JPH02191531A - Filter module by hollow-fiber membrane - Google Patents
Filter module by hollow-fiber membraneInfo
- Publication number
- JPH02191531A JPH02191531A JP969489A JP969489A JPH02191531A JP H02191531 A JPH02191531 A JP H02191531A JP 969489 A JP969489 A JP 969489A JP 969489 A JP969489 A JP 969489A JP H02191531 A JPH02191531 A JP H02191531A
- Authority
- JP
- Japan
- Prior art keywords
- end wall
- wall
- inner cylinder
- hollow fiber
- cylinder
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 69
- 239000012510 hollow fiber Substances 0.000 title claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 238000001914 filtration Methods 0.000 claims description 50
- 238000009423 ventilation Methods 0.000 claims description 13
- 238000004140 cleaning Methods 0.000 abstract description 7
- 230000001681 protective effect Effects 0.000 abstract description 7
- 230000001174 ascending effect Effects 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 11
- 238000011001 backwashing Methods 0.000 description 10
- 238000005406 washing Methods 0.000 description 8
- 238000005253 cladding Methods 0.000 description 6
- 238000012856 packing Methods 0.000 description 6
- 238000005192 partition Methods 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- 239000003822 epoxy resin Substances 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 229920000647 polyepoxide Polymers 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000000452 restraining effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野)
この発明はプリコート型濾過装置で使用するための中空
糸膜による濾過モジュールに関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a filtration module using a hollow fiber membrane for use in a precoat type filtration device.
〈従来の技術)
中空糸膜による濾過モジュールを用いた中空糸膜型の濾
過装置は、濾過塔内に上向流で原水を供給し、中空糸膜
の筒状膜壁を透過して中空部に得られた処理水は濾過塔
の上部から取出すようになっている。これに対しイオン
交換樹脂の微粒子を表面に付着したプリコート層を有す
る中空エレメントによるプリコート型濾過装置では原水
を濾過塔内に上向流で供給し、表面のプリコート層を透
過し、エレメントの中空部に得られた処理水は中空糸膜
型とは逆に濾過塔の下部から取出す。<Conventional technology> A hollow fiber membrane type filtration device using a filtration module using a hollow fiber membrane supplies raw water in an upward flow into a filtration tower, passes through the cylindrical membrane wall of the hollow fiber membrane, and enters the hollow part. The treated water obtained is taken out from the top of the filtration tower. In contrast, in a precoat type filtration device using a hollow element having a precoat layer with fine particles of ion exchange resin attached to the surface, raw water is supplied into the filtration tower in an upward flow, passes through the precoat layer on the surface, and passes through the hollow part of the element. The treated water obtained is taken out from the bottom of the filtration tower, contrary to the hollow fiber membrane type.
そして、いずれの濾過装置でも、中空糸膜の筒状膜壁や
、中空エレメントのプリコート層が捕捉したクラッドで
目詰まりし、圧力損失が上昇したら空気と洗浄水によっ
て逆洗をし、クラッドを除去するが、この場合、中空糸
膜から逆洗により除かれるのは捕捉したクラッドだけで
あるのに対し、中空部し・メントではクラッドと共に、
プリコート層を構成していたイオン交換樹脂も除去され
るので中空糸膜に較べ非常に大量の廃棄物が生じる。In either filtration device, if the cylindrical membrane wall of the hollow fiber membrane or the precoat layer of the hollow element becomes clogged with captured crud and the pressure loss increases, backwashing is performed with air and washing water to remove the crud. However, in this case, only the trapped crud is removed from the hollow fiber membrane by backwashing, whereas in the hollow fiber membrane, along with the crud,
Since the ion exchange resin constituting the precoat layer is also removed, a much larger amount of waste is produced compared to hollow fiber membranes.
又、濾過を再開するには、その前に中空エレメントの表
面にプリコート層を新設する必要がある。Moreover, before restarting filtration, it is necessary to newly provide a precoat layer on the surface of the hollow element.
そのような理由で、逆洗の際に発生する廃棄物が少なく
、逆洗後、直ちに濾過を再開できる中空糸膜を用い、従
来のプリコート型濾過装置に使用する濾過モジュールが
堤案されている。For this reason, a filtration module has been proposed for use with conventional pre-coat type filtration equipment, which uses a hollow fiber membrane that generates less waste during backwashing and can restart filtration immediately after backwashing. .
〈発明が解決しようとする課題〉
上記公知例は、濾過塔内に上向流で供給した原水のうち
、中空糸膜の筒状膜壁を透過し、その中空部に得られた
処理水をいかにして濾過塔の下部から取出すかの原理を
開示するだけで、中空糸膜の表面が目詰まりした場合に
空気と洗浄水でいかにして逆洗を行なうがなど具体的な
事柄は一切述べられて居らず、そのまSでは実用するこ
とは不可能である。<Problems to be Solved by the Invention> In the above-mentioned known example, raw water supplied in an upward flow into a filtration tower passes through a cylindrical membrane wall of a hollow fiber membrane, and the treated water obtained in the hollow part is collected. It only discloses the principle of how to extract the material from the bottom of the filtration tower, but does not provide any specific details such as how to backwash the hollow fiber membrane with air and washing water if the surface of the hollow fiber membrane becomes clogged. Therefore, it is impossible to put S into practical use as it is.
(課題を解決するための手段)
そこで本発明は実用に供することができる具体的な濾過
モジュールを提供することを目的に開発されたのであっ
て、請求項第1項の中空糸膜による濾過モジュールは、
原水が流通する上下方向の保護筒の内部に、下部が該保
護筒の下端から下に突出する内筒を上下方向に配置し、
上記保護筒の内周と、内筒の外周とで形成された筒形空
間の上下を上端壁と下、端壁とにより閉鎖し、上記筒形
空間の内部には多数本の中空糸膜な上下方向に配列し、
各中空糸膜の上端は前記上端壁を貫通して上端壁上に開
口すると共に、下端は前記下端壁中に埋没して閉鎖され
、前記上端壁上には前記内筒と連通した処理水の集液室
を設け、前記下端壁には上下方向に貫通した通気孔を設
け、下端壁の下には下に開放した空気室を設けたことを
特徴とする。(Means for Solving the Problems) Therefore, the present invention has been developed for the purpose of providing a specific filtration module that can be put to practical use, and is a filtration module using a hollow fiber membrane according to claim 1. teeth,
An inner cylinder whose lower part protrudes downward from the lower end of the protection cylinder is disposed in the vertical direction inside the protection cylinder in the vertical direction through which the raw water flows,
A cylindrical space formed by the inner periphery of the protection cylinder and the outer periphery of the inner cylinder is closed at the top and bottom by an upper end wall, a lower end wall, and an end wall, and a large number of hollow fiber membranes are installed inside the cylindrical space. arranged vertically,
The upper end of each hollow fiber membrane penetrates the upper end wall and opens onto the upper end wall, and the lower end is buried and closed in the lower end wall. A liquid collecting chamber is provided, a ventilation hole penetrating the lower end wall in the vertical direction is provided, and an air chamber opened downward is provided below the lower end wall.
又、請求項第2項の中空糸膜による濾過モジュールは、
原水が流通する上下方向の保護筒の内部に、上部が該保
護筒の上端から上に突出する内筒を上下方向に配置し、
上記保護筒の内周と、内筒の外周とで形成された筒形空
間の上下を上端壁と、下端壁により閉鎖すると共に、内
筒の下端も該下端壁で閉鎖し、上記筒形空間の内部には
多数本の中空糸膜を上下方向に配列し、各中空糸膜の上
端は前記上端壁中に埋没して閉鎖されると共に、下端は
下端壁を貫通して下端壁の下面に開口し、前記内筒の上
端部と、中部及び下部に通気孔を設け、又、下端壁の下
には下に開放した処理水の集液室を設けたことを特徴と
する。Further, the filtration module using hollow fiber membranes according to claim 2,
An inner cylinder whose upper part projects upward from the upper end of the protection cylinder is disposed in the vertical direction inside the protection cylinder in the vertical direction through which the raw water flows,
The upper and lower ends of the cylindrical space formed by the inner periphery of the protective cylinder and the outer periphery of the inner cylinder are closed by an upper end wall and a lower end wall, and the lower end of the inner cylinder is also closed by the lower end wall, and the cylindrical space is Inside, a large number of hollow fiber membranes are arranged in the vertical direction, and the upper end of each hollow fiber membrane is buried and closed in the upper end wall, and the lower end penetrates the lower end wall and is attached to the lower surface of the lower end wall. The inner cylinder is characterized by being open and provided with ventilation holes at the upper end, middle and lower part of the inner cylinder, and a treated water collecting chamber which is open to the bottom and is provided below the lower end wall.
く実 施 例)
第1図は請求項第1項の濾過モジュールの一実施例であ
って、11は上下方向の保護筒、12は保護筒の内部に
上下方向に配置され、下部12’が前記保護筒11の下
端から下に突出する内筒、13は保護筒の内周と、内筒
の外周とで形成された筒形空間、 14は上記筒形空間
の上端部を閉鎖する上端壁、15は同じく上記筒形空間
の下端部を閉鎖する下端
壁、】6・・・は上記筒形空間13の内部に上下方向に
配列され、上端は上端壁14を貫通して該壁の上面に開
口し、下端は下端壁15中に埋没して閉ざされた多数本
の中空糸膜、17は上端壁14上に設けられた処理水の
集液室、18は下端壁に上下方向に貫通して設けられた
通気孔。Embodiment) Fig. 1 shows an embodiment of the filtration module according to claim 1, in which 11 is a vertical protection tube, 12 is arranged vertically inside the protection tube, and the lower part 12' is arranged vertically inside the protection tube. An inner cylinder protrudes downward from the lower end of the protection cylinder 11, 13 is a cylindrical space formed by the inner periphery of the protection cylinder and the outer periphery of the inner cylinder, and 14 is an upper end wall that closes the upper end of the cylindrical space. , 15 is a lower end wall that similarly closes the lower end of the cylindrical space, ]6... are arranged in the vertical direction inside the cylindrical space 13, and the upper end passes through the upper end wall 14 to face the upper surface of the wall. A large number of hollow fiber membranes are opened at the lower end and are closed by being buried in the lower end wall 15, 17 is a treated water collection chamber provided on the upper end wall 14, and 18 is a membrane that penetrates the lower end wall in the vertical direction. ventilation holes provided.
19は下端壁15の下に設けられた空気室を示す。Reference numeral 19 indicates an air chamber provided under the lower end wall 15.
保i1i筒11はポリエチレン、ポリプロピレン、アク
リルなどの硬質プラスチック製で、筒形空間13を囲む
部分には上下方向に複数段の直径10〜15mm程度の
孔20が円周方向に等間隔に開設しである。内筒12は
保護筒の中心に沿って一本、配置してあり、これはプラ
スチック製またはステンレス製である。内筒12は、こ
の実施例では上端壁上の集液室17に上部が突入し、そ
の上部の回りには集液室17の内部と連通ずる通水孔2
1が開設しである。The housing cylinder 11 is made of hard plastic such as polyethylene, polypropylene, or acrylic, and in the part surrounding the cylindrical space 13, multiple holes 20 with a diameter of about 10 to 15 mm are opened in the vertical direction at equal intervals in the circumferential direction. It is. One inner cylinder 12 is arranged along the center of the protection cylinder, and is made of plastic or stainless steel. In this embodiment, the inner cylinder 12 has an upper portion that protrudes into a liquid collection chamber 17 on the upper end wall, and a water passage hole 2 that communicates with the inside of the liquid collection chamber 17 around the upper portion.
1 was opened.
保護筒11も上端壁14から上に、内筒12と同量突出
する上部を有し、内筒の上端と、保護筒の上端には集液
室17の環状の上壁22の内周と外周を固定しである。The protection cylinder 11 also has an upper part that projects upward from the upper end wall 14 by the same amount as the inner cylinder 12, and the inner circumference of the annular upper wall 22 of the liquid collection chamber 17 and the upper end of the inner cylinder and the upper end of the protection cylinder are connected to each other. The outer periphery is fixed.
そして、上壁22上には、外径は土壁と同じであるが、
内径はそれより大きい環状のパツキン23を接着などで
固定しである。Then, on the upper wall 22, although the outer diameter is the same as that of the earthen wall,
An annular packing 23 having a larger inner diameter is fixed with adhesive or the like.
上端壁14と、下端壁15はエポキシ樹脂を固めたボッ
ティングによるシース部で、下端壁15の下面外周には
環状のパツキン24を接着などで取付け、空気室19の
回りを囲む。The upper end wall 14 and the lower end wall 15 are sheath parts made of hardened epoxy resin by botting, and an annular packing 24 is attached to the outer periphery of the lower surface of the lower end wall 15 by adhesive or the like, and surrounds the air chamber 19.
第2図において、31はプリコート型濾過装置の濾過塔
で、底を有する筒胴32と、筒胴の上用のフランジ上に
重なるフランジを下側に有する覆蓋33を備λ、筒胴の
内部は仕切板34で上下に区劃すされ、上が濾過室35
.下が処理水の取出室36になって居り、原水の供給管
37は筒胴の底と、仕切板34を貫通して濾過室35内
に上向流で原水を供給し、取出室36に集液した処理水
は取出管38で塔外に取出す。In Fig. 2, reference numeral 31 denotes a filter tower of a precoat type filtration device, which includes a cylinder body 32 having a bottom, a cover 33 having a flange on the lower side that overlaps the upper flange of the cylinder body, and an interior of the cylinder body. is divided into upper and lower parts by a partition plate 34, and the upper part is the filtration chamber 35.
.. The lower part is a take-out chamber 36 for treated water, and a raw water supply pipe 37 passes through the bottom of the barrel and the partition plate 34 to supply raw water in an upward flow into the filtration chamber 35, and then to the take-out chamber 36. The collected treated water is taken out of the tower through a take-out pipe 38.
尚、原水供給管37は膜洗浄後の洗浄廃水の排出口とし
ても使用する。The raw water supply pipe 37 is also used as a discharge port for cleaning waste water after membrane cleaning.
筒胴32の上用のフランジと、覆蓋33の下側のフラン
ジは、その間に上部側板39を挟んでボルト、ナツト4
0で接合してあり、上部側板39は濾過室35と覆蓋3
3の内部を上下に仕切る。覆蓋33には空気抜き41が
あり、処理室35の上部には逆洗洗浄時の空気を排出す
る排出口42が設けである。The upper flange of the cylinder body 32 and the lower flange of the cover 33 are used to hold bolts and nuts 4 with the upper side plate 39 sandwiched between them.
The upper side plate 39 is connected to the filtration chamber 35 and the cover 3.
Divide the inside of 3 into upper and lower parts. The cover 33 has an air vent 41, and the upper part of the processing chamber 35 is provided with an outlet 42 for discharging air during backwashing.
そして、仕切板34上には濾過モジュールの下端を支持
するための中空の支持台43が多数段けである。この支
持台43は仕切板34にある孔の回りに下端を固定され
た筒部44と、底にある中心孔の回りを筒部44の上端
に結合された受皿部45とからなる。A plurality of hollow support stands 43 are arranged on the partition plate 34 to support the lower end of the filtration module. This support base 43 consists of a cylindrical part 44 whose lower end is fixed around a hole in the partition plate 34, and a saucer part 45 which is connected to the upper end of the cylindrical part 44 around a center hole in the bottom.
前述した濾過モジュールの保護筒11の外径は上記受皿
部45の内径に適合させ、又、内筒12の外径は上記筒
部44の内径に適合させて置く、そして、この濾過モジ
ュールを使用するため仕切板34上には散気管46を敷
設し、覆蓋33にある空気抜き41と、上記散気管46
を、上部側板39を水密に貫通する給気管47で接続し
、空気抜き41から逆洗用の空気を吹込み、散気管46
から噴出できるようにすると共に、各支持台の受皿部4
5の底には通気孔48を開設して置く、又、各支持台の
筒部44内には放射状の支持具49を取付け、該支持具
49の中心には上端部が上部側板39を下から上に貫通
する支持軸50の下端を溶接などで取付け、直立させる
。The outer diameter of the protective tube 11 of the aforementioned filtration module is matched to the inner diameter of the saucer portion 45, and the outer diameter of the inner tube 12 is matched to the inner diameter of the cylindrical portion 44, and this filtration module is used. In order to
are connected by an air supply pipe 47 that penetrates the upper side plate 39 watertightly, and air for backwashing is blown from the air vent 41, and the air diffuser pipe 46
In addition, the saucer part 4 of each support stand
A ventilation hole 48 is provided at the bottom of each support base, and a radial support 49 is installed in the cylindrical part 44 of each support base, and the upper end of the support 49 is located at the center of the support 49 so that the upper side plate 39 is lowered. The lower end of the support shaft 50 penetrating upward is attached by welding or the like, and is made to stand upright.
前述の濾過モジュールをセットするには覆蓋33、上部
側板39を取外し、各支持台43から直立する支持軸5
0を内筒12中に入れてモジュールを支持台43上に降
ろし、内筒の下端部を支持台の筒部44の内周に嵌める
と共に、保護筒11の下端部を受皿部45内に嵌め、空
気室19の回りを囲むパツキン24を受皿部45の底に
圧縮する。そして、支持軸50にはモジュールのパツキ
ン23と、集液室の上壁22の内周部に当接する抑え板
51を嵌め、ナツト52で上から締付ける。このために
支持軸50は上端部に抑え板51を下から受止める殺5
3を有し、段53から上は直径が細い雄ねじ54になっ
ている。To set the above-mentioned filtration module, remove the cover 33 and the upper side plate 39, and attach the support shaft 5 that stands upright from each support stand 43.
0 into the inner cylinder 12, lower the module onto the support stand 43, fit the lower end of the inner cylinder into the inner periphery of the cylindrical part 44 of the support stand, and fit the lower end of the protection cylinder 11 into the saucer part 45. , the packing 24 surrounding the air chamber 19 is compressed to the bottom of the saucer portion 45. Then, the packing 23 of the module and the restraining plate 51 that comes into contact with the inner circumference of the upper wall 22 of the liquid collection chamber are fitted onto the support shaft 50, and tightened from above with a nut 52. For this purpose, the support shaft 50 has a stopper 5 at its upper end that receives the restraining plate 51 from below.
3, and a male screw 54 with a thin diameter is formed above the step 53.
尚、段53の高さ、ないしレベルはモジュールの上壁2
2の上面に合わせである。Note that the height or level of the step 53 is the upper wall 2 of the module.
It is aligned with the top surface of 2.
こうして全部の支持台43上にモジュールを立設したら
上部側板39を筒胴32の1周のフランジ上に載せると
共に、各支持軸の上端部の雄ねじ54を上部側板にある
孔から上に突出させ、この雄ねじ54にねじ込んだナツ
ト55を上・部側抜に対して締付け、各モジュールが揺
動するのを防止する。そして、覆蓋33を上部側板上に
被せ、ボルト、ナツト40で筒胴32と覆蓋33の両フ
ランジ、及び上部側板の周縁部を重合状態に結合する。After the modules are erected on all the support stands 43 in this way, the upper side plate 39 is placed on the flange around the cylinder body 32, and the male screw 54 at the upper end of each support shaft is made to protrude upward from the hole in the upper side plate. A nut 55 screwed into this male screw 54 is tightened against the upper and lower sides to prevent each module from swinging. Then, the cover 33 is placed on the upper side plate, and the flanges of the cylinder body 32 and the cover 33, and the peripheral edge of the upper side plate are joined together with bolts and nuts 40 in an overlapping state.
濾過を行なうには原水を供給管37で濾過室35内に加
圧して供給する。これにより原水は保護筒11の孔20
からモジュールの筒形空間13に入り、原水中のクラッ
ドは中空糸膜16の筒状膜壁に捕捉され、処理水のみが
該膜壁を透過して中空部に流入する。そして、処理水は
中空部を上昇して上端壁14上の集液室17に集まり、
膜室から通水孔21を通じ内筒12中に流れ込み、内筒
中を下降して支持台の筒部44から濾過装置の取出室3
6に入り、取出管38で外に取出される。To perform filtration, raw water is pressurized and supplied into the filtration chamber 35 through the supply pipe 37. This allows the raw water to flow through the hole 20 of the protection tube 11.
The crud in the raw water enters the cylindrical space 13 of the module, and the crud in the raw water is captured by the cylindrical membrane wall of the hollow fiber membrane 16, and only the treated water passes through the membrane wall and flows into the hollow section. The treated water then rises through the hollow section and collects in the liquid collection chamber 17 on the upper end wall 14.
Water flows from the membrane chamber into the inner cylinder 12 through the water passage hole 21, descends through the inner cylinder, and flows from the cylindrical part 44 of the support stand to the extraction chamber 3 of the filtration device.
6 and is taken out through the take-out pipe 38.
損失水頭が上昇したら逆洗を行ない、中空糸膜16・・
・が捕捉したクラッドを剥離除去する。それには取出管
38から洗浄水を圧入した後に、空気抜き41に空気を
吹き込み、散気管46から処理室35内に噴出させる。When the head loss increases, backwashing is performed and the hollow fiber membrane 16...
・Remove the captured crud. To do this, after washing water is pressurized from the take-out pipe 38, air is blown into the air vent 41 and is ejected from the aeration pipe 46 into the processing chamber 35.
水逆洗により洗浄水は取出室36から各モジュールの内
筒12中を上昇し、集液室17から中空糸膜16の一本
宛の中空部中に下向流で流れ込み、中空糸膜の筒状膜壁
を逆に透過する。その後に散気管46から噴出した空気
は細かい気泡になって支持台の受皿部45の底にある通
気孔48を通じ空気室19に入り、こ\から下端壁】5
にある通気孔18を経て筒形空間13を上昇しながら中
空糸膜16・・・の外面に接触し、中空糸膜に捕捉され
たクラッドの剥離を促す。By water backwashing, the cleaning water rises from the take-out chamber 36 into the inner cylinder 12 of each module, flows downward from the liquid collecting chamber 17 into the hollow portion of the hollow fiber membrane 16, and flows downward into the hollow fiber membrane 16. It passes through the cylindrical membrane wall in reverse. After that, the air ejected from the diffuser pipe 46 becomes fine bubbles and enters the air chamber 19 through the ventilation hole 48 at the bottom of the saucer part 45 of the support base, and from there the lower end wall]5
While ascending through the cylindrical space 13 through the ventilation hole 18 located in the hollow fiber membrane 16, it comes into contact with the outer surface of the hollow fiber membrane 16, and promotes the peeling of the cladding captured by the hollow fiber membrane.
こうして中空糸膜の筒状膜壁を内周から外周に透過する
洗浄水と、該膜壁の表面に接触しながら上昇する気泡に
よってクラッドは中空糸膜から剥離され、保護筒11の
孔20から洗浄水や気泡と一緒にモジュールの外に出、
排出口37から装置の外に排出され、洗浄終了後濾過工
程を再開する。In this way, the cladding is peeled off from the hollow fiber membrane by the cleaning water that permeates the cylindrical membrane wall of the hollow fiber membrane from the inner periphery to the outer periphery and the air bubbles that rise while contacting the surface of the membrane wall, and the cladding is removed from the hole 20 of the protection tube 11. It comes out of the module along with cleaning water and air bubbles.
It is discharged from the apparatus through the discharge port 37, and the filtration process is restarted after washing is completed.
第3図は請求項第2項の濾過モジュールの一実施例であ
って、61は上下方向の保護筒、62は保護筒の内部に
上下方向に配置され、上部62′が前記保護筒の上端か
ら上に突出する内筒、63は保護筒の内周と、内筒の外
周とで形成された筒形空間、64は上記筒形空間の上端
部を閉鎖する上端壁、65は同じく上記筒形空間の下端
部を閉鎖する下端壁、66・・・は上記筒形空間63の
内部に上下方向に配列され、上端は上端壁64中に埋没
して閉ざされ、下端は下端壁65中を貫通して膜壁の下
面に開口した多数本の中空糸膜、67は下端壁65の下
に設けられた処理水の集液室、68は内筒の上端部の回
りに設けた通気孔を示す、保護筒61.内筒62の材質
は前述の実施例と同じでよく、保護筒61には上下方向
に複数段の孔69が同様に開設しである。又、内筒62
には筒形空間63の下端部と、中間部に位置する通気孔
70を有する。FIG. 3 shows an embodiment of the filtration module according to claim 2, in which 61 is a vertical protection tube, 62 is arranged inside the protection tube in the vertical direction, and an upper part 62' is an upper end of the protection tube. 63 is a cylindrical space formed by the inner periphery of the protection cylinder and the outer periphery of the inner cylinder; 64 is an upper end wall that closes the upper end of the cylindrical space; 65 is also the cylinder; Lower end walls 66 that close the lower end of the shaped space are arranged in the vertical direction inside the cylindrical space 63, their upper ends are buried and closed in the upper end wall 64, and their lower ends are closed in the lower end wall 65. A large number of hollow fiber membranes are penetrated and open on the lower surface of the membrane wall, 67 is a treated water collecting chamber provided under the lower end wall 65, and 68 is a ventilation hole provided around the upper end of the inner cylinder. As shown, the protective tube 61. The material of the inner cylinder 62 may be the same as that of the above-mentioned embodiment, and the protective cylinder 61 is similarly provided with a plurality of holes 69 in the vertical direction. Also, the inner cylinder 62
It has a lower end of a cylindrical space 63 and a ventilation hole 70 located in the middle.
上端壁64と下端壁65はエポキシ樹脂を固めたボッテ
ィングによるシース部で、下端壁の下面外周には集液室
67の回りを囲む環状のパツキン71を接着などで固定
する。The upper end wall 64 and the lower end wall 65 are sheath portions made of hardened epoxy resin by botting, and an annular packing 71 surrounding the liquid collection chamber 67 is fixed to the outer periphery of the lower surface of the lower end wall by adhesive or the like.
第4図は第2図と同じプリコート型濾過装置の濾過塔で
同じ構成部分には同じ符合を付しである。FIG. 4 shows a filter tower of the same precoat type filtration device as FIG. 2, and the same components are given the same reference numerals.
第3図の濾過モジュールをこの濾過塔で使用するための
改造は、覆蓋33にある空気抜き41に空気を吹き込む
ことができるようにすることS、中空の支持台43の筒
部44には支持具49で支持軸50の下端を固定し、支
持軸50を直立させることき、上部側板39には内筒6
2の上端部を上に貫通させることができる孔56を開設
するだけでよく、散気管46は敷設する必要がない。Modifications for using the filtration module shown in FIG. 3 in this filtration tower include making it possible to blow air into the air vent 41 in the cover 33, and installing a support in the cylindrical part 44 of the hollow support 43. 49 fixes the lower end of the support shaft 50 and when the support shaft 50 is made to stand upright, an inner cylinder 6 is attached to the upper side plate 39.
It is only necessary to open a hole 56 through which the upper end of the air diffuser 2 can pass upward, and there is no need to install the air diffuser pipe 46.
モジュールをセットするには覆蓋33、上部側板39を
外し、内筒62の下端内部を塞いだ下端壁65の中心孔
72を各支持軸50の上端に嵌めてモジュールを支持台
43上に降ろし、保護筒61の下端部を受皿部45の内
周に嵌めると共に、集液室67の回りを囲む環状のパツ
キン71を受皿部45の底の上に圧縮する。下端壁の中
心孔72を下からシールするために支持軸50の下端部
には鍔50′ を固定して上面にOリング57を載せ、
モジュールを受皿部上に降ろしたときOリング57は下
端壁65の下面の中心孔の回りで圧縮されるようにする
とよい。To set the module, remove the cover 33 and the upper side plate 39, fit the center hole 72 of the lower end wall 65 that closed the inside of the lower end of the inner tube 62 into the upper end of each support shaft 50, and lower the module onto the support stand 43. The lower end of the protection tube 61 is fitted into the inner periphery of the saucer section 45, and the annular packing 71 surrounding the liquid collection chamber 67 is compressed onto the bottom of the saucer section 45. In order to seal the center hole 72 of the lower end wall from below, a collar 50' is fixed to the lower end of the support shaft 50, and an O-ring 57 is placed on the upper surface.
The O-ring 57 is preferably compressed around the center hole in the lower surface of the lower end wall 65 when the module is lowered onto the tray.
こうして全部の支持台43上にモジュールを立設したら
上部側板39を筒胴32の上層のフランジ上に載せると
共に、各モジュールの内筒62の上端部を側板にある孔
56から上に突出させ、内筒の上端部外周の雄ねじにナ
ツト58をねじ込んで上部側板に対して締付け、内筒6
2の上端から上に突出する支持軸の上端部の雄ねじ54
にナツト59をねじこんで内筒の上端に対して締付け、
併せてナツト59で内筒62の上端を塞ぐ、上部側板の
孔56.ナツト58.59はモジュールが揺れるのを有
効に防止する。After all the modules are erected on the support bases 43 in this way, the upper side plate 39 is placed on the upper flange of the cylinder body 32, and the upper end of the inner cylinder 62 of each module is made to protrude upward from the hole 56 in the side plate. Screw the nut 58 into the male thread on the outer periphery of the upper end of the inner cylinder and tighten it against the upper side plate.
External thread 54 at the upper end of the support shaft protruding upward from the upper end of 2
Screw in the nut 59 and tighten it against the upper end of the inner cylinder,
At the same time, a hole 56 in the upper side plate is closed with a nut 59 to close the upper end of the inner cylinder 62. Nuts 58,59 effectively prevent the module from shaking.
濾過を行なうには原水を供給管37で濾過室35内に加
圧して供給する。これにより原水は保護筒61の孔69
からモジュールの筒形空間63に入り、原水中のクラッ
ドは中空糸膜66の筒状膜壁に捕捉され、処理水のみが
該膜壁を透過して中空部に流入する。そして、処理水は
中空部を下降して下端壁65の下の集液室67に集まり
、こシから支持台の筒44を経て濾過装置の取出室36
に流下し、取出管38で外に取出される。To perform filtration, raw water is pressurized and supplied into the filtration chamber 35 through the supply pipe 37. As a result, the raw water flows into the hole 69 of the protection tube 61.
The crud in the raw water enters the cylindrical space 63 of the module, and the crud in the raw water is captured by the cylindrical membrane wall of the hollow fiber membrane 66, and only the treated water passes through the membrane wall and flows into the hollow part. Then, the treated water descends through the hollow part and collects in the collection chamber 67 under the lower end wall 65, and passes through the tube 44 of the support stand and into the extraction chamber 36 of the filtration device.
and is taken out through the take-out pipe 38.
損失水頭が上昇したら逆洗を行ない、中空糸膜66・・
・が捕捉したクラッドを剥離除去する。それには取出管
38から洗浄水を圧入した後に空気抜き41に空気を吹
込む。これにより洗浄水は取出室36から支持台の筒部
44、集液室67を経て中空糸膜66の一本宛の中空部
中を上向流し、中空糸膜の筒状膜壁を逆に透過する。そ
の後に空気抜き41から覆蓋33の内部に吹込まれた空
気は、内筒62の上端部にある通気孔68から内筒62
に入って筒内を下降し、内筒の下部及び中部にある通気
孔70から筒形空間63に細かい気泡になって噴出し、
該筒形空間63中を上昇しながら中空糸膜66・・・の
外面に接触し、中空糸膜に捕捉されたクラッドの剥離を
促す。When the head loss increases, backwashing is performed and the hollow fiber membrane 66...
・Remove the captured crud. For this purpose, air is blown into the air vent 41 after washing water is pressurized from the take-out pipe 38. As a result, the washing water flows upward from the extraction chamber 36 through the cylindrical portion 44 of the support stand and the liquid collection chamber 67 into the hollow portion of the hollow fiber membrane 66, and reverses the cylindrical membrane wall of the hollow fiber membrane. To Penetrate. After that, the air blown into the cover 33 from the air vent 41 is transferred to the inner cylinder 62 from the ventilation hole 68 at the upper end of the inner cylinder 62.
The air enters the cylinder and descends inside the cylinder, and is ejected in the form of fine bubbles into the cylindrical space 63 from the ventilation holes 70 in the lower and middle parts of the inner cylinder.
While rising in the cylindrical space 63, it comes into contact with the outer surface of the hollow fiber membranes 66, and promotes peeling of the cladding captured by the hollow fiber membranes.
こうして中空糸膜の筒状膜壁を内周から外周に透過する
洗浄水と、該膜壁の表面に接触しながら上昇する気泡に
よってクラッドは中空糸膜から剥離され、保護筒61の
孔69から洗浄水と一緒にモジュールの外に出、排出口
37から装置の外に排出され、洗浄終了後濾過工程を再
開する。In this way, the cladding is peeled off from the hollow fiber membrane by the cleaning water that permeates the cylindrical membrane wall of the hollow fiber membrane from the inner circumference to the outer circumference and the air bubbles that rise while contacting the surface of the membrane wall, and the cladding is peeled off from the hollow fiber membrane through the hole 69 of the protection tube 61. It exits the module together with the washing water and is discharged from the apparatus through the outlet 37, and after the washing is completed, the filtration process is restarted.
〈発明の効果〉
本発明によれば、既設のプリコート型濾過モジュールを
使用するプリコート型濾過塔、例λばBWR型原子力発
電所の復水濾過器の内部構造物を大規模に改造すること
なく濾通、逆洗が行なえる中空糸膜濾過モジュールを提
供できる。<Effects of the Invention> According to the present invention, the internal structure of a pre-coat type filtration tower using an existing pre-coat type filtration module, for example, a condensate filter in a BWR type nuclear power plant, can be improved without large-scale remodeling. A hollow fiber membrane filtration module that can perform filtration and backwashing can be provided.
第1図は請求項第1項の濾過モジュールの一実施例の断
面図、第2図は第1図の濾過モジュールの使用状態を示
す濾過塔の断面図、第3図は請求項第2項の濾過モジュ
ールの一実施例の断面図、第4図は第3図の濾過モジュ
ールの使用状態を示す濾過塔の断面図である。
図中、11.61は保護筒、12.62は内筒、13、
63は筒形空間、14.64は上端壁、15.65は下
端壁、16.66は中空糸膜、17.67は集液室、1
8.68.70は通気孔、19は空気室を示す。FIG. 1 is a sectional view of an embodiment of the filtration module according to claim 1, FIG. 2 is a sectional view of a filtration tower showing the usage state of the filtration module of FIG. 1, and FIG. FIG. 4 is a sectional view of a filtration tower showing a state in which the filtration module of FIG. 3 is used. In the figure, 11.61 is a protection cylinder, 12.62 is an inner cylinder, 13,
63 is a cylindrical space, 14.64 is an upper end wall, 15.65 is a lower end wall, 16.66 is a hollow fiber membrane, 17.67 is a liquid collection chamber, 1
8.68.70 indicates a ventilation hole, and 19 indicates an air chamber.
Claims (2)
が該保護筒の下端から下に突出する内筒を上下方向に配
置し、上記保護筒の内周と、内筒の外周とで形成された
筒形空間の上下を上端壁と下端壁とにより閉鎖し、上記
筒形空間の内部には多数本の中空糸膜を上下方向に配列
し、各中空糸膜の上端は前記上端壁を貫通して上端壁上
に開口すると共に、下端は前記下端壁中に埋没して閉鎖
され、前記上端壁上には前記内筒と連通した処理水の集
液室を設け、前記下端壁には上下方向に貫通した通気孔
を設け、下端壁の下には下に開放した空気室を設けたこ
とを特徴とする中空糸膜による濾過モジュール。(1) Inside a vertical protection cylinder through which raw water flows, an inner cylinder whose lower part projects downward from the lower end of the protection cylinder is arranged in the vertical direction, and the inner circumference of the protection cylinder and the outer circumference of the inner cylinder are arranged in the vertical direction. The upper and lower ends of the cylindrical space formed by the cylindrical space are closed by an upper end wall and a lower end wall, and a large number of hollow fiber membranes are arranged in the vertical direction inside the cylindrical space, and the upper end of each hollow fiber membrane is connected to the upper end of the cylindrical space. It penetrates the wall and opens onto the upper end wall, and the lower end is buried and closed in the lower end wall, and a treated water collection chamber communicating with the inner cylinder is provided on the upper end wall, and the lower end wall A filtration module using a hollow fiber membrane, characterized in that a ventilation hole is provided that penetrates in the vertical direction, and an air chamber that is open to the bottom is provided below the lower end wall.
が該保護筒の上端から上に突出する内筒を上下方向に配
置し、上記保護筒の内周と、内筒の外周とで形成された
筒形空間の上下を上端壁と、下端壁により閉鎖すると共 に、内筒の下端も該下端壁で閉鎖し、上記筒形空間の内
部には多数本の中空糸膜を上下方向に配列し、各中空糸
膜の上端は前記上端壁中に埋没して閉鎖されると共に、
下端は下端壁を貫通して下端壁の下面に開口し、前記内
筒の上端部と、中部及び下部に通気孔を設 け、又、下端壁の下には下に開放した処理水の集液室を
設けたことを特徴とする中空糸膜による濾過モジュール
。(2) An inner cylinder whose upper part projects upward from the upper end of the protection cylinder is arranged in the vertical direction inside the protection cylinder in the vertical direction through which the raw water flows, and the inner periphery of the protection cylinder and the outer periphery of the inner cylinder are arranged in the vertical direction. The upper and lower ends of the cylindrical space formed by the inner cylinder are closed by an upper end wall and a lower end wall, and the lower end of the inner cylinder is also closed by the lower end wall, and inside the cylindrical space, a large number of hollow fiber membranes are installed in the vertical direction. and the upper end of each hollow fiber membrane is buried and closed in the upper end wall, and
The lower end penetrates the lower end wall and opens on the lower surface of the lower end wall, and ventilation holes are provided at the upper end, middle and lower part of the inner cylinder, and a treated water collection hole is opened below the lower end wall. A filtration module using a hollow fiber membrane characterized by having a chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP969489A JPH02191531A (en) | 1989-01-20 | 1989-01-20 | Filter module by hollow-fiber membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP969489A JPH02191531A (en) | 1989-01-20 | 1989-01-20 | Filter module by hollow-fiber membrane |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02191531A true JPH02191531A (en) | 1990-07-27 |
Family
ID=11727333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP969489A Pending JPH02191531A (en) | 1989-01-20 | 1989-01-20 | Filter module by hollow-fiber membrane |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02191531A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7087173B2 (en) | 1995-08-11 | 2006-08-08 | Zenon Environmental Inc. | Inverted cavity aerator for membrane module |
US7534353B2 (en) | 1995-08-11 | 2009-05-19 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
JP2012066246A (en) * | 1996-12-20 | 2012-04-05 | Siemens Water Technologies Corp | Scouring method |
-
1989
- 1989-01-20 JP JP969489A patent/JPH02191531A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7087173B2 (en) | 1995-08-11 | 2006-08-08 | Zenon Environmental Inc. | Inverted cavity aerator for membrane module |
US7534353B2 (en) | 1995-08-11 | 2009-05-19 | Zenon Technology Partnership | Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes |
JP2012066246A (en) * | 1996-12-20 | 2012-04-05 | Siemens Water Technologies Corp | Scouring method |
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