Selectively permeable barriers

• US 5,147,553 A
• Filed: 03/29/1991
• Issued: 09/15/1992
• Est. Priority Date: 05/04/1988
• Status: Expired due to Fees

• Current Assignee: Ionics Incorporated (Veolia Environnement SA)
• Original Assignee: Ionics Incorporated (Veolia Environnement SA)
• Inventors: Waite, Warren A.
• Primary Examiner(s): SPEAR JR, FRANK
• Application Number:
  US07/677,201
• Time in Patent Office: 536 Days
• Field of Search: 210/500.34, 210/500.41, 210/500.42, 210/490, 210/651, 210/652, 210/654, 423/445, 204/182.4, 264/41, 264/49, 427/245, 427/246
• US Class Current: 210/654
• CPC Class Codes: B01D 69/1251 by interfacial polymerisation

Abstract

Apparatus and process for separating a fluid mixture into less permeable and more permeable fractions employing novel selectively permeable barriers comprised of a porous, emulsion treated substrate and a non-porous selectively permeable barrier layer thereon.

Claims

1. A process for forming a microporous membrane which process comprises contacting a solution comprising one or more polymers in a first liquid, said solution being in the form of a tube or sheet, with a second liquid which second liquid is a substantial solvent for at least part of said first liquid and substantially a non-solvent for at least one of said polymers, said second liquid comprising a suspension or emulsion comprising as the disperse phase particles of one or more carbon compounds which are solids at room temperature and substantially insoluble in said second liquid.

2. A process according to claim 1 in which said one or more polymers is selected from the group consisting of polysulfones, polyarylsulfones, polyether sulfones, polyphenyl sulfones, polypropylene, cellulose, polycarbonates, polyphenylene oxides, polyvinyl chlorides, cellulose nitrates, cellulose acetate-nitrate, polyvinylidene fluorides, polytetrafluoroethylene-coethylene, derivatives of said members of the group and mixture thereof.

3. A process according to claim 1 in which said one or more carbon compounds is a polymer of one or more monomers selected from the group consisting of butadiene, acrylonitrile, styrene, isoprene, vinyl pyridine, vinyl chloride, vinyl acetate, vinylidene chloride, acrylic monomers, vinyl fluoride, vinylidene fluoride, tetrafluorethylene and ethylene.

4. A selectively permeable barrier for separating a fluid mixture into less permeable and more permeable fractions said barrier comprising in whole or in part a microporous membrane prepared in accordance with claim 1.

5. Apparatus for separating a fluid mixture into less permeable and more permeable fractions, said apparatus containing at least a selectively permeable barrier which barrier comprises in whole or in part a microporous membrane prepared in accordance with claim 1.

6. A process for separating a fluid mixture into less permeable and more permeable fractions, said process comprising contacting said fluid mixture with a selectively permeable barrier which barrier comprises in whole or in part a microporous membrane prepared in accordance with claim 1.

7. A process for substantially selectively removing nitrate from water, said process comprising flowing said water through the diluting compartments of an electrodialysis stack in which at least one of the anion selective barriers thereof comprises a microporous substrate prepared in accordance with claim 1 and having on the dilute stream side thereof a barrier layer substantially selective for the removal of nitrate compared to the other ionic species of the same charge sign.

8. Apparatus for substantially selectively removing nitrate from water, said apparatus comprising an electrodialysis stack in which at least one of the anion selective barriers thereof comprises a microporous substrate prepared in accordance with claim 1 and having on the dilute stream side thereof a barrier layer substantially selective for the removal of nitrate compared to other ionic species of the same charge sign.

9. A process for forming a semipermeable non-porous membrane comprising contacting a microporous substrate with a liquid suspension the disperse phase of which comprises particles of at least one solid substantially insoluble in the dispersing phase, such liquid suspension also comprising dissolved components capable of reacting with one or more other components not present in said liquid suspension to form a non-porous, semi-permeable film and subsequently contacting said substrate with a fluid comprising said one or more other components, said fluid characterized by being substantially insoluble in said liquid suspension, said the dispersing phase in said liquid suspension characterized by being substantially insoluble in said fluid.

10. A selectively permeable barrier for separating a fluid mixture into less permeable and more permeable fractions prepared in accordance with claim 9.

11. Apparatus for separating a fluid mixture into less permeable and more permeable fractions, said apparatus comprising a selectively permeable barrier prepared in accordance with claim 9.

12. A process for separating a fluid mixture into less permeable and more permeable fractions, said process comprising contacting said fluid mixture with a selectively permeable barrier prepared in accordance with claim 9.

13. A process for separating a fluid mixture into less permeable and more permeable fractions comprising contacting said fluid mixture with one surface of a selectively permeable barrier prepared by contacting a microporous membrane with a first liquid comprising a suspension or emulsion which suspension or emulsion comprises as the disperse phase particles of one or more compounds which are solids at room temperature and substantially insoluble in said first liquid, said first liquid also comprising one or more moieties selected from the group consisting of polyethylenimines;

reaction products of ethylene diamine, piperazine, methyl piperazine, and/or dimethyl piperazines with a polyepihalohydrin;

phenylene diamines;

xylylene diamines;

chlorophenylene diamines;

benzene triamines;

bis(aminobenzyl) aniline;

tetraaminobenzenes;

piperazine;

methyl piperazine;

dimethyl piperazines;

homopiperazine;

N,N'"'"'-diphenylethylene diamine;

aminobenzamides;

aminobenzhydrazides; and

bis(alkylamino)phenylene diamines

and subsequently contacting said microporous membrane with a second liquid comprising one or more moieties selected from the group consisting of

phthaloyl halides;

benzene tricarboxylic acid halides;

cyclohexane tricarboxylic acid halides;

pyridine dicarboxylic acid halides;

trimellitic anhydride acid halides;

sebacic acid halides;

azelaic acid halides;

adipic acid halides;

dodecanedioic acid halides;

toluene diisocyanate;

methylene bis(phenylisocyanates);

polymethylene bis(phenylisocyanates);

naphthalene diisocyanates;

bitolyene diisocyanates;

hexamethylene diisocyanate; and

phenylene diisocyanates,

creating a pressure difference through said selectively permeable barrier in a direction to urge said more permeable fraction from said one surface of said selectively permeable barrier through said selectively permeable barrier and recovering separately said less permeable and more permeable fractions.

14. Reverse osmosis apparatus containing at least a selectively permeable barrier, said barrier prepared by contacting a microporous membrane with a first liquid comprising a suspension or emulsion which suspension or emulsion comprises as the disperse phase particles of one or more carbon compounds which are solids at room temperature and substantially insoluble in said first liquid, said first liquid also comprising one or more moities selected from the group consisting of

polyethylenimines;

reaction products of ethylene diamine, piperazine, methyl

piperazine and/or dimethyl piperazines with a

polyepihalohydrin;

phenylene diamines;

xylylene diamines;

chlorophenylene diamines;

benzene trimines;

bis(aminobenzyl)aniline;

tetraamino benzenes;

piperazine;

methyl piperazine;

dimethyl piperazines;

homopiperazine;

N,N'"'"'-diphenyl ethylene diamine;

aminobenzamides;

aminobenzhydrazides; and

bis(alkylamino)phenylene diamines

and subsequently contacting said microporous membrane with a second liquid comprising one or more moities selected from the group consisting of

phthaloyl halides;

benzene tricarboxylic acid halides;

cyclohexane tricarboxylic acid halides;

pyridine dicarboxylic acid halides;

trimellitic anhydride acid halides;

sebacic acid halides;

azelaic acid halides;

adipic acid halides;

dodecanedioic acid halides;

toluene diisocyanate;

methylene bis(phenylisocyanates);

polymethylene bis(phenylisocyanates);

naphthalene diisocyanates;

bitolyene diisocyanates;

hexamethylene diisocyanate; and

phenylene diisocyanates.

15. Apparatus for the electrolysis of chlorine brine to caustic and chlorine, said apparatus comprising a microporous substrate having on and/or in only one surface thereof a non-porous, thin, dense barrier layer selectively permeable for alkali metal cations, said barrier layer comprising a hydrolyzed copolymer of at least one monomer selected from the group consisting of alkyl perfluoro-oxa-alkenoates, alkyl perfluor-dioxa-alkenoates, perfluoro-oxa-alkenesulfonyl halides, perfluoro-dioxa-alkene sulfonyl halides, derivatives of said group and mixtures thereof, the other surface of said substrate being substantially free of said hydrolyzed polymer.

16. A process for electrolyzing chloride brine to caustic and chlorine, said process comprising contacting said brine with the barrier layer of a microporous substrate having on and/or in only one surface thereof a non-porous, thin, dense barrier layer selectively permeable for alkali metal cations, said barrier layer comprising a hydrolyzed copolymer of at least one monomer selected from the group consisting of alkyl perfluoro-oxa-alkenoates, alkyl perfluoro-dioxa-alkenoates, perfluoro-oxa-alkenesulfonyl halides, perfluoro-dioxa-alkene sulfonyl halides, derivatives of said group and mixtures thereof, the other surface of said substrate being substantially free of said hydrolyzed polymer and passing a substantially direct electric current through said brine and said barrier layer.