KR890001615A - 그래이드 밀도 피층을 갖는 비대칭성 기체 분리막의 제조방법 및 고점성 원액 - Google Patents
그래이드 밀도 피층을 갖는 비대칭성 기체 분리막의 제조방법 및 고점성 원액 Download PDFInfo
- Publication number
- KR890001615A KR890001615A KR1019870008967A KR870008967A KR890001615A KR 890001615 A KR890001615 A KR 890001615A KR 1019870008967 A KR1019870008967 A KR 1019870008967A KR 870008967 A KR870008967 A KR 870008967A KR 890001615 A KR890001615 A KR 890001615A
- Authority
- KR
- South Korea
- Prior art keywords
- lewis acid
- base
- lewis
- polymer
- membrane
- Prior art date
Links
- 239000012528 membrane Substances 0.000 title claims description 15
- 238000000926 separation method Methods 0.000 title claims description 6
- 238000004519 manufacturing process Methods 0.000 title claims 4
- 239000011248 coating agent Substances 0.000 title 1
- 238000000576 coating method Methods 0.000 title 1
- 239000002841 Lewis acid Substances 0.000 claims 20
- 150000007517 lewis acids Chemical class 0.000 claims 20
- 239000002879 Lewis base Substances 0.000 claims 11
- 150000007527 lewis bases Chemical class 0.000 claims 11
- 229920000642 polymer Polymers 0.000 claims 11
- 239000002904 solvent Substances 0.000 claims 11
- 239000000243 solution Substances 0.000 claims 8
- 239000002585 base Substances 0.000 claims 7
- 238000005345 coagulation Methods 0.000 claims 5
- 230000015271 coagulation Effects 0.000 claims 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 4
- 150000001875 compounds Chemical class 0.000 claims 3
- 238000000034 method Methods 0.000 claims 3
- 238000009987 spinning Methods 0.000 claims 3
- 239000002253 acid Substances 0.000 claims 2
- -1 aromatic sulfone Chemical class 0.000 claims 2
- 238000010494 dissociation reaction Methods 0.000 claims 2
- 230000005593 dissociations Effects 0.000 claims 2
- 239000012530 fluid Substances 0.000 claims 2
- 229920001600 hydrophobic polymer Polymers 0.000 claims 2
- 239000011550 stock solution Substances 0.000 claims 2
- 238000005266 casting Methods 0.000 claims 1
- 239000000470 constituent Substances 0.000 claims 1
- 239000011521 glass Substances 0.000 claims 1
- 239000012510 hollow fiber Substances 0.000 claims 1
- 238000007711 solidification Methods 0.000 claims 1
- 230000008023 solidification Effects 0.000 claims 1
- 238000000108 ultra-filtration Methods 0.000 description 1
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
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0016—Coagulation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
- C08J3/09—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
- C08J3/091—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids characterised by the chemical constitution of the organic liquid
-
- 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
- B01D67/0011—Casting solutions therefor
- B01D67/00111—Polymer pretreatment in the casting solutions
-
- 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
- B01D67/0095—Drying
-
- 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
- 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
- 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
- B01D2325/00—Details relating to properties of membranes
- B01D2325/02—Details relating to pores or porosity of the membranes
- B01D2325/022—Asymmetric membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/38—Hydrophobic membranes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제 1 도는 종래의 비대칭성 기체 분리막과 본 발명의 비대칭성 기체 분리막의 구조를 도시한 것이고,
제 2 도는 종래의 한외여과막을 도시한 것이며,
제 3 도는 본 발명에 의한 막을 도시한 것이다.
Claims (10)
- 루이스산, 루이스염기 및 루이스산과 루이스염기로 형성된 용매 용액에 폴리머를 용해시킨 다음, 겔화점에 근접하는 값을 갖는 용매계와 폴리머로 된 방사점성원액을 형성한 후, 점성원액을 구금(tube-in orifics type)으로부터 방사하고 오리피스를 통해 응고 유액을 주입한 후, 응고 매질로 방사 점성원액을 응고시켜 막을 형성한 다음, 착화합물의 신속한 해리를 이용하여 형성된 막을 디솔베이팅하고 극성매질내에서 막을 세척한 후 막을 실온 내지 플라스전이온보다 20℃가 낮은 온도 범위에서 건조시켜 막의 1차 가열 Tg가 폴리머 벌크 시료의 Tg보다 크고 자유 부피가 증가된 막을 제조함을 특징으로 하는 밀도구배피층(graded density skins)과 거대공극이 없는 소수성 폴리머로 구성된 중공섬유 비대칭성 기체 분리막의 제조방법.
- 제 1 항에 있어서, 루이스산, 루이스염기 및 루이스산 : 염기 착화합물로 된 옹매계는 폴리머의 할데브란트 매개변수 약 1.5㎈1/2/㎝3/2의 범위 이내에 있는 힐데브란트 매개변수를 갖는 것을 특징으로 하는 방법.
- 제 1 항에 있어서, 루이스산, 루이스염기 및 루이스산 : 염기 착화합물은 루이스산 : 염기의 몰비가 0.7 : 1.0 내지 1.2 : 1.0인 농도로 산의 농도가 충분히 낮게 되므로 응고값(g)이 2 이하인 용매계를 제공함을 특징으로 하는 방법.
- 제 1 항에 있어서, 구금내의 오리피스에 주입된 응고유액과 방사되는 점성원액내에 주입된 응고매질은 물로 구성된 것임을 특징으로 하는 방법.
- 루이스산, 루이스염기 및 루이스산과 루이스염기로 형성된 용매 용액에 폴리머를 용해시킨 다음, 겔화점에 근접하는 값을 갖는 용매계와 폴리머로 된 케스팅 점성원액을 형성한 후, 점성원액을 평판상에 케스팅하고 케스팅된 점성원액을 응고시켜 판상의 막을 형성시킨 다음, 착화합물의 신속한 해리를 이용하여 형성된 막을 디솔베이팅하고 실온에서 극성매질로 막을 세척한 후 막을 실온 내지 글라스전이온보다 20℃가 낮은 온도 범위에서 건조시켜 막의 1차 가열 Tg가 폴리머 벌크 시료의 Tg보다 크고 자유 부피가 증가된 막을 제조함을 특징으로 하는 밀도구배피층(graded density skins)과 거대공극이 없는 방향족 설폰 폴리머로 구성된 판상 비대칭성 기체 분리막의 제조방법.
- 제 5 항에 있어서, 루이스산, 루이스염기 및 루이스산 : 염기 착화합물로 된 용매계는 폴리머의 힐데브란트 매개변수 약 1.5㎈½/㎝3/2의 범위 이내에 있는 힐데브란트 매개변수를 갖는 것을 특징으로 하는 방법.
- 제 3 항에 있어서, 루이스산, 루이스염기 및 루이스산 : 염기 착화합물은 루이스산 : 염기의 몰비가 0.7 : 1.0 내지 1.2 : 1.0인 농도로 산의 농도라 충분히 낮게 되므로 응고값(g)이 2 이하인 용매계를 제공함을 특징으로 하는 방법.
- 루이스산, 루이스염기 및 루이스산과 루이스염기 착화합물로 구성된 용매제에 루이스산 존재하에 소수성 폴리머를 충분한 양으로 용해하여 용매계가 응고값(g)이 2이하, 힐데브란트 파라메타가 폴리머의 힐데브란트 파라메타 1.5㎈½/㎝3/2보다 이하인 값을 갖음을 특징으로 하는 밀도 구배피층(graded density skins)과 증가된 자유부피를 갖는 비대칭성이고 거대공극이 없는 기체 분리막 제조용 점성원액.
- 루이스산과 루이스염기가 0.7 : 1.0 내지 1.2 : 1.0의 몰비로 구성된 용매계 및 이렇게 형성된 루이스산 : 염기 착화합물에 충분량으로 존재하는 루이스산에 대하여 30wt% 이상의 양으로 방향족 설폰 폴리머를 용해시켜 용매계가 응고값(g)이 2 이하, 힐데브란트 파라미터가 폴리머의 힐데브란트 파라미터 1.5㎈½/㎝3/2보다 이하인 값을 갖음을 특징으로 하는 밀도 구배피층(graded density skins)과 증가된 자유부피를 갖는 비대칭이고 거대공극이 없는 기체 분리막 제조용 점성원액.
- 제 9 항에 있어서, 용매계는 물과 혼화성이 있어 착화합물이 물에 의해 용이하게 해리되어 해리된 착화합물의 성분 분자들이 물에 혼화됨을 특징으로 하는 점성원액.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US89756686A | 1986-08-15 | 1986-08-15 | |
US897566 | 1986-08-15 | ||
US07/066,751 US4871494A (en) | 1986-08-15 | 1987-06-25 | Process for forming asymmetric gas separation membranes having graded density skins |
US66751 | 2005-02-25 |
Publications (2)
Publication Number | Publication Date |
---|---|
KR890001615A true KR890001615A (ko) | 1989-03-28 |
KR900008713B1 KR900008713B1 (ko) | 1990-11-27 |
Family
ID=26747122
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019870008967A KR900008713B1 (ko) | 1986-08-15 | 1987-08-14 | 그레이드 밀도 피층을 갖는 비대칭성 기체 분리막의 제조방법 및 고점성 원액 |
Country Status (10)
Country | Link |
---|---|
US (1) | US4871494A (ko) |
EP (1) | EP0259288B1 (ko) |
JP (1) | JP2566973B2 (ko) |
KR (1) | KR900008713B1 (ko) |
CN (1) | CN1031289C (ko) |
CA (1) | CA1321687C (ko) |
DE (1) | DE3782128T2 (ko) |
ES (1) | ES2035108T3 (ko) |
IN (1) | IN170064B (ko) |
MX (1) | MX168757B (ko) |
Families Citing this family (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4783201A (en) * | 1987-12-28 | 1988-11-08 | Rice Arthur W | Gas dehydration membrane apparatus |
US4992221A (en) * | 1989-09-27 | 1991-02-12 | Permea, Inc. | Asymmetric gas separation membranes having improved strength |
US5013767A (en) * | 1989-09-27 | 1991-05-07 | Permea, Inc. | Asymmetric gas separation membranes having improved strength |
US5015270A (en) * | 1989-10-10 | 1991-05-14 | E. I. Du Pont De Nemours And Company | Phenylindane-containing polyimide gas separation membranes |
US5209883A (en) * | 1991-04-17 | 1993-05-11 | Hoechst Celanese Corp. | Fabrication of fluoropolymer hollow fibers for asymmetric membranes |
US5480554A (en) * | 1992-05-13 | 1996-01-02 | Pall Corporation | Integrity-testable wet-dry-reversible ultrafiltration membranes and method for testing same |
US5788862A (en) * | 1992-05-13 | 1998-08-04 | Pall Corporation | Filtration medium |
US5795920A (en) * | 1995-08-21 | 1998-08-18 | Korea Institute Of Science And Technology | Polymeric dope solution for use in the preparation of an integrally skinned asymmetric membrane |
WO1998037964A1 (en) * | 1997-02-26 | 1998-09-03 | Integument Technologies, Inc. | Polymer composites and methods for making and using same |
US7217754B2 (en) * | 1997-02-26 | 2007-05-15 | Integument Technologies, Inc. | Polymer composites and methods for making and using same |
US6548590B1 (en) | 2000-03-22 | 2003-04-15 | Integument Technologies, Inc. | Polymer and inorganic-organic hybrid composites and methods for making and using same |
US6413070B1 (en) * | 1997-04-11 | 2002-07-02 | Cuno Incorporated | System for manufacturing reinforced three-zone microporous membrane |
SG67983A1 (en) * | 1997-06-21 | 1999-10-19 | Univ Singapore | Highly permeable polyethersulfone hollow fiber membranes for gas separation |
US5958989A (en) * | 1997-07-08 | 1999-09-28 | Usf Filtration And Separations Group, Inc. | Highly asymmetric ultrafiltration membranes |
SG94705A1 (en) * | 1998-06-16 | 2003-03-18 | Univ Singapore | Ultrathin high-performance hollow fiber membranes |
KR100291632B1 (ko) * | 1998-10-28 | 2001-08-07 | 박호군 | 물리적겔법을이용한비대칭지지막의제조방법및이로부터제조된비대칭지지막 |
US6500233B1 (en) | 2000-10-26 | 2002-12-31 | Chevron U.S.A. Inc. | Purification of p-xylene using composite mixed matrix membranes |
US6547859B1 (en) * | 2000-11-21 | 2003-04-15 | Praxair Technology, Inc. | Process for making microporous membranes having selected gas-selective sites and the membranes so made |
US20060249018A1 (en) * | 2005-05-04 | 2006-11-09 | Hua Wang | Nucleophilic modifier functionalized and/or crosslinked solvent-resistant polymide and copolymer membranes |
US7553440B2 (en) * | 2005-05-12 | 2009-06-30 | Leonard William K | Method and apparatus for electric treatment of substrates |
US7842214B2 (en) * | 2007-03-28 | 2010-11-30 | 3M Innovative Properties Company | Process for forming microporous membranes |
US7699911B2 (en) * | 2007-05-03 | 2010-04-20 | Honeywell International Inc. | Ozone resistant O2/N2 separation membranes |
US20110146492A1 (en) * | 2009-12-18 | 2011-06-23 | Honeywell International Inc. | Air separation module fiber material formulation |
US8641807B2 (en) | 2011-01-31 | 2014-02-04 | Honeywell International Inc. | Hollow-fiber membrane casting solution additive for rapid solvent removal |
US9321015B2 (en) * | 2011-09-06 | 2016-04-26 | Sri International | Process for fabricating PBI hollow fiber asymmetric membranes for gas separation and liquid separation |
CN106861447B (zh) * | 2017-03-02 | 2019-07-16 | 北京航空航天大学 | 一种聚砜纤维膜的制备方法 |
KR101984893B1 (ko) | 2017-10-27 | 2019-05-31 | (주)에어레인 | 바이오가스 고질화용 중공사 복합막, 이를 포함하는 막모듈 및 그 제조방법 |
CN111333867B (zh) * | 2020-03-20 | 2023-02-28 | 浙江理工大学 | 一种较低相转变温度水凝胶、制备方法及其应用 |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3133137A (en) * | 1960-11-29 | 1964-05-12 | Univ California | High flow porous membranes for separating water from saline solutions |
US3752784A (en) * | 1970-12-23 | 1973-08-14 | Du Pont | Process for preparing microporous opencelled cellular polymeric structures |
US3792135A (en) * | 1972-01-06 | 1974-02-12 | Eastman Kodak Co | Process for manufacturing cellulosic reverse osmosis membranes using a very high temperature initial aqueous quench |
US3917777A (en) * | 1972-12-13 | 1975-11-04 | Kobe Steel Ltd | Process for the preparation of dry semipermeable |
JPS5331105B2 (ko) * | 1973-03-27 | 1978-08-31 | ||
ZA762209B (en) * | 1975-04-23 | 1977-04-27 | Envirogenics Syst | Gas separation membrane |
US4230463A (en) * | 1977-09-13 | 1980-10-28 | Monsanto Company | Multicomponent membranes for gas separations |
JPS54145379A (en) * | 1978-05-02 | 1979-11-13 | Asahi Chem Ind Co Ltd | Aromatic polysulfone hollow fiber semipermeable membrane |
IL59581A0 (en) * | 1979-03-28 | 1980-06-30 | Monsanto Co | Methods for preparing anisotropic membranes and membranes prepared therefrom |
JPS5824305A (ja) * | 1981-07-31 | 1983-02-14 | Daicel Chem Ind Ltd | ポリスルホン樹脂半透膜の製造法 |
US4544484A (en) * | 1983-06-24 | 1985-10-01 | E. I. Du Pont De Nemours And Company | Reverse osmosis membrane quenching |
EP0131559B1 (en) * | 1983-06-30 | 1987-12-02 | Monsanto Company | Amorphous aryl substituted polyarylene oxide membranes |
JPS60172312A (ja) * | 1984-02-17 | 1985-09-05 | Toyobo Co Ltd | ポリスルホン中空糸膜の製造法 |
JPS61141907A (ja) * | 1984-12-14 | 1986-06-28 | Sumitomo Bakelite Co Ltd | 中空繊維状分離膜の製造方法 |
-
1987
- 1987-06-25 US US07/066,751 patent/US4871494A/en not_active Expired - Lifetime
- 1987-08-12 DE DE8787870114T patent/DE3782128T2/de not_active Expired - Fee Related
- 1987-08-12 ES ES87870114T patent/ES2035108T3/es not_active Expired - Lifetime
- 1987-08-12 EP EP87870114A patent/EP0259288B1/en not_active Expired - Lifetime
- 1987-08-14 CA CA000544615A patent/CA1321687C/en not_active Expired - Fee Related
- 1987-08-14 KR KR1019870008967A patent/KR900008713B1/ko not_active IP Right Cessation
- 1987-08-14 IN IN588/MAS/87A patent/IN170064B/en unknown
- 1987-08-14 CN CN87106270A patent/CN1031289C/zh not_active Expired - Fee Related
- 1987-08-14 MX MX007743A patent/MX168757B/es unknown
- 1987-08-15 JP JP62203354A patent/JP2566973B2/ja not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP2566973B2 (ja) | 1996-12-25 |
US4871494A (en) | 1989-10-03 |
EP0259288A2 (en) | 1988-03-09 |
CN1031289C (zh) | 1996-03-13 |
JPS63116723A (ja) | 1988-05-21 |
CN87106270A (zh) | 1988-04-27 |
CA1321687C (en) | 1993-08-31 |
IN170064B (ko) | 1992-02-01 |
KR900008713B1 (ko) | 1990-11-27 |
EP0259288B1 (en) | 1992-10-07 |
ES2035108T3 (es) | 1993-04-16 |
DE3782128T2 (de) | 1993-02-18 |
MX168757B (es) | 1993-06-07 |
DE3782128D1 (de) | 1992-11-12 |
EP0259288A3 (en) | 1989-03-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR890001615A (ko) | 그래이드 밀도 피층을 갖는 비대칭성 기체 분리막의 제조방법 및 고점성 원액 | |
Nunes et al. | Evidence for spinodal decomposition and nucleation and growth mechanisms during membrane formation | |
US4056467A (en) | Hollow fibres | |
Strathmann et al. | The formation mechanism of phase inversion membranes | |
US3412184A (en) | Process for the preparation of cellulosic ester reverse osmosis membranes | |
CA1321686C (en) | Asymmetric gas separation membranes having graded density skins | |
ES8205359A1 (es) | Procedimiento para la fabricacion de membranas porosas de fibras huecas para la separacion de plasma | |
JPS5471785A (en) | Selectively permeable membrane and production thereof | |
FR2360623B1 (ko) | ||
KR940005729A (ko) | 다공성 중합체 구조물 및 열 유도 상 분리법에 의한 이러한 구조물의 제조방법 | |
ES403121A1 (es) | Procedimiento para la preparacion de membranas anisotropas semipermeables de poliarileter-sulfonas sulfonadas. | |
JPH03193126A (ja) | スルホン化ヘキサフルオロビス―aポリスルホン膜と流体分離方法 | |
KR950000203A (ko) | 리튬염 형태의 술폰화 방향족 중합체로부터 제조된 유체 분리 복합막 | |
ES8107038A1 (es) | Un metodo mejorado para preparar una membrana anisotropa | |
ES462762A1 (es) | Procedimiento para la produccion de una membrana de ultra- filtracion. | |
Chen et al. | Effect of nonsolvents on the mechanism of wet-casting membrane formation from EVAL copolymers | |
US4283359A (en) | Process for producing polyacrylonitrile reverse osmotic membranes | |
US3520960A (en) | Method of making microphorous cellulose nitrate films | |
JPS60132605A (ja) | 非対称膜の製造法 | |
BR9003375A (pt) | Membrana semi-permeavel,uso e processo para sua preparacao | |
US4631157A (en) | Production of permeable cellulose triacetate membranes | |
JPH0761432B2 (ja) | 高機能性非対称膜の製造方法 | |
KR910005913A (ko) | 기능이 향상된 비대칭성 기체분리막 | |
JPS5670805A (en) | Preparation of selectively permeable membrane for treating organic liquid | |
KR860006490A (ko) | 고강력 셀루로오즈 트리 아세테이트 섬유의 제조방법 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
G160 | Decision to publish patent application | ||
E701 | Decision to grant or registration of patent right | ||
GRNT | Written decision to grant | ||
FPAY | Annual fee payment |
Payment date: 19961014 Year of fee payment: 7 |
|
LAPS | Lapse due to unpaid annual fee |