GB1276151A - Semipermeable membranes - Google Patents
Semipermeable membranesInfo
- Publication number
- GB1276151A GB1276151A GB2224969A GB2224969A GB1276151A GB 1276151 A GB1276151 A GB 1276151A GB 2224969 A GB2224969 A GB 2224969A GB 2224969 A GB2224969 A GB 2224969A GB 1276151 A GB1276151 A GB 1276151A
- Authority
- GB
- United Kingdom
- Prior art keywords
- water
- membrane
- solvent
- cellulosic
- wet
- 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.)
- Expired
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
- B01D67/0095—Drying
Abstract
1276151 Cellulosic membrane EASTMAN KODAK CO 1 May 1969 [3 May 1968] 22249/ 69 Heading B1X [Also in Divisions B5 and C3] To produce a semi-permeable reverse osmosis membrane useful in desalinating water, a water-wet cellulosic semi-permeable membrane, e,g. of cellulose acetate, is dried by first contacting it with a water-miscible organic solvent (A) which is liquid in the range 5- 40‹C and is able to form a clear solution with at least 5% by wt of water, until at least 80%, preferably 90%, of the water is replaced by the solvent and then with a non-polar organic solvent (B) also liquid in the range 5-40‹C and which is able to form a clear solution with at least 5% of (A) until at least 70% of (A) is replaced by (B) which is then removed by evaporation and/or mechanical means. Bath (A) and (B) must be non-solvents for the membrane. Specified solvents are for (A), C 1 _ 4 alkanols and for (B) benzene, toluene, petrol ether, xylene, naphtha, diethyl ether, hexane and cyclohexane. The membrane may also be impregnated with a polyol (e.g. 5-70%) applied as a solution (e.g. 5-25%) in solvent (A). Specified are various glycols and glycerine. The wet membrane may be derived by casting a cellulosic solution followed by quenching in cold water. The wet film may be "tempered" in hot water before drying. Excess water and solvent (A) may be removed mechanically before contacting with solvent (B).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US72655068A | 1968-05-03 | 1968-05-03 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1276151A true GB1276151A (en) | 1972-06-01 |
Family
ID=24919056
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2224969A Expired GB1276151A (en) | 1968-05-03 | 1969-05-01 | Semipermeable membranes |
GB145972A Expired GB1276152A (en) | 1968-05-03 | 1969-05-01 | Cellulosic semi-permeable membrane |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB145972A Expired GB1276152A (en) | 1968-05-03 | 1969-05-01 | Cellulosic semi-permeable membrane |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE732532A (en) |
CA (1) | CA923664A (en) |
DE (1) | DE1922536A1 (en) |
FR (1) | FR2007782A1 (en) |
GB (2) | GB1276151A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0326076A2 (en) * | 1988-01-29 | 1989-08-02 | Hoechst Celanese Corporation | Air dried cellulose acetate membranes |
EP0465697A1 (en) * | 1990-07-10 | 1992-01-15 | Industrial Technology Research Institute | Preparation of gas separation membrane and spiral wound gas separation module |
CN103127744A (en) * | 2011-11-28 | 2013-06-05 | 中国科学院金属研究所 | Method for transferring nano-particles from oil phase into aqueous phase |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2736569B2 (en) * | 1977-08-13 | 1979-07-19 | Hoechst Ag, 6000 Frankfurt | Viscous membrane for hemodialysis and process for their manufacture |
SE423106B (en) * | 1980-07-25 | 1982-04-13 | Gambro Dialysatoren | PLASMAFERES MEMBRANE AND WAY TO MANUFACTURE THIS |
EP0046817B1 (en) * | 1980-09-01 | 1984-11-28 | Gambro, Inc. | Dry polycarbonate membrane and process of manufacture |
-
1969
- 1969-04-03 CA CA047750A patent/CA923664A/en not_active Expired
- 1969-05-01 GB GB2224969A patent/GB1276151A/en not_active Expired
- 1969-05-01 GB GB145972A patent/GB1276152A/en not_active Expired
- 1969-05-02 DE DE19691922536 patent/DE1922536A1/en active Pending
- 1969-05-02 FR FR6914052A patent/FR2007782A1/fr not_active Withdrawn
- 1969-05-05 BE BE732532D patent/BE732532A/xx unknown
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0326076A2 (en) * | 1988-01-29 | 1989-08-02 | Hoechst Celanese Corporation | Air dried cellulose acetate membranes |
EP0326076A3 (en) * | 1988-01-29 | 1990-05-23 | Air Products And Chemicals, Inc. | Air dried cellulose acetate membranes |
EP0465697A1 (en) * | 1990-07-10 | 1992-01-15 | Industrial Technology Research Institute | Preparation of gas separation membrane and spiral wound gas separation module |
CN103127744A (en) * | 2011-11-28 | 2013-06-05 | 中国科学院金属研究所 | Method for transferring nano-particles from oil phase into aqueous phase |
CN103127744B (en) * | 2011-11-28 | 2014-12-10 | 中国科学院金属研究所 | Method for transferring nano-particles from oil phase into aqueous phase |
Also Published As
Publication number | Publication date |
---|---|
BE732532A (en) | 1969-10-16 |
FR2007782A1 (en) | 1970-01-09 |
CA923664A (en) | 1973-04-03 |
DE1922536A1 (en) | 1970-08-27 |
GB1276152A (en) | 1972-06-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |