JPH1028849A - Spiral type membrane module - Google Patents

Spiral type membrane module

Info

Publication number
JPH1028849A
JPH1028849A JP19086996A JP19086996A JPH1028849A JP H1028849 A JPH1028849 A JP H1028849A JP 19086996 A JP19086996 A JP 19086996A JP 19086996 A JP19086996 A JP 19086996A JP H1028849 A JPH1028849 A JP H1028849A
Authority
JP
Japan
Prior art keywords
raw water
membrane
bag
wound body
water
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
Application number
JP19086996A
Other languages
Japanese (ja)
Inventor
Keiji Kamimura
啓二 上村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
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.)
Filing date
Publication date
Application filed by Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP19086996A priority Critical patent/JPH1028849A/en
Priority to US08/895,838 priority patent/US5858229A/en
Priority to DE69731430T priority patent/DE69731430T2/en
Priority to EP97305406A priority patent/EP0819466B1/en
Publication of JPH1028849A publication Critical patent/JPH1028849A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a spiral type membrane module which does not need a water collection pipe and has small permeation water passage resistance by making a winding body by winding a bag-shaped membrane into which a channel material is inserted onto a shaft and dividing a raw water channel into a raw water outward route and a raw water backward route by a partition material which extends in the channel. SOLUTION: A channel material 15 is inserted into a bag-shaped membrane 10 in which side parts 11, 12, 13 are closed and a side part 14 is opened, and adhesives 16, 17, 18 are applied on one surface of the membrane 10. The membrane 10 is wound onto a shaft 20 to form a winding body 24, and a socket 25 is attached to the front end surface of the winding body 24. The adhesive 16 extends from a part of the side part 12 in the longitudinal direction of the shaft 20 to be a partition material which divides a raw water channel into a raw water outward route 21 and a raw water backward route by curing. When raw water is introduced from the end surface on the peripheral side of the socket 25 into the route 21 between the bag-shaped membranes 10, 10, the water is made to permeate the membrane 10 while passing through the raw water channel, and the permeation water is discharged from the back end surface of the winding body 24.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、精密濾過装置、限
外濾過装置、逆浸透膜分離装置などの膜分離装置に用い
られるスパイラル型膜モジュールに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a spiral type membrane module used for a membrane separation device such as a microfiltration device, an ultrafiltration device and a reverse osmosis membrane separation device.

【0002】[0002]

【従来の技術】膜分離装置に用いられる膜モジュールと
して、集水管の外周に分離膜を巻回したスパイラル型膜
モジュールがある。
2. Description of the Related Art As a membrane module used in a membrane separation apparatus, there is a spiral type membrane module in which a separation membrane is wound around a water collecting pipe.

【0003】図5は従来のスパイラル型膜モジュールの
構造を示す一部分解斜視図である。
FIG. 5 is a partially exploded perspective view showing the structure of a conventional spiral membrane module.

【0004】集水管1の外周に複数の袋状の分離膜2が
メッシュスペーサ3を介して巻回されている。
A plurality of bag-shaped separation membranes 2 are wound around the outer periphery of a water collecting pipe 1 via a mesh spacer 3.

【0005】集水管1には管内外を連通するスリット状
開口が穿設されている。分離膜2は袋状のものであり、
その中央部が集水管1をくるんでいる。この袋状分離膜
2の内部にはメッシュスペーサ等よりなる流路材4が挿
入されており、この袋状分離膜(袋状膜)2の内部が透
過水流路となっている。
[0005] The water collecting pipe 1 is provided with a slit-shaped opening communicating with the inside and outside of the pipe. The separation membrane 2 has a bag shape,
The central part surrounds the water collection pipe 1. A channel material 4 made of a mesh spacer or the like is inserted inside the bag-shaped separation membrane 2, and the inside of the bag-shaped separation membrane (bag-shaped membrane) 2 is a permeated water channel.

【0006】袋状膜2の巻回体5の両端にトップリング
6とエンドリング7とが設けられ、その外周にブライン
シール8が周設されている。
[0006] A top ring 6 and an end ring 7 are provided at both ends of a wound body 5 of the bag-shaped membrane 2, and a brine seal 8 is provided around the outer periphery thereof.

【0007】原水は、巻回体5の前端面から袋状膜2同
士の間の原水流路に流入し、そのまま巻回体5の長手方
向に流れ、巻回体5の後端面から濃縮水として流出す
る。この原水流路を流れる間に水が袋状膜2を透過して
その内部に入り、集水管1内に流入し、該集水管1の後
端側からモジュール外に取り出される。
The raw water flows into the raw water flow path between the bag-shaped membranes 2 from the front end face of the wound body 5 and flows in the longitudinal direction of the wound body 5 as it is, and the concentrated water flows from the rear end face of the wound body 5 Leaked as. While flowing through the raw water flow path, water permeates the bag-like membrane 2 and enters the inside thereof, flows into the water collecting pipe 1, and is taken out of the module from the rear end side of the water collecting pipe 1.

【0008】[0008]

【発明が解決しようとする課題】上記従来のスパイラル
型膜モジュールには、次のような解決すべき課題があっ
た。
The above-mentioned conventional spiral type membrane module has the following problems to be solved.

【0009】 集水管1内の透過水流量を多くするた
めには該集水管1を大径化する必要があるが、そのよう
にするとスパイラル型膜モジュールの径も大きくなって
しまう。
In order to increase the flow rate of the permeated water in the water collecting pipe 1, it is necessary to increase the diameter of the water collecting pipe 1, but in such a case, the diameter of the spiral membrane module becomes large.

【0010】 袋状膜2内に透過してきた透過水は、
該袋状膜2内をスパイラル状に回りながら集水管1まで
流れるため、袋状膜2内の流通抵抗が大きい。しかも、
袋状膜2内から集水管1に流れ込む集水管スリット部付
近での流通抵抗も大きい。
The permeated water that has permeated into the bag-like membrane 2 is
Since the water flows into the water collecting pipe 1 while spirally rotating in the bag-shaped membrane 2, the flow resistance in the bag-shaped membrane 2 is large. Moreover,
The flow resistance near the slit portion of the water collecting pipe flowing into the water collecting pipe 1 from inside the bag-shaped membrane 2 is also large.

【0011】 原水流路を流れる原水流量は、下流側
になるほど減少する。(原水が濃縮される分だけ原水流
量が減る。)このため、原水流路下流域では原水流速が
小さくなり、汚れが付着し易くなる。
[0011] The flow rate of the raw water flowing through the raw water flow path decreases toward the downstream side. (The flow rate of the raw water is reduced by an amount corresponding to the concentration of the raw water.) For this reason, the flow velocity of the raw water is reduced in the downstream region of the raw water flow path, and dirt is easily attached.

【0012】本発明は、上記従来の問題点を解決し、集
水管が不要であり、透過水流通抵抗が小さいスパイラル
型膜モジュールを提供することを目的とする。
An object of the present invention is to solve the above-mentioned conventional problems and to provide a spiral-wound membrane module which does not require a water collecting pipe and has low permeated water flow resistance.

【0013】また、本発明は、原水流路下流域でも原水
(濃縮水)の流速を大きなものとすることができるスパ
イラル型膜モジュールを提供することを目的とする。
Another object of the present invention is to provide a spiral-wound membrane module that can increase the flow rate of raw water (concentrated water) even in the downstream region of the raw water flow path.

【0014】[0014]

【課題を解決するための手段】本発明のスパイラル型膜
モジュールは、袋状膜の内部に透過水流路材が配置さ
れ、袋状膜同士の間には原水流路材が配置されているス
パイラル型膜モジュールにおいて、該袋状膜は第1、第
2、第3及び第4の辺部を有した略方形であり、該第
1、第2及び第3の辺部は封じられ、該第4の辺部が開
放部となっており、前記第4の辺部と直交する第1の辺
部をシャフトに当てて袋状膜を巻回して巻回体とし、前
記第4の辺部を該巻回体の後端面に臨ませ、該第4の辺
部に対向する第2の辺部を該巻回体の前端面に臨ませ、
該袋状膜同士の間の原水流路は、該第3及び第4の辺部
において封じられており、該原水流路は、該巻回体の軸
心線と略平行方向に該巻回体の前端面から巻回体の該軸
心線方向の途中まで延在する仕切材によって原水往路と
原水復路とに区画され、該原水往路と原水復路とは該巻
回体の後部側で連通しており、該原水往路は、該巻回体
の前端面の外周側及び内周側の一方に臨んでおり、該原
水復路は、該巻回体の前端面の外周側及び内周側の他方
に臨んでいることを特徴とするものである。
The spiral-type membrane module of the present invention has a spiral membrane in which a permeated water flow path material is disposed inside a bag-like membrane, and a raw water flow path material is disposed between the bag-like membranes. In the mold membrane module, the bag-like membrane is a substantially rectangular shape having first, second, third, and fourth sides, and the first, second, and third sides are sealed, and 4 is an open portion, a first side perpendicular to the fourth side is applied to a shaft, and a bag-shaped membrane is wound to form a roll. Facing the rear end face of the wound body, facing the second side facing the fourth side to the front end face of the wound body,
The raw water flow path between the bag-shaped membranes is sealed at the third and fourth sides, and the raw water flow path is wound in a direction substantially parallel to the axis of the wound body. A raw material forward path and a raw water return path are defined by a partition member extending from the front end surface of the body to the middle of the wound body in the axial direction, and the raw water forward path and the raw water return path communicate with each other on the rear side of the wound body. The raw water outward path faces one of the outer peripheral side and the inner peripheral side of the front end face of the wound body, and the raw water return path is the outer peripheral side and the inner peripheral side of the front end face of the wound body. It is characterized by facing the other.

【0015】かかるスパイラル型膜モジュールにおいて
は、巻回体の前端面の外周側(又は内周側)から原水が
原水往路に流入する。この原水は、原水往路を巻回体軸
心線と略平行方向に流れ、次いで流れ方向を反転させ、
原水復路を流れ、巻回体前端面の内周側(又は外周側)
から濃縮水として流出する。
In such a spiral-wound membrane module, raw water flows into the raw water outward path from the outer peripheral side (or inner peripheral side) of the front end face of the wound body. This raw water flows in the raw water outward path in a direction substantially parallel to the axis of the wound body, and then reverses the flow direction,
It flows through the raw water return path and is on the inner side (or outer side) of the front end surface of the wound body
From the wastewater as concentrated water.

【0016】袋状膜を透過した水は、袋状膜内を巻回体
軸心線と略平行方向に流れ、巻回体の後端面の開放口か
ら流出する。
The water that has passed through the bag-like membrane flows in the bag-like membrane in a direction substantially parallel to the axis of the wound body, and flows out from an opening at the rear end face of the wound body.

【0017】このように、透過水が袋状膜内を巻回体の
軸心線と平行方向に流れるため、従来のスパイラル型膜
モジュールに用いられていた集水管が不要となる。そし
て、袋状膜内から該集水管内に流れ込む際の流通抵抗が
無くなり、透過水流通抵抗が小さくなる。
As described above, since the permeated water flows in the bag-shaped membrane in a direction parallel to the axis of the wound body, the water collecting pipe used in the conventional spiral membrane module becomes unnecessary. Then, there is no flow resistance when flowing into the water collecting pipe from inside the bag-shaped membrane, and the flow resistance of permeated water is reduced.

【0018】なお、集水管を無くしているため、その分
だけ袋状膜の巻回方向の長さを大きくとることができ、
膜面積を拡張できる。そして、このように袋状膜の巻回
方向長さを大きくしても透過水の流通抵抗は増大せず、
透過水量を多くすることができる。
Since the water collecting pipe is eliminated, the length of the bag-like membrane in the winding direction can be increased accordingly.
The membrane area can be expanded. And even if the length in the winding direction of the bag-like membrane is increased, the flow resistance of the permeated water does not increase,
The amount of permeated water can be increased.

【0019】本発明では、原水往路及び原水復路の流路
幅を下流側ほど小さくするのが好ましい。このようにす
ることにより、原水流路の下流側での原水(濃縮水)流
速を従来よりも高めることができ、原水流路下流域にお
ける汚れの付着を防止できる。
In the present invention, it is preferable that the flow path widths of the raw water outgoing path and the raw water return path are made smaller toward the downstream side. By doing so, the flow rate of the raw water (concentrated water) on the downstream side of the raw water flow path can be increased as compared with the conventional case, and the adhesion of dirt in the downstream area of the raw water flow path can be prevented.

【0020】本発明では、複数枚の袋状膜が一つのシャ
フトの周りに巻回されており、前記仕切材は、一つの袋
状膜とそれに重なる別の袋状膜との間に介在され、該仕
切材は該袋状膜の数と同数個設けられており、該仕切材
の前端部は、それぞれ該巻回体の前端面に臨み、且つ巻
回体の軸心から等半径位に位置しており、前記仕切材の
前端部に連なる円筒状のソケットが巻回体と同軸的に巻
回体の前端面に連設されていることが好ましい。このソ
ケットによって原水の流入側と濃縮水の流出側とが区画
される。
In the present invention, a plurality of bag-like membranes are wound around one shaft, and the partition member is interposed between one bag-like membrane and another bag-like membrane overlapping therewith. The same number of the partition members as the number of the bag-shaped membranes are provided, and the front ends of the partition members face the front end surface of the wound body, respectively, and are at the same radius from the axis of the wound body. It is preferable that a cylindrical socket, which is located and is continuous with the front end of the partition member, is connected to the front end face of the wound body coaxially with the wound body. The socket separates the inflow side of the raw water and the outflow side of the concentrated water.

【0021】本発明では、袋状膜の第2の辺部のうち前
記仕切材の前端部の位置からフィンが突設されており、
該フィンが前記ソケットに接合されていることが好まし
い。このようにすることにより、ソケットと仕切材とが
フィンを介してつながるようになり、原水の流入側と濃
縮水の流出側とが水密的に区分けされる。
In the present invention, fins are protruded from the position of the front end of the partition member in the second side of the bag-like membrane,
Preferably, the fin is joined to the socket. By doing so, the socket and the partition member are connected via the fins, and the inflow side of the raw water and the outflow side of the concentrated water are separated in a watertight manner.

【0022】[0022]

【発明の実施の形態】以下図面を参照して発明の実施の
形態について説明する。図1(a)は本発明の実施の形
態に係るスパイラル型膜モジュールに用いられる一枚の
袋状膜及び該袋状膜が巻き付けられるシャフトの斜視図
である。図1(b),(c)はそれぞれ図1(a)のB
−B線、C−C線に沿う断面図である。図1(d)は図
1(a)のD付近の構成を示す斜視図である。図2はシ
ャフトの周りに袋状膜を巻き付ける方法を示す断面図、
図3は巻回体とソケットとの係合関係を示す斜視図、図
4はスパイラル型膜モジュールの側面図である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1A is a perspective view of one bag-like membrane used in the spiral membrane module according to the embodiment of the present invention and a shaft around which the bag-like membrane is wound. FIGS. 1B and 1C respectively show B in FIG. 1A.
It is sectional drawing which follows the -B line and CC line. FIG. 1D is a perspective view showing a configuration near D in FIG. 1A. FIG. 2 is a sectional view showing a method of winding a bag-like membrane around a shaft;
FIG. 3 is a perspective view showing an engagement relationship between the wound body and the socket, and FIG. 4 is a side view of the spiral membrane module.

【0023】この実施の形態に用いられている袋状膜1
0は、正方形又は長方形状のものであり、第1の辺部1
1、第2の辺部12、第3の辺部13及び第4の辺部1
4を有している。この袋状膜10は、長い一枚の分離膜
フィルムを第2の辺部12の部分で二つに折り返し、第
1の辺部11及び第3の辺部13において折り重なった
分離膜フィルム同士を接着剤等によって接着し、第4の
辺部14については接着を行うことなく開放口とした袋
状のものである。この袋状の膜10内に流路材(例えば
メッシュスペーサ等よりなる。)15が挿入配置されて
いる。なお、第2の辺部12部分で二つに折り返さず二
枚の分離膜フィルムを第1の辺部11、第2の辺部1
2、第3の辺部13を接着するようにしても良い。
The bag-like membrane 1 used in this embodiment
0 is a square or rectangular shape, and the first side 1
1, second side 12, third side 13, and fourth side 1
Four. This bag-shaped membrane 10 is formed by folding one long separation membrane film into two at the second side portion 12 and separating the separation membrane films folded at the first side portion 11 and the third side portion 13 from each other. The fourth side portion 14 is formed in a bag-like shape with an open port without bonding. A flow path material (for example, made of a mesh spacer or the like) 15 is inserted and arranged in the bag-shaped membrane 10. Note that the two separation membrane films are not folded in two at the second side portion 12 and the two separation membrane films are separated into the first side portion 11 and the second side portion 1.
The second and third sides 13 may be bonded.

【0024】この袋状膜10の一方の面には、接着剤1
6,17,18が付着され、この袋状膜10がシャフト
20の周りに巻き付けられる。接着剤16は、第2の辺
部12の途中部分からシャフト20の長手方向と略平行
方向に延在している。この実施の形態にあっては、接着
剤16は長帯状に付着されており、第2の辺部12から
離れるほど第1の辺部11から離反する方向に斜めに設
けられている。
On one surface of the bag-like film 10, an adhesive 1
6, 17, 18 are attached, and the bag-like membrane 10 is wound around the shaft 20. The adhesive 16 extends from an intermediate portion of the second side portion 12 in a direction substantially parallel to the longitudinal direction of the shaft 20. In this embodiment, the adhesive 16 is applied in a long strip shape, and is provided obliquely in a direction away from the first side 11 as the distance from the second side 12 increases.

【0025】接着剤17は第3の辺部13に沿って付着
され、接着剤18は第4の辺部14に沿って付着されて
いる。
The adhesive 17 is applied along the third side 13, and the adhesive 18 is applied along the fourth side 14.

【0026】複数枚の袋状膜10をシャフト20の周囲
に巻き付けることにより、重なり合った袋状膜10同士
は接着剤16,17,18の部分において水密的に接合
される。これにより、袋状膜10,10同士の間には、
矢印,,,の順で原水(及び濃縮水)が流れる
原水流路が構成される。接着剤16は、硬化することに
より原水流路を原水往路21と原水復路22とに区画す
る仕切材となる。
By wrapping a plurality of bag-like films 10 around the shaft 20, the overlapping bag-like films 10 are joined to each other at the adhesives 16, 17, and 18 in a water-tight manner. Thereby, between the bag-shaped membranes 10 and 10,
A raw water flow path through which raw water (and concentrated water) flows in the order of arrows,. The adhesive 16 becomes a partitioning material that partitions the raw water flow path into the raw water forward path 21 and the raw water return path 22 by being cured.

【0027】この実施の形態にあっては、第2の辺部1
2のうち接着剤16の端部が臨む部分から、前方に向っ
てフィン19が延設されている。このフィン19は、例
えば合成樹脂フィルム又はシートよりなり、袋状膜10
に対し接着等により接合されるのが好ましい。
In this embodiment, the second side 1
A fin 19 extends forward from a portion of the 2 facing the end of the adhesive 16. The fin 19 is made of, for example, a synthetic resin film or sheet, and
It is preferred to be bonded by bonding or the like.

【0028】袋状膜10,10…をシャフト20の周り
に巻き付けることにより、図3に示すように巻回体24
が形成される。この巻回体24の前端面からは、フィン
19が延出する。各袋状膜10の第2の辺部12におい
て同一箇所にフィン19を設けておくことにより、フィ
ン19は巻回体24の軸心から等半径位上に位置し、フ
ィン19が重なり合うことによりフィン19がリング状
の突出部を形成することになる。このリング状の突出部
内に円筒状のソケット25の後端を挿入し、該ソケット
25とフィン19を接着剤等により接合する。なお、ソ
ケット25をフィン19に外嵌めしても良い。また、フ
ィン19の部分を旋盤で切込み溝を付け、該溝にソケッ
ト25を埋め込むようにしても良い。
By wrapping the bag-like membranes 10, 10,... Around the shaft 20, as shown in FIG.
Is formed. The fin 19 extends from the front end face of the wound body 24. By providing the fins 19 at the same location on the second side portion 12 of each bag-like membrane 10, the fins 19 are located on the same radius from the axis of the wound body 24, and the fins 19 overlap. The fin 19 forms a ring-shaped protrusion. The rear end of the cylindrical socket 25 is inserted into the ring-shaped protrusion, and the socket 25 and the fin 19 are joined with an adhesive or the like. Note that the socket 25 may be externally fitted to the fin 19. Alternatively, the fin 19 may be provided with a cutting groove using a lathe, and the socket 25 may be embedded in the groove.

【0029】このようにソケット25とフィン19とを
接合することにより、巻回体24の前端面の外周側に原
水の流入口が形成され、ソケット25の内周側に濃縮水
の流出口が形成される。
By joining the socket 25 and the fins 19 in this manner, an inlet for raw water is formed on the outer peripheral side of the front end face of the wound body 24, and an outlet for concentrated water is formed on the inner peripheral side of the socket 25. It is formed.

【0030】なお、図4に示すように、巻回体24の前
縁及び後縁にそれぞれトップリング26及びエンドリン
グ27を合成樹脂モールド等により形成し、トップリン
グ26の外周にブラインシール28を周設する。
As shown in FIG. 4, a top ring 26 and an end ring 27 are respectively formed on the front edge and the rear edge of the wound body 24 by a synthetic resin mold or the like, and a brine seal 28 is provided on the outer periphery of the top ring 26. Install around.

【0031】なお、袋状膜10をシャフト20の周りに
巻き付けるに際しては、図2に示すように、接着剤16
よりも内周側と外周側とにそれぞれメッシュスペーサ2
9,30を介在させておく。これらのメッシュスペーサ
29,30を介在させることにより、原水流路が構成さ
れる。
When the bag-like film 10 is wound around the shaft 20, as shown in FIG.
Mesh spacers 2 on the inner peripheral side and the outer peripheral side
9, 30 are interposed. With these mesh spacers 29 and 30 interposed, a raw water flow path is formed.

【0032】このように構成されたスパイラル型膜モジ
ュールにおいては、図4に示すように、ソケット25の
外周側の端面から原水が袋状膜10,10同士の間の原
水往路21に流入する。この原水は、巻回体24の軸心
線と略平行方向に原水往路21を流れ、次いで図1の
のように接着剤16(仕切材)の先端側を回り込んで原
水復路22に流入し、再び巻回体24の軸心線と平行方
向に流れ、ソケット25の内側の端面から取り出され
る。そして、このように原水が原水流路を流れる間に、
水が袋状膜10内に透過し、透過水は巻回体24の後端
面から流出する。
In the spiral membrane module configured as described above, as shown in FIG. 4, raw water flows into the raw water outgoing path 21 between the bag-like membranes 10 from the outer peripheral end face of the socket 25. This raw water flows through the raw water outward path 21 in a direction substantially parallel to the axis of the wound body 24, and then flows around the tip side of the adhesive 16 (partition material) as shown in FIG. 1 and flows into the raw water return path 22. Flows again in a direction parallel to the axis of the wound body 24 and is taken out from the inner end face of the socket 25. And while raw water flows through the raw water flow path in this way,
Water permeates into the bag-like membrane 10, and the permeated water flows out from the rear end face of the wound body 24.

【0033】このスパイラル型膜モジュールにあって
は、透過水が袋状膜10内を巻回体24の軸心線と平行
方向に流れて後端面から取り出されるため、従来のスパ
イラル型膜モジュールに用いられていた集水管が不要で
ある。このため、袋状膜から集水管内に流れ込む際の流
通抵抗が無くなり、透過水流通抵抗が著しく小さくな
る。
In this spiral type membrane module, the permeated water flows in the bag-like membrane 10 in a direction parallel to the axis of the wound body 24 and is taken out from the rear end face. The used collecting pipe is unnecessary. For this reason, the flow resistance when flowing from the bag-like membrane into the water collecting pipe is eliminated, and the permeated water flow resistance is significantly reduced.

【0034】なお、集水管を省略しており、その分だけ
袋状膜10の巻回方向の長さを大きくとることができ、
膜面積を大きくとることが可能である。袋状膜の巻回方
向の長さを大きくしても、透過水流通抵抗は増大せず、
透過水量を多くすることができる。
The water collecting pipe is omitted, and the length of the bag-like membrane 10 in the winding direction can be increased accordingly.
It is possible to increase the film area. Even if the length of the bag-like membrane in the winding direction is increased, the permeated water flow resistance does not increase,
The amount of permeated water can be increased.

【0035】この実施の形態にあっては、原水往路21
及び原水復路22はそれぞれ下流側ほど流路幅が小さく
なるように構成されている。従って、原水流路の下流側
においても原水(濃縮水)の流速が十分に大きなものと
なり、原水流路下流域における汚れの付着を防止するこ
とができる。
In this embodiment, the raw water
The raw water return path 22 is configured such that the flow path width becomes smaller toward the downstream side. Therefore, the flow rate of the raw water (concentrated water) becomes sufficiently large also on the downstream side of the raw water flow path, and it is possible to prevent the adhesion of dirt in the downstream area of the raw water flow path.

【0036】また、この実施の形態にあっては、ソケッ
ト25をフィン19を用いて巻回体24に接続してお
り、ソケット25と巻回体24との接続強度が高い。そ
して、このソケット25によって原水の流入側と濃縮水
の流出側とが水密的に区画分離される。
Further, in this embodiment, the socket 25 is connected to the winding body 24 using the fins 19, and the connection strength between the socket 25 and the winding body 24 is high. Then, the inflow side of the raw water and the outflow side of the concentrated water are partitioned in a watertight manner by the socket 25.

【0037】なお、上記実施の形態においては、ソケッ
ト25の外周側に原水流入部を配置し、ソケット25の
内側に濃縮水流出部を配置しているが、逆にソケット2
5の内側を原水流入部とし、ソケット25の外周側を濃
縮水流入部としても良い。ただし、この場合には、接着
剤16を図1とは逆向きに、即ち接着剤16が第2の辺
部12から離れるほど第1の辺部11に接近するように
傾ける。
In the above-described embodiment, the raw water inflow portion is arranged on the outer peripheral side of the socket 25 and the concentrated water outflow portion is arranged inside the socket 25.
5 may be used as the raw water inflow portion, and the outer peripheral side of the socket 25 may be used as the concentrated water inflow portion. However, in this case, the adhesive 16 is inclined in the opposite direction to that in FIG. 1, that is, so that the adhesive 16 gets closer to the first side 11 as the distance from the second side 12 increases.

【0038】[0038]

【発明の効果】以上の通り、本発明のスパイラル型膜モ
ジュールにおいては、集水管が不要であり、透過水の流
通抵抗が小さい。また、膜面積を大きくとることがで
き、しかも膜面積を大きくしても透過水流通抵抗が増大
しない。
As described above, the spiral-wound membrane module of the present invention does not require a water collecting pipe and has low flow resistance of permeated water. Further, the membrane area can be increased, and even if the membrane area is increased, the permeated water flow resistance does not increase.

【0039】本発明では、原水流路の下流域における原
水(濃縮水)の流速を大きくし、原水流路下流域におけ
る汚れの付着を防止することも可能である。
According to the present invention, it is also possible to increase the flow rate of the raw water (concentrated water) in the downstream area of the raw water flow path to prevent the adhesion of dirt in the downstream area of the raw water flow path.

【図面の簡単な説明】[Brief description of the drawings]

【図1】(a)図は実施の形態に係る袋状膜の斜視図、
(b)図は(a)図のB−B線に沿う断面図、(c)図
は(a)図のC−C線に沿う断面図、(d)図は(a)
図のD付近の構成を示す斜視図である。
FIG. 1A is a perspective view of a bag-like membrane according to an embodiment,
(B) is a sectional view taken along line BB of (a), (c) is a sectional view taken along line CC of (a), and (d) is (a).
It is a perspective view which shows the structure of D vicinity of the figure.

【図2】実施の形態に係るスパイラル型膜モジュールの
袋状膜の巻き付け方法を示す断面図である。
FIG. 2 is a cross-sectional view showing a method of winding a bag-like membrane of the spiral membrane module according to the embodiment.

【図3】巻回体とソケットとの係合関係を示す斜視図で
ある。
FIG. 3 is a perspective view showing an engagement relationship between a wound body and a socket.

【図4】実施の形態に係るスパイラル型膜モジュールの
側面図である。
FIG. 4 is a side view of the spiral membrane module according to the embodiment.

【図5】従来のスパイラル型膜モジュールの構造を示す
一部分解斜視図である。
FIG. 5 is a partially exploded perspective view showing the structure of a conventional spiral membrane module.

【符号の説明】[Explanation of symbols]

10 袋状膜 11 第1の辺部 12 第2の辺部 13 第3の辺部 14 第4の辺部 15 流路材 16,17,18 接着剤 19 フィン 20 シャフト 21 原水往路 22 原水復路 24 巻回体 25 ソケット 29,30 メッシュスペーサ Reference Signs List 10 bag-like membrane 11 first side 12 second side 13 third side 14 fourth side 15 channel material 16, 17, 18 adhesive 19 fin 20 shaft 21 raw water outgoing path 22 raw water return path 24 Wound body 25 Socket 29, 30 Mesh spacer

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 袋状膜の内部に透過水流路材が配置さ
れ、袋状膜同士の間には原水流路材が配置されているス
パイラル型膜モジュールにおいて、 該袋状膜は第1、第2、第3及び第4の辺部を有した略
方形であり、該第1、第2及び第3の辺部は封じられ、
該第4の辺部が開放部となっており、 前記第4の辺部と直交する第1の辺部をシャフトに当て
て袋状膜を巻回して巻回体とし、前記第4の辺部を該巻
回体の後端面に臨ませ、該第4の辺部に対向する第2の
辺部を該巻回体の前端面に臨ませ、 該袋状膜同士の間の原水流路は、該第3及び第4の辺部
において封じられており、 該原水流路は、該巻回体の軸心線と略平行方向に該巻回
体の前端面から巻回体の該軸心線方向の途中まで延在す
る仕切材によって原水往路と原水復路とに区画され、 該原水往路と原水復路とは該巻回体の後部側で連通して
おり、 該原水往路は、該巻回体の前端面の外周側及び内周側の
一方に臨んでおり、 該原水復路は、該巻回体の前端面の外周側及び内周側の
他方に臨んでいることを特徴とするスパイラル型膜モジ
ュール。
1. A spiral-type membrane module in which a permeated water flow path material is disposed inside a bag-shaped membrane and a raw water flow path material is disposed between the bag-shaped membranes. A substantially rectangular shape having second, third and fourth sides, wherein the first, second and third sides are sealed;
The fourth side is an open section, and a first side perpendicular to the fourth side is applied to a shaft to wind a bag-like membrane to form a roll, and the fourth side is formed. Part facing the rear end face of the wound body, a second side part facing the fourth side part facing the front end face of the wound body, and a raw water flow path between the bag-shaped membranes. Are sealed at the third and fourth sides, and the raw water flow path extends from the front end face of the wound body in a direction substantially parallel to the axis of the wound body. The raw water forward path and the raw water return path are divided by a partition member extending halfway in the direction of the core line, and the raw water forward path and the raw water return path communicate with each other on the rear side of the winding body. A spiral characterized in that it faces one of the outer peripheral side and the inner peripheral side of the front end face of the wound body, and the raw water return path faces the other of the outer peripheral side and the inner peripheral side of the front end face of the wound body. Mold membrane Lumpur.
JP19086996A 1996-07-19 1996-07-19 Spiral type membrane module Pending JPH1028849A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP19086996A JPH1028849A (en) 1996-07-19 1996-07-19 Spiral type membrane module
US08/895,838 US5858229A (en) 1996-07-19 1997-07-17 Spiral wound type membrane module
DE69731430T DE69731430T2 (en) 1996-07-19 1997-07-18 Spirally wound membrane module
EP97305406A EP0819466B1 (en) 1996-07-19 1997-07-18 Spiral wound type membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19086996A JPH1028849A (en) 1996-07-19 1996-07-19 Spiral type membrane module

Publications (1)

Publication Number Publication Date
JPH1028849A true JPH1028849A (en) 1998-02-03

Family

ID=16265120

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19086996A Pending JPH1028849A (en) 1996-07-19 1996-07-19 Spiral type membrane module

Country Status (1)

Country Link
JP (1) JPH1028849A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11169684A (en) * 1997-12-12 1999-06-29 Kurita Water Ind Ltd Method of backwashing spiral membrane module
JP2010253360A (en) * 2009-04-23 2010-11-11 Kawasaki Thermal Engineering Co Ltd Method and apparatus for treating cooling water of refrigerator/cold and warm water machine
US8337698B2 (en) 2009-10-30 2012-12-25 A. O. Smith (Shanghai) Water Treatment Products Co., Ltd. Spiral wound reverse osmosis membrane element
CN107998894A (en) * 2016-12-27 2018-05-08 佛山市顺德区美的饮水机制造有限公司 Spiral wound reverse-osmosis membrane element and water purifier
CN108421416A (en) * 2017-02-14 2018-08-21 佛山市顺德区美的饮水机制造有限公司 Spiral wound reverse-osmosis membrane element and water purifier

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11169684A (en) * 1997-12-12 1999-06-29 Kurita Water Ind Ltd Method of backwashing spiral membrane module
JP2010253360A (en) * 2009-04-23 2010-11-11 Kawasaki Thermal Engineering Co Ltd Method and apparatus for treating cooling water of refrigerator/cold and warm water machine
US8337698B2 (en) 2009-10-30 2012-12-25 A. O. Smith (Shanghai) Water Treatment Products Co., Ltd. Spiral wound reverse osmosis membrane element
KR101302800B1 (en) * 2009-10-30 2013-09-02 에이. 오. 스미스 (상하이) 워터 트리트먼트 프로덕츠 컴퍼니 리미티드 A spiral wound reverse osmosis membrane element
CN107998894A (en) * 2016-12-27 2018-05-08 佛山市顺德区美的饮水机制造有限公司 Spiral wound reverse-osmosis membrane element and water purifier
CN107998894B (en) * 2016-12-27 2023-09-01 佛山市顺德区美的饮水机制造有限公司 Spiral wound reverse osmosis membrane element and water purifier
CN108421416A (en) * 2017-02-14 2018-08-21 佛山市顺德区美的饮水机制造有限公司 Spiral wound reverse-osmosis membrane element and water purifier

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