CA1159199A

CA1159199A - Ion exchange resins

Info

Publication number: CA1159199A
Application number: CA000367437A
Authority: CA
Inventors: Tadeusz F. Molinski; Michael V. Markus
Original assignee: ICI Australia Ltd
Current assignee: Orica Ltd
Priority date: 1979-12-28
Filing date: 1980-12-23
Publication date: 1983-12-20
Also published as: EP0032021A2; EP0032021B1; NZ195570A; JPS56100638A; FI803941L; ZA807247B; FI68067B; DE3070402D1; US4385130A; FI68067C; EP0032021A3

Abstract

ABSTRACT
Ion Exchange Resins A cation exchange resin, suitable for use as a membrane in electrolysis cells, comprising a per-halogenated fluorine containing hydrocarbon polymeric substrate with pendant active side chains containing dicarboxylic acid groups or their derivatives, and method of preparation thereof.

Description

~ 1 t) 9 i 9 ~ ~

The presen-t invention relates to novel cation exchange resins, their preparation and their use; in particular it relates to cation exchange materials suit-able for use as permselective membranes in electrolytic cells such as are used in the manufacture of alkali metal hydroxide solutions and chlorine.
Alkali metal hydroxide solutions and chlorine axe generally manufactured in mercury cells or diaphragm cells. Mercury cells have the advantage of producing concentrated alkali metal hydroxide solutions but give rise to problems associated with the disposal of mercury-containing effluents. On the other hand, diaphragm cells, in which the anodes and cathodes are separated by porous diaphragms which permit the passage of both positive and negative ions and of electrolyte, avoid the aforesaid effluent problem, but have the disadvantage that (1) relatively weak impure alkali metal hydroxide solutions are produced, which results in increased evaporation costs, and (2) there is a possibility of product gases, namely hydrogen and chlorine, becoming mixed.
Attempts have been made to overcome dis-advantages of both mercury cells and diaphragm cells by the use of cells in which the anodes and cathodes are separated by cation-active permselective membranes;
these are membranes which are selectively permeable so as to allow the passage of only positively charged ions and not the passage of bulk electrolyte. Cation-active perm-selective membranes which are suitable for this use in chlorine cells include, for example, those made of synthetic organic copolymeric material containing cation-exchange groups, for example sulphonate, carboxy-late and phosphonate.
- In particular, synthetic fluoropolymers which will withstand cell conditions for long periods of time '~

~ ~59i9~3 are useful, for example the perfluorosulphonic acid membran~s manufactured and sold by E I DuPont de Nemours and Company under the trade mark 'NAFION' and which are based upon hydrolysed copolymers of perfluorinated hydrocarbons (for example polytetrafluoroethylene) and fluorosulphonated perfluorovinyl ethers. Such membranes are described for example in US Patent Nos 2 636 851;
3 017 338; 3 496 077; 3 560 568; 2 967 807; 3 282 875 and UK Patent No 1 184 321.
The active sites in the molecular structure of the resins from which these membranes are made are provided by the fluorosulphonated perfluorovinyl ether component. These sites are present on side chains attached by an ether linkage to the skeletal structure of the resin.
However such membranes have a limited operating life at high caustic concentrations because of water up-take producing swelling and degradation of the membrane.
This water uptake is related to the number and type of active sites in the molecular structure.
The membranes could be improved by the replace-ment of the active sites by ones havinghigher individual capacities, for example, replacement by dicarboxylic acid sites which have double the capacity of the sulphonic acid sites.
The preparation of cation exchange membranes containing dicarboxylic acid groups is described in Plasticheskie Massy 1976, 1, p 49. In this paper it is alleged that they are made by the graft copolymerisation (sic) of, for example, a mixture of maleic acid and styrene with a copolymer of hexafluoropropylene and vinylidene fluoride which copolymer provides the skeletal structure. The graft copolymerisation is effected by a radical-type initiator such as benzoyl peroxide. The ~ ~5'~ ~L9~

reaction conditions described would indicate that rather than graft copolymerisation (as defined in "Organic Chemistry of Synthetic High Polymers" by R W Lenz Interscience Publishers 1967 page 251) taking place in fact an inter-penetrating polymer network (IPPN) is more likely to be formed. However, even if graft polymeri-sation does occur under the stated conditions, because the reaction is radical initiated, the molecular structure of the skeletal backbone on to which the graft-ing occurs has to contain hydrogen atoms or double bonds.
It is advantageous for the skeletal structureo~ cation exchange resins which are to be used in mem-branes in electrolytic cells to be free of hydrogen atoms and double bonds and to be fully halogenated, ie perhalogenated, because these are the most stable resins under the rigorous operating conditions of an electro-lytic cell. Heretofore it has not been possible to pre-pare cationic ion exchange resins, suitable for use as membranes, which comprise a skeletal structure of a per-halogenated fluorine-containing hydrocarbon polymer and~ as active side chains, chains containing dicarboxylic acid groups.
We have now found a process for preparing resins in which the perhalogenated skeletal structure does not contain any active groups, its function being to provide a polymeric skeletal substrate to which active side chains containing dicarboxylic acia groups and/or their derivatives are attached. Heretofore an ion exchange resin with a support str1~cture of a perhalogenated fluorine containing hydrocarbon polymer with dicarboxylic acid groups present to provide the active exchange sites has not heen known.
Accordingly the present invention provides a novel cation exchange resin having a molecular structure comprising an inactive, as hereinafter defined, per-halogenated fluorine-containing hydrocarbon polymeric skeletal substrate with at least one attached active, as hereinafter defined, pendant side chain, said side chain comprising at least one active group derived from un-saturated dicarboxylic acids or derivatives thereof andat least one vinyl group derived from a vinyl monomer wherein said side chain is linked to the said substrate by at leas~ one said vinyl group and wherein the molar ratio of said active groups to vinyl groups in said side chain is in the range of 1:1 to 1:20.
Preferably the molar ratio of the active groups to vinyl groups is in the range of 1:1 to 1:3.
By 'inactive' in the context of the description ~f the substrate we mean that the polymeric substrate structure does not contain any ion exchange groups.
This has the advantage that the substrate possesses the desirable physical properties of stability and low water uptake typical of an unsubstituted fluorine containing hydrocarbon homopolymer.
By 'active' in the context of the description of the side chains we mean that the side chains contain groups which have, or can be converted to those having, cation exchange properties, in particular we refer to dicarbo~ylic acids and derivatives thereof.
The perhalogenated polymeric substrate may be perfluorinated or partly fluorinated. The preferred fluorine containing hydrocarbon substrate is a homo-polymer or copolymer of fluorinated ethylene, especially a homopolymer or copolymer of tetrafluoroethylene or chlorotrifluoroethylene.
The side chains in the molecular structure of the resins of the present invention comprise active and linking vinyl groups.
The active groups are those represented by the ~ 1 5gi ~

general formula:

X' X"
-- C -- C --COOH COOH

Where X' and X" may be the same or different and they represent hydrogen, fluorine, chlorine, alkyl group, halogenated alkyl group or a double bond.
Such groups are derived from monomers such as amides, anhydrides, acids, esters and salts.
The active groups are preferably derived from monomers such as maleic anhydride, 1,2-difluoromaleic anhydride and acetylenedicarboxylic acid and their derivatives.
. The linking groups used in the products of the invention are those derived from both aliphatic and aromatic vinyl monomers. Suitable aliphatic vinyl monomers are, for example, those having the following general formula CX2 = CXY
whilst suitable aromatic monomers are, for example, those having the following general formula CX=CXY

i i~91~

Where in the aforementioned aliphatic and aromatic monomers X = hydroyen or fluorine Y = hydrogen, fluorine or chlorine Z = hydrogen, alkyl, alkene, halogenated alkyl or halogenated alkene group The preferred monomers to provide the linking groups are styrene and its halogenated derivatives, such as ~ trifluorostyrene; divinylbenzene and its halogenated derivatives, such as ~ ' ,e~
hexafluoxodivinylbenzene; and ethylene and its halogena-ted derivatives such as tetrafluoroethylene.
Further suitable aromatic vinyl monomers are analogues of the aforesaid monomers having halogen atoms and/or functional groups, such as sulphonate and mono-carboxylic groups, attached to the aromatic ring.
The molecular structures of one type of the side chains of the resins of the present invention may be represented diagrammatically as follows (perhalogenated hydro-(L)a carbon polymer substrate) (A)b I
_ ( I ) C_ d X

When L - linking vinyl group A = active group X = polymer chain terminating group or fluorinated hydrocarbon polymer substrate 1 15919~

a = on~ or more b = one or more c = zero, one or more d = one or more It will be appreciated that this representa-tion does not cover all the possible configurations of the side chains of the resins of the present invention, for example it is also intended that the scope of the invention shall include side chains having branched con-figurations, and/or having ordered or random distribution of the linking and active groups and/or having more than one type of active group and/or-having more than one type of linking group. It is characteristic of all t~e side chains that they are linked to the substrate by at least one of their constituent vinyl groups.
The function of the linking vinyl group is to provide the means whereby the active groups may be linked by a graft copolymerisation with the perhalogenated, fluorine-containing hydrocarbon polymeric material which comprises the skeletal substrate. We have found that this graft copolymerisation can be effected by radiation grafting.
This novel process of radiation graft co-polymerisation of an active group and a substrate com-prising a halogenated hydrocarbon polymer with a linkinggroup is also applicable to resins comprising partly halogenated fluorine-containing hydrocarbon skeletal substrates. Such partly halogenated substrates may suitably comprise fluorinated olefin/olefin copolymers, preferably fluorinated ethylenP/ethylene copolymers, and especially copolymers of tetrafluoroethylene ana ethylene, or of chlorotrifluoroethylene and ethylene; an example of this copolymer is 'HALAR', the trade name for a 1:1 copolymer of chlorotrifluoroethylene and ethyle~e manu-factured and sold by Allied Chemical Corporation.

Thus we have now found that if a first monomeric material, rom which a dicarboxylic acid active group may be derived, and a second monomeric material capable of being graft copolymerised with the active S group monomer and with a fluorine containing hydrocarbon polymer, are all three together subjected to a radiation grafting process, the second monomeric material will link to the polymer and the first monomer to form a cation exchange resin having a fluorine containing hydro-carbon polymeric skeletal substrate with pendant sidechains containing dicarboxylic acid ion exchange groups.
Accordingly the present invention also provides a process for the preparation of a cation exchange resin comprising a fluorine containing hydrocarbon polymeric skeletal substrate with at least one active side chain containing at least one ion exchange group derived from a dicarboxylic acid or a derivative thereof in which process a mixture of a vinyl monomeric material and an active monomeric material capable of providing said ion exchange groups is subjected to irradiation in the presence of a material comprising a fluorine containing hydrocarbon polymeric skeletal substrate so that part of the said vinyl monomeric material is grafted to the said substrate and so that copolymerisation of the vinyl monomeric material and the active monomeric material takes place to form a product having at least one pendant sidechain on the said substrate.
In the process of the invention the vinyl monomeric material and the active monomeric material are mixed in proportions such that the molar ratio of the monomers present is in the range of 20:1 to 1:9 res-pectively. Preferably the molar ratio is in the range of 4:1 to 1:2 and, more preferably, in order to obtain the preferred resins of this invention, the monomeric materials are mixed in approximately equimolar 1 1 5~ 99 proportions, (ie in the range 1.1:1.0 to 1.0:1.1).
The mixture of monomeric materials has to be in a liquid form and, if necessary, a common solvent is used to prepare a solution of them. Commonly one of the monomeric materials itself will provide the liquid ~hase dissolving the other monomeric material. Alte~natively, with advantage, the solvent used is one which will penetrate the substrate material and cause it to swell, thereby allowing the solution of monomers to be absorbed right through the substrate material. Suitable solvents are, for example, toluene and xylene. It is also within the scope of this invention for the substrate material to be pre-swelled with such solvents prior to the addîtion of the monomers, the advantage of this procedure being that minimum ~uantities of solvent are used.
Any of the known methods of radiation grafting may be employed. For example, the substrate and monomeric materials may be subjected together to con-tinuous or intermittent radiation, or the substrate may be pre-irradiated prior to bringing it into contact with the monomeric materials. Preferably the substrate and monomeric materials are irradiated together; the sub-strate, which is a solid and may be in the for~ o~ fine particles or as a sheet or film, is immersed in the liquid phase containing the mixed monomeric materials and the whole subjected to irradiation by y-rays, or X-rays, or electron beam; preferably by y-rays.
It is essential for the process of the invention that both the linking monomeric material and the active monomeric material are present together during the grafting process so that the free radicals generatea by the radiation may initiate both the grafting of link-ing groups to the substrate and, concurrently, the co-polymerisation of the linking and active monomeric materials to form the active chains which characterise the resins of the present invention. Preferably the grafting process is carried out in the absence of oxygen.
In those cases where a derivative of the active monomer is employed in the grafting process, eg maleic anhydride, subsequent chemical treatment such as hydrolysis is re~uired to render the dicarboxylate derivative into the active acid form.
It lies within the scope of our invention to prepare cation exchange resins by using the process of our invention whereby dicarboxylic-acid-containing side chàins are grafted onto a fluorine containing hydrocarbon polymeric skeletal substrate to which other active side chains, for example side chains conta}ning sulphonic acid or monocarboxylic acid groups, are already attached. For example, the process of our invention may be applied to '~AFIONI to give a cation exchange resin having both sulphonate group-containing side chains and dicarboxylic acid group-containg side chains.
Italso lies within the scope of our invention to introduce further active groups to the resins, as hereinbefore defined, comprising a substrate, linking groups and active groups. The additional active groups are introduced by chemical modification of the groups already present. Thus, for example, the linking groups in the side chains may be sulphonated and/or carboxylated to give active resins having an enhanced capacity.
Ion-exchange resins, according to the present invention, have enhanced properties particularly as regards resistance to degradation by water uptake during use. This is obviously of importance when they are used for their titular purpose, but they find particular application in the form of films as perm-selective membranes in electrolysis cells.
These membranes may be fabricated from particles ~ 1 59 1 99 of resins of the present invention, or preferably a perhalogenated fluorine-containing hydrocarbon polymeric ~ilm is made which is then subjected to the process of the present invention to form a resin of the present in-vention in the form of a membrane.
Accordingly, in an embodiment of the presentinvention, there is provided a perm-selective membrane, suitable for use in electrolysis cells, which comprises a resin having cation exchange properties, wherein the said resin is made by irradiation induced grafting of linking vinyl groups, as hereinbefore defined, to a substrate comprising a perhalogenated fluorine-containing hydrocarbon polymer and concurrently forming copolymers of vinyl groups and active groups, as hereinbefore defined, thereby forming a resin having a molecular structure consisting of a perhalogenated fluorine-containing hydrocarbon polymeric substrate with side chains of said copolymers, said side chains comprising at least one active group derived from unsaturated di-carboxylic acids or derivatives thereof and at least onevinyl group, said active groups and vinyl groups being in a molar ratio in the range of 1:1 to 1:20.
Preferably said active groups and vinyl groups are present in the side chains in a molar ratio in the range of 1:1 to 1:~.
The membranes according to this embodiment of the invention may be made by forming a film, by any known suitable film forming process, eg compression"from particles of the cation exchange resin, or alternatively and preferably the perhalogenated fluorine-containing hydrocarbon polymeric substrate material is formed first into a film. This film is then subjected to the grafting process which renders it suitable for use as a membrane in an electrolytic cell.
Such membranes have a lower water uptake and have ~ 159199 a higher degradation resis-tance than conventional mem-branes of similar performance characteristics.
The membranes according to this invention may also be usefully employed in other electrochemical systems, for example, as separators and/or solid electrolytes in batteries, fuel cells and electrolysis cells.

i 159 199 The invention is now ilLustrated by, but not limited to, the following examples in which all ion exchange capacities are those relating to highly alkaline conditions, ie both carboxylic acid groups acting as exchange sites.

100 gra~s of commercially available "KEL-F"
powder (registered Trade Mark for the homopolymer of chlorotrifluoroethylene), free of additives and having a particles size about +150 mesh, were suspended in monochlorobenzene (300 ml), containing also 10.0 g (0.096 moles~ of styrene and 9.4 g (0.096 moles) of maleic anhydride, in a reaction vessel fitted with stirring means, heating means, gas inlet and outlet ports and condensing means. The suspension was sub-jected to gamma radiation. Before and during the gamma radiation a stream of nitrogen gas was bubbled through the contents of the vessel. The contents of the vessel were heated to 52.5C under continuous agitation and subjected to gamma radiation for a total of 4.5 hrs at a dose rate of 250 krad/hr. The radiated mixture re-ceived the total dose of 1125 krad, after which the radiation, heating and stirring ceased. The grafted resin powder was quantitatively transferred to a washing column and washed free from unreacted monomers, solvent and unwanted byproducts. Finally the resin was converted into the acid form and dried in vacuum oven at 60C.
The percentage graft, which is calculated by expressing the weight increase of the resin as a per-centage of the weight of grafted resin produced, was2.25%. The ion exchange capacity was determined by titration to be 0.18 meq/g. Assuming equimolar proportions of the groups derived from the styrene and from the maleic anhydride monomers in the polymeric side chains grafted onto the "KEL-F" skeleton, the theoretical ~ 1591 99 ion exchange capac:ity of a resin with a 2.25% graft would be 0.20 meq/g. Examination of the infra-red spectrum of the product had shown the presence of di-carboxylic acid and styrene in the molecular structure of the resin.

Graft copolymers of styrene-maleic anhydride to "KEL-F" powder, according to the present invention, were.
made by the method described in Example 1, except that different total monomer concentrations (keeping the molar ratios of monomers constant) were used to produce various levels of grafts, resulting in various exchange capac-ities of the grafted product resin as shown in Table 1.

_ ` _ Example 2 3 4 5 Concentration.of monomers.
in monochlorobenzene Styrene g/l 21.0 53.3126.6 286.6 .
Maleic anhydride g/l 19.750.7 120.0 266.6 Percentage graft % 1.25 3.125.06 8.01 Theoretical ion exchange capacity meq/g 0.11 0.280.44 0.67 Measured ion exchange capacity meq/g 0.09 n.dØ40 n d.

~ 15~)199 Infra-red analysis confirmed that presence of dicarboxylic acid and styrene in the molecular structure of the gra~ted resin products.

These examples illustrate the products of the present invention having a different fluorine containing hydrocarbon polymer substrate to those of examples 1 to 5. In these examples styrene and maleic anhydride were graft copolymerised by the process according to the invention, using the conditions described in example 1, to "FLUON" powder, which is a homopolymer of tetrafluoro-ethylene ~"FLUON" is a trade mark of Imperial Chemical Industries Ltd). The percentage-grafts and ion-exchange capacities of the product resins in their acid form obtained using various monomer concentrations are given in Table 2.

Example 6 7 8 Concentration of monomers in monochiorobenzene styrene g/l 21.0 33.7143.3 maleic anhydride g/l 19.7 31.7135.0 Percentage graft % 0.75 1~223.12 Theoretical ion exchange capacity meq/g 0.Q6 o.ll0.28 Measured ion exchange capacity meq/g n.d. 0.~8n.d.

Infra-red analysis confirmed the presence of ~ 15gl'39 dicarboxylic acid and styrene in the molecular structure of the grafted resin products.
EXAMPI,ES 9 T0 12 Treatment of samples of products from some of the previous examples by a known process for substituting sulphonate groups into the styrene groups produced sulphonated resins having ion-exchange capacities given in table 3.

Ion-exchange capacity meq/g Example Sulphonated .
No product from _ __ _ theoretical measured . _ _ . . ...
9 example 1 0.31 0O26 ~ 2 0.17 0.13 11 .. 4 0.64 0.52 12 .. 7 0.17 0.13 .

The ion-exchange capacities of these sulphonated resins were all greater than their non-sulphonated analogues.

These examples illustrate the application of the process of the present invention to the gra~t copolymeri-sation of styrene and maleic anhydride to films of fluorine containing hydrocarbon polymeric materials to give products of the invention in a form which makes them suitable for use as perm selective membranes in electrolysis cells.
The mixture of monomers dissolved in toluene in the concentrations indicated in table 4 in the presence ~ 159199 of films of various fluorine containing polymers were subjected to a total gamma radiation dose of 1000 krad over four hours 300 ml of monomer solution were used to treat 10 g of film. The grafted films were washed to remove any residual monomers, solvent and side products and converted into the acid form. The ion-exchange capacities of the films so produced are given in table 4.

Example No 13 14 15 ~ 16 17 ¦ 18 .. _._ . _ Substrate film material PTFE* "KEL-F" "NllF~ ON" "N390~ ~N"

Concentration of monomers in toluene styrene g/l 36.7 36.7 36.790.0 36.7 90.0 maleic .
anhydride g/l 35.0 35.0 35.085.0 35.0 85.0 Percentage graft ~ 1.10 1.75 2.50 4.80 1.60 4.10 Theoretical .
ion exchange .
capacity meq/g 0.09 0 16 l.OZ 1.22 0.75 0.97 * PTFE = poly-(tetrafluoroethylene) The "NAFION" 110 and "NAFION" 390 films, which are known perm-selective membranes, used as substra~es had ion-exchange capacities of 0.79 meq/g and 0.60 meq/g ~ 159 199 respectively. I~ all cases the addition of further active side chains by yraft copolymerisation with styrene and maleic anhydride monomers improved the ion-exchange capacities of the "NAFION" films used.
EX~MPLES 19 TO 24 Samples of the grafted films prepared in examples 13 to 18 were sulphonated, thereby further enhancing their ion-exchange capacities as indicated in table 5.

Ion-exchange capacity me~/g Example Sulphonated No product from theoretical measured .
19 example 13 0.15 o.ll " 14 0.25 0.19 21 " 15 1.13 1.05 22 1~ 16 1.43 1.31 23 " 17 0.82 0.7g 24 " 18 1.15 1.0 100 grams of "KEL-F" powder similar to that used in Example 1 were suspended in 300 ml of a solution of maleic anhydride and tetrafluoroethylene in toluene. The solution contained 0.7 g/kg of maleic anhydride and 0.7 g/kg of tetrafluoroethylene.
The suspension was frozen by immersing its container in liquid nitrogen. It was degassed and allowed to regain room temperature. The degassing procedure was repeated three times and the container sealed.
The solution in the sealed container was heated ~ 1 5 ~

to 70C and held at that temperature for 24 hours. The container and its contents were sub]ected to y-radiation for a total of 50 hours at a dose rate of 100 krad~hr.
After irradiation the container was again immersed in liquid ni-trogen, a necessary precaution with tetrafluoethylene, to freeze the suspension before the container was opened. The powder was washed free of unreacted monomers and ungrafted homopolymer. It was found that 20% graft had taken place. The powder was pressed to form a membrane which was then hydrolysed.
The ion exchange capacity of the hydrolysed membrane was determined to be 0.64 meq/g. On the basis of the percentage graft and the ion exchange capacity it was calculated that the molar ratio of active to vinyl groups in the side chains grafted on the "KEL-F"
substrate was approximately 1:3.

In this example, the advantage of using a swelling solvent is demonstrated.
4 grams of "KEL-F" powder similar to that used in Example 1 were immersed in hot xylene. The powder swelled and absorbed an amount of xylene equal to approximately 7% of its own weight. Excess xylene was removed. An equimolar mixture of styrene and maleic anhydride was added to the swollen powder. After 12 hours the excess liquid phase was decanted off and the swollen powder with absorbed monomers was irradiated under nitrogen with radiation at a level of 80 krad/hour for 24 hours.
After removal of any homopolymer formed and of any unreacted monomers, the powder was hydrolysed.
The ion exchange capacity of the resin was determinçd to be 1.1 meq/g~

~ 1 59 :~99 A portion of the resin was pressed into a film and hydrolysed in 30% w/w sodium hydroxide solution overnight. The film was then placed in a small jacketed electrolytic cell fitted with platinum electrodes. The anode side of the cell was filled with concentrated sodium chloride brine and the cathode side with 30~ w/w sodium hydroxide solution. ~lectrolysis at 90C and a current density of 1.6 kA/m2 produced ch~orine at the anoce and hy-G~ogen and sodl~-Lt.lydroxide at the cathode.

A piece of film consisting of a copolymer of tetrafluoethylene and hexafluoropropylene (FEP) (250 microns thick, 2.8 g) was soa~ed in a solution of maleic anhydride (20 g), styrene (250 g) and carbon tetrachloride (250 g) with quinol (2.0 g). The mixture was heated at 60C for 4 hrs, then irradiated at room temperature for 10 hrs at a dose-rate of 100 krad/hr.
After irradiation the contents were kept at 60C for another 6 hrs with vigorous stirring. Then the film was taken out and washed f~ree of unreacted monomers and co-polymers and dried to constant weight. By the weight increase it was calculated that there had been a 12%
graft.
The treated FEP film was hydrolysed in 30%
w/w sodium hydroxide solution at 90C for 60 hrs and the ion exchange capacity was determined to be 0.85 meq/g from which it was calculated that the molar ratio of groups derived from maleic anhydride and from styrene was 2:3.
The film was tested in a small electrolytic cell in the manner described in example 26. The current efficiency determined by measuring the chlorine evolved was found to be 76% (weight of chlorine evolved expressed . ..

~ 159:~99 as a percentage of the theoretical weight of chlorine equivalent to the current passed) which compares favour-ably with that obtained usin~ a 'NAFION' membrane under the sarne conditions which was 50~.

Claims

What we claim is: - 23 -

1. A cation exchange resin having a molecular structure comprising a perhalogenated, fluorine-containing hydrocarbon polymeric skeletal substrate which contains no ion exchange group but has attached to it at least one pendant side chain which contains at least one active group having cation exchange properties derived from an unsaturated dicarboxylic acid or a derivative thereof and which said side chain also contains at least one vinyl group derived from a vinyl monomer wherein the said side chain is linked to the said substrate by at least one said vinyl group and wherein the molar ratio of said active groups to vinyl groups in the said side chain is in the range of 1:1 to 1:20.

2. A cation exchange resin according to claim 1 wherein the molar ratio of the active groups to the vinyl groups in the side chain is in the range 1:1 to 1:3.

3. A cation exchange resin according to claim 1 wherein the perhalogenated fluorine-containing hydro-carbon polymeric substrate is perfluorinated.

4. A cation exchange resin according to claim 3 wherein the perhalogenated fluorine-containing hydro-carbon polymeric substrate is poly-(tetrafluoroethylene).

5. A cation exchange resin according to claim 1 wherein the perhalogenated fluorine-containing hydro-carbon polymeric substrate also contains chlorine.

6. A cation exchange resin according to claim 5 wherein the perhalogenated fluorine-containing hydro-carbon polymeric substrate is a homopolymer of chlorotrifluoroethylene.

7. A cation exchange resin according to claim 1 wherein the active group is a dicarboxylic acid, or a derivative thereof group, having a general formula represented by where X' and X" are independently selected from the group consisting of hydrogen, fluorine, chlorine,an alkyl group and a halogenated alkyl group.

8. A cation exchange resin according to claim 1 wherein the active group is

9. A cation exchange resin according to claim 1 wherein the said vinyl group is derived from an aliphatic vinyl monomer.

10. A cation exchange resin according to claim 9 wherein the vinyl group is derived from a monomer selected from the group of monomers having the general formula a CX2 = CXY

where X is hydrogen or fluorine;
and Y is hydrogen, fluorine or chlorine.

11. A cation exchange resin according to claim 10 wherein the vinyl group is derived from tetrafluoroethylene.

12. A cation exchange resin according to claim 1 wherein the said vinyl group is derived from an aromatic vinyl monomer.

13. A cation exchange resin according to claim 12 wherein the vinyl group is derived from a monomer selected from the group of monomers having the general formula of where X is hydrogen or fluorine Y is hydrogen or fluorine or chlorine Z is hydrogen, alkyl, alkene, halogenated alkyl or halogenated alkene group.

14. A process for the preparation of a cation exchange resin comprising a fluorine-containing hydro-carbon polymeric skeletal substrate with at least one active side chain containing at least one ion exchange group derived from a dicarboxylic acid or a derivative thereof in which process a mixture of a vinyl monomeric material and an active monomeric material capable of providing said ion exchange groups is subjected to irradiation in the presence of a material comprising a fluorine-containing hydrocarbon polymeric skeletal substrate so that part of the said vinyl monomeric material is grafted to the said substrate and so that copolymerisation of the vinyl monomeric material and the active monomeric material takes place to form a product having at least one pendant side chain on the said substrate.

15. A process according to claim 14 wherein the said mixture of monomeric materials consists of vinyl monomeric material and active monomeric material in proportions such that the molecular ratio of vinyl monomer to active monomer is in the range of 20:1 to 1:9.

16. A process according to claim 14 wherein the molecular ratio of vinyl monomer to active monomer is in the range of 4:1 to 1:2.

17. A process according to claim 14 wherein the molecular ratio of monomers in the monomeric mixture is in the range of 1.1:1.0 to 1.0:1.1.

18. A process according to claim 14 wherein the material comprising the said substrate and the said mixture of monomers are subjected together to irradiation by any one form of radiation selected from the group consisting of .gamma.-rays, X-rays and electron beams.

19. A process according to claim 14 wherein the said fluorine-containing hydrocarbon polymeric skeletal substrate is perhalogenated.

20. A process according to claim 14 wherein the said substrate is a fluorinated olefin/olefin copolymer.

21. A process according to claim 20 wherein the said substrate is a copolymer of ethylene and a fluorinated olefin selected from the group of fluorinated ethylenes consisting of tetrafluoroethylene and chloro-trifluoroethylene.

22. A process according to claim 14 wherein the said mixture of monomers is dissolved in a solvent capable of swelling the said material comprising a fluorine-containing hydrocarbon polymeric skeletal substrate.

23. A perm-selective membrane, suitable for use in electrolysis cells, which comprises a cation exchange resin according to claim 1.

24. A process of making a perm-selective membrane according to claim 23, in which process the said cation exchange resin is subjected to compression so as to form it into a thin membrane.

25. A process of making a perm-selective membrane according to claim 23, in which process a film comprising a perhalogenated fluorine-containing hydrocarbon polymeric substrate is impregnated with a mixture of a vinyl monomeric material and an active monomeric material containing ion exchange groups derived from dicarboxylic acid and said impregnated film is then subjected to irradiation so that the monomers in the said mixture are graft copolymerised to the said substrate to form active side chains on the said substrate.