GB2052381A - A process for joining fluorinated polymer cation exchange membrane - Google Patents

A process for joining fluorinated polymer cation exchange membrane Download PDF

Info

Publication number
GB2052381A
GB2052381A GB8004894A GB8004894A GB2052381A GB 2052381 A GB2052381 A GB 2052381A GB 8004894 A GB8004894 A GB 8004894A GB 8004894 A GB8004894 A GB 8004894A GB 2052381 A GB2052381 A GB 2052381A
Authority
GB
United Kingdom
Prior art keywords
cation exchange
membranes
fluorinated polymer
joining
exchange membrane
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.)
Withdrawn
Application number
GB8004894A
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry Co Ltd
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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Publication of GB2052381A publication Critical patent/GB2052381A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C66/00General aspects of processes or apparatus for joining preformed parts
    • B29C66/01General aspects dealing with the joint area or with the area to be joined
    • B29C66/02Preparation of the material, in the area to be joined, prior to joining or welding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C65/00Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor
    • B29C65/02Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor by heating, with or without pressure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C66/00General aspects of processes or apparatus for joining preformed parts
    • B29C66/70General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material
    • B29C66/71General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material characterised by the composition of the plastics material of the parts to be joined
    • 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
    • C08J5/2293After-treatment of fluorine-containing membranes
    • 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
    • C08J2371/00Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
    • C08J2371/08Polyethers derived from hydroxy compounds or from their metallic derivatives
    • C08J2371/10Polyethers derived from hydroxy compounds or from their metallic derivatives from phenols
    • C08J2371/12Polyphenylene oxides

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

A process for joining fluorinated polymer cation exchange membrane is provided, wherein fluorinated polymer cation exchange membranes containing the pendent groups of -COOH on at least one side of the membranes are treated with a tertiary amine or a quarternary ammonium base, then heat- pressed.

Description

SPECIFICATION A process for joining fluorinated polymer cation exchange membrane The present invention pertains to a process for joining fluorinated polymer cation exchange membranes. More particularly, it pertains to a process for joining fluorinated polymer cation exchange membranes which comprises treating fluorinated polymer cation exchange membranes containing the pendent groups of -COOH on at least one side of the membranes with a tertiary amine or a quaternary ammonium base, then heat-pressing the membranes so treated.
The joining of cation exchange membranes is exceedingly useful in the industry. In the industrial utilization of the joining art of cation exchange membranes, there are included, for example, formation of the cation exchange membrane in any desired shape, production of a sufficient size of the cation exchange membrane required for an industrial use when such a large size is difficult to be prepared. It is also useful in repairing a tear or a hole of cation exchange membranes which took place during utilization or handling.
The joining process of the present invention is characterized in that fluorinated polymer cation exchange membranes containing the pendent groups of -COOH on at least one side of the membranes are treated with a tertiary amine or a quaternary ammonium base, then heat-pressed.
The cation exchange membrane having carboxylic acid groups as the pendent group are known to the art as a capable membrane in a wide use and the joining art of the membrane is very much useful in the industry.
The cation exchange membrane used in the present invention includes a perfluorocarbon backbone cation exchange membrane with the pendent group of -COOH, and the like. The cation exchange membrane may contain the pendent group of -COOH on both surfaces of the membrane, in the entirety of the membrane or the one surface of the membrane. The thickness of such carboxylic acid group layer may be 1 11 or more, preferably 10 C1 or more. Carboxylic acid group has to be -COOH type, and -COOAtype (A: alkali metals) cation exchange membrane is not heat-processed.
As a treating agent for -COOH type fluorinated polymer cation exchange membranes, a tertiary amine or a quaternary ammonium base is suitably employed. -COOA type fluorinated polymer cation exchange membrane is not heat-presed, even if treated with a tertiary amine or a quaternary ammonium base.
A process for joining fluorinated polymer cation exchange membranes having sulfonic acid groups or sulfon amide groups is disclosed, for example, in the Japanese Patent Publication (non-examined) No.
49394/1975, wherein the membranes are treated with a tertiary amine, a quaternary ammonium base, or a salt thereof, then heat-melted. Notwithstanding, it has been discovered that the cation exchange membrane with the pendent group of carboxylic acid groups exhibits a somewhat different behaviour from the cation exchange membrane having the pendent groups of sulfonic acid groups or sulfon amide groups. That is, the membranes having alkali metal salts of carboxylic acid groups are not joined, even when treated with a salt of a tertiary amine or a quaternary ammonium base, then heat-pressed.
The present inventors have made a series of studies on treatment conditions, heat-melting conditions and the like and now discovered that the joined membranes satisfying the joining strength required for a wide variety of industrial use can be provided by treating fluorinated polymer cation exchange membranes containing the pendent groups of -COOH on at least one side of the membranes with a tertiary amine or a quaternary ammonium base, thereafter heat-pressing the so treated membranes.
It is not clear why -COOH type cation exchange membranes treated with a tertiary amine or a quaternary ammonium base are heat-processable, while -COOA type cation exchange membranes are not heat-processable even when treated with a salt of a tertiary amine or a quaternary ammonium base, but conjectured as follows. That is, the former is treated by neutralization reaction and thus the reaction takes place smoothly whereas the latter is treated by double decomposition reaction which does not occur thoroughly.
The heat-pressing is carried out using a hot press and the like at 200 to 300 C, preferably 230 to 260 C.
The pressing pressure is 2 to 150 kg/cm2, preferably 10 to 100 kg/cm2. The pressing time is 1 to 30 min., preferably 3 to 10 min.
The present invention will be explained in more detail by way of examples, which examples are not construed to limit the scope of the present invention.
Example 1 Cation exchange membranes obtained by denaturizing both sides of sulfon acid type cation exchange membranes to the carboxylic acid type was treated with hydrochloric acid to obtain -COOH type membranes. The so obtained membranes were treated with a 50 % aqueous methanol solution containing 0.2 mole of tetra(n-butyl)ammonium hydroxide for 1.5 hours, then heat-pressed for 5 min. at 2500C under the pressure of 80 kg/cm2. The resulting joined membranes were immersed for 1 month in a depleted brine discharged from an ion exchange membrane electrolytic cell, but no peeling off of the joined portion was observed.
Example 2 Cation exchange membranes, which were obtained by denaturization of one side of sulfonic acid type cation exchange membranes to the carboxylic acid type, was treated with hydrochloric acid, thereby obtaining -COOH type membranes. The obtained membranes were treated for 1.5 hours with a 50 % aqueous methanol solution containing 0.2 mole of tetra(n-butyl)ammonium hydroxide. The sides of carboxylic acids of the membranes thus treated were heat-pressed at 240 C under the pressure of 70 kg/cm2. The joined membranes were immersed in a depleted brine removed from an ion exchange membrane electrolytic cell. Even after 1 month, peeling off of the joined portion did not occur.

Claims (2)

1. A process for joining fluorinated polymer cation exchange membranes which comprises treating fluorinated polymer cation exchange membranes containing the pendent groups of -COOH on at least one side of the membranes with a tertiary amine or a quaternary ammonium base, then heatpressing the membranes so treated.
2. A process for joining fluorinated polymer cation exchange membranes substantially as described with reference to any one of the examples herein.
GB8004894A 1979-04-28 1980-02-13 A process for joining fluorinated polymer cation exchange membrane Withdrawn GB2052381A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5315579A JPS55145539A (en) 1979-04-28 1979-04-28 Joining method of cation exchange membrane

Publications (1)

Publication Number Publication Date
GB2052381A true GB2052381A (en) 1981-01-28

Family

ID=12934946

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8004894A Withdrawn GB2052381A (en) 1979-04-28 1980-02-13 A process for joining fluorinated polymer cation exchange membrane

Country Status (5)

Country Link
JP (1) JPS55145539A (en)
DE (1) DE3016340A1 (en)
FR (1) FR2455063A1 (en)
GB (1) GB2052381A (en)
IT (1) IT1144083B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998008679A2 (en) * 1996-08-26 1998-03-05 Minnesota Mining And Manufacturing Company Multi-layer articles comprising a fluoropolymer

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2121352B (en) * 1982-05-25 1986-03-19 Chlorine Eng Corp Ltd Bonding of cation exchange membrane
FR2617760B1 (en) * 1987-07-10 1989-11-24 Souriau & Cie PROCESS FOR ASSEMBLING PARTS OF POLYMERIC MATERIALS

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998008679A2 (en) * 1996-08-26 1998-03-05 Minnesota Mining And Manufacturing Company Multi-layer articles comprising a fluoropolymer
WO1998008679A3 (en) * 1996-08-26 1998-06-18 Minnesota Mining & Mfg Multi-layer articles comprising a fluoropolymer
US5855977A (en) * 1996-08-26 1999-01-05 Minnesota Mining And Manufacturing Company Multi-layer compositions comprising a fluoropolymer

Also Published As

Publication number Publication date
IT8048507A0 (en) 1980-04-24
JPS55145539A (en) 1980-11-13
FR2455063A1 (en) 1980-11-21
DE3016340A1 (en) 1980-11-13
IT1144083B (en) 1986-10-29

Similar Documents

Publication Publication Date Title
US6924318B2 (en) Method for making a bipolar membrane and use of resulting bipolar membrane
US4065366B1 (en)
US3510417A (en) Electrodialysis process for selectively transferring ions of the same charge
ZA892353B (en) Chlorine-resistant semipermeable membranes
US4670125A (en) Production of bipolar membranes
ATE119064T1 (en) METHOD FOR THE ELECTROCHEMICAL CLASSIFICATION OF ALKALINE SULPHATES.
EP0416312A2 (en) Method of continuously removing and obtaining ethylene diamine tetraacetic acid (EDTA) from the process water of electroless copper plating
GB2088883B (en) Cation exchange membrane and process for producing same
GB2052381A (en) A process for joining fluorinated polymer cation exchange membrane
US2318184A (en) Laminated sheet and method of producing same
CA1336898C (en) High performance bipolar membranes
US5849167A (en) Method for making a bipolar membrane
WO1996022154A3 (en) Regenerating acids, particularly strong organic acids, using bipolar membranes
JP3143222B2 (en) Method for producing acid and alkali
CA2321727A1 (en) Membrane filtration of polymer containing solutions
US4246091A (en) Process for the electrolytic treatment of alkali halide
JPS54130490A (en) Ion exchange membrane*its manufacture and use
JP3339961B2 (en) Method for producing amphoteric membrane and aqueous alkali metal hydroxide solution
CA1242555A (en) Production of ion-exchange membrane
DE2621590B2 (en) Electrolysis and electrodialysis method for an aqueous solution of a base
GB2040222A (en) A method for joining a fluorinated polymer film and a fluorinated polymer cation exchange membrane
GB2040803A (en) A method for joining fluorinated polymer cation exchange membranes
ATE117322T1 (en) AQUEOUS SOLUTIONS OR DISPERSIONS OF HYDROXY-FUNCTIONAL COPOLYMERS, A METHOD FOR THEIR PRODUCTION AND THEIR USE.
CA2415020A1 (en) Activation of a cathode
US3723273A (en) Electrodialytic production of stannic oxide sol

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)