JPS62273008A - Membrane module - Google Patents
Membrane moduleInfo
- Publication number
- JPS62273008A JPS62273008A JP11800986A JP11800986A JPS62273008A JP S62273008 A JPS62273008 A JP S62273008A JP 11800986 A JP11800986 A JP 11800986A JP 11800986 A JP11800986 A JP 11800986A JP S62273008 A JPS62273008 A JP S62273008A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- membrane wall
- water
- treated
- membrane module
- 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 56
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000010008 shearing Methods 0.000 abstract 1
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/20—By influencing the flow
- B01D2321/2008—By influencing the flow statically
- B01D2321/2016—Static mixers; Turbulence generators
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
8 発明の詳細な説明
〔産業上の利用分野〕
本発明は、管状膜壁の内外一側に被処理水用流路を形成
すると共に、他側に誤処理水用流路を形成してある液体
処理用膜モジュールに関する。Detailed Description of the Invention 8 Detailed Description of the Invention [Industrial Field of Application] The present invention provides a method for forming a flow path for water to be treated on one side of the inner and outer sides of a tubular membrane wall, and a flow path for water to be treated on the other side. The present invention relates to a membrane module for liquid treatment in which a flow path is formed.
ひLれるように、被処理水用流路0R1)を形成してあ
った。A flow path 0R1) for the water to be treated was formed so that the water flow path 0R1) could be opened.
しかし、被処理水の流れは、中心部よりも膜Q(1A)
近傍が迷い流れとなるために、彼処理水の処理に伴って
膜壁(1A)にスケールが蓄積しや(く、短期で目詰ま
りする欠点があろた。However, the flow of the water to be treated is closer to the membrane Q (1A) than from the center.
Due to the stray flow in the vicinity, scale tends to accumulate on the membrane wall (1A) during the treatment of treated water, resulting in clogging in a short period of time.
本発明の目的は、膜壁のスケールを抑制できるようにす
る点にある。An object of the present invention is to suppress scale on the membrane wall.
本発明の水処理用膜モジュールの特徴構成は、被処理水
用流路内に、管状膜壁の中心周りで旋回流を生じさせる
ガイドを設けてあることにあり、その作用効果は、次の
通りCある。The characteristic structure of the membrane module for water treatment of the present invention is that a guide is provided in the flow path for water to be treated to generate a swirling flow around the center of the tubular membrane wall, and its effects are as follows. There is street C.
つまり、被処理水用流路を流れる被処理水は、ガイドに
よって旋回流となって、膜壁近傍での流述が速くなるた
め膜壁近傍はその流速の増加に比例してl断力が増加す
ることとなる。In other words, the water to be treated flowing through the flow path for treated water becomes a swirling flow due to the guide, and the flow rate near the membrane wall increases, so that the shear force near the membrane wall increases in proportion to the increase in flow velocity. This will result in an increase.
その結果、膜壁へ堆漬しようとするスケールは、堆積出
来ず、膜壁のスケーリング層を従来よりも抑制すること
となる。 即ち、膜のブランクスの低下を防止すること
となる。As a result, the scale that attempts to deposit on the membrane wall cannot be deposited, and the scaling layer on the membrane wall is suppressed more than before. In other words, deterioration of the membrane blank is prevented.
従って、被処理水の供給流速を増加させなくとも、長期
にわたって簡単な構造で7ラツクスを効率良く維持する
ことができた。Therefore, it was possible to efficiently maintain 7 lux over a long period of time with a simple structure without increasing the supply flow rate of the water to be treated.
次に、本発明の実施例を、図面に基づいて説ツクス製膜
チューブfl)の複数本を、夫々の両端部が管叉狩板(
2)に支持された状態で、ステンレス族の族モジュール
容器(3)に内装し、膜チューブfilの一端に連通ず
る彼処理水の供給口(4A)を備えたステンレス製第1
接続部材(4)を、膜モジュール(3)の一端に取付け
ると共に、各膜チューブfl)の他端に連通ずる処理済
水の排出口(5A)を備えたステンレス製@2接続部材
(6)を、膜モジユール容器(3)の他f−に取付け、
膜モジュール(3)の周壁に、各膜チューブ(1)から
透過した処理液の回収口(8A)を設けて族モジュール
を構成してある。Next, an embodiment of the present invention will be explained based on the drawings.
2), the first stainless steel module is installed inside the stainless steel module container (3) and is equipped with a treated water supply port (4A) communicating with one end of the membrane tube fil.
A connecting member (4) is attached to one end of the membrane module (3), and a stainless steel @2 connecting member (6) is provided with a treated water outlet (5A) communicating with the other end of each membrane tube fl). Attach it to f- in addition to the membrane module container (3),
A collection port (8A) for the treatment liquid permeated from each membrane tube (1) is provided on the peripheral wall of the membrane module (3) to constitute a group module.
@1図イ)(ロ)に示すように、前記膜チューブ(1)
は、その膜壁(1A)の内側に被処理水用流f111α
1)を形成すると共に、外側に処理水用流路(R2)を
形成してあり、被処理水用流路(R+)を形成する膜壁
(1A)内面に、軸芯周りでの旋回流を生じさせるよう
に、螺旋状の突起(9)を一体形成してある。As shown in Figure 1 (a) and (b), the membrane tube (1)
is a flow f111α for water to be treated inside the membrane wall (1A).
1), a flow path for treated water (R2) is formed on the outside, and a swirling flow around the axis is formed on the inner surface of the membrane wall (1A) forming the flow path for treated water (R+). A spiral protrusion (9) is integrally formed so as to produce the following.
そして、前記突起(9)を内面に形成した膜チューブ+
13は、第2図に示す断面形状の口金i10+から、押
出し成形により製造され、口金[101に対して押出さ
れたチューブillを相対回転させながら受けることで
、内面に螺旋状の突起(9)が一体形成された状態に成
形される。and a membrane tube + having the protrusion (9) formed on its inner surface.
13 is manufactured by extrusion molding from a cap i10+ having the cross-sectional shape shown in FIG. are molded into an integrated state.
前記セラミックス製膜チューブ(1)に代え、ポリスル
ホン・セルローズアセテート等の有機系高分子材料でコ
ーティングされたものでも良く、それらを膜モジュール
と総称する。Instead of the ceramic membrane tube (1), one coated with an organic polymer material such as polysulfone or cellulose acetate may be used, and these are collectively referred to as a membrane module.
前記突起(9)は、第4図に示すように径方向の対向す
る位置に一対投けたり、第6図に示すように、断面弯曲
形状にしても良い。The protrusions (9) may be provided in pairs at radially opposite positions as shown in FIG. 4, or may have a curved cross section as shown in FIG.
また、第G図イ)、(ロ)及び第7図に示すように、膜
チューブ[1)の外周面に、外方に突出する突起(9)
を管中心円りに螺旋状に一体形成しても良く、この場合
は、膜壁(1A)の外側に被処理水用流路(R+)を形
成すると共に、内側に処理水用流路(R2)を形成すれ
ばよい。In addition, as shown in Figure G A), (B) and Figure 7, there are protrusions (9) projecting outward on the outer peripheral surface of the membrane tube [1].
may be integrally formed in a spiral shape around the center of the tube. In this case, a flow path for treated water (R+) is formed on the outside of the membrane wall (1A), and a flow path for treated water (R+) is formed on the inside of the membrane wall (1A). R2) may be formed.
前記突起(9)は、蝶旋状をこ連続するもの以外に断続
的に形成してあるものでも良(、単にガイドと称する。The protrusions (9) may be formed intermittently instead of continuously forming a spiral shape (simply referred to as a guide).
図面は本発明に係る膜モジュールの実施例を示し、第1
図(イ)は膜モジュールの斜視図、第1図(ロ)は膜モ
ジュールの断面図、第2図は口金の断面図、第8図は膜
モジュールの全体断面図、第4図、第5図は別実施例の
膜モジュールの断面図、第6図イ)は別実施例の一部断
面を示す側面図、第7図(ロ)は(イ)の側面図、第7
図は別実施例の暎モジュールの断面図、第8図は従来例
をボす膜モジュールの−giS断面を有する側面図であ
る。
(1A)・・・・・・膜壁、(9)・・・・・・ガイ
ド、(R+)・・・・・・被処理水用流路、(Rx)
−−処理水用流路。。
代理人 弁理士 北 村 修
第7図
第8図
手続補正書(鳥人)
%式%
2、発明の名称
膜モジュール
3、補正をする者
事件との関係 特許出願人
住 所 大阪府大阪市浪速区敷津東1丁目2番47号名
称 (105) 久保田鉄工株式会社4、代理人
7、補正の内容
明細書第5頁13行目〜第6頁5行目の「図面の簡単な
説明」の欄を次のように訂正します。
「4、図面の簡単な説明
図面は本発明に係る膜モジュールの実施例を示し、第1
図(イ)は膜モジュールの斜視図、第1図(II)は膜
モジュールの断面図、第2図は口金の断面図、第3図は
膜モジュールの全体断面図、第4図、第5図は別実施例
の膜モジュールの断面図、第6図(イ)は別実施例の一
部断面を示す側面図、第6図(El)は(イ)の側面図
、第7図は別実施例の膜モジュールの断面図、第8図は
従来例を示す膜モジュールの一部断面を有する側面図で
ある。The drawings show an embodiment of the membrane module according to the present invention.
Figure (A) is a perspective view of the membrane module, Figure 1 (B) is a sectional view of the membrane module, Figure 2 is a sectional view of the cap, Figure 8 is an overall sectional view of the membrane module, Figures 4 and 5. The figure is a sectional view of a membrane module of another embodiment, FIG. 6(a) is a side view showing a partial cross section of another embodiment, FIG.
The figure is a sectional view of a membrane module according to another embodiment, and FIG. 8 is a side view of a membrane module of a conventional example, having a -giS cross section. (1A)...Membrane wall, (9)...Guy
(R+)...Flow path for treated water, (Rx)
--Flow path for treated water. . Agent Patent attorney Osamu Kitamura Figure 7 Figure 8 Procedural amendment (Birdman) % formula % 2. Name of the invention Membrane module 3. Relationship with the case of the person making the amendment Patent applicant address Naniwa, Osaka City, Osaka Prefecture 1-2-47 Shikitsu Higashi, Ward Name (105) Kubota Tekko Co., Ltd. 4, Agent 7, “Brief explanation of the drawings” from page 5, line 13 to page 6, line 5 of the statement of contents of the amendment ” column as follows. "4. Brief description of the drawings The drawings show an embodiment of the membrane module according to the present invention, and the first
Figure (A) is a perspective view of the membrane module, Figure 1 (II) is a sectional view of the membrane module, Figure 2 is a sectional view of the cap, Figure 3 is an overall sectional view of the membrane module, Figures 4 and 5. The figure is a cross-sectional view of a membrane module of another embodiment, Figure 6 (A) is a side view showing a partial cross section of another embodiment, Figure 6 (El) is a side view of (A), and Figure 7 is another example. FIG. 8 is a sectional view of a membrane module according to an embodiment, and FIG. 8 is a side view with a partial cross section of a membrane module showing a conventional example.
Claims (1)
)を形成すると共に、他側に膜処理水用流路(R_2)
を形成してある膜モジュールであつて、前記被処理水用
流路(R_1)内に、前記管状膜壁(1_A)の中心周
りでの旋回流を生じさせるガイド(9)を設けてある膜
モジュール。There is a flow path (R_1) for treated water on one side of the inner and outer sides of the tubular membrane wall (1A).
) and a membrane-treated water flow path (R_2) on the other side.
A membrane module comprising: a guide (9) for generating a swirling flow around the center of the tubular membrane wall (1_A) in the water flow path (R_1); module.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11800986A JPS62273008A (en) | 1986-05-22 | 1986-05-22 | Membrane module |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11800986A JPS62273008A (en) | 1986-05-22 | 1986-05-22 | Membrane module |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62273008A true JPS62273008A (en) | 1987-11-27 |
Family
ID=14725794
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11800986A Pending JPS62273008A (en) | 1986-05-22 | 1986-05-22 | Membrane module |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62273008A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07236820A (en) * | 1994-02-28 | 1995-09-12 | Hiroyoshi Inoue | Method for increasing separation speed in membrane separation operation and filter device therefor |
US5647950A (en) * | 1991-06-28 | 1997-07-15 | Pall Corporation | Filter assembly with a spin welded end cap |
US5776342A (en) * | 1995-01-13 | 1998-07-07 | Pall Corporation | Filter assembly |
JPH1119480A (en) * | 1997-06-27 | 1999-01-26 | Hitachi Metals Ltd | Precision filter |
EP3643385A4 (en) * | 2017-06-21 | 2021-04-28 | M. Technique Co., Ltd. | Filtration membrane module and filtration method |
-
1986
- 1986-05-22 JP JP11800986A patent/JPS62273008A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5647950A (en) * | 1991-06-28 | 1997-07-15 | Pall Corporation | Filter assembly with a spin welded end cap |
JPH07236820A (en) * | 1994-02-28 | 1995-09-12 | Hiroyoshi Inoue | Method for increasing separation speed in membrane separation operation and filter device therefor |
US5776342A (en) * | 1995-01-13 | 1998-07-07 | Pall Corporation | Filter assembly |
JPH1119480A (en) * | 1997-06-27 | 1999-01-26 | Hitachi Metals Ltd | Precision filter |
EP3643385A4 (en) * | 2017-06-21 | 2021-04-28 | M. Technique Co., Ltd. | Filtration membrane module and filtration method |
US11161079B2 (en) | 2017-06-21 | 2021-11-02 | M. Technique Co., Ltd. | Filtration membrane module and filtration processing method |
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