WO1997012918A1 - Sirop (meth)acrylique, procede d'elaboration de ce sirop et procede d'elaboration d'un materiau de moulage contenant un tel sirop - Google Patents
Sirop (meth)acrylique, procede d'elaboration de ce sirop et procede d'elaboration d'un materiau de moulage contenant un tel sirop Download PDFInfo
- Publication number
- WO1997012918A1 WO1997012918A1 PCT/JP1996/002860 JP9602860W WO9712918A1 WO 1997012918 A1 WO1997012918 A1 WO 1997012918A1 JP 9602860 W JP9602860 W JP 9602860W WO 9712918 A1 WO9712918 A1 WO 9712918A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- meth
- syrup
- compound
- parts
- acrylic
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/46—Reaction with unsaturated dicarboxylic acids or anhydrides thereof, e.g. maleinisation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2800/00—Copolymer characterised by the proportions of the comonomers expressed
- C08F2800/20—Copolymer characterised by the proportions of the comonomers expressed as weight or mass percentages
Definitions
- the present invention relates to a (meth) acrylic syrup and a method for producing the same, and a method for producing a molding material containing (meth) acrylic syrup.
- the present invention relates to a (meth) acrylic syrup and a method for producing the same, and a method for producing a molding material containing the (meth) acrylic syrup.
- Japanese Patent Publication No. S64-11652 discloses a crosslinked type containing a polymer having a carboxyl group and a crosslinkable monomer having a plurality of functional groups.
- Acrylic syrup having a carboxyl group is disclosed in Japanese Patent Publication No. Sho 61-24357.
- Japanese Patent Publication No. 52-1189 discloses a syrup obtained by treating a thiol compound remaining in a syrup with maleic anhydride and a basic compound.
- the above thiol compound is used as a chain transfer agent for polymerization reaction and as a stabilizer for syrup. Therefore, unreacted thiol is added to syrup polymerized in the presence of thiol compound. Compounds are included. If the thiol compound remains on the sill, odor due to the thiol compound Paper (Rule 26)
- a monomer component containing a (meth) acrylic acid ester is polymerized in the presence of a thiol compound, and then the reaction mixture is treated with maleic anhydride and a basic compound. In addition, a carboxyl-containing vinyl monomer is added to the reaction mixture.
- storage stability in the case of forming a molding material is achieved by using a vinyl monomer having a carboxyl group and treating the reaction mixture with maleic anhydride and a basic compound. It is possible to produce (meth) acryl syrup having excellent properties in a shorter time than conventional ones. Further, according to the above method, it is possible to provide (meth) acryl syrup having excellent storage stability when used as a molding material.
- a molding material according to the present invention is characterized in that it includes (meth) acrylyl syrup obtained by the above-mentioned manufacturing method in order to solve the above-mentioned problems. Further, in order to solve the above-mentioned problems, the molding material according to the present invention is obtained by polymerizing a monomer component containing a (meth) acrylic ester in the presence of a thiol compound, and then reacting the reaction mixture with anhydrous maleic anhydride. It is characterized by containing (meth) acrylyl syrup treated with an acid and a basic compound, and a vinyl monomer having a carboquinol group.
- a molding material can be provided.
- the (meth) acrylyl syrup according to the present invention comprises a monomer component containing a (meth) acrylic ester and a vinyl monomer containing a carboxyl group in the presence of a thiol compound. After polymerization, the reaction mixture is replaced with anhydrous matting paper (Rule 26) To provide. Disclosure of the invention
- the present inventors have diligently studied a (meth) acrylic syrup and a method for producing the same, and a method for producing a molding material containing (meth) acrylic syrup, in order to achieve the above object.
- a monomer component containing a (meth) acrylic acid ester and a vinyl monomer having a carboxyl group are polymerized in the presence of a thiol compound
- the reaction mixture is subjected to anhydrous maleic polymerization.
- (Meth) acrylic syrup treated with an acid and a basic compound, and the above monomer component containing a (meth) acrylic acid ester are polymerized in the presence of a thiol compound.
- the (meth) acrylic syrup obtained by treating the reaction mixture with maleic anhydride and a basic compound and adding the above-mentioned carboxyl group-containing vinyl monomer to the reaction mixture is as follows: It has been found that it has excellent storage stability (so-called shelf life) when used as a molding material. It has also been found that by molding a molding material containing the above (meth) acryl syrup, it is possible to obtain a molded article excellent in various physical properties such as heat resistance, solvent resistance, weather resistance and water resistance. The present invention has been completed.
- a method for producing a (meth) acryl syrup according to the present invention comprises, in order to solve the above-mentioned problems, a monomer component containing a (meth) acrylic ester and a vinyl monomer containing a carboxyl group. And c. Polymerizing in the presence of a thiol compound, and then treating the reaction mixture with maleic anhydride and a basic compound.
- the method for producing (meth) acryl syrup according to the present invention Before or after the addition, glycidyl (meth) acrylate and / or methyl glycidyl (meth) acrylate are added to the reaction mixture to esterify the carboxyl group contained in the polymer, thereby polymerizing the polymer. It includes a (meth) acrylic acid ester-based polymer in which a side chain having an acidic double bond is bonded to the main chain.
- the (meth) acryl syrup according to the present invention is obtained by polymerizing a monomer component containing a (meth) acrylic acid ester and a vinyl monomer containing a carboxyl group in the presence of a thiol compound. Thereafter, the reaction mixture and the unsaturated epoxy compound are esterified in the presence of a metal compound containing at least one element selected from the group consisting of zinc, tin, and zirconium, whereby polymerizable double It includes a (meth) acrylic acid ester-based polymer in which a side chain having a bond is bonded to a main chain.
- the above polymer may include an oligomer having a degree of polymerization of about 2 to 20 or a prepolymer obtained by stopping the polymerization reaction of the monomer in the middle.
- the above monomer component contains a (meth) acrylic acid ester and, if necessary, a vinyl compound (monomer).
- Specific examples of the above (meth) acrylates include, for example, methyl (meth) acrylate, ethyl (meth) acrylate, and n-propyl (meth) acrylate , Isopropyl (meth) acrylate, n-butyl (meth) acrylate, i-butyl (meth) acrylate, s -butyl (meth) acrylate, t-butyl ( (Meth) acrylate, 2-ethylhexyl (methyl) acrylate, lauryl (meth) acrylate, etc. (meth) acrylate alkyl ester; cyclohexyl (meth) atalyte (Return paper, etc. (paper (Rule 26) It has been treated with leic acid and a basic compound.
- the (meth) acrylic syrup according to the present invention is obtained by polymerizing the above-mentioned monomer component containing a (meth) acrylic acid ester in the presence of a thiol compound, and then reacting the reaction mixture with an anhydride.
- the treatment is carried out using maleic acid and a basic compound, and the above-mentioned vinyl monomer having a carboxyl group is added to the reaction mixture.
- the (meth) acrylyl syrup according to the present invention comprises a vinyl ether compound and a reaction mixture obtained by polymerizing a monomer component containing a (meth) acrylic ester in the presence of a thiol compound. And / or a vinyl ether compound is added.
- the (meth) acryl syrup according to the present invention is obtained by polymerizing a monomer component containing a (meth) acrylic ester and a vinyl monomer containing a carboxyl group in the presence of a thiol compound. Thereafter, a vinyl ether compound and / or a vinyl thioether compound are added to the reaction mixture.
- the (meth) acrylyl syrup according to the present invention is obtained by polymerizing a monomer component containing a (meth) acrylic acid ester in the presence of a thiol compound, and then adding a vinyl ether compound and Z or A vinylthioether compound is added and the above-mentioned vinyl monomer containing a carboxyl group is added to the reaction mixture.
- the (meth) acryl syrup according to the present invention is obtained by polymerizing a monomer component containing a (meth) acrylic ester and a vinyl monomer containing a carboxyl group in the presence of a thiol compound. Thereafter, a vinyl ether compound and / or a vinyl thioether compound are added to the reaction mixture.
- Styrene compounds such as styrene and chlorostyrene: vinyl esters such as vinyl acetate; aryl alcohols such as aryl alcohol, ethylene glycol monoaryl ether, and propylene glycol monoaryl ether; (meta) atari Lonitrinole; Unsaturated basic compound; N-Methylmaleide, N-Ethylmaleide, Nn-Pro-Biremaleide, N-Isopropinolemate, N-Butylmaleide, N-F Enilmale Mid, N—m—Tri-male Mid, N— ⁇ —Tri-male Mid, N—Hi-Naphthyl Male Mid, N-Benzyl Male Mid, N—Cyclohexyl Male Mid, N , N'—Ethylene bismuth raymide, N, N'-Trimethylene bismuth raymide, N, ⁇ '1 m—Fenylene bismuth ⁇ -substituted maleimides
- the (meth) acrylic acid ester containing a hydroxyl group a glycol (meth) acrylate obtained by esterifying at least one of the hydroxyl groups of glycol is used.
- Relates are particularly preferred, specifically, for example, 2—hydroxylethyl (meta) acrylate, 2—hydroxypropylpropyl (meta) acrylate, and the like.
- (Meta) acrylates having a roxyalkyl group glycerin mono (meta) acrylate, glycerin di (meta) acrylate, pentaerythritol mono (meta) (Meth) acrylates of polyhydric alcohols, such as acrylates and benzoyl erythritol (meta) acrylate; polyethylene glycol mono (meta) acrylates (Meta) acrylates of high molecular weight glycols, such as relays.
- Cycloalkyl acrylate glycidyl (meth) acrylate; dimethylaminoethyl (meth) acrylate, basic (meta) such as getylaminoethyl (meth) acrylate Acrylate; and the like, but are not particularly limited.
- (meth) acrylic acid esters include (meth) acrylamide; N-alkoxy-substituted (meth) acrylamide such as N-methoxymethylacrylamide, N-ethoxyquinylacrylamide and the like. And the like. These (meth) acrylic acid esters may be used alone or as a mixture of two or more.
- methyl methacrylate and (meth) acrylic acid esters containing methyl methacrylate as a main component are particularly preferred.
- methyl methacrylate as a main component, various physical properties such as weather resistance, transparency, and surface gloss of a molded product (cured product) obtained by molding a molding material containing (meth) acryl syrup can be obtained. Appearance, safety, etc. can be further improved.
- a basic (meth) acrylic acid ester When a basic (meth) acrylic acid ester is used as the (meth) acrylic acid ester, neutral (100% by weight or more) relative to the basic (meth) acrylic acid ester is used. It is preferable to use a (meth) acrylic acid ester in combination.
- the neutral (meth) acrylate ester the alkyl (meth) acrylate, cycloalkyl (meth) acrylate and the like exemplified above can be used.
- the above-mentioned vinyl compound may be any compound that does not contain a carboxyl group.
- the vinyl compound include ⁇ -olefins, gens, acetylenes; styrene, monomethylstyrene, and vinyl toluene.
- unsaturated monocarboxylic acids such as acrylic acid, methacrylic acid, crotonic acid, and vinylbenzoic acid
- unsaturated dicarboxylic acids such as maleic acid, fumaric acid, itaconic acid and citraconic acid; And the like, but are not particularly limited.
- unsaturated dicarboxylic acid monoester examples include, for example, monomethyl maleate, monoethyl maleate, monobutyl maleate, monooctyl maleate, monomethyl fumarate, monoethyl fumarate, monobutyl fumarate And monooctyl fumarate, monoethyl citrate, and the like.
- a compound obtained by monoesterifying an acid anhydride with a (meth) acrylic acid ester containing a hydroxyl group, that is, a half ester (half ester) of the acid anhydride is used as a vinyl monomer. You can do that too.
- acid anhydrides include succinic anhydride, phthalic anhydride, and hexahydrofuroic anhydride.
- Examples of the above (meth) acrylic acid esters containing a hydroxyl group include, for example, 2-hydroxyethyl (meth) acrylate, and ⁇ -force of 2-hydroxyethyl (meth) acrylate.
- examples of the half-ester of an acid anhydride include succinic acid monoester, phthalic acid monoester, and hexaphthalic acid monoester.
- These vinyl monomers may be used alone, or two or more of them may be used as an appropriate mixture.
- the ratio (ratio) of the monomer component and the vinyl monomer the total amount of both is 100% by weight, and the monomer component is 80% by weight to 9 Replacement paper (Rule 26)
- These vinyl compounds may be used alone or in combination of two or more.
- the mixing ratio of the two that is, the content of the vinyl compound in the monomer component, depends on the type of the vinyl compound and the (meth) acrylic ester. Although it depends on the combination and the like, 50% by weight or less is more preferable.
- the vinyl compound is an N-substituted maleimide
- the range of 5% to 40% by weight is more preferable, and the range of 10% to 30% by weight is more preferable. Particularly preferred is a range of 15% by weight to 25% by weight.
- the vinyl compound is a (meth) acrylic acid ester containing a hydroxyl group
- the content is more preferably in the range of 0.5% by weight to 20% by weight, and more preferably in the range of 1% by weight to 15% by weight. Is more preferable, and the range of 3% by weight to 10% by weight is particularly preferable.
- the vinyl compound is a (meth) acrylic acid ester containing a hydroxyl group
- the proportion of the vinyl compound is less than 0.5% by weight, the weight obtained by polymerizing the monomer component is reduced.
- the compound (hereinafter, referred to as a hydroxy group-containing polymer) is reacted with an unsaturated isocyanate compound or an unsaturated acid anhydride (all of which will be described later) to be introduced into the (meth) acrylic wrap.
- the number of polymerizable double bonds (polymerizable double bonds) is limited, so it is not possible to obtain molded articles with excellent physical properties such as hot strength.
- the carboxyl group-containing vinyl monomer (hereinafter, simply referred to as a vinyl monomer) may be a compound containing a polymerizable double bond and a carboxyl group in one molecule.
- a vinyl monomer specifically, replacement paper (Rule 26) As a result, it becomes impossible to obtain a molded article having excellent properties such as hot strength. If the ratio of the vinyl monomer exceeds 20% by weight, the weather resistance and water resistance of the obtained molded article are undesirably reduced.
- the vinyl monomer may be mixed with the monomer component before polymerization, or may be mixed with the reaction mixture before treating the added thiol compound, that is, after the polymerization, and further added. After treating the thiol compound, it may be mixed with the reaction mixture. Alternatively, after producing the (meth) acrylic syrup by treating the added thiol compound, the (meth) acrylic syrup and the vinyl monomer may be mixed when producing the molding material. .
- the thiol compound is a chain transfer agent having a mercapto group in the molecule, and has a function of adjusting the molecular weight and the like of the polymer in the reaction mixture.
- t-butyl mercaptan Alkyl mercaptans such as butane, n-octyl mercaptan, and n-dodecyl mercaptan; aromatic mercaptans such as thiophenol and thionaphthol; thioglycolic acid; octyl thioglycolate, ethylene glycol dithioglycolate Alkyl esters of thioglycolic acid, such as trimethylolprohan tris (thioglycolate) and pentaerythritol tolte traquisoo (thioglycolate); —mercaptopropionic acid (3—mercaptopropionic acid);
- Alkyl topropionate and the like, but are not particularly limited thereto.
- These thiol compounds may be used singly or on replacement paper (Rule 26). It is preferably in the range of 9.5% by weight, while the vinyl monomer is preferably in the range of 0.5% to 20% by weight, and more preferably in the range of 0% to 15% by weight. .
- the vinyl monomer is more preferably in the range of 1.5% by weight to 10% by weight
- the vinyl monomer is more preferably in the range of 3% by weight to 10% by weight.
- the vinyl monomer in the above range it is possible to produce (meth) acryl syrup in a shorter time than before, and to mold a molding material containing the (meth) acryl syrup.
- Various physical properties such as heat resistance, solvent resistance, weather resistance, and water resistance of the resulting molded article can be improved.
- the molding material can be cured in a shorter time than before, and the average molecular weight of the cured product (molded product) increases. Further, it is possible to obtain a molded article having excellent hot strength and less coloring.
- the proportion of the vinyl monomer is less than 0.5% by weight, the expected action and effect of using the vinyl monomer become poor. That is, the effect of reducing the time required to produce (acrylic syrup) is poor, and furthermore, various physical properties such as heat resistance of the obtained molded article are deteriorated, which is not preferable. Also, the molecular weight of the cured product does not increase.
- the reaction conditions of reaction temperature and reaction time and the like when carrying out the polymerization is not particularly limited, for example, among the c which may be a known reaction conditions, the polymerization of the monomer composition
- the method of terminating the reaction on the way is more preferable because (meth) acrylic syrup can be obtained in one step. Thereby, a reaction mixture containing a polymer containing a carboxyl group is obtained. Further, by polymerizing (partially polymerizing) the monomer component, a reaction mixture containing a polymer having no carboxyl group can be obtained.
- the weight average molecular weight (Mw) of the polymer is about 6, 000 to 1, 0000, 0000, more preferably 30, 000 to 1, 0, 00, 00. It is possible to adjust the number average molecular weight (Mn) to about 0,000 to 500,000, more preferably about 100,000 to 200,000. More desirable, but not particularly limited. Further, the polymerization is preferably performed under a nitrogen atmosphere. Further, at the end of the reaction, the ratio (ratio) between the polymer and the unreacted monomer composition (or monomer component) in the reaction mixture is defined as 100 wt. Is preferably in the range of 7% to 80% by weight, and unreacted monomer composition (or monomer replacement paper (Rule 26)) Two or more types may be used in combination. Note that, as a chain transfer agent, para-methylstyrene dimer, carbon tetrachloride, or the like can be used in combination.
- the amount of the thiol compound added to the mixture of the monomer component and the vinyl monomer (hereinafter, referred to as a monomer composition) or the amount of the thiol compound added to the monomer component depends on the type of the thiol compound. It should be selected according to the combination with the monomer composition and the like, and is not particularly limited, but is preferably in the range of 0.01% by weight to 15% by weight. The optimum range is from 0% to 2% by weight. By adding a thiol compound, the polymerization reaction can be controlled very easily.
- the polymerization method specifically, for example, various polymerization methods such as bulk polymerization (bulk polymerization), solution polymerization, suspension polymerization, and emulsion polymerization can be employed.
- bulk polymerization is particularly preferred.
- suspension polymerization for example, the monomer composition (or monomer component) is suspended in a dispersion medium such as water using a dispersion stabilizer such as polyvinyl alcohol. I just need.
- polymerization initiator When polymerizing the above monomer composition in the presence of a thiol compound, or when polymerizing a monomer component in the presence of a thiol compound, it is desirable to use a polymerization initiator.
- Specific examples of the above-mentioned polymerization initiator include, for example, benyl peroxide, lauroyl peroxide, methylethyl ketone peroxide, t-butylperoxy-2-ethylhexanoate, t-butylvinyl oxyoxide.
- N-cyclohexylmaleamide can be synthesized by reacting maleic anhydride with cyclohexylamine to obtain N-cyclohexylmaleic acid monoamide and then performing a ring closure reaction. it can.
- the monomer composition used for obtaining the oligomer and the polymer may contain the vinyl compound exemplified above in addition to the N-substituted maleimide.
- the amount of the maleimide compound used is preferably in the range of 5% by weight to 40% by weight, with the total amount of both being 100% by weight. Preferably, it is more preferably in the range from 10% to 30% by weight, particularly preferably in the range from 15% to 25% by weight. If the use amount is less than 5% by weight, the moldability of the obtained molding material is reduced, and the heat resistance, gloss and surface smoothness of the molded product are not preferred. On the other hand, if the amount is as high as 40% by weight, the strength of the obtained molded article is undesirably reduced.
- (meth) acrylic Rirushirappu when it is necessary to distinguish it from others, (meth) acrylate Rirushirappu A and referred c the (meth) acrylic Rirushirappu A is, for example sea Tomorudi It is suitable as a molding compound (hereinafter, referred to as SMC), a bulk molding compound (hereinafter, referred to as BMC), a premix material, or a casting material.
- SMC molding compound
- BMC bulk molding compound
- premix material a casting material.
- (meth) acrylic syrup B when it is necessary to distinguish the (meth) acrylic syrup from the others, it is referred to as (meth) acrylic syrup B.
- the (meth) acrylic syrup B is suitable as, for example, a casting material ⁇ a bremimix material. is there.
- the (meth) acrylyl syrups AB may contain unreacted monomer components.
- Replacement paper in which monomer components are polymerized in the presence of a thiol compound (Rule 26) Min) is preferably in the range of 93% to 20% by weight.
- a monomer composition (or a monomer component) may be further added to the reaction mixture, or after the polymer is separated from the reaction mixture, the monomer composition is added to the polymer.
- a substance (or a monomer component) may be further mixed.
- the monomer composition (or monomer component) to be further mixed may be the same as the monomer composition (or monomer component) used for obtaining the reaction mixture.
- alkyl methacrylate and styrene compounds are particularly preferred.
- alkyl methacrylate examples include methyl methacrylate, ethyl methacrylate, n-propyl methacrylate, n-butyl methacrylate, s-butyl methacrylate, and t-butyl methacrylate.
- Styrene is particularly preferred as the styrene-based compound.
- a maleimide compound may be further added to the reaction mixture.
- the maleimide-based compound described above refers to N-substituted maleimide; an oligomer obtained by polymerizing a monomer composition containing the N-substituted maleimide; and a polymer. These maleimide compounds may be used alone or in combination of two or more.
- N-hexylhexyl maleimide can suppress coloring of a molded product obtained by pressure molding, and can provide a molded product having a good appearance. Therefore, it is particularly preferable.
- the maleimide compound may be a commercially available product or a compound synthesized by a known method.
- Example Replacement form (Rule 26) If the amount of the basic compound used exceeds 1.5 times the mol of the thiol compound added during the polymerization, it is not preferable because the weather resistance of the obtained molded article is reduced. On the other hand, if the amount of maleic anhydride used exceeds 3.0 times the mol of the thiol compound added at the time of polymerization, it is not preferable because the aqueous solution of the resulting molded article is reduced.
- the processing conditions such as the processing temperature and the processing time when performing the processing of the thiol compound are not particularly limited. For example, a thiol compound can be treated simply by mixing maleic anhydride and a basic compound into a reaction mixture and stirring the mixture.
- a method of polymerizing a monomer component and a vinyl monomer in the presence of a thiol compound and then treating the reaction mixture with maleic anhydride and a basic compound, or After the components are polymerized in the presence of the thiol compound, the reaction mixture is treated with maleic anhydride and a basic compound, and a liquid (meth) acrylic acid is prepared by adding a vinyl monomer to the reaction mixture. Lil syrup is obtained.
- the (meth) acrylic syrup in the present invention may be a mixture of (meth) acrylic syrups A and B obtained by the above two or three different methods (this method).
- the vinyl ether compound according to the present invention may be any compound having a double bond capable of reacting with a thiol compound, and specific examples of the vinyl ether compound include, for example, methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, Aliphatic vinyl ethers such as isopropyl vinyl ether, n-butyl vinyl ether, and isobutyl vinyl ether; cycloalkyl vinyl ethers such as cyclohexyl vinyl ether; 2,3—dihydrofuran, 3,4— Dihydrofuran, 2, 3 — Jihidraw 2H—Pyran, 3,4—Jihidraw 2H—Pi Down, 3, 4 - replacement example paper (Rule 26) Thereafter, a molding material obtained by mixing a vinyl monomer with (meth) acrylic syrup obtained by treating the reaction mixture with maleic anhydride and a basic compound is suitable, for example, as a casting material.
- the basic compound examples include primary amines such as methylamine and ethylamine: secondary amines such as dimethylamine and getylamine; trimethylamine and triethylamine. Tertiary amines; diaza compounds: triabourne compounds; and the like, but are not particularly limited. These basic compounds may be used alone or in combination of two or more.
- the basic compound is preferably used in an amount of 0.01 to 5 times the molar amount of the thiol compound added during the polymerization, and preferably in a range of 0.03 to 1.2 times the molar amount. More preferred to use within.
- the maleic anhydride used in combination with the above basic compound is preferably used in an amount of 0.5 to 3.0 moles, more preferably 0.7 times, the mole of the thiol compound added at the time of polymerization. More preferably, it is used in the range of from mol to 2.8 mol.
- the amount of the basic compound used is less than 0.01 times the mol of the thiol compound added during the polymerization, or when the amount of the maleic anhydride is less than 0.5 times the mol, the thiol compound is used. It is not desirable because it may not be completely processed.
- the thiol compound remains in the reaction mixture, that is, the (meth) acryl syrup, the storage stability when the (meth) acryl syrup is used as a molding material is reduced. In addition, it takes a long time to cure the molding material containing (meth) acrylic syrup, and the average molecular weight of the cured product does not increase. Replacement form (Rule 26) If the amount used exceeds 5 moles, the weatherability of the resulting molded article is undesirably reduced.
- the processing conditions such as the processing temperature and the processing time when the thiol compound is processed may be determined according to the composition of the reaction mixture and the like, and are not particularly limited.
- the method of adding the vinyl ether compound and the Z or vinylthioether compound is not particularly limited. For example, these compounds may be added to the reaction mixture, or the reaction mixture may be added to the above compound. .
- the thiol compound can be treated simply by mixing the reaction mixture with the vinyl ether compound and the Z or vinyl thioether compound and stirring.
- (meth) acrylic syrup (hereinafter referred to as (meth) acrylic syrup C when it is necessary to distinguish it from others) treated with a vinyl ether compound and / or a vinyl thioether compound is used as a paint.
- a molding material such as SMC and BMC, a premix material, a casting material, a pultrusion molding material, an injection molding material, and an extrusion molding material.
- the treatment of the thiol compound may be performed in the presence of a catalyst such as a Lewis acid, an amine salt, a tertiary amine, a quaternary ammonium salt, a phosphonium salt, or a metal salt.
- a catalyst such as a Lewis acid, an amine salt, a tertiary amine, a quaternary ammonium salt, a phosphonium salt, or a metal salt.
- a catalyst such as a Lewis acid, an amine salt, a tertiary amine, a quaternary ammonium salt, a phosphonium salt, or a metal salt.
- a solvent can be used if necessary.
- the solvent water and Z or an organic solvent are preferable.
- the reaction mixture contains a carboxyl group.
- Jihi Draw 2 Metal H—Pyran, 3, 4 —Jihi Draw 2—Ethoxy 2 H—Pyran, 3,4-Dihydro 1, 4,4 Dimethyl 2 H—Pyran 1 2 —On Cyclic ether: and the like, but are not particularly limited.
- These vinyl ether compounds may be used alone or in combination of two or more.
- the vinyl thioether compound according to the present invention may be any compound having a double bond capable of reacting with a thiol compound.
- the vinyl thioether compound include a compound having a structure in which an oxygen atom in the above-described vinyl ether compound is replaced with a sulfur atom. That is, as the vinyl thioether compound, specifically, for example, an aliphatic vinyl thioether corresponding to the above-described aliphatic vinyl ether; a cycloalkyl vinyl thioether corresponding to the above-described cycloalkyl vinyl ether; Cyclic thioether corresponding to the exemplified cyclic ether; and the like, but are not particularly limited. These vinylthioether compounds may be used alone or in combination of two or more.
- the usage amount of the vinyl ether compound and / or the vinyl thioether compound is preferably in the range of 0.5 to 5 moles, and more preferably in the range of 0.8 to 3 moles than the thiol compound added during the polymerization. More preferred. If the amount is less than 0.5 mole, the thiol compound may not be completely treated, which is not preferable.
- the reaction mixture that is, when the remaining thiol compound (meth) acrylate Rirushira-up, also c storage stability when the a (meth) acrylic Rirushira-up and the molding material is reduced, the (meth) acrylic Rirushirappu It takes a long time to cure the containing molding material, and the average molecular weight of the cured product does not increase.
- the amount of the esterification catalyst to be added is determined according to the type, the composition of the reaction mixture, the amount of (meth) glycidyl acrylate and Z or (meth) methyl glycidyl acrylate, the combination thereof, and the like.
- the amount is not particularly limited, but is preferably within a range of 0.01 to 5 parts by weight, more preferably 0.1 to 3 parts by weight, based on 100 parts by weight of the reaction mixture. Further preferred is the range of parts.
- a polymerization inhibitor can be allowed to coexist if necessary.
- the polymerization inhibitor include, for example, hydroquinone, methylhydroquinone, methoxyhydrone quinone, t-butylhydroquinone, and the like.
- a solvent can be used if necessary. As the solvent, water and Z or an organic solvent are preferable.
- a (meth) acrylic syrup (untreated (meta)) is obtained by polymerizing a monomer component containing a (meth) acrylic acid ester and a carboxyl group-containing vinyl monomer in the presence of a thiol compound.
- An esterification reaction (acrylic sip) and an unsaturated epoxy compound in the presence of a metal compound to be described later (hereinafter referred to as an esterification reaction B when it is necessary to distinguish it from others)
- molding materials can also be obtained.
- the unsaturated epoxy compound described above may be a compound containing an epoxy group capable of reacting with a carboxyl group and a polymerizable double bond in one molecule.
- Specific examples of the unsaturated epoxy compound include, for example, aryl glycidyl ether, glycidyl (meth) acrylate, methyl glycidyl (meth) acrylate; Meta) acrylate; and the like, but are not particularly limited.
- These unsaturated evo papers (regulations) nowadays J26
- the reaction mixture may contain glycidyl (meth) acrylate and Z or (meth) acrylic acid, if necessary. More preferably, methyl glycidyl is added to esterify the carboxyl group contained in the polymer. As a result, (meth) acrylyl syrup C ′ containing a polymer containing an ester bond is obtained.
- the amount of the above-mentioned glycidyl (meth) acrylate and Z or (meth) glycidyl (meth) acrylate may be set according to the composition of the reaction mixture, and is not particularly limited. It is more preferably in the range of 0.5 to 2 moles, more preferably in the range of 0.8 to 1.5 moles relative to the body.
- esterification reaction A When performing the above-mentioned esterification reaction (hereinafter, referred to as esterification reaction A when it is necessary to distinguish it from the others), an esterification catalyst can be used as necessary.
- the esterification catalyst is not particularly limited as long as it is a compound capable of promoting a ring-opening reaction between a carboxyl group and an epoxy group.
- esterification catalyst examples include tertiary amines such as dimethylbenzylamine, triethylamine, tetramethylethylenediamine, and tri-n-octylamine; tetramethylammonium; Quaternary ammonium salts such as emuchloride, tetramethylammonium bromide and tetraptylammonium bromide; quaternary phosphonium salts such as benzyl triphenylphosphonium bromide: Metal Salt; and the like.
- tertiary amines such as dimethylbenzylamine, triethylamine, tetramethylethylenediamine, and tri-n-octylamine
- tetramethylammonium Quaternary ammonium salts such as emuchloride, tetramethylammonium bromide and tetraptylammonium bromide
- quaternary phosphonium salts such as
- the oxo acid metal salt includes a hydrogen salt such as zinc hydrogen phosphate.
- C Examples of the above-mentioned polyoxo acid metal salt include metal borates and poly borates.
- organometallic compounds include, for example, a compound represented by the general formula (1)
- M represents zinc, tin, or zirconium
- R represents an alkyl group such as a methyl group or an ethyl group, or an alkoxy group such as a methoxy group or an ethoxy group
- n represents 1 to Is an integer of 6
- organic acid metal salts examples include metal stone, metal acetate, metal benzoate, metal salicylate, metal oxalate, metal tartrate, metal lactate, metal citrate and the like.
- metal experiment examples include fatty acid metal salts such as metal laurate, metal myristate, metal palmitate, metal stearate, and metal oleate; metal salts of naphthenic acid; Examples thereof include metal salts, metal salts of sulfonic acids, metal salts of sulfates, and metal salts of phosphate esters.
- octyl replacement paper As the xy compound, only one kind may be used, or two or more kinds may be used in combination.
- the amount of the unsaturated epoxy compound to be used may be set according to the type thereof, the combination with the untreated (meth) acrylic syrup, and the like, and is not particularly limited.
- the molar ratio is more preferably in the range of 0.5 to 2 moles, more preferably in the range of 0.8 to 1.5 moles, relative to the vinyl monomer used in the production of ril syrup.
- the above metal compound is an esterification catalyst containing at least one element selected from the group consisting of zinc, tin and zirconium, and has a high catalytic activity, so that untreated (meth) acrylic syrup has The esterification reaction B between the carboxyl group and the epoxy group of the unsaturated epoxy compound can be mainly promoted.
- Examples of the above metal compounds include inorganic metal compounds, oxo acid metal salts, polyoxo acid metal salts, organic metal compounds, organic acid metal salts, metal complex salts and the like.
- the molding material obtained by using the metal compound is more excellent in storage stability. Further, by using the molding material, it is possible to obtain a molded product having less coloring.
- the inorganic metal compounds include metal halides such as metal fluorides, metal chlorides, metal bromides, and metal iodides; metal chalcogenides such as metal oxides and metal sulfides: metal nitrides; metal phosphorus; Metal arsenide; metal carbide; metal gayide; metal boride; metal cyanide; metal hydroxide; metal chloride oxide and the like. And, specifically, for example, zinc chloride, zirconium oxide, tin sulfide and the like can be mentioned.
- metal halides such as metal fluorides, metal chlorides, metal bromides, and metal iodides
- metal chalcogenides such as metal oxides and metal sulfides: metal nitrides; metal phosphorus; Metal arsenide; metal carbide; metal gayide; metal boride; metal cyanide; metal hydroxide; metal chloride oxide and the like.
- Examples of the above oxo acid metal salts include metal sulfates, metal nitrates, As a result, an esterification reaction (ring-opening reaction) occurs between the carboxyl group of the untreated (meth) acrylyl syrup and the epoxy group of the unsaturated epoxy compound, resulting in a (meth) acryl syrup (hereinafter referred to as “methacrylyl syrup”). Where necessary, a polymerizable double bond can be introduced into (meth) acrylyl syrup E).
- a molding material containing a (meth) acrylic acid ester-based polymer in which a side chain having a polymerizable double bond is bonded to the main chain via an ester bond is obtained.
- the molding material is a metal containing at least one element selected from the group consisting of (meth) acrylyl syrup E into which a polymerizable double bond is introduced via an ester bond, and submarine, tin, and zirconium. And a compound.
- a molding material containing (meth) acrylic syrup E is particularly suitable as a molding material such as SMC, BMC, blend material, casting material, pultrusion molding material, injection molding material, and extrusion molding material.
- (meth) acrylic sap E is thermosetting because it has a polymerizable double bond.
- a polymerizable double bond can be introduced by subjecting a (meth) acrylic acid ester-based polymer having an ethoxy group to an esterification reaction with a vinyl monomer.
- the double bond equivalent in the (meth) acrylic acid ester-based polymer into which the polymerizable double bond is introduced is 200 to It is preferably in the range of 100,000, more preferably in the range of 1,000 to 8,800, and in the range of 2,000 to 5,000. Is most preferably within the range.
- the replacement paper obtained by curing the molding material (Rule 26) Zincate, tin stearate; zinc acetate, tin salicylate and the like.
- the above metal complex salts include, for example, those represented by the general formula (2)
- M represents zinc, tin, or zirconium
- L represents a ligand such as acetylaceton
- n is an integer of 1 to 6.
- the amount of the metal compound to be used may be set according to the type of the metal compound, the combination with an untreated (meth) acrylic sap and an unsaturated epoxy compound, and is not particularly limited. It is more preferable that the amount is within the range of 0.01 to 5 parts by weight, and more preferably within the range of 0.1 to 3 parts by weight, based on 100 parts by weight of the (acrylic) syrup. I like it.
- esterification reaction B when the esterification reaction B is performed, for example, the polymerization inhibitor exemplified above can be allowed to coexist as necessary. Further, when the above esterification reaction B is performed, for example, the above-mentioned solvents can be used as necessary. When performing the esterification reaction B, the esterification catalyst described above can be used instead of the metal compound.
- the order and method of mixing the untreated (meth) acrylic wrap, the unsaturated epoxy compound, and the metal compound are not particularly limited. In short, it suffices that the metal compound be present in the reaction system at the time of the esterification reaction B between the untreated (meth) acryl syrup and the unsaturated epoxy compound.
- Paper (Rule 26) A molded article having excellent surface properties such as surface smoothness and gloss can be obtained.
- thermoplastic polymer is“ dispersed ”in (meth) acrylic syrup C ′ ⁇ E” means that the thermoplastic polymer (dispersed phase) becomes fine particles in (meth) acrylic syrup C ′ ⁇ E. Indicates a scattered state. More specifically, it is assumed that the thermoplastic polymer (disperse phase) is dispersed in (meth) acrylic syrup C ' ⁇ E in the form of fine particles having a particle diameter of 1 mm or less, and the molding material is opaque. Show.
- the term “dissolve” indicates a state in which the dispersed phase has a particle size of about the size of molecules or ions and is dispersed, and the molding material is transparent.
- thermalsetting refers to a property of increasing the viscosity by heating and generating a product insoluble in a solvent by a crosslinking reaction.
- Thermoplasticity refers to the property of decreasing the viscosity by heating and being soluble in at least one kind of solvent. Further, by using a low-shrinkage agent described later in combination with the thermoplastic polymer described here, the shrinkage rate can be more effectively reduced.
- the thermoplastic elastomer has a rubber component (soft component) having an elastic structure and a resin component (hard component) having a structure for preventing plastic deformation in a molecule.
- the thermoplastic resin refers to a thermoplastic polymer having only a resin component (hard component) having a structure for preventing plastic deformation in a molecule and having no rubber elasticity at room temperature.
- Rubber refers to a polymer that exhibits rubber elasticity at room temperature or high temperature.
- thermoplastic elastomer examples include, for example, styrene “ethylene” ⁇ propylene / styrene copolymer (SEPS), and styrene styrene replacement paper (Rule 26) Cracks can be suppressed in the shaped product.
- SEPS propylene / styrene copolymer
- Rule 26 styrene styrene replacement paper
- the double bond equivalent is less than 200, a molded article obtained by curing the molding material may be poor in surface properties such as surface smoothness and gloss.
- the double bond equivalent exceeds 10,000,000, the volume shrinkage of the molding material during curing cannot be sufficiently suppressed, and the surface of the molded product obtained by curing the molding material cannot be obtained. Surface properties such as smoothness and gloss, or heat strength may decrease.
- the weight average molecular weight of the (meth) acrylic acid ester-based polymer when a polymerizable double bond is introduced is preferably in the range of 3,000 to 500,000. More preferably, it is in the range of 5, 000 to 100, 000, and most preferably, it is in the range of 100, 0000 to 40, 0000.
- the weight average molecular weight is less than 3,000, the physical properties of the obtained molded article are reduced.
- the weight average molecular weight exceeds 500,000, the viscosity of (meth) acrylyl syrup E becomes too high, and the workability in molding work and the like deteriorates.
- the molding material containing (meth) acrylic syrup E and the metal compound, or the molding material containing (meth) acrylic syrup C 'described above, may be made of thermoplastic elastomer, thermoplastic resin, or rubber, if necessary. It may contain at least one kind of thermoplastic polymer selected from the group consisting of:
- thermoplastic polymer is dispersed in the (meth) acrylic syrup C ′ ⁇ E.
- the thermoplastic polymer thermally expands when cured by heating, so that the shrinkage of the molding material, that is, the cured product can be efficiently suppressed. That is, since the molding material has a low volumetric shrinkage upon curing, the curing of the molding material allows replacement paper (Rule 26).
- thermoplastic resin examples include, for example, acid-modified vinyl acetate (acid-modified PVAc), vinyl chloride-vinyl acetate copolymer (VC1-1VAc), and ethylene vinyl acetate Copolymer (EVA), cellulose acetate butylate (CAB), acrylonitrile rubber, ethylene propylene rubber / styrene copolymer (AES), acrylyl rubber, acrylyl Examples include nitrile'styrene copolymer (AAS), but are not particularly limited.
- One of these thermoplastic resins may be used alone, or two or more thereof may be used in combination.
- the thermoplastic resin may be appropriately selected according to the type of (meta) acrylic wrap C ' ⁇ E and the like.
- the above rubber examples include styrene butadiene rubber (SBR), hydrogenated styrene butadiene rubber (HSBR), nitrile butadiene rubber (NBR), butadiene rubber (BR), and natural rubber.
- Gen-based rubbers such as rubber and isoprene rubber; chloroprene rubber; butyl rubber; ethylene-propylene rubber; acryl rubber (ACM); urethane rubber; and the like, but are not particularly limited.
- One type of these rubbers may be used alone, or two or more types may be used in combination.
- the rubber may be appropriately selected according to the type of (meth) acrylyl syrup C ′ ⁇ E (the glass transition temperature of the above thermoplastic polymer (hereinafter, referred to as T g) is from 100 ° C. 'is preferably is C, one 7 0 e C ⁇ 3 O' 8 O C Dearuko and more preferably, a 6 0 e Celsius to 0 at which it is most favored arbitrariness.
- T g Gar 1 If it is lower than 00, the surface gloss of the molded article obtained by curing the molding material is reduced, while if the above Tg exceeds 80 ° C, the thermoplastic polymer is unlikely to thermally expand.
- the Tg of the thermoplastic polymer is, for example, replacement paper (Rule 26).
- SEBS Ethylene * butylene, styrene copolymer
- maleic anhydride modified styrene ethylene * butylene * styrene copolymer ( ⁇ !
- Octamodified ⁇ EBS Octamodified ⁇ EBS
- styrene isoprene * styrene copolymer (SIS ), Styrene-butadiene-styrene copolymer (SBS), styrene-ethylene-propylene copolymer (SEP), etc .
- styrene-based thermoplastic elastomer polyester-based thermoplastic elastomer
- polybutene-based thermoplastic Elastomer etc., but are not particularly limited.
- One of these thermoplastic elastomers may be used alone, or two or more thereof may be used in combination.
- the thermoplastic elastomer may be appropriately selected according to the type of the (meta) acrylic syrups C 'and E.
- the styrene-based thermoplastic elastomer is used.
- the styrene thermoplastic elastomer may be linear or radial.
- the styrene content of the styrene-based thermoplastic elastomer is determined based on whether the unreacted vinyl monomer contained in the (meth) acrylic sylcap C ' ⁇ E is methyl methacrylate or not.
- the unreacted vinyl compound is styrene, it is preferably in the range of 10 to 25% by weight, more preferably in the range of 13 to 20% by weight.
- (meth) acrylyl syrup C ′ ⁇ ⁇ contains methyl methacrylate—an unreacted compound other than styrene, for example, t-butyl methacrylate
- the styrene content Is preferably in the range of 10% by weight to 40% by weight, and more preferably in the range of 13% by weight to 30% by weight.
- thermoplastic polymer As a method of dispersing the thermoplastic polymer in the (meth) acrylic syrup C ' ⁇ E, for example, 1) a method of adding the thermoplastic polymer to the (meth) acrylic syrup C' ⁇ E and stirring the mixture; (2) A method in which a thermoplastic polymer is added to the monomer composition and stirred, followed by polymerization: (3) A thermoplastic polymer is added to the vinyl monomer and stirred, and then a (meth) acryl-based polymer is added. A method of adding a polymer; a method of adding a thermoplastic polymer to a vinyl monomer, stirring the mixture, and then adding (meth) acrylic syrup C ′ ⁇ E.
- the stirring may be performed at a stirring speed of about 100,000 rpm using, for example, a high-speed stirrer.
- the stirring time may be appropriately selected according to the stirring speed and the like, but is preferably 1 minute or more, and more preferably 10 minutes or more.
- the method of adding a thermoplastic polymer to (meth) acrylic slurries C 'and E and stirring them is the simplest and most efficient method for producing a molding material. Particularly preferred.
- the molding material according to the present invention is obtained by polymerizing the above-mentioned monomer component containing (meth) acrylic acid ester and a carboxyl group-containing vinyl monomer in the presence of a thiol compound.
- the reaction mixture contains (meth) acrylyl syrup A obtained by treating maleic anhydride and a basic compound.
- the molding material according to the present invention is obtained by polymerizing a monomer component containing a (meth) acrylic acid ester in the presence of a thiol compound, and then treating the reaction mixture with maleic anhydride and a basic compound.
- (Meth) acryl syrup B and vinyl monomer are examples of the thermoplastic polymer.
- the amount of the thermoplastic polymer added is preferably in the range of 2% by weight to 50% by weight, assuming that the total of (meth) acrylic syrup C ′ ⁇ E and the thermoplastic polymer is 100% by weight. More preferably, it is in the range of 5% to 30% by weight-most preferably in the range of 10% to 20% by weight. If the addition amount is less than 2% by weight, the effect of suppressing the shrinkage of the molding material, that is, the cured product, becomes insufficient, so that the volume shrinkage upon curing becomes high, and a molded article having excellent surface properties is obtained. You won't get it. On the other hand, if the addition amount exceeds 50% by weight, the viscosity of the (meth) acrylic syrup C ′ ⁇ E becomes too high, and it becomes difficult to prepare a compound.
- thermoplastic polymer only needs to be stably dispersed in the (meth) acrylic syrup C ' ⁇ E, but more preferably forms a dispersed phase having a particle size of 5 nm to 800 m.
- a dispersed phase with a particle size of 50 nm to 500 m is formed, and a dispersed phase with a particle size of 100 nm to 100 m is formed. Is particularly preferred.
- a molding material containing (meth) acrylic syrup E and a metal compound, or a molding material containing (meth) acrylic syrup C ' may be used as necessary to stabilize the dispersed state of the thermoplastic polymer. Further, a dispersion stabilizer may be further contained. As a result, the preferred combination of (meth) acrylic syrup C ′ ⁇ ⁇ and a thermoplastic polymer is further increased.
- the above-mentioned dispersion stabilizer may be a polymer having, in the molecule, a portion having a high affinity for (meth) acrylic syrup C ′ ⁇ ⁇ and a portion having a high affinity for a thermoplastic polymer.
- Dispersion stabilizers include, for example, thermoplastic polymers. Contains (meth) acrylyl syrup E containing acrylate polymers.
- a vinyl ether compound and / or a vinyl thioether compound are added to the reaction mixture.
- (Meth) acrylyl syrup D obtained by adding the above-mentioned carboxyl-containing vinyl monomer to the reaction mixture.
- Still another molding material according to the present invention is at least one kind selected from the group consisting of (meth) acrylyl syrup E having a polymerizable double bond introduced through an ester bond and zinc, tin, and zirconium. And a metal compound containing an element.
- the molding material according to the present invention further includes, if necessary, a thickener, a succinic acid derivative, a reinforcing material, and the like.
- the molding material can be cured in a shorter time than before.
- components other than the reinforcing material in the molding material will be referred to as a compound.
- Specific examples of the above-mentioned thickener include, for example, magnesium oxide, calcium oxide, etc. Alkaline earth metal oxides; alkaline earth metal hydroxides such as magnesium hydroxide and calcium hydroxide; and the like, but are not particularly limited to the above. These thickeners may be used alone or in combination of two or more.
- the molding material according to the present invention is obtained by adding a vinyl ether compound and a Z or vinyl thioether compound to a reaction mixture obtained by polymerizing a monomer component containing a (meth) acrylic acid ester in the presence of a thiol compound.
- the (meth) acrylic syrup C is a reaction obtained by polymerizing a monomer component containing (meth) acrylic acid ester and a vinyl monomer having a carboxyl group in the presence of a thiol compound.
- a mixture obtained by adding a vinyl ether compound and a vinyl or vinyl thioether compound to the mixture may be used.
- the molding material according to the present invention is characterized in that a monomer component containing a (meth) acrylic acid ester and a vinyl monomer having a carboxyl group are polymerized in the presence of a thiol compound, and a vinyl ether is added to the reaction mixture.
- a monomer component containing a (meth) acrylic acid ester and a vinyl monomer having a carboxyl group are polymerized in the presence of a thiol compound, and a vinyl ether is added to the reaction mixture.
- Add glycidyl (meth) acrylate and / or methyl glycidyl (meth) acrylate to the reaction mixture before or after the compound and Z or vinyl thioether compound are added (Meth) acrylic syrups, including (meth) acrylic acid ester-based polymers, in which the carboxyl group contained in the polymer is esterified, whereby the side chain having a polymerizable double bond is bonded to the main chain. Contains C '
- the molding material according to the present invention is obtained by polymerizing a monomer component containing a (meth) acrylic acid ester and a vinyl monomer having a carboxyl group in the presence of a thiol compound.
- a polymerizable double bond is formed by esterifying the reaction mixture and the unsaturated epoxy compound in the presence of a metal compound containing at least one element selected from the group consisting of zinc, tin, and zirconium.
- the amount of the succinic acid derivative to be added depends on the type thereof, the combination with the (meth) acrylic syrup and the thickener, the use of the molding material, and the like. More preferably, the amount is in the range of 0.01 to 10 parts by weight. If the amount of the succinic acid derivative is less than 0.01 part by weight, the expected action and effect of using the succinic acid derivative are poor. That is, the effect of suppressing the excessive thickening behavior by the thickener may be poor. If the amount of the succinic acid derivative added is more than 10 parts by weight, the viscosity of the compound after the thickening does not reach a predetermined value suitable for molding work or the like, or becomes longer before reaching a predetermined value. May have time.
- the reinforcing material include inorganic fibers such as glass fibers, metal fibers, and fibers made of ceramics (such as boron nitride and silicon carbide); aramid polyester, and carbon fibers. And the like, but are not particularly limited.
- the form of the fiber should be replaced paper (Rule 26) It is more preferably in the range of 10 parts by weight or less, more preferably in the range of 5 parts by weight or less, based on the weight part.
- the amount of the thickener used is more than 10 parts by weight, the viscosity of the compound after the thickening becomes too high, and the workability such as a molding operation is reduced, and the weather resistance and the weatherability of the obtained molded product are reduced. Water resistance may be reduced.
- the above-mentioned succinic acid derivative has a function of suppressing excessive thickening behavior due to the thickener, particularly the initial thickening behavior.
- the succinic acid derivative has a succinic acid skeleton or a succinic anhydride skeleton in the molecule, and an alkyl group, an alkenyl group, an alicyclic hydrocarbon group, an aromatic hydrocarbon group, or the like in an ethylene group portion of the skeleton. It is not particularly limited as long as it is a compound having the following substituents, but a compound having 8 to 30 carbon atoms in total is preferable. Succinic acid derivatives having a total carbon number of 7 or less are not preferred because of their poor solubility in (meth) acrylic syrup.
- a succinic acid derivative having a total carbon number of 31 or more has poor expected action and effect by using the succinic acid derivative. That is, it is not preferable because the effect of suppressing the excessive thickening behavior by the enlarging agent is low.
- succinic acid derivatives include, for example, hexyl succinic acid, heptyl succinic acid, octyl succinic acid, nonyl succinic acid, decyl succinic acid, dodecyl succinic acid, tetradecyl succinic acid, and pen decyl succinic acid.
- the reinforcing material is a roving chopped strand, or the like
- the reinforcing material and the compound are kneaded, or the reinforcing material is sandwiched between compounds to be impregnated. I just need to.
- the molding material according to the present invention desirably contains a curing agent (polymerization initiator), and further includes, if necessary, a filler, a crosslinkable monomer (crosslinking agent), an additive, and the like. May be included.
- a curing agent polymerization initiator
- crosslinking agent crosslinkable monomer
- Examples of the above-mentioned curing agent include, but are not particularly limited to, the above-described polymerization initiator used in producing the (meth) acryl syrup.
- the amount of the curing agent to be added may be set according to the type thereof, the combination with (meth) acrylic syrup, and the like, and is not particularly limited. However, the amount of (meth) acrylic syrup is 100% by weight. It is preferably in the range of 0.1 parts by weight to 5 parts by weight based on parts.
- the above-mentioned filler include, for example, aluminum hydroxide, calcium carbonate, barium sulfate, alumina, clay, talc, minoredov ivar, silica (silica sand), river sand, diatomaceous earth, mica powder, gypsum, and cold water.
- Inorganic fillers such as stone (sand), asbestos powder, glass powder, and glass spheres; and organic fillers such as Bolima beads; are not particularly limited. These fillers may be used alone or in combination of two or more.
- the form of the filler, such as the average particle size, is not particularly limited.
- the amount of the filler is determined by the type, combination with (meth) acrylic syrup, etc., and the use of the molding material.
- roving, cloth, mat, woven fabric, chopped roving, chopped strand, and the like are not particularly limited.These reinforcing materials may be used alone, or two or more types may be used. You may use them together.
- a molding material containing a reinforcing material is suitable, for example, as SMC or BMC.
- the length of the reinforcing material is particularly preferably 1 mm or more and 6 mm or less. This makes it possible to further improve the strength, surface smoothness, and gloss of a molded product obtained by molding the molding material.
- the amount of the reinforcing material used is preferably in the range of more than 0 to 40% by weight or less based on the total weight of the molding material, but is not particularly limited, and the type, (meth) acryl syrup, etc. May be set in accordance with the combination of the above, the use of the molding material and the desired physical properties.
- the amount of the reinforcing material used is more preferably in the range of 10% by weight to 40% by weight based on the total weight.
- the amount of the reinforcing material used is more preferably in the range of 2% by weight to 30% by weight based on the total weight.
- the amount of the reinforcing material is preferably in the range of 1 to 9% by weight based on the total weight of the molding material.
- the method of mixing the reinforcing material and the compound is not particularly limited.
- the amount of the monomer to be added may be set according to the type thereof, the combination with (meth) acrylic syrup and the like, the use of the molding material, the desired physical properties, and the like, and is not particularly limited.
- the above-mentioned crosslinkable monomer is added as necessary when polymerizing the monomer composition in the presence of the thiol compound or when polymerizing the monomer component in the presence of the thiol compound. You can also.
- the amount of the crosslinkable monomer to be added may be set according to the type, combination with the monomer composition (or monomer component), etc., the use of the molding material, the desired physical properties, and the like. And is not particularly limited.
- additives various commonly used additives can be employed, and are not particularly limited. Examples thereof include a low shrinkage agent, a (internal) release agent, a colorant, and a polymerization inhibitor. And the like. These additives may be appropriately added depending on, for example, the use of the molding material and the desired physical properties.
- the amount of the additive may be set according to the type of the additive, a combination with (meth) acrylyl syrup, or the like, and is not particularly limited.
- Specific examples of the low-shrinkage agent include methyl polymethacrylate, polyethylene, polypropylene, polystyrene, polyethylene glycol, polypropylene glycol, cellulose butyrate, and acetate.
- thermoplastic polymers not containing a carboxyl group such as poly (vinyl chloride), polyvinyl acetate, poly (caprolactone), and saturated polyester.
- thermoplastic polymers not containing a carboxyl group such as poly (vinyl chloride), polyvinyl acetate, poly (caprolactone), and saturated polyester.
- a low shrinkage agent By adding a low shrinkage agent, the curing shrinkage of the molding material can be suppressed, so that the dimensional stability of the molding can be further improved.
- the weight average molecular weight of the above-mentioned low shrinkage agent that is, the thermoplastic polymer
- the weight average molecular weight of the above-mentioned low shrinkage agent, that is, the thermoplastic polymer is 0.
- Replacement paper (Rule 26)
- a range of 100 parts by weight to 600 parts by weight with respect to 100 parts by weight of (meth) acrylic syrup is preferable.
- the amount of the filler is preferably in the range of 30 parts by weight to 300 parts by weight with respect to 100 parts by weight of (meth) acrylyl syrup. preferable.
- the amount of the filler is in the range of 150 parts by weight to 600 parts by weight with respect to 100 parts by weight of (meth) acrylic syrup. Is more preferable.
- the amount of the filler is in the range of 30 parts by weight to 350 parts by weight based on 100 parts by weight of (meth) acrylic syrup. Is more preferable.
- the amount of the filler is from 10 parts by weight to 200 parts by weight with respect to 100 parts by weight of the (meth) acrylic syrup. Within the range is more preferable.
- the crosslinkable monomer has a function of increasing the crosslink density of the cured product.
- the crosslinkable monomer may be a compound containing a plurality of functional groups that react with the functional groups contained in the (meth) acryl syrup.
- crosslinkable monomer examples include, for example, ethylene glycol di (meth) acrylate, diethylene glycol di (meth) acrylate, propylene glycol (meta) Attalylate, dipropylene glycol (meta) acrylic, neopentyl glycol (meta) atalylate, trimethylolpropane tri (meta) acrylate, pentaerythrate Polyfunctional (meta) acrylates, such as thoritol tetra (meta) acrylate; eboxy (meta) acrylates; divinylbenzene, diarylphthalate, divinylbenzene But not limited thereto, but include, but are not limited to, triarylsophthalate, trilulicyanurate, and trilulian cyanurate.
- the method for curing the molding material that is, the method for producing the molded product is not particularly limited.
- the molding material according to the present invention can be applied to various molding methods such as a compression molding method, an injection molding method, and a transfer molding method, but the compression molding method is particularly preferable.
- the molding pressure may be set according to the shape, size, etc. of the molded product to be manufactured, and is not particularly limited, but is preferably about 0.1 MPa to 20 MPa.
- the molding time may be appropriately set in consideration of molding conditions such as molding temperature and molding pressure, and the curing speed of the molding material, and is not particularly limited.
- the method for producing (meth) acrylic syllap A comprises the steps of: polymerizing a monomer component and a vinyl monomer in the presence of a thiol compound; This is a method of treating with maleic acid and a basic compound.
- the method for producing (meth) acrylyl syrup B according to the present invention comprises the steps of: polymerizing a monomer component in the presence of a thiol compound; treating the reaction mixture with maleic anhydride and a basic compound; In this method, a vinyl monomer is added to the reaction mixture.
- the method for producing (meth) acrylic syllap C comprises the steps of: adding a vinyl ether compound to a reaction mixture obtained by polymerizing a monomer component containing a (meth) acrylic ester in the presence of a thiol compound; This is a method of adding a Z or vinyl thioether compound.
- the method for producing (meth) acrylic syrup C according to the present invention is characterized in that a monomer component containing (meth) acrylic acid ester and a replacement paper containing a carboxyl group (Rule 26) More preferably, it is not less than 00 and not more than 200,000.
- a monomer component containing (meth) acrylic acid ester and a replacement paper containing a carboxyl group (Rule 26) More preferably, it is not less than 00 and not more than 200,000.
- the amount of the low-shrinkage agent to be added may be set according to the type, combination with (meth) acryl syrup, etc., the use of the molding material and the desired physical properties, etc., and is not particularly limited.
- the amount is preferably in the range of 5 parts by weight to 50 parts by weight based on 100 parts by weight of (meth) acrylic syrup.
- the release agent include, for example, stearate, zinc stearate, aluminum stearate, calcium stearate, barium stearate, amide stearate, and triphenylphospho.
- Felt alkyl phosphate; commonly used waxes, release agents such as silicone oil: and the like.
- the coloring agent include known inorganic pigments and organic pigments.
- the molding material having the above configuration is suitable as SMC, BMC, casting material, and the like.
- SMC can be easily manufactured using a so-called SMC manufacturing device.
- BMC can be easily manufactured using a kneading machine such as a double-arm kneader.
- Casting material, c can be readily prepared using a mixer and, SMC or BMC, for example 6 0.
- press molding By heating and press forming (press molding) at C to 160 ° C, more preferably at 70 to 140 ° C, more preferably at 80 to 130 ° C It is a molded product.
- casting material is a molded article by injecting (casting), for example cell at room temperature ⁇ 7 0 e C.
- Each of the above molding materials can be cured in a shorter time than before, and have excellent properties such as heat resistance, solvent resistance, weather resistance and water resistance, as well as surface smoothness and gloss. It is possible to provide a molding material capable of obtaining a molded article having excellent surface properties such as the above and dimensional stability. Further, a molding material containing (meth) acrylyl syrup E and a metal compound is more excellent in storage stability, and by using the molding material, is excellent in heat strength and less colored. Goods can be obtained.
- Examples of molded articles obtained by molding the molding material according to the present invention include various articles used outdoors such as so-called daylighting domes, benches, tables, tanks, public notice boards, waterproof boards, etc .; Components that make up railcars, ships, etc .; Roofs, walls, and other structural exterior materials; Bathtubs, kitchen counters (kitchen tops), various counter tops, artificial marble suitable for washstands, etc .; Electrical parts; and the like, but are not particularly limited.
- the molded article is excellent in aesthetic appearance and is suitable for various uses requiring the aesthetic appearance.
- a molded article formed by molding a molding material containing a filler has a beautiful marble-like pattern, and is therefore most suitable as an artificial marble.
- a vinyl ether compound and a Z or vinyl thioether compound may be added to a reaction mixture obtained by polymerizing a vinyl monomer to be reacted in the presence of a thiol compound.
- the method for producing a (meth) acrylic syrup C ′ comprises the steps of: (a) preparing a monomer component containing a (meth) acrylic acid ester and a vinyl monomer containing a carboxyl group into a thiol compound; After polymerization under the reaction mixture, before or after adding the vinyl ether compound and the z or vinyl thioether compound to the reaction mixture, glycidyl (meth) acrylate and / or (meth) acrylyl are added to the reaction mixture.
- a side chain having a polymerizable double bond is bonded to a main chain by adding methyl glycidyl acid and esterifying a carboxyl group contained in the polymer.
- a monomer component containing (meth) acrylic acid ester is polymerized in the presence of a thiol compound, and then a vinyl ether compound and Z are added to the reaction mixture.
- a vinyl thioether compound is added, and the above vinyl monomer having a carboxyl group is added to the reaction mixture.
- the method for producing (meth) acrylyl syrup E according to the present invention comprises: polymerizing a monomer component containing a (meth) acrylic ester with a vinyl monomer having a carboxyl group in the presence of a thiol compound.
- (Meth) acrylic syrup (untreated (meth) acrylic syrup) and an unsaturated epoxy compound containing at least one element selected from the group consisting of zinc, tin and zirconium According to each of the above methods, there is no odor caused by the thiol compound, and molding and replacement paper (Rule 26) As a result, (meth) acrylic syrup A according to the present invention was obtained.
- the viscosity of (meth) acrylic A is 7 Boys (25 ° C), and the ratio of polymer in acrylic (A) is 23.5%. there were.
- the weight average molecular weight (M w) of the (meth) acrylyl syrup A measured by gel permeation chromatography (GPC) was 61,000.
- the casting material is cast using a cell in which the surroundings of two glass plates facing each other with a distance (gap) of 3 mm between each other are closed with a so-called elastic gasket. did. That is, after the casting material was poured into the above-mentioned cell, it was cured by heating to 60 eC .
- the gel time (gelation time) at 60 ° was measured based on JISK6901. That is, a casting material, which is a sample, is put into a test tube having a diameter of 18 mm so as to have a depth of 100 mm, and is then held in a thermostat adjusted to a temperature of 60. The time required for the temperature of the casting material to rise from 65 to 65 by the heat of reaction was measured, and this time was taken as the gel time. ⁇ As a result, the gel time at 60'C was 45 minutes. Met.
- the viscosity of the reaction solution became 30 to 35 vise (25 ° C.), and the reaction was terminated at this point (that is, the reaction time was The reaction solution was further added with 35 parts of methyl methacrylate, and then cooled (rapidly cooled) at 40.
- Example 1 the same operation as in Example 1 was performed to obtain a casting material for comparison.
- the same casting as in Example 1 was performed using the obtained casting material for comparison to obtain a resin plate for comparison.
- the gel time was 58 minutes.
- the obtained comparative resin plate was insoluble in THF and acetate and had good solvent resistance.
- the comparative casting material was inferior in storage stability.
- Table 1 The main reaction conditions and the results are shown in Table 1.
- Example 1 The same reaction and treatment as in Example 1 were carried out, except that the used amount (prepared amount) of methyl methacrylate in Example 1 was changed from 196 parts to 200 parts and methacrylic acid was not used.
- a (meth) acrylic sham for comparison was prepared. The reaction time was 500 minutes. The viscosity of the obtained (meth) acryl syrup for comparison was 6 boys (25 ° C), the solid content was 21.9%, and the weight average molecular weight was 61,000. Was.
- the same operation as in Example 1 was performed to obtain a casting material for comparison. The obtained comparative casting material was excellent in storage stability.
- the same casting as in Example 1 was performed to obtain a resin plate for comparison. The gel time was 69 minutes. However, the obtained comparative resin plate was soluble in THF and acetone, and had poor solvent resistance.
- Table 1 The main reaction conditions and the results are shown in Table 1.
- Example 1 was repeated except that the amount of methyl methacrylate used (prepared amount) in Example 1 was changed from 196 parts to 184 parts, and the amount of methacrylic acid was changed from 4 parts to 16 parts.
- the same reaction and treatment as in Example 1 were carried out to prepare (acrylic syrup A).
- the reaction time was 300 minutes.
- a resulting (meth) Viscosity accession Rirushirappu A 8 Boyes (2 5 e C) a solid content of 2 2.3%, weight average molecular weight is met 6 4, 0 0 0 Was.
- Example 1 the same operation as in Example 1 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same casting as in Example 1 was performed to obtain a resin plate.
- the gel time was 30 minutes.
- the obtained resin plate was insoluble in THF and acetate, and had good solvent resistance.
- the main reaction conditions and the results are shown in Table 1.
- Example 3 The same reaction and the like as in Example 1 were performed in Example 1 except that maleic anhydride and triethylamine were not used, to prepare (meth) acrylyl syrup for comparison. That is, a (meth) acryl syrup for comparison was prepared by not treating the added n-dodecyl mercapone.
- the viscosity of the resultant comparative (meth) acrylate Rirushirabbu 7 is Boyes (2 5 e C), a solid content of 2 4.1%, filed example paper weight average molecular weight is 6 2, 0 0 0 (Rule 26) (Example 3)
- the compound is applied to the polyethylene film surface so as to have a constant thickness, and a glass arrowhead (a 1-inch-length chopped roving) as a reinforcing material is evenly applied on the applied material. Scattered. Then, on top of this, an applied material obtained by applying the compound on the surface of the polyethylene film so as to have a constant thickness was superimposed. In other words, glass fiber was sandwiched between the compounds. As a result, SMC was obtained as a molding material. The ratio of the above glass fibers in the SMC was adjusted to be 25%. Thereafter, the obtained SMC was packed in cellophane film and aged at 40 C for 1 day. After aging, the compound, that is, the SMC was not hardened, and the surface of the SMC was not sticky.
- a glass arrowhead a 1-inch-length chopped roving
- the above SMC was heated and pressed. That is, a mold having a predetermined size was used, and the temperature of the upper mold was set at 110 ° C and the temperature of the lower mold was set at 100 ° C. Then, SMC cut to a predetermined size is applied to the above-mentioned mold, clamped at a pressure of 6 MPa, and heated and pressed for 10 minutes to form a molded product having a thickness of A 3 mm plate was created.
- the gel time at 110 ° C is determined using a Curastrameter V (Replacement paper (Rule 26)
- Example 1 2 Methyl methacrylate (parts) 19 6 1 8 4 t 10 ⁇ 5 ⁇ 10 ⁇ 5 >>
- Example 1 the amount of methyl methacrylate used (prepared amount) was changed from 196 parts to 19.9 parts, and the amount of methyl methacrylate was changed from 4 parts to 0.6 parts. Other than the above, the same reaction and processing as in Example 1 are performed.
- Replacement paper (Rule 26) Orientec) was used as a measuring device. That is, the sample SMC is heated to 110, and the time from when the temperature is reached (at the start of heating) to when the torque measured by the above measuring device rises is measured, and this time is defined as the gel time. did. As a result, the gel time at 110 ° C. was 200 seconds.
- the obtained molded article had a gloss on its surface and was excellent in smoothness.
- the molded product was insoluble in THF and acetone, and had good solvent resistance.
- no substantial discoloration or chalking was observed in the molded product.
- the molded article after the test had a gloss on its surface, and a substantial change was observed.
- the molded article was left in an oven set at 170 ° C for 1 hour, and the heat resistance was evaluated. As a result, the molded article did not show any change in appearance such as yellowing. The surface gloss was not lost. Table 2 summarizes the main reaction conditions and results described above.
- Example 3 First, the same reaction, treatment, and the like as in Example 2 were performed to prepare (meth) acrylyl syrup A. Next, using this (meth) acrylyl syrup A, the amount of magnesium oxide used in Example 3 was changed from 1 part to 2 parts, and the amount of pendedodecenylsuccinic acid was changed from 1 part to 3 parts. Other than the above, the same operation and molding as in Example 3 were performed to produce a molded product. The gel time was 16.5 seconds. The obtained molded article had a gloss on its surface and was excellent in smoothness. In addition, the main replacement paper for obtaining the above molded article (Rule 26) 68,000.
- Example 2 Subsequently, the same operation and casting as in Example 1 were performed to obtain a comparative molded product, and the c- gel time was 17 minutes. Further, the obtained comparative molded article was insoluble in THF and acetate, and had good solvent resistance.
- Example 3 the same operation and molding as in Example 3 were performed using the above (meta) acryl syrup for comparison to produce a molded article for comparison.
- the surface of the compound that is, the surface of the comparative SMC was not sticky.
- the gel time was 120 seconds.
- the obtained comparative molded product was insoluble in THF and acetate, and had good solvent resistance. Furthermore, the molded product was excellent in heat resistance. However, the comparative molded product was inferior in weather resistance and water resistance. Table 3 summarizes the above main reaction conditions and results.
- Example 1 Except that the addition amount of maleic anhydride in Example 1 was changed from 0.7 part to 0.2 part, and the addition amount of triethylamine was changed from 0.04 part to 0.004 part. The same reaction and treatment as in Example 1 were performed to prepare (meth) acrylic syrup for comparison.
- the above-mentioned maleic anhydride was added so that it might become 0.4 times mol with respect to the added n-dodecyl mercaptan. Further, the above-mentioned triethylamine was added so as to be 0.008-fold mol with respect to the added n-dodecylmer force.
- the viscosity of the obtained (meth) acryl syrup for comparison was 7 boys (25 ° C.), the solid content was 21.1%, and the weight average molecular weight was 63,000. Was.
- Example 2 Subsequently, the same operation and casting as in Example 1 were performed to obtain a resin plate for comparison ( gel time was 65 minutes. However, the obtained resin plate for comparison was THF and acetate. And the solvent resistance was poor.
- Example 3 Next, the same operation and the like as in Example 3 were performed using the above-mentioned (meta) acryl syrup for comparison to obtain a SMC for comparison.
- the obtained comparative SMC was aged at 40 ° C. for 1 day. However, the surface of the comparative SMC was slightly sticky.
- Example 3 Next, the same operation, molding, and the like as in Example 3 were performed using this comparative SMC to produce a comparative molded product.
- the gel time was 230 seconds.
- the obtained comparative molded product gradually dissolved in THF and acetate, and had poor solvent resistance.
- the molded article for comparison showed a slight change in appearance such as yellowing.
- the main reaction conditions described above and the results are summarized in Table 3.
- Example 1 was repeated except that the amount of methyl methacrylate used (prepared amount) was changed from 196 parts to 150 parts and the amount of methacrylic acid was changed from 4 parts to 50 parts in Example 1.
- the same reaction and treatment as in Example 1 were performed to prepare (meth) acryl syrup for comparison.
- the reaction time was 240 minutes.
- the aluminum hydroxide 100 parts and glass powder as a filler (Nitto Boseki Co., Ltd., FMB300W-001) 50 parts.
- a molded product was prepared by performing the same operation, molding, and the like as in Example 3 except that was mixed.
- Example 1 instead of 35 parts of methyl methacrylate added after the completion of the polymerization reaction, 25 parts of methyl methacrylate and 25 parts of trimethylolpropane trimethyl acrylate as a crosslinkable monomer were added. Except for adding 0 parts, the same reaction and treatment as in Example 1 were carried out to prepare (meth) acrylyl syrup A.
- the viscosity of the obtained (meth) acrylyl syrup A was 8 boys (25 ° C.), the solid content was 21.7%, and the weight average molecular weight was 62,000. .
- Example 3 Next, using this (meth) acryl syrup A, the same operation and molding as in Example 3 were performed to produce a molded product.
- the gel time was 180 seconds.
- the obtained molded article had gloss on its surface and was excellent in smoothness.
- Table 2 summarizes the main reaction conditions and results of the above molded products.
- Example 2 First, the same reaction and treatment as in Example 2 were performed to prepare (meth) acrylyl syrup A. Next, the amount of magnesium oxide used in Example 3 was changed from 1 part to 2 parts by using the (meth) acrylic sialp A, and the amount of pendecose dodecenylsuccinic acid was changed from 1 part to 3 parts. Modified, and instead of aluminum hydroxide (150 parts), aluminum hydroxide (100 parts) and calcium carbonate as filler (Whiteton P-70, manufactured by Toyo Fine Chemicals Co., Ltd.), 50 parts A molded article was prepared by performing the same operation, molding, and the like as in Example 3 except that was mixed. After aging, the surface of the compound, that is, the surface of SMC was not sticky. The gel time was 160 seconds.
- the obtained molded article had a gloss on its surface and was excellent in smoothness.
- Table 2 summarizes the main reaction conditions and results of the above molded products. Furthermore, the molded product was excellent in heat resistance. In addition, as a result of evaluating the weather resistance and the water resistance, the molded article was excellent in these physical properties although slight discoloration and a slight decrease in gloss were observed as compared with the molded article of Example 4. , (Example 6)
- Example 8 First, the same reaction, treatment, and the like as in Example 1 were performed to prepare (meth) acrylyl syrup A. Next, 100 parts of the (meth) acrylic syrup, 1 part of magnesium oxide, 2 parts of pendedodecenylsuccinic acid, 1 part of t-butylperoxy-1-ethylhexanoate, 1 part of zinc stearate, 4 parts of water After mixing 350 parts of aluminum oxide (Hygirite H-320, manufactured by Showa Denko KK) and glass fiber (a 1/4 inch long chopped strand) as a reinforcing material, This mixture was kneaded using a double-arm kneader. As a result, BMC as a molding material was obtained. The ratio of the glass fiber in the BMC was adjusted to be 5%. Then get
- Acetone insoluble insoluble insoluble insoluble insoluble insoluble insoluble heat resistance good good good good good good good good good good good good weather resistance good good good good good good good good good good good good good good good good good good good good good good good good good good good good good good good water resistant good good good good good good good Good Good Good
- the obtained artificial marble plate had a glossy surface, was excellent in smoothness, and had a so-called high-grade feel and texture.
- Table 4 summarizes the main reaction conditions and results of the above artificial marble plate.
- the obtained artificial marble plate for comparison was soluble in THF and acetate, and had poor solvent resistance. Further, as a result of evaluating the heat resistance, the artificial artificial marble plate for comparison showed a change in appearance such as yellowing and the gloss of the surface was lost, resulting in unevenness. Table 5 summarizes the above main reaction conditions and results.
- a molded product was prepared by subjecting the above BMC to heat and pressure molding by a predetermined method.
- the gel time was 190 seconds.
- the obtained molded article had gloss on its surface and was excellent in smoothness.
- Table 4 summarizes the main reaction conditions and results of the above molded products.
- Example 11 the same reaction and treatment as in Example 2 were performed to prepare (meth) acrylyl syrup A.
- 100 parts of the (meth) acrylic syrup A was mixed with 1 part of bis (4-t-butyl sulphate) carbonyl oxide as a curing agent, and aluminum hydroxide (manufactured by Showa Denko KK, Replacement form (Rule 26) (Example 11)
- the reactor (2) was exchanged with nitrogen gas. Next, the temperature was raised to 80 while stirring the above methyl methacrylate, and then 0.1 part of AIBN and 1.0 part of n-dodecylmercaptan were added to initiate a polymerization reaction. After the initiation of the polymerization reaction, the reaction is terminated when the viscosity of the reaction solution reaches 30 to 35 boises (25 te), and the reaction solution is mixed with 25 parts of methyl methacrylate and methyl methacrylate. After further adding 10 parts, the mixture was cooled (rapidly cooled) to 40 ° C.
- Example 10 Next, the same operation, molding, and the like as in Example 10 were performed using the (meth) acrylyl syrup B to produce an artificial marble plate.
- the casting material that is, the compound, was excellent in storage stability.
- the obtained artificial marble plate had a glossy surface, was excellent in smoothness, and had a so-called high-grade feel and texture.
- Table 4 summarizes the main reaction conditions and results of the above artificial marble plate.
- the obtained casting material was cast using a glass cell. That is, after the casting material was injected into the above cell, it was cured at 60 ° C. for 1 hour. After removal from the mold, post-curing was performed at 100 eC for 2 hours to obtain an artificial marble plate as a molded product.
- the obtained artificial marble plate had a glossy surface, was excellent in smoothness, and had a so-called high-grade feel and texture.
- Table 4 summarizes the main reaction conditions and results of the above artificial marble plate. Replacement form (Rule 26) Example 1 0 1 1 Magnesium oxide (parts)
- Pentato'decenyl succinic acid (parts) 2 Hydroxylamine (parts) 3 5 0 2 0 0 2 0 0 2 0 0 2 0 0 Molding material after aging Good good Gel time (seconds) 19 0
- Aceton insoluble insoluble insoluble insoluble insoluble insoluble insoluble good good good good good good good good weatherproof good good good good good good good good good good good good good good good water resistance good good good good good good good good
- Example 10 Next, 5 parts of methyl methacrylate was added to 95 parts of the (meth) acrylic syrup, and the same operation and molding as in Example 10 were performed to produce an artificial marble plate.
- the casting material that is, the compound, was excellent in storage stability.
- the obtained artificial marble plate had a glossy surface, was excellent in smoothness, and had a so-called high-grade feel and texture.
- Table 5 summarizes the main reaction conditions and results of the above artificial marble plate.
- (meth) acryl syrup C ′ was obtained.
- the method according to the present example provides (meth) acrylic syrups A and B having excellent storage stability when used as a molding material. It can be seen that it can be manufactured in a shorter time than in the past. Further, it can be seen that the molding material according to the present example is suitable for heat and pressure molding and can be cured in a relatively short time. Furthermore, it is understood that the obtained molded article is excellent in various physical properties such as heat resistance, solvent resistance, weather resistance and water resistance.
- Example 13 A reactor equipped with a thermometer, a cooler, a nitrogen gas inlet pipe, and a stirrer was charged with 194 parts of methyl methacrylate and 6 parts of methacrylic acid.
- Example 13 the same reaction and treatment as in Example 13 were performed except that isobutyl vinyl ether was not used. As a result, a (meth) acrylyl syrup having a gradually increased viscosity during the esterification and an increased solid content, viscosity, and weight average molecular weight was obtained.
- Example 13 the same operation as in Example 13 was performed to obtain a casting material for comparison.
- casting was performed in the same manner as in Example 13 to obtain a resin plate for comparison.
- Gel time at 6 0 e C was 6 0 minutes.
- the comparative casting material obtained was poor in storage stability.
- the obtained comparative resin plate swelled in THF and acetone. Table 6 shows the main reaction conditions, and Table 7 shows the results.
- Example 13 Except for changing the order of the thiol treatment and the esterification in Example 13, the same reaction and treatment as in Example 13 were performed to obtain (meth) acrylyl syrup C ′.
- the obtained (meth) acrylyl syrup C ′ had a solid concentration of 50, a viscosity of 150 boise, an acid value of 11, and a weight average molecular weight of 58,000.
- Example 13 the same operation as in Example 13 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same casting as in Example 13 was performed to obtain a resin plate.
- Gel time at 60 ° C was 30 minutes, replacement paper (Rule 26) The number was calculated. From the number of moles of polymerizable double bond in 1 g of (meth) acrylic polymer and the number of moles of 1 g of (meth) acrylic polymer, the number of double bonds per molecule of (meth) acrylic polymer is calculated. The number was calculated. As a result, the number of double bonds per molecule was 5.3.
- Example 14 the casting material was injected into a cell similar to the cell of Example 1, and then cured by heating to 60 °.
- the gel time was measured in the same manner as in Example 1. As a result, the gel time at 60 ° C. was 30 minutes.
- post-curing (so-called after-curing) was performed at 100 ° C. to obtain a resin plate as a molded product.
- the obtained resin plate was insoluble in THF and acetate. That is, the above resin plate was excellent in solvent resistance.
- Table 6 shows the main reaction conditions described above, and Table 7 shows the results. (Example 14)
- Example 13 The same reaction and treatment as in Example 13 were performed, except that 3,4-dihydro 2 H-pyran was used in place of isoptylvinyl ether in Example 13 as the vinyl ether compound.
- Acrylic syrup C ' was obtained.
- the resulting (meth) acrylic syrup C ' had a solid content of 43%, a viscosity of 31 Boys, an acid value of 11, and a weight average molecular weight of 39,000.
- isoptyl vinyl ether was added to the above reaction mixture, and then the temperature was raised to 100 and the mixture was stirred for 1 hour to treat n-dodecylmercaptan remaining in the reaction mixture.
- the above isoptyl vinyl ether was added so as to be 2.0-fold mol with respect to the n-dodecylmer compound added during the polymerization.
- (meth) acrylic slab C was obtained.
- the resulting (meth) acrylic syrup C had a solid content of 24, a viscosity of 7 boise, an acid value of 12, and a weight average molecular weight of 61,000.
- Example 13 the same operation as in Example 13 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same casting as in Example 13 was performed to obtain a resin plate. 6 0 gel time at ° C also 4 0 minutes and was the t, solvent resistance of the obtained resin plate was good.
- Table 8 shows the main reaction conditions and Table 9 shows the results.
- Example 18 The same reaction and treatment as in Example 18 were carried out in Example 18 except that isobutyl vinyl ether was not used, to obtain (meth) acrylyl syrup.
- Example 13 The same operation as in Example 13 was performed with a gun to obtain a casting material for comparison. Next, using the obtained casting material for comparison, the same casting replacement as in Example 13 (Rule 26) Subsequently, glycidyl methacrylate, 0.1 part of triphenylphosphine, and 0.01 part of hydroquinone were added, and the mixture was stirred at 100 ° C for 8 hours to be esterified. The reaction was performed. The above-mentioned glycidyl methacrylate was added so as to be 1.0-fold the molar amount of methacrylic acid. Thus, (meth) acrylic syrup C ′ was obtained. The resulting (meth) acrylic syrup C ′ had a solid content of 52%, a viscosity of 39 boise, an acid value of 27 and a weight average molecular weight of 14,000.
- Example 13 the same operation as in Example 13 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same casting as in Example 13 was performed to obtain a resin plate.
- the gel time at 6 0 e C was 1 5 min ⁇ Additionally, solvent resistance of the obtained resin plate was good.
- Table 8 shows the main reaction conditions described above, and Table 9 shows the results.
- Example 16 Except that the amount of methyl methacrylate used (prepared amount) in Example 16 was changed from 180 parts to 196 parts and the amount of methacrylic acid was changed from 20 parts to 4 parts. Then, the same reaction and treatment as in Example 16 were performed to prepare (meth) acrylyl syrup C ′.
- Example 13 the same operation as in Example 13 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same casting as in Example 13 was performed to obtain a resin plate. 6 0 gel time at ° C also 4 0 minutes and was the c, solvent resistance of the obtained resin plate was good.
- Table 8 shows the main reaction conditions and Table 9 shows the results.
- Example 19 The same reaction, treatment, and the like as in Example 19 were performed in Example 19 except that isobutyl vinyl ether was not used, to obtain a beaded polymer. Then, by the addition of I Sopuchiru ether was heated and the resulting beads Borima to 2 4 0 e C, n you remain in the in beaded polymer - was treated dodecylmercapto turnip Yun. The above-mentioned isobutyl vinyl ether was added in a molar amount of 3.0 times the n-dodecyl mercaptan added during the polymerization.
- Example 10 summarizes the above main reaction conditions and results. Replacement form (Rule 26) Example Example Comparative Example
- Weight average molecular weight (Mw) 14,000 13,000 61,000 60,000 Number of double bonds per molecule 7.6 1.8
- the mixture was added to the reactor, and stirred at 500 rpm to form a uniform suspension. Subsequently, the temperature was raised to 75 while blowing nitrogen gas, and stirring was continued at this temperature for 5 hours to carry out a suspension polymerization reaction.
- Reaction temperature (° C) 9 0 2 4 0 Reaction time (hr) 1.0 Adhesion of carbide to screw No No Yes Yes No odor due to thiol No No Yes
- Example 21 First, the same reaction and treatment as in Example 13 were performed to prepare (meth) acrylyl syrup C '. Next, 1 part of magnesium oxide, 1 part of pentadodecenylsuccinic acid, 1 part of tert-butylperoxy-2-ethylethyl hexanoate, 1 part of zinc stearate, Part and aluminum hydroxide (manufactured by Showa Denko KK, Highlight
- Example 20 the same reaction and treatment as in Example 20 were performed to obtain a beaded polymer. Subsequently, the same operation as in Example 20 was performed except that no isobutyl vinyl ether was added, and a pellet for comparison was prepared. At this time, a large amount of carbide was attached to the screw. At the time of pellet preparation, an odor was considered to be attributed to the titanium compound.
- Table 10 The main reaction conditions described above and the results are summarized in Table 10.
- Example 21 First, the same reaction, treatment, and the like as in Example 14 were performed to prepare (meth) acrylyl syrup C ′. Next, using this (meth) acrylyl syrup C ', the amount of magnesium oxide used in Example 21 was changed from 1 part to 2 parts, and the amount of pendedodecenylsuccinic acid was changed from 1 part to 3 parts. Except for the change, the same operation and forming as in Example 21 were performed to form a formed plate. The gel time at 110'C was 100 seconds. The obtained molded plate had a gloss on its surface and was excellent in smoothness. Table 11 summarizes the main reaction conditions and results of the above molded plate.
- the compound was applied on the surface of the polyethylene film so as to have a constant thickness, and then glass fibers (1 inch long chopped roving) as a reinforcing material were uniformly spread on the applied material. Then, on top of this, an applied material formed by applying the compound to the surface of the polyethylene film so as to have a constant thickness was overlaid. In other words, glass fiber was sandwiched between the compounds. As a result, SMC was obtained as a molding material. The ratio of the above glass fibers in the SMC was adjusted to be 25%. Then, the obtained SMC was packed in cellophane film and aged at 40 ° C for 1 day.
- the above SMC was subjected to heat and pressure molding. That is, a mold having a size of 200 mm ⁇ 200 mm was used, and the temperature of the upper mold was set at 110 ° C. and the temperature of the lower mold was set at 100 ° C. Then, the SMC cut to a predetermined size is filled in the above mold, clamped at a pressure of 6 MPa, and heated and pressed for 5 minutes to form a molded product having a thickness of 3 mm. Was formed.
- the obtained molded plate had a gloss on its surface and was excellent in smoothness.
- the molded plate was insoluble in THF and acetone, and had good solvent resistance.
- Sunshine Replacement Form (Rule 26)
- the amount of dodecenyl succinic acid used was changed from 1 part to 3 parts, and instead of 150 parts of aluminum hydroxide, 100 parts of aluminum hydroxide and carbon dioxide as a filler were used. Except for mixing 50 parts of calcium (Whiteton P-70, manufactured by Toyo Fine Chemical Co., Ltd.), the same operations and molding as in Example 21 were carried out to prepare a molded plate.
- the gel time at 110 ° C was 80 seconds.
- the obtained molded plate had a gloss on its surface and was excellent in smoothness. Also, the molded plate was excellent in heat resistance. Further, as a result of evaluating the weather resistance and the water resistance, the molded plate showed slight discoloration and a slight decrease in gloss as compared with the molded plate of Example 21, but these physical properties were superior. Was. Table 11 summarizes the main reaction conditions and results described above. (Example 24)
- Example 21 First, the same reaction and treatment as in Example 16 were performed to prepare (meth) acrylic syrup C ′. Next, using this (meth) acrylyl syrup C ′, the amount of magnesium oxide used in Example 21 was changed from 1 part to 2 parts, and the amount of pendedodecenylsuccinic acid was changed from 1 part to 3 parts. Modified, and instead of 150 parts of aluminum hydroxide, 100 parts of aluminum hydroxide and glass powder as a filler (FMB30W-001, manufactured by Nitto Bospela Corporation) Except for mixing with 50 parts, the same operation and molding as in Example 21 were performed to prepare a molded plate. Gate-time in 1 1 0 e C was 1 2 0 sec.
- the obtained molded plate had a gloss on its surface and was excellent in smoothness. Further, the molded plate was excellent in heat resistance, weather resistance and water resistance. Table 11 summarizes the main reaction conditions and results described above. Replacement form (Rule 26) (Comparative Example 14)
- Example 13 the same reactions and treatments as in Example 13 were carried out except that the addition amount of isobutyl vinyl ether to n-dodecylmercaptan was changed from 2.0 times mol to 0.05 times mol. Was. As a result, a (meth) acrylyl syrup having an increased solid content, viscosity, and weight average molecular weight during esterification was obtained.
- Example 11 summarizes the main reaction conditions described above.
- Example 15 the same reaction and treatment as in Example 15 were performed, except that the addition amount of isobutyl vinyl ether relative to n-dodecyl mercaptan was changed from 2.0 times mol to 0.05 times mol. . As a result, a (meth) acrylyl syrup having an increased solid content, viscosity, and weight average molecular weight during esterification was obtained.
- Example 11 summarizes the main reaction conditions described above.
- Example 21 the same reaction, treatment and the like as in Example 15 were performed to prepare (meth) acrylyl syrup C ′.
- the amount of magnesium oxide used in Example 21 was reduced from 1 to 2 parts and the paper (Rule 26> Table 11
- Example 21 First, the same reaction and treatment as in Example 17 were performed to prepare (meth) acrylyl syrup C ′. Next, the amount of (meth) acrylyl syrup C 'in Example 21 was changed from 100 parts to 85 parts, and 15 parts of trimethylolpropane trimethacrylate was added. The same operation, molding, and the like as in Example 21 were performed to produce a molded plate. Gel Time in 1 1 0 e C was 7 5 seconds.
- the obtained molded plate had a gloss on its surface and was excellent in smoothness. Further, the molded plate was excellent in heat resistance, weather resistance and water resistance. Table 11 summarizes the main reaction conditions and results described above.
- the obtained artificial marble plate had a glossy surface, was excellent in smoothness, and had a so-called high-grade feel and texture. Also, the artificial marble plate was excellent in heat resistance, weather resistance and water resistance. Table 12 summarizes the above main reaction conditions and results.
- a molded plate (molded product) was prepared by subjecting the above BMC to heat and pressure molding by a predetermined method. 1 1 0.
- the gel time in C was 110 seconds.
- the obtained molded plate had a gloss on its surface and was excellent in smoothness. Further, the molded plate was excellent in heat resistance, weather resistance and water resistance.
- Table 12 summarizes the above main reaction conditions and results.
- a molding material can be suitably obtained by using the production method according to this example. That is, the molding material according to Example 19 or Example 20 did not generate odor due to the thiol compound at the time of molding, and the replacement of carbide in the molding die at the time of molding ⁇ paper (Rule 26) ) 1 part of butyl Z), aluminum hydroxide (manufactured by Showa Denko KK, Hygilite H-31) 200 parts, and Zelek as a molding agent UN (trade name, DuPont, USA) A 7-part pultruded material was obtained.
- the obtained pultruded material was formed together with 75 glass rovings using a mold having a total length of 800 mm and a hole size of 113 mm ⁇ 3.1 mm.
- the mold temperature was 90 ° C and the drawing speed was 0.8 m / min. As a result, a molded plate (molded product) was obtained.
- the obtained molded plate had a gloss on its surface and was excellent in smoothness. Further, the molded plate was excellent in heat resistance, weather resistance and water resistance. Table 12 summarizes the main reaction conditions and results described above.
- glass fiber (a 1/4 inch long tiobdos strand) was added to the compound and kneaded with a double-arm kneader.
- BMC as a molding material was obtained.
- the ratio of the glass fibers in the BMC was adjusted to be 5%.
- the obtained BMC was placed in a metal container and aged at 40 ° C for 1 day. After aging, the compound, ie, BMC, was not hardened, and the surface of BMC was not sticky.
- the BMC was heated and pressed. That is, using a mold of a predetermined size, the temperature of the upper mold was set to 120, and the temperature of the lower mold was set to 110'C. Then, the BMC cut into a predetermined size is filled in the above-mentioned mold, clamped at a pressure of 6 MPa, and heated and pressed for 7 minutes to obtain a molded product having a thickness of 3 mm. mm plate was made. The gel time at 120'C was 70 seconds.
- the resulting molded article had a good gloss (60 ° gloss) of 85 and a low degree of yellowness (Y I) of 2.31.
- the molded product was excellent in surface smoothness with no net-like embossed appearance due to glass fibers on the surface.
- a separable flask equipped with a thermometer, a cooler, a nitrogen gas inlet tube, and a stirrer, 130 parts of methyl methacrylate and 40 parts of N-cyclohexyl maleimide as a vinyl compound were added. And 30 parts of styrene, and then the inside of the reactor was purged with nitrogen gas. Next, the temperature of the mixture was raised to 85 with stirring, and then 0.006 parts of AIBN and 0.3 part of n-dodecylmercaptan were added to initiate a polymerization reaction.
- isobutylbutyl ether was added to the above reaction mixture, the temperature was raised to 100 ° C., and the mixture was stirred for 30 minutes to treat n-dodecyl mercaptan remaining in the reaction mixture. .
- the above-mentioned isobutyl vinyl ether was added in a molar amount of 2.0 times the amount of n-dodecyl mercaptan added during the polymerization.
- (meth) acrylyl syrup C was obtained.
- the (meth) ataryl syrup C had a solids concentration of 29%, a viscosity of 8.5 boise, and a weight average molecular weight of 103,000. Satoshi Substitution (Rule 26) That is, the BMC was not cured, and the surface of the BMC was not tacky.
- the BMC was heated and pressed. That is, a mold having a predetermined size was used, and the temperature of the upper mold was set to 120 ° C., and the temperature of the lower mold was set to 110 °. Then, the BMC cut into a predetermined size is filled in the above mold, clamped at a pressure of 6 MPa, and heated and pressed for 7 minutes to obtain a molded product having a thickness of 3 mm. mm plate was made. The gel time at 120 ° C. was 60 seconds.
- the resulting molded article had a good gloss (60 ° gloss) of 85 and a low degree of yellowness (Y I) of 2.10.
- the molded product had excellent surface smoothness with no mesh-like embossment due to glass fibers on the surface.
- Example 29 The same operation as in Example 29 was carried out except that 118 parts of methyl methacrylate and 12 parts of methacrylic acid were used instead of 130 parts of methyl methacrylate in Example 29. The polymerization reaction was started.
- the (meth) acrylic syrup C had a solid concentration of 28%, a viscosity of 9.5 voids and a weight average molecular weight of 107,000.
- glass fiber chopped strand having a length of 1 Z4 inches
- BMC as a molding material
- the ratio of the glass fibers in the BMC was adjusted to be 5%.
- the obtained BMC was placed in a metal container and aged at 40 ° C. for 1 day. Compound after aging. ⁇ . T3 ⁇ 4i 'j26) was added to initiate the polymerization reaction.
- the (meth) acrylic syrup C had a solid content of 29%, a viscosity of 7.5 voise and a weight average molecular weight of 1,500,000.
- Example 13 the number of double bonds per molecule of (meth) acrylic polymer (polymer) in (meth) acrylic syrup C ′ was measured. As a result, the number of double bonds per molecule was 13. Then, the same kneading and aging operation as in Example 30 was carried out except that the (meth) acrylic syrup C 'was used instead of the (meth) acrylic syrup C in Example 30 to obtain BMC. Was. Further, the same molding operation as in Example 30 was performed to produce a molded product, a plate having a thickness of 3 mm. The gel time at 120'C was 55 seconds.
- the obtained molded article had a good gloss (60 ° gloss) of 85 and a low degree of yellowness (Y I) of 2.43.
- the molded product was excellent in surface smoothness with no net-like embossed appearance due to glass fibers on the surface.
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to tin octylate, to obtain (meth) acrylyl syrup E.
- the (meth) acrylic syrup E was colorless and transparent, had a solid content of 52%, a viscosity of 35 boise, and a weight average molecular weight of 16,000.
- the same operation as in Example 33 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same operation as in Example 33 was performed to obtain a molded plate. Deflection temperature under load of the resulting molded plate was 1 1 8 e C.
- Table 13 shows the main reaction conditions described above. Table 15 shows the obtained results.
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to zirconium octylate, to obtain (meth) acrylyl slab E.
- the (meth) acrylic slab E was colorless and transparent, had a solid content of 52%, a viscosity of 35 boise, and a weight average molecular weight of 16,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- Example 33 the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 118′C.
- Table 13 shows the main reaction conditions described above.
- Table 15 shows the obtained results.
- Example 36 Replacement paper (Rule 26) Then, 1 part of AIBN and 4 parts of n-dodecylmerbutane as a chain transfer agent were added, and a copolymerization reaction was carried out for 4 hours to obtain a reaction mixture (untreated acrylic syrup).
- the casting material is cast using a cell that is closed with a so-called elastic gasket around two glass plates that are placed opposite each other so that the distance (gap) between them is 7 mm. did. That is, after the casting material was poured into the above-mentioned cell, it was heated to 60 ° C. to be cured.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 120 °.
- Table 14 shows the main reaction conditions described above.
- Table 15 shows the obtained results.
- Example 3 Except for changing the Okuchiru zinc in Example 3 3 in-phosphate hydrogen zinc (Z n HP 0 4), and in the same manner as in Example 3 3, to obtain a (meth) acrylic syrup E.
- the (meth) acrylic slab E was colorless and transparent, had a solid content of 51%, a viscosity of 36 boys, and a weight average molecular weight of 17,000.
- Example 33 Then, the same operation as in Example 33 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- Example 33 the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 120.
- Table 14 shows the main reaction conditions described above.
- Table 15 shows the obtained results.
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to zinc acetylacetonate (Zn (acac) 2 ), to obtain (meth) acrylic syrup E.
- the (meth) acrylic syrup E was colorless and transparent, had a solid content of 52%, a viscosity of 45 boise, and a weight average molecular weight of 2 to 0.00.
- Example 33 was performed to obtain a casting material.
- Replacement paper obtained (Rule 26) The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to zinc stearate, to obtain (meth) acrylyl syrup E.
- the (meth) acrylic syrup E was colorless and transparent, had a solid content of 52%, a viscosity of 36 boise, and a weight average molecular weight of 17,000.
- the same operation as in Example 33 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 120.
- Table 13 shows the main reaction conditions described above. Table 15 shows the obtained results.
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to zinc benzoate, to obtain (meth) acrylylsilab E.
- the (meth) acryl syrup E was colorless and transparent, had a solid content of 52%, a viscosity of 37 boys, and a weight average molecular weight of 17,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 120 ° C.
- Table 13 shows the main reaction conditions described above.
- Table 15 shows the obtained results.
- Example 3 Except for changing the Okuchiru zinc in Example 3 3 in zinc chloride (Z n C 1 2), and in the same manner as in Example 3 3, to obtain a (meth) acrylic Rirushira' Bed E.
- the (meth) acrylic syrup E is colorless and transparent, has a solid content of 5196, a viscosity of 37 boise, and a weight average molecular weight of 18,000. Table 13
- (Meth) acrylyl syrup E was obtained by performing the same reaction as in Example 33 except that n-dodecylmercaptan in Example 33 was changed to 3-mercaptopropionic acid (thiol compound).
- the (meth) acrylic wrap E was colorless and transparent, had a solid content of 51%, a viscosity of 37 boys, and a weight average molecular weight of 18,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material.
- the obtained casting material was excellent in storage stability.
- the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 125 ° C.
- Table 14 shows the main reaction conditions described above.
- Table 15 shows the obtained results.
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to cobalt octylate, to obtain (meth) acrylyl syrup.
- the (meth) acryl syrup was dark blue, had a solids concentration of 54%, a degree of variance of 40 boises, and a weight average molecular weight of 19,000.
- Example 33 A reaction was carried out in the same manner as in Example 33 except that zinc octylate in Example 33 was changed to triethylbenzylammonium chloride to obtain (acrylic syrup).
- the (meth) acrylic slab was light brown, had a solid content of 53%, a viscosity of 36 boys, and a weight average molecular weight of 16,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material for comparison.
- the comparative casting material obtained was poor in storage stability.
- Example 33 the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 110.
- Table 16 shows the main reaction conditions described above.
- Table 18 shows the obtained results.
- Example 33 The same reaction as in Example 33 was carried out except that glycidylmethacrylate was not added in Example 33, to obtain (meth) acrylyl syrup.
- the (meth) acrylic syrup was colorless and transparent, had a solid content of 50%, a viscosity of 30 boys, and a weight average molecular weight of 14,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material for comparison.
- the comparative casting material obtained was poor in storage stability.
- the same operation as in Example 33 was performed to obtain a molded plate. Load deflection temperature of the obtained molded plate, 9 0 e C and lower, were inferior in hot strength.
- Table 16 shows the main reaction conditions described above.
- Table 18 shows the obtained results.
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate was not added in Example 33, to obtain (meth) acrylyl syrup.
- the (meta) replacement sheet (Rule 26) The comparative casting material obtained was poor in storage stability. Then, the embodiment
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to iron octylate, to obtain (meth) acrylyl syrup.
- the (meth) acryl syrup was dark brown, had a solid content of 51%, a viscosity of 35 boise, and a weight average molecular weight of 15,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material for comparison.
- the comparative casting material obtained was poor in storage stability.
- Example 33 the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 105.
- Table 16 shows the main reaction conditions described above.
- Table 18 shows the obtained results.
- Example 33 The same reaction as in Example 33 was carried out except that zinc octylate in Example 33 was changed to triethylamine, to obtain (meth) acrylyl syrup.
- the (meth) acrylic syrup was brownish in color, had a solid content of 52%, a degree of trimming of 36 boys, and a weight average molecular weight of 17,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material for comparison.
- the comparative casting material obtained was poor in storage stability.
- Example 33 the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained molded plate was 120.
- Table 16 shows the main reaction conditions described above.
- Table 18 shows the obtained results.
- the acrylic syrup was colorless and transparent, had a solids concentration of 46%, a viscosity of 27 vise, and a weight average molecular weight of 14,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material for comparison.
- the comparative casting material obtained was poor in storage stability.
- the same operation as in Example 33 was performed to obtain a molded plate. Load deflection temperature of the obtained molded plate, 9 0 e C and lower, were inferior in hot strength.
- Table 17 shows the main reaction conditions described above.
- Table 18 shows the obtained results.
- Example 33 In place of 93 parts of methyl methacrylate and 7 parts of methacrylic acid in Example 33, 100 parts of methyl methacrylate was used, and the addition amount of n-dodecyl mercaptan was 4 to 3 parts.
- the reaction was carried out in the same manner as in Example 33 except for changing to, to obtain (meth) acrylyl syrup.
- the (meth) acrylic syrup was colorless and transparent, had a solid content of 4696, a viscosity of 27 boise, and a weight average molecular weight of 14,000.
- Example 33 the same operation as in Example 33 was performed to obtain a casting material for comparison.
- the obtained comparative casting material was excellent in storage stability.
- Example 33 the same operation as in Example 33 was performed to obtain a molded plate.
- the deflection temperature under load of the obtained formed plate was as low as 90 ° C., and was inferior in the strength at the time of heating.
- Table 17 shows the main reaction conditions described above.
- Table 18 shows the obtained results.
- the molding materials according to Examples 33 to 41 have little coloring and excellent storage stability.
- the molded product (cured product) obtained by molding the above molding material has excellent strength when heated.
- the BMC was heated and pressure-formed. That is, using a mold of a predetermined size, the temperature of the upper mold was set to 120, and the temperature of the lower mold was set to 110 ° C. Then, the BMC cut into a predetermined size is filled in the above-mentioned mold, the mold is clamped at a pressure of 6 MPa, and heated and pressed for 7 minutes to obtain a molded product having a thickness of 3 mm. mm ⁇ was created. The gel time at 120 ° C. was 55 seconds.
- the resulting molded article had a good gloss (60 ° gloss) of 87 and a low degree of yellowness (Y I) of 2.0.
- the molded product was excellent in surface smoothness with no net-like embossed appearance due to glass fibers on the surface. .
- glass fiber (a 1-inch to 4-inch length of a chopped strand) was added to the compound and kneaded with a double-arm kneader.
- BMC as a molding material was obtained.
- Percentage of the glass fiber in the BMC Casting was performed using a chained cell. That is, after the casting material was poured into the above-described cell, it was cured by heating at 60 ° C.
- the deflection temperature under load (HDT; thermal deformation temperature) of the obtained molded plate was measured by a method according to JIS 6911, and was found to be 118 ° C.
- the polymer was removed by removing water from the suspension (reaction mixture) after polymerization. Then, 30 parts of the polymer was dissolved in 70 parts of methyl methacrylate.
- the casting material is closed with a so-called elastic gasket around two glass plates facing each other so that the gap (gap) between them is 7 mm.
- the molded product was excellent in surface smoothness, with no net-like embossing of glass fibers on the surface.
- Example 44 First, the same reaction and treatment as in Example 44 were performed to obtain (meth) acrylic syrup A. Next, using this (meth) acryl syrup A, instead of the aluminum hydroxide 150 parts in Example 44, the aluminum hydroxide 100 parts and glass powder (manufactured by Nitto Boseki Co., Ltd.) SMB was obtained in the same manner as in Example 44, except that a mixture with 50 parts of FMB 30 W-001) was used. Further, the same aging and molding operations as in Example 44 were performed to prepare a molded product having a thickness of 3 mm. 1 2 0. The gel time at C was 90 seconds.
- the resulting molded article had a good gloss (60 ° gloss) of 83 and a low yellowness (Y I) of 3.92.
- the molded product was excellent in surface smoothness with no net-like embossed appearance due to glass fibers on the surface.
- the above SMC was heated and pressed. That is, using a mold of a predetermined size, the temperature of the upper mold was set to 120, and the temperature of the lower mold was set to 110 ° C. Then, the SMC cut into a predetermined size is filled in the above mold, clamped at a pressure of 6 MPa, and heated and pressed for 7 minutes to obtain a molded product having a thickness of 3 mm. mm ⁇ was created. Gel evening I ⁇ in 1 2 0 e C was found to be 9 0 seconds.
- the obtained molded article had a good gloss (60 ° gloss) of 80 as measured based on JISK7105, and the yellowness (YI) measured based on JISK7103. Of 4.08 and low coloring property. Further, No mesh-like embossing of glass fiber was observed on the surface, and the surface was excellent in surface smoothness.
- Example 44 the same reaction and treatment as in Example 44 were performed to obtain (meth) acrylyl slab A.
- the same operation as in Example 46 was performed using the obtained compound to obtain BMC. Further, the same molding operation as in Example 44 was performed to produce a molded product, a plate having a thickness of 3 mm.
- the gel time at 120 ° C. was 50 seconds.
- the resulting molded article had a good gloss (60 ° gloss) of 85 and a low degree of yellowness (YI) of 2.12.
- the molded product was excellent in surface smoothness with no net-like embossed appearance due to glass fibers on the surface.
- Shuffle paper (Rule 26) No substantial discoloration or chalking was observed.
- the molded article was left in an oven set at 150 ° C for 1 hour to evaluate the heat resistance. As a result, the molded article did not show any change in appearance such as yellowing, The surface gloss was not lost.
- the above SMC did not cure even when stored at 40 days for 2 months. That is, the SMC was excellent in storage stability. Table 19 summarizes the main results described above.
- glass fiber (a 1-inch to 4-inch length of a chopped strand) was added to the compound and kneaded with a double-arm kneader.
- BMC as a molding material was obtained.
- the ratio of the glass fibers in the BMC was adjusted to be 5%.
- the obtained BMC was placed in a metal container and aged at 40 ° C. for 1 day. After aging, the compound, ie, BMC, was not hardened, and the surface of BMC was not sticky.
- the same molding operation as in Example 44 was performed to prepare a molded product, 3 mm thick.
- the gel time at 120 ° C. was 60 seconds.
- the resulting molded article had a good gloss (60 ° gloss) of 85 and a low degree of yellowness (YI) of 2.02.
- articles must be listed on table ⁇ paper (Rule 26)
- a result of an accelerated weathering test for 1,000 hours no substantial discoloration or choking was observed in the molded product.
- molded products
- Example 44 The same reaction as in Example 44 was carried out except that N-phenylmaleimide (vinyl compound) was used instead of N-cyclohexylmaleimide in Example 44, to give (meth) acrylyl syrup A I got The viscosity of the resulting (meth) acrylic Rirushirabbu A is 6 Boise (2 5 e C), 2 2. 8% solids concentration, a weight average molecular Tung was 9 6 0 0 0.
- Example 44 the same operation as in Example 44 was performed using this (meth) acrylic syrup A to obtain SMC.
- the maturation and molding operations were performed in the same manner as in Example 44 to produce a 3 mm thick plate as a molded product.
- the gel time at 120 was 98 seconds.
- the obtained molded article had a yellowness (YI) of 21.3 and a strong yellowish tint, but had a good gloss (60 gloss) of 79.
- the molded product was excellent in surface smoothness, with no net-like embossing of glass fiber on the surface.
- Example 44 The same reaction and treatment as in Example 44 except that methacrylic acid was not used and that the amount of methyl methacrylate used (prepared amount) was changed from 55 parts to 58 parts. (Meth) acrylic syrup was obtained (the viscosity of the obtained (meth) acrylic syrup was 7 Boys (25 ° C).
- the solid content was 22.7% and the weight average molecular weight was 9 Next, 100 parts of this (meth) acrylyl syrup, 1 part of t-butyl baroxy 2-ethylhexanoate, 4 parts of zinc stearate, and aluminum hydroxide ( The compound was obtained by mixing 400 parts of Hygilite HS-320 (manufactured by Showa Denko K.K.) The same operation as in Example 46 was carried out using the obtained compound, In addition, the same molding operation as in Example 4 was performed. Gel time in creating the ⁇ of 3 mm thick is elegance. 1 2 0 e C was 7 0 seconds.
- the resulting molded article had a good gloss (60 ° gloss) of 85 and a low yellowness (YI) of 2.12.
- the molded product was excellent in surface smoothness with no net-like embossed appearance due to glass fibers on the surface. 26 Except for the above, the same reaction and treatment as in Example 44 were performed to obtain a (meth) acrylic syrup.
- the viscosity of the obtained (meth) acrylyl syrup was 7 voices (25 C), the solid content was 23.9%, and the weight average molecular weight was 98,000.
- Example 44 using this (meth) acryl syrup, the same operation as in Example 44 was performed to obtain SMC for comparison. Further, the same aging and molding operations as in Example 44 were performed, and a 3 mm-thick plate as a comparative molded product was produced. The gel time at 120 was 130 seconds.
- the obtained comparative molded article had a gloss (60 ° gloss) of 18 which was poor. Further, in the comparative molded product, a network-like embossment due to glass fibers was observed on the surface, and the surface smoothness was poor.
- the comparative molded article was placed in an oven set at 150 ° C. for 1 hour and evaluated for heat resistance. As a result, the molded article showed changes in appearance such as yellowing, In addition, the gloss of the surface was lost, and unevenness occurred. Table 19 summarizes the above main results.
- Example 44 The same reaction as in Example 44 was carried out except that N-isopropylmaleimide (vinyl compound) was used instead of N-cyclohexylmaleimide in Example 44, to give (meth) acrylyl syrup A I got The resulting (meth) acrylic syrup A had a viscosity of 7 boys (25 V), a solid content of 23.8%, and a weight average molecular weight of 110,000.
- Example 44 the same operation as in Example 44 was performed using this (meth) acrylyl syrup A to obtain an SMC.
- the same aging and molding operations as in Example 44 were performed to produce a 3 mm thick plate as a molded product. 1 2 0 e C to your Keru gel time Atsuta 1 0 0 seconds.
- the obtained molded article had a good gloss (60 ° gloss) of 80 and a low degree of yellowness (Y I) of 5.31. Further, the molded product was excellent in surface smoothness, with no net-like embossing of glass fiber on the surface.
- Example 4 N-six-hexylmaleimide was not used, and the amount of methyl methacrylate used (prepared amount) was changed from 55 parts to 77 parts. You can see that.
- a reactor equipped with a thermometer, a cooler, a nitrogen gas inlet tube, and a stirrer was charged with 98 parts of methyl methacrylate and 2 parts of methacrylic acid, and then reactor ⁇ was replaced with nitrogen gas. .
- 80 was stirred while the above mixture was stirred. After the temperature was raised to C, 0.01 part of AIBN and 0.3 part of n-dodecylmercaptan were added to initiate a polymerization reaction.
- reaction solution had a viscosity of 100 to 110 voids (25). After cooling, the mixture was cooled. Hydroquinone was added at 50 ppm based on the weight of the reaction solution.
- the molding materials according to Examples 44 to 50 are suitable for pressure molding and can be cured in a relatively short time.
- molded products obtained by pressing molding materials are excellent in various physical properties such as heat resistance, gloss, surface smoothness, and storage stability.
- a lump-shaped molding material was obtained.
- the obtained molding material was placed in a closed container and aged at 40 ° C for 1 day. After aging, the molding material had no stickiness on the surface and was easy to handle.
- Example 51 the above molding material was compression molded in the same manner as in Example 51 to obtain a box-shaped molded product.
- the obtained box-shaped molded product had a linear shrinkage of 0.27%, was smoothly released, had no cracks, cracks, warpage, or deformation, and had good moldability.
- the gloss of the obtained box-shaped molded product was measured in the same manner as in Example 51, the gloss (60 ° gloss) of the flat portion of the box was 79, and the gloss (60 ° gloss) of the side surface of the box was not. 7 3 was good. Furthermore, no irregularities were observed on the surface of the box-shaped molded product, and the box-shaped molded product was excellent in surface smoothness.
- the strength of the obtained box-shaped molded product was measured based on JIS K6911. As a result, the flexural strength was 70 MPa and the flexural modulus was 11.9 GPa. .
- a reactor equipped with a thermometer, a cooler, a nitrogen gas inlet tube, and a stirrer was charged with 98 parts of methyl methacrylate and 2 parts of methyl acrylate, and the inside of the reactor was purged with nitrogen gas. .
- the temperature of the mixture was raised to 80 ° C. while stirring, and then 0.02 parts of AIBN and 0.2 parts of n-dodecylmercaptan were added to initiate a polymerization reaction.
- the above molding material was compression molded. That is, using a box-molding die is Dimensions width 3 8 cm X Depth 2 8 cm X height 9 cm, the upper mold temperature of 1 2 5 e C, the temperature of the mold of the lower was set to 1 1 0'C. Then, 200 g of the above molding material was filled into the above mold, clamped at a pressure of 6 MPa, and compression molded for 7 minutes to create a box-shaped molded product with a thickness of 7 mm. did.
- the obtained molded product had a linear shrinkage of 0.25%, could be smoothly released from the mold, had no cracks, cracks, warpage, or deformation, and had good moldability.
- the molded product had a good gloss (60 ° gloss) at the bottom of the box of 80 and a gloss (60 ° gloss) of 75 at the side of the box. Further, the molded article had no unevenness on the surface and was excellent in surface smoothness.
- the bending strength was 88 MPa and the flexural modulus was 12.5 GPa.
- Example 51 Instead of using 0.1 part of AI BN and 0.3 part of n-dodecyl mercaptan in Example 51, 0.02 part of AI BN and 0.2 part of ⁇ -dodecyl mer force butane were used instead of 0.2 part.
- (meth) acrylyl syrup ⁇ ⁇ ⁇ according to the present invention was obtained.
- the solids concentration in the (meth) acrylic syrup A was 41.5%, and its weight average molecular weight was 108,000. GP a.
- Example 51 the same reaction and treatment as in Example 51 were performed to obtain a compound.
- the compound was mixed with 15 parts of glass fiber (chopped strand having a length of 6 mm) and commercially available methyl polymethacrylate (weight average molecular weight 90,000) as a low-shrinking agent. And kneaded for 30 minutes with a double-armed cutter. As a result, a massive molding material was obtained. The ratio of the glass fibers in the molding material was adjusted to 9%. Thereafter, the same aging and compression molding as in Example 51 were performed to produce a box-shaped molded product.
- the obtained molded product had a linear shrinkage of 0.17%, could be smoothly released from the mold, had no cracks, cracks, warpage, or deformation, and had good moldability.
- the molded product had a favorable gloss (60 ° gloss) at the bottom of the box of 84 and a gloss (60 ° gloss) of 83 at the side of the box. Further, the molded article had no unevenness on the surface and was excellent in surface smoothness.
- the flexural strength was 83 MPa and the flexural modulus was 12.5 GPa.
- Example 54 was repeated except that methyl poly (methacrylate) in Example 54 was replaced by 15 parts of a commercially available polystyrene (weight average molecular weight: 180,000) as a low-shrinking agent. The same reaction and operation were performed to obtain a molding material. Thereafter, aging and compression molding were performed in the same manner as in Example 51 to produce a box-shaped molded product.
- methyl poly (methacrylate) in Example 54 was replaced by 15 parts of a commercially available polystyrene (weight average molecular weight: 180,000) as a low-shrinking agent.
- the same reaction and operation were performed to obtain a molding material.
- aging and compression molding were performed in the same manner as in Example 51 to produce a box-shaped molded product.
- the obtained molded product has a linear shrinkage of 0.18%, can be smoothly released from the mold, has no cracks, cracks, warpage, or deformation, and has good moldability.
- Example 51 the same operation as in Example 51 was performed using the obtained reaction mixture to obtain a compound.
- glass fiber chopped strand having a length of 6 mm
- the mixture was kneaded for 30 minutes with a double-armed cutter.
- the ratio of the glass fiber in the comparative molding material was adjusted to be 20%.
- the same aging and compression molding as in Example 51 were performed to produce a box-shaped molded product for comparison.
- the obtained molded article for comparison had poor gloss (60 ° gloss) of 65 at the bottom of the box and 63 of gloss at the side of the box (60 ° gloss). Further, the molded article is uneven across the surface is observed as a result of the intensity of c molded article was inferior in surface smoothness was measured, 0 flexural strength 1 l MP a, flexural modulus 1 4. 5 GPa.
- Example 51 The same reaction as in Example 51 except that, in Example 51, glass fiber having a length of 3 mm was added instead of glass fiber having a length of 6 mm so that the ratio in the molding material was 9%. ⁇ By performing operations, etc., a molding material was obtained. Thereafter, aging and compression molding were performed in the same manner as in Example 51 to produce a box-shaped molded product.
- the obtained molded product had a linear shrinkage of 0.27%, could be smoothly released from the mold, had no cracks, cracks, warpage, or deformation, and had good moldability.
- the molded product had a favorable gloss (60 ° gloss) at the bottom of the box of 83 and a gloss (60 ° gloss) at the side of the box of 78. Further, the molded article had no unevenness on the surface and was excellent in surface smoothness.
- the bending strength was 89 MPa and the bending elastic modulus was 12.9.
- Nyl ether was added in a molar amount of 2.0 times the amount of n-dodecyl mercaptan added during the polymerization.
- the resulting dispersion (molding material) was opaque.
- the particle size distribution of the dispersed phase was measured using a particle size measuring device (NICOMP370, manufactured by Pacific Scientific Co., Ltd.) and found to be 50 nm to 100 ⁇ m.
- the molding material of the present embodiment has a low linear shrinkage and c it can be seen that the moldability is good, forming the molding composition It can be seen that the molded article obtained by this method is excellent in gloss and surface smoothness. Further, it can be seen that the molding material according to the present example has a sufficient strength for practical use although the strength is slightly lower than the molding material according to the comparative example.
- Example 13 the number of double bonds per molecule of the (meth) acrylic polymer (polymer) in the (meth) acrylic syrup E was measured. As a result, the number of double bonds per molecule was 12.
- a dispersion liquid was obtained by performing the same operation as in Example 56 using this (meth) acrylsilap E. The resulting dispersion was opaque, and the particle size distribution of the dispersed phase was measured to be 50 nm to 100 zm. I got Thereafter, the obtained compound was aged at 40 ° C for 1 day, and the thickened compound was poured into a 11.3 mm diameter cylinder heated to 120 ° C. Then, the tip of the cylinder was covered with a lid so that the compound did not leak. Thereafter, the piston was inserted with the tip of the cylinder facing downward, and the compound was cured while applying a pressure of 20 kgf Z cm 2 to the inside of the cylinder with the piston.
- the obtained cured product had a volume shrinkage of 3.0%.
- the cured product was excellent in surface smoothness with no pinholes or uneven gloss.
- the cured product was cut into two, and its cross section was observed using a scanning electron microscope. Many voids of about 30 micron were observed in the center of the cured product.
- the above compound before thickening was applied to the surface of the polyethylene film so as to have a constant thickness, and on this applied material, glass fiber (chopping 1 inch long) as a reinforcing material was applied. The compound was applied evenly. ⁇ Then, the applied material obtained by applying the compound to the surface of the polyethylene film so as to have a constant thickness was overlapped. In other words, the glass fiber was sandwiched between the components. As a result, SMC was obtained as a molding material. The ratio of the above glass fibers in the SMC was adjusted to be 25%. Thereafter, the obtained SMC was packed in cellophane film and aged at 40 ° C for 1 day.
- isoptyl vinyl ether was added to the obtained reaction mixture, the temperature was raised to 100, and the mixture was stirred for 30 minutes to treat the n-dodecyl mercapone added to the reaction mixture. .
- the above-mentioned isobutyl vinyl ether was added so as to be 2.0 times the mol of n-dodecyl mercaptan added during the polymerization.
- by adding 5 parts of methyl acrylate to 95 parts of the reaction mixture after the above treatment (meth) acryl syrup D according to the present invention was obtained.
- the obtained casting material was cast-formed using a glass cell. That is, after injecting the casting material into the above cell, cure it at 60 for 1 hour and replace with ffl paper (Rule 26) Was.
- a compound was obtained by performing the same operation as in Example 56 using the above dispersion liquid. Thereafter, the obtained compound was aged at 40 ° C for 1 day.
- the compound after thickening was cured in the same manner as in Example 56.
- the obtained cured product had a volume shrinkage of 3.0%.
- the cured product was excellent in surface smoothness with no pinholes or unevenness in gloss on the surface.
- a large number of voids of about 30 microns were found in the center of the cured product.
- the above compound before thickening is applied to the polyethylene film surface so as to have a constant thickness, and a glass fiber (a 1-inch chopped roving) as a reinforcing material is uniformly applied on the applied material.
- the compound was applied on the surface of the polyethylene film so as to have a constant thickness. In other words, the glass fiber was sandwiched between the components.
- SMC was obtained as a molding material. The ratio of the glass fibers in the SMC was adjusted to be 25%. Thereafter, the obtained SMC was packed in cellophane film and aged at ⁇ 40 for 1 day.
- the above SMC was heated and pressed. That is, a mold having a size of 300 mm ⁇ 300 mm was used, the temperature of the upper mold was set to 110, and the temperature of the lower mold was set to 100 ° C. Then, the SMC cut into a size of 150 mm xi 50 mm was filled in the above mold, clamped at a pressure of 6 MPa, and heated and pressed for 10 minutes to form a mold. A 3 mm-thick molded plate was formed as a molded product. The resulting molded plate, on both the front and back sides, is pin-hoed paper Rule 26 The compound had excellent storage stability.
- the obtained marble plate had a gloss on its surface, was excellent in smoothness, and had a so-called high-grade feel and texture. Also, artificial Dali stone is insoluble in THF and acetone, and c solvent resistance was good, artificial marble plate, heat resistance, ⁇ resistance, and water resistance in the main have a c above excellent.
- Table 20 The various reaction conditions and results are summarized in Table 20.
- isoptyl vinyl ether was added to the obtained reaction mixture, the temperature was raised to 100 ° C., and the mixture was stirred for 30 minutes to treat the n-dodecyl mercaptan added to the reaction mixture. did.
- the above isobutyl vinyl ether was added so as to be 2.0 times the mol of n-dodecyl mercaptan added during the polymerization to obtain (meth) acrylyl syrup C.
- the resulting marble plate has a glossy surface and is excellent in smoothness Was. Then, after demolding, an artificial marble plate as a molded product was obtained by post-curing at 100 ° C. for 2 hours.
- the obtained marble plate had a gloss on its surface, was excellent in smoothness, and had a so-called high-grade feel and texture. Also, artificial Dali stone is insoluble in THF and acetone, ⁇ agent resistance was good £ Further, artificial marble plate, heat resistance, weather resistance, and c above main which was excellent in water resistance The reaction conditions and results are summarized in Table 20.
- isoptyl vinyl ether was added to the obtained reaction mixture, the temperature was raised to 100, and the mixture was stirred for 30 minutes to treat the n-dodecyl mercaptan added to the reaction mixture. did.
- the above-mentioned isobutyl vinyl ether was added so as to be 2.0 times the mol of n-dodecyl mercaptan added at the time of polymerization to obtain the (meth) acrylyl scrub D according to the present invention.
- the above-mentioned isobutyl vinyl ether was added so as to be 2.0 times the mol of n-dodecyl mercaptan added at the time of polymerization to obtain the (meth) acrylyl scrub D according to the present invention.
- Example 10 Next, the same operation, molding, and the like as in Example 10 were carried out using the (meth) acrylic syrup D to prepare an artificial marble plate.
- the casting material ie, the replacement paper (Rule 26)
- the present invention can be implemented with various modifications within the spirit of the present invention and the scope of the claims described below.
- Examples of molded articles obtained by molding the molding material according to the present invention include various articles used outdoors such as so-called daylighting domes, benches, tables, tanks, public notice boards, waterproof boards, etc .; Constituent materials that make up railway vehicles, ships, etc .; Exterior materials for structures such as roofs and walls; Artificial marble suitable for bathtubs, kitchen loungers (kitchen tops), various counter tops, vanities, etc .; Electrical parts; and the like, but are not particularly limited.
- the molded article is excellent in aesthetic appearance and is suitable for various uses requiring the aesthetic appearance.
- a molded article obtained by molding a molding material containing a filler has a beautiful marble-like pattern, and is therefore most suitable as an artificial marble.
- the (meth) acrylic syrup C and (meth) acrylic syrup D which are excellent in storage stability when used as a molding material, can be stably produced by the method according to Examples 58 to 60. , And can be manufactured easily. Further, the molding material according to Examples 58 to 60 is suitable for heat and pressure molding, and the obtained molded article is excellent in various physical properties such as heat resistance, solvent resistance, and weather resistance. I understand.
- the (meth) acrylate according to claim 8 wherein the reaction mixture is obtained by partially polymerizing a monomer component containing a (meth) acrylic ester and a vinyl monomer containing a carboxyl group. Manufacturing method of Ril syrup.
- reaction mixture After polymerizing a monomer component containing a (meth) acrylic acid ester in the presence of a thiol compound, the reaction mixture is treated with maleic anhydride and a basic compound, and the reaction mixture is treated.
- a method for producing (meth) acrylic syrup in which a vinyl monomer having a carboxyl group is added to the mixture.
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Macromonomer-Based Addition Polymer (AREA)
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/849,612 US6191229B1 (en) | 1995-10-06 | 1996-10-02 | (Meth)acryl syrup, method of manufacturing the same, and method of manufacturing molding material including the same |
EP96932796A EP0796873A4 (en) | 1995-10-06 | 1996-10-02 | (METH) ACRYLIC SYRUP, METHOD FOR THE PRODUCTION THEREOF AND METHOD FOR THE PRODUCTION OF A SAME-CONTAINING MOLDING MATERIAL |
KR1019970703762A KR100232546B1 (ko) | 1995-10-06 | 1996-10-02 | (메타)아크릴시럽 및 그 제조방법, (메타)아크릴시럽을 함유하는 성형재료의 제조방법 |
Applications Claiming Priority (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7/260530 | 1995-10-06 | ||
JP7260530A JP3004571B2 (ja) | 1995-10-06 | 1995-10-06 | (メタ)アクリルシラップおよびその製造方法並びに(メタ)アクリルシラップを含む成形材料 |
JP8/65001 | 1996-03-21 | ||
JP06500196A JP3910230B2 (ja) | 1996-03-21 | 1996-03-21 | 樹脂組成物の処理方法および樹脂材料 |
JP10160396A JPH09286889A (ja) | 1996-04-23 | 1996-04-23 | 成形材料 |
JP8/101603 | 1996-04-23 | ||
JP18970496A JP3953551B2 (ja) | 1996-07-18 | 1996-07-18 | (メタ)アクリル系樹脂組成物およびその製造方法 |
JP8/189704 | 1996-07-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1997012918A1 true WO1997012918A1 (fr) | 1997-04-10 |
Family
ID=27464524
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1996/002860 WO1997012918A1 (fr) | 1995-10-06 | 1996-10-02 | Sirop (meth)acrylique, procede d'elaboration de ce sirop et procede d'elaboration d'un materiau de moulage contenant un tel sirop |
Country Status (5)
Country | Link |
---|---|
US (1) | US6191229B1 (ja) |
EP (1) | EP0796873A4 (ja) |
KR (1) | KR100232546B1 (ja) |
CN (1) | CN1152058C (ja) |
WO (1) | WO1997012918A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009110503A1 (ja) * | 2008-03-05 | 2009-09-11 | 株式会社日本触媒 | 重合体、硬化性樹脂組成物、硬化物、及び物品 |
Families Citing this family (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6433098B1 (en) * | 1994-06-13 | 2002-08-13 | Rohm And Haas Company | Process of preparing curable compositions and compositions therefrom |
TWI266787B (en) * | 1999-11-19 | 2006-11-21 | Mitsubishi Rayon Co | Resin compositions |
US6794486B2 (en) * | 2002-02-19 | 2004-09-21 | Rhodia Chimie | Process for removing a dithiocarbonyl group at the end of a polymer chain |
US6767980B2 (en) * | 2002-04-19 | 2004-07-27 | Nippon Shokubai Co., Ltd. | Reactive diluent and curable resin composition |
US20050127561A1 (en) * | 2003-12-16 | 2005-06-16 | Scimed Life Systems, Inc. | Method of making expandable-collapsible bodies by temperature gradient expansion molding |
KR100727219B1 (ko) * | 2004-11-08 | 2007-06-13 | 주식회사 엘지화학 | (메타)아크릴 시럽의 제조 방법 |
DE602006006028D1 (de) * | 2005-02-04 | 2009-05-14 | Denki Kagaku Kogyo Kk | Harzzusammensetzungen, daraus gewonnener gehärteter artikel sowie folie |
US20070085236A1 (en) * | 2005-10-17 | 2007-04-19 | Horn Donald R | Process for making solid surface counter tops |
JP4911456B2 (ja) | 2006-11-21 | 2012-04-04 | 富士フイルム株式会社 | ポジ型感光性組成物、該ポジ型感光性組成物に用いられる高分子化合物、該高分子化合物の製造方法及びポジ型感光性組成物を用いたパターン形成方法 |
US20080241446A1 (en) * | 2007-03-28 | 2008-10-02 | Adzima Leonard J | Composite material and methods of filament winding, pultrusion and open molding that material |
KR101142261B1 (ko) * | 2008-11-28 | 2012-05-08 | 엘지엠엠에이 주식회사 | 내화학성과 내열성이 우수한 메타크릴계 공중합체 |
FR2943073B1 (fr) * | 2009-03-16 | 2012-12-14 | Astrium Sas | Utilisation de resines durcissables contenant un prepolymere a base de (meth)acrylate de glycidyle pour la fabrication de materiaux composites a usage spatial |
FR2981652B1 (fr) * | 2011-10-21 | 2015-03-27 | Arkema France | Composites via la polymerisation in-situ de resines thermoplastiques methacryliques |
KR101548342B1 (ko) * | 2011-12-26 | 2015-08-28 | 제일모직주식회사 | 인조대리석용 칩, 이를 함유하는 인조대리석 및 그 제조방법 |
FR2993581B1 (fr) | 2012-07-18 | 2016-01-22 | Arkema France | Procede d'impregnation pour un substrat fibreux, sirop (meth)acrylique liquide pour le procede d'impregnation, son procede de polymerisation et produit structure obtenu a partir de celui-ci |
DE102013226503B3 (de) * | 2013-12-18 | 2015-06-11 | Tesa Se | Verfahren zur Herstellung kurzkettiger Makromoleküle auf Basis von Acrylatmonomeren |
FR3016641B1 (fr) | 2014-01-22 | 2020-02-21 | Arkema France | Procede d'impregnation pour un substrat fibreux fonctionnel, sirop monomere liquide pour le procede d'impregnation, sa methode de polymerisation et article structurel obtenu |
FR3016642B1 (fr) | 2014-01-22 | 2020-02-21 | Arkema France | Procede d'impregnation pour un substrat fibreux, sirop monomere liquide pour le procede d'impregnation, sa methode de polymerisation et article structurel obtenu |
DE102014202161B4 (de) * | 2014-02-06 | 2021-06-02 | Robert Bosch Gmbh | Temperierplatte, Verwendung einer Temperierplatte und Verfahren zur Herstellung einer Temperierplatte |
KR101948686B1 (ko) | 2014-09-29 | 2019-02-18 | 주식회사 엘지화학 | 아크릴 시럽의 제조방법 및 아크릴 시럽 |
WO2020021958A1 (ja) * | 2018-07-25 | 2020-01-30 | 日立化成株式会社 | アクリル樹脂及びその製造方法、樹脂組成物セット、蓄熱材並びに物品 |
KR102312578B1 (ko) * | 2019-10-07 | 2021-10-15 | (주) 웹스 | 인조대리석 제조용 조성물 |
WO2023178314A1 (en) * | 2022-03-17 | 2023-09-21 | Magna Exteriors Inc. | Recyclable sheet molding compound using liquid thermoplastic (meth) acrylic resin |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5035278A (ja) * | 1973-07-24 | 1975-04-03 | ||
JPS63179912A (ja) * | 1986-11-27 | 1988-07-23 | ソシエテ シミック デ シャルボナージュ エス.アー. | 不飽和ポリアクリル系樹脂組成物 |
Family Cites Families (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1154943B (de) | 1960-03-02 | 1963-09-26 | Reichhold Chemie Ag | Verfahren zur Verbesserung von Mischpolymerisaten auf der Grundlage acrylierter Epoxyharzester |
US3310540A (en) * | 1962-08-02 | 1967-03-21 | Du Pont | Water-soluble polymers |
US3532708A (en) | 1967-11-02 | 1970-10-06 | Monsanto Co | Crosslinkable pressure-sensitive adhesive resins |
US3730930A (en) * | 1971-08-16 | 1973-05-01 | Ford Motor Co | Compositions for powder coatings containing acrylate polymers or esters of fluorinated fatty acids as flow control agents |
US4085246A (en) | 1975-06-18 | 1978-04-18 | E. I. Du Pont De Nemours And Company | Simulated granite and its preparation |
JPS5850271B2 (ja) | 1975-08-05 | 1983-11-09 | 日石三菱株式会社 | ヒフクケイセイホウ |
JPS532189A (en) | 1976-06-29 | 1978-01-10 | Katsushi Toyoda | Device for supporting and transferring bag in packer |
JPS5731912A (en) | 1980-08-01 | 1982-02-20 | Dainippon Ink & Chem Inc | Production of acrylic smc or bmc |
JPS58225145A (ja) | 1982-06-21 | 1983-12-27 | Mitsubishi Monsanto Chem Co | 耐熱性樹脂組成物 |
US4565854A (en) | 1983-04-07 | 1986-01-21 | Kuraray Co., Ltd. | Polymer having thiol end group |
US4524190A (en) | 1984-05-14 | 1985-06-18 | The United States Of America As Represented By The Secretary Of The Navy | Process for preparation of cross-linked poly(tri-n-butyltin)methacrylate with simultaneous particle size reduction |
US4617367A (en) * | 1984-11-28 | 1986-10-14 | Mitsui Toatsu Chemicals, Inc. | Methyl methacrylate syrup composition |
JPS61243804A (ja) | 1985-04-23 | 1986-10-30 | Nippon Shokubai Kagaku Kogyo Co Ltd | 耐熱性人工大理石の製法 |
DE3664328D1 (en) | 1985-05-01 | 1989-08-17 | Mitsubishi Rayon Co | Process for preparing methacrylimide-containing polymers |
US4806600A (en) | 1986-04-15 | 1989-02-21 | Mitsui Toatsu Chemicals, Incorporated | Methyl methacrylate syrup composition |
ZA872282B (en) | 1986-05-23 | 1987-11-25 | Grace W R & Co | Radiation curable liquid maleated polymeric hydrocarbon(meth)acrylate prepolymer and formulations containing same |
JPH0730125B2 (ja) | 1986-08-01 | 1995-04-05 | 昭和高分子株式会社 | 硬化性樹脂の製造方法 |
DE3709562A1 (de) * | 1987-03-24 | 1988-10-06 | Roehm Gmbh | Vertraegliche mischungen von polycarbonat- und methylmethacrylat-copolymeren |
CA1339485C (en) | 1988-05-17 | 1997-09-30 | Kenji Seko | Active energy ray-curable unsaturated resin composition |
US5242968A (en) * | 1990-08-27 | 1993-09-07 | Aristech Chemical Corporation | Acrylic-filled thermoformable acrylic sheet |
JP3198133B2 (ja) * | 1991-12-26 | 2001-08-13 | 三井化学株式会社 | 成形用樹脂組成物 |
BE1005993A3 (nl) * | 1992-06-10 | 1994-04-12 | Dsm Nv | Hars voor poedercoatings toepasbaar in de automobielindustrie. |
JPH06298883A (ja) | 1993-04-14 | 1994-10-25 | Dainippon Ink & Chem Inc | 成形材料及び人工大理石の製造方法 |
DE4337481A1 (de) * | 1993-11-03 | 1995-05-04 | Basf Ag | Radikalisch vernetzbare Copolymerisate |
JPH07188505A (ja) * | 1993-12-27 | 1995-07-25 | Nippon Shokubai Co Ltd | アクリル樹脂プリミックスおよび人工大理石の製造方法 |
DE4405041C2 (de) | 1994-02-17 | 1995-12-21 | Herberts Gmbh | Verfahren zur Herstellung von Makromonomeren und deren Verwendung als Comonomere bei Polymerisations-, Polyadditions- oder Polykondensations-Reaktionen |
KR0185028B1 (ko) * | 1995-06-21 | 1999-05-15 | 아이다 겐지 | (메트)아크릴계 성형재료 및 그의 제조방법 |
-
1996
- 1996-10-02 WO PCT/JP1996/002860 patent/WO1997012918A1/ja not_active Application Discontinuation
- 1996-10-02 CN CNB961914319A patent/CN1152058C/zh not_active Expired - Fee Related
- 1996-10-02 US US08/849,612 patent/US6191229B1/en not_active Expired - Fee Related
- 1996-10-02 EP EP96932796A patent/EP0796873A4/en not_active Withdrawn
- 1996-10-02 KR KR1019970703762A patent/KR100232546B1/ko not_active IP Right Cessation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5035278A (ja) * | 1973-07-24 | 1975-04-03 | ||
JPS63179912A (ja) * | 1986-11-27 | 1988-07-23 | ソシエテ シミック デ シャルボナージュ エス.アー. | 不飽和ポリアクリル系樹脂組成物 |
Non-Patent Citations (1)
Title |
---|
See also references of EP0796873A4 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009110503A1 (ja) * | 2008-03-05 | 2009-09-11 | 株式会社日本触媒 | 重合体、硬化性樹脂組成物、硬化物、及び物品 |
US8399583B2 (en) | 2008-03-05 | 2013-03-19 | Nippon Shokubai Co., Ltd. | Polymer, curable resin composition, cured product, and article |
Also Published As
Publication number | Publication date |
---|---|
US6191229B1 (en) | 2001-02-20 |
KR100232546B1 (ko) | 1999-12-01 |
CN1168144A (zh) | 1997-12-17 |
CN1152058C (zh) | 2004-06-02 |
EP0796873A1 (en) | 1997-09-24 |
EP0796873A4 (en) | 1999-11-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO1997012918A1 (fr) | Sirop (meth)acrylique, procede d'elaboration de ce sirop et procede d'elaboration d'un materiau de moulage contenant un tel sirop | |
KR0185028B1 (ko) | (메트)아크릴계 성형재료 및 그의 제조방법 | |
JP3910230B2 (ja) | 樹脂組成物の処理方法および樹脂材料 | |
JP4212704B2 (ja) | (メタ)アクリル系樹脂組成物およびその硬化物 | |
JP3072052B2 (ja) | (メタ)アクリル系成形材料およびその製造方法 | |
JP2000273130A (ja) | (メタ)アクリル系シラップ、その製造方法および上記(メタ)アクリル系シラップを含む成形材料ならびに成形品 | |
JP3004571B2 (ja) | (メタ)アクリルシラップおよびその製造方法並びに(メタ)アクリルシラップを含む成形材料 | |
JP3953551B2 (ja) | (メタ)アクリル系樹脂組成物およびその製造方法 | |
JP3847388B2 (ja) | (メタ)アクリル系樹脂組成物およびそれを含む人工大理石用組成物 | |
JP2001220500A (ja) | プレス成形用樹脂組成物及び該プレス成形用樹脂組成物を用いた人工大理石成形物 | |
JPS6018506A (ja) | 熱可塑性重合体低プロフアイル添加剤を含有する硬化性成形組成物 | |
JPH09286889A (ja) | 成形材料 | |
JP3056695B2 (ja) | 成形材料およびその成形方法 | |
JP3270734B2 (ja) | 耐衝撃性アクリル樹脂組成物、その製法及び成形品 | |
JPH09302010A (ja) | (メタ)アクリル系樹脂組成物およびその製造方法 | |
JP2001262012A (ja) | ゲルコート用(メタ)アクリル系樹脂組成物 | |
JPH09227750A (ja) | 加圧成形用成形材料およびその製造方法 | |
JPH0251556A (ja) | 不飽和ポリエステル樹脂組成物、成形材料及び成形物 | |
JPH02117953A (ja) | 低収縮性熱硬化性樹脂組成物 | |
JP2000143927A (ja) | (メタ)アクリル系樹脂組成物及びそれを用いた成形体 | |
JP2001294634A (ja) | 型内被覆用組成物、型内被覆された樹脂成形品および該樹脂成形品の製造方法 | |
JPH09194513A (ja) | 樹脂組成物の製造方法 | |
JP2000159967A (ja) | (メタ)アクリル系成形材料及びそれを用いた成形品 | |
JPH09286888A (ja) | 加圧成形用成形材料 | |
JPH0819210B2 (ja) | 硬化性樹脂組成物、該組成物を成形硬化してなる人工大理石およびその製造方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 96191431.9 Country of ref document: CN |
|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): CN KR US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 08849612 Country of ref document: US |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1019970703762 Country of ref document: KR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1996932796 Country of ref document: EP |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWP | Wipo information: published in national office |
Ref document number: 1996932796 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1019970703762 Country of ref document: KR |
|
WWG | Wipo information: grant in national office |
Ref document number: 1019970703762 Country of ref document: KR |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 1996932796 Country of ref document: EP |