GB733100A - Permselective membranes, their manufacture and use in electrodialysis - Google Patents

Permselective membranes, their manufacture and use in electrodialysis

Info

Publication number
GB733100A
GB733100A GB3889/53A GB388953A GB733100A GB 733100 A GB733100 A GB 733100A GB 3889/53 A GB3889/53 A GB 3889/53A GB 388953 A GB388953 A GB 388953A GB 733100 A GB733100 A GB 733100A
Authority
GB
United Kingdom
Prior art keywords
membrane
group
compound
replaced
membranes
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
Application number
GB3889/53A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO
Original Assignee
Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO
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 Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO filed Critical Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO
Publication of GB733100A publication Critical patent/GB733100A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/422Electrodialysis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • B01D67/0006Organic membrane manufacture by chemical reactions
    • 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
    • B01D71/76Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74
    • B01D71/82Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74 characterised by the presence of specified groups, e.g. introduced by chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B11/00Preparation of cellulose ethers
    • C08B11/02Alkyl or cycloalkyl ethers
    • C08B11/04Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals
    • C08B11/14Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals with nitrogen-containing groups
    • C08B11/15Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals with nitrogen-containing groups with carbamoyl groups, i.e. -CO-NH2
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/30Introducing nitrogen atoms or nitrogen-containing groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/20Manufacture of shaped structures of ion-exchange resins
    • C08J5/22Films, membranes or diaphragms
    • C08J5/2206Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
    • C08J5/2218Synthetic macromolecular compounds
    • C08J5/2256Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions other than those involving carbon-to-carbon bonds, e.g. obtained by polycondensation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/20Manufacture of shaped structures of ion-exchange resins
    • C08J5/22Films, membranes or diaphragms
    • C08J5/2287After-treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/12Chemical modification
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2375/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04Polyurethanes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Abstract

Semi-permeable selective membranes are made of high molecular weight organic substances in which hydrogen atoms of reactive hydroxyl groups have been at least partly replaced by side chains of the formula <FORM:0733100/IV (a)/1> in which R represents an organic group containing at least one ionic group, i.e. an ionisable radical capable of dissociating in aqueous medium so that an electrically charged radical remains linked to the high molecular weight substance. A membrane of cellulose such as paper, transparent paper or regenerated cellulose, or of regenerated amylose, polyvinyl alcohol or similar high molecular weight substance with reactive hydroxyl groups may be reacted with a compound containing at least one N-methylol acid amide group with at least one ionic group or with a group which can readily be replaced by an ionic group in a second processing stage. A N-methylol compound of an acid amide wherein at least one hydrogen atom bound to a carbon atom has been replaced by halogen or by a trialkylamino, dialkylamino or sulphonic acid group may be used for introducing the desired groups into the substance of the membrane. For producing a positive membrane, the methylol compound of carbamidomethyl-trimethyl ammonium chloride or the methylol compound of chloro-acetamide may be used. For the production of a negative membrane from the compound thus obtained, the chlorine atom may be replaced by a sulphonic acid group, e.g. by the action of potassium sulphite. If the chlorine atom is replaced by dimethylamine, a positive membrane is obtained and the positive character may further be intensified by the action of methyl iodide. The membranes obtained preserve their selectivity in relatively strong salt concentrations in a liquid to be desalted and in the rinsing liquids. The selectivity of the membranes may be measured by determination of the concentration potential between solutions of potassium chloride of different concentrations separated by the membrane. A concentration potential of 55 mV, as compared with an ideal value of 58 mV, may be obtained when a membrane into which quaternary ammonium groups have been introduced is arranged as a partition between a 0.001 N KCl and a 0.01 N KCl solution. To reduce the swelling of the membranes in aqueous solutions, they may be reacted with compounds such as formaldehyde or the dimethylol compound of adipamide so as to form non-ionic bridge-bonds. Alternatively bridgebonds containing at least one ionic group may be formed, e.g. the cellulose or other membrane may be reacted with the methylol compound of a ,a 1-dibromoadipic diamide. In an example, a ,a 1 - bisdimethylamino - adipamide hydrochloride is dissolved in an aqueous solution of formaldehyde and then caustic soda is added. After one hour, oxalic acid is added and the precipitated sodium oxalate is filtered off. A regenerated cellulose membrane is soaked in the solution, dried, and then heated at 100 DEG C. In another example, a membrane of polyvinyl alcohol is impregnated with a solution obtained by heating a solution containing carbamido-methyl-trimethyl-ammonium chloride and adipamide with formaldehyde and potassium carbonate and subsequently acidifying with oxalic acid and hydrochloric acid to a pH of 2.0. The impregnated membrane is dried and then heated at 140 DEG C. for 10 minutes. The membranes have good ion-selective properties with respect to polyvalent ions and may be used for desalting brackish water containing magnesium sulphate. In an example, sea-water with a NaCl content of 30 gm./litre is placed in a three-chamber apparatus in which the anode compartment is separated from the dialysis compartment by a positive ion-selective membrane of regenerated cellulose which has been combined with the methylol compound of carbamidomethyl - trimethyl - ammonium chloride, and in which the cathode compartment is separated from the dialysis compartment by a negative ion-selective membrane of regenerated cellulose which has been combined with the methylol compound of a ,a 1-adipamide-disulphonic acid. The dialysis may be carried out at current densities of 2.5-25 m.Amp./sq. cm.ALSO:Semi-permeable selective membranes are made of high molecular weight organic substances in which hydrogen atoms of reactive hydroxyl groups have at least been partly replaced by side chains of the formula <FORM:0733100/IV (b)/1> in which R represents an organic group containing at least one ionic group, i.e. an ionizable radical capable of dissociating in aqueous medium so that an electrically charged radical remains linked to the high molecular weight substance. A membrane of regenerated amylose, or similar high molecular weight substance with reactive hydroxyl groups may be reacted with a compound containing at least one N-methylol acid amide group with at least one ionic group or with a group which can readily be replaced by an ionic group in a second processing stage. A N-methylol compound of an acid amide wherein at least one hydrogen atom bound to a carbon atom has been replaced by halogen or by a trialkylamino, dialkylamino, or sulphonic acid group may be used for introducing the desired groups into the substance of the membrane. For producing a positive membrane, the methylol compound of carbamidomethyl-trimethyl ammonium chloride or the methylol compound of chloro-acetamide may be used. For the production of a negative membrane from the compound thus obtained, the chlorine atom may be replaced by a sulphonic acid group, e.g. by the action of potassium sulphite. If the chlorine atom is replaced by dimethylamine, a positive membrane is obtained and the positive character may further be intensified by the action of methyl iodide. The membranes obtained preserve their selectivity in relatively strong salt concentrations in a liquid to be desalted and in the rinsing liquids. To reduce the swelling of the membranes in aqueous solutions, they may be reacted with compounds such as formaldehyde or the dimethylol compound of adipamide so as to form non-ionic bridge-bonds. Alternatively bridge-bonds containing at least one ionic group may be formed, e.g. the amylose membrane may be reacted with the methylol compound of a ,a -dibromoadipic diamide. In an example, a membrane of amylose is impregnated with a solution obtained by heating an aqueous solution containing carbamidomethyl-trimethyl-ammonium chloride, formaldehyde, and potassium carbonate and subsequently acidifying with oxalic acid to a pH of 2.0. The impregnated membrane is dried and then heated in air at 140 DEG C. for 10 minutes.
GB3889/53A 1952-02-11 1953-02-11 Permselective membranes, their manufacture and use in electrodialysis Expired GB733100A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL733100X 1952-02-11

Publications (1)

Publication Number Publication Date
GB733100A true GB733100A (en) 1955-07-06

Family

ID=19820332

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3889/53A Expired GB733100A (en) 1952-02-11 1953-02-11 Permselective membranes, their manufacture and use in electrodialysis

Country Status (3)

Country Link
BE (1) BE517435A (en)
GB (1) GB733100A (en)
NL (1) NL77406C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0147369A2 (en) * 1983-12-22 1985-07-03 Ciba-Geigy Ag Cellulosic material ionically modified, its preparation and use
EP0167488A2 (en) * 1984-07-06 1986-01-08 Ciba-Geigy Ag Ionically modified polysaccharides, process for their preparation and their use
CN113437341A (en) * 2021-06-28 2021-09-24 泰山学院 Amphoteric ion conduction membrane for flow battery and preparation method thereof

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0147369A2 (en) * 1983-12-22 1985-07-03 Ciba-Geigy Ag Cellulosic material ionically modified, its preparation and use
EP0147369A3 (en) * 1983-12-22 1986-12-10 Ciba-Geigy Ag Cellulosic material ionically modified, its preparation and use
EP0167488A2 (en) * 1984-07-06 1986-01-08 Ciba-Geigy Ag Ionically modified polysaccharides, process for their preparation and their use
EP0167488A3 (en) * 1984-07-06 1987-05-20 Ciba-Geigy Ag Ionically modified polysaccharides, process for their preparation and their use
US5010184A (en) * 1984-07-06 1991-04-23 Ciba-Geigy Corporation Ionically modified agarose
CN113437341A (en) * 2021-06-28 2021-09-24 泰山学院 Amphoteric ion conduction membrane for flow battery and preparation method thereof
CN113437341B (en) * 2021-06-28 2022-04-12 泰山学院 Amphoteric ion conduction membrane for flow battery and preparation method thereof

Also Published As

Publication number Publication date
NL77406C (en)
BE517435A (en)

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