JPS5624006A - Maintainance method of capacity of permeable membrane in membrane separation - Google Patents
Maintainance method of capacity of permeable membrane in membrane separationInfo
- Publication number
- JPS5624006A JPS5624006A JP10009879A JP10009879A JPS5624006A JP S5624006 A JPS5624006 A JP S5624006A JP 10009879 A JP10009879 A JP 10009879A JP 10009879 A JP10009879 A JP 10009879A JP S5624006 A JPS5624006 A JP S5624006A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- fluid
- permeating
- gas
- backwashing
- 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 abstract 12
- 238000000034 method Methods 0.000 title 1
- 238000000926 separation method Methods 0.000 title 1
- 239000012530 fluid Substances 0.000 abstract 8
- 238000011001 backwashing Methods 0.000 abstract 5
- 239000007788 liquid Substances 0.000 abstract 3
- 239000000126 substance Substances 0.000 abstract 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- 239000011148 porous material Substances 0.000 abstract 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
PURPOSE: To prevent a membrance surface from being deposited with polluting substances as well as to maintain the membrane capacity by removing deposited polluting substances effectively by introducing a fluid to a permeating side and a residual side of a membrane surface of a cell when a permeating membrane is polluted.
CONSTITUTION: When a M surface of a permeating membrane is polluted, a pressure pump P1 for sending a liquid to be treated is stopped and a supply pump P2 of a backwashing fluid is operated to supply a backwashing fluid of a storage tank B of a membrane permeating water to a membrane permeating side of a cell A. The backwashing water is elluted from a rear side of the membrane M to a membrane surface side exhausted out of a system. A gas is sent at the same time or different time with this fluid is sent to be mixed with the backwashing fluid and the membrane is washed while flushed. Moreover, in sending the backwashing fluid, a gas may be supplied from a fluid conduit 10 to form a gas-liquid mixed fluid. Moreover, a liquid from an inflow pipe 2 may be mixed with a gas from a conduit 3. Thereby, polluting substances on a membrane surface or in fine pores are effectively removed.
COPYRIGHT: (C)1981,JPO&Japio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10009879A JPS5624006A (en) | 1979-08-06 | 1979-08-06 | Maintainance method of capacity of permeable membrane in membrane separation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10009879A JPS5624006A (en) | 1979-08-06 | 1979-08-06 | Maintainance method of capacity of permeable membrane in membrane separation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5624006A true JPS5624006A (en) | 1981-03-07 |
Family
ID=14264916
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10009879A Pending JPS5624006A (en) | 1979-08-06 | 1979-08-06 | Maintainance method of capacity of permeable membrane in membrane separation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5624006A (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4767539A (en) * | 1983-09-30 | 1988-08-30 | Memtec Limited | Cleaning of hollow fiber filters utilized in lumenal gas flow |
US4816160A (en) * | 1985-03-28 | 1989-03-28 | Memtec Limited | Cooling hollow fibre cross-flow separators |
US4844809A (en) * | 1984-11-16 | 1989-07-04 | Nitto Chemical Industry Co., Ltd. | Method for purifying reaction solution obtained by using microbial cell, immobilized microbial cell, or immobilized enzyme |
US4931186A (en) * | 1985-03-05 | 1990-06-05 | Memtec Limited | Concentration of solids in a suspension |
JPH05285354A (en) * | 1992-04-14 | 1993-11-02 | Ishigaki Mech Ind Co | Washing and regenerating method for filter membrane |
JPH06182338A (en) * | 1992-12-16 | 1994-07-05 | Kurita Water Ind Ltd | Membrane separating device |
JPH06277664A (en) * | 1993-01-29 | 1994-10-04 | Daicel Chem Ind Ltd | Method and apparatus for clarifying surface flowing water with membrane |
JPH07204474A (en) * | 1994-01-13 | 1995-08-08 | Electric Power Dev Co Ltd | Membrane separation apparatus and washing thereof |
US5769539A (en) * | 1995-08-07 | 1998-06-23 | Phase Technology | Backflush system for a filter membrane located upstream of a hydrocarbon analyzer apparatus |
US7220358B2 (en) | 2004-02-23 | 2007-05-22 | Ecolab Inc. | Methods for treating membranes and separation facilities and membrane treatment composition |
US7247210B2 (en) | 2004-02-23 | 2007-07-24 | Ecolab Inc. | Methods for treating CIP equipment and equipment for treating CIP equipment |
US7392811B2 (en) | 2004-02-23 | 2008-07-01 | Ecolab Inc. | Delivery head for multiple phase treatment composition, vessel including a delivery head, and method for treating a vessel interior surface |
CN102371253A (en) * | 2010-08-17 | 2012-03-14 | 蓝星环境工程有限公司 | Analyzing and cleaning device for membrane pollution and control method thereof |
-
1979
- 1979-08-06 JP JP10009879A patent/JPS5624006A/en active Pending
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4767539A (en) * | 1983-09-30 | 1988-08-30 | Memtec Limited | Cleaning of hollow fiber filters utilized in lumenal gas flow |
US4844809A (en) * | 1984-11-16 | 1989-07-04 | Nitto Chemical Industry Co., Ltd. | Method for purifying reaction solution obtained by using microbial cell, immobilized microbial cell, or immobilized enzyme |
US4931186A (en) * | 1985-03-05 | 1990-06-05 | Memtec Limited | Concentration of solids in a suspension |
US4816160A (en) * | 1985-03-28 | 1989-03-28 | Memtec Limited | Cooling hollow fibre cross-flow separators |
JPH05285354A (en) * | 1992-04-14 | 1993-11-02 | Ishigaki Mech Ind Co | Washing and regenerating method for filter membrane |
JPH06182338A (en) * | 1992-12-16 | 1994-07-05 | Kurita Water Ind Ltd | Membrane separating device |
JPH06277664A (en) * | 1993-01-29 | 1994-10-04 | Daicel Chem Ind Ltd | Method and apparatus for clarifying surface flowing water with membrane |
JPH07204474A (en) * | 1994-01-13 | 1995-08-08 | Electric Power Dev Co Ltd | Membrane separation apparatus and washing thereof |
US5769539A (en) * | 1995-08-07 | 1998-06-23 | Phase Technology | Backflush system for a filter membrane located upstream of a hydrocarbon analyzer apparatus |
US7220358B2 (en) | 2004-02-23 | 2007-05-22 | Ecolab Inc. | Methods for treating membranes and separation facilities and membrane treatment composition |
US7247210B2 (en) | 2004-02-23 | 2007-07-24 | Ecolab Inc. | Methods for treating CIP equipment and equipment for treating CIP equipment |
US7392811B2 (en) | 2004-02-23 | 2008-07-01 | Ecolab Inc. | Delivery head for multiple phase treatment composition, vessel including a delivery head, and method for treating a vessel interior surface |
CN102371253A (en) * | 2010-08-17 | 2012-03-14 | 蓝星环境工程有限公司 | Analyzing and cleaning device for membrane pollution and control method thereof |
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