JP5208818B2 - SOUND ABSORBING MODIFIED POLYSTYRENE RESIN FOAM MOLDED BODY AND PROCESS FOR PRODUCING THE SAME - Google Patents

Description

  The present invention relates to a modified polystyrene resin foam molded article having sound absorbing performance. The sound-absorbing modified polystyrene resin foam molded article of the present invention is used for automobile members, building materials and the like.

Conventionally, a foam is used as a sound absorbing material by forming a void in the foam. As a modified polystyrene resin foamed molded article having such voids, Patent Document 1 discloses that styrene-modified polyolefin resin foam pieces are heat-foamed and thermally fused together, and 10 to 40 between the pieces. A styrene-modified polyolefin resin foam molded article having a% void is disclosed.
However, in order to form a porosity of 10 to 40% in the foamed molded product, it is necessary to suppress secondary foaming of the pre-foamed particles during molding, and the steam temperature during molding is reduced or the heating time is shortened. There is a need to. As a result, the foaming pressure of the foam pieces is lowered, the thermal fusion between the foam pieces is lowered, and the mechanical strength of the obtained foamed molded product tends to be lowered.

Moreover, in patent document 2, the absorbance ratio in 698cm < ^-1 > and 1376cm < ^-1 > obtained from the infrared absorption spectrum of the particle | grain surface measured by ATR method infrared spectroscopy is the range of 0.1-2.5. It is obtained by foam-molding styrene-modified polyolefin resin pre-expanded particles containing 100 to 400 parts by mass of a styrene resin component with respect to 100 parts by mass of the polyolefin resin component, and has a porosity of 5 to 50%. Foam molded bodies have been proposed.
However, as with the foamed molded product of Patent Document 1, this foamed product also has a problem that the heat-fusible properties between the pre-foamed grains are low, and the resulting foamed molded product tends to have low mechanical strength. .

Japanese Patent Laid-Open No. 7-80873 JP 2008-239793 A

  The sound-absorbing modified polystyrene resin foam molded article obtained by the conventional methods disclosed in Patent Documents 1 and 2 is capable of heat-sealing foam pieces while suppressing secondary foaming of pre-foamed particles during molding. Although it was difficult to mention and had sufficient voids, the mechanical strength of the foamed molded product was likely to be low.

  The present invention has been made in view of the above circumstances, exhibits excellent heat-fusibility in in-mold foam molding, has excellent mechanical strength, particularly crack resistance and impact resistance, and has a large number of void portions. An object of the present invention is to provide a sound-absorbing modified polystyrene resin foam molded article having excellent sound-absorbing properties.

In order to achieve the above object, the present invention provides a polystyrene resin in an amount of 100 parts by mass or more with respect to 100 parts by mass of a propylene resin having a propylene-ethylene copolymer and a melting start temperature in the range of 60 to 100 ° C. The ratio between the absorbance D698 at 698 cm ^{−1 and} the absorbance D1376 at 1376 cm ⁻¹ obtained from the infrared absorption spectrum of the particle surface containing less than 400 parts by mass and measured by ATR infrared spectroscopy (D698 / D1376) In the range of 0.166 to 0.20 g / cm ³ , the modified polystyrene resin particles having a bulk density of 0.0166 to 0.20 g / cm ³ are impregnated with a hydrocarbon-based foaming agent and pre-foamed. The amount of the remaining foaming agent is 0.0 to 3.0% by mass by forcibly reducing the foaming agent remaining in the prefoamed particle. And foams remove the foamed particles and then performing mold foaming a blowing agent removal expanded particles,
(A) a density in the range of 0.0166 to 0.20 g / cm ³ ;
(B) the porosity is in the range of 10 to 30%,
(C) The bending break point displacement measured according to the method described in JIS K7221-2: 1999 is 10 mm or more,
(D) According to ASTM E1050, when the normal incident sound absorption coefficient is measured at a thickness of 30 mm, there is a portion having a sound absorption coefficient of 0.5 or more in the range of 500 Hz to 6000 Hz,
A method for producing a sound-absorbing modified polystyrene resin foam molded article, characterized in that a sound-absorbing modified polystyrene resin foam molded article satisfying the above conditions is obtained.

In the production method of the present invention, the modified polystyrene resin particles are:
(A) A step of dispersing 100 parts by mass of polypropylene resin particles, 100 parts by mass or more and less than 400 parts by mass of a styrene monomer, and a polymerization initiator in an aqueous suspension containing a dispersant,
(B) heating the obtained dispersion to a temperature at which the styrenic monomer is not substantially polymerized to impregnate the polypropylene resin particles with the styrenic monomer;
(C) When the melting point of the polypropylene resin particles is T ° C., the step of performing the first polymerization of the styrene monomer at a temperature of (T−10) ° C. to (T + 20) ° C.,
(D) Subsequent to the first polymerization step, a styrene monomer and a polymerization initiator are added, and when the melting point of the polypropylene resin particles is T ° C, (T-25) ° C to By setting the temperature to (T + 10) ° C., the polypropylene resin particles are preferably manufactured through the step of impregnating the polypropylene resin particles with the styrene monomer and performing the second polymerization.

  In the production method of the present invention, the hydrocarbon-based blowing agent may be one or more selected from the group consisting of propane, n-butane, i-butane, n-pentane, i-pentane, and cyclopentane. preferable.

In the production method of the present invention, the step of forcibly reducing the foaming agent remaining in the pre-expanded particles,
(i) A treatment method in which pre-expanded particles are placed in a gas-permeable container and hot-air drying at 50 to 80 ° C. is performed for several hours to several days
(ii) It is preferably one of the treatment methods in which the pre-foamed particles are placed in a breathable container and allowed to stand at room temperature until the amount of the remaining foaming agent is 0.0 to 3.0% by mass.

  In the production method of the present invention, the amount of the remaining foaming agent in the foaming agent-removed foamed particles is preferably in the range of 0.0 to 3.0% by mass.

  The present invention also provides a sound-absorbing modified polystyrene resin foam molded article obtained by the above-described method for producing a sound-absorbing modified polystyrene resin foam molded article.

  In the sound-absorbing modified polystyrene-based resin foam molded article of the present invention, the heating dimensional change rate at 80 ° C. measured by B method of JIS K6767: 1999K is preferably less than 1.5%.

According to the present invention, a foamed molded article that exhibits excellent heat-fusibility in in-mold foam molding, has excellent mechanical strength, in particular, crack resistance and impact resistance, and has a large number of void portions. It is possible to provide a sound-absorbing modified polystyrene resin foam molding that can be obtained.
Furthermore, since the obtained foamed molded article is a foamed molded article that has low combustibility due to a small amount of residual foaming agent gas and is difficult to undergo tertiary foaming. It is possible to provide a sound-absorbing modified polystyrene-based resin foam molded article that is easy to increase the crystallinity of the nucleus and has excellent heat shrinkage resistance.

The method for producing a sound-absorbing modified polystyrene resin foam molded article of the present invention is based on 100 parts by mass of a propylene resin having a propylene-ethylene copolymer and a melting start temperature in the range of 60 to 100 ° C. Absorbance D698 at 698 cm ⁻¹ and Absorbance D1376 at 1376 cm ⁻¹ obtained from the infrared absorption spectrum of the particle surface containing 100 parts by mass or more and less than 400 parts by mass of the resin based on ATR method The modified polystyrene resin particles having a ratio (D698 / D1376) in the range of 0.1 to 2.5 are impregnated with a hydrocarbon foaming agent and then pre-foamed so that the bulk density is 0.0166 to 0. and pre-expanded particles is in the range of .20g / cm ^3, forcibly reduce foaming agent remaining in the pre-expanded particles, the residual blowing agent weight ( Lower, referred to as the residual gas amount) is a foaming agent removing foamed particles is 0.0 to 3.0 wt%, then under mold foaming a blowing agent removal expanded particles,
(A) a density in the range of 0.0166 to 0.20 g / cm ³ ;
(B) the porosity is in the range of 10 to 30%,
(C) The bending break point displacement measured according to the method described in JIS K7221-2: 1999 is 10 mm or more,
(D) According to ASTM E1050, when the normal incident sound absorption coefficient is measured at a thickness of 30 mm, there is a portion having a sound absorption coefficient of 0.5 or more in the range of 500 Hz to 6000 Hz,
It is characterized by obtaining a sound-absorbing modified polystyrene-based resin foam molded article that satisfies the above conditions.

In the production method of the present invention, a particularly noteworthy point is that the residual gas amount of the pre-expanded particles is forcibly reduced to obtain foaming agent-removed expanded particles having a residual gas amount of 0.0 to 3.0% by mass. The foaming agent-removed foamed particles were produced and subjected to in-mold foam molding to maintain a bending break point displacement of 10 mm or more according to the method described in JIS K7221-2: 1999, while maintaining 10-30% This is to obtain a modified polystyrene-based resin foam molded article having a porosity.
Further, by reducing the residual gas amount of the pre-expanded particles, the residual gas amount of the foam molded product obtained by in-mold foam molding is also reduced, so that the molded product has low combustibility and hardly undergoes tertiary foaming. I also understood that. In addition, by reducing the residual gas amount of the pre-expanded particles, the secondary foamability during in-mold foam molding can be suppressed, and since the heating is performed at a higher temperature for a longer time, the crystallinity of the polypropylene core increases. It was also found that the heat shrinkage of the obtained molded body was reduced.

  The polypropylene resin, which is one of the resin materials of the sound-absorbing modified polystyrene resin foam molded article of the present invention, contains a propylene-ethylene copolymer, has two endothermic peaks in the DSC curve, and has a melting point peak. In addition, it is preferable that the melting start temperature has an endothermic peak in the range of 60 to 100 ° C. When there is an endothermic peak in the range of 60 to 100 ° C., the mechanical strength (particularly bending strength and bending break point displacement) of the obtained foamed molded product tends to be high. On the other hand, when there is no endothermic peak in the range of 60 to 100 ° C., the mechanical strength (particularly, bending strength and bending break point displacement) of the obtained foamed molded product is lowered. This propylene-ethylene copolymer is mainly composed of a copolymer of ethylene and propylene, but may contain ethylene or another monomer that can be copolymerized with propylene in the molecule. Good. Examples of such a monomer include one or more selected from α-olefins, cyclic olefins, and diene monomers.

The polypropylene-based resin may contain additives such as a flame retardant, a flame retardant aid, an antioxidant, an ultraviolet absorber, a pigment, and a colorant as necessary.
The colorant may be an inorganic pigment or an organic pigment.
Examples of inorganic pigments include chromates such as chrome yellow, zinc yellow and barium yellow, ferrocyanides such as bitumen, sulfides such as cadmium yellow and cadmium red, oxides such as iron black and red husk, and ultramarine blue. And silicates such as titanium oxide.
Examples of organic pigments include azo pigments such as monoazo pigments, disazo pigments, azo lakes, condensed azo pigments, chelate azo pigments, phthalocyanine-based, anthraquinone-based, perylene-based, perinone-based, thioindigo-based, quinacridone-based, and dioxazine-based pigments. And polycyclic pigments such as isoindolinone and quinophthalone.

  Examples of the polystyrene resin that is another resin material of the sound-absorbing modified polystyrene resin foam molded article of the present invention include styrene resins such as styrene, α-methylstyrene, p-methylstyrene, and t-butylstyrene. Examples thereof include resins obtained by polymerizing monomers. Furthermore, the polystyrene resin may be a copolymer of a styrene monomer and another monomer copolymerizable with the styrene monomer. Examples of other monomers include polyfunctional monomers such as divinylbenzene, and (meth) acrylic acid alkyl esters that do not contain a benzene ring in the structure such as butyl (meth) acrylate. . You may use these other monomers in the range which does not exceed 5 mass% substantially with respect to a polystyrene-type resin. In the present specification, styrene and a monomer copolymerizable with styrene are also referred to as a styrene monomer.

  The resin composition of the sound-absorbing modified polystyrene resin foam molded article of the present invention is in a range of 100 parts by mass or more and less than 400 parts by mass of polystyrene resin with respect to 100 parts by mass of the polypropylene resin. When the polystyrene-based resin component is less than 100 parts by mass, the polypropylene-based resin component is increased, and when the gel fraction is reached, the foamed molded product according to the claims cannot be obtained. When the polystyrene resin component exceeds 400 parts by mass, the polystyrene resin component increases, secondary foaming is likely to occur during in-mold foam molding, and only a foam molded article having a low porosity and low sound absorption can be obtained.

In the production method of the present invention, the modified polystyrene resin particles have an absorbance D698 at 698 cm ^{−1 and} an absorbance D1376 at 1376 cm ⁻¹ obtained from the infrared absorption spectrum of the particle surface measured by ATR infrared spectroscopy. The ratio (D698 / D1376) is in the range of 0.1 to 2.5, and more preferably in the range of 0.2 to 2.0. The particle surface includes a region having a depth of several μm from the surface.
When this absorbance ratio is higher than 2.5, the ratio of the polypropylene resin on the surface of the resin particles is lowered, and as a result, the chemical resistance and impact resistance of the foamed molded product obtained by pre-foaming and molding are reduced. Is unfavorable because it decreases. Further, when the absorbance ratio is lower than 0.1, the foaming agent dissipates significantly from the surface of the pre-foamed particles, so that the finished appearance of the foam molded product due to shrinkage or the like is deteriorated in the in-mold foam molding. Therefore, it is not preferable.

  Here, the ATR (Attenuated Total Reflectance) method infrared spectroscopic analysis in the present invention is an analysis method for measuring an infrared absorption spectrum by a single reflection type ATR method using total reflection absorption (Attenuated Total Reflectance). This analysis method is a method in which an ATR prism having a high refractive index is closely attached to a sample, infrared light is irradiated to the sample through the ATR prism, and the reflected light from the ATR prism is spectrally analyzed.

  ATR infrared spectroscopic analysis is not limited to organic materials such as polymer materials because the spectrum can be measured simply by bringing the sample into close contact with the ATR prism and surface analysis up to a depth of several μm is possible. It is widely used for surface analysis of various substances.

In addition, the light absorbency D698 in 698cm < ^-1 > obtained from an infrared absorption spectrum says the height of the peak which appears in 698 cm < ^-1 > vicinity derived from the out-of-plane bending vibration of the benzene ring mainly contained in a polystyrene-type resin.

In addition, the absorbance D1376 at 1376 cm ⁻¹ obtained from the infrared absorption spectrum is a high peak appearing in the vicinity of 1376 cm ⁻¹ derived from the symmetrical bending vibration of CH ₃ of —C—CH ₃ hydrocarbon contained in the polypropylene resin. Say it.

As a method for obtaining the composition ratio of polystyrene resin and polypropylene resin from the absorbance ratio, a plurality of types of standard samples are prepared by uniformly mixing polystyrene resin and polypropylene resin at a predetermined composition ratio, and each standard is prepared. A sample is subjected to particle surface analysis by ATR infrared spectroscopy to obtain an infrared absorption spectrum. The absorbance ratio is calculated from each of the obtained infrared absorption spectra. A calibration curve is drawn by taking the composition ratio (polystyrene resin ratio (% by mass) in the standard sample) on the vertical axis and the absorbance ratio (D698 / D1376) on the horizontal axis. Based on the calibration curve, the composition ratio of the polystyrene resin and the polypropylene resin in the modified polystyrene resin particles can be determined from the absorbance ratio of the modified polystyrene resin particles.
The preparation of the calibration curve is conventionally known as described in paragraphs [0040] to [0043] of FIG. 1 and Japanese Patent Laid-Open No. 2008-239793 and FIG.

Further, the modified polystyrene resin particles is calculated from the absorbance ratio at 698cm ^-1 and 1376cm ^-1 obtained from an infrared absorption spectrum of the particles heart measured by ATR method infrared spectroscopy (D698 / D1376) The polystyrene resin ratio in the center of the particle is preferably 1.2 times or more, more preferably 1.35 times or more, and still more preferably 1.4 times or more with respect to the polystyrene resin ratio of the entire particle.
Here, the “particle central part” is a part in a cross section passing through the center of the particle, ranging from the center of the particle to 1/4 of the diameter (particle diameter) of the particle. The particle central portion of a spherical particle having a diameter of 1 mm is a portion having a radius of 125 μm from the center of the particle.

  When the calculated polystyrene resin ratio in the center of the particle is 1.2 times or less than the polystyrene resin ratio of the whole particle, the gradient of the gradient of the polystyrene resin ratio decreases from the surface layer to the inside. As a result, the expansion ratio and heat resistance of the foamed molded product obtained by foaming the pre-expanded particles are unfavorable.

The modified polystyrene resin particles used in the production method of the present invention can be produced efficiently and with a high yield by the production method including the following steps (A) to (D).
(A) A step of dispersing 100 parts by mass of polypropylene resin particles, 100 parts by mass or more and less than 400 parts by mass of a styrene monomer, and a polymerization initiator in an aqueous suspension containing a dispersant,
(B) heating the obtained dispersion to a temperature at which the styrenic monomer is not substantially polymerized to impregnate the polypropylene resin particles with the styrenic monomer;
(C) When the melting point of the polypropylene resin particles is T ° C., the step of performing the first polymerization of the styrene monomer at a temperature of (T−10) ° C. to (T + 20) ° C.,
(D) Subsequent to the first polymerization step, a styrene monomer and a polymerization initiator are added, and when the melting point of the polypropylene resin particles is T ° C, (T-25) ° C to (T + 10) A step of impregnating the polypropylene resin particles with the styrene monomer and performing a second polymerization by setting the temperature to (T + 10) ° C.
In addition, each process of (A)-(D) is a well-known polymerization method such as a suspension polymerization method or a seed polymerization method of a polystyrene resin for producing beaded polystyrene resin particles using a styrene monomer as a raw material. Although it can implement using the autoclave polymerization apparatus etc. which are used when implementing a method, the manufacturing apparatus to be used is not limited to this.

In the step (A), the polypropylene resin particles are obtained by, for example, melting the polypropylene resin with an extruder and granulating it by strand cutting, underwater cutting, hot cutting, etc., or by directly using a pulverizer. It is obtained by grinding and pelletizing the particles. In addition, examples of the shape include a true spherical shape, an elliptical spherical shape (egg shape), a cylindrical shape, and a prismatic shape. The preferred resin particle size of the polypropylene resin particles is in the range of 0.5 mm to 1.5 mm, more preferably in the range of 0.6 mm to 1.0 mm.
Moreover, in the said (A) process, as a polypropylene resin, what has melting | fusing point is 120 to 145 degreeC is suitable.

  Examples of the dispersant used in the step (A) include organic dispersants such as partially saponified polyvinyl alcohol, polyacrylate, polyvinyl pyrrolidone, carboxymethyl cellulose, and methyl cellulose, magnesium pyrophosphate, calcium pyrophosphate, calcium phosphate, and carbonic acid. Examples thereof include inorganic dispersants such as calcium, magnesium phosphate, magnesium carbonate, and magnesium oxide. Of these, inorganic dispersants are preferred. When using an inorganic dispersant, it is preferable to use a surfactant in combination. Examples of such a surfactant include sodium dodecylbenzene sulfonate and α-olefin sulfonic acid sodium.

  Moreover, as a polymerization initiator, the conventionally well-known polymerization initiator currently used widely for superposition | polymerization of a styrene-type monomer can be used. For example, benzoyl peroxide, lauroyl peroxide, t-amyl peroxy octoate, t-butyl peroxybenzoate, t-amyl peroxybenzoate, t-butyl peroxybivalate, t-butyl peroxyisopropyl carbonate, t- Butyl peroxyacetate, t-butylperoxy-3,3,5-trimethylcyclohexanoate, di-t-butylperoxyhexahydroterephthalate, 2,2-di-t-butylperoxybutane, dicumyl peroxide And azo compounds such as azobisisobutyronitrile and azobisdimethylvaleronitrile. In addition, a polymerization initiator may be used independently or may be used together.

  Moreover, when adding a crosslinking agent, the addition method is, for example, a method of adding a crosslinking agent directly to a polypropylene resin, or adding a crosslinking agent dissolved in a solvent, a plasticizer or a styrene monomer. And a method in which a crosslinking agent is dispersed in water and then added. Among these, a method of adding a crosslinking agent after dissolving it in a styrene monomer is preferable.

  The styrene monomer can be continuously or intermittently added to the aqueous medium in order to impregnate the polypropylene resin particles. The styrenic monomer is preferably added gradually to the aqueous medium. Examples of the aqueous medium include water and a mixed medium of water and a water-soluble medium (for example, alcohol).

In the step (B), the dispersion obtained in the step (A) is heated to a temperature at which the styrene monomer is not substantially polymerized, and the polypropylene resin particles are impregnated with the styrene monomer. The temperature is in the range of 45 ° C to 70 ° C, preferably in the range of 50 ° C to 65 ° C.
When the impregnation temperature is less than the above range, the impregnation of the styrene monomer is insufficient and a polymerized polystyrene powder is generated, which is not preferable. On the other hand, if the impregnation temperature exceeds the above range, it is not preferable because the styrene monomer is polymerized before being sufficiently impregnated with the polypropylene resin particles.

In the steps (C) and (D), the polymerization temperature is an important factor. When the melting point of the polypropylene resin is T ° C., in the step (C) (first polymerization), (T-10 ) ° C. to (T + 20) ° C., and in the step (D) (second polymerization), the temperature range is (T−25) ° C. to (T + 10) ° C. By carrying out the polymerization in the temperature range, the resin particle central part has a large amount of polystyrene resin (that is, a large amount of polypropylene resin in the surface layer). As a result, the polypropylene resin and the polystyrene resin The modified polystyrene resin particles excellent in rigidity, foam moldability, chemical resistance and heat resistance can be provided by taking advantage of each of the above.
When the polymerization temperature is lower than the above temperature range, the abundance of the polystyrene-based resin is small at the center of the obtained resin particles, and resin particles and foamed molded articles exhibiting good physical properties cannot be obtained. Also, if the polymerization temperature is higher than the above temperature range, the polymerization starts before the styrene monomer is sufficiently impregnated with the polypropylene resin particles, so that resin particles and foamed molded articles having good physical properties are obtained. I can't. In addition, an expensive polymerization facility with excellent heat resistance is required.

  The reason for dividing the process of polymerizing the styrene monomer impregnated into the polypropylene resin particles into two stages of (C) process (first polymerization) and (D) process (second polymerization). This is because if a polypropylene resin is impregnated with many styrene monomers at once, the styrene monomer is not sufficiently impregnated in the polypropylene resin and remains on the surface of the polypropylene resin. Therefore, as in the method for producing the modified polystyrene resin particles according to the present invention, the styrene monomer is surely obtained in the step (C) by dividing into the two steps of the step (C) and the step (D). The styrene monomer is impregnated toward the center of the polypropylene resin in the step (D).

After performing the polymerization in the step (D), the reaction vessel is cooled, and the formed modified polystyrene resin particles are separated from the aqueous medium, whereby the polystyrene resin is added to 100 parts by mass of the polypropylene resin. The ratio of the absorbance D698 at 698 cm ^{−1 and} the absorbance D1376 at 1376 cm ⁻¹ obtained from the infrared absorption spectrum of the particle surface containing 100 parts by mass or more and less than 400 parts by mass and measured by ATR infrared spectroscopy (D698) / D1376) is obtained in the range of 0.1 to 2.5 modified polystyrene resin particles.

As described above, after the polypropylene resin particles, the styrene monomer and the polymerization initiator are dispersed in the aqueous suspension containing the dispersant, the polypropylene resin particles are impregnated with the styrene monomer. When the melting point of the polypropylene resin particles is T ° C, the first stage polymerization is carried out at a temperature of (T-10) ° C to (T + 20) ° C, and then the temperature of (T-25) ° C to (T + 10) ° C. The ratio of the absorbance D698 at 698 cm ^{−1 and} the absorbance D1376 at 1376 cm ⁻¹ obtained from the infrared absorption spectrum of the particle surface measured by ATR infrared spectroscopy by performing the second stage polymerization (D698 / The modified polystyrene resin particles having D1376) in the range of 0.1 to 2.5 can be efficiently produced with a high yield. The obtained modified polystyrene resin particles are obtained by pre-expanding expandable resin particles obtained by impregnating a foaming agent, filling the mold with a mold, and performing in-mold foam molding. The advantages of each of the polystyrene-based resins are utilized, and it is suitable for the production of a molded article having excellent rigidity, foam moldability, chemical resistance and heat resistance.

The modified polystyrene resin particles described above are then impregnated with a hydrocarbon foaming agent to form expandable modified polystyrene resin particles.
As the hydrocarbon-based foaming agent impregnated into the modified polystyrene resin particles, those having a boiling point equal to or lower than the softening temperature of the polymer and easily volatile, such as propane, n-butane, i-butane, n-pentane, Examples include i-pentane and cyclopentane, and these blowing agents can be used alone or in combination of two or more. The amount of the hydrocarbon-based foaming agent used is preferably in the range of 5 to 25 parts by mass with respect to 100 parts by mass of the modified polystyrene resin particles.

  Furthermore, you may use a foaming adjuvant with a foaming agent. Examples of such foaming aids include solvents such as toluene, xylene, ethylbenzene, cyclohexane, and D-limonene, and plasticizers (high-boiling solvents) such as diisobutyl adipate, diacetylated monolaurate, and palm oil. . In addition, as addition amount of a foaming adjuvant, 0.1-2.5 mass parts is preferable with respect to 100 mass parts of modified polystyrene resin particles.

  In addition, a surface treatment agent such as a binding inhibitor, a fusion accelerator, an antistatic agent, or a spreading agent may be added to the expandable modified polystyrene resin particles.

  The anti-bonding agent serves to prevent the pre-expanded particles from being bonded to each other when the expandable modified polystyrene resin particles are pre-expanded. Here, coalescence means that a plurality of pre-expanded particles are united and integrated. Specific examples include talc, calcium carbonate, zinc stearate, aluminum hydroxide, ethylene bis stearamide, tricalcium phosphate, dimethylpolysiloxane, and the like.

The fusion accelerator plays a role of promoting fusion between the pre-foamed particles when the pre-foamed particles are subjected to secondary foam molding. Specific examples include stearic acid, stearic acid triglyceride, hydroxystearic acid triglyceride, sorbitan stearate, and the like.
Examples of the antistatic agent include polyoxyethylene alkylphenol ether and stearic acid monoglyceride. Examples of the spreading agent include polybutene, polyethylene glycol, and silicone oil. In addition, as for the total addition amount of the said surface treating agent, 0.01-2.0 mass parts is preferable with respect to 100 mass parts of modified polystyrene resin particles.

  The method of impregnating the modified polystyrene resin particles with the foaming agent can be appropriately changed according to the type of the foaming agent. For example, a method in which a foaming agent is pressed into an aqueous medium in which modified polystyrene resin particles are dispersed, and the foaming agent is impregnated in the resin, and the modified polystyrene resin particles are supplied to a rotary mixer. Examples thereof include a method in which a foaming agent is pressed into a rotary mixer and the resin particles are impregnated with the foaming agent. The temperature at which the modified polystyrene resin particles are impregnated with the foaming agent is usually preferably 50 ° C to 140 ° C.

Next, the expandable modified polystyrene resin particles are heated and foamed by contacting with a heating medium such as water vapor to obtain pre-expanded particles.
The pre-foaming heating conditions and the apparatus used for the pre-foaming can be the same as those for the production of conventional polystyrene resin pre-foamed particles. For example, it is obtained by heating the expandable modified polystyrene resin particles in an atmosphere of a water vapor pressure of about 0.5 to 4.0 kg / cm ² G (about 0.05 to 0.4 MPa) in a pre-foaming apparatus. be able to. The heating time is generally about 20 to 120 seconds.

In the production method of the present invention, the pre-expanded particles have a bulk density of 0.0166 to 0.20 g / cm ³ . A preferred bulk density is in the range of 0.02 to 0.10 g / cm ³ , and a more preferred bulk density is in the range of 0.022 to 0.05 g / cm ³ . When the bulk density is less than 0.0166 g / cm ³ , the closed cell ratio of the foamed particles decreases, so that shrinkage occurs during molding, and a good foamed molded article cannot be obtained. On the other hand, if the bulk density is larger than 0.20 g / cm ³ , the density of the foamed molded product obtained by in-mold foam molding of the pre-foamed particles is undesirably high.
Moreover, when this bulk density is expressed by a bulk foaming factor, it is bulk foaming factor (times) = 1 / bulk density (g / cm ³ ), so that this pre-expanded particle has a bulk foaming factor of 5 to 60 (times). The preferred bulk foaming factor is 10 to 50 (times), and the more preferred bulk foaming factor is 20 to 45 (times).

  The form of the pre-expanded particles is not particularly limited as long as it does not affect the subsequent in-mold foam molding. For example, a true spherical shape, an elliptical spherical shape (egg shape), a cylindrical shape, a prismatic shape, and the like can be given. Of these, a true spherical shape and an elliptical spherical shape, which can be easily filled into the cavity of the mold, are preferable.

  The pre-expanded particles may contain an additive. Additives include foaming nucleating agents such as talc, calcium silicate, ethylene bis-stearic acid amide, methacrylic acid ester copolymers, fillers such as synthetic or naturally produced silicon dioxide, hexabromocyclododecane, triallyl Examples include flame retardants such as isocyanurate 6 bromine compounds, plasticizers such as diisobutyl adipate, liquid paraffin, glycerin diacetomonolaurate and coconut oil, colorants such as carbon black and graphite, UV absorbers and antioxidants. .

  Next, the foaming agent remaining in the pre-foamed particles is forcibly reduced to obtain foaming agent-removed foamed particles having a residual gas amount of 0.0 to 3.0% by mass.

In the production method of the present invention, a sound-absorbing modified polystyrene resin having a density of 0.0166 to 0.20 g / cm ³ , a porosity of 10 to 30%, and a bending breaking point displacement of 10 mm or more. In order to obtain a foam-molded product, it is an essential condition that the residual gas amount of the pre-foamed particles is reduced to 0.0 to 3.0% by mass and the foaming agent-removed foam particles are subjected to in-mold foam molding. The residual gas amount of the foaming agent-removed foam particles is preferably in the range of 0.0 to 2.0 mass%, and more preferably in the range of 0.0 to 1.0 mass%. If the residual gas amount is larger than 3.0% by mass, the secondary foamability when the pre-expanded particles are subjected to in-mold foam molding is increased, and a foam molded article having a sufficient proportion of voids cannot be obtained.

In the production method of the present invention, in order to reduce the amount of residual gas in the pre-foamed particles, the pre-foamed particles after pre-foaming are usually allowed to stand at room temperature for about 12 hours and then aged, then tough cloth or the like (hole Transferred to an open plastic bag, etc., and annealed at 60 ° C. (50-80 ° C.) for several hours to several days in an oven or the like (hot air dryer, etc.), thereby reducing the amount of residual gas in the pre-expanded particles to 0.0-3 It can be reduced to 0.0% by mass.
Further, after the pre-expanded particles are transferred to tough cloth or the like, the amount of residual gas in the pre-expanded particles is reduced to 0.0 to 3.0% by mass even if left in a constant temperature room of 23 ± 2 ° C. be able to.

As described above, the foaming agent-removed foamed particles in which the amount of residual gas in the pre-foamed particles is reduced to 0.0 to 3.0% by mass are filled in the mold cavity and heated for in-mold foam molding. The sound-absorbing modified polystyrene resin foam molded article of the present invention having a desired shape can be obtained by fusing and integrating the pre-expanded particles. This in-mold foam molding can be performed, for example, by introducing water vapor having a vapor pressure of about 0.5 to 4.5 kg / cm ² G (about 0.05 to 0.45 MPa) into the mold.

  The sound-absorbing modified polystyrene resin foam molded product of the present invention (hereinafter abbreviated as a foam molded product) satisfies the following conditions (a) to (d).

(A) The foamed molded product of the present invention has a density of 0.0166 to 0.20 g / cm ³ . The density is preferably in the range of 0.02 to 0.10 g / cm ³ , and more preferably the density is in the range of 0.022 to 0.05 g / cm ³ .
If the density of the foamed molded product is smaller than 0.0166 g / cm ³ , the closed cell ratio of the pre-expanded particles is lowered, and thus shrinkage occurs during molding, and a good foamed molded product cannot be obtained. On the other hand, when the density of the foamed molded product is larger than 0.20 g / cm ³ , the mass of the foamed molded product obtained by foaming the pre-foamed particles is not preferable.
In addition, when this density is expressed in terms of expansion ratio, since expansion ratio (times) = 1 / density (g / cm ³ ), this pre-expanded particle has a expansion ratio of 5 to 60 (times), which is preferable. The expansion ratio is 10 to 50 (times), and a more preferable expansion ratio is 20 to 45 (times).

(B) In the foamed molded article of the present invention, the porosity is in the range of 10 to 30%, and more preferably in the range of 12 to 25%. When the porosity is less than 10%, a good sound absorption rate cannot be obtained. On the other hand, if the porosity exceeds 30%, there are too many voids in the molded body, and a predetermined strength cannot be obtained.

(C) The foamed molded product of the present invention has a bending break point displacement measured according to the method described in JIS K7221-2: 1999 of 10 mm or more. More preferably, it is 15 mm or more. If the bending break point displacement is less than 10 mm, the mechanical strength (fusibility) of the foamed molded product is lowered, and the test piece is separated when an impact test of the foamed molded product is performed. The bending break point displacement amount can be regarded as an index for measuring the fusion property between the foamed particles in the foamed molded article, and a larger bending break point displacement amount is more preferable because of better fusion property. When the bending displacement at the breaking point exceeds 55 mm, the test piece falls off by a predetermined measuring method, and a correct value cannot be measured.

(D) The foamed molded article of the present invention has a portion having a sound absorption coefficient of 0.5 or more in a range of 500 Hz or more and 6000 Hz or less when the normal incident sound absorption coefficient is measured at a thickness of 30 mm in accordance with ASTM E1050. Is preferred. If there is no portion having a sound absorption coefficient of 0.5 or more, the required performance as a sound absorbing material, particularly a sound absorbing material for automobiles, cannot be satisfied.

Further, it is desirable that the foamed molded product of the present invention has a shrinkage ratio of the foamed molded product of 1.5% or less in dimensional change measurement under the condition of 80 ° C. based on JIS K6767. When the shrinkage rate exceeds 1.5%, the dimensional stability is not preferable.
In addition, since shrinkage | contraction rate is so preferable that it is small, it is not necessary to provide the lower limit in particular. For example, it is desirable that the lower limit value of the shrinkage rate is zero.

  The foamed molded article of the present invention has excellent mechanical strength, particularly crack resistance and impact resistance, and has a large number of voids, and exhibits excellent sound absorption. The foamed molded product of the present invention can be used in various applications such as a vehicle bumper core material, a vehicle cushioning material such as a door interior cushioning material, electronic parts, various industrial materials, food containers and the like.

  EXAMPLES Hereinafter, the present invention will be specifically described with reference to examples, but the present invention is not limited thereto. In the following Examples, melting point, melting start temperature, absorbance ratio of particle surface layer and polystyrene resin ratio (hereinafter referred to as PS ratio), bulk density of pre-expanded particles, residual gas amount of pre-expanded particles, foam molded article A method for measuring the density, the bending displacement at break, the porosity, the sound absorption rate, and the heating dimensional change rate is described below.

<Absorbance ratio and PS ratio of particle surface layer>
The absorbance ratio (D698 / D1376) was measured as follows.
That is, an infrared absorption spectrum was obtained by performing ATR infrared spectroscopic analysis on the particle central part or surface of each of 10 randomly selected pre-expanded particles.
In the measurement of the particle surface layer, an ATR prism is closely attached to the surface of each pre-expanded particle.
The absorbance ratio (D698 / D1376) was calculated from each infrared absorption spectrum, and the minimum absorbance ratio and the maximum absorbance ratio were excluded. The arithmetic average of the remaining 8 absorbance ratios was taken as the absorbance ratio (D698 / D1376). The absorbance ratio (D698 / D1376) was measured, for example, using a measuring apparatus sold under the trade name “Fourier transform infrared spectrophotometer MAGMA 560” from Nicolet (current name: Thermofisher).
The PS ratio (% by mass) of the particle surface layer was calculated from the absorbance ratio (D698 / D1376) based on a calibration curve prepared in advance using a standard product.

<Bulk density of pre-expanded particles>
The bulk density of the pre-expanded particles was measured as follows.
First, pre-expanded particles were filled up to 500 cm ^{3 and} a graduation of 500 cm ^{3 in} a measuring cylinder. When the graduated cylinder was visually observed from the horizontal direction and any pre-expanded particles reached the scale of 500 cm ³ , the filling of the pre-expanded particles into the graduated cylinder was completed at that point.
Next, the mass of the pre-expanded particles filled in the measuring cylinder was weighed with two significant figures after the decimal point, and the mass was defined as W (g).
And the bulk density of the pre-expanded particles was calculated by the following formula.
Bulk density (g / cm ³ ) = W / 500

<Remaining gas amount of pre-expanded particles>
The amount of residual gas of the pre-expanded particles is about 20 mg of the pre-expanded particles obtained by pre-expanding, and is set at the inlet of the pyrolysis furnace PYR-1A manufactured by Shimadzu Corporation for about 15 seconds. Purge with helium to discharge the mixed gas during sample setting. After sealing, the sample was inserted into a 200 ° C. core, heated for 120 seconds to release the gas, and the released gas was quantified using a gas chromatograph GC-14B (detector: TCD) manufactured by Shimadzu Corporation. The measurement conditions were a column temperature (100 ° C.), a carrier gas (helium), a carrier gas flow rate (1 ml / min), an inlet temperature (120) using Polapack Q (80/100) 3 mmφ × 1.5 m manufactured by GL Sciences. ° C) and detector temperature (120 ° C).

<Density of foam molding>
The density of the foamed molded product was measured as follows.
It was measured by the method described in JIS K7122: 1999 “Foamed Plastics and Rubbers—Measurement of Apparent Density”.
A test piece of 50 cm ³ or more (100 cm ³ or more in the case of semi-rigid and soft materials) was cut so as not to change the original cell structure of the material, its mass was measured, and calculated by the following formula.
Density (g / cm ³ ) = Test piece mass (g) / Test piece volume (cm ³ )
Test piece condition adjustment and measurement test pieces were cut out from samples that had passed 72 hours or more after molding, and were subjected to atmospheric conditions of 23 ° C. ± 2 ° C. × 50% ± 5% or 27 ° C. ± 2 ° C. × 65% ± 5%. It has been left for more than an hour.

<Foaming multiple>
The expansion ratio of the foamed molded product was calculated by the following formula.
Foaming multiple (times) = 1 / density (g / cm ³ )

<Displacement of bending break point>
The bending strength is measured according to the method described in JIS K7221-2: 1999 “Hard foamed plastic—bending test—Part 2: measurement of bending properties”. That is, using a Tensilon universal testing machine UCT-10T (Orientec Co., Ltd.), the specimen size is 75 × 300 × 25 mm, the compression speed is 10 mm / min, the tip jig is a pressure wedge 10R, and a support base 10R. The distance between fulcrums was measured as 200 mm.
The breaking point displacement amount of the bending was defined as the breaking point displacement point where the following phenomenon occurred in the bending test. When the break detection sensitivity is set to 0.5% and the decrease exceeds the set value of 0.5% compared to the previous load sampling point, the previous sampling point.

<Porosity>
The porosity of the foamed molded product was measured according to the measurement method described in ASTM D2856-87. Specifically, five test pieces (cubes each having a side of 25 mm) made of a cut surface having no skin such as a molding surface with six surfaces were cut out from the foamed molded product, and the apparent volume of the test piece was measured using calipers. W ₄ is measured. Next, the volume W ₅ of the test piece can be measured by an 1-1 / 2 atm method using an air comparison type hydrometer, and the porosity of the foamed molded product can be calculated based on the following formula. In addition, the air comparison type hydrometer can use what is marketed by Tokyo Science company by the brand name "1000 type | mold".
Porosity (%) of foam molded article = 100 × (W ₄ −W ₅ ) / W ₄

<Sound absorption rate>
The sound absorption rate was measured in accordance with ISO 10534-2 (Determination of sound absorption coefficient and Impedance in impulse tubes Part 2: Transfer-function method) and ASTM E 1050.
That is, using a normal incident sound absorption coefficient measurement system 4206 type acoustic impedance tube (manufactured by Bruel & Care) and measurement software MS1021 type (manufactured by Matsushita Techno Trading), measurement conditions are a temperature of 20 ° C., a sample thickness of 30 mm, and the back surface of the sample. A frequency range of 500 Hz to 6000 Hz was measured without an air layer.

<Heating dimensional change rate>
The heating dimensional change rate was measured by the method B described in JIS K 6767: 1999K “foamed plastic-polyethylene test method”.
The test piece is 150 x 150 x original thickness (mm), and three straight lines are written in the center part in parallel with each other in the vertical and horizontal directions at intervals of 50 mm. After 22 hours, the sample was taken out and left in a standard state for 1 hour, and the vertical and horizontal line dimensions were measured by the following formula.
S = (L1-L0) / L0 × 100
In the formula, S represents a heating dimensional change rate (%), L1 represents an average dimension (mm) after heating, and L0 represents an initial average dimension (mm).
The heating dimensional change rate S was evaluated according to the following criteria.
A: 0 ≦ S <1.5; the rate of dimensional change was low, and the dimensional stability was good.
(Triangle | delta): 1.5 <= S <5; Although the change of a dimension was seen, it was usable practically.
X: S ≧ 5; dimensional change was remarkably observed, and practical use was impossible.

<Impact test>
The test piece has an original thickness of 150 mm in the vertical direction and 100 mm in the horizontal direction.
The experiment was conducted in accordance with JIS Z0235 “Dynamic compression test method for packaging buffer material”. First, a dropping jig is provided above the test piece. Next, an accelerometer is attached to the scissors jig, and a displacement meter is attached to the test piece to measure the amount of displacement due to the dropping of the scissors jig. Next, the dredge jig is dropped on the test piece with a free drop tester, and the load (unit: N) and the displacement of the test piece (unit: mm) applied to the test piece as time passes after the dredge jig is dropped Asked.
The scissors jig has an arc shape with a weight of 8.4 kg, a width W of 80 mm, a length L of 91 mm, and a radius of 40 mm at one end, and is located at a height H (0.625 m) from the surface of the test piece. Let fall from.
The sample after the test was visually observed, and the impact absorption characteristics were evaluated according to the following criteria.
○: The test piece remained without separation, and the impact absorption of the test piece was good.
(Triangle | delta): Although a part of test piece was isolate | separated, it was usable practically.
X: The test piece was completely separated and could not be used practically.

[Example 1]
100 parts by mass of polypropylene resin (manufactured by Prime Polymer Co., Ltd., trade name “F-744NP”, melting point: 140 ° C., melting start temperature 60-100 ° C.) is supplied to an extruder, melt-kneaded, and granulated pellets by strand cutting. As a result, spherical (egg-like) polypropylene resin particles were obtained.
The polypropylene resin particles at this time were adjusted to 56 mg per 100 particles and an average particle diameter of about 1 mm.
Next, 800 g of the polypropylene resin particles are put into a 5 L autoclave with a stirrer, and 2 kg of pure water, 20 g of magnesium pyrophosphate and 0.5 g of sodium dodecylbenzenesulfonate are added as an aqueous medium, and the mixture is stirred and suspended in the aqueous medium. Held for 10 minutes, and then heated to 60 ° C. to obtain an aqueous suspension.
Next, 400 g of a styrene monomer in which 0.8 g of dicumyl peroxide was dissolved in this suspension was dropped in 30 minutes. After dropping, the mixture was held for 30 minutes to allow the polypropylene resin particles to absorb the styrene monomer.
Next, the temperature of the reaction system was raised to 140 ° C., which is the same as the melting point of the polypropylene resin particles, and held for 2 hours, and the styrene monomer was polymerized (first polymerization) in the polypropylene resin particles.
Next, the reaction liquid of the first polymerization is set to 120 ° C. that is 20 ° C. lower than the melting point of the polypropylene resin particles, and 1.5 g of sodium dodecylbenzenesulfonate is added to this suspension, and then the polymerization initiator is used. 800 g of styrene monomer in which 3.6 g of dicumyl peroxide was dissolved was dropped over 4 hours, and polymerization (second polymerization) was carried out while absorbing the polypropylene resin particles (PP resin / PS ratio = 40 / 60).
After completion of the dropping, the mixture was held at 120 ° C. for 1 hour, then heated to 140 ° C. and held for 3 hours to complete the polymerization, and modified polystyrene resin particles were obtained.
Next, it was cooled to room temperature, and the resin particles were taken out from the 5 L autoclave. After taking out, 2 kg of modified polystyrene resin particles and 2 L of water were again put into a 5 L autoclave with a stirrer, and 300 g of butane as a blowing agent was injected into the 5 L autoclave with a stirrer. After the injection, the temperature was raised to 70 ° C. and stirring was continued for 4 hours.
Then, after cooling to normal temperature, it took out from the 5L autoclave, and after dehydrating and drying, expandable modified polystyrene resin particles were obtained.
Next, the obtained expandable modified polystyrene resin particles were pre-expanded to a bulk expansion ratio of 40 times to obtain pre-expanded particles. And the light absorbency was measured using the obtained pre-expanded particle | grains, and the polystyrene-type resin ratio was computed.
The pre-foamed pre-foamed particles are allowed to stand at room temperature for about 12 hours and aged, then transferred to a perforated plastic bag, and heated at 60 ° C. (50-80 ° C.) in an oven (hot air dryer). The foaming agent was removed by annealing. The residual gas amount of the pre-expanded particles after removing the foaming agent was measured. In this example, the residual gas amount of the pre-expanded particles was reduced to 0.0% by mass.
Next, the pre-expanded particles after removing the foaming agent are filled into the cavities of a mold having a size of 400 mm × 300 mm × 30 mm, and 0.11 MPa of water vapor is introduced into the mold for 60 seconds. And it cooled until the maximum surface pressure of a foaming molding fell to 0.001 MPa, and the foaming molding was obtained. A foamed molded article having good voids in both appearance and fusion was obtained under these molding conditions.
For foam molding, a foam molding machine (manufactured by Sekisui Koki Co., Ltd., trade name “ACE-3SP”) was used.
Using the obtained foamed molded product, the density of the foamed molded product, the amount of bending break point displacement, the porosity, the sound absorption rate, and the heating dimensional change rate were measured.
In addition, in the present Example, the foaming molding of the expansion ratio 40 times was also able to be obtained.

[Example 2]
In the production of the pre-expanded particles, the modified polystyrene resin foam was made in the same manner as in Example 1 except that the residual gas amount was 0.9 mass% and the heating time at the time of foam molding was 45 seconds. A molded body was produced.

[Example 3]
In the production of the pre-expanded particles, the modified polystyrene resin foam was made in the same manner as in Example 1 except that the residual gas amount was 2.9% by mass and the heating time at the time of foam molding was 30 seconds. A molded body was produced.

[Example 4]
A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the PP resin / PS ratio was 30/70.

[Example 5]
Except that the PP resin / PS ratio was 30/70, the residual gas amount was 2.7% by mass, and the heating time during foam molding was 30 seconds, the same as in Example 1, A modified polystyrene resin foam molded article was produced.

[Example 6]
A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the PP resin / PS ratio was 20/80 and the vapor pressure during foam molding was 0.10 MPa.

[Example 7]
The PP resin / PS ratio was 20/80, the residual gas amount was 3.0% by mass, the vapor pressure during foam molding was 0.10 MPa, and the heating time during foam molding was 30. A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that it was changed to seconds.

[Example 8]
A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the PP resin / PS ratio was 50/50 and the vapor pressure during foam molding was 0.12 MPa.

[Example 9]
The PP resin / PS ratio was 50/50, the residual gas amount was 3.0% by mass, the vapor pressure during foam molding was 0.12 MPa, and the heating time during foam molding was 30. A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that it was changed to seconds.

[Example 10]
A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the amount of residual gas was 0.9 mass% and the bulk expansion ratio of the pre-expanded particles was 5 times.

[Example 11]
Except that the amount of residual gas was 1.0% by mass, the bulk expansion ratio of the pre-expanded particles was 60 times, and the heating time during foam molding was 30 seconds, the same as in Example 1. Then, a modified polystyrene resin foam molded article was produced.

[Example 12]
A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the residual gas amount was 0.9 mass% and the vapor pressure during foam molding was 0.12 MPa.

[Example 13]
A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the vapor pressure during foam molding was 0.10 MPa and the heating time during foam molding was 30 seconds. .

[Comparative Example 1]
The PP resin / PS ratio was 55/45, the residual gas amount was 3.2% by mass, the bulk expansion ratio of the pre-expanded particles was 4.5 times, and the vapor pressure during foam molding was A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the pressure was 0.08 MPa and the heating time during foam molding was 45 seconds.

[Comparative Example 2]
The PP resin / PS ratio was 60/40, the residual gas amount was 3.3% by mass, the bulk expansion ratio of the pre-expanded particles was 4.5 times, and the vapor pressure during foam molding was A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the pressure was 0.08 MPa and the heating time during foam molding was 45 seconds.

[Comparative Example 3]
The PP resin / PS ratio was set to 10/90, the residual gas amount was set to 3.8% by mass, the bulk expansion ratio of the pre-expanded particles was set to 65 times, and the vapor pressure during foam molding was set to 0.00. A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the pressure was set to 08 MPa and the heating time during foam molding was set to 45 seconds.

[Comparative Example 4]
The PP resin / PS ratio was set to 15/85, the residual gas amount was set to 3.8% by mass, the bulk expansion ratio of the pre-expanded particles was set to 65 times, and the vapor pressure during foam molding was set to 0.00. A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that the pressure was set to 08 MPa and the heating time during foam molding was set to 45 seconds.

[Comparative Example 5]
The PP resin / PS ratio was 40/60, the residual gas amount was 3.5% by mass, the vapor pressure during foam molding was 0.08 MPa, and the heating time during foam molding was 30. A modified polystyrene resin foam molded article was produced in the same manner as in Example 1 except that it was changed to seconds.

[Comparative Example 6]
A modified polystyrene resin foam molded article was produced in the same manner as in Example 1, except that the residual gas amount was 3.5% by mass and the heating time during foam molding was 30 seconds.

[Comparative Example 7]
Example 1 except that the residual gas amount was 3.9% by mass, the vapor pressure during foam molding was 0.08 MPa, and the heating time during foam molding was 45 seconds. Thus, a modified polystyrene resin foam molded article was produced.

[Comparative Example 8]
Except that the residual gas amount was 1.2% by mass, the vapor pressure during foam molding was 0.08 MPa, and the heating time during foam molding was 45 seconds, the same as in Example 1. Thus, a modified polystyrene resin foam molded article was produced.

[Comparative Example 9]
Except that the PP resin / PS ratio was 30/70, the residual gas amount was 3.5% by mass, and the heating time during foam molding was 30 seconds, the same as in Example 1, A modified polystyrene resin foam molded article was produced.

[Comparative Example 10]
Except that the PP resin / PS ratio was 20/80, the residual gas amount was 4.0% by mass, and the heating time during foam molding was 30 seconds, the same as in Example 1, A modified polystyrene resin foam molded article was produced.

[Comparative Example 11]
Except that the PP resin / PS ratio was 50/50, the residual gas amount was 3.8% by mass, and the heating time during foam molding was 30 seconds, the same as in Example 1, A modified polystyrene resin foam molded article was produced.

The results of Examples 1 to 13 are summarized in Table 1.
In addition, the results of Comparative Examples 1 to 11 are collectively shown in Table 2.

From the results of Tables 1 and 2, in Examples 1 to 13 according to the present invention, the amount of the remaining foaming agent in the pre-foamed particles is 0.0 to 3.0% by mass, and the foaming agent-removed foamed particles are used for in-mold foaming. By making a foamed molded body by molding,
(A) a density in the range of 0.0166 to 0.20 g / cm ³ ;
(B) the porosity is in the range of 10 to 30%,
(C) The bending break point displacement measured according to the method described in JIS K7221-2: 1999 is 10 mm or more,
(D) According to ASTM E1050, when the normal incident sound absorption coefficient is measured at a thickness of 30 mm, there is a portion having a sound absorption coefficient of 0.5 or more in the range of 500 Hz to 6000 Hz,
It was possible to obtain a sound-absorbing modified polystyrene-based resin foam molded article that satisfies all of the above conditions.

  On the other hand, in Comparative Examples 1 to 11 using pre-expanded particles having a residual foaming agent amount exceeding 3.0% by mass, each of the above conditions (a) to (d) was obtained even if the in-mold foam molding conditions were changed. A sound-absorbing modified polystyrene resin foam molded article satisfying all of the above was not obtained.

  The sound-absorbing modified polystyrene resin foam molded article of the present invention is used in various applications such as a vehicle bumper core material, a vehicle cushioning material such as a door interior cushioning material, electronic parts, various industrial materials, food containers and the like. Can be used.

Claims (7)

100 parts by mass of a polystyrene resin and less than 400 parts by mass of a polystyrene resin with respect to 100 parts by mass of a propylene resin containing a propylene-ethylene copolymer and having a melting start temperature in the range of 60 to 100 ° C., and the ATR method The ratio (D698 / D1376) of the absorbance D698 at 698 cm ^{−1 and} the absorbance D1376 at 1376 cm ⁻¹ obtained from the infrared absorption spectrum of the particle surface measured by infrared spectroscopy is in the range of 0.1 to 2.5. A modified polystyrene resin particle is impregnated with a hydrocarbon foaming agent and then prefoamed to obtain prefoamed particles having a bulk density in the range of 0.0166 to 0.20 g / cm ^3. The remaining foaming agent is forcibly decreased to obtain foaming agent-removed foamed particles having a residual foaming agent amount of 0.0 to 3.0% by mass. The agent removing foam particles perform mold foaming,
(A) a density in the range of 0.0166 to 0.20 g / cm ³ ;
(B) the porosity is in the range of 10 to 30%,
(C) The bending break point displacement measured according to the method described in JIS K7221-2: 1999 is 10 mm or more,
(D) According to ASTM E1050, when the normal incident sound absorption coefficient is measured at a thickness of 30 mm, there is a portion having a sound absorption coefficient of 0.5 or more in the range of 500 Hz to 6000 Hz,
A method for producing a sound-absorbing modified polystyrene resin foam molded article, characterized by obtaining a sound-absorbing modified polystyrene resin foam molded article that satisfies the above conditions. The modified polystyrene resin particles are
(A) A step of dispersing 100 parts by mass of polypropylene resin particles, 100 parts by mass or more and less than 400 parts by mass of a styrene monomer, and a polymerization initiator in an aqueous suspension containing a dispersant,
(B) heating the obtained dispersion to a temperature at which the styrenic monomer is not substantially polymerized to impregnate the polypropylene resin particles with the styrenic monomer;
(C) When the melting point of the polypropylene resin particles is T ° C., the step of performing the first polymerization of the styrene monomer at a temperature of (T−10) ° C. to (T + 20) ° C.,
(D) Subsequent to the first polymerization step, a styrene monomer and a polymerization initiator are added, and when the melting point of the polypropylene resin particles is T ° C, (T-25) ° C to It is manufactured through the step of impregnating the polypropylene resin particles with the styrene monomer and performing a second polymerization by setting the temperature to (T + 10) ° C. A method for producing a sound-absorbing modified polystyrene resin foam molded article.   The hydrocarbon blowing agent is one or more selected from the group consisting of propane, n-butane, i-butane, n-pentane, i-pentane, and cyclopentane. 2. A method for producing a sound-absorbing modified polystyrene resin foam molded article according to 2. The step of forcibly reducing the foaming agent remaining in the pre-expanded particles,
(i) A treatment method in which pre-expanded particles are placed in a gas-permeable container and hot-air drying at 50 to 80 ° C. is performed for several hours to several days,
(ii) The pre-foamed particles are placed in a breathable container and left at room temperature until the amount of the remaining foaming agent is 0.0 to 3.0% by mass. The manufacturing method of the sound-absorbing property modified polystyrene-type resin foam molding of any one of Claims 1-3 to do.   The sound-absorbing modified polystyrene resin foam according to any one of claims 1 to 4, wherein the residual foaming agent amount of the foaming agent-removed foamed particles is in the range of 0.0 to 3.0 mass%. Manufacturing method of a molded object.   A sound-absorbing modified polystyrene resin foam molded article obtained by the method for producing a sound-absorbing modified polystyrene resin foam molded article according to any one of claims 1 to 5.   JIS K6767: Heat-absorbing modified polystyrene-based resin foam molded article according to claim 6, wherein the heating dimensional change rate at 80 ° C measured by B method of JIS K6767: 1999K is less than 1.5%.