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TW201143876A - Header member, membrane module, and method for manufacturing membrane module - Google Patents

Header member, membrane module, and method for manufacturing membrane module Download PDF

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Publication number
TW201143876A
TW201143876A TW100106264A TW100106264A TW201143876A TW 201143876 A TW201143876 A TW 201143876A TW 100106264 A TW100106264 A TW 100106264A TW 100106264 A TW100106264 A TW 100106264A TW 201143876 A TW201143876 A TW 201143876A
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TW
Taiwan
Prior art keywords
head cover
cover member
hollow fiber
fiber membrane
module
Prior art date
Application number
TW100106264A
Other languages
Chinese (zh)
Inventor
Yuzuru Ishibashi
Shuichi Nakata
Original Assignee
Asahi Kasei Chemicals Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by Asahi Kasei Chemicals Corp filed Critical Asahi Kasei Chemicals Corp
Publication of TW201143876A publication Critical patent/TW201143876A/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/021Manufacturing thereof
    • B01D63/022Encapsulating hollow fibres
    • B01D63/0221Encapsulating hollow fibres using a mould
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/21Specific headers, end caps

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

Abstract

Closed-end tubular header members (9) are mounted to the ends of a hollow fiber membrane bundle (7) and are affixed to the hollow fiber membrane bundle (7) by a sealing material (S) filled into and solidified in the inside of the closed-end header members (9). The header members (9) each comprises: an inlet-side tube section (21) provided to the inlet side into which the hollow fiber membrane bundle (7) is inserted; and an end-side tube section (23) having an inner diameter smaller than that of the inlet-side tube section (21) and provided further toward the end side than the inlet-side tube section (21). A step (St) is formed between the inner surface of the inlet-side tube section (21) and the inner surface of the end-side tube section (23). Annular grooves (21a, 23a, 23b) extending about the axis (L) of the header member (9) are formed in the inner surface of the inlet-side tube section (21) and/or the inner surface of the end-side tube section (23).

Description

201143876 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種用以製造包括中空纖維膜束之膜模組 的頭蓋構件、膜模組及膜模組之製造方法。 【先前技術】 作為利用精密過濾膜、超過濾膜的膜過濾法中所使用之 膜’中空纖維膜已為人所知。使用有中空纖維膜之膜模組 之膜面積大,且可使裝置小型化,因此’廣泛利用於各種 膜分離之用途中。中空纖維膜模組通常包括:包含複數個 中空纖維膜之中空纖維膜束;密封固定部,其於中空纖維 膜束之兩端開放之狀態下,對中空纖維膜束之兩端部進行 接著密封;以及套管’其收容由密封固定部密封的中空纖 維膜束。另—方面,不存在套管且可裝脫地插人至稱為外 殼的殼體的濾筒型之膜模組亦已為人所知(參照專利文獻 1)。渡筒型之膜模組之構造基本上與固^於套管内的通常 之膜模組之構造相同’但具有如下特徵,_,以將中*纖 維膜束包圍之方式而安裝有稱為保護網或保護筒之保: 件’且將其收容於外殼内β x再 之頭蓋構件覆蓋於中ίΛ?織她梅土 ' 干復盖於H維膜束之端部之方式而安 ==構Γ利用離,法將密封材料填充二 將中二纖維膜束固定於頭蓋構件之後,將…BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of manufacturing a head cover member, a film module, and a film module for manufacturing a film module including a hollow fiber membrane bundle. [Prior Art] A membrane hollow fiber membrane used in a membrane filtration method using a microfiltration membrane or an ultrafiltration membrane is known. The membrane module using the hollow fiber membrane has a large membrane area and can be miniaturized, and is therefore widely used in various membrane separation applications. The hollow fiber membrane module generally comprises: a hollow fiber membrane bundle comprising a plurality of hollow fiber membranes; and a sealing fixing portion which seals both ends of the hollow fiber membrane bundle in a state in which both ends of the hollow fiber membrane bundle are open And a sleeve that houses a bundle of hollow fiber membranes sealed by a seal fixing portion. On the other hand, a filter cartridge type membrane module which does not have a sleeve and is detachably inserted into a casing called a casing is also known (refer to Patent Document 1). The structure of the membrane module of the tortoise type is basically the same as that of the conventional membrane module fixed in the sleeve, but has the following features, _, which is called to protect the medium fiber bundle The protection of the net or the protective tube: the piece 'and the inside of the outer casing of the β x and then the cover member covering the middle of the Λ 织 梅 梅 梅 ' 干 干 干 干 干 干 梅 梅 梅 梅 梅 ' = = = = = = = = = ΓUsing the separation method, the sealing material is filled into two, and the second fiber fiber bundle is fixed to the head cover member, and ...

側之-部分與中空纖維膜束 ISide-part and hollow fiber membrane bundle I

併予以切斷,作為J 153942.doc 201143876 結果,形成模組端面’該模組端面形成有連通於中空纖維 膜之内部之開口。使用頭蓋構件而製造膜模組,藉此,作 為成品之膜模組之尺寸穩定性變高。 [先前技術文獻] [專利文獻] [專利文獻1]曰本專利特表2007-503298號公報 【發明内容】 [發明所欲解決之問題] 近年來,於啤酒或葡萄酒等之釀造飲料之製造中 係進行矽藻土過濾,但近年來,自環境保護之觀點考慮, 開始採用不使用矽藻土之膜分離法,故用來代替石夕藻土之 膜模組市場擴大。於該領域中使用濾筒型之膜模組,該廣 筒型之膜模組係於高壓(二氧化碳氣體壓力)條件下進行過 濾操作,且插入至不鏽鋼製外殼中使用。於上述釀造飲料 之製造步驟中,經過數。C之過濾步驟之後,反覆地進行約 8〇 C之藥液清洗步驟,該藥液清洗步驟係用以除去因過瀘 而堆積於膜面之堆垢物質而使過濾性能恢復。亦即,於一 系列之過濾操作之過程中,中空纖維膜模組會反覆地暴露 於低溫與高溫之環境中。當由於反覆地進行上述低溫之過 濾步驟與咼溫之清洗步驟,而使得先前之頭蓋構件中的與 密封材料接觸的内表面與密封材料之間產生剝離時,該剝 離容易成長,結果’有時會導致膜模組之品質下降。 本發明係鑒於如上所述之問題開發而成之發明,本發明 之目的在於提供如下頭蓋構件、膜模組及膜模組之製造方 153942.doc 201143876 法,該頭蓋構件尤其於啤酒醱酵液等之釀造飲料之過濾 中,於反覆進行低溫之過濾步驟與高溫之清洗步驟之苛刻 之運轉環境下,亦可抑制與密封材料發生接觸之内表面與 填充至内部<密封材料之間之剝離的產生或成長,從而有 助於提高膜模組之品質。 [解決問題之技術手段] 本發明係—種有底筒狀之頭蓋構件,其安裝於中空纖維 膜束之端部,並且内部填充且固化有密封材料,藉此,固 定於中空纖維膜束,該有底筒狀之頭蓋構件之特徵在於: 包括:入口側筒部’其設置於插入中空纖維膜束之入口 側;以及端部側筒部,其内徑小於入口側筒部之内徑,且 設置於較入口側筒部更靠端部側;並且,於入口側筒部之 内表面與端部側筒部之内表面之間形成有階差,且於入口 側筒部及端部側筒部中之 ^ ^ m从 Π丨T之至)-者之内表面,形成有圍繞 頭盍構件之軸線之環狀之槽。 根據本發明’即便於通罢 使於頭盍構件之入口侧產生剝離,由於 在入口側筒部之内表面盥 階差,故而藉心階差:㈣部之内表面之間形成有 階差而阻止剝離自入口側筒部側朝端邱 側筒部傳播,因此,剝雜夕士 p ^ ^ 充至商签 ' 成長又到抑制。而且,由於填 充至頭羞構件之内部之密 /L , m L, <、王咏狀之槽内而固And cut off, as a result of J 153942.doc 201143876, the end face of the module is formed. The end face of the module is formed with an opening communicating with the inside of the hollow fiber membrane. The film module is manufactured by using the head cover member, whereby the dimensional stability of the film module as a finished product becomes high. [Prior Art] [Patent Document 1] [Patent Document 1] Japanese Patent Laid-Open Publication No. 2007-503298 [Draft of the Invention] [Problems to be Solved by the Invention] In recent years, in the manufacture of brewed beverages such as beer or wine In order to filter the diatomaceous earth, in recent years, from the viewpoint of environmental protection, the membrane separation method which does not use diatomaceous earth has been used, so the membrane module market used to replace Shishizao soil has expanded. A filter cartridge type membrane module is used in this field, and the wide-tube membrane module is subjected to filtration under high pressure (carbon dioxide gas pressure) and inserted into a stainless steel casing. In the manufacturing steps of the brewed beverage described above, the number is passed. After the filtration step of C, a chemical cleaning step of about 8 〇 C is carried out, which is used to remove the fouling material deposited on the membrane surface due to over-twisting to restore the filtration performance. That is, during a series of filtration operations, the hollow fiber membrane module is repeatedly exposed to low temperature and high temperature environments. When peeling occurs between the inner surface of the previous head cover member in contact with the sealing material and the sealing material by performing the above-described low-temperature filtration step and the cleaning step of the temperature, the peeling tends to grow, and as a result, sometimes This will result in a decrease in the quality of the membrane module. The present invention has been made in view of the above problems, and an object of the present invention is to provide a method for manufacturing a head cover member, a film module and a film module, 153942.doc 201143876, which is particularly suitable for beer fermentation broth In the filtration of the brewed beverage, in the harsh operating environment in which the low-temperature filtration step and the high-temperature cleaning step are repeated, the peeling of the inner surface in contact with the sealing material and the filling to the inner <sealing material can be suppressed. Produced or grown to help improve the quality of the membrane module. [Technical means for solving the problem] The present invention is a bottomed cylindrical head member which is attached to an end portion of a hollow fiber membrane bundle and which is internally filled and solidified with a sealing material, thereby being fixed to the hollow fiber membrane bundle, The bottomed cylindrical head cover member is characterized by comprising: an inlet-side tubular portion 'which is disposed on an inlet side of the hollow fiber membrane bundle; and an end-side tubular portion having an inner diameter smaller than an inner diameter of the inlet-side tubular portion, And disposed on the end side of the inlet-side tubular portion; and a step is formed between the inner surface of the inlet-side tubular portion and the inner surface of the end-side tubular portion, and on the inlet-side tubular portion and the end portion side The inner surface of the tube portion from the Π丨T to the inner surface is formed with an annular groove around the axis of the head 盍 member. According to the present invention, even if the peeling occurs on the inlet side of the head 盍 member, the step is formed on the inner surface of the inlet side cylindrical portion, so that the step is formed by the inner surface of the (four) portion. The peeling is prevented from spreading from the side of the inlet side tube side toward the end side of the tube side of the tube, and therefore, the stripping of the stalks p ^ ^ to the merchant's sign 'growth again to suppression. Moreover, due to the denseness of the inside of the head-shaving member, /L, <, the shape of the king-shaped groove is solid

化,因此,頭蓋構件與密封 U 嵌合且宝田^之接觸面彼此呈凹凸狀地 。且牛固地結合,從而對於抑制 有效。作為其結果、 座生次成長而, 了有助於如咼膜模組之品 而且,較佳為,頭蓋 頌盖構件之端部侧筒部包括:筒狀之主 153942.doc 201143876 體部、與一體成形於該主體部之底部。 而且,較佳為上述槽包括:形成於入口側筒部之淺槽、 與形成於端部側筒部且較淺槽更深之深槽◊於將密封材料 填充至頭蓋構件之内部之情形時,例如,於頭蓋構件之端 部側形成密封材料之導入口,經由該導入口而填充密封材 料。形成於頭蓋構件之内表面之槽越深,則密封材料與頭 蓋構件之間之結合越牢固,從而於抑制剝離之方面有^ 然而,對於自頭蓋構件之端部側充填密封材料之方法而 言,與端部側筒部相比較,密封材料更難以進入至入口側 筒部’因此,若使入口側筒部之槽過深,則密封材料益法 完全進入,從而存在於密封材料與頭蓋構件之間產生間隙 w性3方面,與入口側筒部相比較,密封材料易 於進入至端部側筒部,因此,即便積極地使槽之深度加 深,亦可充分地使密封材料進入。亦即,根據上述構成, 於自頭蓋構件之端部側填充密封材料之情形時,可確實地 填充㈣材料,並且易於實現頭蓋構件與密封材料之間之 牛固之結合,即便於高壓(例如二氧化碳氣㈣力)且過濟 步驟、清洗步驟之溫度變化之幅度超祕。c之非常苛㈣ 運轉條件下,對於抑_離之成長而言亦有效。 繞ΐ蓋::為於本發明之端部侧筒部之内表面,形成有圍 =冓:之軸線之環狀之凸部。填充至頭蓋構件之内部 ㈣空纖維膜束與頭蓋構件之間之間隙 u部之内表面之凸部予以遮 盍 至頭羞構件之内部之密封材料於固化之過程中會 153942.doc 201143876 發生熱收縮’但於該情形時,將 係以夾持凸部之方式而收縮,因此二:=封材料 之過程中之剝離。作為其結果 料固化 模組之品質提高方面有效。抑_離之成長而使膜 又,本發明之膜模組之特徵在於: 構件而形成之筒狀之頭蓋部、包含插頭:== 罢却— ·乘维膜束將中空纖維膜束固定於頭 面封部、以及使中空纖維膜之内部開放之模組端 根據本發明,即便於頭蓋部之入口側產生剝離,由於於 ==内表Γ端部側筒部之内表面之間形成有階 筒部傳播*該階差而阻止剝離自入口側筒部朝端部側 凹凸狀地.:且,由於頭蓋部與密封材料之接觸面彼此呈 品質=牢固地結合’因此,可有助於使膜模組之 筒二’較佳為上述膜模組進而包括筒狀之保護構件,該 “呆護構件呈環狀地將中空纖維膜束予以包圍,且與 件膜束一併藉由密封部而固定於頭蓋部,於保護構 伴數個貫通孔、與自固定於頭蓋部之側之端部朝 =構,之軸線方向突出之線狀之突出部。藉由保護構件 生良好地保持中空纖維膜束,保護該中空纖維膜束 ;卜部之衝擊等之影響。又,於保護構件之端部,以朝 :::件之軸線方向突出之方式而設置有線狀之突出部。 ,曰藉由無突出部之平坦之圓周而形隸護構件之端部 153942.doc 201143876 時,右於該端部產生剝離,則該剝離易於沿圓周方向傳 播,剝離易於成長。然而,根據上述構成,形成於保護構 件之端部之突出部成為障礙物而阻止剝離朝圓周方向傳 播,因此,對於抑制剝離之成長而言有效。 而且,較佳為保護構件為網狀,且具有形成貫通孔之複 數個網眼’ x出部形成為於保護構件之端部自連接為環狀 之複數個網眼分別突出。藉由設置分別對應於複數個網眼 之複數個突出冑’突出部以大致均等之間隔而配置於圓周 方向從可有效果地阻止剥離朝圓周#向傳播。 又’本發明係使用上述頭蓋構件而製造膜模組之方法, 、 /在於匕括如下步驟:對複數個中空纖維膜進行捆 束而形成中工纖維膜束;將頭蓋構件安裝於中空纖維膜束 之端。Ρ,將液狀之密封材料填充至頭蓋構件之内部·使填 充至頭蓋構件之内部之密封材料固化而形成密封部;以及 成㈣之後’與申空纖維膜之端部—併將頭蓋構件 之端部側之一部分及荣Α 數個中*纖唯膜之內 刀予以切斷’形成使複 数個中工纖維膜之内部開放之模組端面。 根據本發明,於形忐您h ί邛之過程中,即便於頭蓋構件 之入口側產生剝離,由 η ; 口側筒部之内表面與端部側 =内表面之間形成有階差,因此,藉由該階 朝端部側筒部傳播,而且,由於填充 故=1 密封材料進入至環狀之槽内而固化, 牢固地結合,因此’可製、=呈凹凸狀地嵌合且 製每αο質向之臈模組。 153942.doc 201143876 [發明之效果] 根據本發明,可抑制與填充至内部之密封材料之間之剝 離之產生或成長’從而提高膜模組之品質。 【實施方式】 以下,參照圖式對本發明之較佳實施形態進行說明。 利用各種方法作為自水溶液中除去酵母或菌體等之微生 物粒子之方法,但尤其利用有精密過濾膜或超過攄膜之膜 過慮法可除去全部之微生物,而且可進行大量之連續處 理,因此適合於工業利用。此種膜過遽法中所使用之膜過 滤裝置具有如下類型:收容於套管内之中空纖維膜之束固 定於套管而經模組化;或不具備套管且中空纖維膜之束經 -體化Μ為膜模組,該膜模組裝脫自如地收容於稱為外 殼之殼體内等。本實施形態之膜模組係後者之稱為滤筒模 組之類型。 爐筒模組1(參照圖7)裝脫自如地收容於特;t之外殼3内 而使用。例如,將頭蓋構件9(參照圖1}固定於複數個中* 纖維膜之束(以下稱為「中空纖維膜束」)7之兩端而製造模 組前驅物5,進而將模組前驅物5之兩端之一部分予以切 斷,形成使中空纖維膜以之端部開放之模組端面6,藉 此,製造遽筒模组卜首先,對模組前驅物5進行說明。3 (模組前驅物)Therefore, the head cover member is fitted to the seal U and the contact faces of the Baotian^ are concave-convex with each other. And the cattle are solidly combined to be effective for inhibition. As a result of the growth of the seat, it is advantageous for the product such as the diaphragm module. Preferably, the end side tubular portion of the head cover member includes: a cylindrical main body 153942.doc 201143876 body, And integrally formed on the bottom of the main body portion. Further, it is preferable that the groove includes a shallow groove formed in the inlet-side tubular portion and a deep groove deeper in the shallower groove formed in the end-side tubular portion, in a case where the sealing material is filled into the inside of the head cover member, For example, an introduction port of a sealing material is formed on the end side of the head cover member, and the sealing material is filled through the introduction port. The deeper the groove formed on the inner surface of the head cover member, the stronger the bond between the sealing material and the head cover member, thereby suppressing the peeling. However, for the method of filling the sealing material from the end side of the head cover member Compared with the end side tubular portion, the sealing material is more difficult to enter into the inlet side tubular portion. Therefore, if the groove of the inlet side tubular portion is made too deep, the sealing material is fully ingested, so that it exists in the sealing material and the head cover member. In the case where the gap w is 3, the sealing material can easily enter the end-side tubular portion as compared with the inlet-side tubular portion. Therefore, even if the depth of the groove is actively deepened, the sealing material can be sufficiently entered. That is, according to the above configuration, when the sealing material is filled from the end side of the head cover member, the (four) material can be surely filled, and the combination of the head cover member and the sealing material can be easily realized even at a high pressure (for example, Carbon dioxide gas (four) force) and the extent of the temperature change in the over-the-step and cleaning steps is super-secret. c is very harsh (4) Under operating conditions, it is also effective for the growth of _ _ _. Winding cover: In the inner surface of the end side tubular portion of the present invention, an annular convex portion having an axis of 冓: is formed. Filling the inside of the head cover member (4) The convex portion of the inner surface of the gap u between the hollow fiber membrane bundle and the head cover member is concealed to the inside of the head shame member. The sealing material will be in the process of curing. 153942.doc 201143876 Shrinking 'But in this case, it will shrink in such a manner as to clamp the convex portion, so the second: = peeling during the sealing of the material. As a result, the quality of the material curing module is effective. Further, the membrane module of the present invention is characterized in that: the tubular head portion formed by the member, including the plug: == stop - the multi-dimensional membrane bundle fixes the hollow fiber membrane bundle to According to the present invention, the head surface seal portion and the module end opening the inside of the hollow fiber membrane are peeled off at the inlet side of the head cover portion, and are formed between the inner surfaces of the inner tube portion of the end portion of the inner surface The stepped portion propagates the step to prevent peeling from the inlet side cylindrical portion toward the end portion side. In addition, since the contact faces of the head cover portion and the sealing material are in good quality = firmly bonded together, Preferably, the membrane module 2' is preferably the membrane module further comprising a tubular protective member, the "protective member" encloses the hollow fiber membrane bundle in an annular shape, and is sealed together with the membrane bundle The portion is fixed to the head cover portion, and has a plurality of through holes and a linear protruding portion that protrudes in the axial direction from the end portion fixed to the side of the head cover portion, and is protected by the protective member. a bundle of hollow fiber membranes to protect the bundle of hollow fiber membranes; In addition, at the end of the protective member, a linear protruding portion is provided so as to protrude toward the axis of the ::: member, and the ridge is protected by the flat circumference without the protruding portion. When the end portion of the member is 153942.doc 201143876, peeling is generated right at the end portion, the peeling is likely to propagate in the circumferential direction, and the peeling is easy to grow. However, according to the above configuration, the protruding portion formed at the end portion of the protective member becomes an obstacle. Further, the peeling is prevented from propagating in the circumferential direction, and therefore, it is effective for suppressing the growth of peeling. Further, it is preferable that the protective member has a mesh shape and a plurality of meshes forming the through holes are formed in the protective member. The end portions are respectively protruded from a plurality of meshes which are connected in a ring shape, and the plurality of protruding protrusions corresponding to the plurality of meshes are disposed at substantially equal intervals and arranged in the circumferential direction to effectively prevent peeling. Further, the present invention is a method for manufacturing a film module by using the above-mentioned head cover member, and/or includes the following steps: a plurality of hollow fiber membranes are introduced Bundling to form a bundle of medium fiber fibers; attaching the head cover member to the end of the hollow fiber membrane bundle. Ρ, filling the liquid sealing material into the inside of the head cover member, and solidifying the sealing material filled into the inside of the head cover member a sealing portion; and after (4) and after the end portion of the hollow fiber membrane - and cutting off one end portion of the head cover member and the inner knife of a plurality of medium-fibre films, forming a plurality of intermediate workers The end face of the module which is open inside the fiber membrane. According to the invention, even if peeling occurs on the inlet side of the head cover member during the process of the shape, the inner surface and the end side of the mouth side tubular portion are A step is formed between the inner surfaces, and therefore, the step is propagated toward the end side tubular portion, and since the sealing material enters into the annular groove due to filling, the solidified and solidly bonded, so that it can be made , = fit in a concave-convex shape and make a module for each α-quality. [Effect of the Invention] According to the present invention, the occurrence or growth of peeling between the sealing material filled in the inside can be suppressed, thereby improving the quality of the film module. [Embodiment] Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings. Various methods are used as a method for removing microbial particles such as yeast or bacteria from an aqueous solution, but in particular, it is possible to remove all microorganisms by a membrane filtration method having a fine filtration membrane or a membrane exceeding the ruthenium membrane, and it is possible to carry out a large number of continuous treatments, and thus it is suitable. Used in industry. The membrane filtration device used in the membrane filtration method has the following types: a bundle of hollow fiber membranes housed in a sleeve is fixed to a sleeve and modularized; or a sleeve without a sleeve and a bundle of hollow fiber membranes - The enthalpy is a membrane module, and the membrane module is detachably housed in a casing called a casing. The membrane module of this embodiment is of the type referred to as a cartridge mold set. The furnace module 1 (see Fig. 7) is detachably housed in the outer casing 3 of t; For example, the head cover member 9 (see FIG. 1) is fixed to both ends of a plurality of medium fiber membrane bundles (hereinafter referred to as "hollow fiber membrane bundles") 7 to manufacture a module precursor 5, and then a module precursor One of the two ends is cut to form a module end face 6 for opening the hollow fiber membrane with the end portion thereof, thereby manufacturing the cartridge module. First, the module precursor 5 will be described. Precursor)

如圖1及圖4所示,模組前驅物5包括:有底筒狀之頭蓋 構件9,其安裝於中*總 m A U,其…:端;筒狀之保護構件 其插通有中空纖維膜束7且保護令空纖維膜束7;十字 153942.doc 201143876 板13,其插入至中空纖維膜束7之端部而對中空纖維心 之密度之不均進行修正,且與中空纖維膜束7一併嵌入之 頭蓋構件9之内部;以及密封部15,其藉由填充至頭蓋構 件9之内部且固化之密封材料s而將中空纖維膜束7、保護 構件11、十字板13及頭蓋構件9予以接著(結合)。 頭蓋構件9(參照圖2)包含高分子材料’例如可例示聚 砜、聚醚砜、聚苯砜等之聚砜系樹脂;或者聚碳酸醋或聚 對苯二甲酸乙二醇酯、聚對苯二甲酸丁二醇酯等之聚酯系 樹脂,6-尼龍或6,6-尼龍等之聚醯胺系樹脂;以及ABS (Acrylomtnle Butadiene Styrene’ 丙烯腈·丁二烯_ 苯乙烯) 或AES(Acrylonitrile Ethylene,丙烯腈乙晞苯乙 烯)等之苯乙烯系樹脂。再者,關於頭蓋構件9之材料之選 擇,較佳為考慮膜模組之使用條件而進行選擇。而且,於 用以製造上述釀造飲料之膜模組之情形時,自埘熱性或耐 化學品性之觀點考慮,較佳為使用聚砜系樹脂。 頭蓋構件9為有底圓筒狀(杯狀),且包括:設置於插入 中空纖維膜束7之入口側之入口側筒部2 i、與設置於端部 側之端部側筒部23。入口側筒部21之内徑與端部側筒部23 之内徑不同,端部側筒部23之内徑小於入口側筒部2丨之内 徑。對入口側筒部21與端部側筒部23之内徑ri ' r2彼此進 行對比時之比(頭蓋構件9之内徑比)即r2/ri較佳為〇 5以上 且0.99以下。又,根據與可填充之中空纖維膜根數(模組膜 面積)之關係’上述r2/rl更佳為〇.8以上且〇98以下,尤佳 為0.85以上且0.95以下。此處,rl#r2為後述之座面25之 153942.docAs shown in FIG. 1 and FIG. 4, the module precursor 5 includes: a bottomed cylindrical head cover member 9 mounted on the middle* total m AU, the ...: end; the cylindrical protective member is inserted with hollow fiber Membrane bundle 7 and protective hollow fiber membrane bundle 7; cross 153942.doc 201143876 plate 13, inserted into the end of hollow fiber membrane bundle 7 to correct the density unevenness of hollow fiber core, and with hollow fiber membrane bundle 7 is embedded inside the head cover member 9; and a sealing portion 15 which presses the hollow fiber membrane bundle 7, the protective member 11, the cross plate 13, and the head cover member by filling the inside of the head cover member 9 and solidifying the sealing material s 9 will be followed (combined). The head cover member 9 (see FIG. 2) includes a polymer material 'for example, a polysulfone resin such as polysulfone, polyethersulfone or polyphenylsulfone; or polycarbonate or polyethylene terephthalate or a polypair Polyester resin such as butyl phthalate, polyamide resin such as 6-nylon or 6,6-nylon; and ABS (Acrylomtnle Butadiene Styrene' acrylonitrile butadiene styrene) or AES A styrene resin such as Acrylonitrile Ethylene or acrylonitrile styrene. Further, the selection of the material of the head cover member 9 is preferably selected in consideration of the use conditions of the film module. Further, in the case of producing a film module of the above brewed beverage, it is preferred to use a polysulfone resin from the viewpoint of heat resistance or chemical resistance. The head cover member 9 has a bottomed cylindrical shape (cup shape), and includes an inlet side tubular portion 2i that is provided on the inlet side of the hollow fiber membrane bundle 7, and an end portion side tubular portion 23 that is provided on the end side. The inner diameter of the inlet-side tubular portion 21 is different from the inner diameter of the end-side tubular portion 23, and the inner diameter of the end-side tubular portion 23 is smaller than the inner diameter of the inlet-side tubular portion 2''. The ratio of the inner diameter ri ' r2 of the inlet-side tubular portion 21 and the end-side tubular portion 23 to each other (the inner diameter ratio of the head cover member 9), that is, r2/ri is preferably 〇 5 or more and 0.99 or less. Further, the above r2/rl is more preferably 88 or more and 〇98 or less, and particularly preferably 0.85 or more and 0.95 or less, based on the relationship with the number of hollow fiber membranes that can be filled (module membrane area). Here, rl#r2 is 153942.doc of the seat surface 25 described later.

S 201143876 位置處之内徑。 再者’關於相對於入口側筒部21而設置於端部側 側筒部23’該「端部側」係指入口側之相反側。而且,如 本實施形態所示’於有底筒狀之情形時,上述「端部側」 係指底側,於不具有底部之形態之情形時,上述「端部 側」係指另一開放之端部側。 入口側筒部21與端部側筒部23之内表面彼此經由形成於 與頭蓋構件9之軸線L大致正交之假想之平面上的環狀之座 面25而聯繫。藉由該座面25 ’於人口側筒部21與端部側筒 部23之内表面彼此之間形成有具有高低差之階差參照圖 5)。 、 於入口側筒部21之内表面,形成有複數個圍繞頭蓋構件 9之軸線L的環狀之淺槽21a。於本實施形態中,例示了淺 槽2la之形狀為三角槽(剖面觀察時呈如對直角三角形進行 切割而成之形狀之槽)之形態(參照圖9(b)),但槽形狀包含 角槽(參照圖9(a))、圓槽(參照圖9(c))、筒端凹槽(參照圖 9(e))、及V字狀槽(山形槽)(參照圖9(d))等,可採用眾所周 知之槽形狀。上述槽可於對頭蓋構件9進行射出成形之同 時形成’亦可於對頭蓋構件9進行射出成形之後進行後加 工而形成。 此處’關於淺槽21a之形狀,以採用離心澆鑄法作為將 密封材料S填充至頭蓋構件9之内部之方法之情形為例子而 補充性地進行說明(參照圖9)。於該情形時,考慮到氣泡之 排除容易性、加工之容易性、以及量產時之成本等,淺槽 153942.doc 201143876 21 a較佳為角槽、三角槽、圓槽、及v字狀槽之四種中之任 一種槽形狀、或將上述四種槽形狀適當地組合於複數個淺 槽21a而成之形態,更佳為角槽、三角槽、及v字狀槽之三 種中之任一種槽形狀、或將上述三種類之槽形狀適當地組 合於複數個淺槽21 a而成之形態。 再者,可考慮頭蓋構件9之尺寸、或頭蓋構件9與密封材 料S之易剝離性而適當地決定形成於入口側筒部21之淺槽 21a之條數或加工位置。 於端部側筒部23之内表面,形成有複數個圍繞頭蓋構件 9之軸線L的環狀之深槽23a,而且形成有複數個圍繞頭蓋 構件9之軸線L的環狀之淺槽23be深槽23&設置於偏向入口 側筒部21之兩處,淺槽21a統一地形成於偏向底部处之特 定之區域。端部側筒部23之淺槽23b之形狀及深度實質上 與入口側筒部21之淺槽21 a之形狀及深度相同。 對於本實施形態之深槽23a而言,例示了四角槽(剖面觀 察時呈如對長方形進行切割而成之形狀之槽)之形態,但 槽形狀包含角肖、三角槽、圓槽、筒端凹槽、及v:狀槽 等’可廣泛地採用眾所周知之槽形狀。上述槽可於對頭蓋 構件9進行射出成形之同時形成,亦可於對頭蓋構件9進行 射出成形之後,進行後加工而形成。 此處’關於深槽23a之形狀,以採用離心澆鑄法作為將 :封材料S填充至頭蓋構件9之内部之方法之情形為例子而 :充性地進行說明。於該情形時,考慮到氣泡之排除容易 、加工之容易性、以及量產時之成本等,深槽…較佳 153942.doc -12· 201143876 為角槽、三角槽、圓槽、及v字狀槽之四種中之任一種槽 形狀、或將上述四種槽形狀適當地組合於複數個淺槽2ia 而成之形態,更佳為角槽、三角槽、及、字狀槽之三種中 之任一種槽形狀、或將上述三種類之槽形狀適當地組合於 複數個淺槽21a而成之形態。 深槽23a之深度較形成於入口側筒部21之淺槽21&及淺槽 23b之深度更深,淺槽21a及淺槽23b之平均深度们相對於 深槽23a之平均深度dl之比即d2/dl較佳為〇_丨以上且〇 9以 下’更佳為0.2以上且0.8以下。此處,所謂「槽之深 度」’係指一個槽之最深之部分之深度,上述「平均深 度」,係指複數條槽各自之算術平均值。 又,於本實施形態中,兩條深槽23a中之入口側之一條 深槽23a設置為排列於形成階差St之座面25,作為其結 果,於座面25與深槽23a之間,形成有圍繞頭蓋構件9之軸 線L的環狀之第1凸部23c。又,於相鄰地排列之兩條深槽 23a彼此之間,形成有圍繞頭蓋構件9之軸線L之環狀之第2 凸部23d。 再者,可考慮頭蓋構件9之尺寸與用以形成模組端面6之 切斷位置而任意地決定形成於端部側筒部23之深槽23a或 淺槽23b、或者凸部23c、23d之條數或加工位置。 再者’於本實施形態中’以包括於筒狀之主體部23e__ 體成形有底部23f之有底筒狀之端部側筒部23(參照圖2(b)) 之形態而對頭蓋構件9進行說明。然而,本發明之頭蓋構 件並非僅限定於上述形態,例如亦包括不具有底部之由端 153942.doc 13 201143876 部側筒部與入口側筒部構成 |傅战之肖狀之形態。再者,於後者 之形態之情形時,當進行離心溘臺 屬鑄時’必需預先液密性地 將筒狀體之端部侧筒部、及斑辞 汉興該鳊部側筒部為分體之底部 予以接合而使用,自製造膜禮^ μ 衣每犋模組時之簡便性之觀點考慮, 前者之形態較佳。 繼而’對中空纖維膜束(多孔質膜)7進行說明。以進行 捆束之方式而將多個中空纖維膜7a予以統一,藉此,形成 中空纖維膜束7。中空纖維膜7a之素材並無特別之限定, 可列舉聚乙稀、聚丙稀、聚偏二氯乙稀n聚_、 乙烯-乙烯醇共聚物、聚四氟乙烯、$丙烯腈、以及聚醚 綱等。尤其於用以製造酿造飲料之膜模組之情形時,自对 熱性或耐化學品性之觀點考慮,較佳為使用㈣、聚驗硬 等之聚砜系樹脂。 中空纖維膜束7插通於筒狀之保護構件1;[而受到保護構 :11保護。可根據用途等而選擇保護構件n之形狀,但通 吊於多數情形下’該保護構件11之形狀為圓筒狀於本實 施形態中,亦以圓筒狀為例子而進行說明。可根據被處理 流體或分離成分之種類等而選擇保護構件n之材質,例如 亦可為聚乙烯、聚丙烯、聚氯乙烯、聚碳酸酯、丙烯酸系 聚合物、聚硬、聚醚砜等之塑膠、以及不鏽鋼等之金屬。 通常於多數情形下,使用聚乙烯、聚丙烯、以及聚氣乙烯 等。尤其於用以製造釀造飲料之膜模組之情形時,自耐熱 性或耐化學品性之觀點考慮,較佳為使用聚丙烯或聚砜、 聚醚砜等之聚碾系樹脂。 153942.doc 201143876 保護構件11為具有複數個形成矩形之貫通孔Η之網眼之 網狀(參照圖3),而且保護構件u為規則地排列有複數個網 眼之大致圓筒狀。再者,保護構件u之端部插入至頭蓋構 件9内,該保護構件u設置為與頭蓋構件9大致同心之形 狀:因此,於以下之說明中,將保護構件u之轴線設為與 頭蓋構件9相同之軸線l而進行說明。 保護構件U包括:沿抽線L方向之複數個縱條部山與, 圓周方向之複數個圈狀部llb。複數個縱條部⑴與複數個 圈狀部m以交叉之方式而一體成形,藉此,於保護構件 U形成複數個矩形之貫通孔H。於保護構件u之軸線匕方 向之兩端部’複數個縱條部lla之前端(突出部)uc形成為 自圈狀部1 ib突出。其結果’複數個縱條部i 之突出部 =具體表現為如下形態,即,該突出部m形成為自連接 為環狀之複數個網眼分別突出。 再者,對於本實施形態之保護構件丨丨,例示了圓筒狀之 保護構件,但該保護構件11亦可為多角筒形狀。 較佳為使用實際上與形成密封部15之密封材料s相同之 :料而形成十字板13。例如’藉由環氧樹脂、乙烯酯樹 脂、胺酯樹脂、烯烴系聚合物、矽酮樹脂、以及含氟樹脂 等而形成上述十字板13。十字板13具有作為以不使密度於 周方向上產生偏差(不均)之方式而對多根中空纖維膜7a 進仃整理之插入物的功能,該十字板13係以插入至中空纖 維膜束7之☆而部之方式而安裝。再者,於本實施形態中, 作為插入物之一例,具體地對十字板13進行說明,但該插 153942.doc -15- 201143876 入物亦可為包含-枚平板之形態或以延伸為放射狀之方式 而設置有五枚以上之間隔片之形態等。 十字板13(參照圖4)為如下形狀,即,使矩形之兩枚平 板以彼此正交之方式而嵌合,且具有自作為交線之中央呈 放射狀地延伸之四牧間隔片……考慮有意地使間隔 片13a之表面成為粗糙面’使得填充密封材料s且使該密封 材料S固化時之結合(接著)強度提高。又,間隔片13a之尺 寸對應於頭蓋構件9之端部側筒部23之内徑之大致一半, 經由四枚間隔片l3a之外绫 _ 卜緣之叙心之圓荀之内徑與端部側 3 °内徑之比,即’假想之圓筒之内徑/端部側筒部 23之内徑形成為〇·5〜〇."。藉由四枚間隔片Ua,多根中空 纖維膜束7於端部側筒部23之内部實質上經四等分。 於插入至保護構件11之中Crt?输維胺 有十字板13,藉由十字:二維膜束7之兩端部分插入 十子板13,夕個中空纖維膜束7於目視 時大致均等地被劃分。中* 13之狀熊而奸 工’’,维臈束7係以安裝有十字板 之狀^插人至頭蓋構件9,將中空纖 之保護構件11之前端於商甚拢从Λ 不Τ以已圓 st之座⑽ 錢件9之㈣抵接於形成階差S 201143876 The inner diameter of the location. Further, the "end side" is provided on the opposite side of the inlet side side with respect to the inlet side tubular portion 21, and the "end side". Further, in the case of the bottomed cylindrical shape, the "end side" refers to the bottom side, and when the bottom portion is not provided, the "end side" refers to another opening. The end side. The inner surfaces of the inlet side tubular portion 21 and the end side tubular portion 23 are in contact with each other via an annular seating surface 25 formed on an imaginary plane substantially orthogonal to the axis L of the head cover member 9. A step having a step difference between the population side tubular portion 21 and the end side tubular portion 23 is formed by the seating surface 25' with reference to Fig. 5). On the inner surface of the inlet side tubular portion 21, a plurality of annular shallow grooves 21a surrounding the axis L of the head cover member 9 are formed. In the present embodiment, the shape of the shallow groove 21a is a triangular groove (a groove having a shape cut into a right-angled triangle when viewed in cross section) (see FIG. 9(b)), but the groove shape includes an angle. Groove (see Fig. 9 (a)), circular groove (see Fig. 9 (c)), cylindrical end groove (see Fig. 9 (e)), and V-shaped groove (mountain groove) (refer to Fig. 9 (d) And so on, a well-known groove shape can be employed. The groove may be formed at the same time as the injection molding of the head cover member 9 or may be formed by post-processing the injection molding of the head cover member 9. Here, the shape of the shallow groove 21a is complementarily described by taking a centrifugal casting method as a method of filling the sealing material S into the inside of the head cover member 9 as an example (see Fig. 9). In this case, the shallow groove 153942.doc 201143876 21 a is preferably an angular groove, a triangular groove, a circular groove, and a v shape in consideration of ease of elimination of bubbles, ease of processing, and cost at the time of mass production. Any one of four types of grooves, or a combination of the above four groove shapes in a plurality of shallow grooves 21a, more preferably three kinds of angle grooves, triangular grooves, and v-shaped grooves Any one of the groove shape or the groove shape of the above three types is appropriately combined in a plurality of shallow grooves 21a. Further, the number of the shallow grooves 21a formed in the inlet-side tubular portion 21 or the processing position can be appropriately determined in consideration of the size of the head cover member 9 or the easy peelability of the head cover member 9 and the sealing material S. On the inner surface of the end side tubular portion 23, a plurality of annular deep grooves 23a surrounding the axis L of the head cover member 9 are formed, and a plurality of annular shallow grooves 23be around the axis L of the head cover member 9 are formed. The grooves 23 & are disposed at two places facing the inlet side cylindrical portion 21, and the shallow grooves 21a are uniformly formed in a specific region at the bottom portion. The shape and depth of the shallow groove 23b of the end side tubular portion 23 are substantially the same as the shape and depth of the shallow groove 21a of the inlet side tubular portion 21. In the deep groove 23a of the present embodiment, a four-corner groove (a groove having a shape cut into a rectangular shape when viewed in a cross section) is exemplified, but the groove shape includes a corner horn, a triangular groove, a circular groove, and a cylindrical end. Grooves, and v: grooves, etc. can be widely used in well-known groove shapes. The groove may be formed at the same time as the injection molding of the head cover member 9, or may be formed by post-processing the injection molding of the head cover member 9. Here, the shape of the deep groove 23a is described by way of a centrifugal casting method as a method of filling the inside of the head cover member 9 with the sealing material S as an example. In this case, considering the ease of elimination of bubbles, the ease of processing, and the cost of mass production, etc., deep grooves... preferably 153942.doc -12· 201143876 are angle grooves, triangular grooves, circular grooves, and v characters. Any one of four kinds of groove shapes or a combination of the above four groove shapes in a plurality of shallow grooves 2ia, more preferably three kinds of angle grooves, triangular grooves, and word grooves. Any of the groove shapes or the combination of the above three types of groove shapes in a plurality of shallow grooves 21a. The depth of the deep groove 23a is deeper than the depth of the shallow groove 21& and the shallow groove 23b formed in the inlet side cylindrical portion 21, and the ratio of the average depth of the shallow groove 21a and the shallow groove 23b to the average depth dl of the deep groove 23a is d2 /dl is preferably 〇_丨 or more and 〇9 or less 'more preferably 0.2 or more and 0.8 or less. Here, the "depth of the groove" means the depth of the deepest portion of one groove, and the "average depth" refers to the arithmetic mean of each of the plurality of grooves. Further, in the present embodiment, one of the deep grooves 23a on the inlet side of the two deep grooves 23a is disposed so as to be arranged on the seating surface 25 where the step St is formed, and as a result, between the seating surface 25 and the deep groove 23a, An annular first convex portion 23c is formed around the axis L of the head cover member 9. Further, a second convex portion 23d which is annular around the axis L of the head cover member 9 is formed between the two deep grooves 23a which are adjacently arranged. Further, the size of the head cover member 9 and the cutting position for forming the end face of the module 6 can be arbitrarily determined in the deep groove 23a or the shallow groove 23b formed in the end side tubular portion 23, or the convex portions 23c, 23d. Number of bars or processing location. In the present embodiment, the head cover member 9 is formed in the form of a bottomed tubular end portion tubular portion 23 (see FIG. 2(b)) including a bottom portion 23f formed in a tubular body portion 23e__. Be explained. However, the head cover member of the present invention is not limited to the above-described embodiment, and includes, for example, a shape in which the bottom portion and the inlet side tube portion are not formed by the end portion 153942.doc 13 201143876. Further, in the case of the latter form, when the centrifugal slab is cast, it is necessary to preliminarily and in a liquid-tight manner, the end portion side tube portion of the cylindrical body and the plaque The bottom of the body is joined and used, and the former is preferable in terms of the simplicity of manufacturing the film for each module. Next, the hollow fiber membrane bundle (porous membrane) 7 will be described. The plurality of hollow fiber membranes 7a are unified by bundling, whereby the hollow fiber membrane bundle 7 is formed. The material of the hollow fiber membrane 7a is not particularly limited, and examples thereof include polyethylene, polypropylene, polyvinylidene chloride n-polymer, ethylene-vinyl alcohol copolymer, polytetrafluoroethylene, acrylonitrile, and polyether. Outline. In particular, in the case of a film module for producing a brewed beverage, it is preferred to use a polysulfone-based resin such as (4) or a hard test from the viewpoint of heat resistance or chemical resistance. The hollow fiber membrane bundle 7 is inserted into the tubular protective member 1 [protected by a protective structure: 11]. The shape of the protective member n can be selected depending on the application, etc., but in many cases, the shape of the protective member 11 is a cylindrical shape in the present embodiment, and a cylindrical shape will be described as an example. The material of the protective member n may be selected according to the type of the fluid to be treated or the type of the separated component, and the like, and may be, for example, polyethylene, polypropylene, polyvinyl chloride, polycarbonate, acrylic polymer, polyhard, polyethersulfone or the like. Plastic, metal such as stainless steel. In most cases, polyethylene, polypropylene, polyethylene gas, and the like are usually used. In particular, in the case of a film module for producing a brewed beverage, it is preferred to use a polypropylene resin, a polysulfone, a polyethersulfone or the like from the viewpoint of heat resistance or chemical resistance. 153942.doc 201143876 The protective member 11 is a mesh having a plurality of meshes of rectangular through holes, (see Fig. 3), and the protective member u is substantially cylindrical in which a plurality of meshes are regularly arranged. Further, the end portion of the protective member u is inserted into the head cover member 9, and the protective member u is provided in a shape substantially concentric with the head cover member 9; therefore, in the following description, the axis of the protective member u is set to be the head cover The member 9 has the same axis l and will be described. The protective member U includes a plurality of longitudinal strip portions in the direction of the drawing line L and a plurality of loop portions 11b in the circumferential direction. The plurality of vertical strip portions (1) and the plurality of loop portions m are integrally formed so as to intersect each other, whereby a plurality of rectangular through holes H are formed in the protective member U. The end portions (protrusions) uc of the plurality of vertical strip portions 11a are formed so as to protrude from the loop portion 1 ib at both end portions of the axial direction of the protective member u. As a result, the projections of the plurality of longitudinal strip portions i are specifically expressed in such a manner that the projections m are formed so as to protrude from a plurality of meshes connected in a ring shape. Further, although the cylindrical protective member is exemplified as the protective member 本 of the present embodiment, the protective member 11 may have a polygonal tube shape. It is preferable to form the cross plate 13 by using the same material as the sealing material s forming the sealing portion 15. For example, the cross plate 13 is formed of an epoxy resin, a vinyl ester resin, an amine ester resin, an olefin polymer, an anthrone resin, a fluorine resin, or the like. The cross plate 13 has a function as an insert for arranging a plurality of hollow fiber membranes 7a so as not to cause a deviation (unevenness) in the circumferential direction, and the cross plate 13 is inserted into the hollow fiber membrane bundle. 7 ☆ ☆ and the way to install. Further, in the present embodiment, the cross plate 13 is specifically described as an example of the insert, but the insert 153942.doc -15- 201143876 may also be in the form of a plate or extended to emit radiation. In the form of a shape, five or more spacer sheets are provided. The cross plate 13 (see FIG. 4) has a shape in which two flat plates of a rectangular shape are fitted so as to be orthogonal to each other, and have a four-grain spacer extending radially from the center of the intersection line... It is considered that the surface of the spacer 13a is intentionally made rough surface so that the bonding (subsequent) strength is increased when the sealing material s is filled and the sealing material S is cured. Further, the size of the spacer 13a corresponds to approximately half of the inner diameter of the end portion side tubular portion 23 of the head cover member 9, and the inner diameter and the end portion of the circle of the 叙 _ _ _ _ _ _ _ The ratio of the side 3° inner diameter, that is, the inner diameter of the 'imaginary cylinder/the inner diameter of the end side tubular portion 23 is formed as 〇·5 〇.". The plurality of hollow fiber membrane bundles 7 are substantially equally divided into four in the inside of the end side tubular portion 23 by the four spacers Ua. Inserted into the protective member 11 Crt? transvaminant has a cross plate 13, and the two ends of the two-dimensional film bundle 7 are inserted into the ten-plate 13 by the cross, and the hollow fiber bundle 7 is substantially equally visually observed. Is divided. In the middle of the 13th, the bear and the rapist'', the 臈 臈 bundle 7 series is installed with a cross-shaped plate ^ inserted into the head cover member 9, the front end of the hollow fiber protection member 11 is close to the business The seat of the round st (10) The money of the 9th (four) abuts the formation of the step

St之座面25。以該狀態, ^ ^ ^ 裝有十子板13之_空纖維膜束 7之W收谷於頭蓋構件9之端部側筒部η内。 將頭蓋構件9安裝於中空纖 纖維膜束7之兩個端部之後,將 液狀之密封材料S(亦稱為「封 ]何科」、「接著劑,)填 充至頭蓋構件9之内部,對中 .,, 纖,准膜束7之端部進行密 •列如可將環氧樹脂、乙稀酯;$ 聚入物埽®曰樹知、胺酯樹脂、烯烴系 ° 樹脂、以及含氟樹脂等用作密封材料S。 153942.docThe seat of St is 25. In this state, ^ ^ ^ is filled with the hollow fiber membrane bundle 7 of the ten-plate 13 in the end-side tubular portion η of the head cover member 9. After the head cover member 9 is attached to both end portions of the hollow fiber fiber membrane bundle 7, the liquid sealing material S (also referred to as "sealing" Heke" and "adhesive" are filled into the inside of the head cover member 9, For the center, the fiber, and the end of the quasi-membrane bundle 7 are made of epoxy resin, ethyl ester; $ 聚 埽 曰 曰 胺, amine ester resin, olefin resin, and A fluororesin or the like is used as the sealing material S. 153942.doc

S -16· 201143876 又,經由形成於頭蓋構件9之底部外之導入口 9&而填充密 封材料s,例如,適當地藉由離心澆鑄法或靜置澆鑄法等 而填充密封材料S。使填充至頭蓋構件9之内部之密封材料 s固化’藉此形《密封部! 5,從而形成模組前驅物5。 (遽筒模組) 如圖1、圖4及圖7所示,使用模組前驅物5而製造濾筒模 ’且(膜模組)1 »模組前驅物5處於藉由密封部丨5而將中空纖 維膜7a之兩端堵塞之狀態,& 了完成濾筒模組】,必需形 成使中空纖維膜〜之兩端開放之模組端面6。於本實施形 態中,藉由將頭蓋構件9之端部侧之一部分切斷除去而形 成模組端面6(參照圖4⑷),從而完成濾筒模組i。 遽筒模組1包括:使用頭蓋構件9而形成之筒狀之頭蓋部 L 3插入至頭蓋部la内之複數個中空纖維膜&之中空 纖維膜束7 ;冑中空纖維膜束7固定於頭蓋部1&之密封部 15 ;使中空纖維膜7&之内部開放之模組端面6 ;以及筒狀 之保善構件i i ’其呈環狀地將中空纖維膜束7包圍,且與 中空纖維膜束7 一併藉由密封部15而固定於頭蓋部心 、慮筒模組1插人至外殼3内且裝脫自如地被安裝,藉此構 :過濾膜單元。可根據用途等而選擇外殼3之形狀,但通 吊:夕數情形下,該外殼3之形狀為圓筒狀。可根據被處 理流體:分離成分之種類等而選擇外殼3之材質,例如亦 ::聚虱乙烯、聚碳酸酯、丙烯酸系聚合物、聚砜、聚醚 之塑膠、以及不鏽鋼等之金屬。通常於多數情形下, 使用不鏽鋼、f氣乙浠、以及聚硬等。尤其於用以製造釀 153942.doc •17· 201143876 造飲料之㈣組之,_時,自耐熱 性顧性強度)之觀 耐化子-性、耐麼 1愿較佳為使用不鏽鋼。 現以圓筒狀之外殼3j^丨2 綱 外殼3包括.^ 具體地對構造進行說明, 卜设3匕括.收谷濾筒模㈣之圓筒狀之 而組裝於主體體h,藉由螺合 备 a之兩舳之_對頂蓋扑,以及 ^由將頂蓋3b擰緊而夾持於該頂蓋外與主體 主 =::端部形成有成為濃縮水之排出口或原水之二 有成為原水之導入口=:致為圓錐狀,且於頂部形成 成k ’慮水之排出口等之管部3 e。 (遽筒模組之製造方法) 繼而參…、圖8對濾筒模組(膜模組”之製造方法 首先,執行對複數個中空纖維膜7a進行捆束而形成; 二纖維膜束7之步驟(步驟S1)。 具體而S ’包括:")以大致平行於長度方向之方式對特 定根數之中空纖維膜〜進行整理且予以統-之步驟;b)以 達到特定長度之方式而整齊地將中空纖維膜7a予以切斷之 步驟’以及c)將中空纖維膜7a之中空部堵塞之步驟。而且 亦可適當地進行d)對中空纖維膜7&之端部之細孔之開口度 進行調節之步驟。作為對開口度進行調節之方法,例如可 列舉形成如下狀態之方法,即,使甘油水溶液含浸於細孔 令之後進行乾燥’使細孔中含有甘油。上述a)〜d)之單位步 驟可以記載之順序進行,亦可適當地改變順序而進行。 繼而,執行模組前驅物要素之組裝步驟(步驟Μ)。具體 而。,將整束之中空纖維膜束7插入至保護構件1 1。繼 153942.doc 201143876 而’以均等地對中空纖維膜束7進行分割之方式,將十字 板13插入至自保護構件11露出之部分’以該狀態將頭蓋構 件9安裝於中空纖維膜束7之兩個端部,從而進行模組前驅 物要素之組裝。 繼而,執行將液狀之密封材料S填充至頭蓋構件9之内部 之步驟(步驟S3)。密封材料S之充填方法有利用離心力而 填充密封材料s之離心澆鑄法或利用重力而填充密封材料s 之靜置澆鱗法等,此處以離心澆鑄法與靜置澆鑷法為代表 而進行說明。 使用包括稱為離心盒之夾具之離心澆鑄機而進行離心澆 鑄法。將模組前驅物要素予以組裝而成之構造體係以水平 地橫臥之狀態而安裝於離心'盒,以紐垂軸為旋轉軸而於水 平面上旋轉。藉由離心盒之旋轉,離心力作用於頭蓋構件 9,利用該離心力而將密封材料8填充至頭蓋構件9之内 部。對於利用離心力之充填方法而言,例如根據中空纖維 膜束7之長度’可考慮如下之兩個方法。一個方法係同時 對兩個端部進行離4鑄之方法,另—個方法係於每一側 進:兩次離心_之方法。例如’ #於每—側進行兩次離 u ;鑄時,將成為接著對象之一端部配置成為離心方向之 將另—端部配置成為離心、方向之内側。利用離心力 液狀之雄、封材料S移送至成為離心方向 構件9側,進而,經由形成於頭蓋構件9之底部二= %而將密封材料S填充至内部。 之導入口 另方面,靜置洗鑄法係將安裝有頭蓋構件9之中空纖 J53942.doc •19- 201143876 維膜束7配置為沿鉛垂方向豎立之狀態。中空纖維膜束7之 成為接著對象之一端部處於下側,而另一端部處於上側。 液狀之密封材料S經由底部9b之導入口 9a而填充至下側之 頭蓋構件9之内部。此處,密封材料S藉由水頭差或泵等而 導入且無間隙地填充至頭蓋構件9之内部。其後,密封材 料S之流動性消失之後將上下反轉密封材料$與上述同 樣地填充至處於下側之頭蓋構件9之内部。 上述步驟S3中之密封材料s之充填係於密封材料s呈液狀 期間進行。再者,對於所填充之密封材料S而言,反應隨 時間而進行,該密封材料S之流動性逐步消失而成為固體 狀態。 繼而,執行使填充至頭蓋構件9之内部之密封材料s固化 而形成社封部15之步驟(步驟S4)。密封材料S固化而形成 密封部15之後,以特定溫度T1(例如5〇。〇加熱特定時間而 進行固化(步驟S5)。繼而,以高於丁丨之高溫T2(例如9〇β〇 加熱特定時間而進一步進行固化(步驟S6)。藉由上述操作 而完成模組前驅物5。 繼而,執行如下步驟,即,與中空纖維膜、之端部一併 將頭蓋構件9之底部9b側之一部分及密封部15之一部分予 以切斷’形成使複數個中空纖維膜7a之内部開放之模組端 面6(步驟S7),從而完成濾筒模組i。 繼而’對頭蓋構件9及遽筒模組r效果進行說明。當製 造模組前驅物5時,以將頭蓋構件9之内部之間隙予以=埋 之方式而填充密封材料S(參照圖5及圖6),進而使該密封 153942.doc -20· 201143876 材料S固化’將中空纖維膜束7、十字板"、保護構件"、 士頭蓋構件9之内表面予以接著(結合)。對於頭蓋構件9而 言,入口側筒部21之内徑大於端吾Μ則筒部23之内徑rl, 於入口侧筒部2 1與端部側筒部23之内表面彼此之間設置有 階差St。於密封材料S固化之過程中,密封材料8會稍微發 生熱收縮。藉由該熱收縮,假設即便於人π側筒部21處, 在與密封材料S之接觸面上產生剝離,自入口側筒部川則 朝向端部侧筒部23之剝離之傳播亦會受階差sm止,因 此’剝離之成長受到抑制。 又於頭蓋構件9之内表面形成有深槽23a或淺槽21a、 23b,密封材料8進入至深槽23&或淺槽21&、之几而固化。 因此’頭蓋構件9與密封材料s之接觸面彼此呈凹凸狀地嵌 。且牛固地接著(結合),從而對於抑制剝離之成長而言有 效,應對剝離之效果(不產生洩漏之效果)大,例如,亦可 财受滅g時之熱或壓力或者放射線處理。作為其結果,可 有助於使濾筒模組1之品質提高。 此外,於頭蓋構件9之入口側筒部21處形成有淺槽2ia, 於端部側筒部23處除形成有淺槽21a之外,亦形成有深槽 23a例如,形成於頭蓋構件9之内表面之槽之深度越深, 則密封材料S進入至越縱深之處且固化,因此,槽之深度 越冰,則上述密封材料s會越牢固地結合於頭蓋構件9,從 而於抑制剝離之方面有利。然而,對於自頭蓋構件9之底 部外側填充密封材料S之方法而言,與端部側筒部23相比 較,密封材料S更難以進入至入口側筒部2丨,因此,若使 153942.doc •21 · 201143876 入口側筒部21之槽過深’則密封材料8無法完全進入至入 口側筒部21,從而存在於密封材料s與頭蓋構件9之間產生 間隙之可能陡。另一方面,與入口側筒部2 i相比較,密封 材料s易於進入至端部側筒部23,因此,即便積極地使槽 之深度加深,亦可充分地使密封材料s進人。亦即,根據 頭蓋構件9,於自底部9b側填充密封材料8之情形時可確 實地填充密封材料S ’並且易於實現頭蓋構件9與密封材料 S之間之牢固之結合’ &而對於抑止剝離或抑制剝離之成 長而5有效。再者,於本實施形態之端部側筒部23處,處 形成有深槽23a之外’亦形成有淺槽23b,但亦可僅形成深 槽23a而不形成淺槽23b。 又於頭蓋構件9之端部側筒部23之内表面,形成有圍 繞頭蓋構件9之軸線L之環狀之第丨凸部23c及第2凸部23d。 密封材料S填充至頭蓋構件9之内部之後,將第i凸部23c及 第2凸部23d予以遮蓋。如上所述,密封材料s於固化之過 程中會發生熱收縮,但於該情形時將凸部Μcd予以 覆蓋之密封材料s係以包夾凸部23c、23(1之方式而發生收 縮,因此,可防止密封材料s固化過程中之剝離。作為其 …果於抑制剝離之成長而使濾筒模組1之品質提高之方 面有效。 又本實施形態之濾请模組1使用上述頭蓋構件9而形成 有頭蓋部la,因此,藉由使密封材料s固化而形成密封部 15時之剝離之產生及傳播受到抑制,從而可期待高品質。 又/慮疴模組1包括呈環狀地將中空纖維膜束7予以包圍 153942.doc -22- 201143876 之筒狀之保護構件u,因此,藉由保護構件丨丨而統一性良 好地保持中空纖維膜束7,保護該中空纖維膜束7不受外部 之衝擊等之影響。 又,於保護構件11,形成有自固定於頭蓋部1&之兩端部 朝軸線L方向突出之線狀(條狀)之突出部i lc。例如當藉由 無突出部1 lc之平坦之圓周而形成保護構件丨丨之端部時, 若於該端部產生剝離’則該剝離易於沿圓周方向傳播,剝 離易於成長。然而,根據本實施形態之保護構件丨丨,由於 突出部11c成為障礙物而阻止剝離朝圓周方向傳播,因 此’對於抑制剝離之成長而言有效。再者,可根據自製作 據筒模組1之步驟中之固化前後等之外觀所見的有無產生 剥離’而確認突出部丨丨c之效果。 又’即便當使用濾筒模組1而進行膜過濾時,例如亦存 在因物理清洗或化學品清洗等而導致頭蓋部la與密封部15 之間產生剝離之可能性。然而’於本實施形態中,由於頭 蓋部la與密封部15牢固地接著(結合),因此,可有效果地 防止剝離之產生,而且假設即便產生剝離時,亦可有效果 地抑制剝離之成長。 又’根據上述濾筒模組(膜模組)1之製造方法,於形成 密封部15之過程中,即便於頭蓋構件9之入口側產生剝 離’亦會藉由形成於入口侧筒部21之内表面與端部側筒部 23之内表面之間的階差st而阻止剝離自入口側筒部2丨側朝 端部側筒部23傳播。而且’由於填充至頭蓋構件9之内部 之密封材料S進入至環狀之淺槽21a、23b或深槽23a内而固 153942.doc -23- 201143876 化,因此,頭蓋構件9與密封材料8之接觸面彼此呈凹凸狀 地嵌合且牢固地接著(結合),從而對於抑制剝離之產生或 成長而言有效。作為其結果’可製造高品質之濾筒模組 1 ° 藉由上述製法而獲得之濾筒模組(膜模組)丨尤其於上述 釀造飲料之製造中,即便於反覆地進行高壓(二氧化碳氣 體壓力)且數°C (低溫)之過濾步驟與7crc (高溫)之清洗步驟 之苛刻之運轉環境下,亦不會於與密封材料s發生接觸之 内表面與填充至内部之密封材料S之間產生剝離而使原液 朝過渡側洩漏,可穩定地進行過濾。 [實施例] 以下,根據實施例及比較例而更具體地對本發明進行說 明,但本發明並不限定於以下之實施例。 (多孔質中空纖維膜之製造例1) 以70°c,於62重量%之冰甲基-2-吡咯烷酮中對18重量% 之聚礙(SOLVAY ADVANCED POLYMERS公司製造,Udel P3 5 00)、15重量0/〇之聚乙烯吡咯烷酮(BASF公司製造,In addition, the sealing material s is filled through the introduction port 9& which is formed outside the bottom of the head cover member 9, and the sealing material S is filled, for example, by a centrifugal casting method or a static casting method. The sealing material s filled into the inside of the head cover member 9 is solidified by the "sealing portion!" 5, thereby forming a module precursor 5. (Cylinder Module) As shown in FIG. 1, FIG. 4 and FIG. 7, the cartridge mold is manufactured using the module precursor 5 and (membrane module) 1 » the module precursor 5 is placed by the sealing portion 5 On the other hand, in the state in which both ends of the hollow fiber membrane 7a are blocked, and the completion of the cartridge module, it is necessary to form the end face 6 of the module in which both ends of the hollow fiber membrane are opened. In the present embodiment, the module end face 6 is formed by cutting off one of the end portions of the head cover member 9 (see Fig. 4 (4)), thereby completing the cartridge module i. The cartridge module 1 includes a plurality of hollow fiber membranes & hollow fiber membrane bundles 7 that are inserted into the head cover portion 1a by the head cover portion L 3 formed by the head cover member 9; the hollow fiber membrane bundle 7 is fixed to the hollow fiber membrane bundle 7 a sealing portion 15 of the head cover portion 1 & a module end face 6 for opening the inside of the hollow fiber membrane 7 & and a cylindrical good-preserving member ii 'to enclose the hollow fiber membrane bundle 7 in an annular shape, and the hollow fiber membrane The bundle 7 is fixed to the head cover portion by the sealing portion 15, and the cartridge module 1 is inserted into the outer casing 3 and detachably mounted, thereby constituting the filtration membrane unit. The shape of the outer casing 3 can be selected depending on the use, etc., but the outer casing 3 has a cylindrical shape. The material of the outer casing 3 may be selected depending on the fluid to be treated, the type of the separated component, and the like, and is, for example, a metal such as polystyrene, polycarbonate, acrylic polymer, polysulfone, polyether, or stainless steel. In most cases, stainless steel, f gas, and polyhard are generally used. Especially for the production of 153942.doc •17·201143876 Beverages (Group 4), _, from the viewpoint of heat resistance, resistance, resistance, resistance, and resistance 1 It is preferable to use stainless steel. Now, the cylindrical outer casing 3j^丨2 outer casing 3 includes a concrete structure, and the cylindrical structure of the receiving filter cylinder mold (4) is assembled to the main body h by The two parts of the screw assembly a are attached to the top cover 3b and are clamped to the outside of the top cover and the main body of the main body::: the end portion is formed as a discharge port for concentrated water or raw water. There is an inlet port that becomes raw water =: a tube portion 3 e which is formed into a conical shape and formed into a discharge port of k 'water. (Manufacturing method of the cartridge module) Next, the manufacturing method of the cartridge module (membrane module) of FIG. 8 is first performed by bundling a plurality of hollow fiber membranes 7a; Step (Step S1). Specifically, S' includes: ") a step of arranging and arranging a specific number of hollow fiber membranes in a manner substantially parallel to the length direction; b) in a manner to achieve a specific length The step of cutting the hollow fiber membrane 7a neatly, and the step of clogging the hollow portion of the hollow fiber membrane 7a, and appropriately performing the opening of the pores of the end portion of the hollow fiber membrane 7& In the method of adjusting the degree of opening, for example, a method of forming a state in which a glycerin aqueous solution is impregnated into a pore and then drying is performed, and glycerin is contained in the pores. The above a) to d The unit steps can be performed in the order described, or can be appropriately changed. Then, the assembly steps of the module precursor elements are performed (step Μ). Specifically, the bundle of hollow fiber membrane bundles 7 is Into the protective member 1 1. Following the 153942.doc 201143876 and 'dividing the hollow fiber membrane bundle 7 equally, inserting the cross plate 13 into the exposed portion of the self-protecting member 11' installs the head cover member 9 in this state. The assembly of the module precursor elements is performed at both ends of the hollow fiber membrane bundle 7. Then, the step of filling the liquid sealing material S into the inside of the head cover member 9 is performed (step S3). The filling method includes a centrifugal casting method in which the sealing material s is filled by centrifugal force, a static casting method in which the sealing material s is filled by gravity, and the like. The centrifugal casting method and the standing pouring method are mainly described. The centrifugal casting method is used for the centrifugal casting machine of the clamp of the centrifugal box. The structural system in which the module precursor elements are assembled is mounted horizontally on the centrifugal 'box, with the vertical axis as the rotation axis. Rotating on a horizontal plane, centrifugal force acts on the head cover member 9 by the rotation of the centrifugal box, and the sealing material 8 is filled into the inside of the head cover member 9 by the centrifugal force. For the filling method of the centrifugal force, for example, according to the length of the hollow fiber membrane bundle 7, two methods can be considered. One method is to simultaneously cast the two ends from the four casting methods, and the other method is on each side. In the case of two centrifugation methods, for example, '# every two sides are separated from u; when casting, one end of the object to be placed is placed in the centrifugal direction, and the other end is placed in the inner side of the centrifugation and direction. The liquid material is transferred to the side of the centrifugal direction member 9 by the centrifugal force, and the sealing material S is filled into the inside via the bottom portion 2 of the head cover member 9. The introduction port is additionally placed on the inside. The system is equipped with a hollow fiber J53942.doc • 19- 201143876 with a head cover member 9 configured to be erected in the vertical direction. One end of the hollow fiber membrane bundle 7 which becomes the next object is on the lower side, and the other end is on the upper side. The liquid sealing material S is filled into the inside of the lower head cover member 9 via the introduction port 9a of the bottom portion 9b. Here, the sealing material S is introduced by a head difference, a pump, or the like, and is filled into the inside of the head cover member 9 without a gap. Thereafter, after the fluidity of the sealing material S disappears, the upper and lower reverse sealing material $ is filled in the same manner as described above to the inside of the lower head cover member 9. The filling of the sealing material s in the above step S3 is performed while the sealing material s is in a liquid state. Further, with respect to the filled sealing material S, the reaction proceeds with time, and the fluidity of the sealing material S gradually disappears to become a solid state. Then, the step of solidifying the sealing material s filled in the inside of the head cover member 9 to form the sealing portion 15 is performed (step S4). After the sealing material S is solidified to form the sealing portion 15, the curing is performed at a specific temperature T1 (for example, 5 〇. 〇 heating for a specific time (step S5). Then, the temperature is higher than the high temperature T2 of the butyl enthalpy (for example, 9 〇 β 〇 heating specific The curing is further carried out in time (step S6). The module precursor 5 is completed by the above operation. Then, the following steps are performed, that is, one portion of the end portion of the hollow fiber membrane and the bottom portion 9b of the head cover member 9 And a part of the sealing portion 15 is cut "to form a module end face 6 that opens the inside of the plurality of hollow fiber membranes 7a (step S7), thereby completing the cartridge module i. Then the 'head cover member 9 and the cartridge module The effect of the r is explained. When the module precursor 5 is manufactured, the sealing material S is filled with the gap between the inside of the head cover member 9 (see Figs. 5 and 6), and the seal 153942.doc - 20· 201143876 Material S solidified 'The inner surface of the hollow fiber membrane bundle 7, the cross plate", the protective member", the head cover member 9 is then joined (bonded). For the head cover member 9, the inlet side tubular portion 21 Inner diameter is larger than Duanwu The inner diameter rl of the tubular portion 23 is provided with a step St between the inner surfaces of the inlet-side tubular portion 21 and the end-side tubular portion 23. During the curing of the sealing material S, the sealing material 8 may slightly occur. By the heat shrinkage, it is assumed that even if the human π side tubular portion 21 is peeled off at the contact surface with the sealing material S, the peeling from the inlet side tubular portion toward the end side tubular portion 23 is spread. Also, the step sm is stopped, so that the growth of the peeling is suppressed. Further, the inner surface of the head cover member 9 is formed with deep grooves 23a or shallow grooves 21a, 23b, and the sealing material 8 enters the deep groove 23 & or the shallow groove 21 & Therefore, the contact surfaces of the head cover member 9 and the sealing material s are embedded in a concavo-convex shape, and the cows are solidly bonded (bonded), thereby being effective for suppressing the growth of peeling, and the effect of peeling off (not The effect of causing a leak is large, for example, heat or pressure or radiation treatment when the gas is destroyed. As a result, the quality of the cartridge module 1 can be improved. Further, the entrance of the head cover member 9 A shallow groove 2ia is formed at the side tubular portion 21 at the end In addition to the shallow groove 21a formed in the side tube portion 23, a deep groove 23a is formed, for example, the deeper the groove formed on the inner surface of the head cover member 9, the deeper the sealing material S enters and solidifies. Therefore, the more the depth of the groove is iced, the stronger the above-mentioned sealing material s is bonded to the head cover member 9, thereby being advantageous in suppressing peeling. However, for the method of filling the sealing material S from the outside of the bottom of the head cover member 9 The sealing material S is more difficult to enter the inlet-side tubular portion 2 than the end-side tubular portion 23, and therefore, if the groove of the inlet-side tubular portion 21 is 153942.doc • 21 · 201143876 is too deep, the sealing material 8 It is impossible to completely enter the inlet side cylindrical portion 21, so that there is a possibility that a gap is generated between the sealing material s and the head cover member 9. On the other hand, the sealing material s easily enters the end side tubular portion 23 as compared with the inlet side tubular portion 2i. Therefore, even if the depth of the groove is actively deepened, the sealing material s can be sufficiently introduced. That is, according to the cover member 9, when the sealing material 8 is filled from the bottom portion 9b side, the sealing material S' can be surely filled and the firm bonding between the head cover member 9 and the sealing material S can be easily achieved. Peeling or inhibiting the growth of peeling is effective. Further, in the end portion side tubular portion 23 of the present embodiment, the shallow groove 23b is formed in the outer side of the deep groove 23a. However, only the deep groove 23a may be formed without forming the shallow groove 23b. Further, on the inner surface of the end portion side tubular portion 23 of the head cover member 9, an annular second convex portion 23c and a second convex portion 23d which surround the axis L of the head cover member 9 are formed. After the sealing material S is filled into the inside of the head cover member 9, the i-th convex portion 23c and the second convex portion 23d are covered. As described above, the sealing material s undergoes heat shrinkage during the curing process, but in this case, the sealing material s covering the convex portion Μcd shrinks by sandwiching the convex portions 23c and 23 (1). It is possible to prevent the peeling of the sealing material s during the curing process, and it is effective in suppressing the growth of the peeling and improving the quality of the cartridge module 1. The filter module 1 of the present embodiment uses the above-described head cover member 9 Since the head cover portion 1a is formed, the generation and spread of the peeling when the sealing portion 15 is formed by curing the sealing material s are suppressed, and high quality can be expected. Further, the module 1 includes an annular shape. The hollow fiber membrane bundle 7 surrounds the cylindrical protective member u of 153942.doc -22- 201143876, and therefore, the hollow fiber membrane bundle 7 is uniformly maintained by the protective member ,, and the hollow fiber membrane bundle 7 is protected. In addition, the protective member 11 is formed with a linear (stripe) protruding portion i lc that is fixed to the both end portions of the head cover portion 1 & No protrusion 1 lc When the end portion of the protective member is formed on the flat circumference, if peeling occurs at the end portion, the peeling tends to propagate in the circumferential direction, and the peeling tends to grow. However, according to the protective member of the present embodiment, the protruding portion 11c becomes an obstacle and prevents peeling from propagating in the circumferential direction, so it is effective for suppressing the growth of peeling. Further, peeling can be caused by the presence or absence of appearance before and after curing in the step of manufacturing the cartridge module 1. Further, the effect of the protruding portion 丨丨c is confirmed. Further, even when the membrane filtration is performed using the cartridge module 1, for example, peeling occurs between the head cover portion 1a and the sealing portion 15 due to physical cleaning or chemical cleaning. However, in the present embodiment, since the head cover portion 1a and the sealing portion 15 are firmly joined (bonded), the occurrence of peeling can be effectively prevented, and even if peeling occurs, it is effective. The growth of the peeling is suppressed. Further, according to the manufacturing method of the cartridge module (membrane module) 1, in the process of forming the sealing portion 15, even in the head cover The peeling of the inlet side of the member 9 also prevents the peeling from the side of the inlet side tubular portion 2 by the step st formed between the inner surface of the inlet side cylindrical portion 21 and the inner surface of the end side tubular portion 23 The end side tubular portion 23 is propagated. And 'the sealing material S filled into the inner portion of the head cover member 9 enters into the annular shallow groove 21a, 23b or the deep groove 23a, and is solidified, therefore, 153942.doc -23-201143876 The contact faces of the head cover member 9 and the sealing material 8 are fitted in a concavo-convex shape and firmly adhered (bonded), thereby being effective for suppressing generation or growth of peeling. As a result, a high-quality filter cartridge module can be manufactured. 1 ° The filter cartridge module (membrane module) obtained by the above-described production method, in particular, in the manufacture of the above-mentioned brewed beverage, even in the case of repeatedly performing high pressure (carbon dioxide gas pressure) and several ° C (low temperature) filtration steps and In the harsh operating environment of the 7crc (high temperature) cleaning step, no peeling occurs between the inner surface in contact with the sealing material s and the sealing material S filled in the inner portion, so that the raw liquid leaks toward the transition side, and the ground can be stably get on Filter. [Examples] Hereinafter, the present invention will be specifically described based on examples and comparative examples, but the present invention is not limited to the following examples. (Production Example 1 of Porous Hollow Fiber Membrane) 18% by weight of chloroformyl-2-pyrrolidone in 62% by weight (manufactured by SOLVAY ADVANCED POLYMERS, Udel P3 5 00), 15 0/〇polyvinylpyrrolidone (manufactured by BASF Corporation,

Luvitec k80)進行攪拌且使其溶解,添加5重量%之甘、、由, 進一步進行攪拌,製備製膜原液。以7〇t將該製膜原液| 作為内部凝固液之90重量%之NMP水溶液一併自雙環妨綠 喷嘴(最外徑為2.4 mm ’中間徑為1.2 mm,最内徑為〇 6 mm)擠出,經過50 mm之自由流動距離,於8〇〇Γ l爻水中凝 固。此時,自紡口至凝固浴為止係由可對溫度進行調整且 底面積為38 cm2之筒狀物包圍,且將自由流動部八 刀疋溫度 153942.doc • 24· 201143876 設為75°C,將相對濕度設為100%(絕對濕度240 g/m3)。此 時’於水中進行去溶劑之後,於2〇〇〇 ρριη之次氣酸鈉水溶 液中’以15小時對聚乙烯吡咯烷酮進行分解處理之後,以 90 C進行水洗3小時,獲得多孔質中空纖維膜。所獲得之 中空纖維之外徑為2_3 mm #,内徑為1.4 mm《,最小孔經 為0.4 μηι ’ 25°C時之每平方米内表面積之純水透過量為 15800 L/m2/hr/100 kPa。將該中空纖維膜浸潰於6〇°C之30 重量/〇之甘油水溶液中,使甘油水溶液含浸於中空纖維膜 之細孔之後’以70。(:進行乾燥以製造膜模組。 (多孔質中空纖維膜之製造例2) 以50°C,於71重量%之二曱基乙醯胺中對2〇重量0/〇之聚 礙(SOLVAY ADVANCED POLYMERS 公司製造,Udel P3 500)、9重量%之四乙二醇(日本觸媒公司製造)進行攪拌 且使其溶解,製備製膜原液。以50〇c將該製膜原液與作為 内部凝固液之純水一併自雙環紡絲噴嘴(最外徑為24 mm,中間徑為1.2 mm,最内徑為0 6 mm)擠出,經過1〇 mm之自由流動距離,於30〇c之水中凝固。此時,於水中 進行去溶劑之後,以90T:進行水洗3小時,獲得多孔質中 空纖維膜。所獲得之中空纖維之外徑為2 3 mm 0,内徑為 1.4 mm#,區分分子量為6000,25^時之每平方米内表面 積之純水透過量為250 L/m2/hr/100 kPa。將該中空纖維膜 浸潰於60°C之30重量%甘油水溶液中,使甘油水溶液含浸 於中空纖維膜之細孔之後,以70»C進行乾燥以製造膜模 153942.doc •25- 201143876 (中空纖維膜模組之製造例) 使用下述之—體地成形有底部與筒狀體之頭蓋構件與網 狀保護筒*製造據筒型中空纖維膜模組。 《模組構造》 (1)頭蓋構件 材質:聚頌1 (透明) 入口側筒部:高度(内尺寸)28 mm,Luvitec k80) was stirred and dissolved, and 5 wt% of sugar was added thereto, and further stirred to prepare a film forming stock solution. The film preparation stock solution at 7 〇t is used as a 90% by weight aqueous solution of NMP in the internal coagulating liquid from the double-loop green nozzle (the outermost diameter is 2.4 mm 'the intermediate diameter is 1.2 mm, and the inner diameter is 〇6 mm) Extrusion, after a free flow distance of 50 mm, solidified in 8 〇〇Γ l爻 water. At this time, from the spinning port to the coagulation bath, it is surrounded by a cylinder which can adjust the temperature and has a bottom area of 38 cm2, and the free-flowing portion of the eight-knife temperature 153942.doc • 24· 201143876 is set to 75 ° C. Set the relative humidity to 100% (absolute humidity 240 g/m3). At this time, after desolvation in water, the polyvinylpyrrolidone was decomposed in an aqueous sodium hypochlorite solution of 2 〇〇〇ρριη for 15 hours, and then washed with water at 90 C for 3 hours to obtain a porous hollow fiber membrane. . The obtained hollow fiber has an outer diameter of 2_3 mm # and an inner diameter of 1.4 mm. The minimum pore permeation is 0.4 μηι ' at 25 ° C. The permeation per square meter of internal surface area is 15800 L/m2/hr/100. kPa. The hollow fiber membrane was impregnated into a 30 wt/3 glycerin aqueous solution at 6 °C to impregnate the pores of the hollow fiber membrane with an aqueous solution of glycerin at 70. (: Drying to produce a membrane module. (Production Example 2 of porous hollow fiber membrane) At 50 ° C, in 2 wt% of decyl acetamidine, the weight of 2 〇 0 / 〇 (SOLVAY) Manufactured by ADVANCED POLYMERS, Udel P3 500), 9% by weight of tetraethylene glycol (manufactured by Nippon Shokubai Co., Ltd.), and dissolved to prepare a film-forming stock solution. The film-forming stock solution was coagulated at 50 〇c. The pure water of the liquid is extruded from a double-ring spinning nozzle (the outer diameter is 24 mm, the intermediate diameter is 1.2 mm, and the inner diameter is 0 6 mm). After a free flow distance of 1 mm, at 30 〇c In this case, after desolvation in water, the mixture was washed with water at 90T for 3 hours to obtain a porous hollow fiber membrane. The obtained hollow fiber had an outer diameter of 2 3 mm 0 and an inner diameter of 1.4 mm#. The pure water permeation amount per square meter of the molecular weight of 6000, 25 ^ is 250 L / m2 / hr / 100 kPa. The hollow fiber membrane is impregnated in a 30% by weight aqueous solution of glycerin at 60 ° C to make an aqueous glycerin solution After impregnation of the pores of the hollow fiber membrane, drying at 70»C to produce a membrane mold 153942.doc • 25- 201143876 (Manufacturing example of hollow fiber membrane module) The hollow fiber membrane module is manufactured using the head cover member and the mesh protection cylinder* which are formed with the bottom and the cylindrical body as follows. Construction" (1) Head cover member material: Poly 颂 1 (transparent) Entrance side tube: height (inner size) 28 mm,

S 端部側筒部:高度(内尺寸)64 mm 入口側筒部以及端部側筒部之内徑、槽之形狀尺寸表示 於表 1以及表2中。 再者 j 藉由對聚硬製之材料(直徑200 mmx長度1000 進行 切 削加工而製作上述頭蓋構件 0 (2) 網 狀保護筒 材質 聚丙烯 形狀 内徑151 mm,外徑159 mm, 長度 1020 mm, 線寬 軸方向3.5 mm,圓周方向5 mm, 開口 部 8·5 mm(軸方向)xl2 mm(圓周 方向), 再者 轴方向之突起表示於表1以及表2中。 (3) 中 空纖維膜 材質 聚砜 尺寸 内徑1.4 mm ’外徑2.3 mm 根數 2800 根 膜面 積 :内表面積為12 m2/模組 (4) 十 字板 153942.doc -26- 201143876 性環氧樹脂(與密封材料相同之樹 材質·雙液混合型熱固 脂之固化物) 形狀:十字狀 度為148 mm,軸方向長度為 υν ill Hi 尺寸:厚度為 《製造方法》 預先使兩端之中空部 卩堵塞之中空纖維膜大致平行地對齊 且整理為束狀之後,將其切 丹刀斷為1280 mm。將該中空纖維 膜束插入至網狀保護筒,將十字板插人至自上述網狀保護 筒突出之中空纖維膜端部。此時,對十字板進行配置,使 得中空纖維膜均等地分配 %田十子板分成四部分之各區 域0 (實施例1〜8) 】而,將上述中空纖維臈束之兩端部插入至頭蓋構件内 之後將其载置於架台,將兩端部之頭蓋構件固定於架 。。其後’將上述架台安裝於離心盒,藉由離心澆鑄法而 將雙液混合型熱固性環氧樹脂之混合液自兩端部之頭蓋構 件之底側予以注入’且使之固化。繼而,以5(TC加執48小 時,進而以9代加熱16小時而使之固化之後,將兩個頭蓋 構件之底側端予㈣斷,使中空部形錢口。切斷之後之 頭蓋構件之長度為6〇 mm,模組全長為^⑽醜。 表示使用製造例1之多孔質中空纖維膜、與各種頭蓋構 件而製造之中空纖維膜模組之例子。頭蓋構件之形狀及尺 寸表示於表1中。 對所製造之膜模組中之中空部及切斷端面進行觀察。將 153942.doc -27- 201143876 觀察結果表示於··^ 1 + Γ 於表1中。再者,表1之「頭蓋構件之内徑 比」係私(鳊。[5側筒部之内徑)/(入口側筒部之内徑)。 於實施例8中’未觀察到剝離,但於入口側筒部之槽中 滞留有氣泡。 (比牧例1、 除使用表2所示之形狀以及尺寸之頭蓋構件與保護射 以外’與實施例1〜8同樣地製作模組’且與實施例同樣知 進行觀察。將觀察結果表示於表2中。對於比較例2之膜右 組而&,於製造之後之階段未發現剝離,但觀察到於設3 於入口側筒部之角槽内殘留有氣泡。再者,表2之 構件之内徑比」係指(端部側筒部之 内徑)小於比較例艸, 二 有實質性之槽,而且,於入口側筒:广之内表面未㈣ 實質性之槽。因此,認為表2中戶=之内表面亦未形成凑 入口側筒部之槽實質上為相同之深:之端部側筒部之槽病 對於端部側筒部之槽之平均深户^^入口側筒部之槽相 ^比記載為「1.0」。 153942.doc •28- 201143876 【1<】 εεο- uuu 〇9i ιυε 9 ~ϊ~~ IUE 〇·寸 UUU·—1 画001 ~~Ί~ εαι 〇·寸 ε£ ς·ι憋吡 εΕΟιηιΙ ΟΟΊ 寸 601 璣蒺难 鎳蒺碟S End side tube portion: height (inner size) 64 mm The inner diameter of the inlet side tube portion and the end portion side tube portion and the shape and size of the groove are shown in Table 1 and Table 2. Furthermore, j is made by grinding a polyhard material (diameter 200 mm x length 1000) to make the above-mentioned head cover member 0 (2) mesh protection cylinder material polypropylene shape inner diameter 151 mm, outer diameter 159 mm, length 1020 mm , the line width axis direction is 3.5 mm, the circumferential direction is 5 mm, the opening portion is 8·5 mm (axial direction) xl2 mm (circumferential direction), and the axial direction protrusions are shown in Table 1 and Table 2. (3) Hollow fiber Membrane material Polysulfone size inner diameter 1.4 mm 'Outer diameter 2.3 mm Number of roots 2800 Film area: Internal surface area is 12 m2/module (4) Cross plate 153942.doc -26- 201143876 Epoxy resin (same as sealing material) Tree material · Two-liquid mixed type thermosetting solidified material) Shape: The cross-degree is 148 mm, the axial length is υν ill Hi Dimensions: The thickness is "Manufacturing method" The hollow portion of the hollow ends is blocked in advance. After the fiber membranes are aligned substantially in parallel and arranged in a bundle shape, the cutting knife is cut into 1280 mm. The hollow fiber membrane bundle is inserted into a mesh protection cylinder, and the cross plate is inserted to protrude from the mesh protection cylinder. At the end of the hollow fiber membrane, at this time, the cross plate is disposed such that the hollow fiber membrane is evenly distributed to each of the four regions 10 (Examples 1 to 8), and the hollow fiber bundle is bundled. After the two end portions are inserted into the head cover member, they are placed on the gantry, and the head cover members at both ends are fixed to the frame. Thereafter, the gantry is mounted on the centrifugal box, and the two-liquid mixing is performed by centrifugal casting. The mixture of the thermosetting epoxy resin is injected into the bottom side of the head cover member at both ends and is solidified. Then, after 5 (TC is added for 48 hours, and then heated for 9 hours in the 9th generation to be cured, The bottom side ends of the two head cover members are (4) broken to make the hollow portion shaped. The length of the head cover member after cutting is 6 〇 mm, and the total length of the module is ^ (10) ugly. The porous hollow of the manufacturing example 1 is used. Examples of the hollow fiber membrane module manufactured by the fiber membrane and various head cover members. The shape and size of the head cover member are shown in Table 1. The hollow portion and the cut end surface of the manufactured membrane module were observed. .doc -27- 201143876 The results are shown in Table 1. In addition, the "inner diameter ratio of the head cover member" in Table 1 is private (鳊. [5 inner tube inner diameter) / (inlet side cylinder portion) "Inner diameter". In Example 8, 'no peeling was observed, but air bubbles were trapped in the groove of the inlet side tube portion. (Before the case 1, the head cover member and the protective shot except the shape and size shown in Table 2 were used. In the same manner as in the first to eighth embodiments, the module was produced in the same manner as in the examples. The observation results are shown in Table 2. With respect to the film right group of Comparative Example 2, no peeling was observed at the stage after the production, but it was observed that air bubbles remained in the corner grooves of the inlet side cylindrical portion. Furthermore, the inner diameter ratio of the members of Table 2 means that the inner diameter of the end side tubular portion is smaller than that of the comparative example, and the second has a substantial groove, and the inlet side cylinder: the inner surface is not (4) substantially Slot of sex. Therefore, it is considered that the inner surface of the household in Table 2 does not form the groove of the inlet side tubular portion substantially the same depth: the groove of the end side tubular portion is the average deep groove of the groove of the end side tubular portion ^ ^ The groove phase ratio of the inlet side tube portion is described as "1.0". 153942.doc •28- 201143876 [1<] εεο- uuu 〇9i ιυε 9 ~ϊ~~ IUE 〇·inch UUU·—1 painting 001 ~~Ί~ εαι 〇·inchε£ ς·ι憋py εΕΟιηιΙ ΟΟΊ inch 601 玑蒺 蒺 蒺 蒺

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[表2] 比較例1 比較2 内徑 160 mm 160 mm 入 槽形狀 無槽 角槽 口 側 筒 槽深度 0.0 mm 1.5 mm 槽寬 0.0 mm 4.0 mm 部 槽數 0 2 頭 蓋 槽間距 0 mm 6 mm 内徑 160 mm 160 mm 構 件 端 槽形狀 無槽 角槽 部 側 筒 槽深度 0.0 mm 1.5 mm 槽寬 0.0 mm 4.0 mm 部 槽數 0 2 槽間距 0 mm 18 mm 内徑比 1.00 1.00 槽平均深度之比 1.00 1.00 保護構件 端部之形狀 無突出部 無突出部 剝 離心澆鑄之後之狀況 有剝離 無剝離 離 產 生 狀 50°C固化之後之狀況 有剝離 無剝離. 90°C固化之後之狀況 有剝離 無剝離 切斷之後之狀況 有剝離 無剝離 況 綜合判斷 NG OK (實施例9) 以下,表示進行冷熱循環測試所得之結果。 將與實施例1〜6同樣地製造之膜模組收納於不鏽鋼製外 殼之後,將該不鏽鋼製外殼安裝於過濾裝置,將於2小時 内通入冷卻至5°C之純水之步驟與於2小時内通入加熱至 80°C之純水之步驟重複1 〇〇〇個循環。再者,於該冷熱循環 測試中,將入口處之壓力設定為0.2 MPa,將透過側出口 處之壓力設定為0.15 MPa,以交叉流過濾方式通入上述純 水。 直至測試結束(1000個循環)為止之期間,每隔100個循 153942.doc •30- 201143876 環’以後述之方法推a 為止,各膜模組均完==查時’直至1000個循環結束 模組取出,詳細地對頭二漏。又,自外殼將令空纖維膜 未發現剝離。、h㈣行觀察時,於各膜模組中均 《泡漏檢查方法》[Table 2] Comparative Example 1 Comparison 2 Inner diameter 160 mm 160 mm In-groove shape No groove angle Notch Side groove depth 0.0 mm 1.5 mm Groove width 0.0 mm 4.0 mm Number of grooves 0 2 Head cover groove pitch 0 mm 6 mm Diameter 160 mm 160 mm Member end groove shape grooveless groove groove side groove depth 0.0 mm 1.5 mm groove width 0.0 mm 4.0 mm groove number 0 2 groove pitch 0 mm 18 mm inner diameter ratio 1.00 1.00 groove average depth ratio 1.00 1.00 The shape of the end of the protective member is free of protrusions. There is no protrusion. The condition after peeling is cast. There is no peeling and peeling off. The condition after curing at 50 ° C is peeled off without peeling. After curing at 90 ° C, there is peeling and peeling. In the case after the break, there was a peeling and no peeling condition. Comprehensive judgment NG OK (Example 9) Hereinafter, the results obtained by performing the cooling and heating cycle test are shown. After the film module manufactured in the same manner as in Examples 1 to 6 was housed in a stainless steel case, the stainless steel case was attached to a filter device, and the step of cooling to 5 ° C of pure water was carried out within 2 hours. The step of heating to 80 ° C of pure water was repeated for 1 hour and repeated for 1 cycle. Further, in the hot and cold cycle test, the pressure at the inlet was set to 0.2 MPa, and the pressure at the outlet side outlet was set to 0.15 MPa, and the above pure water was introduced by cross-flow filtration. Until the end of the test (1000 cycles), every 100 cycles of 153942.doc •30-201143876 ring 'described later, push a, each membrane module is finished == check time' until 1000 cycles end The module is taken out and the first two leaks in detail. Also, no peeling of the hollow fiber membrane was observed from the outer casing. , h (four) line observation, in each membrane module are "bubble inspection method"

將空氣導入至外M 0.3略,觀察纖維膜外表面側加壓至 内表面否料模組端面。#於頭蓋構件之 内表面4產生剝離, 5亥剝離邠自固定部之内側朝外側貫 通夺’ *氣自該剝離部分漏出。 (實施例10) 除使用與實施例7同樣地製造之膜模組 同樣地進行冷熱循環測試。 〃貫施例9 與貫施例9同樣地,每隔1〇〇個循環進行茂漏檢查時,直 至1000個循環結束為止完全無洩漏。繼而,自外殼中將中 空纖維膜模組取出,# 對碩蓋。卩進行觀察時,於頭蓋構件 階差部分處之侔嘈姐μ Α Τ^ 保濩構件與頭蓋構件之接觸面附近產生剝 又,改變為將於2小時内通入冷卻至之純水之步驟與 於2]時内通入加熱至40°c之純水之步驟予以重複,除此 之卜肖實施例9同樣地進行冷熱循環測試。 每隔10◦個猶環進行茂漏檢查時,直至1000個循環結束 為止疋全無攻漏。繼而,與上述同樣地對頭蓋部進行觀察 〃 V "’、循%測試之前相比較無變化,且亦未發現 離。 153942.doc 201143876 (實施例11) 除使用與實施例8同樣地製造之膜模組之外,與實施例9 同樣地進行冷熱循環測試。 與實施例9同樣地,每隔100個循環進行洩漏檢查時,直 至1000個循環結束為止完全無洩漏。繼而,自外殼中將中 空纖維膜模組取出,對頭蓋部進行觀察時,於頭蓋構件之 入口側筒部之接著部界面觀察到輕微之間隙(已剝離之部 分)。該剝離部止於階差部。推測該剝離係以滯留於設置 在入口側筒部之角槽内之氣泡之部分為起點而產生,且自 入口側筒部之入口端發展至階差部為止。 又,改變為將於2小時内通入冷卻至5它之純水之步驟與 於2小時内通入加熱至4〇°C之純水之步驟予以重複,除此 之外’與實施例9同樣地進行冷熱循環測試時,完全無茂 漏。又,對頭蓋部進行觀察時,與冷熱循環測試之前相比 較無變化,且亦未發現剝離。 (比較例3) 與比較例2同樣地製造膜模組。該膜模組於製造之後之 階段,完全未發現剝離。然而,於設置於入口側筒部之角 槽内殘留有氣泡。 除使用上述膜模組之外’與實施例9同樣地進行冷熱循 環測試。 與實施例9同樣地,每隔1 〇〇個循環進行洩漏檢查時,於 100循環之後無洩漏,但於200循環之後產生茂漏。 繼而’自外殼中將中空纖維膜模組取出,對頭蓋部進行 -32- 153942.docThe air was introduced to the outer M 0.3 slightly, and the outer surface side of the fiber membrane was observed to be pressed to the inner surface of the module end face. # The inner surface 4 of the head cover member is peeled off, and the 5 kel peeling detachment from the inner side of the fixed portion to the outside is leaked from the peeling portion. (Example 10) A thermal cycle test was carried out in the same manner as in the film module produced in the same manner as in Example 7. Example 9 In the same manner as in Example 9, when the leak inspection was performed every one cycle, there was no leakage until the end of 1000 cycles. Then, the hollow fiber membrane module is taken out from the outer casing, #对对盖盖.卩When observing, the peeling of the contact surface between the 侔嘈 μ Α Τ 濩 濩 濩 濩 濩 濩 与 与 与 与 与 与 与 与 与 , , 产生 产生 产生 产生 产生 产生 产生 产生 产生 产生 产生 产生 产生 产生The procedure of heating to 40 ° C of pure water was repeated in the same manner as in 2), except that Example 9 was subjected to a thermal cycle test in the same manner. When the leak detection is carried out every 10 犹 环 ring, until the end of 1000 cycles, there is no leakage. Then, the head cover portion was observed in the same manner as above, 〃 V "', and there was no change before the % test, and no difference was found. 153942.doc 201143876 (Example 11) A hot and cold cycle test was performed in the same manner as in Example 9 except that the film module manufactured in the same manner as in Example 8 was used. In the same manner as in the ninth embodiment, when the leak inspection was performed every 100 cycles, there was no leakage until the end of 1000 cycles. Then, the hollow fiber membrane module was taken out from the outer casing, and when the head cover portion was observed, a slight gap (the peeled portion) was observed at the interface of the entrance portion of the inlet-side tubular portion of the head cover member. The peeling portion ends at the step portion. It is presumed that the peeling is generated starting from the portion of the bubble which is retained in the corner groove of the inlet-side tubular portion, and proceeds from the inlet end of the inlet-side tubular portion to the step portion. Further, it is changed to a step of introducing cooling water to 5 of its pure water within 2 hours and a step of introducing pure water heated to 4 ° C for 2 hours, except for 'with Example 9' When the thermal cycle test is performed in the same manner, there is no leakage at all. Further, when the head cover portion was observed, there was no change compared with that before the hot and cold cycle test, and no peeling was observed. (Comparative Example 3) A film module was produced in the same manner as in Comparative Example 2. At the stage after the manufacture of the film module, no peeling was found at all. However, air bubbles remain in the corner grooves provided in the inlet side cylindrical portion. The hot and cold cycle test was carried out in the same manner as in Example 9 except that the above film module was used. In the same manner as in Example 9, when the leak inspection was performed every one cycle, no leakage occurred after 100 cycles, but a leak occurred after 200 cycles. Then, the hollow fiber membrane module is taken out from the outer casing, and the head cover portion is subjected to -32-153942.doc

S 201143876 觀察時,自頭蓋構件之入口側筒部之接著部界面至端部側 筒部之切斷端面為止連續地觀察到間隙(已剝離之部分)。 推測該剝離係以滞留於設置在入口側筒部之角槽内之氣泡 之部分為起點而產生,且自入口側筒部之入口端發展至切 斷端面為止。 又’改變成將於2小時内通入冷卻至5它之純水之步驟與 於2小時内通入加熱至4(rc之純水之步驟予以重複,除此 之外,與貫施例9同樣地進行冷熱循環測試時,直至$〇〇個 循環之後為止無洩漏’但於6〇〇個循環之後產生洩漏。 如上所述,對於將於2小時内通入冷卻至5〇c之純水之步 驟與於2小時内通入加熱至8〇°C之純水之步驟重複2〇〇個循 環之後無洩漏的膜模組而言’即便重複1 〇〇〇個循環,亦不 會產生洩漏。另一方面,如比較例3所示,即便於製造之 後未觀察到剝離’當上述冷熱循環不足2〇〇個循環時亦產 生洩漏。因此,對於在上述冷熱循環測試中,於2〇〇個循 環之後無洩漏之膜模組而言,於實際運用方面,可無問題 地使用。 (實施例12) 以下,表示於高壓下進行冷熱循環測試所得之結果。 除使用製造例2之多孔質中空纖維膜之外,與實施例 同樣地製造膜模組。於製造之後,觀察到各膜模組均完全 無剝離。 繼而’將入口處之壓力設定為0.5 MPa,將透過側出口 處之壓力s免疋為0.3 MP a ’除此之外’與實施例9同樣地進 153942.doc -33- 201143876 行冷熱循環測試。與實施例9同樣地,每隔丨〇〇個循環進行 茂漏檢查時,直至1000個循環結束為止,各膜模組均完全 無洩漏。又,自外殼中將中空纖維膜模組取出,詳細地對 頭蓋部進行觀察時,均未發現各膜模組產生剝離。 如上所述,即便於如釀造飲料之過濾中所暴露的高壓下 反覆進行低溫之步驟與高溫之步驟之苛刻的運轉環境下, 亦可不引起剝離而進行使用。 【圖式簡單說明】 圖1係本發明之實施形態之濾筒模組之製造中所使用之 膜模組前驅物的分解立體圖。 圖2係表示本實施形態之頭蓋構件之圖’圖2(a)係底視 圖’圖2(b)係沿圖2(a)之b-b線之剖面圖。 圖3係表示圓筒狀之保護構件之圖,圖3(幻係側視圖,圖 3(b)係沿圖3(a)之b-b線之局部剖面圖。 圖4係表示模組前驅物之圖,圖4(a)係側視圖,圖4(b)係 沿圖4(a)之b_b線之剖面圖,圖4(c)係沿圖4(a)之c_c線之剖 面圖且表示模組端面。 圖5係放大表示插入有中空纖維膜束之狀態下的頭蓋構 件之入口側的剖面圖。 圖6係表示將接著材料填充至頭蓋構件之内部之途中之 狀態的放大剖面圖。 圖7係用以對將濾筒模組安裝於外殼之形態進行說明之 分解立體圖。 圖8係表示製造濾筒模組之順序之流程圖。 153942.docS 201143876 When observed, the gap (the peeled portion) was continuously observed from the joint interface of the inlet side tubular portion of the head cover member to the cut end surface of the end side tubular portion. It is presumed that the peeling is generated from the portion of the bubble which is retained in the angular groove provided in the inlet-side tubular portion, and proceeds from the inlet end of the inlet-side tubular portion to the cut end face. Also, 'change to a step of cooling to 5 of its pure water within 2 hours and repeating the step of heating to 4 (r pure water in 2 hours), in addition to the example 9 In the same hot and cold cycle test, there is no leakage until after one cycle. 'But after 6 cycles, a leak occurs. As mentioned above, for pure water that will be cooled to 5〇c within 2 hours. The step is to repeat the process of heating to 8 〇 ° C of pure water within 2 hours. After repeating 2 循环 cycles, the leak-free membrane module will not leak even if it repeats 1 cycle. On the other hand, as shown in Comparative Example 3, no peeling was observed even after the production. When the above-mentioned cold heat cycle was less than 2 cycles, a leak occurred. Therefore, in the above-mentioned hot and cold cycle test, at 2〇〇 The membrane module which has no leakage after the cycle can be used without any problem in practical use. (Example 12) Hereinafter, the results obtained by performing the thermal cycle test under high pressure are shown. In addition to hollow fiber membranes, and examples The membrane module was fabricated in the sample. After the manufacture, it was observed that each membrane module was completely free of peeling. Then the pressure at the inlet was set to 0.5 MPa, and the pressure s at the outlet side was reduced to 0.3 MP a ' In the same manner as in the ninth embodiment, 153942.doc -33 - 201143876 was subjected to the hot and cold cycle test. In the same manner as in the ninth embodiment, the leak test was performed every other cycle until the end of 1000 cycles. Each of the membrane modules was completely leak-free. Further, the hollow fiber membrane module was taken out from the outer casing, and when the head cover portion was observed in detail, no peeling of each membrane module was observed. As described above, even if a brewed beverage In the harsh operating environment in which the high temperature step and the high temperature step are repeated under the high pressure exposed in the filtration, the peeling may be used without any peeling. [Fig. 1] Fig. 1 is a filter cartridge mold according to an embodiment of the present invention. Fig. 2 is a perspective view showing the head cover member of the present embodiment. Fig. 2(a) is a bottom view of Fig. 2(b) is shown in Fig. 2(a) A cross-sectional view of the bb line. 3 is a view showing a cylindrical protective member, FIG. 3 (a side view of the magical system, and FIG. 3(b) is a partial cross-sectional view taken along line bb of FIG. 3(a). FIG. 4 is a view showing a precursor of the module. Fig. 4(a) is a side view, Fig. 4(b) is a cross-sectional view taken along line b_b of Fig. 4(a), and Fig. 4(c) is a cross-sectional view taken along line c_c of Fig. 4(a) and showing a mode Fig. 5 is an enlarged cross-sectional view showing the inlet side of the head cover member in a state in which the hollow fiber membrane bundle is inserted. Fig. 6 is an enlarged cross-sectional view showing a state in which the adhesive material is filled in the middle of the head cover member. 7 is an exploded perspective view for explaining a state in which a cartridge module is attached to a casing. Fig. 8 is a flow chart showing the sequence of manufacturing a cartridge module. 153942.doc

S •34- 201143876 圖9係用以對本發明中之槽之形態進行說明之剖面圖, 圖9(a)係角槽之剖面圖,圖9(b)係三角槽之剖面圖,圖9(c) 係圓槽之剖面圖,圖9(d)係V字狀槽之剖面圖,圖9(e)係筒 端凹槽之剖面圖。 【主要元件符號說明】 1 濾筒模組(膜模組) la 頭蓋部 3 外殼 3a 主體 3b 頂蓋 3c 密封環 3d ' 3e 管部 5 模組前驅物 6 模組端面 7 中空纖維膜束 7a 中空纖維膜 9 頭蓋構件 9a 導入口 9b 、 23f 底部 11 保護構件 11a 縱條部 lib 圈狀部 11c 突出部 13 十字板 153942.doc -35- 201143876 13a 間隔片 15 密封部 21 入口側筒部 21a ' 23b 淺槽 23 端部側筒部 23a 深槽 23c 第1凸部 23d 第2凸部 23e 主體部 25 座面 b-b 、 c-c 線 dl ' d2 平均深度 H 保護構件之贯通孔 L 軸線 ri 入口側筒部之内徑 r2 端部側筒部之内徑 S 密封材料 St 階差 SI 〜S7 步驟 153942.doc 36-S.34-201143876 Fig. 9 is a cross-sectional view for explaining the form of the groove in the present invention, Fig. 9(a) is a sectional view of the angular groove, and Fig. 9(b) is a sectional view of the triangular groove, Fig. 9 ( c) A sectional view of the circular groove, Fig. 9(d) is a sectional view of the V-shaped groove, and Fig. 9(e) is a sectional view of the groove of the cylindrical end. [Main component symbol description] 1 Filter cartridge module (membrane module) la Head cover 3 Housing 3a Main body 3b Top cover 3c Sealing ring 3d ' 3e Tube part 5 Module precursor 6 Module end face 7 Hollow fiber membrane bundle 7a Hollow Fiber membrane 9 Head cover member 9a Entrance 9b, 23f Bottom 11 Protective member 11a Vertical strip portion lib Loop portion 11c Projection portion 13 Cross plate 153942.doc -35- 201143876 13a Spacer 15 Sealing portion 21 Inlet side tubular portion 21a ' 23b Shallow groove 23 End portion side tubular portion 23a Deep groove 23c First convex portion 23d Second convex portion 23e Main body portion 25 Seat surface bb, cc line dl' d2 Average depth H Through hole L of protective member Axis ri Entrance side tubular portion Inner diameter r2 Inner diameter of the end side tube portion S Sealing material St Step difference SI to S7 Step 153942.doc 36-

Claims (1)

201143876 七、申請專利範圍: =蓋構件,其安裝於中空纖維膜束之端部並且内 束且固化有密封材料,藉此’固定於上述, 膜束,該頭蓋構件之特徵在於: 包括:入口側筒部,其設置於插入上述中空纖維膜束 '以:端部側筒部,其内徑小於上述入口側筒 ^且6又置於較上述入口側筒部更靠端部側;並且 於上述入口側筒部之内表面與上述端部側筒部之内表 面之間形成有階差, 述入口側筒部及上述端部側 商部中之至少—^ ^ βη ± ^ 之抽線… 形成有圍繞上述頭蓋構件 之釉線的環狀之槽。 2. 如請求項1之頭蓋構件’其中上述頭蓋構件之上述端部 側筒部包括:筒狀之主體部、盥一 體成形於上述主艘邱 之底部。 體^ 3. 如請求項1或2之頭蓋構件,其中 再1干具中上述槽包括:形成於上 述入口側筒部之漤神、盘彡 與形成於上述端部側筒部且齡卜 述淺槽更深之深槽。 4. 如請求項1至3中任一項之頭蓋 貝盘構件’纟中於上述端部側 筒部之内表面,形成右囹姑μ 成有圍%上述頭蓋構件之軸線的環狀 之凸部。 5_ 一種膜模組,其特徵在於包括: 使用如請求項1至4中任一項 上返頭蓋構件而形成的 筒狀之頭蓋部、包含插入至上述頭蓋部内之複數個中* 纖維膜的中空纖維膜束、將上述中空纖維膜束固定於上 153942.doc 201143876 述頭羞部之密封部、以好姑 以及使上述甲空纖維膜之内部開放 之模組端面》 1现 6_如請求項5之膜模組,装隹 其進而包括茼狀之保護構件,該 '狀之保護構件係呈環狀地將增空纖維膜束包圍, 且與上述中空纖維膜束一併藉由上述密封 述頭蓋部, 疋於上 Τ上述保護構件,設置有複數個貫通孔、與自固定於 碩蓋部之側之端部朝上述保護構件之軸線方向突出 的線狀之突出部。 Π大出 7 如凊求項6之膜模組’其中上述保護構件為網狀,且具 有形成上述貫通孔之複數個網眼,上述突 二 :述保護構件之端部分別自連接為環狀之複數個= 出0 8. —種膜模組之製造方法,其係使用如請求項…令任— 項之上述頭蓋構件而製造膜模組之方法’其特徵在 括如下步驟: 、 對複數個中空纖維膜進行捆束,從而形成中空纖維膜 束, 將上述頭蓋構件安裝於上述中空纖維臈束之端部,將 液狀之密封材料填充至上述頭蓋構件之内部; ,使填充至_h述頭蓋構件之内部之上述密封材料固化, 從而形成密封部;以及 於形成上述密封部之後,與上述中空纖維膜之端部一 併將上述頭蓋構件之端部側之一部分及上述密封部之— 153942.doc 201143876 部分予以切斷,形成使複數個上述中空纖維膜之内部開 放之模組端面。 153942.doc201143876 VII. Patent application scope: = cover member, which is installed at the end of the hollow fiber membrane bundle and is internally bundled and solidified with a sealing material, thereby being fixed to the above-mentioned membrane bundle, the head cover member is characterized by: a side tubular portion which is disposed in the hollow fiber membrane bundle to be inserted into the end side tubular portion, the inner diameter of which is smaller than the inlet side cylinder and 6 is placed closer to the end side than the inlet side tubular portion; A step is formed between the inner surface of the inlet-side tubular portion and the inner surface of the end-side tubular portion, and at least the extraction line of the inlet-side tubular portion and the end-side quotient portion is −^βη±^ An annular groove is formed around the glaze of the head cover member. 2. The head cover member of claim 1, wherein the end side tubular portion of the head cover member comprises: a tubular body portion, and a body is integrally formed at a bottom portion of the main ship. The head cover member of claim 1 or 2, wherein the groove in the other dry tool comprises: a scorpion formed on the inlet side tubular portion, a disk cymbal and an intermediate ridge formed on the end side tubular portion Deep grooves with shallow grooves. 4. The head cover bezel member of any one of claims 1 to 3, which is formed on the inner surface of the end side tubular portion, forming a ring-shaped convex portion having a right axis of the head cover member unit. 5_ A film module, comprising: a cylindrical head portion formed by returning a head cover member according to any one of claims 1 to 4, and a hollow comprising a plurality of medium* fiber membranes inserted into the head cover portion The fiber membrane bundle, the hollow fiber membrane bundle is fixed to the sealing portion of the head imaginary part of the 153942.doc 201143876, and the end face of the module which opens the interior of the hollow fiber membrane is as follows. The membrane module of 5, further comprising a braid-shaped protective member, the protective member of the shape is surrounded by the hollow fiber membrane bundle in an annular shape, and is combined with the hollow fiber membrane bundle by the above-mentioned sealing The head cover portion is provided with a plurality of through holes and a linear protruding portion that protrudes toward the axial direction of the protective member from an end portion that is fixed to the side of the base portion. The membrane module of claim 6 wherein the protective member is in the form of a mesh and has a plurality of meshes forming the through-holes, wherein the ends of the protective members are self-joined into a ring shape. The plural method = the output method of the film module, which is a method for manufacturing a film module using the above-mentioned head cover member as claimed in the claims - the following steps are included: The hollow fiber membranes are bundled to form a hollow fiber membrane bundle, and the head cover member is attached to the end portion of the hollow fiber bundle, and a liquid sealing material is filled into the inside of the head cover member; The sealing material inside the head cover member is cured to form a sealing portion; and after the sealing portion is formed, a portion of the end portion of the head cover member and the sealing portion are provided together with an end portion of the hollow fiber membrane 153942.doc 201143876 Partially cut to form a module end face that opens the inside of a plurality of hollow fiber membranes. 153942.doc
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Cited By (3)

* Cited by examiner, † Cited by third party
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Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013139011A (en) * 2012-01-06 2013-07-18 Daicen Membrane Systems Ltd Hollow fiber membrane module
WO2014024961A1 (en) 2012-08-10 2014-02-13 宇部興産株式会社 Gas-separating membrane module
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US10426884B2 (en) 2015-06-26 2019-10-01 Novaflux Inc. Cartridges and systems for outside-in flow in membrane-based therapies
US10399040B2 (en) 2015-09-24 2019-09-03 Novaflux Inc. Cartridges and systems for membrane-based therapies
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Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06277460A (en) * 1993-03-29 1994-10-04 Dainippon Ink & Chem Inc Manufacturing method of hollow fiber membrane module
JP4622163B2 (en) * 2001-06-15 2011-02-02 Nok株式会社 Hollow fiber membrane module
JP3908052B2 (en) * 2002-02-19 2007-04-25 旭硝子エンジニアリング株式会社 Hollow fiber membrane assembly and manufacturing method thereof
JP2008279374A (en) * 2007-05-11 2008-11-20 Toray Ind Inc Vessel for injecting potting material and manufacturing method of hollow fiber membrane module using the same

Cited By (3)

* Cited by examiner, † Cited by third party
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