IL41210A - Polymeric membranes for reverse osmosis and their preparation - Google Patents

Polymeric membranes for reverse osmosis and their preparation

Info

Publication number
IL41210A
IL41210A IL41210A IL4121072A IL41210A IL 41210 A IL41210 A IL 41210A IL 41210 A IL41210 A IL 41210A IL 4121072 A IL4121072 A IL 4121072A IL 41210 A IL41210 A IL 41210A
Authority
IL
Israel
Prior art keywords
membrane
process according
water
polypiperazinamide
solvent
Prior art date
Application number
IL41210A
Other versions
IL41210A0 (en
Original Assignee
Montedison Spa
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Montedison Spa filed Critical Montedison Spa
Publication of IL41210A0 publication Critical patent/IL41210A0/en
Publication of IL41210A publication Critical patent/IL41210A/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/56Polyamides, e.g. polyester-amides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/42Polyamides containing atoms other than carbon, hydrogen, oxygen, and nitrogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

1391559 Reverse osmosis membranes MONTECATINI EDISON SpA 1 Jan 1973 [30 Dec 1971] 59662/72 Heading B5B An isotropic reverse osmosis membrane of a polypiperazinamide having recurring units of the general formula is disclosed, where R is an organic substituent of the piperazine ring, x is from 1 to 8 and Y is an oxygen or sulphur atom. Preferably R is C 1 to C 4 alkyl, especially methyl or ethyl and x = 1 or 2. Specified polypiperazinamides include poly (2-methyl piperazin-thiofurazanamide), poly (2 - methylpiperazin - furazanamide), poly (trans - 2,5 - dimethylpiperazin - thio furazanamide), and poly (trans - 2,5 - dimethyl piperazin-furazanamide). A solution of the polypiperazinamide in an organic water soluble aprotic polar solvent is spread preferably at room temperature, on a smooth surface to form a film suitably of 0À002 to 0À2 cm. thickness, a membrane made therefrom by surface evaporation of the solvent, e.g. at 70‹ to 200‹ C., especially 80‹ to 180‹ C., for from 1 min. to 3 hours, especially 3 to 30 mins. and the membrane congulated by immersion in a coagulating bath, suitably water or an aqueous saline solution, e.g. of sodium or calcium chloride or magnesium sulphate, or alternatively mixtures of water with methanol, ethanol or isopropyl alcohol. The congulating liquid temperature is suitably 0‹ to 30‹ C. especially 0‹ to 5‹C. Specified solvents include dimethylformamide, dimethyl-acetamide, dimethyl sulphoxide, N- methylpyrrolidone and tetramethyl sulphone, which may also contain dissolved therein, water, and a salt soluble in water and in the organic solvent, e.g. lithium chloride, bromide and nitrate, calcium, zinc and magnesium chlorides and magnesium chlorate. The membrane may be subjected to a heat treatment before use by immersion in water at 60-100‹ C. for from 1 min. to 5 hours. [GB1391559A]

Claims (25)

1. An anisotropic reverse osmosis membrane of a polypiperazinamide having units of the general formul in which R is an organic substituent of the piperazine ring, x is an integer from 1 to 8 and Y is an oxygen or sulphur atom.
2. A membrane according to Claim 1,wherein R represents an alkyl radical that contains from 1 to 4 carbon atoms.
3. A membrane according to Claim 2, wherein R represents a methyl or ethyl radical.
4. A membrane according to any preceding claim, wherein x is 1 or 2.
5. A membrane according to Claim 1, wherein the polypiperazinamide is poly (2-methylpiperazin-thiofura-zanamide) .
6. A membrane according to Claim 1, wherein the polypiperazinamide is poly (2-methylpiperazin-furazanamide)
7. A membrane according to Claim 1, wherein the polypiperazinamide is polytrans-2 , 5-dimethylpiperazin-thiofurazanamide) .
8. A membrane according to Claim 1, wherein the polypiperazinamide is poly- (trans-2 , 5-"dimethylpiperazin-furazanamide) .
9. A reverse osmosis membrane of a polypiperazinamide substantially as described in -any of the Examples 41210/2
10. A process for the preparation of a reverse osmosis membrane according to any of Claims 1 to 8, which comprises carrying out the following successive steps: (1) preparing a solution of the polypiperazin- amide in an organic water soluble aprotic polar solvent, (2) spreading a film of the solution on a smooth surface, (3) forming a membrane by the surface evaporation of the solvent, and (4) coagulating the membrane by immersion in a coagulating liquid.
11. A process according to Claim 10, wherein the solvent of step (1) is dimethylformamide , dimethyl-acetamide, dimethylsulphoxide , N-methylpyrrolidone or tetramethylsulphone .
12. A process according to Claim 10 or Claim 11, wherein the solvent of step (1) contains dissolved therein a salt soluble in water and in the organic solvent.
13. A process according to Claim 12, wherein the salt is lithium chloride, lithium nitrate, lithium bromide, calcium chloride, zinc chloride, magnesium chloride or magnesium perchlorate.
14. A process according to Claim 12 or Claim 13, wherein the solvent of step (1) also contains water.
15. A process according to any of Claims 10 to 14, wherein the film of step (2) has a thickness of from 0.002 to 0.2 cm.
16. A process according to any of Claims 10 to 15, wherein the film of step (2) is spread at room temperature.
17. A process according to any of Claims 10 to 15, 41210/2
18. A process according to Claim 17,wherein the surface evaporation of step (3) is carried out at from 80eC to 180eC.
19. A process according to any of Claims 10 to 18, wherein the surface evaporation of step (3) is carried out for from 1 minute to 3 hours.
20. A process according to Claim 19, wherein the surface evaporation of step (3) is carried ou for from 3 to 30 minutes.
21. A process according to any of Claims 10 to 20, wherein the coagulating liquid of step (4) is water.
22. A process according to any of Claims 10 to 21, wherein the temperature of the coagulating liquid of step (4) is 0eC to 30*C.
23. A process according to Claim 22, wherein the temperature of the coagulating liquid o step (4) is 0eC to 5eC.
24. A process according to any of Claims 10 to 23, wherein the membrane is subjected to a heat treatment before use by immersing the membrane in water at from 60*C to 100° for from 1 minute 5 hours. -----·
25. A process for the preparation of a reverse osmosis membrane of a polypiperazinamlde, substantially as described in any of Examples 1 to 8 herein. ND/AJ
IL41210A 1971-12-30 1972-12-29 Polymeric membranes for reverse osmosis and their preparation IL41210A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT33137/71A IT944578B (en) 1971-12-30 1971-12-30 POLYMER MEMBRANES FOR REVERSE OSMOSIS WITH HIGH FLOW OF WATER AND HIGH SALINE REJECTION AND METHOD OF PREPARATION OF SUCH MEMBRANES

Publications (2)

Publication Number Publication Date
IL41210A0 IL41210A0 (en) 1973-02-28
IL41210A true IL41210A (en) 1976-08-31

Family

ID=11236670

Family Applications (1)

Application Number Title Priority Date Filing Date
IL41210A IL41210A (en) 1971-12-30 1972-12-29 Polymeric membranes for reverse osmosis and their preparation

Country Status (13)

Country Link
JP (1) JPS5611484B2 (en)
BE (1) BE793504A (en)
BR (1) BR7209266D0 (en)
CA (1) CA1018315A (en)
DE (1) DE2263774C2 (en)
EG (1) EG10806A (en)
ES (1) ES410178A1 (en)
FR (1) FR2166115B1 (en)
GB (1) GB1391559A (en)
IL (1) IL41210A (en)
IT (1) IT944578B (en)
NL (1) NL175884C (en)
ZA (1) ZA729171B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ZA74296B (en) * 1973-01-16 1974-11-27 Montedison Spa Reverse osmosis anisotropic membranes with great water flow and strong saline rejection,based on polypiperazine amides,and process for preparing such membranes
DE3220376A1 (en) * 1982-05-29 1983-12-01 Seitz-Filter-Werke Theo & Geo Seitz GmbH und Co, 6550 Bad Kreuznach MEMBRANE FILTER FOR MICROFILTRATION AND METHOD FOR THE PRODUCTION THEREOF
IT1153101B (en) * 1982-07-01 1987-01-14 Montedison Spa PROCEDURE FOR THE PREPARATION OF ANISOTROPIC FORMED BODIES BASED ON POLY-PIPERAZINAMIDES
IT1222627B (en) * 1987-09-09 1990-09-05 Separem Spa PROCEDURE FOR THE PREPARATION OF MEMBRANES FOR REVERSE OSMOSIS AND MEMBRANES OBTAINED BY THIS PROCEDURE
US4921611A (en) * 1987-10-14 1990-05-01 Schucker Robert C Thin film composite membrane prepared by deposition from a solution
US4837054A (en) * 1987-10-14 1989-06-06 Exxon Research And Engineering Company Thin film composite membrane prepared by deposition from a solution
US4879044A (en) * 1987-10-14 1989-11-07 Exxon Research And Engineering Company Highly aromatic anisotropic polyurea/urethane membranes and their use for the separation of aromatics from non aromatics
US4861628A (en) * 1987-10-14 1989-08-29 Exxon Research And Engineering Company Thin film composite membrane prepared by suspension deposition
US4828773A (en) * 1987-10-14 1989-05-09 Exxon Research And Engineering Company Highly aromatic anisotropic polyurea/urethane membranes and their use for the separation of aromatics from non-aromatics
US5045354A (en) * 1989-12-19 1991-09-03 Exxon Research & Engineering Company Production of supported thin film membranes

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7009957A (en) * 1969-07-08 1971-01-12
NL171019C (en) * 1969-07-08 1983-02-01 Consiglio Nazionale Ricerche MEMBRANES FOR REVERSE OSMOSIS.

Also Published As

Publication number Publication date
NL175884C (en) 1985-01-16
BR7209266D0 (en) 1973-09-25
ES410178A1 (en) 1975-12-01
GB1391559A (en) 1975-04-23
IT944578B (en) 1973-04-20
JPS4880481A (en) 1973-10-27
DE2263774C2 (en) 1982-04-01
IL41210A0 (en) 1973-02-28
JPS5611484B2 (en) 1981-03-14
BE793504A (en) 1973-06-29
FR2166115A1 (en) 1973-08-10
NL7217668A (en) 1973-07-03
NL175884B (en) 1984-08-16
CA1018315A (en) 1977-10-04
FR2166115B1 (en) 1976-04-23
DE2263774A1 (en) 1973-07-12
ZA729171B (en) 1973-09-26
EG10806A (en) 1976-09-30

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