KR920011570A - 폴리설폰 중공사 분리막의 제조방법 - Google Patents
폴리설폰 중공사 분리막의 제조방법 Download PDFInfo
- Publication number
- KR920011570A KR920011570A KR1019900022497A KR900022497A KR920011570A KR 920011570 A KR920011570 A KR 920011570A KR 1019900022497 A KR1019900022497 A KR 1019900022497A KR 900022497 A KR900022497 A KR 900022497A KR 920011570 A KR920011570 A KR 920011570A
- Authority
- KR
- South Korea
- Prior art keywords
- additive
- hollow fiber
- manufacturing
- spinning
- fiber membrane
- Prior art date
Links
- 239000012510 hollow fiber Substances 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000012528 membrane Substances 0.000 title claims description 5
- 229920002492 poly(sulfone) Polymers 0.000 title claims 3
- 239000000654 additive Substances 0.000 claims 8
- 230000000996 additive effect Effects 0.000 claims 7
- 238000009987 spinning Methods 0.000 claims 7
- 239000000701 coagulant Substances 0.000 claims 4
- 239000000243 solution Substances 0.000 claims 4
- 238000000034 method Methods 0.000 claims 3
- 229910017053 inorganic salt Inorganic materials 0.000 claims 2
- 239000003960 organic solvent Substances 0.000 claims 2
- 229920000642 polymer Polymers 0.000 claims 2
- 239000011347 resin Substances 0.000 claims 2
- 229920005989 resin Polymers 0.000 claims 2
- 239000002904 solvent Substances 0.000 claims 2
- 230000001112 coagulating effect Effects 0.000 claims 1
- 230000015271 coagulation Effects 0.000 claims 1
- 238000005345 coagulation Methods 0.000 claims 1
- 150000007522 mineralic acids Chemical class 0.000 claims 1
- 239000011550 stock solution Substances 0.000 claims 1
- 238000004804 winding Methods 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
Classifications
-
- 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
- B01D69/087—Details relating to the spinning process
- B01D69/0871—Fibre guidance after spinning through the manufacturing apparatus
-
- 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
- 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
- B01D69/085—Details relating to the spinneret
-
- 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
- B01D2323/08—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
- B01D2323/12—Specific ratios of components used
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/15—Use of additives
- B01D2323/218—Additive materials
- B01D2323/2181—Inorganic additives
- B01D2323/21815—Acids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/15—Use of additives
- B01D2323/218—Additive materials
- B01D2323/2181—Inorganic additives
- B01D2323/21817—Salts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/219—Specific solvent system
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/50—Control of the membrane preparation process
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Artificial Filaments (AREA)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명에 따른 중공사 분리막 제조에 이용되는 중공사 제조장치의 개략적인 구성도이고, 제2도는 본 발명에 따라 제조된 중공사 분리막의 단백질 분자량에 따른 배제율을 나타낸 그래프이다.
Claims (3)
- 이중관 구조의 중공사 제조용 노즐을 이용하고, 방사원액인 폴리설폰 수지와 유기용매 및 첨가제로 이루어진 방사용액을 방사하여 응고시킴으로써 중공사 분리막을 제조함에 있어서, 상기 중공사 제조시 방사원액으로서의 폴리설폰계 수지 10∼25중량%와 유기용매 45∼85중량%, 빈용매(poor solvent)첨가제 0∼30중량%, 용출성 고분자 첨가제 0∼20중량%, 무기염 첨가제 0∼8중량% 및 무기산 0∼1중량%로 이루어진 방사용액을 사용하되, 상기 방사용액의 방사시 내부 응고제의 온도는 상기 방사용액의 온도와 30℃이하의 차이를 유지하며 외부 응고제의 온도는 5∼60℃로 조절하여 응고시키고, 이때의 권취속도는 10∼45m/min으로 조절하여서 됨을 특징으로 하는 폴리설폰 중공사 분리막의 제조방법.
- 제1항에 있어서, 상기 빈용매 첨가제, 용출성 고분자 첨가제 및 무기염 첨가제의 총사용량은 40중량%이하가 되도록 하고, 이들 3가지 첨가제중 적어도 어느 한성분은 사용함을 특징으로 하는 중공사 분리막의 제조방법.
- 제1항에 있어서, 상기 외부 응고제를 이용한 응고 과정은 2단계로 실행하되 각 단계에서의 외부 응고제의 온도차가 80℃이하가 되도록 함을 특징으로 하는 중공사 분리막의 제조방법.※ 참고사항:최초출원 내용에 의하여 공개하는 것임.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019900022497A KR930003740B1 (ko) | 1990-12-29 | 1990-12-29 | 폴리설폰 중공사 분리막의 제조방법 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019900022497A KR930003740B1 (ko) | 1990-12-29 | 1990-12-29 | 폴리설폰 중공사 분리막의 제조방법 |
Publications (2)
Publication Number | Publication Date |
---|---|
KR920011570A true KR920011570A (ko) | 1992-07-24 |
KR930003740B1 KR930003740B1 (ko) | 1993-05-10 |
Family
ID=19308995
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019900022497A KR930003740B1 (ko) | 1990-12-29 | 1990-12-29 | 폴리설폰 중공사 분리막의 제조방법 |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR930003740B1 (ko) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101489746B1 (ko) * | 2013-04-30 | 2015-02-04 | 주식회사 퓨어멤 | 바이러스 제거용 폴리설폰 중공사막의 제조방법 |
KR101894077B1 (ko) * | 2016-08-05 | 2018-09-04 | 한국화학연구원 | 분리 성능이 우수한 폴리술폰계 고분자 중공사막의 제조방법 |
-
1990
- 1990-12-29 KR KR1019900022497A patent/KR930003740B1/ko not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
KR930003740B1 (ko) | 1993-05-10 |
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