JPS6287206A - Method for washing pipe material for precision filtration - Google Patents
Method for washing pipe material for precision filtrationInfo
- Publication number
- JPS6287206A JPS6287206A JP22731685A JP22731685A JPS6287206A JP S6287206 A JPS6287206 A JP S6287206A JP 22731685 A JP22731685 A JP 22731685A JP 22731685 A JP22731685 A JP 22731685A JP S6287206 A JPS6287206 A JP S6287206A
- Authority
- JP
- Japan
- Prior art keywords
- micropores
- air
- fine
- bubbles
- semipermeable membrane
- 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
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
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- 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
- B01D2321/16—Use of chemical agents
- B01D2321/164—Use of bases
-
- 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
- B01D2321/16—Use of chemical agents
- B01D2321/168—Use of other chemical agents
-
- 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
- B01D2321/18—Use of gases
- B01D2321/185—Aeration
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】
〈産業上の利用分野〉
本発明は、被処理液中に浸漬されて、限外濾過により前
記被処理液を濾過するのに用いられ、その内管路または
管外から透過液が取出される精密濾過用管材の洗浄方法
に関する。Detailed Description of the Invention <Industrial Application Field> The present invention is used to filter the treated liquid by ultrafiltration by being immersed in a liquid to be treated. The present invention relates to a method for cleaning a precision filtration tube from which a permeate is extracted.
〈従来技術〉
精密濾過用管材aは、第1図に示すように、セルロース
とか、ポリアミド等の高分子膜等の半透膜すを中空管状
に形成してなるものであり、半透Hbの内部に内管路C
が形成される。前記管材aの管径は、例えば外径85ル
、内径42終等のように、極細状をしている。<Prior art> As shown in Fig. 1, precision filtration tube material a is formed by forming a semipermeable membrane such as cellulose or polymer membrane such as polyamide into a hollow tube shape, and is capable of semipermeable Hb. Internal pipe C
is formed. The diameter of the tube material a is extremely thin, for example, an outer diameter of 85 mm and an inner diameter of 42 mm.
前記管材aは、圧力0.5〜5 Kg/crn’の加圧
被処理液中に浸漬するか、前記内管路Cに加圧被処理液
を注入されて、前記半透!lbの作用により、低分子物
質を分別する限外濾過に適用されるものである。すなわ
ち、前記被処理液中に浸漬する場合(内側取出しという
)には、その圧力により、被処理液中の塩類、糖類等の
低分子物質が半透膜すを管材aの内側へ透過して、内管
路Cから透過液として取出されるとともに、高分子物質
を被処理液中に残留させる。また、前記内管路Cに被処
理液を流す場合(外側取出しという)には、低分子物質
が半透膜すを外側へ透過して、管外から透過液が取出さ
れる。The tube material a is immersed in a pressurized liquid to be treated at a pressure of 0.5 to 5 Kg/crn', or a pressurized liquid to be treated is injected into the inner pipe line C to make the semi-permeable! This method is applied to ultrafiltration that separates low-molecular substances by the action of lb. That is, when immersing in the liquid to be treated (referred to as internal extraction), low molecular substances such as salts and sugars in the liquid to be treated permeate through the semi-permeable membrane to the inside of the tube material a due to the pressure. , is taken out as a permeated liquid from the inner pipe C, and the polymer substance remains in the liquid to be treated. Furthermore, when the liquid to be treated is allowed to flow through the inner pipe C (referred to as external extraction), the low molecular weight substance permeates the semipermeable membrane to the outside, and the permeated liquid is extracted from outside the tube.
この場合に、例えば前記セルロースの場合は、分離し得
る最大分子量(分画分子量)は15000であり、ポリ
アミド等の場合には8000である。このように、その
材質を適宜に選定することにより、所望の分子量の物質
のみを分離することができ、精密濾過が可能となる。In this case, for example, in the case of cellulose, the maximum molecular weight that can be separated (molecular weight cut off) is 15,000, and in the case of polyamide, etc., it is 8,000. In this manner, by appropriately selecting the material, only substances with a desired molecular weight can be separated, and precision filtration becomes possible.
〈発明が解決しようとする問題点〉
かかる半透!Ibを使用する精密濾過用管材aにあって
、前記半透!Ibの微細孔dに、高分子等により目詰ま
りを生ずると、濾過機能が低下するとともに、その液の
供給圧を高くする必要を生じ、その洗浄を要することと
なる。ところで、従来は前記目詰まりに際しては、前記
内管路にエアーを供給したり、水を供給するようにして
いた。ところが、各手段とも、高い清浄効果を得ること
ができず、長時間の清浄工程を要していた。これは、エ
アー、水によると、微細孔dに目詰まりを生じていても
、その間隙から管外へ流出してしまう傾向があり、目詰
まりしている物質を1好に押出すことができないことに
起因するもののようである。<Problems to be solved by the invention> Such semi-transparent! In precision filtration tube material a using Ib, the semi-transparent! If the micropores d of Ib become clogged with polymers or the like, the filtration function will be degraded, and the supply pressure of the liquid will need to be increased, making it necessary to clean it. By the way, conventionally, when the clogging occurs, air or water is supplied to the inner pipe line. However, with each method, a high cleaning effect could not be obtained and a long cleaning process was required. This is because even if the micropores d are clogged with air or water, they tend to flow out of the tube through the gaps, making it impossible to push out the clogged substances. This seems to be caused by this.
本発明は、洗浄効果の高い、精密濾過用管材aの洗浄方
法の提供を目的とするものである。An object of the present invention is to provide a method for cleaning a precision filtration tube material a, which has a high cleaning effect.
く問題点を解決するための手段〉
本発明は、精密濾過用管材aの、その内管路または管外
に、外径10ル〜0.001gの範囲の微細気泡yを含
有した加圧洗称液Xを流入させ、前記微細気泡yを半透
膜の微細孔dに透過させるようにしたものである。Means for Solving the Problems> The present invention provides a pressure washing method containing fine bubbles y with an outer diameter of 10 l to 0.001 g in the inner pipe line or outside of the microfiltration pipe material a. A liquid X is introduced into the semipermeable membrane, and the microbubbles y permeate through the micropores d of the semipermeable membrane.
前記微細気泡yの大きさは、精密絽適用管材aの微細孔
dに近似するものとすることが好ましいが、前記微細気
泡yの大きさは、管の内外の水圧により影!を受けるこ
ともあって、厳密に設定することは困難である。It is preferable that the size of the microbubbles y be similar to the micropores d of the pipe material a to which precision mesh is applied, but the size of the microbubbles y is influenced by the water pressure inside and outside the pipe. It is difficult to set a precise setting because of the
く作用〉
第1図に示す、内側取出しの場合について説明する。加
圧洗浄液X内の微細気泡yは、その内圧により微細孔d
に透過し、該微細孔d中の目詰まりを生じさせている物
質2を除去する。この場合に、前記気泡yの径は、その
内圧と外圧との均衡により定まり、精密濾過用管材aの
外部は、前記管内に比して低圧であるから、前記微細孔
d内において、管外へ移動するにつれて大径となる。こ
のこともあって、効果的に、前記微細孔d内の物質2を
外へ押し出し、これにより前記微細孔dを清浄化する。Effect> The case of inside extraction shown in FIG. 1 will be explained. The microbubbles y in the pressure washing liquid X form micropores d due to their internal pressure.
The substance 2 that is clogging the micropores d is removed. In this case, the diameter of the bubble y is determined by the balance between its internal pressure and external pressure, and since the outside of the precision filtration tube material a has a lower pressure than the inside of the tube, inside the micropore d, the outside of the tube is The diameter becomes larger as you move towards the end. Due to this, the substance 2 in the micropores d is effectively pushed out, thereby cleaning the micropores d.
外側取出しの場合は、微細気泡yの流れが逆になるが、
その作用は前記と等しく説明を省略するい。In the case of outside extraction, the flow of microbubbles y is reversed, but
Its operation is the same as above, and the explanation will be omitted.
〈実施例〉
第3図は、精密濾過用管材aを用いた精密濾過装置lの
一例であり、内側取出しに用いるものである。<Example> FIG. 3 shows an example of a precision filtration device 1 using a tube material a for precision filtration, which is used for internal extraction.
ここで2は長尺状の通水管であって、その上部に前記管
材aを多数本束ねた集束体4が、その上端部を接合され
て、該上端縁に開口する各管材aの内管路Cを、前記通
水管2上部に形成された流出O4にのみ連通させている
。前記集束体3の末端は接着され、前記内管路C下端を
閉塞させている。Here, reference numeral 2 denotes a long water flow pipe, on the top of which a bundle 4 in which a large number of the pipe materials a are bundled is joined at its upper end, and the inner tube of each pipe material a opens at the upper end edge. The passage C is communicated only with the outflow O4 formed at the upper part of the water pipe 2. The end of the bundle 3 is glued to close the lower end of the inner channel C.
また前記通水管2の上側部には、被処理液が流入する流
入口5が形成され、さらに前記通水管2の下端には前記
被処理液が流下する流出口6が設けられている・
さらにまた、前記通水管2の上側部にはエアー抜きロア
が設けられている。Further, an inlet 5 through which the liquid to be treated flows is formed at the upper side of the water pipe 2, and an outlet 6 through which the liquid to be treated flows down at the lower end of the water pipe 2. Further, an air vent lower is provided on the upper side of the water pipe 2.
前記構成からなる精密濾過装Mlは、前記流入口5から
被処理液が流入し、前記集束体3の各管材aの周面をっ
たって流下し、前記流出口6から排出される。この際に
、前記集束体3の各管材aの周面において、前記通水管
2内に供給される被処理液の圧力により逆浸透現象を生
じる。このため、前記管材aの半透Hbの微細孔dに、
溶媒及び低分子物質が、前記半透膜すから透過して内管
路C内に侵入し、高分子物質は被処理液中に残留する。In the precision filtration device Ml having the above structure, the liquid to be treated flows in from the inlet 5, flows down along the circumferential surface of each tube material a of the bundle 3, and is discharged from the outlet 6. At this time, a reverse osmosis phenomenon occurs on the circumferential surface of each tube material a of the bundle 3 due to the pressure of the liquid to be treated that is supplied into the water pipe 2. Therefore, in the semi-permeable Hb micropores d of the tube material a,
The solvent and low-molecular substances permeate through the semipermeable membrane and enter the inner pipe C, and the high-molecular substances remain in the liquid to be treated.
この内管路C内に流入した透過液は流出口4から精密濾
過装置l外に取出される。The permeated liquid that has flowed into the inner pipe C is taken out from the microfiltration device l through the outlet 4.
ところで、かかる工程を継続すると、前記半透膜すの微
細孔dに目詰まりを生ずる。そこで、本発明の洗浄方法
を適用する。However, if this process is continued, the micropores d of the semipermeable membrane will become clogged. Therefore, the cleaning method of the present invention is applied.
すなわち、まず第一工程として、前記流出口4から、マ
イクロエアー又はコロイド状エアー等の微細気泡yを水
に含有した加圧洗浄液Xを通入する。前記洗浄液は、視
覚によっては形状を把握できない微細気泡yを含有して
いるから、白濁した状態として視認される。That is, as a first step, a pressurized cleaning liquid X containing fine bubbles y such as micro air or colloidal air in water is introduced from the outlet 4. Since the cleaning liquid contains fine bubbles y whose shape cannot be determined visually, it is visually recognized as a cloudy state.
第2図に模型的に示すように、かかる流入により、前記
洗浄液X中の微細気泡yは、前記洗浄液Xの圧力と、集
束体3周部の圧力差により微細孔d内に侵入する。とこ
ろで前記気泡yの径は、その内圧と外圧との均衡により
定まるから、かかる微細孔d内で、前記管外側へ移動す
るにつれて、大径となる。この際に、微細孔d内に詰ま
っていた物質2が管外へ押し出される。前記管材aの外
部に流出した気泡yはエアー抜きロアから回収される。As schematically shown in FIG. 2, due to this inflow, the fine bubbles y in the cleaning liquid X enter the fine holes d due to the pressure difference between the pressure of the cleaning liquid X and the pressure around the bundle 3. By the way, since the diameter of the bubble y is determined by the balance between its internal pressure and external pressure, the diameter becomes larger as it moves toward the outside of the tube within the micropore d. At this time, the substance 2 clogged within the micropores d is pushed out of the tube. The air bubbles y that have flowed out of the tube material a are collected from the air vent lower.
次に第二工程で、流出口4からエアーを供給して、内管
路C内を清浄化する。Next, in a second step, air is supplied from the outlet 4 to clean the inside of the inner pipe C.
さらに第三工程で、前記流出口4からカセイソーダ、塩
酸等、被処理液中の物質を溶解させ得る薬液中に、前記
微細気泡yが混入された洗浄液を流入する。これにより
、前記第一工程によっても微細孔d内に残留した物質2
を、前記薬液により溶融しながら、前述した微細気泡y
の作用で管外に押出す。Furthermore, in a third step, the cleaning liquid in which the fine bubbles y are mixed is introduced from the outlet 4 into a chemical solution such as caustic soda or hydrochloric acid that can dissolve substances in the liquid to be treated. As a result, the substance 2 remaining in the micropores d even after the first step is removed.
While melting with the chemical solution, the above-mentioned fine bubbles y
It is pushed out of the tube by the action of
この後水洗いして、洗浄工程が終了し、前記物質Zの排
除がなされ得る。This is followed by washing with water to complete the washing process and eliminate the substance Z.
かかる洗浄工程は、前記した各工程を任意に組合わせる
ことができ、また、各工程を複数回繰返してもよい。In this cleaning step, the above-mentioned steps can be arbitrarily combined, and each step may be repeated multiple times.
尚、微細気泡yを洗浄液Xに混入するには、高圧下で、
エゼクタにより空気を液中に噴出させる公知手段により
施し得る。In addition, in order to mix the fine bubbles y into the cleaning liquid X, under high pressure,
This can be done by known means of ejecting air into the liquid using an ejector.
〈発明の効果〉
本発明は、上述のように、管材aを清浄にするために、
洗浄液X中の微細気泡yを半透膜の微細孔dに透過させ
、該微細孔dに目詰まりしている物質2を押出すように
したから、その洗浄を効果的に施すことができる優れた
効果がある。<Effects of the Invention> As described above, the present invention provides the following steps to clean the pipe material a:
The fine bubbles y in the cleaning liquid It has a positive effect.
第1図は管材aの縦断拡大断面図、第2図は管材aの半
透膜すをさらに拡大して気泡の動態を示す縦断側面図、
第3FI4は精密濾過装置lの縦断側面図である。
a;管材 b;半透膜 C;内管路 X;洗浄液 y:
微細気泡 l;精密濾過装置 2;通水管 3;集束体
4;流出口 5;流入口6;流出口FIG. 1 is an enlarged longitudinal sectional view of tube material a, and FIG. 2 is a longitudinal side view of the semipermeable membrane of tube material a further enlarged to show the dynamics of bubbles.
3rd FI4 is a longitudinal cross-sectional side view of the precision filtration device 1. a; Pipe material b; Semipermeable membrane C; Inner pipe X; Cleaning liquid y:
Microbubbles l; precision filtration device 2; water pipe 3; bundle 4; outflow port 5; inflow port 6; outflow port
Claims (1)
される、半透膜で構成した精密濾過用管材の、その内管
路または管外に、外径10μ〜0.001μの範囲の微
細気泡を含有した加圧洗浄液を流入させ、前記微細気泡
を半透膜の微細孔に透過させることを特徴とする精密濾
過用管材の洗浄方法A tube with an outer diameter of 10 μm to 0.001 μm is placed inside or outside the tube of a microfiltration tube material made of a semipermeable membrane, from which the permeate is extracted from the inner tube or outside the tube after being subjected to ultrafiltration. A method for cleaning tube material for precision filtration, characterized by flowing a pressurized cleaning liquid containing fine bubbles within a range of 100 to 100 mm, and allowing the fine bubbles to permeate through the fine pores of a semipermeable membrane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22731685A JPS6287206A (en) | 1985-10-09 | 1985-10-09 | Method for washing pipe material for precision filtration |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22731685A JPS6287206A (en) | 1985-10-09 | 1985-10-09 | Method for washing pipe material for precision filtration |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6287206A true JPS6287206A (en) | 1987-04-21 |
Family
ID=16858890
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22731685A Pending JPS6287206A (en) | 1985-10-09 | 1985-10-09 | Method for washing pipe material for precision filtration |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6287206A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2679465A1 (en) * | 1991-07-26 | 1993-01-29 | Hydrex Traitements | METHOD AND DEVICE FOR DECOLMAGING FILTRATION MEMBRANES |
JPH0565257U (en) * | 1991-07-02 | 1993-08-31 | キューピー株式会社 | Hangers for hanging products |
JP2010064039A (en) * | 2008-09-12 | 2010-03-25 | Mitsubishi Rayon Eng Co Ltd | Apparatus and method for treating wastewater |
US8236183B2 (en) | 2004-07-02 | 2012-08-07 | Pall Corporation | Methods and systems for filtration |
US8641897B2 (en) | 2007-11-14 | 2014-02-04 | 8452059 Canada Inc. | Water treatment apparatus and method |
US9206380B2 (en) | 2013-03-14 | 2015-12-08 | Ecolab Usa Inc. | Method of generating carbonate in situ in a use solution and of buffered alkaline cleaning under an enriched CO2 atmosphere |
US10099264B2 (en) | 2008-02-11 | 2018-10-16 | Ecolab Usa Inc. | Bubble enhanced cleaning method and chemistry |
-
1985
- 1985-10-09 JP JP22731685A patent/JPS6287206A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0565257U (en) * | 1991-07-02 | 1993-08-31 | キューピー株式会社 | Hangers for hanging products |
FR2679465A1 (en) * | 1991-07-26 | 1993-01-29 | Hydrex Traitements | METHOD AND DEVICE FOR DECOLMAGING FILTRATION MEMBRANES |
EP0526372A1 (en) * | 1991-07-26 | 1993-02-03 | Societe De Traitements Hydrex S.N.C. | Process and apparatus for cleaning filter membranes |
US8236183B2 (en) | 2004-07-02 | 2012-08-07 | Pall Corporation | Methods and systems for filtration |
US8641897B2 (en) | 2007-11-14 | 2014-02-04 | 8452059 Canada Inc. | Water treatment apparatus and method |
US10099264B2 (en) | 2008-02-11 | 2018-10-16 | Ecolab Usa Inc. | Bubble enhanced cleaning method and chemistry |
JP2010064039A (en) * | 2008-09-12 | 2010-03-25 | Mitsubishi Rayon Eng Co Ltd | Apparatus and method for treating wastewater |
US9206380B2 (en) | 2013-03-14 | 2015-12-08 | Ecolab Usa Inc. | Method of generating carbonate in situ in a use solution and of buffered alkaline cleaning under an enriched CO2 atmosphere |
US9845447B2 (en) | 2013-03-14 | 2017-12-19 | Ecolab Usa Inc. | Method of generating carbonate in situ in a use solution and of buffered alkaline cleaning under an enriched CO2 atmosphere |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8070947B2 (en) | Permselective membrane module and method for manufacturing the same | |
DE69914581T2 (en) | Hollow fiber membrane cartridge | |
JP5283618B2 (en) | Hollow fiber membrane module and method for producing the same, hollow fiber membrane module assembly and method for purifying suspended water using them | |
US4781834A (en) | Membrane separation apparatus | |
JP2003024751A (en) | Hollow fiber membrane cartridge | |
US4244820A (en) | Fluid purification system | |
JP6319493B1 (en) | Cleaning method for hollow fiber membrane module | |
JPH11309351A (en) | Washing of hollow fiber membrane module | |
JPS6287206A (en) | Method for washing pipe material for precision filtration | |
EP0122920A1 (en) | Filter | |
JP6618708B2 (en) | Method for operating hollow fiber membrane module and filtration device | |
JP6653154B2 (en) | Cleaning method and filtration device for hollow fiber membrane module | |
JP3161654B2 (en) | Hollow fiber membrane module and filtration device using the same | |
KR20180114820A (en) | Antifouling Hollow fiber membrane module, Method for preparing the same and Uses thereof | |
JP3354257B2 (en) | Oil-water separation method and oil-water separation device | |
JPH0679147A (en) | Filtration method | |
KR102051368B1 (en) | Tubular Macrofiltration Membrane | |
CN214159181U (en) | Cross-flow MSF microfiltration membrane device | |
KR102508296B1 (en) | A water treatment device using a precision filtration film of a highly permeable hydrophilic cellulose | |
KR102014105B1 (en) | Tubular Macrofiltration Membrane | |
JP2001029755A (en) | Washing method of hollow fiber membrane module | |
JPH0824590A (en) | Method for filtering concentrated organic solution | |
JP2017217581A (en) | Hollow fiber membrane filter device and cleaning method of the same | |
JPH04118032A (en) | Jet flow type filter | |
JP2005161179A (en) | Method of cleaning hollow-fiber membrane module |