An aqueous, chlorinated polyolefin-based resin composition and its manufacture

Abstract: An aqueous, chlorinated polyolefin-based resin composition which has an acid value of 1 - 500 mg KOH/g and which is obtained by chlorination in the range of 5 -50 wt.% of one or more kinds of polymers selected from polyolefins modified with the following compounds (A), (B), and (C): (A) α, β-unsaturated carboxylic acids represented by any of the formulae I, II, and III below wherein each of R 1 , R 2 , R 3 , R 4 and R 5 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 and -COOH. (B) and/or acid anhydrides of α, β-unsaturated carboxylic acids of (A), represented by either of the formulae IV and V below in which R 1 and R 2 are each independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 10 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 . in which R 1 , which is connected to the ring carbon atom by an ethylenic double bond, is selected from -CH 2 , -C 2 H 4 , -C 3 H 6 , -C 4 H 8 , -C 5 H 10 , -C 6 H 12 , -C 7 H 14 , -C 8 H 16 , -C 9 H 18 , -C 10 H 20 , -CHCOOH, -C(CH 3 )COOH, -C(C 2 H 5 )COOH, -C(C 3 H 7 )COOH and -C(C 4 H 9 )COOH; and R 2 is selected from H,-CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 . (C) and/or compounds having one or more double bonds in a molecule, represented by either of the formulae VI or VII below CH 2 =C(R 1 )COOR 2 in which R 1 is H or -CH 3 and R 2 is selected from H, CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 10 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 , -C 11 H 23 , -C 12 H 25 , -C 13 H 27 , -C 14 H 29 , -C 15 H 31 , -C 16 H 33 , -C 17 H 35 , -C 18 H 37 , -C 19 H 39 , -C 20 H 41 . -C 2 H 4 OH, -C 3 H 6 OH, -C 4 H 9 OH, -C 5 H 10 OH, -C 6 H 12 OH, -C 7 H 14 OH, -CH 2 CH 2 N(CH 3 ) 2 , -CH 2 CH 2 N(CH 2 CH 3 ) 2 , -CH 2 CH 2 OCOCH 2 CH 2 COOH, -CH 2 CH 2 OCOC(CH 3 )=CH 2 , -(CH 2 CH 2 O) 2 COC(CH 3 )=CH 2 , -C 4 H 8 OCOC(CH 3 )=CH 2 , -C 6 H 12 OCOC(CH 3 )=CH 2 , -CH 2 C(CH 2 =C(R 1 )COOCH 2 ) 2 CH 2 CH 3 , -CH 2 CH(OH)CH 2 OCOC(CH 3 )=CH 2 , (CH 2 CH 2 O) COC(CH 3 )=CH 2 ; 1≤ x ≤20 in which each of R 1 , R 2 , R 3 , R 4 and R 5 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 has use as an adhesive, in inks and as coating materials for polyolefin base materials.

Description: This invention relates to less polluting or non-polluting, aqueous, chlorinated polyolefin-based resin compositions which are used as a primer or coating compositions for moldings or films consisting mainly of polyolefin resins, such as polypropylene, ethylene-propylene copolymers, and ethylene-propylene-butene copolymers. In particular, the invention relates to an aqueous, chlorinated polyolefin-based resin composition and to a method of its manufacture, which resin composition, when used as a primer or a base coat for moldings or films of polyolefin-based resins, forms a coating film having a good adhesiveness to the polyolefin base material and also a good interlayer adhesiveness to the base coat and/or the top coat, and having good gasohol resistance, moisture resistance, impact resistance, and flexibility; and also which, when used as a single-coat material, gives a coating film having good adhesiveness to the polyolefin base material, and has a good miscibility or compatibility with polymer emulsions and pigments used in combination with it, and in addition keeps good the physical properties of the coating film from it after exposure. In addition to the use as an adhesive as mentioned above, the resin composition is used for inks, coating materials, their primers, etc. Polyolefin resins are relatively inexpensive and have useful properties, such as chemical resistance, water resistance, heat resistance, etc. Thus, they have been used as industrial materials in a wide range of applications; the use for auto parts is an example. Having those advantages, however, polyolefin resins are crystalline and have no reactive functional groups on their surface; so it has been difficult to apply adhesives and coatings to base materials of the polyolefin-based resin. To solve this problem, attempts have been made to improve the adhesiveness of coating films to polyolefin-based resins by modifying the resin surface through vapour cleaning, defatting, acid treatment, corona discharge treatment or plasma treatment. On the other hand, in the field of coatings, adhesives and inks, chlorinated polyolefins, which have relatively good adhesiveness to such hard-to-coat resin surfaces as mentioned above, have been used. However, most of those chlorinated polyolefins were of the solution type, dissolved in an organic solvent such as toluene, xylene, and/or esters. The vapours of such organic solvents are released in substantial amounts into the atmosphere at the time of coating operations and this has a serious environmental and sanitary impact on coating workers and citizens living in a wide area around the location of the coating operations, and even on the surrounding ecosystem. Based on this situation, a patent application (WO9303104) has recently been made for an aqueous emulsion in which chlorinated polyolefins are blended with resins containing carboxylic acids. In these blend systems, however, a phase separation occurred between the different polymers after the formation of the coating film and a hydrophilic component, such as a surfactant, was introduced into the coating polymers, leading to degraded strength and lowered water resistance of the coating film. GB-A-2273294 discloses an aqueous polyolefin resin composition based on a polyolefin or modified polyolefin which may be used as a paint, primer, ink, sealant or adhesive. The composition contains a substance with a structure of poly(alkylene oxide) and a solubility parameter of not lower than 7 to not higher than 12. Also disclosed is an acid-modified, chlorinated polyolefin as the base polymer of the composition. WO-A-94/28077 discloses a water-based primer composition made up of a water-compatibilised modified polyolefin type resin, a water-compatibilised acrylic resin, and a water compatibilised polyurethane resin. Considering what has been written above, the applicant of this patent has already completed the invention in which an aqueous emulsion is obtained by dissolving chlorinated polyolefins in monomers or oligomers and emulsifying the solution with a surfactant and then polymerising (tokukaihei 5-209006, tokukaihei 5-287251, tokukaihei 6-287521, tokukaihei 8-176309). The object of these inventions was to increase the strength and water resistance of the coating film by copolymerisation of chlorinated polyolefins with acrylic monomers to achieve the higher molecular weight; in order to achieve the polymerisation as originally intended, however, the surfactant had to be selected from a narrow range and in addition it had to be used in a larger amount. To improve the water resistance of the coating film from these chlorinated polyolefin-based resin emulsions, the use of water-soluble substances had to be further decreased. The object of this invention is to achieve, without vapour-cleaning or defatting the surface of a polyolefin base material with chlorine-containing organic solvents such as trichloroethane, etc., a coating which has adhesiveness to the polyolefin base material and also has an improved interlayer adhesiveness to the base coat and/or the top coat and improved levels in properties such as water resistance, gasohol resistance, etc., and also which is less polluting or non-polluting. In an attempt to solve the problem mentioned above, the inventors made a lot of effort to complete the invention. The first aspect of this invention is an aqueous, chlorinated polyolefin-based resin composition which has an acid value of 1 - 500 mg KOH/g and which is obtained by chlorination to a percentage by weight of chlorine in the range of 5 -50 wt.% of one or more kinds of polymers selected from polyolefins modified with the following compounds (A), (B), and (C): (A) α, β-unsaturated carboxylic acids represented by any of the formulae I, II, and III below wherein each of R 1 , R 2 , R 3 , R 4 and R 5 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 and -COOH, and wherein R 8 is selected from CH 2 , C 2 H 4 , C 3 H 6 , C 4 H 8 , C 5 H 10 , C 6 H 12 , C 7 H 14 , C 8 H 16 , C 9 H 18 , C 10 H 20 , CHCOOH, C(CH 3 )COOH, C(C 2 H 5 )COOH, C(C 3 H 7 )COOH and C(C 4 H 9 )COOH; (B) and/or acid anhydrides of α, β-unsaturated carboxylic acids of (A), represented by either of the formulae IV and V below in which R 6 and R 7 are each independently selected from H,-CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 10 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , - C 9 H 19 , -C 10 H 21 . in which R 8 , which is connected to the ring carbon atom by an ethylenic double bond, is selected from -CH 2 , -C 2 H 4 , -C 3 H 6 , -C 4 H 8 , -C 5 H 10 , -C 6 H 12 , -C 7 H 14 , -C 8 H 16 , -C 9 H 18 , -C 10 H 20 and -CHCOOH, -C(CH 3 )COOH, -C(C 2 H 5 )COOH, -C(C 3 H 7 )COOH and -C(C 4 H 9 )COOH; and R 9 is selected from H,-CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 . (C) and/or compounds having one or more double bonds in a molecule, represented by either of the formulae VI or VII below CH 2 =C(R 10 )COOR 11 in which R 10 is H or -CH 3 and R 11 is selected from H, CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 10 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 , -C 11 H 23 , -C 12 H 25 , -C 13 H 27 , -C 14 H 29 , -C 15 H 31 , -C 16 H 33 , -C 17 H 35 , -C 18 H 37 , -C 19 H 39 , -C 20 H 41 , -C 2 H 4 OH, -C 3 H 6 OH, -C 4 H 9 OH, -C 5 H 10 OH, -C 6 H 12 OH, -C 7 H 14 OH, -CH 2 CH 2 N(CH 3 ) 2 , -CH 2 CH 2 N(CH 2 CH 3 ) 2 ,-CH 2 CH 2 OCOCH 2 CH 2 COOH, -CH 2 CH 2 OCOC(CH 3 )=CH 2 , -(CH 2 CH 2 O) 2 COC(CH 3 )=CH 2 , -C 4 H 8 OCOC(CH 3 )=CH 2 , -C 6 H 12 OCOC(CH 3 )=CH 2 , -CH 2 C(CH 2 =C(R 1 )COOCH 2 ) 2 CH 2 CH 3 , -CH 2 CH(OH)CH 2 OCOC(CH 3 )=CH 2 , (CH 2 CH 2 O) x COC(CH 3 )=CH 2 ; 1≤ x ≤20 in which each of R 1 , R 2 , R 3 , R 4 and R 5 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 . After the completion of the chlorination mentioned above, an epoxy compound having one epoxy group in a molecule or its oligomer is added so that the weight ratio of (the compound having one epoxy group in a molecule and/or its oligomer) to (the aqueous, chlorinated polyolefin-based resin composition) is 0.1:100 - 50:100. A second aspect is the aqueous, chlorinated polyolefin-based resin composition described above as the first aspect, in which the chlorinated polyolefins have polar groups introduced by further modification with the compounds (A), (B), and (C) as defined above in the solution system or in the heterogeneous dispersion system. A third aspect is the aqueous, chlorinated polyolefin-based resin composition described above as the first or, second aspect, which contains, as the main constituents, α, β-unsaturated carboxylic acids represented by any of the formulae I, II or III above and/or their acid anhydrides represented by either of the general formulae IV or V above in an amount between 0.01 wt.% and 60 wt.%. A further embodiment of the invention is the aqueous, chlorinated polyolefin-based resin composition described above, which, in preparation of the aqueous, chlorinated polyolefin-based resin composition, contains, as the main constituents, compounds having one or more double bonds in a molecule, represented by either the formulae VI and VII above in an amount between 0.01 wt.% and 60 wt.%. A yet further aspect of the invention is a method for manufacture in an aqueous, chlorinated polyolefin-based resin composition in which during preparation of or after preparation of the aqueous, chlorinated polyolefin-based resin composition described above, a polymer containing oxazoline is added in an amount between 0.01 wt.% and 60 wt.%. In an even further aspect, the invention provides a method for manufacture of the emulsion of the aqueous, chlorinated polyolefin-based resin composition described above, in which during preparation of the aqueous, chlorinated polyolefin-based resin composition, 0.01 - 20 wt.parts of an organic or inorganic basic substance is added for 100 wt. parts of chlorinated polyolefins or chlorinated polyolefins having polar groups introduced, to neutralize with the organic or inorganic basic substance the aqueous, chlorinated polyolefin-based resin composition so as to have a pH value in the range of 5 - 10. According to a preferred embodiment, in the method for manufacture of the aqueous, chlorinated polyolefin-based resin composition described above, during preparation of the aqueous, chlorinated polyolefin-based resin composition 0.01 - 100 wt. parts of a nonionic surfactant and/or anionic or cationic surfactant are added for emulsification. More preferably, during preparation of or after preparation of the aqueous, chlorinated polyolefin-based resin composition described above, an aqueous polyurethane-based resin having a hydroxyl group and/or carboxyl group and/or an isocyanate group in its molecule or having no functional group, or the emulsion of said aqueous polyurethane-based resin, is added in an amount between 0.01 wt. part and 2000 wt. parts. The inventors have found that this invention gives a stable emulsion with the surfactant of a very small amount or without the surfactant, the surfactant amount, if any, being much smaller compared to cases in which other monomers are used, and that as a result the coating film has an excellent water resistance. Further the inventors have found that the stability and compatibility are good also when an oxazoline-containing polymer and/or an aqueous polyurethane-based resin or its aqueous emulsion are added, and so the properties of the coating film, such as water resistance, etc., are excellent. The solubility parameter, SP value, of the α, β-unsaturated carboxylic acids of the formulae I, II and III used in claim 1 (A) of this invention is preferably 9.5 or greater, and 15.5 or less; the SP value of the compounds having one or more double bonds in the molecule, having the formulae VI or VII used in claim 1 (C) is preferably 7.5 or greater, and 15.5 or less. The solubility parameter, SP value, indicates the polarity of the compound, and can be calculated using the method by Fedors, based on the chemical composition of the monomers. The method by Fedors for calculation of the SP value is shown below: SP value = (ΔH -RT 1/2 )/V = (Σe i /Σv i ) 1/2 , where ΔH : heat of vaporisation V : molar volume (cm 3 /mol) Σe i = ΔH - RT (cal/mol) Σv i : sum of each molar volume (cm 3 /mol) With what is written above, the SP value can be calculated using Δe i and ΔV i given by Fedors. In the synthesis of aqueous, chlorinated polyolefin-based resin compositions using this invention, polyolefins are modified so as to have a higher polarity with polar monomers having an SP value between 9.5 and 15.5 and/or polar monomers having an SP value between 7.5 and 15.5. After chlorination, the second stage modification for a further higher polarity may be applied, if necessary, using monomers having SP values in the same range as mentioned above. By this modification, the aqueous, chlorinated polyolefin-based resin composition can be synthesized without use of surfactants or with use of those in a very small amount. This invention relates to an aqueous, chlorinated polyolefin-based resin composition synthesized in such a way. In manufacture of said aqueous chlorinated polyolefin-based resin composition using this invention, aqueous chlorinated polyolefin-based resin compositions which contain, as their constituents, α,β-unsaturated carboxylic acids and/or their acid anhydrides in an amount between 0.01 wt.% and 60 wt.%, and/or compounds having one or more double bonds in a molecule in an amount between 0.01 wt.% and 60 wt.%, are included. Besides, the addition of an organic or inorganic basic substance during the manufacture is effective in increasing greatly the stability of the emulsion of the aqueous, chlorinated polyolefin-based resin composition of this invention. The use of the surfactant in the manufacturing process mentioned above not only increases remarkably the stability of the emulsion of the aqueous, chlorinated polyolefin-based resin composition but also improves the secondary properties such as the properties of the coating film, compared to those in the case in which no surfactant is used, depending upon the molecular weight, molecular weight distribution, and chlorination degree of the chlorinated polyolefin used as a base, the kind and amount of the polar component contained, the kind and amount of the coexisting solvent, and the emulsifying conditions. Therefore, the kind and amount of the surfactant to be used are decided considering the molecular weight, molecular weight distribution, and chlorination degree of the chlorinated polyolefin used as a base, the kind and amount of the polar component contained, and the kind and amount of the coexisting solvent; one from the nonionic surfactant, the anionic one, and the cationic one, or a blend of the nonionic one and the anionic one, or that of the nonionic one and the cationic one is used. Compounding with an oxazoline-containing polymer during or after the synthesis is good for the emulsion of the aqueous, chlorinated polyolefin-based resin composition. The more detailed explanation of this invention will be given below, but the scope of the invention is not limited to what will be explained below. The polyolefin-based resin used in this invention includes, for example, polypropylene, ethylene-propylene copolymer, and ethylene-propylene-butene copolymer; also included are block copolymers and random copolymers of ethylene or propylene with other monomers such as butene, pentene, hexene, heptene, octene, nonene, etc.; also included are copolymers of two or more components selected from the monomers mentioned above and/or monomers other than ones mentioned above. These polymers are used solely or used in a blend of two or more kinds of them. It is known that there are stereoregular isomers in polypropylene homopolymer or propylene-based copolymers as listed below: (a) isotactic, (b) atactic, (c) syndiotactic, (d) hemi-isotactic, and (e) stereoblock. Polypropylene moldings which need to be good at mechanical properties, such as rigidity, impact strength, etc., or at durability, are made mainly of (a) isotactic polypropylene today, the automobile bumper being its example. Thus, in order to achieve the object of this invention in coating those moldings, the emulsion of the aqueous, chlorinated polyolefin-based resin composition of this invention with an isotactic polymer, such as isotactic polypropylene, as a main component, is used; by doing so, good coating properties including adhesiveness are attained. On the other hand, the use of the emulsion of the aqueous, chlorinated polyolefin-based resin composition of this invention with an atactic polymer, such as (b) atactic polypropylene or a syndiotactic polymer, such as (c) syndiotactic polypropylene, as a main component, results in unsatisfactory adhesiveness or bad coating properties. The weight-average molecular weight of these polymers used are in the range of 1,000 - 300,000; the more preferable molecular weight is between 5,000 and 100,000 as a weight-average molecular weight. The polymers having a weight-average molecular weight less than 1,000 cannot be used, because the coating film strength is lowered after chlorination or because coating film properties such as gasohol resistance, water resistance, etc. are lowered. The weight-average molecular weight higher than 300,000 is undesirable because of the viscosity increase in the modification and/or chlorination processes leading to difficulty in operation. Instead of using polyolefins as it is, they may be used after degradation by heat decomposition or by oxidation with an oxidizing agent such as oxygen, peroxides, etc., in solution in an appropriate solvent or not in solution. In order to achieve the object of the invention, the preferable crystallinity of the polyolefin used in this invention is between 20% and 70%. the crystallinity lower than 20% causes decrease in the coating film strength after chlorination or lowering in the coating film properties such as gasohol resistance, water resistance, etc.; besides the low crystallinity causes development of coating film tackiness leading to lowered coating film properties; thus such polyolefins cannot be used. In the case of the crystallinity higher than 70%, a lot of crystals remain in the coating polymer after chlorination, and the polymer is difficult to dissolve in an aromatic organic solvent such as toluene, leading to difficulty in the modification stage that follows. The modification of polyolefins is carried out in their solution in an organic solvent such as toluene and xylene, using α,β-unsaturated carboxylic acids and/or their acid anhydrides and/or compounds having one or more double bonds in a molecule in the presence of a radical-generating agent; or in another way the modification is carried out in an autoclave or a single-shaft or two-or-more shaft extruder which can heat polyolefins to a temperature higher than their softening points or melting points and make them react in the molten state, using α, β-unsaturated carboxylic acids and/or their acid anhydrides and/or compounds having one or more double bonds in a molecule in the presence or absence of a radical-generating agent. The following compounds are listed as a radical-generating agent for the modification reaction: peroxides such as di-tert-butyl perphthalate, tert-butyl hydroperoxide, dicumyl peroxide, benzoyl peroxide, tert-butyl peroxybenzoate, tert-butyl peroxyethylhexanoate, tert-butyl peroxypivalate, methyl ethyl ketone peroxide, di-tert-butyl peroxide, etc; azo nitriles such as azobisisobutyronitrile, azobisisopropionitrile, etc. In the graft copolymerization using these peroxides, the preferable amount of the peroxide is 0.1 wt. part - 50 wt. parts for polyolefin, or more preferably 0.5 wt. part - 30 wt. parts. The α,β-unsaturated carboxylic acid and/or its acid anhydrides includes, for example, maleic acid, maleic anhydride, fumaric acid, citraconic acid, citraconic anhydride, mesaconic acid, itaconic acid, itaconic anhydride, aconitic acid, aconitic anhydride, etc. These monomers can be used solely, but the combined use of two or more kinds of them results often in better properties of the coating film. The following compounds are listed as a compound having one or more double bonds in a molecule and being used in the modification reaction: monomers of the (meth) acrylic acid type such as (meth)acrylic acid, methyl (meth)acrylate, ethyl (meth)acrylate, propyl (meth)acrylate, butyl (meth)acrylate, 2-hydroxypropyl (meth)acrylate, 4-hydroxybutyl (meth)acrylate, cyclohexyl (meth)acrylate, tetrahydrofurfuryl (meth)acrylate, isobornyl (meth)acrylate, benzyl (meth)acrylate, 2-hydroxybutyl (meth)acrylate, (di)ethylene glycol di(meth)acrylate, 1,4-butanediol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, trimethylolpropane tri(meth)acrylate, glycerin di(meth)acrylate, 2-ethylhexyl (meth)acrylate, lauryl (meth)acrylate, stearyl (meth)acrylate, acrylamide, etc.; monomers of the styrene type such as styrene, α-methylstyrene, p-methylstyrene, chloromethylstyrene, etc. Besides the following monomers of the vinyl type can be used in combination with other monomers: divinylbenzene, vinyl acetate, vinyl ester of versatic acid, etc. In the graft copolymerization with these monomers, one or more kinds of monomers are used; the use of two or more kinds of monomers is desirable. The preferable amount of the monomers used is 0.1 wt. part or more, and 50 wt. parts or less for the polyolefin; or more preferably 0.5 wt. part or more, and 30 wt. parts or less. The acid value of the modified polyolefin is preferably 1 KOH-mg/g - 500 KOH-mg/g, or more preferably 5 KOH-mg/g - 100 KOH-mg/g. When emulsified and neutralized, the polymer itself works as a surfactant if the acid value is appropriate. In the modification reaction, purging with nitrogen has to be done fully in the case of the reaction in the solution system using an organic solvent, for example toluene and/or xylene, and also in the case of the reaction in the heterogeneous dispersion system using a non-solvent, for example water. The chlorinated polyolefin used in this invention can be prepared by a method already known. For example, chlorinated polyolefin is prepared by allowing polyolefin to react with chlorine blown in, the polyolefin being dissolved or dispersed in a solvent for chlorination, under ultraviolet irradiation or in the presence of a catalyst containing a peroxide, for example, benzoyl peroxide, under normal or elevated pressure at a temperature of 50 - 150°C. For the chlorination product (referred to as modified chlorinated polyolefin hereafter) from polyolefin modified with α,β-unsaturated carboxylic acids and/or their acid anhydrides and/or compounds having one or more double bonds in a molecule, all explained above for use in this invention, the degree of chlorination in the range of 5 - 50 wt.% is acceptable; preferably it is 10 - 40 wt.%. For the chlorination degree lower than 5%, the state of the solution becomes worse; for the chlorination degree higher than 50%, adhesiveness to polyolefin-based resins and solvent resistance are lowered. The acid value of chlorinated polyolefins is in the range of 1 to 500, and preferably it is 10-400. The acid value less than 1 causes the solvent resistance to decrease; the acid value greater than 500 results in decrease in the interlayer adhesiveness to the base coat and/or the top coat. After completing chlorination, the modified chlorinated polyolefin is compounded with epoxy compounds or their oligomers for giving heat stability to the modified chlorinated polyolefin. In this invention the compounding weight ratio of a compound having one epoxy group in a molecule and/or its oligomer to the aqueous chlorinated polyolefin-based resin composition is 0.1:100 - 50:100. The compounding ratio less than 0.1 cannot give a sufficient stabilising effect, and that greater than 50 makes lower the adhesiveness to moldings and films of polyolefin-based resins. The use of above-mentioned compounds having an epoxy group and/or their oligomers suppresses a crosslinking reaction caused during storage due to bifunctional epoxy compounds and acid anhydrides or organic acids; this is advantageous. The compound having one epoxy group in a molecule and/or its oligomer used in this invention is one having a good compatibility with chlorinated polyolefins. The following are such compounds: phenyl glycidyl ether, 2-methylphenyl glycidyl ether, tert-butylphenyl glycidyl ether, 4-chlorophenyl glycidyl ether, 4-methoxyphenyl glycidyl ether, 2-biphenyl glycidyl ether, 1-naphthyl glycidyl ether, methyl glycidyl ether, isopropyl glycidyl ether, butyl glycidyl ether, tert-butyl glycidyl ether, 2-ethyl glycidyl ether. These can be used solely, but two or more of them, used mixedly, increase the effect. As already mentioned, the object of this invention is to achieve the following using the aqueous, chlorinated polyolefin-based resin emulsion: (1) removing environmental pollution, (2) achieving an excellent adhesiveness to plastic materials such as a polyolef in base material, and (3) achieving a coating system good at coating film properties such as water resistance, gasohol resistance, etc. Further modification of the modified chlorinated polyolefins obtained above, with α, β-unsaturated carboxylic acids and/or their acid anhydrides and/or compounds having one or more double bonds in a molecule, in the solution system or in the heterogeneous dispersion system, is effective for achieving the object described above. The further modification increases further the polarity of the modified chlorinated polyolefin, and thus facilitates the realization of the object (1) - (3) mentioned above; the improvement in adhesiveness (2) checks penetration of water (moisture) or gasoline from outside the coating system, resulting in improved properties and increased durability of the coating film. Surfactants used in this invention include: nonionic surfactants such as polyoxyethylene alkylphenyl ethers, polyoxyethylalkyls, polyoxyethylene alkylaryl ethers, polyethylenealkyl esters, sorbitan alkyl esters, polyoxyethylene sorbitan alkyl esters, poly(oxyethyleneoxypropylene) block copolymers, etc.; anionic surfactants such as higher alkyl sulfates, alkyl arylpolyoxyethylene ester-salts of sulfuric acid, higher fatty acid salts, alkylarylsulfonic acid salts, alkyl ester-salts of phosphoric acid, etc. As a cationic surfactant, amines with alkoxy groups can be used. Besides emulsifiers of the polymer type or dispersing agents also can be used; the use of these can increase the viscosity in the system and so contributes to stabilization. The typical ones of them which can contribute to the object of this invention are listed below: polymers such as gelatin, tragacanth gum, starch, methylcellulose, carboxymethyl cellulose, hydroxypropylcellulose, hydroxyethylcellulose, etc., and the derivatives of the polymers above; water-soluble organic polymers such as poly(vinyl alcohol), partially saponified poly(vinyl alcohol), ethylene-vinyl alcohol copolymer, ethylene-vinyl alcohol-vinyl acetate copolymer, poly (acrylic acid) salts, etc; dispersing agents such as barium sulfate, calcium sulfate, barium carbonate, calcium carbonate, magnesium carbonate, calcium phosphate, etc.--these are water-insoluble inorganic compounds in the form of fine powder--the mixture of the above compounds, inorganic substances such as talc, bentonite, silicic acid, diatomaceous earth, clay, etc., and metal oxide powders. The anionic, nonionic, and cationic surfactants and the dispersing agents of the polymer type and of the inorganic type, listed above, can be used solely, but the combination use of two or more of them often improves the properties of the coating film. Reactive surfactants also can be used; the anionic and nonionic ones of them are of common use; particularly preferable are ones having a polyoxyethylene group in the molecule as a hydrophilic group; an example of the preferable reactive surfactant is an adduct of alkylpropenyl(di)phenol poly(ethylene oxide) and/or its sulfuric acid ester-salt. The combination of a non-reactive surfactant and a reactive surfactant also can be used, and two or more kinds of surfactants for each of the types also can be used. The preferable amount of the surfactant above or their mixture to be used is 0.01 - 100 wt. parts for 100 wt. parts of the chlorinated polyolefin. In order to obtain the objective emulsion, the modified chlorinated polyolefin has to be emulsified with water. This can be done without addition of surfactants, but, if added, emulsions having better properties can be obtained. An example of the emulsification procedure will be described below. An aqueous solution containing a specified amount of the surfactant is placed in a vessel equipped with an emulsifying device, for example a homomixer, and the modified chlorinated polyolefin is added there slowly to be emulsified. The modified chlorinated polyolefin has to be dissolved in an organic solvent like toluene and/or xylene beforehand or at least has to be swelled or dispersed beforehand, so that the resin can be emulsified and dispersed well in the water; otherwise, the agitating power would not be well transferred into the system and the desirable particle size could not be obtained. In this procedure the organic solvent like toluene and/or xylene remains in the system, so the solvent has to be removed afterwards by concentration under reduced pressure. Of course, it is possible in the emulsification that the modified chlorinated polyolefin and its organic solvent are placed in the vessel first and then the aqueous solution of the surfactant and/or water are added. The addition of a basic substance to the emulsion described above increases the stability of the emulsion, because the basic substance neutralizes the acid components introduced into the polymer and makes the acid components ionized, resulting in stretching of the polymer molecules and thus increasing the viscosity of the system. The pH of the system can be adjusted to a desirable level by adding basic substances. The basic substance to be used are as follows: organic basic substances such as (di)methylamine, (di)ethylamine, (di)propylamine, (di)butylamine, (di)hexylamine, (di)octylamine, (di)ethanolamine, (di)propanolamine, N-methyldiethanolamine, triethylamine, N,N-dimethylethanolamine, 2-dimethylamino-2-methyl-1-propanol, 2-amino-2-methyl-1-propanol, morpholine, etc.; inorganic basic substances such as aqueous ammonia, sodium hydroxide, potassium hydroxide, sodium carbonate, sodium hydrogencarbonate, ammonium carbonate, potassium carbonate, etc. These basic substances can be used solely, but the combination use of two or more of them can achieve the object of this invention more effectively. The preferable amount of the basic substance used for neutralization is 0.1 - 10 wt. parts for the modified chlorinated polyolefin resin, depending upon how far the polyolefin has been modified. As said before, the object of this invention is to achieve the following: (1) removing environmental pollution, (2) achieving an excellent adhesiveness to plastic materials such as the polyolefin base material, and (3) achieving a coating system good at coating film properties such as water resistance, gasohol resistance, etc. In pursuit of the third item above, the two-part curable emulsion which uses the oxazoline polymer is employed in this invention. What is called oxazoline polymer here is an aqueous crosslinking agent having the oxazoline group introduced into the polymer as a pendant. The crosslinking agent is used to cross-link polymers having the carboxyl group and/or the acid anhydride group; it can form the crosslink when it is compounded at an appropriate compounding ratio and the coating film is baked or warmed. The oxazoline polymer is soluble or dispersible in water and has one or more oxazoline groups in its polymer molecule; its main component polymer is of the (meth)acryl type, of the urethane type, and/or of the polyester type, etc. The preferable compounding ratio of the oxazoline polymer to the modified chlorinated polyolefin is in the range of 1:300 - 300:1, and particularly preferably 1:60 - 5:1. The temperature for baking or warming after compounding and application onto the object to be coated, is preferably 70°C - 130°C, and more preferably 80°C - 120°C. A water-soluble weak acid, for example citric acid, may be added as a catalyst to promote the curing reaction. In pursuit of the third item of the object of this invention, i.e., achieving a coating system good at coating film properties such as water resistance, gasohol resistance, the inventors have found that a certain system which, unlike the two-part curable type, does not include the curing reaction can much improve the properties of the coating film: for example, blending with an aqueous polyurethane-based resin or an aqueous polyurethane-based emulsion which has a good compatibility with the modified chlorinated polyolefin can do that. What is called here aqueous polyurethane-based resin or aqueous polyurethane-based emulsion is an aqueous resin or an aqueous emulsion whose base polymer consists mainly of polyurethane. What is called polyurethane here is a reaction product of a compound having the active hydrogen atom and a polyisocyanate, and can be obtained by the already known method, using a chain extender, a reaction-stopping agent and already known various additives as the need arises. As the compound having the active hydrogen atom, high-molecular-weight polyols and polyamines are cited, for example. The high-molecular-weight polyol includes polyetherpolyol, polyesterpolyol, (hydrogenated)polybutadienepolyol, polycarbonatediol, etc; the hydroxyl group equivalent of the high-molecular-weight polyol is generally 200 - 3,000. The preferable low-molecular-weight polyol includes (di)ethylene glycol, 1,4-butanediol, dimethylolpropionic acid, 3-methylpentanediol, 2-ethyl-1,3-hexanediol, etc. As polyamine, cited are hexamethylenediamine, isophoronediamine, diethanolamine, N-hydroxyethylenediamine, 4,4'-diaminodicyclohexylmethane, etc. The sole use of the high-molecular-weight polyol or the combination use of the high-molecular-weight polyol with the low-molecular-weight polyol and/or the polyamine is the usual manner of using these compounds having the active hydrogen atom. As for the polyisocyanate, a variety of already known aromatic, aliphatic, and alicyclic isocyanates can be used. For example, TDI (toluenediisocyanate), MDI (4,4'-diphenylmethanediisocyanate), HDI (hexamethylenediisocyanate), IPDI (isophoronediisocyanate), hydrogenated MDI, and tetramethylxylylenediisocyanate are cited. In the manufacture of polyurethane resins, the quantitative proportion of polyisocyanate to the compound having the active hydrogen atom can be decided arbitrarily, but usually the proportion is in the range from 1:1 to 1:2 as a ratio in the equivalent. The number-average molecular weight of the polyurethane is usually 3,000 - 300,000. In this invention, polyurethane having the carboxyl group and/or the hydroxyl group and/or the isocyanate group in its molecule is particularly effective. There are various methods for making polyurethane aqueous, and many of them are already known. For example, a polyurethane having sodium carboxylate or sodium sulfonate in the molecule is synthesized in the acetone/water system; then the acetone is distilled out. The introduction of a hydrophilic group into the molecule makes the polymer itself more hydrophilic, and the polymer can be well self-emulsified without using surfactants. What is called an aqueous resin of the soap-free type is mostly a resin like this. Thus the total amount of the surfactants in the system can be decreased if the aqueous, chlorinated polyolefin-based resin composition of this invention is blended with and/or is allowed to react with such polyurethane, and good coating film properties can be obtained if the compatibility between both the polymers is good. The aqueous, chlorinated polyolefin-based resin composition of this invention which has been emulsified as described above, is good not only at the adhesiveness to plastic materials of low polarity like polyolefin base materials, but also good at coating film properties such as water resistance and gasohol resistance and also at the stability of the emulsion. In addition the storability is also good. This emulsion can be applied to aqueous coating systems, aqueous adhesives, aqueous inks, etc. In the industrial practice of the aqueous coating like this, vaporization of water often becomes rate-determining. However, the aqueous, chlorinated polyolefin-based resin emulsion of this invention is affinitive to water as a result of having its polarity increased, and in addition it is well miscible with film-forming auxiliaries or vaporization promoters of the alcoholic type and of other types, and it can also be stored for a long time in the practical situation. The typical film-forming auxiliaries or vaporization promoters which are preferably used in this invention are listed below: isopropyl alcohol, ethylene glycol, ethylene glycol monomethyl ether, ethylene glycol monobutyl ether, ethylene glycol monoethyl ether, ethylene glycol-2-ethylhexyl, propylene glycol, propylene glycol monomethyl ether, propylene glycol monobutyl ether, propylene glycol monoethyl ether, propylene glycol-2-ethylhexyl, diethylene glycol, diethylene glycol monomethyl ether, diethylene glycol monobutyl ether, diethylene glycol monoethyl ether, diethylene glycol-2-ethylhexyl, dipropylene glycol, dipropylene glycol monomethyl ether, dipropylene glycol monobutyl ether, dipropylene glycol monoethyl ether, and dipropylene glycol-2-ethylhexyl. The use of one of these compounds or the combination use of two or more of them enables the full development of the various coating properties. 0.1 - 300 wt. parts or particularly preferably 0.5 - 100 wt. parts of these compounds are used for the aqueous, chlorinated polyolefin-based resin emulsion, being mixed with the emulsion. Besides following additives can be added to the aqueous, chlorinated polyolefin-based resin composition of this invention: organic and/or inorganic pigments and/or dyes, thickeners, antisagging agents, thixotropy agents, viscosity-adjusting agents, antifoamers, weatherizing agents, ultraviolet absorbers, antimolds, stabilizers, and other aqueous coatings and/or aqueous emulsions such as aqueous polyurethanes, aqueous acrylic resins, aqueous epoxy resins, aqueous amino resins, aqueous silicone resins, etc. To further illustrate the present invention, and not by way of limitation, the following examples are given. [Example 1] Two hundred eighty kilograms of isotactic polypropylene (Mw = about 30,000), 5.0g of acrylic acid, 16.8g of maleic anhydride, 5.6g of dicumyl peroxide and 420g of toluene were added in an autoclave equipped with a stirrer. After 5-minute displacement of the air with nitrogen, the mixture was allowed to react at 140°C for 5 hours with heating and stirring. (Hereafter, this step is referred as Graft Polymerization 1). After the reaction completed, the reaction mixture was put into a large amount of methyl ethyl ketone to precipitate a resin. The resultant resin was then washed several times with methyl ethyl ketone to remove unreacted monomers, and dried fully at 60°C under reduced pressure of 10 torr 1333.2 Pa. One hundred grams of the resultant acid-modified resin and 900g of tetrachloroethylene were added in a four-neck flask. After about five-minute displacement of the air with nitrogen, the resin was heated to 110°C and fully dissolved. One gram of di- tert -butyl peroxide was then added and gaseous chlorine was bubbled. After 3-hour bubbling with 63g of gaseous chlorine, the nitrogen gas was bubbled to remove unreacted gaseous chlorine and hydrochloride. After the solvent, tetrachloroethylene, was evaporated with an evaporator, toluene was added alternatively to obtain 20wt% solution in toluene of acid-modified, chlorinated polyolefin (Acid Value = 50mg KOH/g; Chlorine content = 22.2wt%; and Mw = 25,000). Denacol EX-141 (phenyl glycidyl ether, an epoxy compound with an epoxy equivalent of 154, available from Nagase Kasei Kogyo Co. Ltd.) was added to the resultant composition, i.e. the above-described 20wt% solution in toluene, in an amount of 4wt% based on the resin, and stirred fully. One hundred grams of the above-described 20.6wt% solution in toluene was put in a flask. Separately, 1.0g of Neocol P (an anionic surfactant available from Daiichi Kogyo Seiyaku Co. Ltd.) and 1.0g of Neugen EA-190D (a non-ionic surfactant available from Daiichi Kogyo Seiyaku Co. Ltd.) were put in another flask. One-hundred grams of deionized water was then added in the flask to dissolve the mixture fully at 50°C. The solution in toluene and the surfactant solution were combined and stirred in an emulsifier at 20, 000rpm for 5 minutes to obtain a pre-emulsion. The particle size determination for the pre-emulsion showed a 50% particle size of 0.22µm with a degree of dispersion of 1.0; where, the degree of dispersion is given by the following equation, Degree of dispersion =(90% particle size)*(10% particle size)/(50% particle size). The pre-emulsion was adjusted to pH 8 with 25% aqueous ammonium and then put in an one-litter evaporation flask with 50g of deionized water. Toluene in the system was evaporated under reduced pressure of 100-200 torr (13332.2 - 26664.4 Pa) with an evaporator while the temperature of the pre-emulsion was maintained at 45°C. The remaining portion was cooled to 25°C, filtered through a #400-mesh metal strainer to remove a trace amount of emulsified materials and undissolved matters with a diameter of about fifty micrometers or more. This gave an emulsion of an aqueous, chlorinated polyolefin resin having a pH value of 7.8, a solid content of 20.2wt%, a 50% particle size of 0.24µm with a degree of dispersion of 1.1, and no residual toluene. [Example 2] Two hundred eighty kilograms of isotactic polypropylene (Mw = 50,000), 6.8g of maleic anhydride, 5.6g of dicumyl peroxide and 420g of toluene were added in an autoclave equipped with a stirrer. After 5-minute displacement of the air with nitrogen, the mixture was allowed to react at 140°C for 5 hours with heating and stirring. After the reaction completed, the reaction mixture was put into a large amount of acetone to precipitate a resin. The resultant resin was then washed several times with acetone to remove unreacted monomers, and dried fully at 60°C under reduced pressure of 10 torr (1333.2 Pa). One hundred grams of the resultant acid-modified resin and 1,000g of tetrachloroethylene were added in a four-neck flask. After about five-minute displacement of the air with nitrogen, the resin was heated to 110°C and fully dissolved. One gram of di- tert -butyl peroxide was then added and gaseous chlorine was bubbled. After 3-hour bubbling of 80g of gaseous chlorine, the nitrogen gas was bubbled to remove unreacted gaseous chlorine and hydrochloride. After the solvent, tetrachloroethylene, was evaporated with an evaporator, toluene was added alternatively to obtain a 20wt% solution in toluene of acid-modified chlorinated polypropylene (Acid value = 60mg KOH/g; chlorine content = 24.1wt%; and Mw = 48,000). Denacol EX-141 (phenyl glycidyl ether available from Nagase Kasei Kogyo Co. Ltd.) was added to the resultant composition, i.e. the 20wt% solution in toluene, in an amount of 4wt% based on the resin, and stirred fully. The above-described 20.5wt% solution in toluene was transferred into a flask equipped with a stirrer, a dropping funnel, a condenser, a thermometer and a nitrogen introduction tube. One gram of benzoyl peroxide, 2.5g of methacryl acid and a previously well-dissolved mixture of 1.5g of 2-ethylhexyl methacrylate and 10g of toluene were added in the funnel. After about five-minute displacement of the air with nitrogen, the mixture in the flask was heated to 90°C and then the content in the funnel was dropped into it at a constant rate over 3 hours with heating and stirring. The reaction mixture was then allowed to react for 5 hours at 90°C. (Hereafter, this reaction is referred as Graft Polymerization 2.) The resultant reaction mixture was diluted with toluene to prepare 20wt% solution. Separately, 2 g of Neugen EA-190D (a non-ionic surfactant available from Daiichi Kogyo Seiyaku) was put in another flask, and 100g of deionized water was then added to dissolve fully at 50°C. The above-described solution in toluene and the surfactant solution were combined and stirred in an emulsifier at 20,000rpm for 5 minutes to obtain a pre-emulsion. The particle size determination for the pre-emulsion showed a 50% particle size of 0.22µm with a degree of dispersion of 1.3. The pre-emulsion was adjusted to pH 9 with morpholine and then put in a one-litter evaporation flask with 50g of deionized water to evaporate toluene under reduced pressure, as described in Example 1. The resultant mixture was cooled to 25°C and filtered through a #400-mesh metal strainer to remove a trace amount of unemulsified and undissolved matters with a size of about fifty micrometers or more. This gave an emulsion of an aqueous, chlorinated polyolefin resin having a pH value of 8.5, a solid content of 19.8wt%, a 50% particle size of 0.19 µm with a degree of dispersion of 0.9, and no residual toluene. [Examples 3 - 15] Emulsions in water of chlorinated polyolefin were prepared in the same way as described in Example 1 or 2, except that the components and their amount shown in Table 1 were used for Graft Polymerization 1 or 2. [Example 16] One hundred grams of the emulsion of the aqueous, chlorinated polyolefin resin (20.2% resin solids) obtained in Example 1 and 100g of NeoRez R972 (an aqueous urethane resin containing 20% resin solids, available from Zeneca Co. Ltd.) were mixed well. 4.9g of EpoCross WS-500 (an oxazoline-group containing, water-soluble polymer containing 40% resin solids, available from Nihon Shokubai Co. Ltd.) was added to the mixture and stirred well to prepare a resin blend composition consisting of the emulsion of the aqueous, chlorinated polyolefin resin, the aqueous urethane resin, and the oxazoline-group containing, water-soluble polymer. [Examples 17 - 30] Resin blend compositions were prepared in the same way as described in Example 16, except that the composition shown in Table 2 was used to blend an aqueous urethane resin and/or an acrylic emulsion and an oxazoline-group containing, water-soluble polymer. [Example 31] One hundred grams of the emulsion of the aqueous, chlorinated polyolefin resin (20.2% resin solids) obtained in Example 1 and 100g of NeoRez R972 (an aqueous urethane resin adjusted to 20wt% resin solids, available from Zeneca Co. Ltd.) were mixed well and then 15.5g of NeoRez 990 (an aqueous, isocyanate block containing urethane having 35wt% resin solids, available from Zeneca Co. Ltd.) was added. The mixture was stirred well to prepare a resin composition consisting of the emulsion of the aqueous, chlorinated polyolefin resin, the aqueous urethane resin and the aqueous urethane resin containing blocks of isocyanate groups. [Comparative Examples 1 - 5] Emulsions of aqueous, chlorinated polyolefin resins were synthesized in the same way as described in Example 1 or 2, except that the components and their amount shown in Table 1 were used. The following physical properties of the resultant emulsions were measured. The results are shown in Table 3. Chemical formula 1 2 6 3 4 5 7 8 9 10 1 2/25 X ( 0/25) × × × × × 2 0/25 " × × × × × 3 1/25 " × × × × × 4 2/25 " × × × × × 5 5/25 " × × × × × 6 2/2 5 " × × × × × 7 0/25 " × × × × × 8 2/25 " × × × × × 9 0/25 " × × × × × 10 0/25 " × × × × × 11 2/25 " × × × × × 1 Example No. 2 Coating Film Characteristics 3 Adhesion 4 Moisture resistance 5 Gasohol resistance 6 Emulsion Characteristics 7 High-temperature stability 8 Low-temperature stability 9 Grain 10 Dilution stability 1 Comparative Example No. 2 Moisture resistance: ○: Good (No change observed) ; × : No good (Lots of blisters) Gasohol resistance: ○: Good (No change observed); × : No good (Separation observed) (Table 3] (1) Adhesion: The surface of polypropylene plates (made by forming Mitsui Noblene SB-E3 under pressure into 100mm×50mm size and 2mm thickness according to a predetermined method) was cleaned with isopropyl alcohol and coated with each of the compositions obtained in Examples 1 to 12 and Comparative Examples 1 to 5 with an air spray gun (F-88 type available from Meiji Kikai Seisakusho Co. Ltd.). The plates were dried at 80°C for 30 minutes and allowed to cool at room temperature. The base agent and curing agent of a two-part urethane paint (Rethane PG-80 available from Kansai Paint Co. Ltd.) were mixed at a weight ratio of 100:25. After a thinner was then mixed so that the coating amount could be 50 - 60 g/m 2 , the mixture was applied onto the plate surface with an air spray gun. The plates were then dried at 120°C for 30 minutes and allowed to cool to room temperature and to stand for 24 hours for subsequent testing. The plates were evaluated in the following procedure: On the surface of each plate, grooves reaching the plate itself were made to prepare 25 lattices. A cellophane adhesive tape was applied onto the lattices and then peeled at a right angle to the coating surface. The number of lattices remained was counted. (2) Moisture resistance: Polypropylene plates were coated in the same way as described in (1). After the plates were dipped in portable water maintained at 40°C for 240 hours, the appearance of the coatings on one side of the coated pieces was investigated. At the same time, the plates were was evaluated for adhesion in the same way as described in (1). (3) Gasohol resistance: Polypropylene plates were coated in the same way as described in (1). After the plates were dipped in gasohol (a 90wt%:10wt% mixture of regular gasoline and ethanol) maintained at 20°C for 10 minutes, the condition of the coatings thereon was investigated. (4) High-temperature stability of emulsion: The 50% particle size of the water-based compositions with a resin content of 20wt% was determined before and after they were allowed to stand for 6 months in a thermostat at 40°C. The ratio of the size before treatment to that after treatment, i.e., (50% particle size after 6 months)/(50% particle size immediately after production), was calculated. (○ = 0.9 - 1.1; Δ = 1.2 - 2.0; and × = 2 or more.) (5) Low-temperature stability of emulsion: The 50% particle size of the water-based compositions with a resin content of 20wt% was determined before and after they were allowed to stand for 1 month in a thermostat at 40°C. The ratio of the size before treatment to that after treatment, i.e., (50% particle size after 6 months)/(50% particle size immediately after production), was calculated. (○ = 0.9 - 1.1; Δ = 1.2 - 2.0; and × = 2 or more.) (6) Grain(s): The water-based compositions with a resin content of 20wt% were allowed to stand for 1 month in a thermostat at 40°C. The resultant compositions were investigated with a grain gauge tester (available from Taiyu Kizai Co. Ltd.) according to JIS K5400. (○ means that the composition contained no grain with a diameter of 40 µm or more and less than 5 grains with a diameter of less than 40µm; Δ means that the composition contained at least one grain with a diameter of 40µm or more and at least 5 grains with a diameter of less than 40µm; and × means that the composition contained at least one grain with a diameter of 40µm or more and at least 5 grains with a diameter of less than 40µm.) (7) Stability upon propylene glycol dilution: Twenty grams of propylene glycol was added gradually to each of the water-based compositions with a resin content of 20wt% with stirring in a thermostat at 25°C to prepare a homogeneous blend. The resultant blends were allowed to stand therein for 1 month. At the end of the storage period, each blend was taken from the thermostat to investigate the appearance and particle size. The ratio of the size before treatment to that after treatment, i.e., (50% particle size after 1 month)/(50% particle size immediately after production), was calculated. (○ = 0.9 - 1.1; Δ = 1.2 - 2.0; and × = 2 or more.) [Comparative Examples 6 - 10] Resin blend compositions were prepared in the same way as described in Example 16, except that an oxazoline-group containing polymer was used according to the composition shown in Table 3. [Comparative Example 11] A resin blend composition was prepared in the same way as described in Example 31, except that an aqueous, isocyanate block containing urethane was included according to the compositions shown in Table 2. The water-based emulsion of the aqueous, chlorinated polyolefin resin composition according to the present invention is excellent in adhesion to molded plastic products or films containing a polyolefin, such as polypropylene, and having a low-polarity surface. It is also excellent in other coating characteristics, such as moisture resistance and gasohol resistance, and in emulsion stability. In addition, it is excellent not only in compatibility with oxazoline-group containing polymers, curing agents, such as aqueous, isocyanate block containing urethanes, or other aqueous resins, but also in stability upon the addition of a film-forming co-agent, such as propylene glycol monomethyl ether, or an evaporation facilitating co-agent is added, and during storage. Therefore, the emulsion according to the present invention can provide a better coating film than the water-based compositions of the prior art used for paints and primers therefor as well as coatings containing adhesives and primers therefor for molded plastic products or films containing polyolefin, such as polypropylene, and having a low-polarity surface. In addition, the emulsion of the present invention is remarkably excellent from the viewpoint of environmental protection, safety and health, because it contains no organic solvent, including aromatic solvents, such as toluene and xylene.

Claims: An aqueous, chlorinated polyolefin-based resin composition which has an add value of 1-500mg KOH/g and which is obtained by chlorination to a percentage by weight of chlorine in the range of 5-50% of one or more kinds of polymers selected from polyolefins modified with one or more of the following compounds (A), (B) and (C): (A) α, β-unsaturated carboxylic acids represented by any of the formulae I, II and III below wherein each of R 1 , R 2 , R 3 , R 4 and R 5 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 and -COOH, and wherein R 8 is selected from CH 2 , C 2 H 4 , C 3 H 6 , C 4 H 8 , C 5 H 10 , C 6 H 12 , C 7 H 14 , C 8 H 16 , C 9 H 18 , C 10 H 20 , CHCOOH, C(CH 3 )COOH, C(C 2 H 5 )COOH, C(C 3 H 7 )COOH and C(C 4 H 9 )COOH; (B) acid anhydrides of α, β-unsaturated carboxylic acids of (A), represented by either of the formulae IV and V below in which R 6 and R 7 are each independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 ; in which R 8 which is connected to the ring carbon atom by an ethylenic double bond, is selected from -CH 2 , -C 2 H 4 , -C 3 H 6 , -C 4 H 8 , -C 5 H 10 , -C 6 H 12 , -C 7 H 14 , -C 8 H 16 , -C 9 H 18 , -C 10 H 20 ,-CHCOOH, -C(CH 3 )COOH, -C(C 2 H 5 )COOH, -C(C 3 H 7 )COOH and -C(C 4 H 9 )COOH; and R 9 is selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 ; and (C) compounds having one or more double bonds in a molecule, represented by either of the formulae VI or VII below (VI) CH 2 =C(R 10 )COOR 11 in which R 10 is H or -CH 3 and R 11 is selected from CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 , -C 11 H 23 , -C 12 H 25 , -C 13 H 27 , -C 14 H 29 , -C 15 H 31 , -C 16 H 33 , -C 17 H 35 , in which R 10 is H or- CH 3 and R 11 is selected from CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 , -C 11 H 23 , -C 12 H 25 , -C 13 H 27 , -C 14 H 29 , -C 15 H 31 , -C 16 H 33 , -C 17 H 35 , -C 18 H 37 , -C 19 H 39 , -C 20 H 41 , -C 2 H 4 OH, -C 3 H 6 OH, -C 4 H 9 OH, -C 5 H 10 OH, -C 6 H 12 OH, -C 7 H 14 OH, -CH 2 CH 2 N(CH 3 ) 2 , -CH 2 CH 2 N(CH 2 CH 3 ) 2 , -CH 2 CH 2 OCOCH 2 CH 2 COOH, -CH 2 CH 2 OCOC(CH 3 )=CH 2 , -(CH 2 CH 2 O) 2 COC(CH 3 )=CH 2 , -C 4 H 8 OCOC(CH 3 )=CH 2 , -C 6 H 12 OCOC(CH 3 )=CH 2 , -CH 2 C(CH 2 =C(R 1 )COOCH 2 ) 2 CH 2 CH 3 , -CH 2 CH(OH)CH 2 OCOC(CH 3 )=CH 2 , (CH 2 CH 2 O) x COC(CH 3 )=CH 2 ; 1≤ × ≤20 in which each of R 12 , R 13 , R 14 , R 15 and R 16 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 , wherein the aqueous, chlorinated polyolefin-based composition obtained by chlorination is compounded with an epoxy compound having one epoxy group in a molecule or its oligomer after the completion of chlorination so that the weight ratio of (the compound having one epoxy group in a molecule and/or its oligomer) to (the aqueous, chlorinated polyolefin-based resin composition) is 0.1:100 - 50:100, and wherein the epoxy compound is selected from phenyl glycidyl ether, 2-methylphenyl glycidyl ether, tert-butylphenyl glycidyl ether, 4-chlorophenyl glycidyl ether, 4-methoxyphenyl glycidyl ether, 2-biphenyl glycidyl ether, 1-naphthyl glycidyl ether, methyl glycidyl ether, isopropyl glycidyl ether, butyl glycidyl ether, tert-butyl glycidyl ether, 2-ethyl glycidyl ether. The aqueous, chlorinated polyolefin-based resin composition of claim 1 wherein polar groups are introduced into the chlorinated polyolefin obtained in claim 1, by further modifying it with one or more of the compounds (A), (B) and (C), as defined in claim 1, in a solution system using an organic solvent or in a heterogeneous dispersion system using a non-solvent. The aqueous, chlorinated polyolefin-based resin composition of claim 1 or 2 wherein, as the main constituents, α, β-unsaturated carboxylic acids represented by any one of the general formulae I, II or III and/or their acid anhydrides represented by either of general formulae IV or V are contained in the chlorinated polyolefin composition in an amount between 0.01 wt.% and 60 wt.%. The aqueous, chlorinated polyolefin-based resin composition of any one of claims 1 to 3 wherein, in preparation of the aqueous, chlorinated polyolefin-based resin composition, as the main constituents, compounds having one or more double bonds in a molecule, represented by either of general formulae VI or VII are contained in the chlorinated polyolefin composition in an amount between 0.01 wt.% and 60 wt.%. A process for the manufacture of an aqueous, chlorinated polyolefin-based resin composition which has an acid value of 1-500mg KOH/g, which process comprises chlorinating to a percentage by weight of chlorine in the range of 5-50% one or more kinds of polymers selected from polyolefins modified with one or more of the following compounds (A), (B) and (C): (A) α, β-unsaturated carboxylic acids represented by any of the formulae I, II and III below wherein each of R 1 , R 2 , R 3 , R 4 and R 5 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 and -COOH, and wherein R 8 is selected from CH 2 , C 2 H 4 , C 3 H 6 , C 4 H 8 , C 5 H 10 , C 6 H 12 , C 7 H 14 , C 8 H 16 , C 9 H 18 , C 10 H 20 , CHCOOH, C(CH 3 )COOH, C(C 2 H 5 )COOH, C(C 3 H 7 )COOH and C(C 4 H 9 )COOH; (B) acid anhydrides of α, β-unsaturated carboxylic acids of (A), represented by either of the formulae IV and V below in which R 6 and R 7 are each independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 ; in which R 8 which is connected to the ring carbon atom by an ethylenic double bond, is selected from -CH 2 , -C 2 H 4 , -C 3 H 6 , -C 4 H 8 , -C 5 H 10 , -C 6 H 12 , -C 7 H 14 , -C 8 H 16 , -C 9 H 18 , -C 10 H 20 ,-CHCOOH, -C(CH 3 )COOH, -C(C 2 H 5 )COOH, -C(C 3 H 7 )COOH and -C(C 4 H 9 )COOH; and R 9 is selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 ; and (C) compounds having one or more double bonds in a molecule, represented by either of the formulae VI or VII below (VI) CH 2 =C(R 10 )COOR 11 in which R 10 is H or -CH 3 and R 11 is selected from CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 , -C 11 H 23 , -C 12 H 25 , -C 13 H 27 , -C 14 H 29 , -C 15 H 31 , -C 16 H 33 , -C 17 H 35 , -C 18 H 37 , -C 19 H 39 , -C 20 H 41 , -C 2 H 4 OH, -C 3 H 6 OH, -C 4 H 9 OH, -C 5 H 10 OH, -C 6 H 12 OH, -C 7 H 14 OH, -CH 2 CH 2 N(CH 3 ) 2 , -CH 2 CH 2 N(CH 2 CH 3 ) 2 , -CH 2 CH 2 OCOCH 2 CH 2 COOH, -CH 2 CH 2 OCOC(CH 3 )=CH 2 , -(CH 2 CH 2 O) 2 COC(CH 3 )=CH 2 , -C 4 H 8 OCOC(CH 3 )=CH 2 , -C 6 H 12 OCOC(CH 3 )=CH 2 , -CH 2 C(CH 2 =C(R 1 )COOCH 2 ) 2 CH 2 CH 3 , -CH 2 CH(OH)CH 2 OCOC(CH 3 )=CH 2 , (CH 2 CH 2 O)COC(CH 3 )=CH 2 ; 1≤ × ≤20 in which each of R 12 , R 13 , R 14 , R 15 and R 16 is independently selected from H, -CH 3 , -C 2 H 5 , -C 3 H 7 , -C 4 H 9 , -C 5 H 11 , -C 6 H 13 , -C 7 H 15 , -C 8 H 17 , -C 9 H 19 , -C 10 H 21 , wherein the process further comprises compounding the aqueous, chlorinated polyolefin-based composition with an epoxy compound having one epoxy group in a molecule or its oligomer after the completion of chlorination so that the weight ratio of (the compound having one epoxy group in a molecule and/or its oligomer) to (the aqueous, chlorinated polyolefin-based resin composition) is 0.1:100 - 50:100, and wherein the epoxy compound is selected from phenyl glycidyl ether, 2-methylphenyl glycidyl ether, tert-butylphenyl glycidyl ether, 4-chlorophenyl glycidyl ether, 4-methoxyphenyl glycidyl ether, 2-biphenyl glycidyl ether, 1-naphthyl glycidyl ether, methyl glycidyl ether, isopropyl glycidyl ether, butyl glycidyl ether, tert-butyl glycidyl ether, 2-ethyl glycidyl ether. A process according to claim 5, further comprising adding a polymer containing oxazoline in an amount between 0.01 wt.% and 60 wt.% during preparation of or after preparation of the aqueous, chlorinated polyolefin-based resin composition. A process according to claim 6, further comprising adding, during preparation of the aqueous chlorinated polyolefin-based resin composition, 0.01-20 wt. parts of an organic or inorganic basic substance for 100 wt. parts of the chlorinated polyolefins to neutralise with the organic or inorganic basic substance the aqueous, chlorinated polyolefin-based resin composition so as to have a pH value in the range of 5-10. A process according to claim 6 or 7, further comprising adding, during preparation of the aqueous chlorinated polyolefin-based resin composition, 0.01-100 wt. parts per 100 parts of base resin of a nonionic surfactant and/or an anionic or cationic surfactant for emulsification. A process according to any one of claims 5 to 8, further comprising adding, during preparation of or after preparation of the aqueous chlorinated polyolefin-based resin composition, an aqueous polyurethane-based resin having an hydroxyl group and/or a carboxyl group and/or an isocyanate group in its molecule or having no functional group, or the emulsion of said aqueous polyurethane-based resin in an amount between 0.01 wt. part and 2000 wt. parts.

Inventors: ASHIHARA TERUAKI, FUNASAKA TADANOBU, MAEKAWA SOJI, ORITA RYOZO, ASHIHARA, TERUAKI, FUNASAKA, TADANOBU, MAEKAWA, SOJI, ORITA, RYOZO, Ashihara, Teruaki, c/o Toyo Kasei Kogyo Co., Ltd., Funasaka, Tadanobu, c/o Toyo Kasei Kogyo Co., Ltd., Maekawa, Soji, c/o Toyo Kasei Kogyo Co., Ltd., Orita, Ryozo, c/o Toyo Kasei Kogyo Co., Ltd.
Applicants: TOYO KASEI KOGYO CO LTD, TOYO KASEI KOGYO COMPANY LIMITED
Application year: 1998
Main classification: C09D151
IPC codes: C08F287, C08F8, C08F255, C08L51, C08L23