WO2001093992A1 - Procede permettant de commander la permeabilite par l'intermediaire d'une onde de frequence elevee et procede de fabrication d'une membrane organique de separation - Google Patents
Procede permettant de commander la permeabilite par l'intermediaire d'une onde de frequence elevee et procede de fabrication d'une membrane organique de separation Download PDFInfo
- Publication number
- WO2001093992A1 WO2001093992A1 PCT/JP2001/004449 JP0104449W WO0193992A1 WO 2001093992 A1 WO2001093992 A1 WO 2001093992A1 JP 0104449 W JP0104449 W JP 0104449W WO 0193992 A1 WO0193992 A1 WO 0193992A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- membrane
- separation membrane
- high frequency
- organic separation
- organic
- 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.)
- Ceased
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0081—After-treatment of organic or inorganic membranes
- B01D67/009—After-treatment of organic or inorganic membranes with wave-energy, particle-radiation or plasma
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/12—Controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/22—Controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/24—Dialysis ; Membrane extraction
- B01D61/32—Controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/36—Pervaporation; Membrane distillation; Liquid permeation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/42—Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
- B01D61/44—Ion-selective electrodialysis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/08—Polysaccharides
- B01D71/12—Cellulose derivatives
- B01D71/14—Esters of organic acids
- B01D71/16—Cellulose acetate
Definitions
- a method for controlling the permeability of a substance to be separated through the organic separation membrane in a process of separating a substance using an organic separation membrane
- the separation process is selected from the group consisting of filtration, microfiltration, ultrafiltration, reverse osmosis (ultrafiltration), dialysis, electrodialysis, electrolysis (membrane method), gas separation and pervaporation.
- the control method according to the first aspect characterized in that:
- the microphone mouth wave that can be used in the method for producing and treating the organic separation membrane of the present invention and the type of the organic separation membrane that can be produced are as described above with respect to the control method of the present invention.
- Fig. 1 shows the outline of the device.
- a sample film is mounted on a cell section 3 of a transmission apparatus having a dummy load 2, and the entire system is vacuum-dried sufficiently while maintaining the entire system under vacuum.
- the sample film in 3 was irradiated.
- gas was introduced from the gas inlet 7 and pressurized in the pressurized tank 1.
- the pressure of the gas on the high pressure side is detected by the high pressure side pressure detector 5 and the pressure of the gas on the low pressure side having a connection port 8 to the vacuum system is detected by the low pressure side pressure detector 6.
- the amount of gas detected and transmitted was calculated from the change in pressure. From the slope of the pressure change,
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Nanotechnology (AREA)
- Urology & Nephrology (AREA)
- Health & Medical Sciences (AREA)
- Physics & Mathematics (AREA)
- Plasma & Fusion (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Treatments Of Macromolecular Shaped Articles (AREA)
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP01934368A EP1300187A4 (en) | 2000-06-02 | 2001-05-28 | PROCESS FOR THE PERMEABILITY CONTROL BY HIGH-FREQUENCY WAVES AND METHOD FOR THE PRODUCTION OF ORGANIC SEPARATE MEMBRANES |
| AU2001260630A AU2001260630A1 (en) | 2000-06-02 | 2001-05-28 | Method for controlling permeability by high frequency wave and method for producing organic membrane for separation |
| US10/304,639 US6706088B2 (en) | 2000-06-02 | 2002-11-27 | Method for controlling membrane permeability by microwave and method for producing organic separation membrane |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000-165429 | 2000-06-02 | ||
| JP2000165429A JP5025844B2 (ja) | 2000-06-02 | 2000-06-02 | マイクロ波による膜透過制御方法 |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US10/304,639 Continuation-In-Part US6706088B2 (en) | 2000-06-02 | 2002-11-27 | Method for controlling membrane permeability by microwave and method for producing organic separation membrane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2001093992A1 true WO2001093992A1 (fr) | 2001-12-13 |
Family
ID=18668898
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2001/004449 Ceased WO2001093992A1 (fr) | 2000-06-02 | 2001-05-28 | Procede permettant de commander la permeabilite par l'intermediaire d'une onde de frequence elevee et procede de fabrication d'une membrane organique de separation |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US6706088B2 (enExample) |
| EP (1) | EP1300187A4 (enExample) |
| JP (1) | JP5025844B2 (enExample) |
| AU (1) | AU2001260630A1 (enExample) |
| WO (1) | WO2001093992A1 (enExample) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7537917B2 (en) * | 2006-03-31 | 2009-05-26 | Collins Michael J | Microwave assisted PCR amplification of DNA |
| US20100081926A1 (en) * | 2008-09-29 | 2010-04-01 | Searete Llc, A Limited Liability Corporation Of The State Of Delaware | Histological facilitation systems and methods |
| US20100081928A1 (en) * | 2008-09-29 | 2010-04-01 | Searete Llc, A Limited Liability Corporation Of The State Of Delaware | Histological Facilitation systems and methods |
| EP2504082A4 (en) * | 2009-11-25 | 2016-11-09 | Univ Sydney | MEMBRANE AND MEMBRANE SEPARATION SYSTEM |
| GB201004229D0 (en) | 2010-03-15 | 2010-04-28 | Univ Leuven Kath | Flux enchancement in membrane seperations by electomagnetic irradiation |
| CN104289108B (zh) * | 2013-07-19 | 2016-08-10 | 中国石油天然气集团公司 | 一种高频脉冲用于真空膜蒸馏再生方法 |
| CN105363352A (zh) * | 2015-11-14 | 2016-03-02 | 大连理工大学 | 一种含氟稀溶液合成高耐酸mor沸石分子筛膜的方法 |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6065107A (ja) * | 1983-09-20 | 1985-04-13 | Terumo Corp | 中空繊維の製造方法 |
| JPS6099313A (ja) * | 1983-11-04 | 1985-06-03 | Agency Of Ind Science & Technol | 液体の膜分離方法 |
| JPS60222196A (ja) * | 1984-04-20 | 1985-11-06 | Sanki Eng Co Ltd | 有機排水の処理方法 |
| JPS62201607A (ja) * | 1986-02-27 | 1987-09-05 | Daido Steel Co Ltd | 流体透過膜の流体透過率制御方法 |
| JPH051166A (ja) * | 1991-06-26 | 1993-01-08 | Ishikawajima Harima Heavy Ind Co Ltd | フツ素樹脂製多孔質膜の製造方法 |
| JPH05146651A (ja) * | 1991-11-26 | 1993-06-15 | Ube Ind Ltd | ガス分離膜の製造法 |
| US5736051A (en) * | 1993-12-22 | 1998-04-07 | Pall Corporation | Polyvinylidene fluoride membrane and method for removing viruses from solutions |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3846521A (en) * | 1971-02-03 | 1974-11-05 | Union Carbide Corp | Low energy electron beam treatment of polymeric films, and apparatus therefore |
| JPS60222111A (ja) * | 1984-04-20 | 1985-11-06 | Sanyo Chem Ind Ltd | 気体分離膜 |
| JPS62289203A (ja) * | 1986-06-10 | 1987-12-16 | Fuji Photo Film Co Ltd | 微孔性膜の透水性改良方法 |
| JPS6463022A (en) * | 1987-09-04 | 1989-03-09 | Nippon Polyurethane Kogyo Kk | Gas separating membrane and production thereof |
| US4976897A (en) * | 1987-12-16 | 1990-12-11 | Hoechst Celanese Corporation | Composite porous membranes and methods of making the same |
| JP2737210B2 (ja) * | 1989-03-10 | 1998-04-08 | エヌオーケー株式会社 | 中空糸膜の熱処理方法 |
| US4952220A (en) * | 1989-04-11 | 1990-08-28 | Air Products And Chemicals, Inc. | Membranes formed from unsaturated polyimides |
| GB9013509D0 (en) * | 1990-06-16 | 1990-08-08 | British Petroleum Co Plc | Polymer synthesis |
| RU2093254C1 (ru) * | 1992-09-28 | 1997-10-20 | Научно-исследовательский институт физической оптики, оптики лазеров и информационно-оптических систем - Головной институт Всероссийского научного центра "Государственный оптический институт им.С.И.Вавилова" | Способ изготовления пористых мембранных фильтров |
| US5409524A (en) * | 1992-12-01 | 1995-04-25 | The Dow Chemical Company | Membranes having improved selectivity and recovery, and process for making same |
| FR2714595B1 (fr) * | 1993-12-30 | 1996-02-02 | Oreal | Emulsion eau dans huile contenant du rétinol, son utilisation et son conditionnement. |
| WO1996030394A1 (en) * | 1995-03-31 | 1996-10-03 | Jakob Bohr | Method for protein folding |
| US6368382B1 (en) * | 2000-07-27 | 2002-04-09 | Uop Llc | Epoxysilicone coated membranes |
-
2000
- 2000-06-02 JP JP2000165429A patent/JP5025844B2/ja not_active Expired - Fee Related
-
2001
- 2001-05-28 EP EP01934368A patent/EP1300187A4/en not_active Withdrawn
- 2001-05-28 AU AU2001260630A patent/AU2001260630A1/en not_active Abandoned
- 2001-05-28 WO PCT/JP2001/004449 patent/WO2001093992A1/ja not_active Ceased
-
2002
- 2002-11-27 US US10/304,639 patent/US6706088B2/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6065107A (ja) * | 1983-09-20 | 1985-04-13 | Terumo Corp | 中空繊維の製造方法 |
| JPS6099313A (ja) * | 1983-11-04 | 1985-06-03 | Agency Of Ind Science & Technol | 液体の膜分離方法 |
| JPS60222196A (ja) * | 1984-04-20 | 1985-11-06 | Sanki Eng Co Ltd | 有機排水の処理方法 |
| JPS62201607A (ja) * | 1986-02-27 | 1987-09-05 | Daido Steel Co Ltd | 流体透過膜の流体透過率制御方法 |
| JPH051166A (ja) * | 1991-06-26 | 1993-01-08 | Ishikawajima Harima Heavy Ind Co Ltd | フツ素樹脂製多孔質膜の製造方法 |
| JPH05146651A (ja) * | 1991-11-26 | 1993-06-15 | Ube Ind Ltd | ガス分離膜の製造法 |
| US5736051A (en) * | 1993-12-22 | 1998-04-07 | Pall Corporation | Polyvinylidene fluoride membrane and method for removing viruses from solutions |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP1300187A4 * |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2001260630A1 (en) | 2001-12-17 |
| JP5025844B2 (ja) | 2012-09-12 |
| US20030075044A1 (en) | 2003-04-24 |
| US6706088B2 (en) | 2004-03-16 |
| EP1300187A4 (en) | 2005-04-27 |
| EP1300187A1 (en) | 2003-04-09 |
| JP2001340733A (ja) | 2001-12-11 |
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