JP2010001384A - Additive for resin, and masterbatch or resin composition containing same, and molded article - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an additive for resin to improve antistatic property, anti-fogging property, and filler dispersibility. <P>SOLUTION: The present invention is an additive for resin which is characterized in that (1) the additive used by being added to the resin contains a polyglycerine alkyl ether compound having a particular structure; (2) the additive further contains an anionic surfactant; (3) the resin is at least one selected from polyethylene, polypropylene, ethylene-vinyl acetate copolymer, vinyl chloride, and polylactic acid. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to an additive for resins excellent in antistatic properties, antifogging properties, filler dispersibility improvement and stability during processing, and a masterbatch or resin composition containing the same, and a molded article.

  Many commonly used plastics have low polarity, and are easily charged or dewed easily under normal room temperature and humidity conditions. If the plastic is charged, it may be an obstacle to the production process, dirt may be attached to the product, and printing defects may occur. In addition, when a food packaging material such as a wrap film has dew condensation, there is a problem that the film surface cannot be clouded due to dew condensation. In the film for agriculture, when dew condensation occurs, there is a problem that the transmittance of sunlight is lowered and the growth of the crop is deteriorated, or water drops fall on the crop to cause pest damage. In addition, fillers such as calcium carbonate, talc, and glass fiber are generally filled for the purpose of improving the rigidity, impact resistance, and heat resistance of the resin (plastic). These fillers are compatible with plastics. In many cases, the solubility is poor and a satisfactory effect cannot be obtained without being sufficiently dispersed in the resin, or unevenness may occur due to poor dispersion of the filler during processing, resulting in failure.

  In order to solve these problems, resin additives such as antistatic agents, antifogging agents, and dispersing agents are generally included in the resin to make the resin surface hydrophilic or to make the interface between the resin and filler compatible. Is called. As such a resin additive, a low molecular surfactant is commonly used.

Surfactants used as additives for resins are classified into anionic, cationic, nonionic, and amphoteric types when classified according to ionicity. Among these, the anionic system does not have a significant surface hydrophilizing effect. Cationic and amphoteric ones have a large surface hydrophilizing effect but have low heat resistance and are susceptible to problems such as coloring. Nonionic type also has a surface hydrophilization effect that is not so great, but due to the molecular structure, it is easy to adjust the hydrophilic / hydrophobic balance by adjusting the number of moles of hydrophilic groups added and the chain length of hydrophobic groups. Since it is easy to apply and problems such as coloring do not easily occur, it is used alone as a resin additive or in combination with an anionic or cationic one.
For the purpose of improving the heat resistance of the polyester resin, a method using a polyoxyethylene alkyl ether or a polyglycerol fatty acid ester (for example, see Patent Document 1), and a method using a polyglycerol fatty acid ester as an antistatic agent for a polyester resin (for example, Patent Document 2) is disclosed, but it is not sufficient in terms of sustainability of the effect.

As nonionic surfactants, ethylene oxide adducts of alkylamines and ethylene oxide adducts of alkylamides are used as highly effective substances, but they contain nitrogen atoms in the molecule and cause yellowing of the resin. Cheap. Also, ethylene oxide adducts such as higher alcohols, glycerin fatty acid esters, and sorbitan fatty acid esters can be used as additives for resins, but depending on the resin, sufficient effects may not be seen or the sustainability of the effects may be poor. is there. In addition, stearic acid monoglyceride is commonly used as a nonionic surfactant, but stearic acid monoglyceride is decomposed when used in combination with anionic, cationic, or nitrogen-containing nonionic surfactants, resulting in inconvenience.
JP 2007-246623 A JP 2007-126500 A

  An object of the present invention is to provide an additive for a resin that is excellent in antistatic properties, antifogging properties, improved dispersibility of fillers, and has excellent stability during processing, and a masterbatch or a resin composition containing the same, and a molded article. There is.

As a result of intensive research on the above problems, the present inventors have found that when a resin additive containing a compound having a specific structure is blended with a resin, it has an excellent surface hydrophilizing effect, The present inventors have found that the resin additive has excellent characteristics in stability and processability, and have completed the present invention.
That is, the present invention has the following configuration.
1. The additive for resin containing the compound represented by following formula (1) in the additive for resin used by adding to resin.
RO- (A) n-H (1)
(In the formula, R is an alkyl group having 8 to 22 carbon atoms, n is an average value of 1 to 20, and A is any one of —CH ₂ CHOHCH ₂ O— and —CH ₂ CH (CH ₂ OH) O—. Represents a group of
2. 2. The additive for resin as described in 1 above, which further contains an anionic surfactant.
3. 3. The resin additive as described in 1 or 2 above, wherein the resin is at least one selected from polyethylene, polypropylene, ethylene vinyl acetate copolymer, vinyl chloride, and polylactic acid.
4). The masterbatch characterized by containing the additive for resin in any one of said 1-3 which contains 5-20 mass% of compounds represented by Formula (1).
5). A resin composition comprising the resin additive as described in any one of 1 to 3 above, containing 0.1 to 20% by mass of the compound represented by the formula (1).
6). 6. A molded product obtained by molding the resin composition as described in 5 above.

  As is apparent from the above description, the present invention provides an additive for resins that has a high surface hydrophilizing effect, is excellent in processability and stability, has little deterioration in mechanical properties and has no degradation during processing, and can suppress coloring. A master batch or a resin composition including the molded product can be obtained.

The present invention will be described in more detail. Hereinafter, the “compound represented by the formula (1)” may be referred to as the compound of the present invention.
The compound of the present invention contained in the resin additive according to the present invention is represented by the formula (1).
RO- (A) n-H (1)
In the formula (1), R represents an alkyl group having 8 to 22 carbon atoms. The alkyl group may be linear or branched, and may be a saturated alkyl group or an unsaturated alkyl group. Examples of the alkyl group that can be used in the present invention include n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, and n-heptadecyl. N-octadecyl, behenyl, 1-methylheptyl, 1-butylhexyl, isostearyl, 2-octenyl, 4-tetradecenyl, oleyl and the like.

  In the formula (1), n is an average degree of polymerization, and although it depends on the production method of the compound represented by the formula (1), n is generally not monodispersed but a value having a distribution. n can be calculated by the following formula (2) based on the hydroxyl value.

  In formula (2), MWal represents the average molecular weight of the alkyl alcohol.

In formula (1), the number of carbon atoms of the alkyl group and the value of n are determined by the target resin of the compound of the present invention and the required performance. The compound of the present invention needs to have hydrophilicity and hydrophobicity according to the polarity of the target resin species, but the hydrophobicity increases as the carbon number of the alkyl group increases, and the hydrophilicity increases as the carbon number decreases.
And when the value of n increases, hydrophilicity increases, and when the value of n decreases, hydrophobicity increases. Further, the molecular weight determined by the sum of the carbon number of the alkyl group and the value of n is also important. When the molecular weight is small, the initial surface hydrophilicity is improved, but the sustainability with time is deteriorated. In addition, there is a demerit that the compound of the present invention easily volatilizes. When the molecular weight is large, the initial surface hydrophilicity is deteriorated, but the sustainability is improved, and the influence of a decrease in physical properties of the resin is reduced. The carbon number of the alkyl group and the value of n need to be selected in a balanced manner from these tendencies, but the alkyl group preferably has a carbon number in the range of 8 to 22, and octyl group, lauryl group, myristyl group, stearyl. Groups are preferred. The alkyl group may have a single carbon number or a mixture of a plurality of carbon atoms.
The value of n is 1 to 20 in the number average, preferably 2 to 20, and more preferably 4 to 10.

  The compound represented by formula (1) can be obtained by a known method. For example, an alkyl alcohol and 3 to 5 equivalents of glycidol with respect to the alkyl alcohol are reacted at 50 to 100 ° C. under an alkali catalyst, and unreacted alkyl alcohol and free polyglycerol are reacted at 130 to 200 ° C. under reduced pressure. Obtained by distilling off.

  In addition to the compound represented by the formula (1), the resin additive according to the present invention includes other surfactants for the purpose of exhibiting surface hydrophilization performance suitable for the resin and application. Can be contained. Examples of the surfactant include an anionic surfactant, a cationic surfactant, a nonionic surfactant, and an amphoteric surfactant. Of these, the combined use with an anionic surfactant is particularly preferable. This anionic surfactant is preferably used in the range of 1 to 50% by mass with respect to the compound represented by the formula (1). The resin additive according to the present invention may contain a known resin additive in addition to the compound of the present invention and the surfactant.

[Anionic surfactant]
Anionic surfactants include alkyl sulfates, polyoxyethylene alkyl sulfates, α-sulfo fatty acid esters, α-olefin sulfonic acids, alkyl sulfonic acids, alkyl benzene sulfonic acids, alkyl or hydroxyalkyl ether carboxylic acids, N-acyl taurines. N-acylmethyl taurine, N-acyl glycine, N-acyl aspartic acid, N-acyl sarcosine, N-acyl glutamic acid, monoalkyl phosphate ester, alkylamide ether sulfate ester, fatty acid monoglyceride sulfate ester, fatty acid polyglycerol sulfate ester, Alkyliminodicarboxylic acid, dialkylsulfosuccinic acid, alkyl glyceryl ether sulfate, alkyl polyglyceryl ether sulfate, secondary amide type N-a Examples include silamino acid salts, tartaric acid alkylamides, malic acid alkylamides, citric acid alkylamides, and salts thereof.

[Cationic surfactant]
Examples of the cationic surfactant include alkyl quaternary ammonium salts, alkyl quaternary ammonium salts having an ether group or an ester group, tetraalkylphosphonium salts or their hydrochlorides, sulfates, nitrates, and organic acid salts.

[Nonionic surfactant]
Nonionic surfactants include alkyl polyhydric alcohol ethers other than the present invention, hydroxyalkyl polyhydric alcohol ethers, higher alcohol ethoxylates, higher alcohol ethoxypropoxylates, nonylphenol ethoxylates, polyoxyethylene alkylamines, fatty acid alkanolamides, Sucrose fatty acid ester, alkyl (poly) glycoside, sorbitan fatty acid ester, glycerol fatty acid ester, polyglycerol fatty acid ester, ethoxylate of these fatty acid esters, fatty acid 2,3-dihydroxypropylamide, fatty acid polyoxyethyleneamide, alkylamine oxide , Alkylamidoamine oxide, polyoxyethylene fatty acid ester, methyl or ethyl glycoside, fatty acid ester, fat Acid, higher alcohol, polyoxyethylene, polyoxyethylene polyoxypropylene block copolymers, and the like Ashirugurukamido.

[Amphoteric surfactant]
Examples of amphoteric surfactants include trialkylcarboxymethyl betaine, sulfobetaine, amidopropyl betaine, imidazolium betaine, carboxybetaine, and phosphobetaine.

According to the purpose of the resin additive according to the present invention, the compound represented by the formula (1) and other resin additives, the compound represented by the formula (1) is 20% by mass or more, more preferably It may be used by mixing at an arbitrary ratio within the range of components (amount exceeding 50% by mass). The resin additive used in combination may be one type or a mixture of several types. Examples of the resin additives that can be used in combination include plasticizers, stabilizers, lubricants, processability improvers, antioxidants, hydrolysis inhibitors, slip agents, pigments, fillers, flame retardants, and the like. When a plurality of resin additives are used in combination, a plurality of resin additives may be mixed in advance and added to the resin, or a plurality of resin additives may be separately added during resin molding. It may be added to and mixed.

  The additive for resin according to the present invention is added to the resin and exhibits its effect. As resin (target resin) to which the additive for resin according to the present invention can be applied, any resin can be used without any particular limitation. Examples of the target resin include polyethylene, polypropylene, polystyrene, AS resin, ABS resin, polymethyl methacrylate, polyvinyl acetate, polyvinyl chloride, polyvinylidene chloride, polyvinyl alcohol, polycarbonate, polyamide, polyacetal, modified polyphenylene ether, polyphenylene sulfide, Thermosetting of thermoplastic resin such as cellulose acetate, polyethylene terephthalate, polybutylene terephthalate, aliphatic polyester, phenol resin, urea resin, melamine resin, unsaturated polyester resin, diallyl phthalate resin, epoxy resin, silicon resin, polyurethane, polyimide, etc. There is a functional resin. Also, thermoplastic elastomers such as polyolefin, polyvinyl chloride, polyurethane, polyester and polyamide, natural rubber, styrene butadiene rubber, acrylonitrile butadiene rubber, ethylene propylene rubber, chloroprene rubber, isoprene rubber, butyl rubber, butadiene Synthetic rubber such as rubber can also be used. Among these, at least one selected from polyethylene, polypropylene, ethylene vinyl acetate copolymer, vinyl chloride, and polylactic acid is a preferable target resin.

The resin composition in the present invention can be subjected to thermoforming such as extrusion, injection, compression, and blow using an extruder, an injection molding machine, a calendar molding machine, a compression molding machine, a blow molding machine, etc. that are used for molding ordinary plastics. It is. The resin and the resin additive may be added separately and kneaded in a molding machine, or may be mixed in advance. In the case of polymer blending, a twin screw extruder is preferred. However, depending on the type of processing machine, when the additive amount of the resin additive is high, the resin bite may be poor and cannot be processed, or even if processed, it may not be kneaded sufficiently, resulting in poor dispersion. For this reason, a master batch containing a resin additive in a high concentration with respect to the resin in advance is prepared by a twin screw extruder or a Banbury mixer, and this is mixed with the resin so as to have a predetermined resin additive concentration. It is preferable to mold. In this case, the concentration of the resin additive in the master batch is preferably such that the amount of the compound represented by the formula (1) in the master batch is 5% by mass or more and 20% by mass or less.
For the production of the master batch according to the present invention, a conventionally known technique can be employed without any particular limitation.

  Further, when the resin additive according to the present invention is used together with a filler and mainly used for improving the dispersibility of the filler, it is preferable that the resin additive is adsorbed on the filler in advance and then kneaded with the resin. For example, the resin additive can be adsorbed to the filler by spraying and sprinkling the melted resin additive while stirring the filler using a ribbon blender. In this case, the use amount of the resin additive according to the present invention relative to the filler is preferably 1% to 100% by mass ratio.

  Examples of the filler that can be used include calcium carbonate, magnesium carbonate, silica, calcium silicate, carbon black, carbon fiber, glass fiber, metal fiber, titanium oxide, clay, mica, talc, magnesium hydroxide, and aluminum hydroxide. Zinc oxide, various organic fibers, wood flour, walnut shell flour, jute, kenaf, cellulose, lignin and the like.

  In the resin composition of the present invention, the amount of the resin additive added to the resin is preferably such that the amount of the compound represented by the formula (1) in the resin composition is 0.1 to 20% by mass, particularly 0. An amount of 1 to 5% by mass is preferable. When the amount of the additive for the resin is less than the range, sufficient surface hydrophilizing effect and dispersibility improvement effect cannot be obtained, and when it is more than the range, the transparency and mechanical properties of the resin are lowered, Bleed out from the resin.

  The resin composition of the present invention can be formed into a sheet or film by T-die, inflation, calender and the like. The film may be either stretched or unstretched. In addition, a molded product can be obtained using an injection molding machine, a compression molding machine or the like. For example, a bottle or the like can be formed by blow molding.

  Hereinafter, the present invention will be described in detail with reference to examples, but the embodiment of the present invention is not limited thereto.

Production Example 1 [polyglycerol monolauryl ether]
Sodium hydroxide (5.746 g, 0.144 mol) was used as a catalyst for 175 g (0.9392 mol) of lauryl alcohol and 200 g (2.700 mol) of glycidol. In the reaction, lauryl alcohol and sodium hydroxide were reacted to form an alkoxide, 200 ml of toluene was added, and glycidol was added dropwise at a reaction temperature of 90 ° C. at a rate of about 0.8 ml / min. After completion of dropping, the mixture was further aged at 90 ° C. for 6 hours. The reaction was carried out under an inert gas atmosphere. After completion of the reaction, the catalyst was neutralized with an equivalent amount of phosphoric acid, the polyglycerol separated from the neutralized salt was filtered off, and toluene was distilled off to obtain 370 g of crude polyglycerol monolauryl ether. Further, unreacted lauryl alcohol was distilled off by distillation under reduced pressure (0.92 kPa, 150 to 180 ° C., 14.5% cut in charge) to obtain 314 g of polyglycerol monolauryl ether [compound (1)]. The hydroxyl value of this compound (1) was 589.2 mgKOH / ml, and the average degree of polymerization determined from the hydroxyl value was 4.3.

Production Example 2 [Glycerol monolauryl ether]
5000 g of the compound (1) produced above was distilled three times at 0.4 ° C., 100 ° C., 110 ° C., and 120 ° C. using a molecular distillation machine (manufactured by ULVAC, CEH-300II). By distillation at 120 ° C., 267 g of glycerol monolauryl ether [compound (2)] was obtained. The hydroxyl value of this compound (2) was 431.3, and the average degree of polymerization determined from the hydroxyl value was 1.0.

Production Example 3 [polyglycerol monoisostearyl ether]
Sodium hydroxide (5.71 g, 0.143 mol) was used as a catalyst for isostearyl alcohol (250 g, 0.925 mol) and glycidol (200 g, 2.700 mol). In the reaction, isostearyl alcohol and sodium hydroxide were reacted to form an alkoxide, 200 ml of toluene was added, and glycidol was added dropwise at a reaction temperature of 90 ° C. at a rate of about 0.8 ml / min. After completion of dropping, the mixture was further aged at 90 ° C. for 6 hours. The reaction was carried out under an inert gas atmosphere. After completion of the reaction, the catalyst was neutralized with an equivalent amount of phosphoric acid, and the polyglycerol separated from the neutralized salt was filtered off, and toluene was distilled off to obtain 436 g of crude polyglycerol monoisostearyl ether. Further, unreacted isostearyl alcohol was distilled off under reduced pressure (0.9 kPa, 160 to 200 ° C., charged to 13.8% cut) to obtain 376 g of polyglycerol monoisostearyl ether [compound (3)]. The hydroxyl value of this compound (3) was 511.2 mgKOH / ml, and the average degree of polymerization determined from the hydroxyl value was 4.5.

Production Example 4 [polyglycerol monohexadecyl ether]
Sodium hydroxide 5.99 g (0.150 mol) was used as a catalyst for 250 g (1.032 mol) of hexadecyl alcohol and 200 g (2.700 mol) of glycidol. In the reaction, hexadecyl alcohol and sodium hydroxide were reacted to form an alkoxide, 200 ml of toluene was added, and glycidol was added dropwise at a reaction temperature of 90 ° C. at a rate of about 0.8 ml / min. After completion of dropping, the mixture was further aged at 90 ° C. for 6 hours. The reaction was carried out under an inert gas atmosphere. After completion of the reaction, the catalyst was neutralized with an equivalent amount of phosphoric acid, and the polyglycerol separated from the neutralized salt was filtered off, and toluene was distilled off to obtain 432 g of crude polyglycerol monohexadecyl ether. Further, unreacted hexadecyl alcohol was distilled off by distillation under reduced pressure (0.9 kPa, 160 to 200 ° C., charge 15.2% cut) to obtain 366 g of polyglycerol monohexadecyl ether [compound (4)]. The hydroxyl value of this compound (4) was 499.6 mgKOH / ml, and the average degree of polymerization determined from the hydroxyl value was 3.4.

Resin (1): Polyethylene (Novatech LD LF440HB: manufactured by Nippon Polyethylene)
Resin (2): Polypropylene (Novatech PP BC03C: manufactured by Nippon Polypro Co., Ltd.)
Resin (3): Polylactic acid (Lacia H-100, manufactured by Mitsui Chemicals)
Resin (4): Polyvinyl chloride (TH700: manufactured by Taiyo PVC Co.)
Resin (5): Polyethylene vinyl acetate copolymer (NUC3758: manufactured by Nihon Unicar)

The test method is as follows.
[Test-1] Antistatic property A test piece having a size of 100 × 100 mm and a thickness of 2 mm was used. The surface resistivity of a test piece aged at room temperature of 20 ° C. and humidity of 65% RH for 1 week was measured with a super insulation meter SEM-10 (manufactured by Toa Denpa Kogyo Co., Ltd.) under the same conditions. The applied voltage was 500 V and the value after 1 minute was read. The surface specific resistance of the resin is usually 10 ¹⁶ Ω or more, but when the resin additive is added, it decreases to about 10 ⁹ to 10 ¹⁴ Ω. The lower the resistance value, the better the antistatic property.

[Test-2] Antifogging test film having a size of 100 × 100 mm and a thickness of 50 μm was used. A test film was aged at room temperature of 20 ° C. and a humidity of 65% RH for 1 week after molding, and was subjected to the test. 200 ml of room temperature distilled water was put into a 300 ml beaker, and a test film was placed on the beaker so as to adhere. A beaker filled with water and covered with a film was placed in a refrigerator at 5 ° C., and water droplets adhering to the film were observed. The case where the film after 1 hour was put in the refrigerator was cloudy was rated as x, and the case where the content of the beaker was clearly visible without being clouded was marked as ◯.

[Test-3] Vicat softening point measurement test A test piece of 25 × 20 mm and a thickness of 2 mm was used. The Vicat softening point (JIS K7206) was measured by HDT TESTER manufactured by Toyo Seiki Co., Ltd. The load is 50 N, and the heating rate is 50 ° C./h.

Examples 1-10, Comparative Examples 1-3
Comparison of antistatic properties of resins (1) to (3) Resin and the compound of the present invention were mixed in the formulation shown in Table 1, and melt-kneaded at 180 ° C. for 15 minutes in a laboratory plast mill (manufactured by Toyo Seiki Co., Ltd.). It was pressed at 180 ° C. with a machine and formed into a 2 mm thick plate. A test piece was cut out to 100 × 100 mm and subjected to Test-1. The results are shown in Table 1.

Example 11, Comparative Example 4
Comparison of antistatic property of resin (4) The mixture shown in Table 2 was mixed at 120 ° C. for 5 minutes with a Henschel mixer. Subsequently, the mixture was melt-kneaded at 170 ° C. for 10 minutes with a Laboplast mill (manufactured by Toyo Seiki Co., Ltd.) and pressed at 170 ° C. with a small press to form a 2 mm thick plate. A test piece was cut out to 100 × 100 mm and subjected to Test-1. The results are shown in Table 2.

Note 1: Epoxidized soybean oil; Daicel Chemical Industries Epoxidized soybean oil Note 2: Tin-based stabilizer; Nitto Kasei Co., Ltd. # 8831

Example 12, Comparative Example 5
Comparison of anti-fogging property of resin (5) The flow rate was adjusted so that the compound (1) was 10% by mass with respect to 90% by mass of the resin (5), and the resin was rotated 190 by a small-sized bi-directional extruder equipped with a strand die. The strand was melt-kneaded at 0 ° C., the strand was cooled with water and cut to prepare a master batch pellet. The produced master batch pellet was dried at 80 ° C. for 12 hours. Then, it mixed by the mixing | blending shown in Table 3, and shape | molded in the 50-micrometer-thick film at 180 degreeC with the inflation molding machine. The formed film was subjected to Test-2. The results are shown in Table 3.

Examples 13-15, Comparative Examples 6, 7
Comparison of antistatic properties when used in combination with an anionic surfactant Mixtures shown in Table 4 were mixed, melt-kneaded at 190 ° C by a small-sized bi-directional extruder equipped with a strand die, and the strands were cooled with water. Cutting and making pellets. The prepared pellets were dried at 100 ° C. for 5 hours. Subsequently, the pellets were molded into a plate shape of 10 × 10 × 2 mm at 190 ° C. with an injection molding machine and subjected to Test-1. The results are shown in Table 4. In addition, the same effect was seen not only about the anionic surfactant shown in Note 3, but about all the exemplary compounds of said [anionic surfactant].

  Note 3: Anionic surfactant: Matsumoto Yushi Co., Ltd. TB-160 (sodium alkyl sulfonate)

Examples 16-18, Comparative Example 8
Comparison of Dispersibility of Filler 100 g of the compound of the present invention shown in Table 5 was added to 100 g of talc (Hytron A, manufactured by Takehara Chemical Co., Ltd.), and the mixture was adsorbed by stirring at 100 ° C. for 10 minutes with a Henschel mixer. The resin, the compound of the present invention, and the talc adsorbed with the compound of the present invention are mixed so that the ratio of talc is as shown in Table 5 and the resin is mixed. The strand was melt-kneaded and cut by water cooling to produce pellets. The prepared pellets were dried at 100 ° C. for 5 hours. Subsequently, the pellet was molded into a test piece having a thickness of 2 mm at 190 ° C., a mold temperature of 105 ° C., and a cooling time of 60 seconds using an injection molding machine. The results are shown in Table 5.

From Table 5, it can be seen that heat resistance is improved by adding talc to the resin, but talc does not have sufficient dispersibility in the resin. On the other hand, by adsorbing the compound of the present invention to talc, It can be seen that the dispersibility of the resin composition is improved and the heat resistance of the resin composition is improved.

Claims (6)

The additive for resin containing the compound represented by following formula (1) in the additive for resin used by adding to resin.
RO- (A) n-H (1)
(In the formula, R is an alkyl group having 8 to 22 carbon atoms, n is an average value of 1 to 20, and A is any one of —CH ₂ CHOHCH ₂ O— and —CH ₂ CH (CH ₂ OH) O—. Represents a group of The additive for resin according to claim 1, further comprising an anionic surfactant. The resin additive according to claim 1 or 2, wherein the resin is at least one selected from polyethylene, polypropylene, ethylene vinyl acetate copolymer, vinyl chloride, and polylactic acid. A masterbatch comprising the resin additive according to any one of claims 1 to 3, comprising 5 to 20% by mass of the compound represented by the formula (1). The resin composition containing the additive for resin in any one of Claims 1-3 containing 0.1-20 mass% of compounds represented by Formula (1). A molded product obtained by molding the resin composition according to claim 5.