CA1137246A - Basic cross-linked polymers - Google Patents

Abstract

ABSTRACT OF THE DISCLOSURE
A basic copolymer whose main chain is cross-linked which comprises about 6 to about 98 % by weight of recurring units of Formula (A) or (B), (A) or

Description

~L137246 This invention relates to a novel basic cross-linked copolymer having substituted aminoethyl groups and a process ~or the production thereof.
Various cross-linked copolymers having substituted aminomethyl groups are known. Of these cross-linked copolymers, weakly basic anion ion-exchange resins having dialkylaminomethyl groups and strongly basic anion ion-exchange resins having trialkylammonium methyl groups (Rl R2 R2 ~CH2- : Rl, R2~ R3, each being an alkyl group) are representat-ive ones and it might be said that almost all the commercially a~ailable anion exchange resins are of these types. The conventionally known representative method of preparing these resins comprises reacting a starting polymer such as a divinylben~ene-styrene copolymer with chloro-methyl methyl ether in the presence of a Friedel-Crafts catalyst to produce a chloromethylated polymer and aminating the chloromethylated polymer with a dialkylamine or a trialkylamine. However, according to this method, cross-linking reaction often occurs as a side reaction in the chloromethylation to disadvantageously increase the degree of cross-linking and to reduce the exchange capacity. With high degrees o~f cross-linking the subsequent amination does not complete. Furthermore, the harm of haloalkyl ethers such as chloromethyl methyl ether is recently at issue.
According to the present invention there is provided a basic copolymer whose main chain is cross~linked which comprises about 6 % to .

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about 98 % by weight of recurring units o Formula (A) or (B), r~ \ R2 CH2 - CH- ~ (A) or CH2 - CH2 - ~R2 2 ~ R3 (B) wherein Rl, R2, R3, which may be the same or different, each represents a hydrogen atom or a hydrocarbon group selected from the group consisting of Cl 20 alkyl groups, C3 10 cycloalkyl . groups, C3_8 alkenyl groups, C6_15 aryl groups, C7_12 arylalkyl groups and Cl_l5 aminoalkyl groups; and X represents an acid radical, - and about 2 % to about 94 % by weight of cross-linked units based on the total weigh~ of the recurring units of Formula (A) or (B) and the cross-linked units, and a process for the~production thereof~
Specific examples of suitable Rl, R2 and R3 groups in Formulae : (A) and (B) as described above include hydrogen atom; Cl 20 alkyl groups such as methyl, ethyl7 n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl~
tert-butyl, n-pentyl, isopentyl, n-hexyl, n-heptyl, n-octyl, 2-ethylhexyl, ~3~4~

n-nonyl, n-decyl, n-dodecyl, n-tetradecyl, n-hexadecyl and n-octadecyl;
C3 lO cycloalkyl groups such as cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl; C3 8 alkenyl groups such as allyl, croty~ ~nd hexenyl;.C6_15 aryl.groups.such.as phenyl,.toluyl, trimethylphenyl, diethylphenyl, naphthyl and blphenyl; C7 12 arylalkyl groups such as benzyl, a-phenethyl, ~-phenethyl, y-phenethyl and phenyl-tert-butyl; and Cl 15 aminoalk~l groups such as aminoethyl, aminopropyl, aminohexyl and aminododecyl. Of these hydrocarbons, the Cl 20 alkyl groups and the Cl 15 aminoalkyl groups are preferred from their ease in the preparation of the starting monomeric materials. When the Cl 20 alkyl groups are employed, the nitrogen content per unit weight of the copolymer is preferably more increased with reduced numbers of carbon atoms. Thus, it is more preferred to employ Cl 8 alkyl groups and Cl 8 aminoalkyl groups. Preferred combinations of the Rl and R2 groups in Formulae (A) and (B) include Rl = CH3 and R2 = CH3; Rl = C2H5 and 2 2 5 1 2 C2H5; Rl = H and R2 = n-C3H7 or iso-C H ;

1 2 Y 6 11; and Rl = CH2CH2NH2 and R2 = CH CH NH
The combinations of Rl ~ R2 = H; and Rl = H and R2 = CH3 have dlfficulty in the preparation of starting monomeric materials. The copolymers where the -CH2 - CH - group is in the para position to the -CH2 - CH2 ~ ~-R
group or the -CH2 - CH2 - ~ Rl group have such advantages that the preparation of the starting monomeric materials are easy and various functions originating from the nitrogen atom can be fully exhibited due to the reduced steric hindrance of the nitrogen affected in the copolymers.
The X group in Formula (B) represents a so-called acid radical.

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Specific examples of suitable X groups include halogen atoms such as F, CQ, Br and I; i~organic anions such as 1/2S04, 1/2S03, HS04, N03, N02, 1/2CrO4, SCN, CQo4, OH, H2P04, 1/2HP04, 1/3P03, HC03, 1/2C03, CN and MnO4; carboxylate anions of R4COO wherein R4 is a Cl 20 alkyl group, a C6_15 aryl group, a Cl_10 haloalkyl group or a Cl 10 hydroxyalkyl group, such as HCOO, CH3COO, C2H5COO, CH3(CH2)8COO, C 3( 2)16 6 5 CH3C6H5COO, CH2CQCOO, CH2FCOO and CH3CH(OH)COO; sulfonate anions of R5S03 wherein R5 is a methyl group, an ethyl group or a C6 20 aryl group, such as CH SO , C H5S03~ C6H5S03, CH3C6H4S03 and C12H25C6 4 3;
ester anions such as CH30S03 and C2H50S03.
The shape or form of the copolymers of this invention is not particularly limited, and the copolymers may be in the form of a mass, a pulverized particle, a spherical particle or a membrane. When the copolymers of this invention are packed in a column and used as ion exchange resins or adsorbents, spherical particles are preferred for practical purposes.
The copolymers of this invention can be produced by~polymeri7ing a monomer mixture comprising about 6 % to about 98 % by weight of a monomer of Formula (C~, / 1 .
~ CH2 ~ CH2 - N \

CH2 = CH ~ ~ : (C) wherein Rl and R2 are the same as defined above, and about 2 % to about 94 % by weight of a cross-linkable monomer having .:
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1~372~i a plurality of vinyl groups based on the total weight of the monomer of Formula (C) and the cross-linkable monomer. A preferred amount of the monomer of Formula (C) ranges from about 10 % to about 90 % by weight based on the total weight of the monomer of Formula (C) and the cross-linkable monomer. A more preferred amount ranges from about 20 X to abou~ 80 % by weight based on the total weight of the monomer of Formula (C) and the cross-linkable monomer.
The monomer of Formula tC) can be produced by reacting an amine of the Formula (D), R~
\ NH (D) ~2 wherein Rl and R2 may be the same or different and each represents a hydrogen atom or a hydrocarbon group selected from the group consisting of Cl 20 alkyl groups, C3_10 cycloalkyl groups, C3 8 alkenyl groups, C6 15 aryl groups, C7 12 arylalkyl groups and Cl 15 aminoalkyl groups, with divinylbenzene in the presence of an alkali meta~l amide of Formula (E), lj .
NM (E) wherein Rl and R2 are the same as defined above and M
represents an alkali metal.

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The divinylbenzene employed may be the para-, meta- or ortho-isomer of divinylbenzene and of these isomers, p-divinylbenzene is preferred due to the high reactivity.
When the number o carbon atoms in Rl and R2 is too large, the molecular weight of the product becomes higher and as a result, the separation of the product by distlllation or other methods becomes difficult. Ammonia (Rl = R2 = H) and methylamine (one of Rl and R2 = H, the other = CH3) may be employsd but their reactivity is remarkably low and the amount of the monomer of Formula (C) obtained is disadvantageously too small.
Examples of suitable amines of Formula (D) include ethylamine, n-propylamine, isopropylamine, n butylamine, sec-butylamine, ter~-butylamine, n-pentylamine, isopentylamine, n-hexylamine, n-heptylamine, 2-ethylhexyl-amine, n-nonylamine, n-decylamine, n-dodecylamine, n~tetradecylamine, n-hexadecylamine, n-octadecylamine, dimethylamine, diethylamine, di-n-propylamine, di-n-butylamine, dl-n-octylamine, cyclohexylamine, cyclopentylamine, dicyclopropylamine, dicyclohexylamine, allylamine, diallylamine, crotylamine, benzylamine, phenethylamine, aniline, N-methylaniline, ethylenediamine~ hexamethylenediamlne, diethylenetriamine~
N-methylethyIenediamine and ~-ethylethylenediamine.
The alkali metals represented by M~employed include lithium, sodium and potassium. Of these alkali metals, lithlum is preferred due to its high reactivity and easy reaction operation.
The lithium amide which can be preferably~employed in the preparation of the monomer of Formula (C) can be prepared by reacting an : ~ . :: : . . . : ~:

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amlne of the formula (D) with a Cl 20 allcyllithium, phenyllithium, lithium ~ydride or lithium aluminum hydride. Of these lithium compounds, the Cl 20 allcyllithium is especially preferred due to its high solubility in a solvent and ease in handling.
Examples of suitable alkyllithi~s which may be employed include methyllit~ium1 ethyllithlum, n butyllithium~ n-octyllithium and the like.
Of these alkyllithiums, commercially produced n-butyllithium is especially preferred and from the standpoint of availability.
The lithium amide o~ Formula (E) has catalytic activity which is one of the characteristic features of the preparation of the monomer of Formula (C).
More specifically, the lithium amide of Formula ~E) is requlred to be used in an amount of less than equimolar amount of divinylbenzene, preferably from about 0.001 to about O.S mole and more preferably from about 0.01 to about 0.2 mole per mole of divinylbenzene.
Since the lithium amide of Formula (E) is deactivated by the reaction with a compound having an active hydrogen such as water, an alcohol or an acid present in the reaction system, it is preferred that the starting material an~ the solvent used are previously purified.
~ut when =uch compounds having an active hydrogen cannot be removed but remain in the reaction mixture, it is preferred to use the lithium amide of Formula (E) in an amount grea-ter than required.
The amine of Formula (D) undergoes stolchiometric reac-tion with divinylbenzene and is preferably used in an amount of from about 0.3 to about 2.5 moles~ more preferably from about 0.6 to 1.3 moles per :: : : :

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mole of divinylbenzene. If the amount of the amine of Formula (D) is too small, the yield of the product is reduced. If an excess amount is used, there can be disadvantageously produced a by-product of the Formula (F), Rl /CH2 - CH2 - N \

\ N - CH - CH ~r~ 2 (F) wherein Rl and R2 are the same as defined above.
The by-product of Formula (F) can be more easily produced with m-divinylbenzene is employed than with p-divinylbenzene.
The reaction of a mixture of the lithium amide of Formula (~) and the amine of Formula (D) with divinylbenzene can be conducted by the following two methods. Cne method comprises adding a mixture of the lithium amide of Farmula (E) and the amine of Formula (D) to divinyl-benzene. This method has an advantage that formation of the by-product of Formula (F) can be suppressed. The other method comprises adding divinylbenzene to a mixture of the lithium amide of Formula (E) and the amine of Formula (D). In this case, it is only required to use one reaction vessel. Another advantage is that the moisture sensi~ive lithiu~
amide solution need not be transferred. Especially when ethylamine or dimethylamine is used as the amine of Formula (D), it is preferred to use the second method wherein divinylbenzene is added unde-s cooling to a mixture of lithium ethyl amide or lithium dimethyl~nide and ethylamine or dimethylamine which is gaseous at room temperature.

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The reaction of ~he present invention can also be conducted in the presence oE an inert solvent. Examples oE suitable solvents which can be employed include aliphatic hydrocarbons such as pentane, hexane, cyclohe~ane and octane; aromatic hydrocarbons such as benzene and toluene; ethers such as diethyl ether, dioxane and tetrahydrofuran, aprotic polar solvents such as dimethyl sulfoxide, N,N-dimethylformamide, and hexamethylphosphoric triamide; and other liquids which do not react with the lithium amide of Formula (E) under the reaction conditions.
Of these solvents, n~hexane, cyclohexane, benzene and tetrahydrofuran are preferred. In particular, ~hen tetrahydrofuran ls used, the rate of reaction is increased to shorten the reaction time. The aliphatic hydrocarbons such as n-hexane can be frequently used as completely inert solvents.
The amount of the solvent used typically ranges from about O.l to about 50 times and preferably about 0.5 to about 20 times the volume of divinylbenzene. If the amount of the solvent is increased 9 the reaction is generally retarded.
The reaction can be conducted at a temperature whi~h is not particularly limited, but typically at about -80C to about 150C, preferably at about -30C to about 100C and more preferably at about -20C to about 60C. When the reaction is performed at a temperature higher than the boiling point of the amine of Formula (D) or the solvent~
it is necessary to use a pressure reaction vessel. The reaction mixture is preferably subjected to stirring or shaking.
The reaction time which is not particularly limitea typically :~

~37Z~6 ranges from one minute to about 24 hours and preferably from about 5 minutes to about 8 hours. The rate oE reaction greatly depends ~Ipon the temperature selected, the amine of Formula ~D) employed, the concentration of the startin~ materlal and the solvent employed.
In order to terminate the reaction, it is convenient to deactivate the lithium compound with an alcohol such as ethanol or propanol or water. The monomer of Formula (C) which is the reaction product may be separated by distillation or column chromatography.
Alternatively, hydrochloric acid or hydrogen chloride gas may be added to the reaction mixture to effect precipitation of the monomex of Formula (C) as its hydrochloride. A more efficient isolation can also frequently be conducted by subjecting the reaction mixture to pretreatment with addition of water, followed by extraction.
The method of preparing diethylaminoethylstyrene [Rl = R2 = C2H5 in Formula (C)] is disclosed in "Makromolekulare Chemie", 177, 3255 -3263 (lg76), by Teiji Tsuruta et al.
The cross-linkable monomers which can be employed in this invention have a plurality of vinyl groups and preferably 2 to 4.
Examples of suitable cross-linkable monomers having a plurality of vinyl groups which can be employed in this invention include:
(i) Co~pounds of the formula, (CH2 = C~ 2--~--r 1 wherein Al is a C6 14 aromatic hydrocarbon radical, a pyridine nucleus or a quinoline nucleus, -~ -- 11 --. : :

~13~46 such as divinylbenzenes, divinyltoluenes, divinylxylenes, divinyl-naphthalenes, divinylethylbenzenes, trivinylbenzenes, divinylpyridines, divinylquinolines, etc.;
(ii) Compounds of the formula, (CH2 = CH-~-2~ A2 wherein 2 is Co-, -52- or _ ~ $ ~3 ~ ~ _ group wherein A3 is -O-, -NH-, -S-, -S02-, -SO- or -~-CH2-~ group wherein Q is zero or an integer of 1 to 4, such as divinyl ketone, divinyl sulfone, bisvinylphenyl ethers, divinyldiphenylamines, divinyldiphenyl sulfide, divinyldiphenyl sulfone, divinyldiphenyl sulfoxide, divinyldiphenyls, divinyldiphenylmethanes, diphenyldibenzyls, etc.;
~iii) Compounds of the formula, / H or CH3 H or CH3 CH = C C = CH2 C - NH - A - NH - C
Il 4 ll O O
wherein A4 is -~-CH2- ~ group wherein p is an integer of 1 to 6, such as N,N'-methylenebisacrylamide, N,N'-me-thylenebismethacrylamide, N,N-trimethylenebisacrylamide, N,Ni-trimethylenebismethacrylamide~
N,N-hexamethylenebisacrylamide and N,N-hexamethylenebisacrylamide, etc.;

, .

~37246 (iv) _ / H or CH3 CH = C
C - 0 -- _~ - A
O q wherein q is an integer of 2 to 4, A5 is a radical of a polyol having q terminal hydroxyl group and a number average molecular weight of at most 1000, such as ethyleneglycol di-acrylate or -methacrylate, diethyleneglycol di-acrylate or -methacrylate, triethyleneglycol di-acrylate or -methacrylate, tetraethyleneglycol di-acrylate or -methacrylaté, polyethyleneglycol (number average molecular weight: 200 to 1,000) di-acrylate or -methacrylate, propyleneglycol di-acrylate or -methacrylate, dipropylene glycol di-acrylate or -methacrylate, polypropyleneglycol (number average molecular weight: 100 to 1,000) di-acrylate or -methacrylate, butyleneglycol di-acrylate or -methacrylate, trimethylolethane tri-acrylate or -methacrylate, trimethylolpropane tri-acrylate or -methacrylate, pentaerythritol tetra-acrylate or -methacrylate, neopentylglycol di-acrylate or -methacryl te,:dibromoneopentyl glycol di-acry~ate or -methacrylate, 1,8-octanediol di-acrylate or -methacrylate~ l,9-nonanediol di-acrylate or -methacrylate, l,10-decanediol di-acrylate or -methacrylate~
1,12-dodecanediol di-acrylate or -methacrylate and 1~18-octadecanediol di-acrylate or -methacrylate, etc.;

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(v) Compounds of the formula, (CH2 = CH -- CH2-)-r ~6 wherein r is an integer o~ 2 or 3, A6 is a radical of a di- or tricarboxylic acid having 2 to 10 carbon atoms, such as diallyl oxalate, diallyl maleate, diallyl fumarate, diallyl adipate, diallyl phthalate, diallyl tartrate, triallyl tricarballylate, t~iallyl trlmellitate, triallyl trimesate, etc.; and (vi) Other cross-linkable monomers having a plurality of vinyl groups such as diallyl carbonate, triallyl phospha~e, triallyl isocyaurate, 1,3,5~triacryloylhexahydro-1~3,5-triazine, diallylmelamine, N-acroylacrylamide, diallylamine, triallylamine, etc.
OE these compounds, divinylbenzenes and the compound of the formula, / H or CH3 H or CH
C~2 = C~ ~C = CH2 Il- ( CH - CH2 - O ~ C

wherein s is an integer of 1 to 20, are preferred.
Such cross-linkable monomers can be employed in an amount of from about 2 % to about 94 % by weigh-t and preferably from about 10 % to about , .
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90 % by weight based on the total weight of the monomer of Formula (C) and the cross-linkable monomer. When the amount is less than about 2 %
by weight, swelling or contraction of the re.sulting copolymers are increased and the mechanical strength is decreased. On the other hand, when the amount is higher than about 9~ % by weight, the degree of cross-linkin~ is excessively increased and correspondingly, the amount of the monomer of Formula (C) is disadvantageously reduced.
Eurther, in this invention the monomer mixture may contain a monoethylenically unsaturated monomer or a conjugated monomer in an amount of at most about 92 % by weight, preferably at most about 60 % by weight and more preferably at most about 40 % by weight based on the total weight of the ~nono~er mixture.
Examples of suitable monoethylenically unsaturated monomers include hydrocarbon compounds such as styrene, methylstyrenes, ethyl-styrenes, vinylnaphthalenes; styrene derivatives such as cblorostyrenes t bromostyrenes, N,N-dimethylaminostyrenes, nitrostyrenes and chloromethyl-aminostyrenes; vinyl sulfide derivatives such as methyl vinyl sulfide and phenylvinyl sulfide; acrylic acid and methacrylic acid; itaconic acid; acrylic acid esters such as methyl acrylate and chloromethyl acrylate; methacrylic acid esters such as cyclohexyl methacrylate, dimethyl-aminoethyl methacrylate, glycidyl methacrylate, tetrahydrofurfuryl methacrylate and hydroxyethyl methacrylate; itaconic acid esters such as dimethyl itaconate, diethyl itaconate and di-n-butyl itaconate; vinyl ketones such as methyl vinyl ketone and ethyl isopropenyl ketone;
vinylidene compounds such as vinylidene chloride and vinylidene bromide;

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acrylamide derivatives such as acrylamide, N-butoxymethyl acrylamide and N,N-dimethylaminoe~hyl acrylamide; vinyl esters of carboxylic acids such as vinyl acetate and vinyl caprate; thio-carboxy~ic acld derivativeR
such as methyl thioacrylate and vinyl thioacetate; and heterocyclic vinyl compounds such as ~-vinylsuccinimide, N-vinylpyrrolidone, N-vinyl-phthalimide, N-vinylcarbazole, vinylfurans, vinylimidazoles, methylvinyl-imidazoles, vinylpyrazoles, vinyloxazolidones, vinylthiazoles, vinyl-pyridines, methylvinylpyridines, 2,4-dimethyl-6-vinyltriazine; and acrylonitrile and methacrylonitrile; and any mixtures thereof.
Examples o suitable conjugated monomers include 1,3-butadiene, isoprene, chloroprene and piperylene.
In addition, porous cross-linked copolymers can be produced according to this invention, for example, by polymerizing a monomer mixture comprising a monomer of Formula (C) and a cross-linkable monomer having a plurality of vinyl groups in the presence of an organic liquid reaction medium which does not react with the monomer mixture and/or in the presence of a linear polymer. When these additives have a high affinity for the copolymer formed by the polymerization, the pore diameter becomes small. ~ith lower affinitles of the additives for the copolymer ~ormed, the pore diametsr is more increased. Ths pore volume of the copolymer fundamentally depends uyon the amount of the addi.tive to the monomer mixture. These porous cross-linked copolymers can be produced by the method as described in "Advance of Polymer Science", 5, 113 - 213 (19~7), by J. Seidel, J. M~linsky, K. Dusek and W. Heitz. A preferred method is the one as described in United States Patent 4,093,570.

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The polymerization of this invention is preferably carried out in the presence of a radical lnitiator. Such radical initiators include, for example, peroxides such as benzoyl Reroxide, lauroyl peroxide, di-tertbutyl peroxide, dicumyl peroxide, methyl ethyl ketone peroxide, cumene hydroperoxide, tert-bu~yl hydroperoxide; and aæo compounds such as azobisisobutyronitrile, 2,2'-azobist2,4-dimethyl valeronitrile), 2-phenyl-azo-2,4-dimethyl-4-methoxy valeronitrile and 2-cyano-2-propylazoformamide.
Of these radical initiators, azo compounds are preferred due to their high reactivity.
The amount of the radical initiator employed may vary depending upon factors such as the polymerization temperature selected, the organic liquid reaction medium chosen, the amount of organic liquid reaction medium employed and other factors. Generally, however, the amount is from about 0.01 to about 12 percent by weight based on the total weight of the monomer mixture. A preferred range is from about 0.1 to about 5 percent by weight, and a more preferred range is from about 0.2 to about 3 percent by weight. Two or more of these initiators having different half life periods may also be employed.
The organic liquid reaction media which can be employed is, for example, described in the "Advance of Polymer Science" as described above.
Radical polymerization methods by irradiation of light or other radiation may also be employed in this invention.
The polymerization temperature is typically from 0C to 200~C, a preferred range is from l5C to 160C, and a more preferred range is from 30C to 130C.

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The time of the polymerization may be varied within wide limits depending upon factors such as the radical initiator selected, the amount of radical initiator employed, the organic llquid reaction mediu~ chosen, the monomers selected, the ratio of monomers to organic li~uid reaction medium and other factors. Generally, the polymerization time is from about 30 minutes to about 50 hours. A preferred time is ~rom about 1 to about 30 hours, and a more preferred time is from about 2 to about 20 hours.
The conventional method of raising the polymerization temperature during polymerization is preferred in the present invention as a way of shortening the polymerization time.
The type of polymerization of this invention may be either bulk polymeriz~tion or solution polymerizatio~ or suspension polymerization or emulsion polymerization. When the particle copolymers of this invention whlch are suitable for ion-exchange resins and adsorbents are produced, a preferred polymerization type is suspension polymerization.
It is preferred to employ a suspending agent when carrying out the suspension polymerization.
Exemplary suspending agents which may be employed in the -suspension polymerization in water include, for example9 viscous substances such as gum arabic, alginic acid, tragacanth~ agar-agar, methyl cellulose, hydroxyethyl cellulose, carboxymethyl cellulose9 starch gelatin glue; synthetic high molecular weight polymers such as sodium polyacrylate, polyvinyl alcohol, polyvinyl pyrrolidone; inorganic substances such as kaolin, bentonite, a hydrated complex of magnesium silicate, titanium dioxide, zinc oxide, calcium carbonate, talc~lm, barium , ~ 18 -. . , . , ~ .

~3 3~

sulphate, hydroxyapatite, aluminum hydroxide, calcium oxalate.
If necessary or if desired, it is effective to additionally employ pH adjustlng agents such as sodlum phosphate, sodium dihydrogen phosphate, ammoni~tm sulphate, sodium acetate, sodium hydrogen carbonate and anion surfactants including soaps of fatty acids, sodium dodecyl benzene sulphonate, sodium dodecyl sulphate and sodium lauryl sulphate, in the suspension polymerization in water. The suspending agent, the pH adjusting agent and the anion surfactant can each be employed, respectively9 in an amount of from about 0.001 to about 10 percent, preferably from about 0.01 to about 5 percent, more preferably from about 0.02 to about 3 percent, by weight based on the weight of the water employed.
The weight ratio of water to the mixture of monomers and organic liquid reaction medium which may be employed in the suspension polymeri~a-tion in water is from about 0.5 to about 15, preferably from about 1 to abDut 10, and more preferably from about 2 to about 8.
The polymers which are obtained under the above described polymerization conditions still contain unreacted monomers and optionally organic liquid reaction medium. Such unreacted monomers and organic liquid reaction medium can effectively be removed by: (1) a method comprislng immersing the polymers in a water soluble medium~ wkich dissolves the monomer and organic medium~ for a-t least about 2 to about 5 hours, subsequently filtering the polymers and washing the polymers with water: or (2) a method comprising placing the poly~ers in a column and passing a water soluble medium which dissolves the monomer mi~ture b -,' ' ~' ~ .' ' ` '`' . ' ~L37;~

and organic liquid medium, and subsequently water, through the column.
Exemplary washin~ media including methanol, ethanol, acetone, dioxane, acetonitrile and dlmethyl formamide whlch are soluble in water.
S~tch washing media remaining in the polymers can readily and easily be eliminated by washing with water.
The mass of the polymeric product thus obtained can be pulverized to particles of the product or cut into thin membranes of the product.
Also, the monomer mixture can be polymerized into a sheet of the polymeric substance.
The method of identifying the copolymers of this invention will now be described.
The copolyme.rs of this inven~ion have a three-dimensionally cross~linked structure and accordingly, many conventional methods which can be used in the identification of general linear copolymers cannot be used. That is, the conception of molecular weight cannot be used due to the three-dimensional structure of the copolymers2 and neither the determination of atomic arrangementby NMR spectral analysis nor the measurement of viscosity are possible since the copolymers are insoluble in any solvents.
In this invention, the foilowing method is employed.
First, the amount of unreacted monomers after completion of the polymerization is quantitatively analyzed by gas or liquid chromatography to measure a yield of polymerization and the chemical composition of the copolymer is calculated and then the copolymer produced is subjected to elemental analysis to confirm the chemical composition of the copolymer.

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5econdly, the degree of cross-linking can be calculated from the weight ratio of the cross-linkable monomer polymerized to the to~al monomer mlxture polymerized. Thirdly, the swellability of the copolymer in case of changing an external liquid medium which is one physlcal quantity governed by the chemical composition, physical structure or porous structure and degree of cross-linking of the copolymer can be evaluated by measuring the height of the copolymer in a column equipped with a glass filter or measuring the particle diameter of the copolymer by a microscope.
Fourthly1 the quantitative analysis of the ion-exchange groups of the copolymer is conducted by measuring the ion-exchange capacity of the copolymer. Fifthly, the density of the copolymer can be measured by the helium substitution method. Further, when the copolymer is porous, the average pore diameter and pore volume can be measured for the method of determining the porosity by a porosimeter as will be described below.
Thus, it is possible to determine various fundamenta~ properties and the chemical composition of the copolymer of this invention but it is impossible to determine the arrangement of repeating units and the three-dimensionally cross-linked structure of the copolymer. It can be assumed that the copolymers of this invention have a structure similar to the conventional three-dimensionally cross-linked structure as described in "Ion Exchange Resins", Chapter 5, by Robert Kunin, published by Robert E. Krieger Publishing Company, Huntington, New York (I972).
When the monomer mi~ture is subjected to bulk polymerization or suspension polymerization, a copolymer of gel type resin can be obtalned.
The gel type resin advantageously has a large amount of functional groups ~37~4~

per unit volume and a high mechanical strength. However, when the gel type resin is employed in a medium which does not swell the resin, the diffusion coeEficient o the resin is remarkabl~ reduced and it i9 difficult to efficiently use the functional groups. Therefore, preEerably macroporosity is imparted to the copolymer, so that the properties of ~he copolymer as a cross-linked functional polymer such as an ion-exchange resin and an adsorbent can be remarkably improved as described in detail, for example, in the "Advance of Polymer Sciencè" as described above.
The porous structure of porous copolymers is measured by mercury pressure porosimetry which is described in detail in "Fine Particle Measurement", Chapter 10, by Clyde Orr, Jr. and J. M. Dallavalle, published by Macmillan Co., New York (1959). The measurement is conducted basically by the method in accordance with A~SI/ASTM D2873-70 (Reapproved 1976) using a ~ercury Penetration Porosimeter, Model 905-1 (manufactured and sold by Micromeritics Instrument Corporation, U. S. A.). In this method, even pores having a pore diameter as small as 35 - 40 A can be measured~ In the present invention, the term "pore" means an open pore communicated to the outside surface of the copolymer and having a pore diameter of at~least about 40 A, and the pore volume is determined with regard to such open pores. The penetrometer readings versus the total absolute pressure are plotted on four phase semilog graph paper and the points are connected using a French curve. The curve obtained represents a profile of the apparent interval pore size distribution.
The "average pore diameter" is defined to be a value of r providing a maximum value of dV/d log r in the curve obtained where r represents a - . . ~ .
. " :: :' .

, ~37246 pore diameter and ~ denotes a cumulative pore volume measured by the merc~lry penetration porosimeter. In the present invention, the "total pore volume" is deE-lned to be a volume o mercury forced into pores oE
1 g of the dry copolymer as the sample dur:Lng the period in which the mercury pressure is increased from 56 psL to 50,000 psi in the mercury penetration method.
In this lnvention, when the average pore diameter of the copolymer is too small, diffusion velocity of adsorbates is greatly r~duced. On the other hand, too large average pore diameters result in disadvantages such as diminution of the surEace area having a great influence on the adsorbability and reduction of the mechanical strength.
The average pore diameter of the polymer typically ranges from about 40 A to about 9,000 R. A preferred average pore diameter ranges from about 60 ~ to 5,000 A and a more preferred average pore diameter ranges from about 60 A to about 3,000 A.
Also, the pore volume is a factor which significantly influences on adsorbability. When the pore volume is too small, a sufficient adsorbing surface cannot be obtained. On the other hand, when the pore volume is too large, the mechanical strength of the copolymer is decreased.
In this invention, the total pore volume typically ranges from about 0.05l~ mQ to about 1.5 ~ mQ per gram of the dry copolymer, wherein Y
represents the percent by weight of the cross-linkable monomer based on the total weight of the monomer mixture. A preferred total pore ranges from about 0.2 ~ mQ to about 1.3 ~ mQ per gram of the dry copolymer.
The bulk density is another index of porosity~ In the present : ~. :

;: ~

~13~ 6 invention, the bulk density is determined by to the following method:
A sample copolymer is filled in a column equipped with a glass filter, and water is suEficiently Elowed through the column and the volume of the sample-packed portion of the column is measured. Then the sample i9 sufficiently dried and weighed, and then the bulk density is calculated by dividing the weight by the volume.
The copolymers of this invention are weakly basic and have an adsorbability for acidic substances and act as a weakly basic anion exchanger in an acidic solution.
When the copolymer of this invention are reacted or neutralized with an acid which is denoted as HX, all or part of the recurring units of Formula (A), ~ R
,CH2 CH2 ~ \ R

~ CH2 ~ CH ~ ~A) in the copolymer are converted into recurring units of Formula (B)', ~Rl 2 2 ~ \ Z

- CH2 ~ 1H~ (B)' wherein Rl and R2 are the s~me as in Formula (A), but when R and/or R2 is a Cl 15 aminoalkyl group, the Cl_l5 aminoalkyl group becomeS a -~ ~H2 ~ -15 ~ 3 g P

. , , ~372~6 Exemplary acids of HX include mineral acids such as hydrogen fluoride, hydrogen chloride, hydrogen bromide, hydrogen iodide, sulEurlc acid, sulfurous acid, nitric acid, nitrous acid, chromic acid, thiocyanic acid, perchloric ac~d, phosphoric acid, carbonic acid and permanganic acid;
carbo~ylic acids such as formic acid, acetic acid, propionic acid, n-capric acid and stearic acid; substituted carbo~ylic acid such as mono-chloroacetic acid, monofluoroacetic acid, lactic acid, benzoic acid and toluic acid, and sulfonic acids such as benzenesulfonic acid, p-toluene-sul~onic acid, dodecylbenzenesulfonic acid, methanesulfonic acid and ethanesulfonic acid.
The amount of the acid of HX which can be employed is not limited and typically ranges from about 0.01 to about 100 equivalents based on the total nitrogen atoms of the copolymer.
In the reaction or neutraliæation with an acid, the copolymer which can be employed may be the one either as such or washed or dried after the polymerization. The acids can be employed either in their pure form or as their solution.
~ lso, the copolymer of this invention can be quaternlzed with a quaternizing agent of R3X to giv~ a copolymer having recurring units of Formula (B), R

2 2 ~ < R2 C 2 ~ tB) ' wherein Rl, R2, R3 and X are the same as defined above excluding R3 = H.

~, : . , ,: ~
, . .

." ` ',' . :.' ~13~72~i Exemplary quaternizing agents of R3X include halogenated allcyls, alkenyls or aryls such as methyl iodide, met`hyl bromide, methyl chloride, ethyl chloride, ethyl bromlde, n-octyl bromide, n-dodecyl chloride, cyclohexyl chloride and cycloheptyl bromide; allyl bromide and crotyl chloride; and benzyl bromide and phenethyl chloride, and dialkyl sulfates such as dimethyl sulfate and diethyl sulfate.
The quaternization agent can be applied either in the liquid phase or as a gas.
The amount of the ~uaternizing agents of R3X which can be employed is not limlted and typically ranges from about 0.01 to about 100 equivalents based on the total nitrogen atoms of the copolymer.
When the gaseous quaternizing agent is employed as a gas, the quaternization can be conducted in an autoclave or by suspending the starting copolymer in a solvent and blowing the gaseous quaternizing agent into the suspension formed. When the quaternizing agent is employed in the liquid phase, the quaternization can be conducted by mixing the liquid quaternizing agent with the s~arting copolymer in the presence or absence of unreactive solvent. Appropriate unreactive solvents for conducting the quaternization in the liquid phase are highly polar solvents or those which swell the copolymers and include acetone, methanol, ethanol, N,N-dimethylfor~amide and dimethyl sulfoxide. However, the most preferred solvent should be selected depending upon the quaternization agent employed and the reaction condition chosen.
It is preferred that the copolymer which can be employed in the quaternization is purified by thoroughly washing with the unreacted solvent or dried prior to use.

~L37Z~6 Further, the copolymer having recurring units of Formula (B) or (B)' can be produced by polymerizing a monomer tnixture comprising a monomer oE Formula (H), Cd ~ Cd ~ ~ R (d) wherein Rl, R2, R3 and X is the same as defined above, and a cross-linkable monomer.
The monomer of Formula (H) can be prepared by reacting the monomer of Formula (C) with the acid of ~ or the quaternizing agent of R3X in the same manner as in the neutralization or the quaternization of the copolymer having recurring units of Formula (A).
In this polymerization the same cross-linkable monomers having plurality of vinyl groups and, if desired, the same monoethylenically unsaturated monomers or conjugated monomers as described above can also be employed in the same manner as described above, and the radical polymerization method as in the polymerization of a monomer mixture comprising the monomer of Formula (C) and a cross-linkable monomer hav mg a plurality of vinyl groups is preferably employed. The polymerization can be carried out in the presence of a radical inltiatDr such as the azo compound as described above. Wh:en solution polymerization is conducted, it is necessary to select a solvent which dlssolves al7 the monomers, and as the solvent a polar solvent such as an alcohol, a ketone and an aprotic polar solvent can be preferably employed due to the high polarity of the monomer of Formula (H). Further, a monomer mixture comprising the ,: ;

, ,` `. ' ' "'. ' `

~37~

monomer of Formula (H~ and a cross-linkable monomer having a plurality of v:inyl groups can be polymerized in the presence of water since the monomer of Formula (H) is soluble in water. In this case, a water soluble peroxide such as cumene sodium peroxide anda redoxsystem catalyst such as sodium peroxodisulfate, potassium peroxodisulfate, potassium peroxodisulfate/
sodium sulfate and sodium chlorate/sodium sulfite can be employed.
However, the cross-linkable monomer and, if desired, a monoethylenically unsaturated monomer or a conjugated monomer are required to be water soluble. In some cases, suspension polymerization can not give a good result since the monomer of Formula ~H) is water soluble.
The copolymer having recurring units of Formulae (B) and ~B)' of this invention has anion exchangeability. When Rl, R2 and R3 are hydrogen atoms at the same time, the copolymer acts a strongly basic anion exchanger and when Rl, R2 and R3 are other groups than hydrogen atoms, the polymer acts as a weakly basic anion exchanger.
The important features of ion-exchange resins such as particle size, density basicity, exchange capacity and rate of exchange can be measured by the conventional methods described in? for example~ "Ion ~xchange Resins", Chapter 15 by Rober~ Kunin as previously described.
As described above, the copolymers of this invention can be produced without using poisonous compounds either on an experimental scale or on an industrial scale. The copolymers of this invention have a wide range of use as wea~ly basic or strongly basic anion exchange resins and adsorbents for acidic substances.
The present invention will now be illustrated in greater detail , .
`:; , ~

~372~

with reference to several Examples, but they are given for illustrative purposes only and are not to be construed as limiting the invention.
Synthesis 1 p~Diethylaminoethylst~rene p~Diethylaminoethylstyrene was synthesized according to the method reported by Tsuruta et al. [Makromol. Chem., 177, 3255 - 3263 (1976)].
In a 200 mQ three necked flask were placed 26 g of p-divinyl benzene and 40 ~Q of cyclohexane, and to the mixture were further added 40 mQ of a cyclohexane solution of an amide-amine complex prepared from 14.8 g of diethyla~ine and 0.512 g of n-butyllithium. The mixture thus obtained was heated at 50C for 3 hours with stirring. Then the reaction solution was added with lO mQ of methanol and subjected to distillation to give 29.0 g of p-diethylaminoethylstyrene having a boiling point of about 84C/l ~mHg.
Infrared Absorption Spectrum:
1800, 1620, 1505, 1195, 1060, 980, 895, 820 cm 1 Elemental Analysis:
C: 82.65 %, H: 10.58 %, N: 6.80 %
Synthesis 2 p-Ethylaminoethylstyrene In a 500 mQ stainless steel autoclave equipped with a stirrer, there were charged 240 mQ of tetrahydrofuran which was dried over metallic sodium and subjected to distillation. Then3 the autoclave was sufficiently cooled externally with a mixture of dry ice-methanol. A bomb containing ethylamine (manufactured by Tokyo Kasei Kogyo Co., Ltd.) was connected to ~: ' ' 1~37246 the autoclave and ethylamine was introduced into the autoclave by opening the valve. From the change in weight of the bomb before and after introduction, 18.9 g of ethylamine was confirmed to be introduced.
While st~rrlng the mixture, 25.2 mQ of 15 % n-butyl li~hium n-hexane solution were introduced. Subsequently, a solution of 54.6 g of p-divinylbenzene dissolved in 120 mQ of dry n-hexane was added to the mixture.
The autoclave was placed in a water bath maintained at 25C and stirring was continued for 2 hours. To the reaction mixture was added 0.5 g of methanol, and the solvent was removed by an evaporator. The product thus obtained was mixed with water and extracted with n~hexane, dried on magnesium sulfate overnight, followed by distillation to give 44 g of the distillate exhibiting a boiling point of 72C to 73C/0.13 mmHg.
This produce was confirmed to be a single compound by gas chromatography.
This compound was found to have the following analytical results.
Elemental Analysis for C12H17N: -Calculated (%~: C: 82.23, H: 9.78, N: 7.99 Found (%) : C: 81.95, H: 9.91, N: 8.03 Infrared Absorption Spectrum:
3280, 1620, 1510, 1120) 985, 900, 820 cm 1 Synthesis 3 p-Isopropylaminoethylstyrene In a 300 mQ four necked flaak equipped with a thermometer, a reflux condenser, an inlet for nitrogen and a stirrer were charged 1860 mQ
of dry n-hexane and 148 g of iso-propylamine. While stirring the mixture, 119 mQ of a 15 % n-butyllithium n-hexane solution were added dropwise .

- ' :' `` ~

~372~;

thereto. During the addition~ the temperature was maintained at 5C to 7C. The color of ~he solution was changed from colorless to pale yellow.
After 10 ~inutes, 325 g of p-divinylbenzene having a purity of 96 % were added to the mixture, whereby the color of the reaction mixture was changed to brown. Then, the inner temperature was elevated to 45C, at which the reaction was continued for 6 hours. After the reaction, the reaction was terminated with ethanol and the solvent was evaporated.
The residue was poured into 2 Q of n-hexane and the insolllble are iltered off, followed by evaporation and distillation, whereby there were obtained 230 g of the product having a boiling point of 62C - 64C/0.08 ~mHg.
Elemental Analysis for C13H19N:
Calculated (%): C: 82.48, H: 10.12, N: 7.40 Found (%) : C: 82.65, H: 10.18: N: 7.32 Infrared Absorption Spectrum (liquid Eilm):
3300, 1630, 1510, 1470~ 1380, 10~0, 990, 910, 835 cm 1 Synthesis 4 -Dimeth laminoeth 1st rene P Y, Y Y
In a 2 ~ four necked flask equipped with a Graham condenser7 a thermometer and two dropping funnel were placed a magnetic stirrer and 100 g of n-hexane which had been dried with sodium metal and distilled.
The flask was externally cooled with a mixed liquid of methanol and dry ice. After the mixed liquid of methanol and dry ice was circulated through the condenser, the end of the condenser was connected to a bomb containing dimethylamine (manufactured by Tokyo Kasei Kogyo Co., Ltd.) and dimethylamine was introduced into the flask by opening the valve. From , :, , ~ .

~L~L372~

the change in weight of the bomb before and a-Eter the introduction of dimethylamine, 115.4 g oE dimethylamine was confirmed to be introduced.
While stirring the n~hexane dimethylamine solution with the magnetic stlrrer, 77 g of a 15 % n-butylllthlum n-he~ane solutlon were added dropwlse to the mi*ture from one dropping funnel at 5uch a rate that the inner temperature of the flask did not rise over -60C, resulting in a ~ellowish solution. Subsequently, a mixed liquid of 435 g of dry n-hexane and 332 g of p-divinylbenzene was added dropwise to the solution from the other dropping funnel at such a rate that the inner temperature of the flask did not rise -60C to give a light green reaction solution~
After completion of the addition of the mixed liquid, stirring was continued for 3.5 hours and as a result, the inner temperature of the flask rose to -20C. When part of the product was sampled and subjected to quantitative analysis of the p-divinylbenæene by gas chromatography the amount of the p-divinylbenzene found was 15 % of that at the start, and the reaction was terminated with 10 mQ of methanol. The reaction m~xture was added with 1 Q of water and extracted twice with n-hexane~
and the oil phase was dried on magnesium sulfate overnight, followed by distillation to give 250 g of the distillate having a boiling point of 75C to 80~C/0.4 mmHg. This product was confirmed to be a single compound by gas chromatography. This compound was found to have the following analytical values.
Elemental Analysis for C12H17N:
CaIculated (%): C: 82.23, H: 9.78, N: 7 99 Found (~ : C: 82.08, H: 9.86, N: 8.07 ''` , , 1372~

Infrared Absorption Spectrum:
2920, 2740, 1620, 1500, 1~40, 1250, 1~30, 1030, 980, 890, 820 cm 1 Synthes:is 5 In a 200 mQ round bottomed flask was charged a variety of mixtures of an amine and a solvent as set forth in Table 1, and to the mixture were injected a 15 % n-butyllithium n-hexane solution and p-divinylbenzene in an amount as set forth in Table 1 via a syringe under stirring with a magnetic stirrer and the reaction was carried out under the reaction conditions as set forth in Table 1. The reaction mixture was added with methanol in an equimolar amount to the n-butyl-lithium employed, poured into 100 mQ of water, extracted three .times with 100 mQ of ethyl ether, dried on magnesium sulfate overnight, followed by evaporation of the ether to give a product. The product thus obtainPd was purified and isolated by gas chromatography or liquid chromatography and subjected to elemental analysis. The results are shown ~n Table 1.

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a c ~e ~ -- 3~ --~ ~13724fi Synthesis 5 `4~Vinylphenethylammonlum bromide All the procedures were conducted in a dry nitrogen atmosphere since the product was extremely hygroscopic. In a 100 mQ two necked flask equipped with a three way cock 8.6 g of the p-diethylaminoethylstyrene as obtained -in Synthesis 1 were dissolved in 35 mQ of absolute methanol and then 12.7 mQ of ethyl bromide were injected via a syringe. The quaternization was completed after 48 hours at 40~C without any side reactions. After the reaction mixture was concentrated under reduced pressure, 10~ mQ of ethyl acetate were injected via a syringe to immediately precipitate white crystals. The crystals thus formed were separated from the solution by filtration under a dry nitrogen atmosphere, washed with ethyl acetate, dried in vacuum and recrystallized from methanol-ethyl acetate solution. The results of elemental analysis of the crystals are as follows;
Elemental Analysis:
Calculated (%): C: 61.41, H: 8.579 N: 4.10, Br: 25.91 Found (%) : C: 61.53, ~: 8.39, N: 4.49, Br: 25.59 Example 1 p-Diethylaminoethylstyrene-Divinylbenzene Copolymer In a 200 mQ four necked flask equipped with a stirrer, a reflux condenser and a thermometer were placed 100 g of pure water in which 0.5 g of partially saponified poly~inyl alcohol having a degree of saponification of 88 % and a viscosity of its 2 % aqueous solution of 23 cps and 2 g of sodium chloride had been dissolved, followed by addition of a mixture of . . . ! `

~ '`, ' ~
.

~37246 16.4 g of the p-diethylaminoethylstyrene as prepared in Synthesis 1, 3.6 g of divinylbenzene having a purity of 56 % and a mole ratio of meta-isomer to para-isomer of 7 to 3 and containing 44 % by weight of ethyl-vinylbenzene and 0.2 g of 2,2'-azobisisobutyronitrile with stirring.
Then the mixture was stirr~d at 60C for 1 hour, at 70C for 2 hours and further at 80C for 4 hours. After the reaction the reaction mlxture was extracted with toluene and the amount of monomer remaining was quantitatively analyzed and found to be 1 % by weight of p-diethylaminoethylstyrene based on the weight of the feed. The copolymer thus produced was spherlcal particles having a particle diameter of 50 to 200 ~.
Infrared Absorption Spectrum (KBr method):
1600, 1505, 1195, 1060, 810 cm 1 Elemental Analysis:
C: 84.50 %, H: 9.95 %, N: 5.65 ~O
Example 2 Porous p-Diethylaminoethylstyrene-Divinylbenzene Copolymer Into a 500 mQ four necked flask were charged 6 g of hydroxy-apatite, 3 g of sodium chloride9 0.3 g of sodium lauryl sulfate and 330 g of pure water, and the mixture was added a mixture of 12.8 g of the same p-diethylaminoethylstyrene as prepared in Synthesis l, 7.2 g of the same divinylbenzene as in Example l, 20 g of acetophenone, 20 g of ethyl benzoate and 0.3 g of 2,2l-aæobisisobutyronitrile under stirring.
Then the mixture was stirred at 60C Eor 1 hour, at 70C for 2 hours and further at 80C for 4 hours. The copolymer in the form of particles thus obtained was thoroughly washed with water on a 300 mesh sieve and - - : .-: . .

- . : .
- . : ::
: : : :
- : - , : ~

:~L13~

repeatedly washed with acetone using a glass filter. Then part of the copolymer was subjected to vacuum drying at 60C for 8 hours. The porous structure o~ the copolymer dried were measured by a mercury penetration porosimeter.
Average Pore Diameter : 280 A
Pore Volume : 0.7 mQ/g Example 3 Anion Exchangeability of Copolymer Each of the copolymers obtained in Examples 1 and 2 was packed into a glass column having an inner diameter of 1.2 cm and equipped with a glass filter at a height of several centimeters, and 200 mQ of lN
hydrochloric acid were flowed down through the column and the height of the copolymer packed was measured. Then 100 m~ of acetone were flowed through the column and subsequently 100 mQ of a lN potassium nitrate solution were flowed through the column and the chlorine ion in the potassium nitrate solution passed was quantitativaly analyzed by the Fajans' method. Furthermore, 100 mQ of lN hydrochloric acid was flowed through the column and then the copolymer packed was withdra~n from the column, subjected to vacuum drying at 80C for 18 hours and subsequently weighed. Tha results are shown in Table 2. The apparent volume of the copolymer in lN hydrochloric acid was 1.28 times greater than that in O.lN sodium hydroxide.

` ~ .
.

` ,; ' ' ~37~6 'Table 2 Exchan~e Capacity Copolyme~ Per Dry Weight Per We~ Volume Bulk Density _ No. _ (meq/~) _ (meq/mQ) in lN HCQ

Example 1 3.92 1.30 0.33 Example 2 2.89 0.64 0.22 .

Example 4 ~uaternization of Copolymer Into a 50 mQ pressure bottle were 2.0 g of the same dried copolymer as prepared in Example 2, 10 g of dimethyl sulfoxide and 5.7 g of methyl iodide and the bottle was hermetically sealed and leEt to stand at 60C for 300 hours. Then the copolymer was withdrawn from the bottle and packed into a glass column equipped with a glass filter, and 200 mQ
of acetone was flowed through the column to wash the copolymer and subsequently 300 mQ of 4N hydrochloric acid was flowed through the column. Further the copolymer was washed with lO0 mQ of acetone and in the same manner as,in Example 3 the chlorine ion bonded to the copolymer was quantitatively analyzed to find to be 5.72 mmole.~ Then the following solutions (i) to (iv) were successively fIowed through the column.
(i) 200 mQ of pure water (ii) 200 mQ of lN sodium hydroxide solution (iii) 200 mQ of pure water (iY) lon mQ of lN sodium chloride solution The hydroxyl ion in the solution (iv) passed was found to be, 1.60 mmole by neutralization titration. As a result, the degree of .: ,: , ~ . :, : , - : , . . : , ~
: ,, , .

~1372~q~

quaternization was 28 % (1.60/5.72). The volume of the copolymer with the solution (iv) shranlc 4 % as compared to that with the solution (ii).
Elemental Analysis:
C: 73.39 %, H: 9.28 %, N: 4.91 %, C : 12.08 %
Example 5 . The procedures of Example 2 were repeated except that the mixture of themonomers,organic liquid medium and initiator as shown below was employed. The properties of the copolymers thus obtained are set forth in Table 3.
Mixture I (g) _Mixture II _ (g) p-Ethylaminoethylstyrene 15.4p-Isopropylaminoethyls-tyrene 15.4 56 % Divinylbenzene 8.6 56 % Divinylbenzene 8.6 2,2'-Aæobisisobutyronitrile 0.3 2,2'-Azobisisobutyronitrile 0.3 Toluene 6 Toluene 6 n-Octane 30 n-Octane 30 Table 3 Copolymer I Copolym_r~
. .
Rate of Polyme.ri~atlvn 99 % ~ 98 %
Average Pore Size 50 ~ 500 ~ 60 - 500 ~
Exchange Capacity 3.20 meq/g 2.98 meq/g Bulk Density (in lN HCQ) 0.22 0.19 Average Pore Diameter 320 A :440 A
Pore Volume 1.19 mQ/g 0.92 mQ/g Swellability (height of resin packed column swollen by changing water as the outer solution to lN HCQ) : - 40 --, : ,, . :,:
, ~L~3~%~

Example 6 The procedures of Exc~mple 1 were repeated except that the amounts of the p-dimethylaminoethylstyrene and the divinylbenzene were changed to 14.6 g and 5.4 g. ~he rate of polymerization was 99 ~ and spherical particles having a particle diameter of 40 to 250 ~ were obtained.
Infrared ~bsorption Spectrum:
1590, 1500, 1440, 13~0, 1250, 1130, 1030, 860, 800, 700 cm 1 Exchange Capacity: 3.62 meq/g Bulk Density (in HCQ solution): 0.43 Elemental Analysis:
C: 85.02 %, H: 9.25 %, N: 5.99 %
Example 7 In a 2 Q four necked flask equipped with a stirrer, reflux condenser and thermometer were placed 800 g of pure water in which 5 g of methyl cellulose having a viscosity of 2 % aqueous solution of 100 cps and 10 g of sodium chloride had been dissolved and thoroughly mixed, followed by addition of a mixture of the monomers and organic liquid medium as set forth in Table 4 with stirrlng. Then the mixture thus obtained was stirred at 70C for 5 hours and further at 80C for 2 ho~rs.
The properties of the copolymers thus obtained are set forth in Table 4.

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The procedures of Example 7 were repeated e~cept that each of the mixtures of the monomers and the organic liquid medium as set forth in Table 5 was used. The properties of the copolymers thus obtained are set forth in Table 5.

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Example 9 In a 200 mQ three necked flask were charged 10 g of the copolymer as obtained in ~un No. 1, Example 7, 100 mQ of acetone and 24 g of benzyl bromide and the reaction was conducted for 12 hours under refluxing with stirring. After the reaction, the copolymer was thoroughly washed with acetone and water, and the degree of quaternization was measured according to the method of Example 4.
Degree of Quaternization: 32 %
Elemental Analysis:
C: 76.87 %, H: 8.37 %, N: 5.22 %
Example 10 In a lOOmQ pressure-resistant glass tube were charged 30 g of p-diethylaminoethylstyrene, 11 g of acrylonitrile, 9 g of 56 %
divinylbenzene and 0.5 g o 2,2'-azobis(2,4-dimethylvaleronitrile) and uniformly mixed. Then the tube was melt-sealed and heated at 60~C for 3 hours and further at 70C for 4 hours. After cooling, the contents were taken out of the tube, finely pulverized and subjected to wet c]assification with a set of sieves to collect polymer particles having a particle si~e of 80 to 200 Tyler mesh. Af-ter the polymer particles thus obtained were thoroughly washed with methanol and various properties were measured.
Exchange Capacity: 2.60 meq/g Bulk Density (ln lN HCQ): 0.40 Swellability (as defined in Table 2): 31 %
Infrared Absorption Spectrum:
2250, 1600, 1510, 1190, 1065 cm 1 :. ~ "
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~IL372~6 Example 11 In a 100 mQ pressure-resistant glass tube were charged 32 g of the p-ethylaminoethylstyrene as obta~ned in Synthesis 2, 18 g of 56 %
divinylbenzene and 0.5 g of 2,2'-azoblsisobutyronitrile and sufficiently mixed. Then the tube was melt-sealed, heated at 80C Eor 6 hours and then opened to give transparent hard mass having a specific gravity of 1.02. The mass thus obtained was pulveriæed by a grinder and packed into a column to measure the exchange capacity of th~ copolymer.
Exchange Capacity: 3.16 meq/g Infrared Absorption Spectrum:
1600, 1510, 1440, 1110, 1020, 820, 790, 700 cm Elemental Analysis:
C: 86.02 %, H: 8.93 %, N: 5.05 %
Example 12 32 g of the p-isopropylaminoethylstyrene as obtained in Synthesis 3, 18 g of 56 % divinylbenzene and 0.5 g of 2,2'-azobisiso-butyronitrile were thoroughly mixed and charged in a 100 mQ pressure-resistant glass tube. Then the glass tube was melt-sealed and heated at 80C for 8 hours and then the mass obtained was taken out of the glass tube, finely pulverlzed, packed into a column and washed with acetone.
Bulk Density (in acetone): 0.44 Exchange Capacity : 2.93 meq¦g Infrared Absorption Spectrum:
1600, 1510, 1440, 1380, 1165, 820, 700 cm Elemental Analysis:
C: 86.21 %, H: 9.03 %, N: 4.82 %

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, ~L~L37246 E*ample 13 In a 50 mQ glass t~tbe were charged 6.25 g of the 4-vinylphenethyl-ammoni~lm bromide as obtained in Synthesis 6, 2 g of N,N'-methylenediacryl-amide, 18.2 g of water, 10 mg of sodium sulfate and 27 mg of potassium peroxodisulfate and homogeneously mixed and to the mixture was added hydrochloric acid to adjust the pH of the mixture to 3.3. Then the tube was melt-sealed and left to stand at 40C for 24 hours and the polymer obtained was taken out of the glass tube, pulverized by a grinder and subjected to the same measurement of exchange capacîty as in Example 3.
Exchange Capacity : 2.42 meq/g Bulk Density (in lN HcQ): 0.21 Comparative Example In a 3 Q four necked flask equipped with a stirrer, a reflux condenser and a thermometer were charged 1,500 g of pure water in which a partially saponified polyvinyl alcohol having a degree of saponification of 88 % and a viscosity of 2 % aqueous solutlon of 23 cps and 30 g of sodium chloride had dissolved, followed by addition of a mixture of 64 g of p-chloromethylstyrene, 36 g of 56 % divinylbenzene~ 100 g of toluene, 100 g of decalin and 2 g of 2,2'-azobisisobutyronitrile with stirring.
Then the mixture was stirred at 60~C for one hour, at 70~C for two hours and further at 80C for four hours.
The copolymer in the form of particles thus ob-tained was placed in a glass filter, washed with 1,000 mQ of water and then with 1,000 mQ
of acetone and charged in a 1 Q four necked flask. Then to the copolymer were add~d 400 mQ of acetone and 70 g of 50 % diethylamine aqueous solution :
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and the mixture was stirred for 16 hours under refluxing. The product thus obtained was thoroughly washed with acetone and then with water.
Part of the anion exchange capacity of the product was measured in accordance with the method of Example 3 and the exchange capacity per dry weight of the product was 2~52 me~!g and that per wet volume oE the product was 0.63 meq/mQ.
While the invention has been described in detail and with reference to specific embodiments thereof, it will be apparent to one skilled in the art that various changes and modiEications can be made therein without departing from the spirit and scope thereof.

~ ~ -.

Claims (59)

WHAT IS CLAIMED IS:

1. A basic copolymer whose main chain is cross-linked which comprises about 6 to about 98 % by weight of recurring units of Formula (A) or (B), (A) or (B) wherein R1, R2 and R3, which may be the same or different, each represents a hydrogen atom or a hydrocarbon group selected from the group consisting of C1-20 alkyl groups, C3- 10 cycloalkyl groups, C3-8 alkenyl groups, C6-15 aryl groups, C7-12 arylalkyl groups and C1-15 aminoalkyl groups; and X is an acid radical, and about 2 to about 94 % by weight of cross-linked units based on the total weight of the recurring units of Formula (A) or (B) and the cross-linked units.

2. The copolymer of Claim 1, wherein X is an acid radical selected from the group consisting of a halogen atom, 1/2SO4, 1/2SO3, HSO4, NO3, NO2, 1/2CrO4, SCN, C?O4, OH, H2PO4, 1/2HPO4, 1/3PO3, HCO3, 1/2CO3, CN, MnO4, R4COO wherein R4 is a C1-20 alkyl group, a C6-15 aryl group, a C1-10 haloalkyl group or a C1-10 hydroxyalkyl group, R5SO3 wherein R5 is a methyl group, an ethyl group or a C6-20 aryl group, CH3OSO3 and C2H5OSO3.

3. The copolymer of Claim 1, wherein the hydrocarbon group is a C1-20 alkyl group.

4. The copolymer of Claim 3, wherein the alkyl group has 1 to 8 carbon atoms.

5. The copolymer of Claim 4, wherein R1 and R2 are methyl groups.

6. The copolymer of Claim 4, wherein R1 and R2 are ethyl groups.

7. The copolymer of Claim 1, wherein R1 is a hydrogen atom and R2 is an ethyl group.

8. The copolymer of Claim 1, wherein R1 is a hydrogen atom and R2 is an isopropyl group.

9. The copolymer of Claim 1, wherein R1 is a hydrogen atom and R2 is a n-propyl group.

10. The copolymer of Claim 1, wherein R1 is a hydrogen atom and R2 is a cyclohexyl group.

11. The copolymer of Claim 1, wherein the hydrocarbon group is a C1-15 aminoalkyl group.

12. The copolymer of Claim 11, wherein R1 and R2 are aminoethyl groups.

13. The copolymer of Claim l, wherein the group is in the para position to the group or the group.

14. The copolymer of Claim 1, wherein the cross-linked units have the formula, wherein A1 is a C6-14 aromatic hydrocarbon radical, a pyridine nucleus or a quinoline nucleus.

15. The copolymer of Claim 14, wherein the cross-linked units have the formula,

16. The copolymer of Claim 15, wherein the cross-linked units have the formula,

17. The copolymer of Claim 1, wherein the cross-linked units have the formula, wherein A2 is -CO-, -SO2- or group wherein A3 is -O-, -NH-, -S-, -SO2-, -SO- or group wherein ? is zero or an integer of 1 to 4.

18. The copolymer of Claim l, wherein the cross-linked units have the formula, wherein A4 is group wherein p is an integer of 1 to 6.

19. The copolymer of Claim 1, wherein the cross-linked units have the formula, wherein q is an integer of 2 to 4 and A5 is a radical of a polyol having q terminal hydroxyl group and a number average molecular weight of at most 1000.

20. The copolymer of Claim 19, wherein the cross-linked units have the formula, wherein s is an integer of 1 to 20.

21. The copolymer of Claim 20, wherein the cross-linked units have the formula

22. The copolymer of Claim 1, wherein the cross-linked units have the formula, wherein A6 is a di- or tri-carboxylate radical having 2 to 10 carbon atoms.

23. The copolymer of Claim 1 which comprises up to about 92 % by weight of units of a monoethylenically unsaturated monomer or a conjugated monomer based on the total weight of the recurring units of Formula (A) or (B), the cross-linked units and the units of the monoethylenically unsaturated monomer or the conjugated monomer.

24. The copolymer of Claim 1 which comprises about 10 to about 90 %
by weight of the recurring units of Formula (A) or (B) based on the total weight of the recurring units of Formula (A) or (B) and the cross-linked units.

25. The copolymer of Claim 24 which comprises about 20 to about 80 %
by weight of the recurring units of Formula (A) or (B) based on the total weight of the recurring units of Formula (A) or (B) and the cross-linked units.

26. The copolymer of Claim 1 having a porous structure.

27. The copolymer of Claim 26 whose average pore diameter ranges from about 40 .ANG. to about 97000 .ANG..

28. The copolymer of Claim 27 whose average pore diameter ranges from about 60 .ANG. to about 5,000 .ANG..

29. The copolymer of Claim 28 whose average pore diameter ranges from about 60 .ANG. to about 3,000 .ANG..

30. The copolymer of Claim 26 whose total pore volume per gram of the dry copolymer ranges from about 0.05?Y m? to about 1.5?Y m? wherein Y represents the percent by weight of the cross-linked units based on the total weight of the copolymer.

31. The copolymer of Claim 30 whose total pore volume per gram of the dry copolymer ranges from about 0.2?Y m? to about 1.3?Y m? wherein Y represents the percent by weight of the cross-linked units based on the total weight of the copolymer.

32. The copolymer of Claim 30 whose shape is shperical.

33. A process for producing the copolymer of Claim 1 having the recurring units of Formula (A) which comprises polymerizing a monomer mixture of about 6 to about 98 % by weight of a monomer of Formula (C), (C) wherein R1 and R2 which may be the same or different, each represents a hydrogen atom or a hydrocarbon group selected from the group consisting of C1-20 alkyl groups, C3-10 cycloalkyl groups, C3-8 alkenyl groups, C6-15 aryl groups, C7-12 arylalkyl groups and C1-15 aminoalkyl groups, and about 2 to 94 % by weight of a cross-linkable monomer having a plurality of vinyl groups based on the total weight of the monomer of Formula (C) and the cross-linkable monomer.

34. The process of Claim 33, wherein R1 and R2 in Formula (C) are C1-20 alkyl groups.

35. The process of Claim 33, wherein R1 and R2 in Formula (C) are C1-8 alkyl groups.

36. The process of Claim 34, wherein R1 and R2 in Formula (C) are methyl groups.

37. The process of Claim 34, wherein R1 and R2 in Formula (C) are ethyl groups.

38. The process of Claim 33, wherein R1 in Formula (C) is a hydrogen atom and R2 in Formula (C) is a C1-8 alkyl group.

39. The process of Claim 38, wherein R1 in Formula (C) is a hydrogen atom and R2 in Formula (C) is an ethyl group.

40. The process of Claim 38, wherein R1 in Formula (C) is a hydrogen atom and R2 in Formula (C) is an isopropyl group.

41. The process of Claim 38, wherein R1 in Formula (C) is a hydrogen atom and R2 in Formula (C) is a n-propyl group.

42. The process of Claim 38, wherein R1 in Formula (C) is a hydrogen atom and R2 in Formula (C) is a cyclohexyl group.

43. The process of Claim 33, wherein R1 and R2 in Formula (C) are C1-15 aminoalkyl groups.

44. The process of Claim 43, wherein R1 and R2 in Formula (C) are aminoethyl groups.

45. The process of Claim 33, wherein the CH2 = CH - group is in the para position to the - CH2 - CH2 - group.

46. The process of Claim 33, wherein the cross-linkable monomer is a compound of the formula, wherein A1 is a C6-14 aromatic hydrocarbon radical, a pyridine nucleus or a quinoline nucleus.

47. The process of Claim 46, wherein the cross-linkable monomer is divinylbenzene.

48. The process of Claim 33, wherein the cross-linkable monomer is a compound of the formula, wherein q is an integer of 2 to 4 and A5 is a radical of a polyol having 2 to 4 hydroxyl group and a number average molecular weight of at most 1000.

49. The process of Claim 48, wherein the cross-linkable monomer is a compound of the formula, wherein s is an integer of 1 to 20.

50. The process of Claim 49, wherein the cross-linkable monomer is ethyleneglycol di-acrylate or -methacrylate.

51. The process of Claim 49, wherein the cross-linkable monomer is diethyleneglycol di-acrylate or -methacrylate.

52. The process of Claim 49, wherein the cross-linkable monomer is polyethyleneglycol having a number average molecular weight of 100 to 1,000 di-acrylate or -methacrylate.

53. The process of Claim 33, wherein the monomer mixture additionally comprises up to about 92 % by weight of a monoethylenically unsaturated monomer or a conjugated monomer based on the total weight of the monomer of Formula (C), the cross-linkable monomer and the monoethylenically unsaturated monomer or a conjugated monomer.

54. The process of Claim 33, wherein the polymerization is conducted in the presence of a radical initiator.

55. The process of Claim 54, wherein the radical initiator is an azo compound.

56. The process of Claim 33, wherein the polymerization is conducted in the presence of an organic liquid medium which does not react with the monomer mixture and/or in the presence of a linear polymer.

57. The process of Claim 33, wherein the polymerization is conducted as suspension polymerization.

58. A process for producing the copolymer of Claim 1 having the recurring units of Formula (B) which comprises reacting the copolymer of Claim 1 having the recurring units of Formula (A) with an acid of HX, wherein X is an acid radical selected from the group consisting of a halogen atom, 1/2SO4, 1/2SO3, HSO4, NO3, NO2, 1/2CrO4, SCN, C?O4, OH, H2PO4, 1/2HPO4, 1/3PO3, HCO3, 1/2CO3, CN, MnO4, R4COO wherein R4 is a C1-20 alkyl group, a C6-15 aryl group, a C1-10 haloalkyl group or a C1-10 hydroxyalkyl group, R5SO3 wherein R5 is a methyl group, an ethyl group or a C6-20 aryl group, CH3OSO3 and C2H5OSO3.

59. A process for producing the copolymer of Claim 1 having the recurring units of Formula (B) which comprises quaternizing the copolymer of Claim 1 having the recurring units of Formula (A) with a quaternizing agent of R3X, wherein R3 is a hydrogen atom or a hydrocarbon group selected from the group consisting of C1-20 alkyl groups, C3-10 cycloalkyl groups, C3-8 alkenyl groups, C6-15 aryl groups, C7-12 arylalkyl group and C1-15 aminoalkyl groups; and X is an acid radical selected from the group consisting of 1/2SO4,1/2SO3, HSO4, NO3, NO2, 1/2CrO4, SCN, C?O4, OH, H2PO4, 1/2HPO4, 1/3PO3, HCO3, 1/2CO3, CN, MnO4, R4COO wherein R4 is a C1-20 alkyl group, a C6-15 aryl group, a C1-10 haloalkyl group, R4SO3 wherein R5 is a methyl group, an ethyl group or a C6-20 aryl group, CH3OSO3 and C2H5OSO3.