KR960021123A - Method for producing hydrophilized ultrafiltration polysulfone separator - Google Patents
Method for producing hydrophilized ultrafiltration polysulfone separator Download PDFInfo
- Publication number
- KR960021123A KR960021123A KR1019940038045A KR19940038045A KR960021123A KR 960021123 A KR960021123 A KR 960021123A KR 1019940038045 A KR1019940038045 A KR 1019940038045A KR 19940038045 A KR19940038045 A KR 19940038045A KR 960021123 A KR960021123 A KR 960021123A
- Authority
- KR
- South Korea
- Prior art keywords
- membrane
- water
- hydrophilized
- polysulfone
- permeation performance
- Prior art date
Links
- 229920002492 poly(sulfone) Polymers 0.000 title claims abstract 6
- 238000004519 manufacturing process Methods 0.000 title claims abstract 4
- 238000000108 ultra-filtration Methods 0.000 title claims abstract 3
- 239000012528 membrane Substances 0.000 claims abstract 8
- 229910052751 metal Inorganic materials 0.000 claims abstract 3
- 239000002184 metal Substances 0.000 claims abstract 3
- JRKICGRDRMAZLK-UHFFFAOYSA-L peroxydisulfate Chemical compound [O-]S(=O)(=O)OOS([O-])(=O)=O JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 claims abstract 3
- 150000003839 salts Chemical class 0.000 claims abstract 3
- 239000012510 hollow fiber Substances 0.000 claims abstract 2
- 238000009987 spinning Methods 0.000 claims 3
- LCPVQAHEFVXVKT-UHFFFAOYSA-N 2-(2,4-difluorophenoxy)pyridin-3-amine Chemical compound NC1=CC=CN=C1OC1=CC=C(F)C=C1F LCPVQAHEFVXVKT-UHFFFAOYSA-N 0.000 claims 1
- 239000007864 aqueous solution Substances 0.000 claims 1
- 239000000701 coagulant Substances 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 229920001477 hydrophilic polymer Polymers 0.000 claims 1
- 238000007654 immersion Methods 0.000 claims 1
- 238000000034 method Methods 0.000 claims 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical group [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims 1
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Substances [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 claims 1
- 239000011550 stock solution Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 3
- 238000001035 drying Methods 0.000 abstract 2
- 239000000463 material Substances 0.000 abstract 2
- 239000003814 drug Substances 0.000 abstract 1
- 230000002209 hydrophobic effect Effects 0.000 abstract 1
- 230000007774 longterm Effects 0.000 abstract 1
- 230000035699 permeability Effects 0.000 abstract 1
- 239000005871 repellent Substances 0.000 abstract 1
- 239000011347 resin Substances 0.000 abstract 1
- 229920005989 resin Polymers 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 238000001179 sorption measurement Methods 0.000 abstract 1
Classifications
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- 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
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0016—Coagulation
-
- 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
- B01D61/145—Ultrafiltration
-
- 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
- B01D67/0093—Chemical modification
- B01D67/00931—Chemical modification by introduction of specific groups after membrane formation, e.g. by grafting
-
- 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
- B01D69/08—Hollow fibre membranes
-
- 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
- B01D71/66—Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
- B01D71/68—Polysulfones; Polyethersulfones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/02—Hydrophilization
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/08—Specific temperatures applied
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/14—Ageing features
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Water Supply & Treatment (AREA)
- Dispersion Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Transplantation (AREA)
- Inorganic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
소수성 수지로 된 분리막으로 형성시키는 경우 현저하게 발수성이 되어 분리막이 물과 친화성이 없어지기 때문에 투과성능을 충분하게 발휘하지 못하고 제약이나 식품공업 등에서 적용시 분리물질의 흡착등으로 인해 투과성능이 운전중에 크게 감소하게 된다. 특히 건조가 발생되면 수투과성능이 현저하게 감소하여 실지 적용시에 많은 문제점을 노출하게 된다.In case of forming a membrane made of hydrophobic resin, the water repellency is remarkably water-repellent and the membrane is not compatible with water, so the permeation performance is not sufficiently exhibited. When applied in pharmaceuticals or food industry, the permeation performance is operated due to adsorption of the separation material. Greatly reduced. In particular, when the drying occurs, the water permeation performance is significantly reduced to expose a number of problems in practical applications.
따라서 본 발명에서는 친수화된 폴리술폰으로 제조된 분리막에 대한 것으로서, 중공사막을 퍼술페이트 금속염에 침지하여 친수성 물질을 막의 표면, 이면 및 내부에 고르게 부착시켜 영구적으로 친수화시킴으로써 막의 투과성이 건조시나 장기 운전시에도 충분히 발휘될 수 있도록 하기 위한 폴리술폰으로 제조된 한외여과성 건조 분리막의 제조방법에 대한 것이다.Therefore, the present invention relates to a membrane made of hydrophilized polysulfone, the hollow fiber membrane is immersed in a persulfate metal salt to attach the hydrophilic material evenly to the surface, the back and the inside of the membrane permanently hydrophilized by permanently hydrophilic, so that the permeability of the membrane during drying or long-term The present invention relates to a method of manufacturing an ultrafiltration dry separator made of polysulfone so as to be sufficiently exerted even during operation.
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음As this is a public information case, the full text was not included.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019940038045A KR960021123A (en) | 1994-12-28 | 1994-12-28 | Method for producing hydrophilized ultrafiltration polysulfone separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019940038045A KR960021123A (en) | 1994-12-28 | 1994-12-28 | Method for producing hydrophilized ultrafiltration polysulfone separator |
Publications (1)
Publication Number | Publication Date |
---|---|
KR960021123A true KR960021123A (en) | 1996-07-18 |
Family
ID=66769827
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019940038045A KR960021123A (en) | 1994-12-28 | 1994-12-28 | Method for producing hydrophilized ultrafiltration polysulfone separator |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR960021123A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020013036A (en) * | 2000-08-10 | 2002-02-20 | 이재근 | Gas separation membraines for dehumidifying module |
-
1994
- 1994-12-28 KR KR1019940038045A patent/KR960021123A/en not_active Application Discontinuation
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020013036A (en) * | 2000-08-10 | 2002-02-20 | 이재근 | Gas separation membraines for dehumidifying module |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
E601 | Decision to refuse application |