配Ϊ Ϊϋ ^ ::,而由各膜管13之基端開D 13&通過 於過渡處理水係由::!1而排出至外部。如上述-般,由 述膜管13内面之^ ί f管13之外側流入至内側,因而使上 13a推出去除。、面附著物從膜管13剝離,再由基端開口314039.ptd Page 22 553765 V. Description of the invention (12) Port 2 0 (refer to Fig. 2) is used as source water supply port 3 1 (an example of the first supply and drainage unit) 'and collect water in the first embodiment The unit 1 9 (refer to FIG. 2) functions as the water distribution unit 32. The source water supply port 31 and the water collection unit 19 are used to form a second supply and discharge unit. In addition, an exhaust port 3 3 is installed in the casing 11. The effect of the above-mentioned configuration will be described below. During normal operation, as indicated by the solid arrows in FIG. 6, the water to be treated (fluid) is supplied from the two-source water supply port 31 to the casing 11 and discharged from the filtered water discharge port 30. To the outside. In other words, the water to be treated supplied from the source water supply port 31 to the water distribution unit 32 flows through the base end opening 1 3 a of each membrane tube 13 and flows into the internal flow path 1 3 c of each membrane tube 13. After flowing out from the inside of each membrane tube 13 to the outside and filtered, it is discharged as filtered water from the inside of the casing through the filtered water discharge port 30 to the outside. As described above, when the treated water flows out from the inside of f ΐ 1 3 to the outside and is filtered, 4 shells' contained in the treated water will be attached to the membrane surface and will be successively attached to the inner surface of each membrane tube 13. Peeling = To remove the attachment on the membrane surface, perform the following reverse washing operation. In other words, when performing the backwash operation, as indicated by the solid arrows in FIG. 6 ^, Mann is to supply the treated water (fluid) from the filtered water discharge port 30 into the shell vortex 1 and supply it from two source waters Port 31 is discharged to the outside. According to the description, the filtered treated water supplied into the housing from the water discharge port 30 is distributed by each membrane tube Ϊ ^ ^ ::, and the base end of each membrane tube 13 is opened D 13 & Caused by ::! 1 and discharged to the outside. As mentioned above, the inner side of the membrane tube 13 flows from the outer side of the f tube 13 to the inner side, so that the upper 13a is pushed out and removed. The surface attachment is peeled from the membrane tube 13 and then opened from the base end

553765 五、發明說明(13) 此時,由上述過濾水排出口 3 0供給至殼體1 1内之過濾 處理水,係由膜管1 3外面以相同方式壓入於膜管1 3之内 側,因此對附著於膜管1 3内面之膜面附著物同樣具有剝離 作用,藉此可輕易使膜面附著物剝離去除。此外,上述過 濾處理水由膜管1 3之外側流入至内側時,因過濾處理水之 流力集束於膜管1 3内,而增加膜管1 3内之内部流路之流 速,藉此,可提昇壓出及剝離去除膜管13内面之膜面附著 物之效果。 在上述第2實施形態中,逆洗運轉係將過濾水排出口 3 0所供給之過濾處理水由源水供給口 3 1排出,但亦可在配 水部3 2中安裝逆洗水排出口 (省略圖例),而由逆洗排出 口排出,從過滤水排出口 3 0所供給之過濾處理水,而非由 原水供給口引排出。 在上述第2實施形態中,進行逆洗運轉時,係由過濾 水排出口 3 0供給過濾處理水(經過濾處理之水)以進行逆 洗,但亦可供給與過濾處理水不同之逆洗專用的逆洗水。 接著,根據第7圖以說明本發明之第3實施形態。 在圓筒狀之配水部4 0兩端分別配置圓筒狀之殼體1卜 在上述配水部4 0兩端設置凸緣4 1。兩殼體1 1之一端係由閉 塞板1 1 c所封閉,而在其相反側之另一端安裝有膜元件插 入口 1 1 a與殼體側凸緣1 2。上述殼體側凸緣1 2與凸緣4 1係 以複數個固定螺栓2 2加以連接。此外,在殼體側凸緣1 2與 凸緣4 1之間,挾置並連接固定有插入於殼體1 1内之膜元件 1 0之集束板1 6以及襯墊1 8,2卜在兩殼體11之外圍上部設553765 V. Description of the invention (13) At this time, the filtered treated water supplied from the filtered water discharge port 30 to the housing 11 is pressed from the outside of the membrane tube 13 into the inside of the membrane tube 13 in the same manner. Therefore, the film surface attachments attached to the inner surface of the film tube 13 also have a peeling effect, so that the film surface attachments can be easily peeled off and removed. In addition, when the above-mentioned filtered water flows into the inside from the outside of the membrane tube 13, the flow force of the filtered water is concentrated in the membrane tube 13, and the flow velocity of the internal flow path in the membrane tube 13 is increased. The effect of extruding and peeling the film surface attachments on the inner surface of the film tube 13 can be improved. In the second embodiment described above, the backwashing operation is to discharge the filtered water supplied from the filtered water discharge port 30 through the source water supply port 31, but a backwash water discharge port may also be installed in the water distribution unit 32. The illustration is omitted), and the filtered treated water supplied from the filtered water discharge port 30 is discharged through the backwash discharge port, instead of being discharged through the raw water supply port. In the second embodiment described above, when the backwash operation is performed, the filtered water (filtered water) is supplied from the filtered water discharge port 30 for backwashing, but a backwash different from the filtered water may be supplied. Dedicated backwash water. Next, a third embodiment of the present invention will be described with reference to FIG. 7. Cylindrical housings 1 are disposed at both ends of the cylindrical water distribution portion 40, and flanges 41 are provided at both ends of the water distribution portion 40. One end of the two casings 1 1 is closed by a blocking plate 1 1 c, and a membrane element inlet 1 1 a and a casing-side flange 12 are installed at the other end on the opposite side. The case-side flange 12 and the flange 4 1 are connected by a plurality of fixing bolts 22. In addition, between the casing-side flange 12 and the flange 41, a cluster plate 16 and a gasket 18, 2 which are fixed and connected with a membrane element 10 inserted into the casing 11 are connected. The upper part of the periphery of the two shells 11 is provided

314039.ptd 第24頁 553765 五、發明說明(14) 有排氣口 4 2,在外圍下部則設有過濾水排出口 4 3 (第1供 排部之一例)。此外,上述過濾水排出口 4 3係於集束板16 之一側與各膜管1 3之外側相連通。 此外,在上述配水部4 0外圍上部設有源水供給部4 4, 在外圍下部則設有逆洗水排出口 45。上述源水供給部44與 逆洗水排出口 45及配水部4〇係用以構成第2供排部,而在 集束板1 6之另一側與各膜管丨3之基端開口丨3 a相連通。 此外’與上述源水供給部4 4相連接之源水供給用配管 4 7中’設有可開關該配管4 7内之流路之源水供給用閥(省 略圖示)。另外’在與上述逆洗水排出口 4 5相連接的逆洗 水排出用配管48中,則設有可開關該配管48内之流路之逆 洗水排出用閥(省略圖示)。 以下’說明上述構成之作用。 進订一般運轉時,如第7圖之實線箭頭所示一般,係 開f源水供給用閥,而關閉逆洗水排出用閥,將被處理水 (流體)由源水供給口 44供給至兩殼體丨丨内,並由兩過濾 水$出口 4 3排出至外部。換言之,由源水供給口 4權給至 的被處理水’係由各膜管13之基端開口 i3a流 $ & /, ΐ =、丨3之内部流路13 c,而由各膜管丨3之内側流出 =、、’經過濾後,作為過濾處理水而由兩殼體11内通過 膜:了水排出口4 3排出至外部。如上述-般,被處理水由 中二雜ί内::2至外側並進行過濾•,包含於被處理水 ^ ; 為膜面附著物,逐漸附著於各膜管1 3之内 剝離去除該膜面附著物時,係進行下述逆洗運轉。314039.ptd Page 24 553765 V. Description of the invention (14) There is an exhaust port 4 2 and a filtered water discharge port 4 3 is provided at the lower part of the periphery (an example of the first supply and discharge unit). The filtered water discharge port 43 is connected to one side of the bundle plate 16 and communicates with the outside of each membrane tube 13. In addition, a source water supply section 44 is provided at the upper part of the periphery of the water distribution section 40, and a backwash water discharge port 45 is provided at the lower part of the periphery. The source water supply unit 44, the backwash water discharge port 45, and the water distribution unit 40 are used to form a second supply and discharge unit, and the other side of the cluster plate 16 is opened with the base end of each membrane tube 3 a is connected. A source water supply valve (not shown) is provided in the source water supply pipe 47 connected to the source water supply unit 44. A backwash water discharge pipe 48 connected to the backwash water discharge port 45 is provided with a backwash water discharge valve (not shown) that can open and close the flow path in the pipe 48. Hereinafter, the effect of the above configuration will be described. During the normal operation of the order, as shown by the solid arrow in FIG. 7, the source water supply valve is opened, the backwash water discharge valve is closed, and the water to be treated (fluid) is supplied from the source water supply port 44. To the inside of the two casings and to the outside through the two filtered water outlets 4 3. In other words, the water to be treated given by the source water supply port 4 flows from the base end opening i3a of each membrane tube 13 & /, ΐ =, the internal flow path 13 c of 3, and each membrane tube 13 The inside outflow of 丨 3 = ,, and 'After filtering, the filtered water passes through the two casings 11 through the membrane: the water discharge port 43 is discharged to the outside. As mentioned above, the water to be treated is contained in the middle two: 2 to the outside and filtered •, included in the water to be treated ^; is a film surface attachment, gradually attached to each membrane tube 1 3 to remove the When the film surface is attached, the following backwash operation is performed.

314039.ptd 第25頁 553765 五、發明說明(15) 亦即,進行逆洗運轉時,如第7圖之虛線箭頭所示一 般,係在關閉源水供給用閥,開啟逆洗水排出用閥之狀態 下,使過濾處理水由兩過濾水排出口 4 3供給至兩殼體1 1 内,再由逆洗水排出口 4 5排出至外部。 根據所述,由兩過濾水排出口 4 3供給至兩殼體1 1内的 過濾、處理水,係由各膜管1 3之外側流入至内側,而由各膜 管1 3之基端開口 1 3 a通過配水部4 0内與逆洗水排出口 4 5而 排出至外部。如上述一般,由於過濾處理水係由各膜管13 之外側流入至内側,使上述膜管1 3内面之膜面附著物,從 膜管1 3剝離,再由基端開口 1 3 a壓出去除,而與逆洗水一 同由逆洗水排出口 4 5排出。 在上述第3實施形態中,逆洗運轉係將兩過濾水排出 口 4 3所供給之過濾處理水由逆洗水排出口 4 5排出,但亦可 不設置逆洗水排出口 4 5,而由源水供給口 4 4排出。 在上述第3實施形態中,進行逆洗運轉時,係由過濾 水排出口 4 3供給過濾處理水(經過濾處理之水)以進行逆 洗,但亦可供給與過濾處理水不同之逆洗專用的逆洗水。 前述之第1實施形態之陶瓷膜組件(參照第2圖)係採 用使被處理水由膜管1 3之外側流入至内側而進行過濾的形 式,而以下所說明之本發明之第4實施形態,係將上述第1 實施形態之陶瓷膜組件之部分予以改良後之膜組件。 如第8圖,第9圖所示,膜元件1 0與殼體1 1係與第1實 施形態共通,此外,源水供給口 1 4 (第1供排部之一例) 係設在殼體11之下部,而兩濃縮水排出口 1 5則設於殼體11314039.ptd Page 25 553765 V. Description of the invention (15) That is, when the backwash operation is performed, as shown by the dotted arrow in Fig. 7, the source water supply valve is closed and the backwash water discharge valve is opened. In this state, the filtered water is supplied into the two casings 1 1 through the two filtered water discharge ports 4 3, and then discharged to the outside through the backwash water discharge port 45. According to the description, the filtered and treated water supplied to the two housings 11 from the two filtered water discharge ports 43 flows into the inside from the outside of each membrane tube 13 and opens at the base end of each membrane tube 13 1 3 a is discharged to the outside through the water distribution unit 40 and the backwash water discharge port 45. As mentioned above, since the filtered water flows from the outside of each membrane tube 13 to the inside, the film surface attachments on the inner surface of the membrane tube 13 are peeled off from the membrane tube 13 and pressed out through the base end opening 1 3 a. It is removed and discharged from the backwash water discharge port 45 together with the backwash water. In the third embodiment described above, the backwashing operation is to discharge the filtered water supplied from the two filtered water outlets 4 3 through the backwashing water outlets 4 5. However, the backwashing water outlets 4 5 may not be provided and the The source water supply port 44 is discharged. In the third embodiment described above, when the backwash operation is performed, the filtered water (filtered water) is supplied from the filtered water discharge port 4 3 for backwashing, but a backwash different from the filtered water may also be supplied. Dedicated backwash water. The ceramic membrane module (refer to FIG. 2) of the first embodiment described above is a form in which the water to be treated flows into the inside from the outside of the membrane tube 13 and is filtered. The fourth embodiment of the present invention described below is used for filtration. It is a membrane module in which a part of the ceramic membrane module of the first embodiment is improved. As shown in FIG. 8 and FIG. 9, the membrane element 10 and the housing 11 are common to the first embodiment, and the source water supply port 14 (an example of the first supply and discharge section) is provided in the housing. 11 lower part, and two concentrated water outlets 15 are provided in the housing 11

314039.ptd 第26頁 553765 五、發明說明(16) 之上部。 於殼體11之兩端,以可自由裝卸方式,安裝用以覆蓋 填充於殼體1 1内之膜元件1 0之各膜管丨3之基端開口 1 3 a側 之帽子狀蓋罩5卜 換言之,在上述蓋罩5 1之開口端之外周緣設置有蓋罩 側凸緣5 2。並在將上述集束板1 6之外周部挾置於上述殼體 側凸緣1 2與蓋軍側凸緣5 2之間的狀態下,藉由使用複數個 固定螺栓2 2連接上述殼體側凸緣1 2與蓋罩側凸緣5 2之方 式’使兩膜元件1 〇分別以水平方式安裝固定於殼體丨丨内。 此外,在集束板1 6與殼體側凸緣1 2之間,係藉由一側 之襯墊以不滲水方式密封。而在集束板丨6與蓋罩側凸緣5 2 之間,則藉由另一側之襯墊以不滲水方式密封。此外,過 濾水排出口 2 0係安裝於上述蓋罩5丨之外周上部,而在蓋罩 5 1之外周下部則設有用以排出蓋罩5丨内之排水之排水排 口 53。 此外’上述蓋罩5 1與過濾水排出口 2 〇,係用以構成第 2供排部,而在集束板丨6之另一側,與各膜管丨3之基端開 口 1 3 a相連通。 以下,說明上述構成之作用。 進行一般運轉時,如第8圖之實線箭頭所示一般,由 源水供給口 1 4供給至殼體11内之被處理水(流體),係在 由各膜管1 3外側透過内側時經各膜管丨3過濾後,作為過遽 處理水通過膜管丨3内部流路1 3c而由基端開口 1 3a流入至^ 罩5 1内’再由過濾水排出口 2 〇排出至外部。此外,在進行314039.ptd Page 26 553765 V. Description of the invention (16) Upper part. At both ends of the housing 11, a cap-shaped cover 5 for covering the base end openings of the membrane elements 10 filled with the membrane elements 10 in the housing 11 in a freely attachable and detachable manner is installed 5 In other words, a cover-side flange 52 is provided on the outer peripheral edge of the open end of the cover 51. In a state where the outer periphery of the bundle plate 16 is interposed between the housing-side flange 12 and the cover-side flange 52, the housing side is connected by using a plurality of fixing bolts 22. The method of the flange 12 and the cover-side flange 52 allows the two membrane elements 10 to be installed and fixed in the housing 丨 丨 horizontally, respectively. In addition, between the cluster plate 16 and the case-side flange 12 are sealed with watertightness by a gasket on one side. Between the cluster plate 6 and the cover-side flange 5 2, it is sealed in a water-tight manner by a gasket on the other side. In addition, the filtered water discharge port 20 is installed at the upper part of the outer periphery of the cover 5 丨, and the lower part of the outer periphery of the cover 5 is provided with a drain outlet 53 for draining water from the cover 5 丨. In addition, the above-mentioned cover 51 and the filtered water discharge port 20 are used to constitute the second supply and discharge section, and on the other side of the cluster plate 6 are connected to the base opening 1 3 a of each membrane tube 3 through. The effect of the above-mentioned configuration will be described below. During normal operation, as indicated by the solid arrow in FIG. 8, the water to be treated (fluid) supplied from the source water supply port 14 to the casing 11 is transmitted from the outside of each membrane tube 13 to the inside. After filtering through each membrane tube 3, the treated water passes through the internal flow path 1 3c of the membrane tube 3 and flows from the base opening 1 3a to the ^ cover 5 1 'and is then discharged to the outside through the filtered water discharge port 2 0. . In addition,

314039.ptd314039.ptd

第27頁 553765 五、發明說明(17) 交叉流入過濾時,濃縮水係在上述一般運轉中由濃縮水排 出口 1 5排出,而在進行全量過濾時,則關閉濃縮水排出口 1 5進行運轉,而不排出濃縮水。 此外,進行逆洗運轉時,如第8圖之虛線箭頭所示一 般,係將過濾處理水由兩過濾水排出口 2 0供給至殼體11 内,並由源水供給口 1 4排出至外部。根據所述,由過濾、水 排出口 2 0供給至蓋罩5 1内的過濾處理水,係由各膜管1 3之 基端開口 1 3a流入至各膜管1 3之内側,而由各膜管1 3之内 側流出至外側,再由殼體1 1内通過源水供給口 1 4排出至外 部。如上述一般,由於過濾處理水係由各膜管1 3之内側流 出至外側,因而使上述膜管1 3外面之膜面附著物從膜管13 剝離去除。 此外,在上述第4實施形態中,進行逆洗運轉時,係 由過濾水排出口 2 0供給過濾處理水(經過濾處理之水)以 進行逆洗,但亦可供給與過濾處理水不同之逆洗專用的逆 洗水。 前述第2實施形態之陶瓷膜組件(參照第6圖)係採用 使被處理水由膜管1 3之内側流出至外側以進行過濾之形 式,以下,說明將上述第2實施形態之陶瓷膜組件之一部 分予以改良後之膜組件,以作為第5實施形態。 如第1 0圖、第1 1圖所示,膜元件1 0與殼體1 1係與第1 及第2實施形態共通,此外,源水供給口 3 1係設在兩蓋罩 5 1之外周下部,並由該源水供給口 3 1與蓋罩5 1構成第2供 排部。此外,在兩蓋罩5 1之外周上部則安裝有排氣口 3 3。Page 27 553765 V. Description of the invention (17) During cross-flow filtration, the concentrated water is discharged from the concentrated water discharge port 15 during the above-mentioned general operation, and when full filtration is performed, the concentrated water discharge port 15 is closed for operation Without draining concentrated water. In addition, when the backwash operation is performed, as shown by the dotted arrows in FIG. 8, the filtered water is supplied into the casing 11 through the two filtered water discharge ports 20 and discharged to the outside through the source water supply port 14. . According to the description, the filtered treated water supplied from the filter and water discharge port 20 to the cover 51 is flowed into the inside of each membrane tube 13 through the base end opening 13a of each membrane tube 13 and The inside of the membrane tube 13 flows out to the outside, and is discharged from the inside of the casing 11 through the source water supply port 14 to the outside. As described above, since the filtered water flows out from the inside of each membrane tube 13 to the outside, the film surface attachments on the outside of the membrane tube 13 are peeled off from the membrane tube 13 and removed. In addition, in the fourth embodiment described above, when the backwash operation is performed, the filtered water (filtered water) is supplied from the filtered water discharge port 20 for backwashing. However, it may be different from the filtered water Dedicated backwash water. The ceramic membrane module of the second embodiment (refer to FIG. 6) is a form in which the treated water flows out from the inside of the membrane tube 13 to the outside for filtering. The ceramic membrane module of the second embodiment will be described below. A part of the modified membrane module is used as a fifth embodiment. As shown in FIG. 10 and FIG. 11, the membrane element 10 and the housing 11 are common to the first and second embodiments, and the source water supply port 31 is provided in the two covers 5 1. A lower part of the outer periphery constitutes a second supply / discharge portion by the source water supply port 31 and the cover 51. In addition, an exhaust port 3 3 is attached to the outer periphery of the two covers 51.

314039.ptd 第28頁 553765 五、發明說明(18) 此外,過濾水排出口 3 0 (第1供排部之一例)係安裝 於殼體1 1之上部,而在殼體1 1下部則設有排水排出口 3 4。 以下,說明上述構成之作用。 進行一般運轉時,如第1 0圖之實線箭頭所示一般,被 處理水(流體)由兩源水供給口 3 1供給至殼體11内,並由 過濾水排出口 3 0排出至外部。換言之,由源水供給口 3 1供 給至蓋罩5 1内之被處理水,係由各膜管1 3之基端開口 1 3 a 流入至各膜管1 3之内部流路1 3 c,並於由膜管1 3之内側透 出於外側時進行過濾,之後,作為過濾處理水而由殼體11 内通過過濾水排出口 3 0排出至外部。 此外,進行逆洗運轉時,如第1 0圖之虛線箭頭所示一 般,係將過濾處理水由過濾水排出口 3 0供給至殼體1 1内, 並由兩源水供給口 3 1排出至外部。根據所述,由過濾水排 出口 3 1供給至殼體1 1内的過濾處理水,係由各膜管1 3之外 側透過内側,而由各膜管1 3之基端開口 1 3 a,通過蓋罩5 1 内及源水供給口 3 1而排出至外部。如上述一般,由於過渡 處理水係由各膜管1 3之外側流入至内側,因而可使上述膜 管1 3内面之膜面附著物從膜管1 3剝離,並由基端開口 1 3 a 推出去除。 此外,在上述第5實施形態中,進行逆洗運轉時,係 由過濾水排出口 3 0供給過濾處理水(經過濾處理之水)以 進行逆洗,但亦可供給與過濾處理水不同之逆洗專用的逆 洗水。 此外,在上述各實施形態中,係將膜管1 3之管外徑作314039.ptd Page 28 553765 V. Description of the invention (18) In addition, the filtered water discharge port 30 (an example of the first supply and discharge part) is installed on the upper part of the casing 11 and is provided on the lower part of the casing 11 There are drainage outlets 3 4. The effect of the above-mentioned configuration will be described below. During normal operation, as indicated by the solid arrows in FIG. 10, the water to be treated (fluid) is supplied into the casing 11 from the two source water supply ports 31 and discharged to the outside through the filtered water discharge port 30. . In other words, the to-be-treated water supplied from the source water supply port 31 to the cover 5 1 flows into the internal flow path 1 3 c of each membrane tube 13 through the base end opening 1 3 a of each membrane tube 13, After filtering from the inside of the membrane tube 13 to the outside, filtering is performed, and thereafter, the filtered water is discharged from the inside of the housing 11 through the filtered water discharge port 30 to the outside. In addition, during the reverse washing operation, as indicated by the dotted arrow in FIG. 10, the filtered water is supplied from the filtered water discharge port 30 into the casing 11 and discharged from the two source water supply ports 31. To the outside. According to the description, the filtered treated water supplied from the filtered water discharge port 31 to the inside of the casing 11 is transmitted from the outside of each membrane tube 13 to the inside, and the base end of each membrane tube 13 is opened 1 3 a. It is discharged to the outside through the inside of the cover 5 1 and the source water supply port 31. As described above, since the transition water flows from the outside of each membrane tube 13 to the inside, the film surface attachments on the inner surface of the membrane tube 13 can be peeled off from the membrane tube 13 and opened at the base end 1 a Introduced for removal. In addition, in the fifth embodiment described above, when the backwash operation is performed, the filtered water (filtered water) is supplied from the filtered water discharge port 30 for backwashing, but it may be different from the filtered water Dedicated backwash water. In addition, in each of the above embodiments, the outer diameter of the film tube 13 is set as

314039.ptd 第29頁 553765 五、發明說明(19) 成1至6mmp ,而將膜管1 3之管壁厚度作成0. 2至0 . 8mm,該 等數值之設計原理係根據以下之說明。 首先,對標準形狀之膜管之測試品進行3點彎曲測試 及純水滲透流束測試,可獲得以下結果以作為膜管之性 能。 〈形狀〉膜管外徑:Do = 3.3mm,膜管厚度=0.35m計膜管 内徑:D尸2 · 6mm 〈3點彎曲測試結果〉彎曲破壞載重·· P b3= 2 8. 9 N (支點間 距離:L : 3Omm) 〈純水滲透流束測試結果〉純水滲透流束:J PW= 2 2 _ 7 m / d a y (壓力:PPW=98jPa,水溫·· tPW = 25°C ) 根據3點彎曲測試結果,可求出膜管材質之3點彎曲強度: 〇 b3° σ b3=M/Z· · · (1) 負載載重點(支點間中央)之彎曲力矩:M = Pb3L/4 • · · (2) 剖面係數:Z = 7T /32x (DoLDA/Do· · · (3) 因此,Μ = 28·9χ 30/4 = 217Ν· mm Ζ = 7Γ /3 2χ ( 3. 3 4- 2. 6 4)/ 3. 3 - 2. 1 7mm3 σ b3=217/2· 17 = 100Mpa 顯示3點彎曲強度與材料強度之不均之威伯爾(W e i b u 1 1 )係 數:由m 推定拉力強度:σ t 一般而言陶瓷材料一般為m = 5至2 0314039.ptd page 29 553765 V. Description of the invention (19) It is 1 to 6mmp, and the thickness of the wall of the membrane tube 13 is made 0.2 to 0.8mm. The design principle of these values is based on the following description. First, a 3-point bending test and a pure water permeation beam test were performed on a test piece of a standard shape film tube, and the following results were obtained as the performance of the film tube. <Shape> Outer diameter of membrane tube: Do = 3.3mm, thickness of membrane tube = 0.35m. Inner diameter of membrane tube: D 2 · 6mm <Result of 3-point bending test> Bending failure load · P b3 = 2 8. 9 N ( Distance between fulcrum points: L: 3Omm) <Test results of pure water osmotic stream> Pure water osmotic stream: J PW = 2 2 _ 7 m / day (pressure: PPW = 98jPa, water temperature ·· tPW = 25 ° C) Based on the results of the 3-point bending test, the 3-point bending strength of the film tube material can be obtained: 〇b3 ° σ b3 = M / Z · · · (1) Bending moment at the load point (center between the fulcrum points): M = Pb3L / 4 • · · (2) Section coefficient: Z = 7T / 32x (DoLDA / Do · · · (3) Therefore, M = 28 · 9χ 30/4 = 217N · mm Zn = 7Γ / 3 2χ (3. 3 4 -2. 6 4) / 3. 3-2. 1 7mm3 σ b3 = 217/2 · 17 = 100Mpa The Weibull (W eibu 1 1) coefficient showing the difference between the bending strength and material strength at 3 points: from m Estimated tensile strength: σ t Generally speaking, ceramic materials are generally m = 5 to 2 0

314039.ptd 第30頁 553765 五、發明說明(20) 但是,由於膜管材質為多孔體之陶瓷,且材質強度 差異較大之故,而假設為m = 5。σ 士與σ bA關係如下。 o t=a b^· { 2x(ra + l )2} Vm 因此,σ t=100+ {2x(5+l)2} 1/5=42. 5Mpa 膜管外徑之下限值=1 m m之根據如下。 根據前列公式(1 )至(3 ),由Do與D求算P b炙公式如 下。314039.ptd Page 30 553765 V. Description of the invention (20) However, since the membrane tube is made of porous ceramics and the material strength varies greatly, it is assumed that m = 5. The relationship between σ and σ bA is as follows. ot = ab ^ · {2x (ra + l) 2} Vm Therefore, σ t = 100 + {2x (5 + l) 2} 1/5 = 42. 5Mpa The lower limit of the outer diameter of the membrane tube = 1 mm Based on the following. According to the foregoing formulae (1) to (3), the formula for calculating P b from Do and D is as follows.

Pb3=4x ο ^ {π /3 2x (Do1- Di^/Do}^ L 藉由以與測試品相同之材質(相同之σ b3)、相同膜 厚、相同3點彎曲測試條件(相同之L)縮小膜管之Do時, P b則如下式所示··Pb3 = 4x ο ^ {π / 3 2x (Do1- Di ^ / Do} ^^ L) By using the same material as the test product (same σ b3), the same film thickness, and the same 3-point bending test conditions (same L ) When reducing the Do of the membrane tube, P b is shown as follows:

Do = 2· 0mm(DI = l· 3mm)一 Pb3二8· 6N Do=l· 0mm(DI = 0· 3mm)— Pb3=l. 3N Do = 0. 8mm(DI = 0. 1mmPb3=0. 7N 根據膜管之使用條件,將PbA下限設定為1. 〇N時,Do 之下限則為1. 0mini右。 膜管外徑之上限值=6 m m之根據如下。 以Do與D求出内壓破壞壓力:P之公式如下。 P t= 2x o ( D ο — D ι)+ (1 · 2x D ο — 0 . 2x D i) 設定形狀係數:7? = 1 藉由以與測試品相同之材質(相同之σ t)、相同膜 厚,加大膜管之D 〇時,P t係如下所示:Do = 2.0mm (DI = 1.3mm)-Pb3 2 8N Do = 1.0mm (DI = 0.3mm)-Pb3 = 1. 3N Do = 0.8mm (DI = 0.1mmPb3 = 0. 7N According to the conditions of use of the membrane tube, when the lower limit of PbA is set to 1.0%, the lower limit of Do is 1.0mini right. The upper limit of the outer diameter of the membrane tube = 6 mm is as follows. Calculated by Do and D Internal pressure failure pressure: The formula for P is as follows: P t = 2x o (D ο — D) + (1 · 2x D ο — 0. 2x D i) Set the shape factor: 7? = 1 When the same material (same σ t) and the same film thickness are used to increase D 〇 of the film tube, P t is as follows:

Do = 5. 0mm(DI=4. Smm)-^ Pt=6. 31MPa Do = 6. OmmCD^S. 3mmPt=5. 20MPaDo = 5. 0mm (DI = 4. Smm)-^ Pt = 6. 31MPa Do = 6. OmmCD ^ S. 3mmPt = 5. 20MPa

314039.ptd 第31頁 553765 五、發明說明(21)314039.ptd Page 31 553765 V. Description of the Invention (21)

Do = 7. OmmCD^e. 3mm)-&gt; Pt=4. 43MPa 根據膜管之使用條件,將Pt^下限設定為5. 0MPa 時,Do之上限則變為6. OmmiL右程度。 膜管厚度下限值=0. 2m m之根據如下。 藉由以與測試品相同之材質(相同之σ t)、相同D ο, 縮小膜管之膜厚時,Ρ係如下所示: 膜厚 sO.SOmnKDfZ.Tmm)— Pf 8. 34MPa 膜厚=0.20111111(0^2.9111111)-^ P ^5. 42MPa 膜厚 rO.lSmnKDfS.Omm)— PpLOlMPa 根據膜管之使用條件,將P A下限設定為5 . 0 MPa 時,膜厚之下限則變為0. 2mm左右。 膜管厚度上限值=0. 8m m之根據如下。 膜過濾中之滲透阻力:J與膜間差壓:P係基於以下關 係。 J = P/ 7? tR 在此為,R:滲透阻力,t: t°C下之滲 透水黏度。換言之,在純水滲透流束測試中,係形成以下 關係。 J pw_ P pw/ &quot; 25尺 此外,在相同之膜材質之情況下,膜厚與R係呈反比 例。 根據上述,在與測試品相同之材質、相同之純水滲透 流束測試條件(相同之P pw,相同之t pw)下增加膜管厚度 時,j p你如下所示: 膜厚=0 · 7 m m ( R =測試品之 2 · 0倍)-&gt; J pw= 1 1 · 4 m / d a yDo = 7. OmmCD ^ e. 3mm)-&gt; Pt = 4. 43MPa When the lower limit of Pt ^ is set to 5.0 MPa according to the conditions of use of the membrane tube, the upper limit of Do becomes 6. OmmiL right degree. The lower limit of the thickness of the membrane tube = 0.2 mm is based on the following. By reducing the film thickness of the film tube with the same material (same σ t) and the same D ο as the test product, P is as follows: Film thickness sO.SOmnKDfZ.Tmm) — Pf 8. 34MPa Film thickness = 0.20111111 (0 ^ 2.9111111)-^ P ^ 5. 42MPa film thickness rO.lSmnKDfS.Omm) — PpLOlMPa When the lower limit of PA is set to 5.0 according to the conditions of use of the film tube, the lower limit of film thickness becomes 0. About 2mm. The upper limit of the thickness of the membrane tube = 0.8 mm is based on the following. Permeation resistance in membrane filtration: Differential pressure between J and membrane: P is based on the following relationship. J = P / 7? TR Here, R: permeation resistance, t: permeation water viscosity at t ° C. In other words, in the pure water osmotic flow test, the following relationship is formed. J pw_ P pw / &quot; 25 feet In addition, with the same film material, the film thickness is inversely proportional to the R system. According to the above, when the thickness of the membrane tube is increased under the same material and test conditions of the same pure water permeating stream as the test product (the same P pw, the same t pw), jp you are as follows: Film thickness = 0 · 7 mm (R = 2 · 0 times the test product)-&gt; J pw = 1 1 · 4 m / day

314039.ptd 第32頁 553765 五、發明說明(22) 膜厚=0.8mm( R =測試品之 2 · 3倍)—Jpw=9.9m/day 膜厚=0.9mm( R =測試品之 2 · 6倍)—jpw=8.7m/day 根據膜管之使用條件,將JPA下限設定為l〇m/day 時,膜厚之上限則變為0 . 8mm左右。 經過以上之檢討製作各種形狀之膜管,以測定其強度 與透水性。第1 2圖係顯示膜管之強度與透水性之測定結果 一覽表。 此外,根據第12圖之一覽表,當膜管之外徑為0. 8mm 時,3點彎曲破壞載重之計算值與實測值兩者皆比下限基 準值之1. 0N小(判定=X),外徑為1. 0mm時,3點彎曲破壞 載重之計算值與實測值兩者皆比下限基準值之1. 0N大(判 定=〇)。根據此點,將膜管1 3之管外形之最小值設定為 1· 0mm 〇 此外,當膜管之外徑為7. 0mm時,内壓破壞壓力之計 算值與實測值兩者皆比下限基準值之5 . OMPa小(判定= X),外徑為6 . 0 mm時,内壓破壞壓力之計算值與實測值兩 者皆比下限基準值之5.0MP a大(判定=〇)。根據此點, 將膜管1 3之管外形之最大值設定為6.0mm。 此外,當膜管之厚度為0.15m m時,内壓破壞壓力之計 算值與實測值兩者皆比下限基準值之5 . 0 Μ P a小(判定= X),厚度為0. 2 0mm時,内壓破壞壓力之計算值與實測值 兩者皆比下限基準值之5 · 0 Μ P a大(判定=〇)。根據此 點,將膜管1 3之厚度之最小值設定為0 . 2 0 mm。 此外,當膜管之厚度為0.90m m時,純粹滲透流束之計314039.ptd Page 32 553765 V. Description of the invention (22) Film thickness = 0.8mm (R = 2 times of the test product)-Jpw = 9.9m / day Film thickness = 0.9mm (R = 2 of the test product · 6 times) —jpw = 8.7m / day According to the use conditions of the film tube, when the lower limit of JPA is set to 10m / day, the upper limit of the film thickness becomes about 0.8mm. After the above review, film tubes of various shapes were made to measure their strength and water permeability. Figure 12 shows a list of measurement results of strength and water permeability of the membrane tube. In addition, according to the list in Figure 12, when the outer diameter of the membrane tube is 0.8 mm, both the calculated value and the measured value of the 3-point bending failure load are smaller than 1. 0N of the lower limit reference value (determination = X), When the outer diameter is 1.0 mm, both the calculated value and the measured value of the 3-point bending failure load are greater than 1.0 N of the lower limit reference value (determination = 0). Based on this, the minimum value of the outer shape of the membrane tube 13 is set to 1.0 mm. In addition, when the outer diameter of the membrane tube is 7.0 mm, the calculated value and the measured value of the internal pressure failure pressure are both lower than the lower limit. The reference value of 5.0 MPa is small (judgment = X), and when the outer diameter is 6.0 mm, both the calculated value and the measured value of the internal pressure failure pressure are larger than the lower limit reference value of 5.0 MP a (decision = 0). Based on this, the maximum value of the outer shape of the film tube 13 is set to 6.0 mm. In addition, when the thickness of the membrane tube is 0.15mm, both the calculated value and the measured value of the internal pressure failure pressure are smaller than the lower limit reference value of 5.0 M P a (decision = X), and the thickness is 0.2 mm. Both the calculated value and the measured value of the internal pressure failure pressure are larger than the lower limit reference value of 5 · 0 Μ Pa (determination = 0). Based on this, the minimum value of the thickness of the membrane tube 13 is set to 0.20 mm. In addition, when the thickness of the membrane tube is 0.90m

314039.ptd 第33頁 553765 五、發明說明(23) 算值與實測值兩者皆比了限基準值之1 〇m/day小(判定=χ )’厚度為0·80ιη m時,純粹滲透流束之計算值與實測值兩 者皆比下限基準值之1 〇 m / d a y大(判定=〇)。根據此點, 將膜管13之厚度之最大值設定為〇.80 mm。 接著,根據第1 3圖至第1 7圖說明本發明之第6實施形 態。 第6實施形態係將上述第4及第5實施形態中之膜管1 3 與集束板1 6之黏接部分變更後之形態,其殼體1 1與膜元件 1 0及蓋罩5 1等係與上述第4及第5實施形態共通。如第8圖 第9圖所示’殼體丨丨係在與兩膜元件丨〇之間所形成之供水 空間11 b相對應之位置,設有用以供給被處理水(被處理 液之一例)之源水供給口 1 4,其兩側則具備有濃縮水排出 口 1 5或是排氣口。 上述膜元件1 〇係如第1 3圖、第1 4圖所示,係由前端閉 塞之細直管狀之陶瓷製之複數個膜管1 3 ;以及將該等膜管 1 3集束固定之圓板形狀之集束板1 6所構成。此外,上述各 膜管1 3係僅以膜形成材形成管壁,並作成管外徑為!至6mm P ,管壁厚度0· 2至0· 8mm,孔徑為0· 05至10/z m,長度約 為3 0 0呈8 0 0 m m之形狀。 此外’於上述集束板1 6上形成有複數個貫穿孔5 5 (參 照第1 6圖),上述各膜管1 3之基端側係插通於該等貫穿孔 5 5。此外’在集束板1 6之外周部則形成有複數個螺栓孔 56〇 一側之襯墊1 8形成圓環狀,並與上述集束板1 6之表面314039.ptd Page 33 553765 V. Explanation of the invention (23) Both the calculated value and the measured value are smaller than the limit reference value of 1 m / day (judgment = χ). When the thickness is 0 · 80 μm, pure penetration Both the calculated and measured values of the beam are larger than 10 m / day of the lower limit reference value (decision = 0). Based on this, the maximum value of the thickness of the membrane tube 13 is set to 0.80 mm. Next, a sixth embodiment of the present invention will be described with reference to Figs. 13 to 17. The sixth embodiment is a modified form of the bonding portion of the membrane tube 13 and the bundle plate 16 in the fourth and fifth embodiments described above, and the casing 11 and the membrane element 10 and the cover 5 1 and the like are changed. It is common to the fourth and fifth embodiments. As shown in FIG. 8 and FIG. 9, the 'housing 丨 丨' is provided at a position corresponding to the water supply space 11 b formed between the two membrane elements 丨 〇, and is provided for supplying treated water (an example of a treated liquid). The source water supply port 14 is provided with a concentrated water discharge port 15 or an exhaust port on both sides. The above-mentioned membrane element 10 is a plurality of membrane tubes 1 3 made of a thin straight tube-shaped ceramic which is closed at the front end as shown in FIG. 13 and FIG. 14; A plate-shaped bundle plate 16 is formed. In addition, each of the above-mentioned film tubes 1 to 3 is formed of a tube wall only with a film forming material, and the outer diameter of the tube is made as follows! To 6 mm P, wall thickness of 0.2 to 0.8 mm, hole diameter of 0.05 to 10 / z m, and length of about 300 to 800 mm. In addition, a plurality of through holes 5 5 are formed in the bundle plate 16 (see FIG. 16), and the base end side of each of the film tubes 13 is inserted into the through holes 55. In addition, a plurality of bolt holes 56 are formed on the outer periphery of the cluster plate 16 and the gasket 18 on one side is formed into a ring shape, and is similar to the surface of the cluster plate 16

314039.ptd 第 34 頁 553765 五、發明說明(24) 1 6 a (面向膜管1 3之前端側之面)之外周部相黏接。一側 之凹部5 7 (參照第1 6圖)係由一側之襯墊1 8之内周面與集 束板1 6之表面1 6 a (相當於表裡一面)所形成。 此外,另一側之襯墊2 1係形成於圓環狀,並與集束板 1 6之背面1 6 b (面向膜管1 3之基端側之面)之外周部相黏 接。另一側之凹部5 8 (參照第1 6圖)係由另一側之襯塾2 1 之内周面與集束板16之背面16b(相當於表裡一面)所形 成。各膜管1 3即是藉由填充於上述一側以及另一侧之凹部 5 7,5 8之黏合劑5 9 (矽膠等)以不滲水方式黏接於集束板 1 6上。 此外,上述一側及另一側之襯墊1 8,2 1中,形成有與 上述螺栓孔相吻合之複數個孔部6 0。此外,上述集束板i 6 係由塑膠或不銹鋼等金屬或是陶瓷等製成。 如第1 5圖所示,在將上述集束板1 6之外周部挾置於上 述殼體側凸緣1 2與蓋罩側凸緣5 2之間的狀態下,使用複數 個固定螺栓2 2、螺帽2 3,以連結殼體側凸緣1 2與蓋罩側凸 緣5 2,藉此,如第8圖所示,可使膜元件1 〇以水平方式安 裝固定於殼體1 1内。 此外,如第1 5圖所示,上述一側之襯墊1 8係以不滲水 方式將集束板1 6與殼體側凸緣1 2之間予以密封,而另一側 之襯墊2 1則以不滲水方式將集束板1 6與蓋罩側凸緣5 2之間 予以密封。 此外,上述固定螺栓2 2係插通在形成於各凸緣1 2,5 2 之複數固螺栓孔2 4與上述襯墊1 8,2 1之孔部6 0 (參照第i 3314039.ptd page 34 553765 V. Description of the invention (24) 1 6 a (face facing the front end side of the membrane tube 13) The outer peripheral parts are adhered. The recess 5 7 on one side (refer to FIG. 16) is formed by the inner peripheral surface of the gasket 18 on one side and the surface 16 a (corresponding to the front and back surfaces) of the beam plate 16. In addition, the gasket 21 on the other side is formed in a ring shape, and is bonded to the outer periphery of the back surface 16b (the surface facing the base end side of the membrane tube 13) of the cluster plate 16. The concave portion 5 8 (refer to FIG. 16) on the other side is formed by the inner peripheral surface of the lining 2 1 on the other side and the rear surface 16 b (corresponding to the front and rear surfaces) of the cluster plate 16. Each membrane tube 13 is adhered to the cluster plate 16 in a water-impermeable manner by an adhesive 5 9 (silicone, etc.) filled in the recesses 5 7, 5 8 on one side and the other side. Further, a plurality of hole portions 60 corresponding to the bolt holes are formed in the spacers 18, 21 on the one side and the other side. In addition, the above-mentioned bundle plate i 6 is made of metal such as plastic, stainless steel, or ceramic. As shown in FIG. 15, a plurality of fixing bolts 2 2 are used in a state where the outer peripheral portion of the bundle plate 16 is interposed between the case-side flange 12 and the cover-side flange 5 2. And nut 2 3 to connect the housing-side flange 12 and the cover-side flange 5 2 so that, as shown in FIG. 8, the membrane element 10 can be installed and fixed horizontally to the housing 1 1 Inside. In addition, as shown in FIG. 15, the gasket 18 on one side seals the cluster plate 16 and the casing-side flange 12 in a watertight manner, and the gasket 2 1 on the other side is sealed. Then, the watertightness is sealed between the cluster plate 16 and the cover-side flange 52. The fixing bolt 22 is inserted through a plurality of fixing bolt holes 24 formed in the flanges 12 and 5 2 and the hole portions 6 0 of the pads 18 and 21 (see i 3

3l4〇39.ptd 第35頁 553765 五、發明說明(25) 圖)以及集束板1 6之螺栓孔5 6 (參照第1 3圖)。 此外,如第8圖、第9圖所示,過濾水排出口 20係設置 於蓋罩5 1之外周上部,而排水排出口 5 3則設置於蓋罩5 1之 外周下部。 以下,說明上述構成之作用。 在製造上述膜元件1 0時,如第1 6圖所示,係利用黏合 劑將一側之襯墊黏接於形成複數個貫穿孔5 5與螺栓孔5 6之 集束板1 6之表面1 6 a,而利用黏合劑將另一側之襯墊黏接 於集束板1 6之背面1 6b。藉此,無須經由機械加工(切削 加工等),即可形成一側以及另一側之凹部5 7,5 8。此 外,如第1 7圖所示,將各膜管1 3之基端開口 1 3 3側插通於 集束板1 6之各貫穿孔55。然後,如第丨3圖所示,於一側之 凹部5 7及另一側之凹部5 8灌入黏合劑並予以填充,而將各 膜管1 3黏接於集束板1 6。 ' 藉此’由於無須經過機械加工(切削加工)即可形成 上述一側及另一側之凹部57,58,因此,可省略在集束板 1 6側進行機械加工’而輕易地將膜管丨3安裝在集束板16 上。 此外,如第13圖所示,因各膜管13係藉由填充於_側 及另一側之凹部57, 5 8之黏合劑59,黏接於集束板16上, 因此可使膜管13穩固且確實地安裳在集束板16上,以避免 產生膜管1 3從集束板1 6上脫落之問題。 如第15圖、第16圖所示,一側之襯墊18,除了具有可 密封集束板16與殼體側凸緣12之間之功能外,冑兼具形成3l40〇39.ptd Page 35 553765 V. Description of the invention (25) Figure) and bolt holes 56 of the cluster plate 16 (refer to Figure 13). In addition, as shown in Figs. 8 and 9, the filtered water discharge port 20 is provided at the upper portion of the outer periphery of the cover 51, and the drain discharge port 5 3 is provided at the lower portion of the outer periphery of the cover 51. The effect of the above-mentioned configuration will be described below. When manufacturing the above-mentioned membrane element 10, as shown in FIG. 16, the gasket on one side is adhered to the surface 1 of the cluster plate 16 forming a plurality of through holes 5 5 and bolt holes 5 6 by using an adhesive. 6 a, and the other side pad is adhered to the back surface 16 b of the cluster plate 16 with an adhesive. This allows the recesses 5 7 and 5 8 on one side and the other side to be formed without machining (cutting, etc.). In addition, as shown in FIG. 17, the base end openings 1 3 and 3 of each membrane tube 13 are inserted into each of the through holes 55 of the cluster plate 16. Then, as shown in FIG. 3, the concave portion 57 on one side and the concave portion 5 8 on the other side are filled with an adhesive and filled, and each film tube 13 is adhered to the cluster plate 16. 'By this', since the recesses 57 and 58 on one side and the other side can be formed without machining (cutting), it is possible to omit the membrane tube easily by machining on the 16 side of the cluster plate 丨3 Installed on the cluster plate 16. In addition, as shown in FIG. 13, since each of the film tubes 13 is adhered to the cluster plate 16 by the adhesive 59 filled in the recesses 57, 5 8 on the _ side and the other side, the film tube 13 can be made. It is firmly and surely installed on the collecting plate 16 to avoid the problem that the film tube 13 is detached from the collecting plate 16. As shown in FIGS. 15 and 16, the gasket 18 on one side has the function of sealing between the concentrating plate 16 and the casing-side flange 12.

553765 五、發明說明(26) ^---一~ ___一 一側之凹部5 7之功能。同樣地 有可密封集束板16與蓋罩側&amp;綠另一側之襯墊21,除了具 形成另一側之凹部5 8之功能。二5 2之間之功能外,另兼具 形成簡易的構造。 错此,可減少零件數量,並 在上述第6實施形態中, 使被處理水由膜管13之外側朝\第8圖所示、,已舉例說明過 月内側渗透過濟之外腔;4膜组 件,但是亦可如第1 0圖所示一加二边、應4外膜式Μ、、且 13之内側朝外側滲透過遽之内膜:式; 接著,根據第1 8圖至第2細…、η口丄々 y 地 币“圖祝明本發明之第7實施形 悲。 、 第7。實施形態之陶莞膜組件係在第5實施形態中裝設流 體分散益7 2,而殼體11與膜元件丨〇及蓋罩5丨則與上述第4 及第5實#施形態共通。此外,安裝固定於殼體^内之膜元 件1 0之膜官1 3之軸心1 3b (參照第3圖)係與殼體11之軸心 11 d (參照第1 8圖)為同一方向。 此外,上述各膜管1 3係僅以膜形成材形成管壁,並作 成管外桎為1至6mmp ,管壁厚度〇. 2至0. 8mm,孔徑為〇· 〇5 至10// m’長度約為3 0 0至8 0 0mm之形狀。 此外,如第1 8圖所示,源水供給口 3 1係設於兩蓋罩5 1 之外周下部,排氣口 3 3則設於兩蓋罩5 1之外周上部。 此外,在殼體1 1之外周上部,設有用以將由各膜管13 所過濾之過濾處理水予以排出之過濾水排出部6 3,另外, 在殼體1 1之外周下部,設有排水排出口 3 4。 如第1 9圖所示,上述過濾水排出部6 3,係由:設於殼553765 V. Description of the invention (26) ^ --- one ~ ___ one Function of the concave part 5 7 on one side. Similarly, there is a gasket 21 that can seal the cluster plate 16 and the cover side &amp; green on the other side, except that it has a function of forming a concave portion 58 on the other side. In addition to the functions between 2 and 5, it also has a simple structure. If this is wrong, the number of parts can be reduced, and in the sixth embodiment, the water to be treated is directed from the outer side of the membrane tube 13 to the \ Figure 8; Membrane module, but it can also be one plus two sides as shown in Figure 10, the outer membrane type M should be 4, and the inner side of 13 penetrates through the inner membrane of the 遽: type; Then, according to Figures 18 to 2 fine ..., η 口 丄 々 y local currency "Figure Zhuming Ming 7th embodiment of the present invention., 7th. The ceramic membrane module of the embodiment is provided with a fluid dispersion benefit 7 in the 5th embodiment. The casing 11 is in common with the membrane element 丨 〇 and the cover 5 丨 with the above-mentioned fourth and fifth embodiments. In addition, the axis of the membrane element 13 of the membrane element 10 installed and fixed in the casing ^ 1 3b (refer to FIG. 3) is the same direction as the axis 11 d (refer to FIG. 18) of the housing 11. In addition, each of the above-mentioned film tubes 1 to 3 is formed of a tube wall using only a film forming material, and is made into a tube. The outer diameter is 1 to 6 mmp, the thickness of the tube wall is 0.2 to 0.8 mm, and the diameter of the hole is 0.05 to 10 m. The length is about 300 to 800 mm. In addition, as shown in FIG. 18 As shown, source water supply The port 3 1 is provided at the lower part of the outer periphery of the two covers 5 1, and the exhaust port 33 is provided at the upper part of the outer periphery of the two covers 5 1. In addition, the upper part of the outer periphery of the casing 11 is provided with a tube for 13 The filtered water discharge section 6 3 that discharges the filtered filtered water, and a drain outlet 3 4 is provided at the lower part of the outer periphery of the casing 1 1. As shown in FIG. 19, the filtered water discharge section 6 described above 3, by: set in the shell

314039.ptd 第37頁 553765 五、發明說明(27) ~~ ' 體11之排出管6 4 ’形成於殼體11可連通上述排出管6 4内部 與殼體11内部之排出口 65 ;以及設於上述排出管64前端之 凸緣66所構成。上述排出管64中,藉由複數個螺栓69、螺 帽7 0接合有具備凸緣6 7之配管6 8。 此外,上述過濾水排出部63,兼具有逆洗水供給部, 係在進行逆洗時’供給用以逆洗膜管丨3之逆洗水(流體之 一例),逆洗時,上述逆洗水係通過配管68而由排出管64 内部經由排出口 6 5供給至殼體1 1内。 如第1 8圖至第2 0圖所示,在上述過濾水排出部6 3中, 没有流體分散器7 2 ’係用以使供給至殼體11内之逆洗水分 散’使之平均地流入至兩膜元件1 〇之各膜管1 3。 如第21圖、弟22圖所示,上述流體分散器72係由:可 安裝於殼體11之過濾水排出部6 3之圓板狀安裝板73 ;及垂 設於該 73中, 成流路 一端( (下端 在 其係沿 形成一 形成於 如 八殼體 7 3之中心部的管體7 4所構 複數個螺栓孔7 5 ◦另外, 上述安裝板7 3上,則形成 相連通之開口部7 7。此外 閉塞板7 8所閉塞。 體7 4之周壁部中,形成有 74之輛心80的方向,隔著 外’上述流通孔7 9係沿著 1 8 〇°對分之2處。 至第20圖所示,將上述管 再將上述安裝板7 3挾置於 安裝板 形成有 7 6,而 上端) )係由 上述管 著管體 列。此 互相呈 第18圖 11内, 成。在上述安裝板 在上述管體7 4内形 有與上述流路7 6之 ,管體74之另一端 複數個流通孔7 9, 預定之間距P並排 管體74之周方向, 體74由排出管64插 兩凸緣6 6,6 7之314039.ptd page 37 553765 V. Description of the invention (27) ~~ 'The discharge pipe 6 4 of the body 11' is formed in the housing 11 and can communicate with the above-mentioned discharge pipe 64 4 and the discharge opening 65 inside the housing 11; and A flange 66 is formed at the front end of the discharge pipe 64. A pipe 68 having a flange 67 is connected to the discharge pipe 64 by a plurality of bolts 69 and nuts 70. In addition, the filtered water discharge section 63 also has a backwash water supply section, which is used to supply the backwash water (an example of a fluid) for backwashing the membrane tube 3 during backwashing. The washing water is supplied from the inside of the discharge pipe 64 to the inside of the casing 11 through the discharge pipe 64 through a pipe 68. As shown in FIG. 18 to FIG. 20, in the above-mentioned filtered water discharge section 63, the absence of the fluid disperser 7 2 'is used to disperse the backwash water supplied into the casing 11 so that it is evenly distributed. Each membrane tube 13 flowing into the two membrane elements 10. As shown in FIG. 21 and FIG. 22, the above-mentioned fluid disperser 72 is composed of: a circular plate-shaped mounting plate 73 that can be mounted on the filtered water discharge portion 63 of the housing 11; One end of the road ((The lower end is formed along the pipe with a plurality of bolt holes 7 5 formed by a pipe body 7 4 at the center of the eight shell 7 3. In addition, the above-mentioned mounting plate 7 3 forms a communicating The openings 7 and 7. In addition, the blocking plates 7 and 8 are occluded. In the peripheral wall portion of the body 74, 74 directions of the car core 80 are formed, and the circulation holes 7 and 9 are bisected along 1 800 ° across the outside. 2. As shown in FIG. 20, the above-mentioned pipe is further placed with the mounting plate 7 3 挟 on the mounting plate to form 7 6, and the upper end)) is the pipe body row formed by the above pipe. This is shown in Figure 18 and Figure 11. A plurality of flow holes 79 are formed on the mounting plate in the pipe body 74 and the flow path 76, the other end of the pipe body 74, and a predetermined distance P is arranged side by side in the circumferential direction of the pipe body 74. The body 74 is discharged from Tube 64 is inserted into two flanges 6 6, 6 7

第38頁 553765 五、發明說明(28) ^~~ --------- 間,使螺栓6 9插通於 ^ 7q 之螺栓孔75,最後^兩凸緣66, 6 7之螺检孔81與安裝板 安裝於過渡水排出=螺帽7°检緊,#此將流體分” 肉空人# #认二 # 63。此時,上述管體74係由排出官64 μ, . L、+、Μ凡件1 〇之膜管1 3前端間的空間部82。 , η,▲瑕74之軸心8 0 (參照第1 9圖)係與殼體 1 1之軸心1 1 d (苓照笛彳〇门、也 ?| ,, 7Π 土丄、、弟18圖)垂直。此外,各流通孔79之 孑L軸心7 9 a之朝向,位也* … 、+士 上 係與各膜管1 3之軸心1 3b (參照第3圖 )垂直,並面向殼體u :匕夕卜,如第19圖所示,:緣66與安裝板73之間,係利 用襯墊8 3加以密封,而—π &amp; D π t ^ n T 而在凸緣6 7與安裝板7 3之間則是以襯 墊8 4加以密封。 以下’說明上述構成之作用。 進行一般過濾時,如第18圖之實線箭頭所示一般,係 :被處理水(被處理流體)由兩源水供給口 3丨供給至蓋罩 5 1之内側空間。藉此,使被處理水由上述内側空間通過各 $官1 3之基端開口 1 3a流入於各膜管丨3之内部流路1 3c (參 &amp;、第3圖)’再由各膜管1 3内側流出外側,並於此時進行 過濾、。如此透過膜管13之被處理水,作為過濾處理水而由 各流通孔7 9流入管體7 4内之流路7 6後,再由開口部7 7排出 至配管6 8。 當上述膜管1 3内側附著膜污染物質等時,則如下述一 般進行逆洗處理。 換言之’如第1 8圖之虛線箭頭所示一般,進行逆洗 時,係將逆洗水(流體之一例)由配管6 8内朝殼體丨“共Page 38 553765 V. Description of the invention (28) ^ ~~ ---------, so that the bolt 6 9 is inserted into the bolt hole 75 of ^ 7q, and finally ^ the two flanges 66, 6 7 The inspection hole 81 and the installation plate are installed at the transitional water discharge = the nut 7 ° is tightened tightly, #this divides the fluid "肉 空 人 # # 识 二 # 63. At this time, the above-mentioned pipe body 74 is discharged by the discharge officer 64 μ ,. The space part 82 between the front ends of the membrane tubes 13 of L, +, and M 10 is 82. The axis 8 0 of η, ▲ 74 (see FIG. 19) is connected to the axis 11 of the housing 11 d (凌 照 笛 彳 〇 门 , 也? | ,, 7Π 土 丄 ,, 弟 18 图) vertical. In addition, the direction of the L axis 7 9 a of each circulation hole 79 is also the position *… + It is perpendicular to the axis 13b (refer to FIG. 3) of each membrane tube 13 and faces the housing u: dipper, as shown in FIG. 19: between the edge 66 and the mounting plate 73, a liner is used. The gasket 8 3 is sealed, and —π &amp; D π t ^ n T is sealed between the flange 67 and the mounting plate 7 3 by a gasket 8 4. The following describes the effect of the above structure. When filtering, as shown by the solid arrows in Figure 18, the system is: the water to be treated (the fluid to be treated) is supplied by two sources of water The feed port 3 丨 is supplied to the inner space of the cover 51. As a result, the water to be treated flows into the inner flow path 1 3c of each membrane tube 3 from the inner space through the base end openings 1 3a of each of the officials 13. (Refer to &amp; Figure 3) 'Then, it flows out from the inside of each membrane tube 13 and filters at this time. The treated water that has passed through the membrane tube 13 passes through each of the flow holes 7 9 as filtered water. After flowing into the flow path 76 in the pipe body 74, it is then discharged to the piping 6 8 through the opening 7 7. When a film contamination substance or the like adheres to the inside of the film tube 13, a backwashing process is generally performed as follows. In other words, ' As shown by the dashed arrows in Figure 18, when backwashing is performed, the backwash water (an example of the fluid) is directed from the inside of the pipe 6 8 to the housing 丨 "

3l4〇39.ptd3l4〇39.ptd

553765 五、發明說明(29) 給。藉此’上述逆洗水會由配管6 8内通過流體分散器7 2之 開口部7 7而流入管體7 4内之流路7 6,再如第2 0圖所示由各 流通孔7 9流出至管體γ 4之外側。 此時’由各流通管7 9流出之逆洗水,一旦碰觸到殼體 1 1之=周面後’即順著兩膜元件1 0之膜管1 3之軸心1扑方 向=變流並如第1 8圖之虛線箭頭所示,往各膜管1 3方 =流動、。藉逆洗水可藉由流體分散器72分散並削減流 长 平句S|L入各膜官1 3。由於係在平均減輕上述逆洗水 之流力強弱並使之均一的狀態下,使逆洗水由各膜管1 3之 外側μ入至内側以進行各膜管丨3之逆洗,因此可防止膜 13因逆洗水而產生振動損傷。 、 、此^卜’由各膜管1 3之外側流入至内側之逆洗水,流入 於各膜官1 3之内部流路1 3c後,由基端開口 1 3a流出至兩蓋 罩5 1之内側空間,並由兩源水供給口 3 1排出。 在上述第7實施形態中,於進行一般過濾時,係將流 政為7 2安裝於過濾水排出部6 3,但亦可在進行一般過 二、日寸’將流體分散器7 2予以拆除,而只在進行逆洗時安裝 流體分散器7 2。 士在上述第7實施形態中,如第1 8圖所示,進行逆洗 守、由k ;慮水排出部6 3供給至殼體1 1之逆洗水之流動係藉 ΐ流體^分散器而使之均勻化,但是,亦可如第8圖所示之 $ 4貝形悲中之陶瓷膜組件一般,於源水供給口丨4裝設 机體分散器7 2,在進行一般過濾時,藉由流體分散器7 2使 由源水ί、給口 1 4供給至殼體1丨内之被處理水之流動均勻553765 V. Description of Invention (29) In this way, the above-mentioned backwash water will flow into the flow path 7 6 in the pipe body 7 4 from the inside of the pipe 6 8 through the opening 7 7 of the fluid disperser 7 2, and then through each of the circulation holes 7 as shown in FIG. 20. 9 flows out of the tube body γ 4. At this time, 'the backwash water flowing out from each of the circulation tubes 7 9 once touches the surface of the housing 11 = after the peripheral surface', then it follows the axis 1 of the membrane tube 1 3 of the two membrane elements 1 and the direction of the flap = changes As shown by the dashed arrows in FIG. 18, the flow is directed to each of the membrane tubes 13 = flow. The backwashing water can be dispersed by the fluid disperser 72 and the flow length can be reduced. Since the flow strength of the above backwash water is lightened and uniformed on average, the backwash water is μ-introduced from the outside of each membrane tube 13 to the inside to perform the backwash of each membrane tube 3, so The membrane 13 is prevented from being damaged by vibration due to backwash water. The backwash water flowing from the outside of each membrane tube 13 to the inside flows into the internal flow path 1 3c of each membrane official 13 and flows out from the base opening 1 3a to the two covers 5 1 The inner space is discharged from the two source water supply ports 31. In the seventh embodiment described above, the fluid filter 72 is installed in the filtered water discharge section 63 during general filtration. However, the fluid disperser 72 can also be removed during normal filtration. The fluid disperser 72 is installed only during backwashing. In the seventh embodiment described above, as shown in FIG. 18, the backwashing is performed by k; the water washing discharge section 63 supplies the backwashing water to the casing 11. The flow of the backwashing water is a diffuser. It can be made uniform, but it can also be a ceramic membrane module in the $ 4 shell shape as shown in Figure 8. A body diffuser 7 2 is installed at the source water supply port 4 and it is used for general filtration. The flow of the water to be treated supplied from the source water 1 and the supply port 1 4 to the housing 1 through the fluid disperser 7 2 is uniform.

第40頁 553765 五、發明說明(30) 化。 在上述第7實施形態中,如第2 2圖所示,係將流體分 散器72之流通孔79之間距全部統一設定為一個種類之間距 旦亦可^乍成數種種類之間距。例如’第8實施形態係如 第23圖所示,在管體74之大致上半部之範圍,將流通孔79 之間距設定為P,而在將大致下半部之範圍,將流通孔7 9 之間距設定為P1,藉由將間距P 1設定成比間距P大(P&lt; P1 ),可使由各流通孔7 9所流出之逆洗水之流速呈大致一 定。此外,亦可藉由在愈往下位處增大上述流通孔7 9之間 距,或藉由改變各流通孔7 9之孔徑’使各流通孔7 9所流出 之逆洗水之流速呈大致一定。 此外,在第7實施形態中,如第1 8圖所示,流體分散 器72之管體了4下端部係到達殼體1 1内之底部附近’但作為 第9實施形態’亦可如第2 4圖所示一般’縮短管體7 4之長 度,使管體了4之下端部位於殼體1 1内之中央部或上部。 上述第7炱第9實施形態中,係在安裝板7 3上裝設一支 管體74,但亦 &lt; 安裝複數支管體74。 在上述第7實施形態中,如第1 8圖所示’過濾水排出 部6 3兼備有進行逆洗時可供給用以逆洗各膜管1 3之逆洗水 之逆洗水供給部’而在殼體1 1中’則不同於上述過濾水排 出部6 3,設有用以供給逆洗水之專用逆洗水供給部’而在 該專用逆洗水供給部中亦可設置流體分散器7 2。此時’上 述專用逆洗水供給部係與上述過濾、水排出部6 3具相同構 成。此外,亦$使用過濾處理水(經過渡處理後之水)作P.40 553765 V. Explanation of the invention (30). In the seventh embodiment described above, as shown in Fig. 22, the distance between the flow holes 79 of the fluid disperser 72 is uniformly set to the distance of one type, and the distance of several types may be changed. For example, as shown in FIG. 23, in the eighth embodiment, the distance between the flow holes 79 is set to P in the range of approximately the upper half of the tube body 74, and the flow holes 7 are set in the range of approximately the lower half. The interval between 9 is set to P1. By setting the interval P1 to be larger than the interval P (P &lt; P1), the flow velocity of the backwash water flowing out of each of the circulation holes 7-9 can be made substantially constant. In addition, the flow rate of the backwash water flowing out of each of the circulation holes 79 can be made substantially constant by increasing the distance between the above-mentioned flow holes 79 or lower, or by changing the aperture of each of the circulation holes 79. . In addition, in the seventh embodiment, as shown in FIG. 18, the lower end of the tube body of the fluid disperser 72 reaches the vicinity of the bottom inside the casing 11 'but as the ninth embodiment', it can also be used as in the ninth embodiment. As shown in FIG. 24, the general length of the pipe body 74 is shortened, so that the lower end of the pipe body 4 is located at the center or upper part of the casing 11. In the seventh to ninth embodiments, one pipe body 74 is mounted on the mounting plate 73, but a plurality of pipe bodies 74 are also mounted. In the seventh embodiment described above, as shown in FIG. 18, 'the filtered water discharge section 63 has a backwash water supply section that can supply backwash water for backwashing each membrane tube 13 when performing backwashing' On the other hand, the housing 11 is different from the filtered water discharge section 63 described above, and is provided with a dedicated backwash water supply section for supplying backwash water, and a fluid diffuser may be provided in the dedicated backwash water supply section. 7 2. In this case, the above-mentioned dedicated backwash water supply unit has the same structure as the filtration and water discharge unit 63 described above. In addition, filtered water (water after transition treatment) is also used.

314039.ptd 第41頁 553765 五、發明說明(31) 為逆洗水。 在上述第7實施形態中,如第1 8圖所示,係將過濾水 排出部6 3設置於殼體1 1之外周上部,但設在外周下部,或 是外周上部與外周下部之間亦無妨。此外,將過濾水排出 部6 3設於殼體外周下部時,流體分散器7 2之管體74,係沿 著殼體1 1之直徑方向呈上下方向之直立狀。此外,將過濾 水排出部6 3設於外周上部與外周下部之間時,上述管體則 沿著殼體1 1之直徑方向形成面向水平方向或是傾斜方向之 狀態。 接著,根據第2 5圖至第2 9圖說明本發明之第1 0實施形 態。 如第2 5圖所示,第1 0實施形態,係在第4實施形態的 膜元件1 0中裝設保護框9 2,9 4與引導構件9 3,其殼體1 1與 膜元件1 0及蓋罩5 1係與上述第4實施形態共通。此外,源 水供給口 1 4與濃縮水排出口 1 5係分別安裝於殼體1 1中。另 外,在上述蓋罩5 1之外周上部另設有過濾水排出口 2 0,而 蓋罩5 1之外周下部則設有用以排出蓋罩5 1内之排水的排水 的排出口 5 3。 此外,膜元件1 0之各膜管1 3,係僅以膜形成材形成管 壁,並作成管外徑為1至6mmp ,管壁厚度0.2至0.8mm,孔 徑為0.0 5至10// m,長度約為30 0至800m m之形狀。 此外,如第2 6圖、第2 7圖所示,在上述膜元件1 0中設 有:用以保護由複數個膜管1 3所形成之膜管群9 1之前端部 之前端保護框9 2 ;用以將上述膜元件1 0引導至進出於膜元314039.ptd Page 41 553765 V. Description of the invention (31) is backwash water. In the seventh embodiment, as shown in FIG. 18, the filtered water discharge portion 63 is provided on the upper outer periphery of the casing 11, but it is also provided on the lower outer periphery or between the upper outer periphery and the lower outer periphery. Anyway. In addition, when the filtered water discharge portion 63 is provided at the lower portion of the outer periphery of the casing, the pipe body 74 of the fluid diffuser 72 is upright in the vertical direction along the diameter direction of the casing 11. In addition, when the filtered water discharge portion 63 is provided between the upper peripheral portion and the lower peripheral portion, the pipe body faces the horizontal direction or the inclined direction along the diameter direction of the casing 11. Next, a tenth embodiment of the present invention will be described with reference to FIGS. 25 to 29. FIG. As shown in FIGS. 25 and 10, the tenth embodiment is provided with a protective frame 9 2, 9 4 and a guide member 9 3 in a membrane element 10 of the fourth embodiment, and a casing 11 and a membrane element 1 thereof. 0 and the cover 5 1 are common to the fourth embodiment. The source water supply port 14 and the concentrated water discharge port 15 are respectively installed in the casing 11. In addition, a filtered water discharge port 20 is provided at the upper peripheral portion of the cover 51, and a drain outlet 53 is provided at the lower peripheral portion of the cover 51 to drain water from the inside of the cover 51. In addition, each membrane tube 1 3 of the membrane element 10 is formed of a tube wall only with a film forming material, and has an outer diameter of 1 to 6 mmp, a thickness of the wall of 0.2 to 0.8 mm, and a pore diameter of 0.0 5 to 10 // m. , The shape is about 300 to 800m in length. In addition, as shown in FIGS. 26 and 27, the above-mentioned membrane element 10 is provided with a protection frame for protecting the front end and the front end of the film tube group 9 formed by a plurality of film tubes 13. 9 2; used to guide the above membrane element 10 to the membrane element

314039.ptd 第42頁 553765 五、發明說明(32) _ '^^^-_ 件插入口 1 1 a之方向Α,β (參照第2 9圖)之 27圖中為4個)引導構件93。 旻數個(在第 換曰之,上述前端保護框9 2係形成包圍膜 a 端部之外側周圍的環形狀,而前端保護框、^ f /則 各膜管1 3之前端更突出於前方。 別端,係比 此外,上述各引導構件93係形成圓棒 ^ 1 3呈平行配置,並位於膜管群9 i之 」且與膜官 合材層η安裝固定於集束板16上。而上述;端=上述黏 設於各引導構件93之前端部,並由 =護框92係 撐。 Ή ¥構件93所支 此外位於各引導構件9 3之軸方向的中門 間保護框94,用以保護膜管群91之軸方向H,設有中 間保護框94係形成包圍位於膜管群 ^二間部°該中 側周圍的環形狀。 &lt; 釉方向之中間部外 被CM此外,在上述兩保護框92,94之内周面盥配署协磁爲 \91之最外周側之膜管13之間形成有極小之間 ;,吕 保護框92,94兼具有對於配置於上述 &amp; &gt;、,上u兩 之膜管13之防振作用。 群91之最外周側 以下’說明上述構成之作用。 田上述膜元件1 0老舊而需更換新, 圖所示之各固定螺检22、螺、帽23拆♦士將=25 凸緣12取下。然後,由膜元件插人〇 ^將將膜皿罩由殼體側 至殼體11之外側。此時,如第29圖所示,引、牛1 0拔出 殼體11之内周面相接觸而產生滑動 j件93將與 稽此j將Μ元件1 〇導314039.ptd Page 42 553765 V. Description of the invention (32) _ '^^^ -_ The direction A, β of the insertion opening 1 1 a (see Figure 2 9) 4 in 27) guide member 93 .旻 Several (in other words, the above-mentioned front protective frame 9 2 is formed in a ring shape surrounding the outer side of the end of the film a, and the front protective frame ^ f / is more protruded at the front end of each membrane tube 1 3 Other than that, in addition, each of the above-mentioned guide members 93 is formed as a round rod ^ 13 in a parallel arrangement, and is located in the membrane tube group 9i "and is fixed to the cluster plate 16 with the membrane official composite material layer η. The above; end = the above is glued to the front end of each guide member 93, and is supported by the = protector frame 92. 构件 ¥ Middle 93 is also supported by the middle door protection frame 94 located in the axial direction of each guide member 93, for The protective film tube group 91 is provided with an intermediate protective frame 94 in the axial direction H to form a ring shape surrounding the middle side of the film tube group ^ two intermediate portions. &Lt; The middle portion of the glaze direction is covered by CM. The inner peripheral surfaces of the two protective frames 92, 94 are formed with a small gap between the membrane tubes 13 on the outermost side of \ 91, and the protective frames 92, 94 also have the same configuration as the & &gt;, the anti-vibration effect of the upper and lower film tubes 13. The outermost side of the group 91 or lower 'explains the effect of the above configuration The above-mentioned membrane element 10 is old and needs to be replaced with new ones. Each fixed screw inspection 22, screw, and cap 23 shown in the figure is removed. Remove the flange = 25. Then, insert the membrane element. ^ Move the membrane dish cover from the housing side to the outer side of the housing 11. At this time, as shown in FIG. 29, the lead and cattle 10 are pulled out of the inner peripheral surface of the housing 11 and come into contact with each other. j will guide the M element 1

314039.ptd 第43頁314039.ptd Page 43

/OD 五、發明說明(33) 向拉出方向A’因此可順利 — 之後,將新的膜元件丨 出膘元件1 0。 殼體11内部。此時,如第28圖^述膜元件插入口 lla插入 管群91之前端部即將接觸到^所示,萬一,膜元件i 〇之膜 緣1 2或是殼體1丨之内周面時,、凡件插入口 1 1 a之殼體側凸 上述膜管群9 1之前端部,因,也可藉由前端保護框92保護 體側凸緣1 2或是殼體丨丨*此’上述前端保護框92會與殼 管群91之前端部接觸到浐二::相接觸。•此,可防止膜 而使膜管1 3產生損壞之^形。,緣1 2或是殼體11之内周面 間保==上;^管群91之轴方向之中間部係由中 方向之中門邱技j,因此,亦可防止位於膜管群91之長邊 使Μ * 1。3 °卩接觸到殼體側凸緣1 2或是殼體11之内周面而 便胰官13產生損壞之情形。 用此外’如第2 9圖所示,藉由引導構件9 3與殼體1 1之内 °相接觸並產生滑動,可使膜元件1 0導向插入方向Β, 此可順利地插入膜元件1 0。 一 如此’將新的膜元件1 0插入殼體1 1内後,如第2 5圖所 7 ’安裝各固定螺栓2 2、螺帽2 3,再將蓋罩5 1連接在殼體 i凸緣1 2。藉此,而以水平方式將膜元件丨〇安裝固定於殼 體11内。 業 如上述一般,由於將膜元件1 〇取出插入於殼體11之作 ^執行容易’因此,例如在膜元件1 〇之更換等維修上可容 易地進行。 此外’如第2 5圖所示,在被處理水由源水供給口 1 4供/ OD V. Description of the invention (33) The pulling direction A ′ can be smoothed-after that, the new membrane element 丨 out of the element 10. Inside the housing 11. At this time, as shown in FIG. 28, the end of the membrane element insertion port 11a before being inserted into the tube group 91 will be in contact with ^, in case, the membrane edge 12 of the membrane element i 〇 or the inner peripheral surface of the housing 1 丨At this time, the housing side of each of the inserting openings 1 1 a protrudes from the front end of the above-mentioned film tube group 9 1. Therefore, the front side protective frame 92 can also be used to protect the body-side flange 12 or the housing. 'The above-mentioned front end protection frame 92 will come into contact with the front end of the shell and tube group 91 at the second end ::. • This prevents the membrane from damaging the membrane tube 13. The edge 1 2 or the inner peripheral surface of the housing 11 == up; ^ The middle part of the tube group 91 in the axial direction is from the middle direction to the middle gate Qiu Ji j, so it can also prevent the film tube group 91 from being located The long side makes M * 1.3 ° contact the housing-side flange 12 or the inner peripheral surface of the housing 11 and the pancreas 13 may be damaged. In addition, as shown in FIG. 2 to FIG. 9, the guide member 93 is brought into contact with the inside of the housing 11 and slides, so that the membrane element 10 can be guided in the insertion direction B, and the membrane element 1 can be smoothly inserted. 0. In this way, after inserting a new membrane element 10 into the housing 1 1, install each fixing bolt 2 2 and a nut 2 3 as shown in FIG. 2 5, and then connect the cover 5 1 to the housing i. Margin 1 2. Thereby, the membrane element 10 is mounted and fixed in the casing 11 in a horizontal manner. As described above, the operation of removing and inserting the membrane element 10 into the casing 11 is easy. Therefore, for example, maintenance of the membrane element 10 can be easily performed. In addition, as shown in FIG. 25, the water to be treated is supplied from the source water supply port 1 4

第44頁 553765 五、發明說明(34) 給至殼體1 1之供水空間1 1 b内之際,由於沿著殼體11之内 周面將產生被處理水之強力水流,而該強力水流會使配置 於膜管群9 1之最外周側之膜管1 3變得十分容易振動。然 而,配置於上述膜管群9 1之最外周側之膜管1 3,即使產生 振動,由於與前端保護框9 2之内周面或中間保護框9 4之内 周面相接觸之故,因而得以減輕振動。因此可避免上述配 置於最外周側之膜管1 3受到因振動所產生之反覆應力而導 致折損之情形。 上述第1 〇實施形態中,如第2 5圖所示,已列舉使被處 理水由膜管1 3外側滲透至内側以進行過濾之外膜式膜組 件,而在第1 1實施形態中,則如第3 0圖所示,亦可採用使 被處理水由膜管1 3内側滲透至外側以進行過濾之内膜式膜 組件。 換言之,上述第1 1實施形態係在第5實施形態中的膜 元件10中裝設保護框92,94與引導構件93,而殼體1 1與膜 元件1 0及蓋罩5 1則與上述第5實施形態共通。此外,源水 供給口 3 1係設在兩蓋罩5 1之外周下部,而過濾水排出口 3 0 則設於殼體1 1之外周上部,排水排出口 3 4係設於殼體1 1之 外周下部,又,排氣口係設於兩蓋罩5 1之外周上部。 藉此,進行逆洗時,係由過濾水排出口 3 0供給逆洗水 並由兩源水供給口 3 1排出。藉此,上述逆洗水由各膜管13 之外側滲透内側,以進行各膜管1 3之逆洗。此時,與上述 第1 0實施形態相同,配置於膜管群9 1之最外周側之膜管 1 3,即使產生振動,也會由於與前端保護框9 2之内周面或Page 44 553765 V. Description of the invention (34) When the water supply space 1 1 b to the casing 11 is supplied, a strong current of treated water will be generated along the inner peripheral surface of the casing 11, and the powerful water flow The membrane tube 1 3 arranged on the outermost peripheral side of the membrane tube group 91 can become very easy to vibrate. However, even if the membrane tube 13 arranged on the outermost peripheral side of the membrane tube group 91 is in contact with the inner peripheral surface of the front protective frame 92 or the inner protective surface of the middle protective frame 94, even if vibration occurs, Vibration is reduced. Therefore, it is possible to avoid the situation where the film tube 13 disposed on the outermost peripheral side is damaged due to the repeated stress caused by vibration. In the above-mentioned 10th embodiment, as shown in FIG. 25, the treated membrane is enumerated from the outside of the membrane tube 13 to the inside to filter the outer membrane membrane module. In the 11th embodiment, Then, as shown in FIG. 30, an inner membrane type membrane module that allows the water to be treated to penetrate from the inside of the membrane tube 13 to the outside for filtering can also be used. In other words, in the above-mentioned 11th embodiment, the protective frame 92, 94 and the guide member 93 are installed in the membrane element 10 in the fifth embodiment, and the housing 11 and the membrane element 10 and the cover 51 are the same as those described above. The fifth embodiment is common. In addition, the source water supply port 31 is provided at the lower part of the outer periphery of the two covers 51, while the filtered water discharge port 30 is provided at the upper part of the outer periphery of the casing 11 and the drainage discharge port 3 4 is provided at the casing 1 1 The lower outer periphery and the exhaust port are provided at the upper outer periphery of the two covers 51. Thus, when backwashing is performed, the backwash water is supplied from the filtered water discharge port 30 and is discharged from the two source water supply ports 31. Thereby, the above-mentioned backwash water penetrates from the outer side of each membrane tube 13 to the inside to perform the backwash of each membrane tube 13. At this time, as in the above-mentioned 10th embodiment, the membrane tube 1 3 disposed on the outermost peripheral side of the membrane tube group 91 is not connected with the inner peripheral surface of the front end protection frame 92 or even if vibration occurs.

314039.ptd 第45頁 553765 五、發明說明(35) 中間保護框9 4之内周面相接觸之故’而減輕振動。如此一 來,可減輕配置於膜管群9 1之最外周側之膜管1 3之振動’ 因此可避免上述配置於最外周側之膜管1 3受到因振動所產 生之反覆應力而導致折損之情形。 於上述第1 0及第1 1實施形態中’如第2 7圖所示’於膜 元件1 0中設有4個引導構件9 3,但並不限定於4個’可視膜 元件1 0之尺寸大小等增減其數量。 於上述第1 0及第11實施形態中’如第2 6圖所示’在各 引導構件9 3之軸方向中的中間部,設有一個中間保護框 9 4,但亦可視膜元件丨〇之尺寸大小等,安裝複數個上述中 間保護框9 4。 此外,在第1 1實施形態中,可使用過濾處理水(經過 據處理後之水)以作為逆洗水。 接著,根據第3 1圖說明本發明之第1 2實施形態。 第1 2實施形態之陶瓷膜組件,係具備先前所說明之第6至 第1 1實施形態。換言之,與第6實施形態相同’係將襯塾 18,21黏接於集束板16之表裡雨面16a,16b,以形成凹部 57,58,在藉由填充於該等凹部57,58之中的黏合劑59, 使膜管1 3黏接於集束板1 6上。 、 此外,與第7至第9實施形態相同’於殼體11中没有? 體分散器72,另夕卜,與第1 0及第11實施形悲相@ ’於膜兀 件1 〇中,則設有保護框92,94及引導構件93 说別舉水作為流體之 此外,在上述各實施形態中,係夕』 例’但亦可使用水以外之液體或是氣體314039.ptd Page 45 553765 V. Description of the invention (35) The inner peripheral surface of the middle protective frame 9 4 is in contact with each other 'to reduce vibration. In this way, the vibration of the membrane tubes 13 arranged on the outermost peripheral side of the membrane tube group 9 1 can be reduced. Therefore, the membrane tubes 13 arranged on the outermost peripheral side can be prevented from being damaged due to the repeated stress caused by vibration. Situation. In the tenth and eleventh embodiments described above, four guide members 9 3 are provided in the membrane element 10 'as shown in Fig. 27', but it is not limited to four of the visible membrane elements 10 Increase or decrease the number of dimensions. In the above-mentioned 10th and 11th embodiments, as shown in FIG. 26, an intermediate protective frame 94 is provided at the middle portion in the axial direction of each guide member 93, but the membrane element can also be seen. Size, etc., a plurality of the above-mentioned intermediate protective frames 9 4 are installed. In addition, in the eleventh embodiment, the filtered water (the water after the data processing) can be used as the backwash water. Next, a twelfth embodiment of the present invention will be described with reference to FIG. 31. The ceramic membrane module according to the twelfth embodiment includes the sixth to eleventh embodiments described above. In other words, the same as in the sixth embodiment, 'the liners 18 and 21 are bonded to the rain surfaces 16a and 16b of the front and back surfaces of the cluster plate 16 to form the recesses 57 and 58. In the adhesive 59, the film tube 13 is adhered to the bundle plate 16. In addition, it is the same as the seventh to ninth embodiments. The body diffuser 72, in addition to the tenth and eleventh embodiments @ 'in the membrane element 10, is provided with a protective frame 92, 94 and a guide member 93 said do not use water as a fluid. In the above embodiments, it is "example", but liquids or gases other than water can also be used.

553765553765

314039.ptd 第47頁 553765 圖式簡單說明 [圖式簡單說明] 第1圖為本發明第1實施形態之陶瓷膜組件之斜視圖。 第2圖為該陶瓷膜組件之剖視圖。 第3圖為該陶瓷膜組件之膜管與集束板之集束固定部 之剖視圖。 第4圖為沿第3圖中箭頭X-X之剖視圖。 第5圖為本發明第2實施形態之陶瓷膜組件之斜視圖。 第6圖為該陶瓷膜組件之剖視圖。 第7圖為本發明第3實施形態之陶瓷膜組件之剖視圖。 第8圖為本發明第4實施形態之陶瓷膜組件之剖視圖。 第9圖為該陶瓷膜組件之斜視圖。 第1 0圖為本發明第5實施形態之陶瓷膜組件之剖視 圖。 第1 1圖為該陶瓷膜組件之斜視圖。 第1 2圖為陶瓷膜組件之膜管之強度與透水性測定結果 之說明圖。 第1 3圖為本發明第6實施形態之陶瓷膜組件之膜元件 之剖視圖。 第1 4圖為沿第1 3圖中箭頭X-X之剖視圖。 第1 5圖為該陶瓷膜組件之殼體側凸緣及蓋罩側凸緣與 集束板之連結部分之放大剖視圖。 第1 6圖為該陶瓷膜組件之膜組件之製造方法之說明 圖,係顯示在集束板上黏接襯塾之狀態。 第1 7圖為該陶瓷膜組件之膜組件之製造方法之說明314039.ptd Page 47 553765 Brief description of drawings [Simplified description of drawings] Fig. 1 is a perspective view of a ceramic membrane module according to the first embodiment of the present invention. Fig. 2 is a sectional view of the ceramic membrane module. Fig. 3 is a cross-sectional view of a bundle fixing portion of a membrane tube and a bundle plate of the ceramic membrane module. Fig. 4 is a sectional view taken along the arrow X-X in Fig. 3. Fig. 5 is a perspective view of a ceramic membrane module according to a second embodiment of the present invention. Fig. 6 is a sectional view of the ceramic membrane module. Fig. 7 is a sectional view of a ceramic membrane module according to a third embodiment of the present invention. Fig. 8 is a sectional view of a ceramic membrane module according to a fourth embodiment of the present invention. FIG. 9 is a perspective view of the ceramic membrane module. Fig. 10 is a sectional view of a ceramic membrane module according to a fifth embodiment of the present invention. Figure 11 is a perspective view of the ceramic membrane module. Fig. 12 is an explanatory diagram of the measurement results of the strength and water permeability of the membrane tube of the ceramic membrane module. Fig. 13 is a sectional view of a membrane element of a ceramic membrane module according to a sixth embodiment of the present invention. FIG. 14 is a sectional view taken along the arrow X-X in FIG. 13. FIG. 15 is an enlarged cross-sectional view of a connection portion between the casing-side flange and the cover-side flange of the ceramic membrane module and the cluster plate. Fig. 16 is an explanatory diagram of a method of manufacturing a membrane module of the ceramic membrane module, which shows a state in which a liner is bonded to a cluster plate. Fig. 17 is a description of a method for manufacturing a membrane module of the ceramic membrane module

314039.ptd 第48頁 553765 圖式簡單說明 圖,係顯示在集束板上插通膜管之基端側之狀態。 第1 8圖為本發明第7實施形態之陶瓷膜組件之剖視 圖。 第1 9圖為該陶瓷膜組件之液體分散器之安裝部分之剖 視圖。 第2 0圖為沿第18圖中箭頭X-X之剖視圖。 第2 1圖為該陶瓷膜組件之液體分散器之斜視圖。 第2 2圖為該陶瓷膜組件之液體分散器圖。 第2 3圖為本發明第8實施形態之陶瓷膜組件之液體分 散器圖。 第2 4圖為本發明第9實施形態之陶瓷膜組件之液體分 散器圖。 第2 5圖為本發明第1 0實施形態之陶瓷膜組件之剖視 圖。 第2 6圖為該陶瓷膜組件之膜組件之剖視圖。 第27圖為沿第26圖中箭頭X-X之剖視圖。 第2 8圖係由膜組件插入口將該陶瓷膜組件之膜組件插 入至殼體内時之說明圖。 第2 9圖係由殼體取出或是插入該陶瓷膜組件之膜組件 時之說明圖。 第3 0圖為本發明第1 1實施形態之陶瓷膜組件之剖視 圖。 第3 1圖為本發明第1 2實施形態之陶瓷膜組件之剖視 圖。314039.ptd Page 48 553765 Brief description of the diagram The diagram shows the state where the base end side of the membrane tube is inserted on the cluster board. Fig. 18 is a sectional view of a ceramic membrane module according to a seventh embodiment of the present invention. Fig. 19 is a sectional view of a mounting portion of the liquid diffuser of the ceramic membrane module. Fig. 20 is a sectional view taken along the arrow X-X in Fig. 18. Figure 21 is a perspective view of the liquid diffuser of the ceramic membrane module. Figure 22 shows the liquid diffuser of the ceramic membrane module. Fig. 23 is a diagram of a liquid diffuser of a ceramic membrane module according to an eighth embodiment of the present invention. Fig. 24 is a diagram showing a liquid diffuser of a ceramic membrane module according to a ninth embodiment of the present invention. Fig. 25 is a sectional view of a ceramic membrane module according to a tenth embodiment of the present invention. Fig. 26 is a sectional view of a membrane module of the ceramic membrane module. Fig. 27 is a sectional view taken along the arrow X-X in Fig. 26. Fig. 28 is an explanatory diagram when the membrane module of the ceramic membrane module is inserted into the casing through the membrane module insertion port. Fig. 29 is an explanatory diagram when the ceramic membrane module is removed from the housing or inserted into the membrane module. Fig. 30 is a sectional view of a ceramic membrane module according to the eleventh embodiment of the present invention. Fig. 31 is a sectional view of a ceramic membrane module according to a 12th embodiment of the present invention.

314039.ptd 第49頁 553765 圖式簡單說明 第3 2圖為習知之膜組件之圖。314039.ptd Page 49 553765 Brief description of the drawings Figures 3 and 2 are diagrams of conventional membrane modules.

卜 11 殼 體 2 中 空 線 膜 3、 51 蓋 罩 10 膜 元 件 11a 膜 元 件 插 入 Π lib 供 水 空 間 12 殼 體 側 凸 線 13 膜 管 13a 基 端 開 α 13c 内 部 流 路 14、 3卜 44 源 水 供 給 Ό 15 濃 縮 水 排 出口 16 集 束 板 16a 表 面 16b 背 面 17 黏 接 材 層 18、 21 襯 墊 19 集 水 部 20&gt; 30^ 43 過 濾 水 排 出 σ 22 固 定 螺 栓 23 螺 帽 32 配 水 部 41 凸 緣 42 逆 洗 水 排 出口 47 配 管 52 蓋 罩 側 凸 緣 53 排 水 排 出 V 55 貫 穿 孔 56 螺 栓 孔 57&gt; 58 凹 部 59 黏 合 劑 60 孔 部 63 過 濾 水 排 出 部 64 排 出 管 65 排 出 α 6 6 ^ 67 凸 緣 68 配 管 69 螺 栓 70 螺 帽 72 流 體 分 散 器 73 安 裝 板 74 管 體 75〜 81 螺 栓 孔 76 流 路 314039.ptd 第50頁 55376511 Housing 2 Hollow wire membrane 3, 51 Cover 10 Membrane element 11a Membrane element insertion Π lib Water supply space 12 Shell-side convex wire 13 Membrane tube 13a Base end opening α 13c Internal flow path 14, 3 Bu 44 Source water supply Ό 15 Concentrated water discharge port 16 Bundle plate 16a Surface 16b Back side 17 Adhesive material layer 18, 21 Pad 19 Water collecting section 20> 30 ^ 43 Filter water discharge σ 22 Fixing bolt 23 Nut 32 Water distribution section 41 Flange 42 Reverse Washing water outlet 47 Piping 52 Cover side flange 53 Drain drainage V 55 Through hole 56 Bolt hole 57 &gt; 58 Recess 59 Adhesive 60 Hole 63 Filter water discharge 64 Discharge pipe 65 Discharge α 6 6 ^ 67 Flange 68 Piping 69 Bolt 70 Nut 72 Fluid diffuser 73 Mounting plate 74 Tube body 75 to 81 Bolt hole 76 Flow path 314039.ptd Page 50 553765

314039.ptd 第51頁314039.ptd Page 51

Claims (1)

553765 六、申請專利範圍 1. 一種陶瓷膜組件,其特徵為:以平行方式配置前端閉 塞之細直管狀之陶瓷製之複數個膜管,並藉由集束板 以不滲水方式將貫通集束板之各膜管之基端予以集束 固定以構成膜元件,再將該膜元件由膜元件插入口填 充於殼體内,並以不滲水方式將集束板配置於膜元件 插入口,並於上述殼體設置有:在上述集束板之一側 與各膜管外側相連通之第1供排部;而在上述集束板之 另一侧與各膜管之基端開口相連通之第2供排部。 2. 如申請專利第1項之陶瓷膜組件,其中,係在殼體中, 裝設用以覆蓋插通於集束板之各膜管之基端開口側的 蓋罩,在裝設於膜元件插入口之外周緣之殼體側凸緣 以及裝設於上述蓋罩之開口端之外周緣之蓋罩側凸緣 之間,挾持上述集束板之外周部之狀態下,藉由連結 上述殼體側凸緣與蓋罩側凸緣,使膜元件固定於殼體 内,並於上述集束板之表裡兩面,黏接用以密封集束 板與殼體側凸緣之間之環狀之一側的襯墊,以及用以 密封集束板與蓋罩側凸緣之間之環狀之另一側的襯 墊,並且在由上述一側之襯墊内周面與集束板表裡之 其中一面所形成之一側的凹部,及另一側之襯墊之内 周面與集束板之表裡之另一面所形成之另一側的凹部 間,填充用以將上述各膜管黏接於集束板上之黏合 劑。 3. 如申請專利範圍第1項之陶瓷膜組件,其中,係在殼體 側設置流體分散器,俾使供給於殼體内之流體分散,553765 6. Scope of patent application 1. A ceramic membrane module, characterized in that a plurality of membrane tubes made of thin straight tubular ceramics with closed front ends are arranged in a parallel manner, and a bundle plate is used to pass through the bundle plate in a watertight manner. The base end of each membrane tube is bundled and fixed to form a membrane element, and then the membrane element is filled into the housing from the membrane element insertion opening, and the bundle plate is arranged at the membrane element insertion opening in a watertight manner, and is placed in the above casing. A first supply and discharge portion communicating with the outside of each membrane tube on one side of the bundle plate and a second supply and discharge portion communicating with the base end opening of each film tube on the other side of the bundle plate are provided. 2. The ceramic membrane module according to item 1 of the application, wherein the ceramic membrane module is housed in a housing, and a cover for covering the open end of the base end of each membrane tube inserted in the cluster plate is installed in the membrane element. The housing-side flange at the outer periphery of the insertion port and the cover-side flange installed at the outer periphery of the opening end of the cover, holding the outer periphery of the cluster plate, and connecting the housing The side flange and the cover side flange are used to fix the membrane element in the casing, and are adhered to seal one side of the ring between the cluster plate and the casing side flange on the two surfaces of the above-mentioned cluster plate. Gasket on the other side of the ring between the cluster plate and the flange on the cover side. Form the concave portion on one side, and the inner peripheral surface of the gasket on the other side and the concave portion on the other side formed on the other side of the front and back surfaces of the cluster plate, and fill the above-mentioned film tubes to the cluster plate. On the adhesive. 3. For example, the ceramic membrane module of the scope of application for a patent, wherein a fluid diffuser is provided on the side of the casing to disperse the fluid supplied into the casing, 314039.ptd 第52頁 553765 六、申請專利範圍 以平均流入至上述各膜管。 4. 如申請專利範圍第3項之陶瓷膜組件,其中,流體分散 器。係由可安裝於殼體側之安裝板;及裝設於該安裝 板上並突入至殼體内之管體所構成,而在上述管體内 形成流路,並有複數個流通孔沿著管體軸心方向排列 形成於管體周壁部,上述各流通孔之朝向,係與膜管 之軸心方向垂直,且面向殼體之内周面。 5. 如申請專利範圍第1項之陶瓷膜組件,其中,係將用以 覆蓋殼體内之膜元件之各膜管之基端開口側的蓋罩, 以可自由裝卸之方式安裝在膜元件插入口 ,而將用以 保護由複數個膜管所形成之膜管群前端部的前端保護 框安裝在上述膜元件上。 6. 如申請專利範圍第5項之陶瓷膜組件,其中,係在集束 板上,安裝可將膜元件引導至可取出插入於膜元件插 入口之方向的複數個引導構件,前端保護框則形成包 圍膜管群前端部之外側周圍的環狀,並由上述引導構 件所支撐,上述引導構件係與膜管平行配置,並位於 膜管群之外側周圍。 7. 如申請專利範圍第1項至第6項中任一項之陶瓷膜組件 ,其中,膜管係僅以膜形成材形成管壁,並作成管外 徑為1至6mπιφ,管壁厚度為0. 2至0. 8mm之形狀。 8. —種陶瓷膜組件之運轉方法,係申請專利範圍第1項所 記載之陶瓷膜組件之運轉方法,在進行一般運轉時, 使流體由第1供排部供給至殼體内,同時由第2供排部314039.ptd Page 52 553765 6. Scope of patent application The average flow into the above membrane tubes. 4. The ceramic membrane module according to item 3 of the patent application scope, wherein the fluid diffuser. It consists of a mounting plate that can be installed on the housing side; and a pipe body that is installed on the mounting plate and protrudes into the housing, and a flow path is formed in the above-mentioned pipe body, and there are a plurality of flow holes along the The axial direction of the tube body is aligned and formed on the peripheral wall of the tube body. The orientation of each of the flow holes is perpendicular to the axial direction of the membrane tube and faces the inner peripheral surface of the casing. 5. For example, the ceramic membrane module of the scope of application for a patent, wherein the cover for covering the open end of the base end of each membrane tube of the membrane element in the casing is installed on the membrane element in a freely removable manner The front end protection frame for protecting the front end portion of the membrane tube group formed by the plurality of membrane tubes is inserted into the insertion port, and is mounted on the membrane element. 6. For example, the ceramic membrane module of the scope of application for patent No. 5 is attached to the cluster board, and a plurality of guide members can be installed to guide the membrane element to the direction where the membrane element can be inserted and inserted, and the front protective frame is formed. A ring shape surrounding the outer side of the front end portion of the membrane tube group is supported by the guide member. The guide member is arranged in parallel with the membrane tube and is located around the outer side of the membrane tube group. 7. For the ceramic membrane module according to any one of the items 1 to 6 of the scope of application for a patent, wherein the membrane tube system only uses a film forming material to form a tube wall, and the outer diameter of the tube is 1 to 6 mπφ, the thickness of the tube wall is The shape of 0.2 to 0.8 mm. 8. — A ceramic membrane module operating method refers to the ceramic membrane module operating method described in item 1 of the scope of patent application. During normal operation, the fluid is supplied from the first supply and discharge unit to the housing, and at the same time, Second supply and discharge department 314039.ptd 第53頁 553765 六、申請專利範圍 排出,而在進行逆洗運轉時,使流體由第2供排部供給 至殼體内,同時由第1供排部排出。 9. 一種陶瓷膜組件之運轉方法,係申請專利範圍第1項所 記載之陶瓷膜組件之運轉方法,在進行一般運轉時, 使流體由第2供排部供給至殼體内,同時由第1供排部 排出,而在進行逆洗運轉時,使流體由第1供排部供給 至殼體内,同時由第2供排部排出。314039.ptd Page 53 553765 6. Discharge of patent applications. During the backwash operation, the fluid is supplied from the second supply and discharge unit to the casing and discharged from the first supply and discharge unit. 9. A ceramic membrane module operating method is the ceramic membrane module operating method described in item 1 of the scope of patent application. During normal operation, the fluid is supplied from the second supply and discharge unit to the housing, and at the same time by the first The first supply / discharge unit discharges the fluid. When the backwash operation is performed, the fluid is supplied from the first supply / discharge unit into the casing, and is simultaneously discharged from the second supply / discharge unit. 314039.ptd 第54頁314039.ptd Page 54
TW091121964A 2001-09-28 2002-09-25 Ceramic membrane module and the operation method thereof TW553765B (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP2001298723 2001-09-28
JP2002267472A JP2004098031A (en) 2002-09-13 2002-09-13 Membrane module
JP2002267471A JP2003170028A (en) 2001-09-28 2002-09-13 Ceramic membrane module and method of operating the same
JP2002269315A JP2004105815A (en) 2002-09-17 2002-09-17 Membrane module
JP2002270830A JP2004105838A (en) 2002-09-18 2002-09-18 Membrane module

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JPH10109022A (en) * 1996-10-03 1998-04-28 Toshiba Ceramics Co Ltd Filter module
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