Method for preparing a polymeric composition

Abstract

A method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer, which comprises polymerizing at least one radical polymerizable vinyl monomer in an aqueous medium polymerization system comprising an inorganic compound dispersed in the presence of an organic acid monomer or organic acid salt monomer, by using a radical polymerization initiator.

Description

The present invention relates to a novel method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer.

Heretofore, there have been active researches for the development of composite materials, wherein two or more materials are combined to mutually complement the properties of the respective materials to present a new useful function. In recent years, an attention has been drawn not only to mere application of an inorganic compound powder to a composite material as a filler, but also to a composite material such as a ceramic material, a magnetic material or a dental material, wherein a powder of an inorganic compound having a high level of function imparted thereto is combined with an organic polymer. However, in this case, the materials to be combined are mutually substantially different in their properties, and the interfacial affinity such as the compatibility or adhesion is poor. Thus, such a combination has inherent drawbacks such that the effectiveness of the combination can not adequately be improved, and the function of the inorganic compound powder itself can hardly adequately be utilized.

Various methods for modifying the surface properties of a powder have been proposed to overcome these drawbacks, to improve the interfacial affinity of the inorganic compound with the organic polymer substance and to attain high packing density, uniform dispersion and high strength. For instance, there may be mentioned a mechano-chemical method in which an inorganic compound is pulverized in the presence of a reactive monomer, followed by grafting an organic polymer, or a radiation method wherein an inorganic substance is irradiated with a high-energy radiation to be grafted with an organic polymer. These methods, however, require a grinding step or installation of a radiation equipment, resulting in complication of the manufacturing process and increase of the manufacturing cost, and present difficult problems for the practicability of the process.

Further, as an example for the surface modification of a powder in which an in situ polymerization for microcapsulation is employed, the present inventors have previously proposed a method for firmly consolidating an inorganic compound and an organic polymer, wherein a radical polymerizable vinyl monomer and an inorganic compound as a third component are contacted in the presence of a certain specific organic acid monomer or organic acid salt monomer (U.S. Pat. No. 4,435,540, issued on Mar. 6, 1984). However, this method is based on the non-catalytic polymerization of the vinyl monomer by the contact of the specific organic acid monomer or organic acid salt monomer with the inorganic compound, and thus has a problem that the degree of polymerization of the monomer and the graft rate i.e. the ratio of the organic polymer firmly consolidated to the formed polymer, are not necessarily adequate. Further, the applicable vinyl monomer is restricted to the one composed mainly of methyl acrylate or methyl methacrylate, and thus has a drawback that the useful monomer is rather limited.

It is an object of the present invention to provide a polymeric composition in which an organic polymer is uniformly and firmly bonded to the surface of an inorganic compound with a remarkably high degree of polymerization and graft rate.

The present invention provides a method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer, which comprises polymerizing at least one radical polymerizable vinyl monomer in an aqueous medium polymerization system comprising an inorganic compound dispersed in the presence of an organic acid monomer or organic acid salt monomer, by using a radical polymerization initiator.

Now, the present invention will be described in detail with reference to the preferred embodiments.

The organic acid monomer or organic acid salt monomer is preferably a sulfonic acid monomer or sulfonate monomer of the formula: ##STR1## wherein R.sub.1 is a hydrogen atom, a C.sub.1 -C.sub.20 alkyl group or a halogen atom, X is --CONH--, ##STR2## (wherein each of R.sub.2 and R.sub.3 is a hydrogen atom or a C.sub.1 -C.sub.15 alkyl group, and R.sub.4 is a C.sub.1 -C.sub.15 alkylene group), --COO(CH.sub.2m (wherein m is an integer of 1 to 20) or CH.sub.2n (wherein n is an integer of 0 to 20), and Y is a hydrogen atom, an ammonium radical or an alkali metal atom; or a carboxylic acid monomer or carboxylate monomer of the formula: ##STR3## wherein each of R.sub.5 and R.sub.6 is a hydrogen atom, a C.sub.1 -C.sub.15 alkyl group or --COOA (wherein A is a hydrogen atom, an ammonium radical or an alkali metal atom), R.sub.7 is a hydrogen atom or a C.sub.1 -C.sub.15 alkyl group, Z is a hydrogen atom, an ammonium radical or an alkali metal atom, and each of R.sub.8 and R.sub.9 is a hydrogen atom or a C.sub.1 -C.sub.15 alkyl group.

A feature of the present invention is that the interaction between the surface of the inorganic compound and the polymer formed according to the method of the present invention, is derived from a firmly consolidated chemical bond beyond simple adsorption or physical adhesion by e.g. van der Waals adsorption.

Referring to a specific manner for carrying out the present invention, an inorganic compound is suspended and dispersed in an aqueous medium at a temperature within a range in which a radical polymerization initiator decomposes, and an organic vinyl monomer, a specific organic acid monomer or organic acid salt monomer and a radical polymerization initiator are added and stirred to conduct aqueous heterogeneous polymerization, whereupon a copolymer of the vinyl monomer with the organic acid monomer or organic acid salt monomer is uniformly and firmly bonded to the surface of the inorganic compound with a high degree of polymerization and graft rate in a predetermined period of polymerization.

In this case, if a usual dispersant such as a polyanion is used, the effect of the present invention can not be obtained.

The sulfonic acid monomer or sulfonate monomer of the formula I is required to have a double bond as an active site attributable to the polymerizability by a radical polymerization initiator and a sulfonic acid group as an active site which brings about a firm consolidation by the interaction with hydroxyl groups present on the surface of the inorganic compound and the resulting polymer. Any compound having a structure containing these functional groups can be employed. For instance, there may be employed 2-acrylamido-2-methylpropanesulfonic acid (hereinafter referred to simply as AMS), sodium 2-methacryloylethanesulfonate (hereinafter referred to simply as SEM-Na), sodium 3-methacryloylpropanesulfonate (hereinafter referred to simply as SPS), sodium 2-propenesulfonate (hereinafter referred to simply as NaAS) and sodium 2-methyl-2-propenesulfonate (hereinafter referred to simply as NaMS). Among them, particularly preferred are AMS containing an amide linkage and SEM-Na and SPS containing an ester linkage, as they have high polymerization activities and graft efficiency (i.e. efficiency for firm consolidation of the formed polymer).

The carboxylic acid monomer or carboxylate monomer of the formulas II and III, is required to have a double bond as an active site attributable to the polymerizability by a radical polymerization initiator and a carboxylic acid group as an active site which brings about a firm consolidation by the interaction with hydroxyl groups present on the surface of the organic compound and the formed polymer. Any compound having a structure containing these functional groups may be employed. For instance, there may be mentioned acrylic acid, methacrylic acid, crotonic acid, tiglic acid, cinnamic acid, maleic anhydride and citraconic anhydride. Among them, particularly preferred are acrylic acid, methacrylic acid, crotonic acid and maleic anhydride, as they have high polymerization activities and graft efficiency (i.e. efficiency for firm consolidation of the formed polymer).

As the inorganic compound to be used in the present invention, a carbide, nitride or boride of silicon or zirconium, or zirconium oxide is particularly preferred, in view of remarkable effects for the activation of the vinyl monomer and for the firm consolidation with the polymer.

As the vinyl monomer to be used in the present invention, any conventional radical polymerizable vinyl monomer may be employed.

As the radical polymerization initiator to be used in the present invention, any conventional peroxide or azo compound may be employed. However, a radical polymerization initiator which is decomposable at a temperature within a range of from 40.degree. to 100.degree. C. is particularly useful. Among them, particularly preferred from the viewpoint of the graft rate are peroxides such as benzoyl peroxide, azobisisobutyronitrile and potassium persulfate, and azo compounds. Now, the present invention will be described in further detail with reference to Examples. However, it should be understood that the present invention is by no means restricted by these specific Examples. In the Examples and Comparative Examples, the term "parts" means "parts by weight" unless otherwise specified.

EXAMPLE 1 and COMPARATIVE EXAMPLES 1 to 5

In a 1000 ml four-necked flask equipped with a condensor, a nitrogen inlet, a stirrer and a thermocouple for detecting the internal temperature, 270.0 g of silicon nitride, used as the inorganic compound, was suspended in 700 ml of deionized water to form a dispersion. After flushing the flask with nitrogen for 30 minutes, 28.0 g of methyl methacrylate, used as the vinyl monomer, was added to the dispersion with vigorous stirring under a nitrogen stream. Then, the above reaction mixture was heated to 70.degree. C. in a warm water bath. After confirming the uniform dispersion of the added monomer, a solution of 10.0 g of SEM-Na as the sulfonate monomer in 20 ml of deionized water and a solution of 1.0 g of benzoyl peroxide as the radical initiator in 2.0 g of methyl methacrylate, were gradually added thereto. The mixture was reacted for polymerization at the same temperature for 8 hours. After completion of the polymerization, about 5 g of the reaction mixture was sampled. The sample was tested for the amount of the remaining unreacted monomer by gas chromatography using dioxane as internal standard, and the conversion was obtained.

Further, the polymeric composition after the reaction was thoroughly dried at 105.degree. C. for one day and night, and then about 5 g of the composition was completely burned at 650.degree. C. for 3 hours, whereupon the amount of the polymer consolidated to the inorganic compound was calculated from the weight reduction. Then, the consolidation rate was obtained in accordance with the following formula: ##EQU1##

For the purpose of comparison, similar polymerization operation and evaluation after the polymerization were conducted with respect to the polymerization behavior in the cases where the radical initiator was omitted as in the conventional non-catalytic polymerization system, the sulfonic acid monomer or sulfonate monomer was not added, and a dispersant was added. The results are shown in Table 1.

TABLE 1__________________________________________________________________________ Radical polymeri- Inorganic Sulfonate zation Vinyl compound monomer initiator monomer Silicon Dispersant Deionized Conversion Consolida- SEM-Na BPO MMA nitride Sodium hexa- water of monomer tion rate (parts)*1 (parts) (parts) (parts)*2 metaphosphate (parts) (%) (%)*3__________________________________________________________________________Example 1 10.0 1.0 30.0 270.0 -- 720 -100 96Comparative 10.0 -- 30.0 270.0 -- 720 71 88Example 1Comparative -- 1.0 30.0 270.0 -- 720 90 4Example 2Comparative 10.0 1.0 30.0 270.0 3.0 720 95 45Example 3__________________________________________________________________________ *1: CH.sub.2C.CH.sub.3COOC.sub.2 H.sub.4SO.sub.3 Na *2: Special grade reagent ##STR4## BPO: Benzoyl peroxide, MMA: Methyl methacrylate

It is evident from Table 1 that in the system of Comparative Example 2 wherein no sulfonic acid monomer or sulfonate monomer was added, the consolidation rate was very poor although a high conversion was obtainable, and a tendency for the separation of the inorganic compound and the homopolymer was observed. Further, it is evident that as compared with Comparative Example 1, the method of the present invention (Example 1) wherein a radical polymerization initiator was added, is superior in both the conversion of monomer and the consolidation rate. Further, in the system of Comparative Example 3 wherein a dispersant was added, the consolidation rate was substantially low, and a tendency for the separation of the homopolymer was observed as in the case of Comparative Example 2.

The polymeric compositions of Example 1 and Comparative Examples 1 to 3 as shown in Table 1, were continuously extracted by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylformamide, as good solvents for methyl methacrylate-SEM-Na copolymers, whereby the reduction in the polymer contents was studied. The results are shown in Table 2. Here, the polymer content after being thoroughly extracted with dimethylformamide for 200 hours, was evaluated to be a graft rate in the sense that the polymer is firmly consolidated to the surface of the inorganic compound by means of a chemical bond. For the purpose of comparison, a similar extraction operation was conducted with respect to each of compositions (Comparative Examples 4 and 5) wherein an inorganic powder (silicon nitride) was coated with a polymer obtained by the solvent blending with polymethyl methacrylate or with a methyl methacrylate-SEM-Na copolymer whereby the reduction in the polymer content was compared.

TABLE 2__________________________________________________________________________ Polymer Polymer content Preparation of content after continuous polymeric before extraction*4 Graft composition*1 extraction (%) (graft rate) % efficiency*5 (%)__________________________________________________________________________ Polymerization systemExample 1 Presence of SEM- 9.6 9.1 90 Na (Present invention)Comparative Non-catalytic 6.5 1.8 23Example 1 polymerization system without addition of BPOComparative No addition of 1.1 -0.0 -0Example 2 SEM-Na as opposed to Example 1Comparative Addition of 4.5 0.9 8.6Example 3 dispersant as opposed to Example 1 Blend systemComparative Solvent blend of 9.6 -0.0 --Example 4 polymethyl meth- acrylate*2Comparative Solvent blend of 9.5 -0.0 --Example 5 methyl meth- acrylate-SEM-Na copolymer*3__________________________________________________________________________ *1: Silicon nitride was used as the inorganic compound. *2: Acrypet (VH), manufactured by Mitsubishi Rayon Co., Ltd., was used. *3: A copolymer prepared in the same manner as in Example 1 except that the method of the present invention was conducted in the absence of the inorganic compound, was used. *4: Continuous extraction by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylformamide. ##STR5##

The polymer components in the compositions of Comparative Examples 2, 4 an 5 were completely extracted by the above continuous extraction operation irrespective of the system being of a polymerization type or of a solvent blend type. This indicates that even in the polymerization system, a polymer forming in the absence of a sulfonic acid monomer or sulfonate monomer, is merely chemically or physically adsorbed on the surface of the inorganic compound. In Comparative Examples 1 and 3, a part of the formed polymer was firmly consolidated to the inorganic compound, but the level of the graft rate was very low. Whereas, in Example 1 according to the method of the present invention wherein a radical polymerization initiator was added in the presence of a sulfonic acid monomer or sulfonate monomer, the extracted rate after the series of severe extraction operations, was very small, indicating a high graft rate. Further, even when the polymeric composition was subjected to washing treatment with an aqueous NaOH solution, it showed a high graft rate substantially equal to the level after the extraction operations. Thus, it was confirmed that the firm consolidation of the polymer to the surface of the inorganic compound was attributable to the presence of a covalent bond-type graft linkage as a chemical bond stronger than a hydrogen bond or ionic bond at the interface.

EXAMPLES 2 to 5

The polymerization was carried out in the same manner as in Example 1, except that SPS, AMS, NaAS or NaMS was used as the sulfonic acid monomer or sulfonate monomer instead of SEM-Na. The graft efficiency was measured, and the results are shown in Table 3.

TABLE 3__________________________________________________________________________ Inorganic Graft Radical polymeri- Vinyl compound Deionized effi-Acid Amounts zation initiator monomer Silicon water ciencymonomer (parts) BPO (parts) MMA (parts) nitride (parts) (parts) (%)__________________________________________________________________________Example 1 SEM-Na 10.0 1.0 30.0 270.0 720 90Example 2 SPS *1 10.5 1.0 30.0 270.0 720 92Example 3 AMS *2 9.9 1.0 30.0 270.0 720 90Example 4 NaAS *3 6.5 1.0 30.0 270.0 720 75Example 5 NaMS *4 7.1 1.0 30.0 270.0 720 78__________________________________________________________________________ *1: CH.sub.2 .dbd.C.CH.sub.3 --COOC.sub.3 H.sub.6 --SO.sub.3 Na *2: CH.sub.2 .dbd.CH--CONH--(CCH.sub.3).sub.2 CH.sub.2 SO.sub.3 H *3: CH.sub.2 .dbd.CHCH.sub.2 SO.sub.3 Na *4: CH.sub.2 .dbd.C.CH.sub.3 --CH.sub.2 SO.sub.3 Na

As is apparent from Table 3, the graft efficiency was very high with SEM-Na, SPS and AMS.

EXAMPLES 6 to 9

The reaction was conducted in the same manner as in Example 1 except that the type of the radical polymerization initiator was changed, and the compositions thereby obtained were evaluated. The results are shown in Table 4.

TABLE 4__________________________________________________________________________ Acid Inorganic GraftRadical monomer Vinyl compound Deionized effi-polymeriza- Amount SEM-Na monomer Silicon water ciencytion initiator (parts) (parts) MMA (parts) nitride (parts) (parts) (%)__________________________________________________________________________Example 1 BPO 1.0 10.0 30.0 270.0 720 90Example 6 LPO *1 1.0 10.0 30.0 270.0 720 93Example 7 AIBN *2 1.0 10.0 30.0 270.0 720 90Example 8 AIBA *3 1.0 10.0 30.0 270.0 720 70Example 9 KPS *4 1.0 10.0 30.0 270.0 720 73__________________________________________________________________________ *1: Lauroyl peroxide *2: Azobisisobutyronitrile *3: 2,2'-Azobis(2aminodipropane)hydrochloride *4: Potassium persulfate

As is apparent from Table 4, the graft efficiency is higher with lipophilic radical polymerization initiators such as BPO, LPO and AIBN than with water-soluble AIBA and KPS.

EXAMPLES 10 and 11

the reaction was conducted in the same manner as in Example 1 except that the vinyl monomer identified in Table 5 was used instead of methyl methacrylate as the vinyl monomer, and the compositions thereby obtained were evaluated. The results are shown in Table 5.

TABLE 5__________________________________________________________________________ Acid Inorganic Graft monomer Radical polymeri- compound Deionized effi-Vinyl Amount SEM-Na zation Silicon water ciencymonomer (parts) (parts) BPO (parts) nitride (parts) (parts) (%)__________________________________________________________________________Example 1 MMA 30.0 10.0 1.0 270.0 720 90Example 10 ST 30.0 10.0 1.0 270.0 720 76Example 11 AN 30.0 10.0 1.0 270.0 720 74__________________________________________________________________________ MMA: Methyl methacrylate, ST: Styrene, AN: Acrylonitrile

As is apparent from Table 5, according to the method of the present invention, a high graft efficiency can be attained with either one of the vinyl monomers (Examples 10 and 11).

EXAMPLE 12

The reaction was conducted in the same manner as in Example 1 except that the type of the inorganic compound was changed, and the composition thereby obtained was evaluated. The results are shown in Table 6.

TABLE 6__________________________________________________________________________ Acid Radical Vinyl Graft monomer polymerization monomer Deionized effi-Inorganic Amount SEM-Na BPO NMA water ciencycompound (parts) (parts) (parts) (parts) (parts) (%)__________________________________________________________________________Example 1 Silicon 270.0 10.0 1.0 30.0 720 92 carbideExample 2 Zirconium 270.0 10.0 1.0 30.0 720 93 oxideExample 3 Zirconium 270.0 10.0 1.0 30.0 720 94 nitrideExample 4 Zirconium 270.0 10.0 1.0 30.0 720 91 borideExample 5 Zirconium 270.0 10.0 1.0 30.0 720 90 carbide__________________________________________________________________________

As is apparent from Table 6, the method of the present invention is superior to the conventional non-catalytic polymerization system in both the polymerization degree and the graft efficiency, and thus indicates that it is capable of providing a polymeric composition of a higher quality.

EXAMPLE 13 and COMPARATIVE EXAMPLES 6 to 9

As an evaluation of the applicability of the polymeric composition obtained by the method of the present invention to a composite material, a combination of the polymeric composition with polymethyl methacrylate as matrix (inorganic compound content: 80 wt. %) was press-molded at 200.degree. C. under 20 kg/cm.sup.2, and the molded product was evaluated for the outer appearance and bending strength. The results are shown in Table 7.

TABLE 7__________________________________________________________________________ Composite material composition *1 Outer Polymer Polymeric appearance Bending Polymeric content composition PMMA of molded strength composition (%) (parts) (parts) product (kg/cm.sup.2)__________________________________________________________________________Example 13 Example 1 9.6 88 12 .circleincircle. 283 Present inventionComparative Comparative Example 1 6.5 86 14 .DELTA. 190Example 6 Non-catalytic polymerization system without addition of BPOComparative Comparative Example 2 1.1 81 19 X 72Example 7 No addition of SEM-Na as opposed to Example 1Comparative Comparative Example 3 4.5 84 16 .DELTA. 140Example 8 Addition of dispersant as opposed to Example 1Comparative Non-treated silicon -- 80 20 64Example 9 nitride__________________________________________________________________________ *1: The ratio of inorganic compound/organic compound = 80/20. PMMA: Polymethyl methacrylate, Acrypet (VH), manufactured by Mitsubishi Rayon Co., Ltd. .circleincircle.: Good, .DELTA.: Fair, X: Poor, : Bad

As is apparent from Table 7, according to the method of the present invention (Example 13), a sustantial improvement in the effects of the combination is observed with respect to the outer appearance and strength of the molded product.

EXAMPLE 14 and COMPARATIVE EXAMPLES 10 to 14

The polymerization and evaluation were conducted in the same manner as in Example 1 except that methacrylic acid as a carboxylic acid monomer was used instead of the sulfonate monomer. For the purpose of comparison, similar polymerization operation and evaluation after the polymerization were conducted with respect to the polymerization behavior in the cases where no radical polymerization initiator was added as in the conventional non-catalytic polymerization system, no carboxylic acid monomer was added, and a dispersant was added. The results are shown in Table 8.

TABLE 8__________________________________________________________________________ Carboxylic Radical acid polymeri- Inorganic monomer zation Vinyl compound Dispersant Methyl initiator monomer Silicon Sodium hexa- Deionized Conversion methacrylic BPO MMA nitride metaphosphate water of monomer Consolidation acid*1 (parts) (parts) (parts)*2 (parts) (parts) (%) rate (%)*3__________________________________________________________________________Example 14 10.0 1.0 30.0 270.0 -- 720 -100 98Comparative 10.0 -- 30.0 270.0 -- 720 73 90Example 10Comparative -- 1.0 30.0 270.0 -- 720 90 5Example 11Comparative 10.0 1.0 30.0 270.0 3.0 720 93 41Example 12__________________________________________________________________________ *1: CH.sub.2C(CH.sub.3)COOH *2: Special grade reagent ##STR6## BPO: Benzoyl peroxide, MMA: Methyl methacrylate

It is evident from Table 8 that in the system where no carboxylic acid monomer was added as in Comparative Example 11, the consolidation rate was very low although the conversion was high, and a tendency for separation of the inorganic compound and the homopolymer was observed. It was further evident that as compared with Comparative Example 10, the method of the present invention is superior in both the conversion of monomer and the consolidation rate. Further, in the system of Comparative Example 12 wherein a dispersant was added, the consolidation rate was substantially low, and a tendency for the separation of the homopolymer was observed as in the case of Comparative Example 11.

The polymeric compositions of Example 14 and Comparative Examples 10 to 12 as shown in Table 8, were continuously extracted by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylformamide, as good solvents for methyl methacrylate-methacrylic acid copolymers, whereby the reduction in the polymer contents was studied. The results are shown in Table 9. Here, the polymer content after being thoroughly extracted with dimethylformamide for 200 hours, was evaluated to be a graft rate in the sense that the polymer is firmly consolidated to the surface of the inorganic compound by means of a chemical bond. For the purpose of comparison, a similar extraction operation was conducted with respect to each of compositions (Comparative Examples 13 and 14) wherein an inorganic powder (silicon nitride) was coated, with a polymer obtained by the solvent blending with polymethyl methacrylate or with a methyl methacrylate-methacrylic acid copolymer whereby the reduction in the polymer content was compared.

TABLE 9__________________________________________________________________________ Polymer Polymer content Preparation of content after continuous polymeric before extraction*4 Graft composition*1 extraction (%) (graft rate) % efficiency*5 (%)__________________________________________________________________________ Polymerization systemExample 14 Presence of 9.7 9.2 92 methacrylic acid (present invention)Comparative Non-catalytic 6.9 2.0 26Example 10 polymerization system without addition of BPOComparative No addition of 1.1 -0.0 -0Example 11 methacrylic acid as opposed to Example 14Comparative Addition of 4.1 0.7 6.8Example 12 dispersant as opposed to Example 14 Blend systemComparative Solvent blend of 9.5 -0.0 --Example 13 polymethyl meth- acrylate*2Comparative Solvent blend of 9.6 -0.0 --Example 14 methyl meth- acrylate-methyl methacrylic acid copolymer*3__________________________________________________________________________ *1: Silicon nitride was used as the inorganic compound. *2: Acrypet (VH), manufactured by Mitsubishi Rayon Co., Ltd., was used. *3: A copolymer prepared in the same manner as in Example 14 except that the method of the present invention was conducted in the absence of the inorganic compound, was used. *4: Continuous extraction by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylformamide. ##STR7##

The polymer components in the compositions of Comparative Examples 11, 13 and 14 were completely extracted by the above continuous extraction operation irrespective of the system being of a polymerization type or of a solvent blend type. This indicates that even in the polymerization system, a polymer forming in the absence of a carboxylic acid monomer, is merely chemically or physically adsorbed on the surface of the inorganic compound. In Comparative Examples 10 and 12, a part of the formed polymer was firmly consolidated to the inorganic compound, but the level of the graft rate was very low. Whereas, in Example 14 according to the method of the present invention wherein a radical polymerization initiator was added in the presence of a carboxylic acid monomer, the extracted rate after the series of severe extraction operations, was very small, indicating a high graft rate. Further, even when the polymeric composition was subjected to washing treatment with an aqueous NaOH solution, it showed a high graft rate substantially equal to the level after the extraction operations. Thus, it was confirmed that the firm consolidation of the polymer to the surface of the inorganic compound was attributable to the presence of a covalent bond-type graft linkage as a chemical bond stronger than a hydrogen bond or ionic bond at the interface.

EXAMPLES 15 to 19

The polymerization was carried out in the same manner as in Example 14, except that acrylic acid, crotonic acid, tiglic acid, cinnamic acid or maleic anhydride was used as the carboxylic acid monomer instead of methacrylic acid. The graft efficiency was measured, and the results are shown in Table 10.

TABLE 10__________________________________________________________________________ Inorganic Radical polymeri- Vinyl compound DeionizedCarboxylic Amount zation initiator monomer Silicon water Graftacid monomer (parts) BPO (parts) MMA (parts) nitride (parts) (parts) efficiency__________________________________________________________________________ (%)Example 14 Methacrylic 10.0 1.0 30.0 270.0 720 92 acidExample 15 Acrylic acid*1 7.6 1.0 30.0 270.0 720 94Example 16 Crotonic acid*2 10.0 1.0 30.0 270.0 720 92Example 17 Tiglic acid*3 11.4 1.0 30.0 270.0 720 71Example 18 Cinnamic 16.7 1.0 30.0 270.0 720 78 acid*4Example 19 Maleic 11.0 1.0 30.0 270.0 720 90 anhydride*5__________________________________________________________________________ *1: CH.sub.2CHCO.sub.2 H *2: CH.sub.3 CHCHCO.sub.2 H *3: CH.sub.3 CHC(CH.sub.3)CO.sub.2 H *4: C.sub.6 H.sub.5 CHCHCO.sub.2 H ##STR8##

As is apparent from Table 10, the graft efficiency was very high with methacrylic acid, acrylic acid, crotonic acid and maleic anhydride.

EXAMPLES 20 to 30

The reaction was conducted in the same manner as in Example 14 except that the type of the radical polymerization initiator was changed, and the compositions thereby obtained were evaluated. The results are shown in Table 11.

TABLE 11__________________________________________________________________________Radical Carboxylic Vinyl Inorganic Graftpolymeri- acid monomer monomer compound Deionized effi-zation Amount Methacrylic MMA Silicon water ciencyinitiator (parts) acid (parts) (Parts) nitride (parts) (parts) (%)__________________________________________________________________________Example 14 BPO 1.0 10.0 30.0 270.0 720 92Example 20 LPO *1 1.0 10.0 30.0 270.0 720 95Example 21 AIBN *2 1.0 10.0 30.0 270.0 720 92Example 22 AIBA *3 1.0 10.0 30.0 270.0 720 72Example 23 KPS *4 1.0 10.0 30.0 270.0 720 75__________________________________________________________________________ *1: Lauroyl peroxide *2: Azobisisobutyronitrile *3: 2,2'-Azobis(2aminodipropane)hydrochloride *4: Potassium persulfate

As is apparent from Table 11, the graft efficiency was higher with lipophilic radical polymerization initiators such as BPO, LPO and AIBN than with water-soluble AIBA and KPS.

EXAMPLES 24 and 25

The reaction was conducted in the same manner as in Example 14 except that the vinyl monomer identified in Table 12 was used instead of methyl methacrylate as the vinyl monomer, and the compositions thereby obtained were evaluated. The results are shown in Table 12.

TABLE 12__________________________________________________________________________ Carboxylic Inorganic Graft acid monomer Radical compound Deionized effi-Vinyl Amount Methacrylic polymerization Silicon water ciencymonomer (parts) acid (parts) BPO (parts) nitride (parts) (parts) (%)__________________________________________________________________________Example 14 MMA 30.0 10.0 1.0 270.0 720 92Example 24 ST 30.0 10.0 1.0 270.0 720 78Example 25 AN 30.0 10.0 1.0 270.0 720 72__________________________________________________________________________ MMA: Methyl methacrylate, ST: Styrene, AN: Acrylonitrile

As is apparent from Table 12, according to the method of the present invention, a high graft efficiency can be attained with either one of the vinyl monomers (Examples 24 and 25). The applicability of a wide range of vinyl monomers is a feature of the present invention in addition to the features of the high conversion and graft rate.

EXAMPLE 26

The reaction was conducted in the same manner as in Example 14 except that the type of the inorganic compound was changed, and the composition thereby obtained was evaluated. The results are shown in Table 13.

TABLE 13__________________________________________________________________________ Carboxylic Radical poly- Vinyl Graft acid monomer merization monomer Deionized effi-Inorganic Amount Methacrylic BPO MMA water ciencycompound (parts) acid (parts) (parts) (parts) (parts) (%)__________________________________________________________________________Example 1 Silicon 270.0 10.0 1.0 30.0 720 94 carbideExample 2 Zirconium 270.0 10.0 1.0 30.0 720 95 oxideExample 3 Zirconium 270.0 10.0 1.0 30.0 720 96 nitrideExample 4 Zirconium 270.0 10.0 1.0 30.0 720 93 borideExample 5 Zirconium 270.0 10.0 1.0 30.0 720 92 carbide__________________________________________________________________________

As is apparent from Table 13, the method of the present invention is superior to the conventional non-catalytic polymerization system in both the polymerization degree and the graft efficiency, and thus indicates that it is capable of providing a polymeric composition of a higher quality.

EXAMPLE 27 and COMPARATIVE EXAMPLES 15 to 18

As an evaluation of the applicability of the polymeric composition obtained by the method of the present invention to a composite material, a combination of the polymeric composition with polymethyl methacrylate as matrix (inorganic compound content: 80 wt. %) was press-molded at 200.degree. C. under 20 kg/cm.sup.2, and the molded product was evaluated for the outer appearance and bending strength. The results are shown in Table 14.

TABLE 14__________________________________________________________________________ Composite material composition *1 Outer Polymer Polymeric appearance Bending Polymeric content composition PMMA of molded strength composition (%) (parts) (parts) product (kg/cm.sup.2)__________________________________________________________________________Example 27 Example 14 9.7 88 12 .circleincircle. 288 Present inventionComparative Comparative Example 10 6.9 86 14 .DELTA. 193Example 15 Non-catalytic polymerization system without addition of BPOComparative Comparative Example 11 1.1 81 19 X 72Example 16 No addition of methacrylic acid as opposed to Example 14Comparative Comparative Example 12 4.1 83 17 .DELTA. 120Example 17 Addition of dispersant as opposed to Example 14Comparative Non-treated silicon -- 80 20 64Example 18 nitride__________________________________________________________________________ *1: The ratio of inorganic compound/organic compound = 80/20. PMMA: Polymethyl methacrylate, Acrypet (VH), manufactured by Mitsubishi Rayon Co., Ltd. .circleincircle.: Good, .DELTA.: Fair, X: Poor, : Bad

As is apparent from Table 14, according to the method of the present invention (Example 27), a substantial improvement in the effects of the combination is observed with respect to the outer appearance and strength of the molded product.

Claims

1. A method for preparing a polymeric composition having an inorganic compound firmly consolidated thereonto, which comprises polymerizing at least one radical polymerizable vinyl monomer using a peroxide or azo compound radical initiator in an aqueous polymerization medium, which medium comprises an inorganic compound dispersed in the presence of an organic acid monomer or organic acid salt monomer, wherein said inorganic compound is selected from the group consisting of a carbide, nitride and boride of silicon and zirconium, and zirconium oxide; and wherein said organic acid monomer and organic acid salt monomer is a carboxylic acid monomer or carboxylate monomer of the formula: ##STR9## wherein each of R.sub.5 and R.sub.6 is a hydrogen atom, a C.sub.1 -C.sub.15 alkyl group or --COOA, wherein A is a hydrogen atom, an ammonium radical or an alkali metal atom; R.sub.7 is a hydrogen atom or a C.sub.1 -C.sub.15 alkyl group; Z is a hydrogen atom, an ammonium radical or an alkali metal atom; and each of R.sub.8 and R.sub.9 is a hydrogen atom or a C.sub.1 -C.sub.15 alkyl group.

2. The method according to claim 1, wherein the carboxylic acid monomer is acrylic acid, methacrylic acid, crotonic acid, tiglic acid, cinnamic acid or maleic anhydride.

3. The method according to claim 1, wherein the radical polymerization initiator is decomposable at a temperature within the range of from 40.degree. to 100.degree. C.