WO2005075564A1 - 樹脂組成物およびそれを成形してなる成形体 - Google Patents
樹脂組成物およびそれを成形してなる成形体 Download PDFInfo
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- WO2005075564A1 WO2005075564A1 PCT/JP2005/001671 JP2005001671W WO2005075564A1 WO 2005075564 A1 WO2005075564 A1 WO 2005075564A1 JP 2005001671 W JP2005001671 W JP 2005001671W WO 2005075564 A1 WO2005075564 A1 WO 2005075564A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L55/00—Compositions of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08L23/00 - C08L53/00
- C08L55/02—ABS [Acrylonitrile-Butadiene-Styrene] polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L69/00—Compositions of polycarbonates; Compositions of derivatives of polycarbonates
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/16—Nitrogen-containing compounds
- C08K5/29—Compounds containing one or more carbon-to-nitrogen double bonds
Definitions
- the present invention relates to a resin composition and a molded product obtained by molding the same.
- biodegradable polyester resins such as polylactic acid have attracted attention from the viewpoint of environmental protection.
- polylactic acid is one of the resins with high heat resistance, and can be mass-produced.
- polylactic acid can be produced using plants such as corn and sweet potato as raw materials, and can contribute to saving of dead resources such as petroleum.
- ABS resin acrylonitrile Z-butadiene Z-styrene copolymer resin
- PC resin a biodegradable polyester resin represented by the polylactic acid resin
- PC resin a polycarbonate resin having high heat resistance
- PA-07-109413 proposes a resin composition comprising a polylactic acid resin and an aromatic polycarbonate resin.
- PA-11-140292 includes a polylactic acid and a crosslinked polycarbonate.
- a resin composition containing the same has been proposed. In each case, the heat resistance is improved to a practical level as compared with polylactic acid alone.
- JP-A-07-109413 it is desirable from the viewpoint of heat resistance and mechanical properties to blend an aromatic polycarbonate resin in a high proportion. Saving resources is not enough. Also, simply melting and kneading polylactic acid and polycarbonate makes it difficult to achieve uniform compatibility because the difference in melt viscosity is large.For example, the nozzle force of a kneading extruder causes the molten resin to be discharged with pulsation. However, there is a problem that stable pelletization is difficult.
- JP-A-11 140292 also states that the use of cross-linked polycarbonate is desirable in terms of the effect of modifying the polylactic acid resin, and that a linear polycarbonate has a significant effect of modifying the impact resistance. Not been.
- polycarbonate has a higher melt viscosity than polylactic acid, so it is difficult to mold a thin material having a thickness of less than lmm.
- the melt viscosity is further increased, so that it is not preferable as a practical molding material.
- JP-A-2001-123055 the components that can be alloyed with polylactic acid resin are limited to aliphatic polyester resins, and therefore, there is a problem that the heat resistance is low even if the impact resistance can be improved. is there. Further, according to the present inventors, the modified olefinic conjugate used as a compatibilizer in JP-A-2001-123055 was mixed with a polylactic acid resin and a polymer alloy of PC resin or polylactic acid resin. Even when mixed with a polymer alloy of PC resin and ABS resin, the improvement in impact resistance as a compatibilizing effect was hardly obtained.
- the present invention solves the above-mentioned problems, and is an alloy of polylactic acid-based biodegradable polyester resin and PC resin having excellent compatibility, and a polylactic acid-based biodegradable polymer having excellent compatibility.
- An alloy of a tellurium resin, a PC resin, and an ABS resin which aims to provide a resin composition that has excellent heat resistance and impact resistance, saves oil resources, and has a low environmental impact. .
- the present inventors have conducted intensive studies, and as a result, have found that a crosslinked biodegradable polyester resin and polycarbonate A resin composition comprising a resin, or a resin composition further containing an acrylonitrile Z-butadiene Z styrene copolymer resin, and a silicone compound or an ethylene Z glycidyl meta having a specific structure further added to the resin composition.
- the present inventors have found that the above-mentioned object is achieved by a resin composition containing a tallylate copolymer, and arrived at the present invention.
- the gist of the present invention is as follows.
- the silicone resin (D) O. 05-10 parts by mass is further contained per 100 parts by mass of the total amount of the resin ( ⁇ )-(C).
- the total amount of the resin (A) — (C) is 100 parts by mass, and the modified Olefin conjugate (E) 0.1— Contains 20 parts by weight.
- the mass ratio of the resins (B) and (C) is (B) / ⁇ (B) + (C) ⁇ ⁇ 0. The relationship of 3 is satisfied.
- the crosslinked biodegradable polyester resin (A) is obtained by reacting the (meth) acrylate ester conjugate with 0.01 to 20 parts by mass per 100 parts by mass of the biodegradable polyester resin.
- Crosslinked biodegradable polyester resin (A) is obtained by reacting peroxide with 0.01 to 20 parts by mass per 100 parts by mass of biodegradable polyester resin from (1) The resin composition of any one of (5) to (5).
- the biodegradable polyester resin of (A) is mainly composed of polylactic acid or polylactic acid. Fat composition.
- the total amount of the resin (A)-(C) is 100 parts by mass, and further the carpo-imide imidized product 0.01-1-5 A resin composition containing parts by weight.
- the resin composition according to (8) which is a compound having an isocyanate as a terminal group in the carbodiimide bonding compound.
- a resin composition and a molded article are provided.
- the resin composition of the present invention can be formed into various molded articles by injection molding or the like.
- the resin composition of the present invention can use a natural-derived resin as a biodegradable polyester resin, so that it can contribute to the saving of depleted resources such as petroleum, and The utility value above is extremely high.
- the resin composition of the present invention comprises a crosslinked biodegradable polyester resin (A), a polycarbonate resin (B) and, if necessary, an acrylonitrile Z butadiene Z styrene copolymer resin (C). Are mixed.
- the mixing ratio of the crosslinked biodegradable polyester resin (A) as the resin component is the same as that of the resin (A)-(C) as the resin component. It is 30-90% by mass, more preferably 50-70% by mass of the total 100% by mass.
- the mixing ratio of the resin (A) is less than 30% by mass, the ratio of the biodegradable raw material is reduced, and the environmental advantage is reduced.
- the amount of the resin (A) exceeds 90% by mass, physical properties such as heat resistance and impact resistance are impaired.
- the crosslinked biodegradable polyester resin (A) is obtained by introducing a crosslinked structure into a biodegradable polyester resin.
- Examples of the biodegradable polyester resin serving as the skeleton of the resin (A) include poly (L-lactic acid), poly (D-lactic acid), polydarcholate, polyproprolataton, polybutylene succinate, polyethylene succinate, and polybutylene. Adipate terephthalate, polybutylene succinate terephthalate and the like can be mentioned, and two or more of these may be used. Above all, heat resistance, molding In terms of properties, it is desirable to use poly (L-lactic acid), poly (D-lactic acid), or a mixture or copolymer thereof. From the viewpoint of biodegradability, it is preferable that poly (L-lactic acid) is mainly used. In addition, from the perspective of saving petroleum resources, poly (L-lactic acid), which is favored by biodegradable polyester resins produced from plant-derived raw materials, satisfies this condition.
- Polylactic acid mainly composed of poly (L-lactic acid) has a different melting point depending on the ratio of the contained D-lactic acid component.
- its melting point should be 160 ° C or more in consideration of the mechanical properties and heat resistance of the molded article obtained from the resin composition. Is preferred.
- the proportion of the D-lactic acid component is less than about 3 mol%.
- melt flow rate of a mixture of multiple biodegradable polyester resins at 190 ° C and a load of 21.2N is 0.1-50gZlO More preferably, it is 0.2 to 20 gZlO, more preferably 0.5 to 10 gZlO. If the melt flow rate exceeds 50 gZlO, the melt viscosity is too low, and the mechanical properties and heat resistance of the molded product may be poor. On the other hand, if the melt flow rate is less than 0.1 lgZlO, the load during molding may be too high and the operability may decrease.
- the biodegradable polyester resin (A) is usually produced by a known melt polymerization method, and some of them are produced by further using a solid phase polymerization method.
- a method for adjusting the melt flow rate of the biodegradable polyester resin to a predetermined range when the melt flow rate is too large, a small amount of a chain extender, for example, diisocyanate disulfide, bisoxane A method of increasing the molecular weight of the resin using a zolini conjugate, an epoxy conjugate, an acid anhydride, or the like can be used.
- a method of mixing with a biodegradable polyester resin or a low molecular weight compound having a large melt flow rate can be used.
- the crosslinked structure of the crosslinked biodegradable polyester resin (A) is not particularly limited. Even if the biodegradable polyester resin molecules are directly crosslinked, they may be indirectly crosslinked via a crosslinking aid. It may be a crosslinked one or a mixture of these crosslinked structures.
- an electron beam is irradiated.
- a known method such as a method using a polyfunctional compound such as a polyvalent isocyanate compound or the like can be applied.
- radical crosslinking by use of a peroxidic acid is preferred.
- peroxide examples include benzoyl peroxide, bis (butyl-butoxy) trimethylcyclohexane, bis (butyl-butoxy) cyclododecane, butylbis (butylperoxy) valerate, and dicumyl peroxide.
- the amount of the peroxide is preferably 0.01 to 20 parts by mass, more preferably 0.1 to 10 parts by mass, per 100 parts by mass of the biodegradable polyester resin. Even if it exceeds 20 parts by mass, it can be used, but the effect is saturated and it is not economical. Since the peroxide is decomposed and consumed when mixed with the resin, even if used at the time of blending, the peroxide may not remain in the obtained resin composition.
- cross-linking auxiliary agent examples include dibutylbenzene, diarylbenzene, divinylnaphthalene, divinylphenol, divinylcarbazole, dibutylpyridine, and their nuclear-substituted conjugates and closely related homologues; Atharylate, butylene glycol diatalylate, triethylene glycol diatalylate, 1,6-hexanediol diatalylate, tetramethylol methane tetraatalylate, ethylene glycol dimetharate, butylene glycol dimetharate, triethylene Glycono resin methacrylate, tetraethylene glycolone dimethacrylate, 1,6-hexanediol dimethacrylate, 1,9-nonanediol dimethacrylate, 1,10-decane
- Polybutylesters of aliphatic and aromatic polycarboxylic acids such as polyallyl ester, polyacryloyloxyalkyl ester, polymethacryloyloxyanolequinole ester, diethylene glycol divininole ether, hydroquinone divinyl ether, and bisphenol A diaryl ether; Aliphatic and aromatic polyhydric alcohols Polybutyl ethers or polyallyl ethers; triaryl cyanurate, triallyl isocyanurate, etc., cyranuric acid or isocyanuric acid allyl ester; triallyl phosphate, trisacryloxyshethyl phosphate, N-phenylmaleimide, N, N, Polyfunctional monomers such as maleimide compounds such as m-phenylenebismaleimide; compounds having two or more triple bonds such as dipropagyl phthalate and dipropagyl maleate can be used.
- the amount of these crosslinking aids is not particularly limited, but is preferably
- (meth) acrylic acid ester conjugates are preferred from the viewpoint of crosslinking reactivity.
- the biodegradable polyester resin component is crosslinked, thereby improving mechanical strength, heat resistance and dimensional stability.
- the (meth) acrylate ester conjugate has a high reactivity with the biodegradable resin and therefore has relatively little toxicity due to the remaining monomer, and has little coloring of the resin.
- Compounds having a (meth) acryl group or having at least one (meth) acryl group and at least one glycidyl group or butyl group are preferred.
- Specific compounds include glycidyl methacrylate, glycidyl atalylate, glycerol dimethacrylate, trimethylolpropane trimethacrylate, trimethylolpropane triatalylate, aryloxy polyethylene glycol monoacrylate, and aryloxy polyethylene.
- Glycol monomethacrylate ethylene glycol diatalate, ethylene glycol dimetharate, polyethylene glycol dimetharate, polyethylene glycol diatalylate, polypropylene glycol dimetharate, polypropylene glycol diatalylate, polytetramethylene glycol Dimetharylate, or a copolymer of an alkylene glycol in which these alkylene glycol moieties have different alkylene groups, Et al in, butanediol meth Tari rate, butanediol Atari rate or the like can be mentioned up.
- the amount is preferably 0.01 to 20 parts by mass with respect to 100 parts by mass of the biodegradable polyester resin. 05-10 parts by weight is even more preferred 0.1-5 parts by weight is even more preferred. It can be used in excess of 20 parts by mass as long as operability is not adversely affected.
- a crosslinking agent such as a peroxide or a crosslinking aid
- a method of melt-kneading using a general extruder can be used. Wear. It is preferable to use a twin-screw extruder in order to improve the kneading state.
- the kneading temperature is in the range of (melting point of biodegradable polyester resin + 5 ° C)-1 (melting point of biodegradable polyester resin + 100 ° C).
- the kneading time is preferably 20 seconds-30 minutes. If the temperature is lower than this range or for a short time, kneading and reaction become insufficient, and if the temperature is higher or longer, decomposition or coloring of the resin may occur.
- a cross-linking agent such as a peroxide or a cross-linking aid is preferably in a solid state by supplying them using a dry blend or a powder feeder. And a method of directly injecting it into the barrel of an extruder.
- a preferred method is to dissolve or disperse the crosslinking aid and a crosslinking agent such as Z or peroxide in a medium.
- a method of injecting into a kneader There is a method of injecting into a kneader. According to this, operability can be significantly improved. That is, when a biodegradable polyester resin component and a crosslinking agent such as a peroxide are melt-kneaded, a solution or dispersion of a crosslinking aid is injected, or the polyester resin component is melt-kneaded. At this time, a solution or dispersion of a crosslinking aid and a crosslinking agent such as a peroxide can be injected or melt-kneaded.
- a general medium is used and is not particularly limited.
- a plasticizer excellent in compatibility with the biodegradable polyester resin according to the present invention is preferable.
- a plasticizer for example, an aliphatic polycarboxylic acid ester derivative, an aliphatic polyhydric alcohol ester derivative, an aliphatic oxyester derivative, an aliphatic polyether derivative, an aliphatic polyether polyvalent carboxylic acid ester derivative, etc.
- a plasticizer for example, an aliphatic polycarboxylic acid ester derivative, an aliphatic polyhydric alcohol ester derivative, an aliphatic oxyester derivative, an aliphatic polyether derivative, an aliphatic polyether polyvalent carboxylic acid este
- Specific compounds include glycerin diacetate monolaurate, glycerin diacetate monoforce plate, dimethyl adipate, dibutyl adipate, triethylene glycol diacetate, acetyl methinole ricinoleate, acetinole tributynolec acid, Examples include polyethylene glycolone and dibutinole diglycol succinate.
- the amount of the plasticizer used as a dispersion medium is preferably 30 parts by mass or less based on 100 parts by mass of the biodegradable polyester resin. Parts by mass are more preferred.
- a plasticizer may not be used. However, when the reactivity is high, it is preferable to use 0.1 part by mass or more. Since this dispersion medium may volatilize when mixed with the resin, it may not remain in the obtained resin composition even when used in the production.
- the component of the polycarbonate resin (B) in the present invention is a repeating unit composed of a bisphenol group residue and a carbonate residue.
- Examples of the starting bisphenols include 2,2-bis (4-hydroxyphenyl) propane, 2,2-bis (3,5-dibutene 4-hydroxyphenyl) propane, and 2,2-bis (3,5-Dimethyl-4-hydroxyphenyl) propane, 1,1-bis (4-hydroxyphenyl) cyclohexane, 1,1bis (3,5-dimethyl-4-hydroxyphenyl) cyclohexane Xan, 1,1-bis (4-hydroxyphenyl) decane, 1,4-bis (4-hydroxyphenyl) propane, 1,1-bis (4-hydroxyphenyl) cyclododecane, 4,4'- Dihydroxydiphenyl ether, 4,4 'dithiodiphenol, 4,4' dihydroxy-3,3'-dichlorodiphenyl ether, 4,4 'dihydroxy-2,5-dihydroxydiphenyl ether and the like. .
- Examples of the precursor for introducing the carbonate residue unit include phosgene and diphenyl carbonate.
- the intrinsic viscosity of the polycarbonate resin (B) is preferably in the range of 0.40 to 0.64. If it exceeds 0.64, the melt viscosity of the resin composition may be so high that kneading extrusion or injection molding may be difficult. On the other hand, if it is less than 0.40, the impact strength of the obtained molded product may be insufficient.
- the mixing ratio of the polycarbonate resin (B) is 10 to 70% by mass in the total amount of the resins (A) and (C) of 100% by mass.
- the content of the resin (B) is less than 10% by mass, the heat resistance and impact resistance of the obtained resin composition are insufficient, and when it exceeds 70% by mass, the dependence of the raw material on petroleum resources is high. As a result, the degree of environmental contribution is low.
- the above-mentioned crosslinked biodegradable polyester resin (A) and In addition to polycarbonate resin (B) and acrylonitrile Z butadiene Z styrene copolymer resin (C) may be used.
- the resin (C) By adding the resin (C), the fluidity of the obtained resin composition at the time of molding is increased, and the residual strain inside the molded article is reduced, so that the warpage of the molded article can be reduced. Further, the appearance of the molded article can be made excellent.
- the mixing ratio of the resin (C) is in the range of 0 to 50% by mass relative to the total amount of the resin (A)-(C) of 100% by mass. Further, the relationship between the mixing ratios of the resins (B) and (C) preferably satisfies (B) / ⁇ (B) + (C) ⁇ ⁇ 0.3 by mass ratio. When the ratio of the polycarbonate resin (B) to the total amount of the resin (B) and the resin (C) satisfying this formula is 0.3 or more, the heat resistance of the obtained resin composition is improved. Impact resistance is further improved.
- Acrylonitrile Z butadiene Z styrene copolymer resin (C) is a resin generally referred to as "ABS resin” as described above, and contains an aliphatic conjugated diene monomer as an essential component.
- ABS resin a resin generally referred to as "ABS resin” as described above, and contains an aliphatic conjugated diene monomer as an essential component.
- a monomer containing a cyanide vinyl monomer and an aromatic vinyl monomer as essential components 30 to 95 It is a graft copolymer obtained by polymerizing mass%.
- Examples of the aliphatic conjugated gen used herein include 1,3-butadiene, isoprene, and chloroprene.
- 1,3-butadiene can be preferably used from the viewpoint of impact resistance.
- the ratio of the aliphatic conjugated diene monomer is preferably 30 to 100 parts by mass based on 100 parts by mass of the total of the monomers used for producing the rubbery polymer. By setting the ratio to 30 parts by mass or more, a graft copolymer having good impact resistance can be obtained.
- the other monomer is a diene monomer.
- Various monomers copolymerizable with the polymer can be used.
- cyanide-based monomer such as acrylonitrile and metal-tol-tolyl
- aromatic-based monomer such as styrene, ⁇ -methylstyrene, ⁇ -chlorostyrene, and ⁇ -methylstyrene
- acrylic acid examples include unsaturated carboxylic esters such as methyl, ethyl acrylate, ⁇ -butyl acrylate, 2-ethylhexyl acrylate, ⁇ -xysyl acrylate, methyl methacrylate, and ethyl methacrylate.
- the monomer to be graft-polymerized to the rubber-like polymer contains vinyl cyanide-based monomer and aromatic vinyl-based monomer as essential components.
- vinyl cyanide-based monomer include acrylonitrile, metharyl-tolyl, cyanidani biylidene, and the like. Among them, acrylonitrile is particularly preferred.
- aromatic vinyl monomer examples include butyltoluenes such as styrene, ⁇ -methylstyrene and ⁇ -methylstyrene, halogenated styrenes such as ⁇ -chlorostyrene, ⁇ -t-butylstyrene, dimethylstyrene, and styrene. -Lunaphthalenes and the like. Of these, styrene and ⁇ -methylstyrene are particularly preferred.
- monomers for graft polymerization in addition to vinyl cyanide-based monomers and aromatic vinyl-based monomers, other monomers can be used in combination, if desired.
- specific examples thereof include unsaturated carboxylic esters such as methyl acrylate, ethyl acrylate, ⁇ -butyl acrylate, 2-ethylhexyl acrylate, ⁇ -xyl acrylate, methyl methacrylate, and ethyl methacrylate.
- Unsaturated monomers such as maleic anhydride, itaconic anhydride and citraconic anhydride; maleimide, ⁇ -methylmaleimide, ⁇ -butylmaleimide, ⁇ -phenylmaleimide, ⁇ -cyclohexylmaleimide, etc. And an imide compound of an unsaturated dicarboxylic acid. These may be used alone or in combination of two or more.
- the monomers for graft polymerization include, as necessary, glycidyl methacrylate, methacrylic acid, acrylic acid, methacrylamide, 2-hydroxyethyl methacrylate, and polyethylene glycol monomethacrylate. It is also possible to use 20% by mass or less, preferably 15% by mass or less based on the total of 100% by mass of the monomers for graft polymerization.
- mass ratio 5-70. / 30-95, preferably 1065-3590.
- metal catalyst When a metal catalyst is used during the polymerization of acrylonitrile Z butadiene Z styrene copolymer resin, it is preferable to remove the metal catalyst after the polymerization. This is because the metal catalyst promotes the hydrolysis of the biodegradable polyester resin, and may lower the wet heat resistance.
- the resin (A)-(C) as each component may be mixed at a predetermined ratio in the final resin composition.
- the mixing order and mixing method are not particularly limited.
- the resin raw materials of the components (A), (B) and (C) may be melt-mixed simultaneously, or two of them may be mixed first, and then the other may be mixed. It is good.
- the polycarbonate resin (B) and the acrylonitrile Z-butadiene Z-styrene copolymer resin (C) may be mixed in advance prior to blending the crosslinked biodegradable polyester resin (A). preferable.
- the fluidity of the final resin composition during molding can be further improved, and the appearance of the molded article can be improved.
- the mixture of the polycarbonate resin (B) and the acrylonitrile Z-butadiene Z-styrene copolymer resin (C) commercially available ones can also be used.
- the resin composition of the present invention can further improve the impact resistance performance by blending the silicone conjugate (D).
- the silicone conjugate is a polymer having a siloxane bond unit (formula 1).
- R SiO (formula 2) as a basic unit is a linear polymer.
- the type of the organic group R bonded to the silicon other than the main chain is not particularly limited, and any known organic group can be used.
- any known organic group can be used.
- a methyl group, a phenyl group, and hydrogen are mentioned.
- a modified silicone compound modified with an organic functional group such as an epoxy group, an amino group, an alcohol group, or a carboxyl group, or an alkyl group, a polyether, or a higher fatty acid ester can also be used. Further, two or more of these may be used in combination.
- the point of compatibility with the methylphenylsilicone conjugate material is also desirable.
- the terminal group of the polymer is not particularly limited, and those having a methyl group, a phenyl group, and other functional groups can be used.
- the trade names of these silicone conjugates are exemplified.
- dimethyl silicone include the TSF451 series from GE Toshiba Silicone, KF96, KF96L, KF96H, KF69, KF92, KF961, KF961, KF965, and KF968 from Shin-Etsu Silicone. And so on.
- Examples of methylphenol silicone include GE Toshiba Silicone's TSF431, TSF433, TSF434, TSF437, TSF4300, and Shin-Etsu Silicone's KF50, KF54, and KF56. No.
- methyl hydrogen silicone examples include “TSF484" from GE Toshiba Silicone and “KF99” from Shin-Etsu Silicone.
- Epoxy-modified silicone oils include “TSF4730” from GE Toshiba Silicones, “KF100T”, “KF101", “KF102” and “KF103” from Shin-Etsu Silicones.
- Amino-modified silicones include GE Toshiba Silicone's TSF4700, TSF4701, TSF4702, TSF47 03, TSF4704, TSF4705, TSF4706, TSF4707, TSF4708, and TSF4708.
- the amount is 0.05-10 parts by mass per 100 parts by mass of the total amount of the resins (A)-(C). If the amount is less than 0.05 part by mass, the effect of improving the impact resistance is poor. If the amount exceeds 10 parts by mass, bleed-out tends to occur, and the heat resistance tends to decrease.
- the modified Olefin conjugate (E) as a compatibilizer, the compatibility can be enhanced and the impact resistance can be further improved.
- the modified resin conjugate in the present invention is obtained by graft copolymerization of poly (meth) acrylate, poly (meth) acrylate, glycidyl methacrylate copolymer, polystyrene, acrylonitrile z styrene copolymer and the like. Add the olefin compound.
- olefin conjugate examples include polyethylene, ethylene Z glycidyl methacrylate copolymer, ethylene Z ethyl acrylate copolymer, ethylene Z butyl acetate copolymer, and ethylene ethyl acrylate.
- Water maleic acid copolymer and the like can be mentioned.
- ethylene Z glycidyl methacrylate copolymer obtained by graft copolymerization of poly (methyl methacrylate) and poly (methyl methacrylate) Z-glycidyl methacrylate copolymer is excellent in impact resistance.
- ethylene Z glycidyl methacrylate copolymer obtained by graft copolymerization of poly (methyl methacrylate) examples include “MODIPA A4200”, “AT13100”, and “AT13130” manufactured by NOF Corporation.
- a specific trade name of an ethylene Z glycidyl methacrylate copolymer obtained by graft copolymerization of a poly (methyl methacrylate) Z glycidyl methacrylate copolymer is, for example, "AT13110" of Nihon Yushi Co., Ltd.
- the compounding amount of the modified olefin conjugate (E) is preferably 0.1 to 20 parts by mass based on 100 parts by mass of the total amount of the resins (A) to (C). If the amount is less than 0.1 part by mass, the effect of compatibilization is hardly exhibited. If the amount exceeds 20 parts by mass, the heat resistance may be reduced.
- a carbodiimide compound can be blended with the resin composition.
- the moist heat resistance of the resin composition is improved by including the carpoimide compound, and a crosslinked structure is introduced between the crosslinked biodegradable polyester resin (A) and the polycarbonate resin (B).
- the compatibility becomes better, and the mechanical properties of the resin composition also improve.
- the carbodiimide compound include 4,4'-dicyclohexylmethanecarbodiimide, tetramethylxylylenecarbodiimide, N, N-dimethylphenylcarbodiimide, and N, N'-di-2,6-diisopropylphenylcarbodiimide. It is not particularly limited as long as it is a carbodiimide compound having one or more carbodiimide groups in a force molecule.
- the carbodiimide compound a compound in which the terminal isocyanate group is sealed with a monoisocyanate or the like may be used, but the moist heat resistance and mechanical properties (particularly, impact resistance) of the resin composition are improved. From this viewpoint, it is preferable to use a carbodiimide compound having an isocyanate group left.
- the isocyanate group has higher reactivity than the carbodiimide group, and a higher effect is obtained.
- the carbodiimide compound can be produced by a conventionally known method, and can be produced by a carbodiimide reaction accompanied by a decarbonation reaction using a diisocyanate compound as a raw material. At this time, if the terminal blocking treatment is not performed, a carbodiimide conjugate having an isocyanate group at the terminal is obtained.
- the amount of the carbodiimide compound is preferably 0.01 to 5 parts by mass, more preferably 0.1 to 13 parts by mass, per 100 parts by mass of the total amount of the resins (A) and (C). If the amount is less than 0.01 parts by mass, the effect of improving the wet heat resistance and the mechanical properties is not obtained, while if it exceeds 5 parts by mass, the heat resistance may be reduced.
- the method of mixing the raw materials is not particularly limited, as long as each component is uniformly dispersed in the resin composition.
- cross-linked biodegradable polyester resin (A), polycarbonate resin (B), acrylonitrile Z butadiene Z styrene copolymer resin (C), silicone resin conjugate (D), modified olefin resin Compound (E) and the like are uniformly blended using a tumbler or Henschel mixer, and then melt-kneaded to pelletize.
- pellets in which two or more types of raw materials are melt-kneaded may be used.
- a composition obtained by melt-kneading or copolymerizing a polycarbonate resin (B) and a silicone conjugate (D), or a composition obtained by mixing a polycarbonate resin (B) with acrylo-tolyl Z butadiene Z styrene Use a composition obtained by melt-kneading the system copolymer resin (C).
- the raw materials other than the carpoimide conjugate are once melt-kneaded with an extruder, and then the carpo-imide conjugate is added and then melt-kneaded again, or extruded by a side feeder or the like.
- a method of adding a carbodiimide compound in the middle of the machine For example, a method of adding a carbodiimide compound in the middle of the machine.
- An organic or inorganic filler may be added to the resin composition for the purpose of improving mechanical strength and heat resistance.
- the compounding amount is preferably 1 to 50 parts by mass with respect to 100 parts by mass of the resin composition.
- Examples of the inorganic filler include glass fibers, metal fibers, carbon fibers, metal whiskers, ceramic whiskers, fibrous reinforcing materials such as potassium titanate, talc, calcium carbonate, and charcoal.
- Examples of the organic filler include naturally occurring polymers such as starch, fine cellulose particles, wood flour, okara, fir husk, bran and kenaf, and modified products thereof.
- glass fibers which are preferred by fibrous reinforcing materials, are most preferable because they can improve heat resistance and impact resistance.
- the glass fiber is preferably subjected to a surface treatment in order to enhance the adhesion to the resin component.
- the hopper force may be added to the extruder at the same time as the other raw materials, or the intermediate force of the kneading machine may be added using a side feeder.
- a master resin filled with a fibrous reinforcing material at a high concentration is prepared, and the master resin can be diluted with a base resin at the time of molding to be used so as to have a desired concentration.
- the resin composition has a pigment, a heat stabilizer, an anti-oxidation agent, a weathering agent, a light-proofing agent, a flame retardant, a plasticizer, a lubricant, a mold release agent, as long as its properties are not significantly impaired.
- An antistatic agent, a crystal nucleus material and the like can be added.
- the heat stabilizer and the anti-oxidizing agent include hindered phenols, phosphorus-containing compounds, hindered amines, zeo compounds, copper compounds, alkali metal halides, and vitamin E.
- As the flame retardant a halogen-based flame retardant, a phosphorus-based flame retardant, and an inorganic flame retardant can be used.
- non-halogen flame retardant examples include phosphorus flame retardants, hydrated metal compounds (aluminum hydroxide, magnesium hydroxide), N-containing compounds (melamine-based, guadin-based), and inorganic compounds. (Borate, Mo compound).
- examples of the inorganic crystal nucleus material include talc and phosphorus
- examples of the organic crystal nucleus material include a sorbitol compound, benzoic acid and a metal salt of the compound, a phosphate metal salt, and a rosin compound. The method of mixing these with the resin composition is not particularly limited.
- the resin composition of the present invention may be formed into various molded articles by a molding method such as injection molding, blow molding, extrusion molding, inflation molding, and vacuum molding, air pressure molding, and vacuum pressure molding after sheet processing. Can be.
- a molding method such as injection molding, blow molding, extrusion molding, inflation molding, and vacuum molding, air pressure molding, and vacuum pressure molding after sheet processing.
- the injection molding method is generally preferred
- molding methods such as gas injection molding and injection press molding can be adopted.
- Injection molding conditions suitable for the resin composition of the present invention vary depending on the resin composition ratio, but it is appropriate that the cylinder temperature is in the range of 180 to 260 ° C, more preferably 190 to 250 ° C. is there .
- the mold temperature should be 140 ° C or less.
- the cylinder temperature is too low, the operability becomes unstable, such as short-circuiting of the molded product, or it tends to overload.On the other hand, if the cylinder temperature is too high, the resin composition will decompose, In some cases, problems such as a decrease in the strength of the obtained molded body and coloring of the molded body may occur.
- the heat resistance of the molded article made of the resin composition of the present invention can be enhanced by promoting crystallization by controlling the conditions during injection molding and performing heat treatment after molding.
- a method for this for example, there is a method of promoting crystallization by cooling in a mold during injection molding. In this case, it is preferable to cool the mold for a predetermined time while keeping the mold temperature at the crystallization temperature of the resin composition ⁇ 20 ° C.
- the mold temperature may be further lowered to the glass transition temperature of the resin composition or lower, and then the mold may be opened to remove the molded product.
- the molded body include resin parts for electric shading products such as a personal computer housing, a printer housing, and a projector lamp housing, and automotive resins such as bumpers, inner panels, and door trims. Parts and the like. Further, it may be a film, a sheet, a hollow molded article, or the like.
- test condition 4 the measurement was performed at 190 ° C and a load of 21.2N.
- Test specimens were prepared as follows. In other words, using an injection molding machine (TOSHIBA MACHINE IS-80G), the resin is melted at a cylinder temperature of 210-240 ° C, and the injection pressure is 100MPa, the injection time is 15 seconds and the mold is 70 ° C. Fill and cool for 30 seconds.
- TOSHIBA MACHINE IS-80G injection molding machine
- the polylactic acid resin was cooled for 20 seconds at a cylinder temperature of 190 ° C., an injection pressure of 100 MPa, an injection time of 10 seconds, and a mold temperature of 30 ° C.
- the cylinder temperature was 190 ° C
- the injection pressure was 100MPa
- the injection time was 15 seconds
- the mold temperature was 100 ° C
- the cooling was performed for 60 seconds.
- test piece was obtained by the same molding method as in (3).
- test pieces were obtained by the same molding method as in (3).
- test pieces were obtained by the same molding method as in (3).
- the bending strength test piece obtained in (6) was treated for 800 hours in an environment of a temperature of 60 ° C and a humidity of 95% RH, and then the bending strength was measured. .
- molding is carried out using an injection molding machine (Toshiba Machine Co., IS-80G) at a cylinder temperature of 220 ° C, a mold temperature of 70 ° C, and an injection pressure of lOOMPa. Flow The moving length (mm) was measured.
- the molding conditions of polylactic acid, crosslinked polylactic acid or crosslinked polylactic acid Z-polybutylene succinate resin were in accordance with (3). The larger the flow length, the better the fluidity.
- a molding test of a square plate was performed (a square is a film gate, and a mold having a thickness of 60. Omm x 60.0 mm x a thickness of lmm was used).
- the molding temperature was set at 220 ° C and the mold temperature was set at 70 ° C.
- Injection speed ⁇ Injection pressure was set so that the molding shrinkage was 0.2%.
- the obtained flat molded product was placed on a horizontal table with the convex side facing up, and the height was measured. The amount of warpage was evaluated as (warpage height) Z (length of flat plate diagonal) X 100 (%). If this value is 0.5% or less, it can be determined that there is no practical problem with the molded product.
- ⁇ Nozzle force of extruder The molten resin is discharged without pulsation, and the step of continuously pelletizing with a pelletizer that does not break the strand can be performed without any problem.
- Nozzle force of extruder Molten resin is discharged with pulsation, and strands are easily cut.
- the process up to pellet cutting may be interrupted.
- the appearance of the molded product was observed and classified as follows.
- cross-linked PLAZPBSJ cross-linked polylactic acid Z-polybutylene succinate resin
- PCZABS Sumitomo Dow IM-6100
- EGMA-gf-PMMA MODIPER A4200 manufactured by NOF Corporation
- Each raw material was supplied to a twin-screw extruder (TEM-37BS, manufactured by Toshiba Machine Co., Ltd.) at the ratios shown in Tables 1, 3, and 4, where it was melt-kneaded at a processing temperature of 220 ° C to 240 ° C and extruded.
- the resin was cut into pellets to obtain a resin composition A-HH. All the raw materials were supplied at the same time from the top feed port, except that the raw material was supplied by side feed when the carbodiimide compound was added.
- Each raw material is supplied to a twin-screw extruder (TEM-37BS, manufactured by Toshiba Machine Co., Ltd.) at the ratios shown in Table 2-4, melt-kneaded at a processing temperature of 210 ° C-230 ° C, and extruded. Was cut into pellets to obtain a resin composition II-1UU.
- the nozzle resin was also discharged while the molten resin was pulsating, and it was difficult to perform pellet siding.
- the resin raw material was directly used for injection molding for preparing various test pieces.
- Tables 14 to 14 summarize the results of the evaluation of various physical properties.
- PLA has almost no improvement in IZOD impact strength when crosslinked by itself (Comparative Examples 6 and 7). Melt kneading of uncrosslinked PLA and PC results in poor operability. On the other hand, when the PLA is cross-linked and further melt-kneaded with PC, the operability is improved, and at the same time, the IZOD impact strength is significantly improved (comparison between Example 1 and Comparative Example 1). [0088] By blending the ABS component, the fluidity is improved, the amount of warpage is reduced, and the appearance is improved. The DTUL and IZOD impact strengths are also better than the PLA alone component (Examples 3-7, 10, 11).
- the IZOD impact strength is improved (Examples 13 to 24).
- the effect of improving the impact strength is observed in various silicone conjugates (Examples 13 to 17).
- Such an effect is small in Comparative Example 8 in which the PLA is not crosslinked and Comparative Example 9 in which the amount of the crosslinked PLA is out of the range of the present invention.
- Carposimidized conjugates having an isocyanate group are useful for improving heat and moisture resistance.
- Comparative Examples 2 and 4 are obtained by adding a carbodiimide conjugate to the composition of Comparative Example 1, and the operability of melt kneading is improved as compared with Comparative Example 1, but PLA is crosslinked. ,, for
- the IZOD impact strength is low and impractical.
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| JP2005281424A (ja) * | 2004-03-29 | 2005-10-13 | Unitika Ltd | ブロック共重合体、その製造方法、および樹脂組成物 |
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- 2005-02-04 WO PCT/JP2005/001671 patent/WO2005075564A1/ja not_active Ceased
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| JP2002371172A (ja) * | 2001-06-14 | 2002-12-26 | Toyota Motor Corp | 乳酸系ポリマー組成物及びその製造方法 |
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| JP5300173B2 (ja) | 2013-09-25 |
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