JP6612634B2 - Styrenic resin foamable particles, foamed particles and foamed molded article - Google Patents

Description

  The present invention relates to styrene resin foamable particles, foamed particles, and a foamed molded article. More specifically, the present invention relates to a styrenic resin foam molded article excellent in heat insulation and flame retardancy, styrene resin foamable particles and foamed particles for producing the molded article.

  Conventionally, foamed molded products are lightweight and excellent in heat insulation and mechanical strength. Therefore, heat insulating materials used in houses and automobiles, heat insulating materials used in building materials, packing materials for transportation such as fish boxes and food containers, and cushioning materials. Etc. are used. Among them, in-mold foam molded articles produced using foamable particles as raw materials are often used because of the advantage that a desired shape is easily obtained.

As the foam molded article, a styrene resin foam molded article derived from styrene resin foamable particles is widely used. The styrenic resin foam molded body heats and expands styrene resin foamable particles to obtain prefoamed particles, and then heats the prefoamed particles obtained by secondary foaming in the mold cavity. It is obtained by integrating by fusing.
Styrenic resin foam moldings have various properties, for example, excellent thermal insulation properties. Excellent heat insulation is required for various applications from the viewpoint of energy saving. Specific applications include wall insulation, floor insulation, roof insulation, automotive insulation, hot water tank insulation, piping insulation, solar system insulation, water heater insulation, food And containers for industrial products, packing materials for fish and agricultural products, embankment materials, tatami core materials, and the like.

It is desired that the heat insulating property required for the foam molded body is further improved from the viewpoint of energy saving. As a method for improving the heat insulation, various methods such as higher magnification, change of resin composition, use of additives, and the like are known. For example, Japanese Patent Application Laid-Open No. 63-183941 (Patent Document 1) proposes a foamed molded article containing fine powder having an infrared reflectance of 40% or more as an additive. In the example of Patent Document 1, a foam molded article using aluminum powder, silver powder, and graphite powder having a reflectance of 40% or more is carbon black (for example, generally used as a blackening agent in the foam molded article (for example, JP, 2013-6966, A: patent documents 2) It is explained that it is excellent in heat insulation than a foaming fabrication object containing an additive which has reflectance of less than 40%.
In addition, various proposals have been made for foam molded articles to improve physical properties such as flame retardancy.

Japanese Unexamined Patent Publication No. 63-183941 JP 2013-6966 A

The technology described in the above publication is difficult to obtain a foamed molded product having sufficient heat insulating properties and flame retardancy that has been required in recent years, and provides a foamed molded product having higher heat insulating properties and flame retardant properties. Is desired.
Further, brominated halogen-based flame retardants widely used for improving flame retardance are desired to be reduced in terms of environmental problems.
Then, this invention makes it a subject to provide the styrene resin foaming molding excellent in heat insulation and a flame retardance, the styrene resin foaming particle and foaming particle for manufacturing the molding.

  The inventors of the present invention have studied additives that are added to the foam molded body in order to improve the heat insulation and flame retardancy of the foam molded body. As a result, the knowledge that the carbon material contributes to the improvement of heat insulation and the specific kind of phosphorus-based flame retardant contributes to the improvement of flame retardancy without impairing the effect is obtained, and the present invention is completed. It was.

Thus, according to the present invention, the phosphorus flame retardant comprises a styrene resin, a carbon material, a foaming agent and a flame retardant, wherein the flame retardant comprises a phosphorus flame retardant having a phosphorus content of 7% by mass or more. Is 5 to 10 parts by mass with respect to 100 parts by mass of the styrene resin , and the carbon material has a volume resistivity of 1.0 × 10 ⁴ Ω · cm or less and a volume resistivity of 1.0 × 10 ^{−. The} conductive carbon black is ¹ Ω · cm or more, the primary particles of the carbon material have an average primary particle diameter of 18 to 125 nm, and the average value of the longest diameter of the aggregate in which a plurality of primary particles are aggregated is 180 to 500 nm. , and the styrene-based resin foamed particles the ratio of the longest diameter of the mean value for the average primary particle diameter is characterized 4.0-10.0 der Rukoto is provided.
Moreover, according to the present invention, the flame retardant includes a styrene resin, a carbon material, and a flame retardant, the phosphorus flame retardant having a phosphorus content of 7% by mass or more, and the phosphorus flame retardant is styrene. 5 to 10 parts by mass with respect to 100 parts by mass of the resin , and the carbon material has a volume resistivity of 1.0 × 10 ⁴ Ω · cm or less and a volume resistivity of 1.0 × 10 ⁻¹ Ω · cm. The conductive carbon black is not less than cm, the primary particles of the carbon material have an average primary particle diameter of 18 to 125 nm, the average value of the longest diameter of the aggregate in which a plurality of primary particles are aggregated is 180 to 500 nm, the expanded styrene resin beads the ratio of the longest diameter of the mean value for the average primary particle diameter is characterized 4.0-10.0 der Rukoto is provided.
Furthermore, according to the present invention, there is provided a foamed molded article comprising a plurality of styrene resin foam particles fused together and containing a styrene resin, a carbon material and a flame retardant, wherein the flame retardant is 7% by mass or more. A phosphorus flame retardant having a phosphorus content, 5 to 10 parts by mass of the phosphorus flame retardant with respect to 100 parts by mass of the styrene resin , and the carbon material having a volume resistivity of 1.0 ×. 10 ⁴ Ω · cm or less and a volume resistivity of 1.0 × 10 ⁻¹ Ω · cm or more, conductive carbon black, and the primary particles of the carbon material have an average primary particle diameter of 18 to 125 nm, primary particles are average longest diameter of more aggregated agglomerates 180～500Nm, foaming ratio of the average value of the longest diameter and wherein 4.0-10.0 der Rukoto to the average primary particle size A shaped body is provided.

  ADVANTAGE OF THE INVENTION According to this invention, the styrene resin foaming molding excellent in heat insulation and a flame retardance, the styrene resin foaming particle and foaming particle for manufacturing the molding can be provided.

In any of the following cases, it is possible to provide styrene resin foamable particles for producing a styrene resin foamable molded article having better heat insulation and flame retardancy.
(1) The flame retardant includes a phosphorus flame retardant and a bromine flame retardant;
(2) 0.5 to 10 parts by mass of a brominated flame retardant in which the flame retardant is tetrabromobisphenol A-bis (2,3-dibromo-2-methylpropyl ether) with respect to 100 parts by mass of the styrene resin Including.
(3) The carbon material is conductive carbon black having a volume resistivity of 1.0 × 10 ⁴ Ω · cm or less.

It is an electron micrograph of the carbon material which formed the aggregate.

(Styrenic resin foamable particles)
Styrenic resin expandable particles (hereinafter, expandable particles) include a styrene resin, a carbon material, a foaming agent, and a flame retardant, and the flame retardant has a phosphorus content of 7% by mass or more. And 3 to 10 parts by mass of the phosphorus flame retardant with respect to 100 parts by mass of the styrene resin.

(1) Styrenic resin The styrene resin is not particularly limited as long as it is a resin capable of obtaining a foam molded article. For example, styrene monomers such as styrene, α-methyl styrene, vinyl toluene, ethyl styrene, i-propyl styrene, t-butyl styrene, dimethyl styrene, bromo styrene, chloro styrene, or a mixture of these monomers The resin derived from is mentioned.
The styrene resin may contain a component derived from a crosslinking agent.
Examples of the crosslinking agent include divinylbenzene, trivinylbenzene, divinyltoluene, divinylxylene, bis (vinylphenyl) methane, bis (vinylphenyl) ethane, bis (vinylphenyl) propane, bis (vinylphenyl) butane, and divinylnaphthalene. , Divinyl anthracene, divinyl biphenyl, and other bifunctional benzene rings, such as a compound in which a vinyl group is bonded directly, bisphenol A ethylene oxide adduct di (meth) acrylate, bisphenol A propylene oxide adduct di (meth) acrylate, etc. A (meth) acrylate compound etc. are mentioned.

  The styrenic resin may be a copolymer of another monomer and the styrenic monomer in an amount that does not impair the characteristics of the present invention. Examples of other monomers include (meth) acrylic acid such as methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate, butyl (meth) acrylate, and cetyl (meth) acrylate. Esters, alkyl maleates such as (meth) acrylonitrile, dimethyl maleate and diethyl maleate, alkyl fumarate such as dimethyl fumarate, diethyl fumarate and ethyl fumarate, maleic anhydride, N-phenylmaleimide, (meth) acrylic An acid etc. are mentioned.

Furthermore, resins other than those described above may be included. Other than the above, polyolefin-modified resins such as polyethylene and polypropylene, rubber modified with addition of diene rubbery polymers such as polybutadiene, styrene-butadiene copolymer, ethylene-propylene-nonconjugated diene three-dimensional copolymer Examples thereof include impact-resistant polystyrene resins, polycarbonate resins, polyester resins, polyamide resins, polyphenylene ethers, acrylonitrile-butadiene-styrene copolymers, and polymethyl methacrylate. The proportion of these other resins is preferably less than 50% by mass, more preferably 30% by mass or less, and still more preferably 10% by mass or less based on the total amount of the base resin.
The styrenic resin preferably has a weight average molecular weight of 100,000 to 1,000,000. When the weight average molecular weight is less than 100,000, the strength of the foamed molded product may be lowered. When larger than 1 million, foamability may fall and it may be inferior to lightness. A weight average molecular weight of 150,000 to 800,000 is more preferable, and 200,000 to 500,000 is more preferable.

  The content of the styrenic resin in the expandable particles is preferably 50% by mass or more. If it is less than 50% by mass, sufficient foamability may not be obtained. A more preferable content rate is 60 mass% or more, and a still more preferable content rate is 80 mass% or more.

(2) Carbon material The carbon material is not particularly limited as long as it does not impair the characteristics of the present invention, but carbon black, activated carbon, graphite, graphene, coke, carbon nanofiber, mesoporous carbon, glassy carbon, hard carbon, and soft carbon Carbon materials, preferably conductive carbon black such as acetylene black and ketjen black.

The carbon material preferably has a volume resistivity of 1.0 × 10 ⁴ Ω · cm or less. When the volume resistivity is higher than 1.0 × 10 ⁴ Ω · cm, the heat insulation may not be sufficiently improved. The preferred volume resistivity is 7.0 × 10 ³ Ω · cm or less, the more preferred volume resistivity is 4.0 × 10 ³ Ω · cm or less, and the more preferred volume resistivity is 2.0 × 10 ³ Ω. · Cm or less, and the most preferable volume resistivity is 1.0 × 10 ³ Ω · cm or less. A lower limit value of the volume resistivity is not particularly provided, but is, for example, about 1.0 × 10 ⁻¹ Ω · cm or more. Specific values of volume resistivity are 1.0 × 10 ³ , 2.0 × 10 ³ , 3.0 × 10 ³ , 4.0 × 10 ³ , 5.0 × 10 ³ , 6.0 × 10 ³ , 7.0 × 10 ³ , 8.0 × 10 ³ , 9.0 × 10 ³ , 1.0 × 10 ⁴ Ω · cm and the like.

  Here, the volume resistivity refers to the raw material carbon material, or when the raw material carbon material is added to the master batch, expandable particles, expanded particles, and expanded molded article, the master batch, expandable particles, The carbon material taken out by removing the styrene resin in the expanded particles and the foamed molded article with an organic solvent is melt-kneaded with a polyethylene resin or a polystyrene resin (carbon material: polyethylene resin or polystyrene resin = 1). : 4 (mass ratio)), and means a value obtained by measuring the surface of the kneaded plate-like molded body. Detailed volume resistivity measurement methods are described in the Examples.

In addition, even if it uses any of a polyethylene-type resin and a polystyrene-type resin, a volume resistivity becomes a comparable value.
In addition, even when using a carbon material as a raw material, even if a carbon material taken out by removing the styrene resin in the master batch, expandable particles, expanded particles, and foamed molded article with an organic solvent is used, the volume resistivity is The value is about the same.

  In addition, when measuring volume resistivity using a polystyrene-based resin, for the procedure of taking out the carbon material by removing the styrene-based resin in the master batch, expandable particles, expanded particles, and foamed molded product with an organic solvent, When the carbon material: polystyrene resin = 1: 4 (mass ratio), the removal of the styrene resin is stopped halfway, or the carbon material: polystyrene resin = 1: 4 (mass ratio). You may take the method of adding (dilution) resin. In the case of adopting a method of stopping the removal of the styrene resin halfway, in order to adjust the carbon material: polystyrene resin = 1: 4 (mass ratio), the masterbatch, expandable particles, expanded particles, carbon in the expanded molded body You may measure the amount of materials, and the amount of styrene resin. Although it does not specifically limit as a measuring method of the amount of carbon materials, For example, the method etc. which use a differential thermothermal weight simultaneous measuring apparatus are mentioned.

The carbon material may be contained in a form in which primary particles of the carbon material are dispersed in the styrene resin, or in the form of an agglomerate in which a plurality of primary particles of the carbon material are aggregated in the styrene resin. May be. Preferably, the primary particles of the carbon material are contained as agglomerates that are agglomerated in the styrene resin.
FIG. 1 shows an example of a carbon material in which aggregates observed using an electron microscope are formed. The primary particle of the carbon material means each of substantially circular particles as observed in FIG. By agglomerate is meant a mass of primary particles that appear to overlap each other, as observed in FIG.

The primary particles preferably have an average primary particle size of 18 to 125 nm.
An average primary particle diameter means the average value of the longest diameter of a primary particle, and can take the value of 18-125 nm. However, this does not restrict the primary particles from taking a shape other than a spherical shape or a substantially spherical shape, and the primary particles may take other shapes such as a cylindrical shape and a prismatic shape. When the primary particles have a shape other than a spherical shape and a substantially spherical shape, the average primary particle size means an average value of the longest diameters obtained by approximating the primary particles to a spherical shape. When the average primary particle diameter is less than 18 nm, moldability may be reduced due to finer bubbles, and when it is greater than 125 nm, moldability may be reduced due to tearing of the bubble film. Specific numerical ranges of the average primary particle diameter include 18 to 120 nm, 18 to 110 nm, 18 to 100 nm, 18 to 90 nm, 18 to 80 nm, 18 to 73 nm, 18 to 66 nm, 18 to 60 nm, 20 to 100 nm, 25 -80 nm, 32-66 nm, 20-125 nm, 25-125 nm, 32-125 nm, 40-125 nm, 50-125 nm, 60-125 nm, 66-125 nm, 73-125 nm, 80-125 nm and the like. Specific values of the average primary particle diameter include 18, 20, 25, 32, 40, 50, 60, 66, 73, 80, 90, 100, 110, 120, 125 nm, and the like.

The agglomerates preferably have (i) an average value of the longest diameter of 180 to 500 nm.
The longest diameter means the longest distance between any two points on the outer edge of the aggregate. For example, in FIG. 1, the diameter indicated by the solid line is defined as the longest diameter of the aggregate. . When the average value of the longest diameter is less than 180 nm, the heat insulating property may not be improved, and when it is larger than 500 nm, bubbles may be broken at the time of foaming and the heat insulating property may not be improved and a good molded product may not be obtained. Specific numerical ranges of the average value of the longest diameter are 180 to 450 nm, 180 to 400 nm, 180 to 370 nm, 180 to 300 nm, 180 to 240 nm, 200 to 450 nm, 220 to 400 nm, 240 to 370 nm, 200 to 500 nm, 220-500 nm, 240-500 nm, 300-500 nm, 370-500 nm, 400-500 nm etc. are mentioned. Specific examples of the average value of the longest diameter include 180, 200, 220, 230, 240, 250, 300, 350, 370, 400, 420, 450, 460, 470, 480, 490, and 500 nm.
The longest diameter of the aggregate is set so as to always overlap the aggregate. In other words, the longest diameter does not pass through the background (styrene resin). For example, in FIG. 1, since the line shown with the broken line has a part which overlaps with a background, it cannot be set as the longest diameter.

  In addition, the agglomerates preferably have (ii) a ratio of “average value of longest diameter” to “average primary particle diameter” of 4.0 to 10.0. When the ratio is less than 4.0, the heat insulating property may not be improved. When the ratio is more than 10.0, bubbles may be broken during foaming and a good molded product may not be obtained. Specific numerical ranges of the above ratio are 4.0 to 9.0, 5.0 to 9.0, 5.0 to 8.9, 5.0 to 8.5, 5.0 to 8. 0, 5.0-7.0, 5.0-6.0, 5.2-8.9, 5.5-8.5, 6.0-8.0, 4.0-10.0, 5.0-10.0, 5.2-10.0, 5.5-10.0, 6.0-10.0 etc. are mentioned. The ratio of the average value of the longest diameter to the specific average primary particle diameter is 4.0, 4.5, 5.0, 5.2, 5.5, 6.0, 7.0, 8. 0, 8.5, 8.6, 8.7, 8.8, 8.9, 9.0, 9.1, 9.2, 9.3, 9.4, 9.5, 9.6, 9.7, 9.8, 9.9, 10.0, etc. are mentioned. Detailed measurement methods of the average value of the longest diameter and the average primary particle diameter are described in Examples.

  Although it does not specifically limit as long as the characteristic of this invention is not inhibited as a carbon material, For example, acetylene black, Ketjen black, carbon nanofiber, a carbon nanotube etc. are mentioned.

  Content of a carbon material is 0.5-25 mass parts with respect to 100 mass parts of styrene resin. When content is less than 0.5 mass part, heat insulation may not fully be improved. On the other hand, when the content exceeds 25 parts by mass, the foam film may be broken, so that the moldability may be reduced and the heat insulation may be inferior. The preferable carbon material content is 0.5 to 15 parts by mass, and the more preferable carbon material content is 0.5 to 10 parts by mass. Specific contents include 0.5, 0.6, 0.7, 0.8, 0.9, 1, 1.01, 2, 2.56, 3, 3.13, 4, 5, 5.26, 6, 7, 7.52, 7.69, 8, 9, 10, 11, 11.11, 12, 13, 14, 15, 16, 17, 18, 19, 20 parts by mass, etc. It is done.

The carbon material preferably has a specific surface area of 10 to 3000 m ² / g. When the specific surface area is less than 10 m ² / g, the desired heat insulating performance may not be obtained. On the other hand, when the specific surface area exceeds 3000 m ² / g, workability may be reduced. For example, as a specific numerical range of the specific surface ^{area, 100~3000m 2 / g, 200~3000m 2} / g, 210~3000m 2 / g, 220~3000m 2 / g, 15~2500m 2 / g, 100~ ^{2500m 2 / g, 210~2500m 2 /} g, 10~2000m 2 / g, 60~2000m 2 / g, 210~2000m 2 / g, 10~1500m 2 / g, 70~1500m 2 / g, 200~1500m ² / g, 210-1500m < ² > / g, etc. are mentioned. When the carbon material is acetylene black, a more preferable specific surface area is 20 to 300 m ² / g. When the carbon material is ketjen black, a more preferable specific surface area is 500 to 2000 m ² / g. As specific surface area values, 10, 15, 20, 25, 30, 40, 50, 60, 70, 80, 90, 100, 150, 200, 210, 220, 230, 240, 250, 260, 270, 280, 290, 300, 400, 500, 700, 1000, 1500, 2000, 2500, 3000 m ² / g and the like.

  In one embodiment, the carbon material is conductive carbon black (eg, acetylene black, ketjen black). Examples of preferable physical property values of the conductive carbon black other than the above-described physical properties include the following.

  The mass ratio of the carbon material and the styrene resin is preferably carbon material: styrene resin = 1: 2 to 1: 1000 (mass ratio). When the mass ratio of the styrene-based resin is less than 2, the foam film may be broken, so that the moldability may be reduced and the heat insulation may be inferior. If the mass ratio is greater than 1000, the heat insulation may not be sufficiently improved. A more preferred mass ratio is 1: 4 to 1: 200, a further preferred mass ratio is 1: 9 to 1:99, a most preferred mass ratio is 1:13 to 1:39, and a very preferred mass ratio is 1:13 to 1:32.

(3) Foaming agent It does not specifically limit as a foaming agent, All can use a well-known thing. In particular, a gaseous or liquid organic compound having a boiling point equal to or lower than the softening point of the styrene resin is suitable. For example, hydrocarbons such as propane, n-butane, isobutane, n-pentane, isopentane, neopentane, cyclopentane, cyclopentadiene, n-hexane, petroleum ether, ketones such as acetone and methyl ethyl ketone, methanol, ethanol, isopropyl alcohol, etc. Low boiling point ether compounds such as alcohols, dimethyl ether, diethyl ether, dipropyl ether, methyl ethyl ether, halogen-containing hydrocarbons such as trichloromonofluoromethane, dichlorodifluoromethane, inorganic gases such as carbon dioxide, nitrogen, ammonia, etc. Can be mentioned. These foaming agents may be used alone or in combination of two or more. Among these, it is preferable to use hydrocarbons from the viewpoint of preventing the destruction of the ozone layer and from the viewpoint of quickly replacing with the air and suppressing the time-dependent change of the foamed molded product. Of the hydrocarbons, hydrocarbons having a boiling point of −45 to 40 ° C. are more preferable, and propane, n-butane, isobutane, n-pentane, isopentane and the like are more preferable.
The content of the foaming agent is preferably in the range of 2 to 12% by mass. If it is less than 2% by mass, a foamed molded article having a desired density may not be obtained from the expandable particles. In addition, since the effect of increasing the secondary foaming power at the time of in-mold foam molding is reduced, the appearance of the foam molded article may not be good. When the amount is more than 12% by mass, the time required for the cooling step in the production process of the foamed molded product becomes long, and the productivity may decrease. A more preferable content is 3 to 10% by mass, a still more preferable content is 4 to 9% by mass, and a most preferable content is 5 to 8% by mass.
A foaming aid may be used in combination with a foaming agent. Examples of the foaming aid include isobutyl adipate, toluene, cyclohexane, and ethylbenzene.

(4) Flame retardant In the present invention, the flame retardant includes a phosphorus-based flame retardant having a phosphorus content of 7% by mass or more.
If the phosphorus content of the phosphorus flame retardant is less than 7% by mass, sufficient flame retardancy may not be obtained. The phosphorus content of a preferable phosphorus flame retardant is 8% to 30% by mass.

Examples of phosphorus flame retardants include phosphate ester compounds and phosphazene compounds.
Examples of phosphate ester compounds include phosphate ester compounds such as trimethyl phosphate, triethyl phosphate, triphenyl phosphate, tricresyl phosphate, trixylenyl phosphate, cresyl diphenyl phosphate.
Examples of the phosphazene compound include hexaphenoxycyclotriphosphazene, octaphenoxycyclotetraphosphazene, decaffeoxycyclopentaphosphazene, dodecaffenoxycyclohexaphosphazene, tetradecaffenoxycycloheptaphosphazene, hexadecaffenoxycyclooctaphosphazene, and other cyclic phenoxyphosphazene compounds. Linear di (bisphenoxy) phosphazene, linear tri (bisphenoxy) phosphazene, linear tetra (bisphenoxy) phosphazene, linear penta (bisphenoxy) phosphazene, linear hexa (bisphenoxy) phosphazene, straight Examples include chain phenoxyphosphazene compounds such as chain hepta (bisphenoxy) phosphazene.
These phosphorus flame retardants may be used alone or in combination of two or more.

3-10 mass parts of phosphorus flame retardants are contained with respect to 100 mass parts of styrene resin.
If the phosphorus flame retardant is less than 3 parts by mass with respect to 100 parts by mass of the styrene resin, sufficient flame retardancy may not be obtained. On the other hand, when the phosphorus-based flame retardant exceeds 10 parts by mass with respect to 100 parts by mass of the styrene resin, the foam moldability may be deteriorated and a good foam molded article may not be obtained.
The content of a preferable phosphorus-based flame retardant is 3 to 7 parts by mass.

In the present invention, the flame retardant may contain a brominated flame retardant in addition to the above phosphorus flame retardant.
Brominated flame retardants include tetrabromocyclooctane, hexabromocyclododecane, trisdibromopropyl phosphate, tetrabromobisphenol A, tetrabromobisphenol A-bis (2,3-dibromo-2-methylpropyl ether), tetrabromobisphenol A-bis (2,3-dibromopropyl ether) etc. are mentioned.
These brominated flame retardants may be used alone or in combination of two or more.

The brominated flame retardant is preferably contained in an amount of 0.5 to 10 parts by mass with respect to 100 parts by mass of the styrene resin.
If the brominated flame retardant is less than 0.5 parts by mass with respect to 100 parts by mass of the styrene resin, the flame retardancy may be insufficient. On the other hand, when the brominated flame retardant exceeds 10 parts by mass with respect to 100 parts by mass of the styrene resin, the foam moldability may be deteriorated and a good foamed molded article may not be obtained.
The content of a preferable brominated flame retardant is 1.0 to 7.0 parts by mass.
In the present invention, the flame retardant is 0.5 to 10 parts by mass of a brominated flame retardant that is tetrabromobisphenol A-bis (2,3-dibromo-2-methylpropyl ether) with respect to 100 parts by mass of the styrene resin. It is preferable to include.

(5) Other additives The foamable particles may contain other additives as necessary. Examples of other additives include plasticizers, flame retardant aids, antistatic agents, spreading agents, bubble regulators, fillers, colorants, weathering agents, anti-aging agents, lubricants, antifogging agents, and fragrances. It is done.
Plasticizers include aromatic hydrocarbons such as toluene and xylene, aliphatic hydrocarbons such as cyclohexane, hexane and heptane, adipic acid esters such as diisobutyl adipate, dioctyl adipate and diisononyl adipate, and glycerin diacetomonolaurate. Glycerin fatty acid esters such as glycerin fatty acid esters, dioctyl phthalate, diisononyl phthalate, diisobutyl phthalate and the like, phthalic acid esters such as liquid paraffin and white oil.

Examples of the flame retardant aid include organic peroxides such as 2,3-dimethyl-2,3-diphenylbutane, 3,4-dimethyl-3,4-diphenylhexane, dicumyl peroxide, and cumene hydroperoxide. .
Examples of the antistatic agent include polyoxyethylene alkylphenol ether, stearic acid monoglyceride, polyethylene glycol and the like.
Examples of the spreading agent include polybutene, polyethylene glycol, glycerin, and silicone oil.

  As the air conditioner, talc, mica, silica, diatomaceous earth, aluminum oxide, titanium oxide, zinc oxide, magnesium oxide, magnesium hydroxide, aluminum hydroxide, calcium hydroxide, potassium carbonate, calcium carbonate, magnesium carbonate, potassium sulfate, Barium sulfate, glass beads, polytetrafluoroethylene, tricalcium phosphate, magnesium pyrophosphate, zinc stearate, magnesium stearate and other metal soaps, ethylene bis stearamide, bisamide compounds such as methylene bis stearamide, stearamide Amide compounds such as 12-hydroxystearic acid amide, and fatty acid glycerides such as stearic acid triglyceride and stearic acid monoglyceride.

Examples of lubricants include metal soaps such as zinc stearate and magnesium stearate, bisamide compounds such as ethylenebisstearic acid amide and methylenebisstearic acid amide, stearic acid amides, amide compounds such as 12-hydroxystearic acid amide, stearic acid triglycerides, Examples include fatty acid glycerides such as stearic acid monoglyceride and hydroxystearic acid triglyceride, polyethylene wax, liquid paraffin, and white oil.
Examples of other additives include phenolic antioxidants, sulfur-based antioxidants, antioxidants such as phosphorus-based antioxidants, stabilizers such as hindered amines, and ultraviolet absorbers.

(6) Method for Producing Expandable Particles The scope of the present invention includes the above-described method for producing expandable particles.
In one embodiment of the invention,
Impregnating the seed particles with a styrene monomer in a dispersion obtained by dispersing seed particles containing a carbon material and a styrene resin in an aqueous medium;
A step of polymerizing the styrenic monomer simultaneously with or after impregnation;
There is provided a method for producing expandable styrenic resin particles comprising a step of impregnating a foaming agent simultaneously with or after polymerization. The flame retardant may be included in the seed particles, may be impregnated into the seed particles simultaneously with the styrene monomer, or may be impregnated simultaneously with the foaming agent.

The aqueous medium is not particularly limited as long as it is a liquid that can dissolve a water-soluble substance at room temperature, and examples thereof include water, lower alcohols having 1 to 4 carbon atoms, and mixtures thereof. Water is particularly preferable. The amount of the aqueous medium used can be appropriately set by those skilled in the art.
Resins other than styrenic resins may be contained in the resin obtained by polymerization. The kind, physical property, and content of such a resin are as described above.

  This embodiment is an embodiment in which expandable particles are produced using a suspension polymerization method, which is one of the typical methods for producing expandable particles in the art. Hereinafter, the suspension polymerization method will be described in more detail. However, the present embodiment is not limited to the conditions described below.

1. Suspension polymerization method In the suspension polymerization method, a polymerization initiator is dissolved in a styrene monomer, and together with water in which the suspending agent is dispersed, the temperature is increased in a reaction tank, polymerized, and then cooled to produce styrene resin foamable particles. Is the way to get. The method of adding a foaming agent during the polymerization and / or after the polymerization is called a one-stage method. The particles obtained by polymerization without adding a blowing agent are screened, and only the particles in the required particle size range are heated in water in which the suspending agent in the reaction vessel is dispersed, and the blowing agent is added here. The method of impregnating the particles is called a two-stage method (post-impregnation method). Further, small polystyrene particles (seed particles) are put into a reaction vessel containing water in which a suspending agent is dispersed, and after the temperature is raised, styrene monomer in which a polymerization initiator is dissolved is continuously added to the reaction vessel. The method of supplying and polymerizing and growing to the target particle size is called a seed polymerization method. In the seed polymerization method, the foaming agent is added during the polymerization and / or after the completion of the polymerization. The styrenic resin expandable particles of the present invention can be produced by any one of a one-stage method, a two-stage method (post-impregnation method), and a seed polymerization method. In addition, any method has an advantage that true spherical expandable particles can be obtained. A preferable production method includes a seed polymerization method. According to the seed polymerization method, polystyrene particles (master batch) containing a carbon material at a high concentration (for example, 20% by mass) can be used as seed particles, and there is an advantage that polymerization inhibition hardly occurs.

Hereinafter, the seed polymerization method of the suspension polymerization method will be described in more detail. However, the present embodiment is not limited to the conditions described below.
As this method, seed particles containing a carbon material and a styrene resin are absorbed with a styrene monomer and polymerized to obtain styrene resin particles, and a foaming agent is added during and / or after the polymerization. There is a method of obtaining expandable particles by injection. In this method, it is easy to obtain expandable particles containing a large amount of carbon material at the center.

(I) Seed particles The seed particles produced by a known method can be used. For example, by melting and kneading a carbon material and a styrene resin with an extruder, the seed particles are extruded into strands, and the strands are cut. An extrusion method for obtaining seed particles may be mentioned. In addition, the resin particles can be used for part or all of the seed particles. In the case of using a recovered product, production of seed particles by an extrusion method is suitable.
The average particle size of the seed particles can be adjusted as appropriate according to the average particle size of the resin particles. Further, the weight average molecular weight of the seed particles is not particularly limited, but is preferably 100,000 to 500,000, and more preferably 150,000 to 400,000.

  The addition amount of the carbon material is 0.5 to 25 parts by mass with respect to a total of 100 parts by mass of the addition amount of the styrene resin and the styrene monomer in the seed particles. That is, seed particles are added so that the amount of carbon material added is 0.5 to 25 parts by mass. When the addition amount is less than 0.5 parts by mass, the heat insulating property may not be sufficiently improved. On the other hand, when the addition amount exceeds 25 parts by mass, the foam film may be broken, so that the moldability may be reduced and the heat insulation may be inferior. A preferable addition amount of the carbon material is 0.5 to 15 parts by mass, and a more preferable addition amount of the carbon material is 0.5 to 10 parts by mass. Specific addition amounts include 0.5, 0.6, 0.7, 0.8, 0.9, 1, 1.01, 2, 2.56, 3, 3.13, 4, 5, 5.26, 6, 7, 7.52, 7.69, 8, 9, 10, 11, 11.11, 12, 13, 14, 15, 16, 17, 18, 19, 20 parts by mass, etc. It is done. In addition, the addition amount can be adjusted so as to have a value approximately the same as the content described for the expandable particles.

(Ii) Polymerization step Each monomer is absorbed in the seed particles by supplying a monomer mixture into a dispersion obtained by dispersing the seed particles in an aqueous medium, and then each monomer is polymerized. Styrenic resin particles can be obtained.
It is preferable that the addition amount of a styrene-type monomer is 50 mass parts or more with respect to 100 mass parts in total of the addition amount of a seed particle and a styrene-type monomer. When the amount is less than 50 parts by mass, sufficient foamability may not be obtained. A more preferable content rate is 60 mass parts or more, and a still more preferable content rate is 80 mass parts or more. In addition, the addition amount can be adjusted so as to have a value approximately the same as the content described for the expandable particles.
Examples of the aqueous medium include water and a mixed medium of water and a water-soluble solvent (for example, alcohol).

  Each monomer to be used may contain a polymerization initiator. The polymerization initiator is not particularly limited as long as it is conventionally used for monomer polymerization. For example, benzoyl peroxide, t-butyl peroxybenzoate, t-butyl peroxy-2-ethylhexanoate, lauryl peroxide, t-butyl peroxide, t-butyl peroxypivalate, t-butyl peroxyisopropyl Carbonate, t-butyl peroxyacetate, 2,2-t-butylperoxybutane, t-butylperoxy-3,3,5-trimethylhexanoate, di-t-butylperoxyhexahydroterephthalate, 2, Examples thereof include organic peroxides such as 5-dimethyl-2,5-di (benzoylperoxy) hexane and dicumyl peroxide, and azo compounds such as azobisisobutyronitrile and azobisdimethylvaleronitrile. Among these initiators, in order to reduce the residual monomer, two or more different polymerization initiators having a decomposition temperature of 80 to 120 ° C. for obtaining a half-life of 10 hours may be used in combination. In addition, a polymerization initiator may be used independently or 2 or more types may be used together.

  A suspension stabilizer may be included in the aqueous medium to stabilize the dispersion of monomer droplets and seed particles. The suspension stabilizer is not particularly limited as long as it is conventionally used for monomer suspension polymerization. Examples thereof include water-soluble polymers such as polyvinyl alcohol, methyl cellulose, polyacrylamide, and polyvinyl pyrrolidone, and poorly soluble inorganic compounds such as tricalcium phosphate, magnesium pyrophosphate, magnesium oxide, and hydroxyapatite. And when using a sparingly soluble inorganic compound as said suspension stabilizer, it is preferable to use an anionic surfactant together, and as such anionic surfactant, for example, fatty acid soap, N-acylamino acid or its Salts, carboxylates such as alkyl ether carboxylates, alkylbenzenesulfonates, alkylnaphthalenesulfonates, sulfonates such as dialkylsulfosuccinates, alkylsulfoacetates, α-olefinsulfonates; higher alcohol sulfates Ester salts, secondary higher alcohol sulfates, sulfates such as alkyl ether sulfates, polyoxyethylene alkylphenyl ether sulfates, etc .; phosphates such as alkyl ether phosphates, alkyl phosphates, etc. Is mentioned.

  Although a polymerization process changes with monomer types to be used, a polymerization initiator seed | species, superposition | polymerization atmosphere, etc., it is normally performed by maintaining 70-130 degreeC heating for 3 to 10 hours. The polymerization step may be performed while impregnating the monomer. In the polymerization step, the total amount of the monomers used may be polymerized in one step, or may be polymerized in two or more steps (including polymerization during the production of seed particles).

(Iii) Foaming agent impregnation step Foamable particles can be obtained by impregnating the above styrene resin particles with a foaming agent.
The impregnation may be performed wet simultaneously with the polymerization, or may be performed wet or dry after the polymerization. When it is carried out in a wet manner, it may be carried out in the presence of a suspension stabilizer and a surfactant exemplified in the polymerization step. The impregnation temperature of the foaming agent is preferably 60 to 120 ° C. When the temperature is lower than 60 ° C., the time required for impregnating the resin particles with the foaming agent becomes long, and the production efficiency may decrease. On the other hand, when the temperature is higher than 120 ° C., the resin particles may be fused to generate bonded particles. A more preferable impregnation temperature is 70 to 110 ° C.

  The amount of the foaming agent to be impregnated is preferably in the range of 2 to 12 parts by mass with respect to 100 parts by mass of the styrene resin obtained by polymerization. When the amount is less than 2 parts by mass, a foamed molded article having a desired density may not be obtained from the expandable particles. In addition, since the effect of increasing the secondary foaming power at the time of in-mold foam molding is reduced, the appearance of the foam molded article may not be good. When the amount is more than 12 parts by mass, the time required for the cooling step in the production process of the foamed molded product may become long and the productivity may decrease. A more preferable content is 3 to 10 parts by mass, a still more preferable content is 4 to 9 parts by mass, and a most preferable content is 5 to 8 parts by mass. In addition, the quantity of the foaming agent to be impregnated can be adjusted so as to have a value almost the same as the content described for the foamable particles. Further, as described above, a foaming aid may be used in combination with a foaming agent. The types of foaming aids and the like are as described above, and the amount added can be appropriately set by those skilled in the art.

In another embodiment of the invention,
A step of melt-kneading the carbon material and the styrene resin;
Injecting a foaming agent into the molten resin obtained in the melt-kneading step;
And a step of extruding, cutting, and then solidifying the molten resin obtained in the blowing agent injection step into a liquid. The flame retardant can be added to the styrenic resin during melt mixing.

  This embodiment is an embodiment in which expandable particles are produced using a melt extrusion method which is one of the typical methods for producing expandable particles in the technical field. Hereinafter, although the melt extrusion method will be described in more detail, the present embodiment is not limited to the conditions described below.

2. Melt extrusion method In the melt extrusion method, polystyrene pellets are supplied to a resin supply device, a foaming agent is press-fitted and kneaded into the polystyrene resin melted in the resin supply device, and the molten resin containing the foaming agent is added to the tip of the resin supply device. It extrudes from the small hole of the die | dye attached to, and it cools after that, and obtains a styrene-type resin foamable particle. A method of directly extruding from a small hole of a die into a cooling liquid, cutting the extrudate with a rotary blade immediately after the extrusion, and cooling the cut particles in the cooling liquid is called a hot cut method. The strand is extruded from the small holes of the die into air in the form of strands, guided into the cooling water tank before the strands are foamed, and after the strands are cooled in the cooling water tank, they are cut into columnar particles. This is called the method (cold cut method). The styrenic resin expandable particles of the present invention can be produced by either the hot cut method or the strand cut method (cold cut method). In addition, any method has an advantage that an arbitrary amount of carbon material can be easily contained in the particles. Further, the carbon material can be uniformly contained in the expandable particles. A preferable production method includes a hot cut method. According to the hot cut method, there is an advantage that substantially spherical expandable particles can be obtained.

Hereinafter, the hot-cut method of the melt extrusion method will be described in more detail, but the present embodiment is not limited to the conditions described below.
In this method, a foaming agent is press-fitted and kneaded into the polystyrene resin melted in the resin supply device, and the molten resin containing the foaming agent is injected into the cooling liquid from the small hole of the die attached to the tip of the resin supply device. The extrudate extruded directly into the cooling liquid is cut with a rotary blade in the cooling liquid, and the extrudate is cooled and solidified by contact with the liquid to obtain expandable particles.
In this method, for example, the following manufacturing apparatus can be used. That is, an extruder as a resin supply device, a die having a large number of small holes attached to the tip of the extruder, a raw material supply hopper for charging the raw material into the extruder, and a blowing agent supply port for the molten resin in the extruder A high-pressure pump for press-fitting the foaming agent through, a cutting chamber in which cooling water is provided in contact with the resin discharge surface provided with a small hole in the die, and the cooling water is circulated and supplied into the chamber, and a small hole in the die A cutter (high-speed rotating blade) that is rotatably provided in the cutting chamber so as to cut the resin extruded from the cutting chamber, and the foaming particles carried along with the flow of cooling water from the cutting chamber are separated from the cooling water. A dehydration dryer with a solid-liquid separation function that obtains foamable particles by dehydration and drying, a water tank for storing cooling water separated by the dehydration dryer with a solid-liquid separation function, and a cooling chamber for cooling water in this water tank A high-pressure pump for sending include manufacturing apparatus that includes a storage container for storing the dewatered dried expandable particles at solid-liquid separating function dehydrating dryer.

  An example of a procedure for producing expandable particles using the production apparatus will be described. First, raw polystyrene resin and carbon material are put into an extruder from a raw material supply hopper. The raw polystyrene resin may be mixed in advance in the form of pellets or granules and then charged from one raw material supply hopper. For example, when multiple lots are used, the supply amount for each lot may be reduced. A plurality of adjusted raw material supply hoppers may be charged and mixed in an extruder. Also, when using a combination of recycled materials from multiple lots, mix the raw materials from multiple lots in advance and remove foreign matter using appropriate sorting means such as magnetic sorting, sieving, specific gravity sorting, and air blowing sorting. It is preferable to keep it. The carbon material may be fed into the extruder as a master batch prepared by melt-mixing with a polystyrene resin in advance.

  The addition amount of the carbon material is 0.5 to 25 parts by mass with respect to 100 parts by mass of the addition amount of the styrene resin. When the addition amount is less than 0.5 parts by mass, the heat insulating property may not be sufficiently improved. On the other hand, when the addition amount exceeds 25 parts by mass, the foam film may be broken, so that the moldability may be reduced and the heat insulation may be inferior. A preferable addition amount of the carbon material is 0.5 to 15 parts by mass, and a more preferable addition amount of the carbon material is 0.5 to 10 parts by mass. Specific addition amounts include 0.5, 0.6, 0.7, 0.8, 0.9, 1, 1.01, 2, 2.56, 3, 3.13, 4, 5, 5.26, 6, 7, 7.52, 7.69, 8, 9, 10, 11, 11.11, 12, 13, 14, 15, 16, 17, 18, 19, 20 parts by mass, etc. It is done. In addition, the addition amount can be adjusted so as to have a value approximately the same as the content described for the expandable particles.

  After supplying the raw material into the extruder, the polystyrene resin is heated and melted, and while the molten resin is transferred to the die side, the blowing agent is injected from the blowing agent supply port with a high-pressure pump, and the blowing agent is mixed into the molten resin. The melt is moved to the tip side while further kneading through a screen for removing foreign substances provided as necessary in the extruder, and the melt added with the foaming agent is pushed out from a small hole in a die attached to the tip of the extruder. .

  Those skilled in the art can appropriately set the conditions for injecting the foaming agent into the molten resin obtained by melt kneading. The addition amount of the foaming agent is preferably in the range of 2 to 12 parts by mass with respect to 100 parts by mass of the molten resin. When the amount is less than 2 parts by mass, a foamed molded article having a desired density may not be obtained from the expandable particles. In addition, since the effect of increasing the secondary foaming power at the time of in-mold foam molding is reduced, the appearance of the foam molded article may not be good. When the amount is more than 12 parts by mass, the time required for the cooling step in the production process of the foamed molded product may become long and the productivity may decrease. A more preferable content is 3 to 10 parts by mass, a still more preferable content is 4 to 9 parts by mass, and a most preferable content is 5 to 8 parts by mass. In addition, the quantity of the foaming agent to inject | pour can be adjusted so that it may become a value substantially comparable as content described about the expandable particle. Further, as described above, a foaming aid may be used in combination with a foaming agent. The type of foaming aid is as described above, and the amount of foaming aid to be added can be appropriately set by those skilled in the art.

A resin discharge surface with a small hole in the die is placed in a cutting chamber in which cooling water is circulated and supplied into the chamber, and a cutter is provided in the cutting chamber so that the resin extruded from the small hole in the die can be cut. Is rotatably provided. When the melted product with foaming agent added is extruded through a small hole in the die attached to the tip of the extruder, the melt is cut into granules and simultaneously cooled in contact with cooling water to solidify while suppressing foaming. It becomes an expandable particle.
The formed expandable particles are transferred from the cutting chamber along with the flow of cooling water to the dehydrating dryer with a solid-liquid separation function, where the expandable particles are separated from the cooling water and dehydrated and dried. The dried expandable particles are stored in a storage container.
In addition, when adding a flame retardant, the addition time is not particularly limited, but it is preferably added to the extruder together with the raw material.

3. Other methods As an example of other methods, in the melt extrusion method, after obtaining styrene resin particles without press-fitting a foaming agent, the particles are foamed by a suspension polymerization two-stage method (post-impregnation method). Examples thereof include a method of producing a styrene resin foamable particle by impregnating an agent, or a method of producing a styrene resin foamable particle by a seed polymerization method of a suspension polymerization method using this particle as a seed particle. Also by these methods, the styrene resin expandable particles of the present invention can be produced. In addition, any method has an advantage that an arbitrary amount of carbon material can be easily contained in the particles by the melt extrusion method. As a preferable production method, there is a method in which particles containing no foaming agent are obtained by a melt extrusion method, and then styrene resin foamable particles are produced by seed polymerization using the particles as seed particles. According to this method, polystyrene particles (masterbatch) containing a carbon material at a high concentration (for example, 20% by mass) can be used as seed particles, and there is an advantage that polymerization inhibition is unlikely to occur. There is an advantage that particles can be obtained.

(Styrene resin foam particles)
The styrene resin expanded particles (hereinafter referred to as expanded particles) include a styrene resin, a carbon material, and a flame retardant, and the flame retardant includes a phosphorus flame retardant having a phosphorus content of 7% by mass or more. A flame retardant is characterized by containing 3-10 mass parts with respect to 100 mass parts of styrene resin. The foamed particles can be obtained by foaming (pre-foaming) the foamable particles, and correspond to pre-foamed particles for producing the following foamed molded product.
The styrene resin, the carbon material, and the flame retardant constituting the expanded particles are the same as the expandable particles.

The expanded particles preferably have a bulk density of 0.009 to 0.400 g / cm ³ . When the bulk density is larger than 0.400 g / cm ³ , the lightness of the foamed molded product may be lowered. When the bulk density is less than 0.009 g / cm ³ , the heat insulating performance and mechanical strength of the foamed molded product may be deteriorated. More preferred bulk density of 0.010~0.100g / cm ^3, even more preferred bulk density of 0.01-0.04 / cm ^3, more preferred bulk density 0.011～0.032G / cm ^3, and most preferred bulk density is 0.014~0.029g / cm ^3. Specific bulk density values are 0.009, 0.010, 0.011, 0.012, 0.0125, 0.013, 0.014, 0.015, 0.02, 0.03, It may be 0.033, 0.035, 0.04, 0.1, 0.2, 0.3, 0.4 g / cm ³ or the like.

  The average diameter (average cell diameter) of the bubbles constituting the expanded particles is preferably 50 to 1000 μm. When the average cell diameter is less than 50 μm, the heat insulating property may be lowered. When the average bubble diameter is larger than 1000 μm, the mechanical strength may be lowered. The average cell diameter is more preferably from 100 to 600 μm, still more preferably from 200 to 300 μm. Specific values of the average cell diameter may be 50, 100, 150, 200, 250, 300, 350, 400, 500, 600, 700, 800, 900, 1000 μm, and the like.

The expanded particles are obtained by expanding the expandable particles to a desired bulk density using water vapor or the like.
The expanded particles may be aged, for example, at normal pressure, prior to the subsequent foam molding process. The aging temperature of the expanded particles is preferably 20 to 60 ° C. When the aging temperature is low, the aging time of the expanded particles may be long. On the other hand, if it is high, the foaming agent in the foamed particles may dissipate and the moldability may deteriorate.

(Styrenic resin foam molding)
A styrene resin foam molded body (hereinafter referred to as a foam molded body) is a foam molded body including a styrene resin, a carbon material, and a flame retardant, and is composed of a plurality of styrene resin foam particles fused together. Includes a phosphorus-based flame retardant having a phosphorus content of 7% by mass or more, and the phosphorus-based flame retardant is included in an amount of 3 to 10 parts by mass with respect to 100 parts by mass of the styrene resin. This foam-molded product can be obtained by foam-molding the foamed particles.
The styrenic resin, the carbon material and the flame retardant constituting the foam molded body are the same as the foamable particles.

Preferably, the foamed molded product is obtained by the following formula in the surface color difference measurement based on JIS Z8729-2004 “Color Display Method—L ^* a ^* b ^* Color System”:
31 ≦ ΔE ′ = L ^* + | a ^* | + | b ^* | ≦ 50
(Where ΔE ′ is blackness, L ^* is lightness, a ^* and b ^* are color coordinates)
Satisfies the relational expression indicated by More preferable ΔE ′ is 32 ≦ ΔE ′ ≦ 45, and still more preferable ΔE ′ is 32 ≦ ΔE ′ ≦ 35. In the case of ΔE ′ <31, the heat insulating property may be lowered. On the other hand, in the case of ΔE ′> 50, the heat insulating property may be lowered. (1) In order to reduce ΔE ′, depending on whether a carbon material closer to black is selected, the content of the carbon material in the foam molded body is increased, or the density of the foam molded body is increased. Can be achieved. (2) In order to increase ΔE ′, depending on whether a carbon material closer to gray is selected, the content of the carbon material in the foam molded body is reduced, or the density of the foam molded body is reduced. Can be achieved. Specific blackness values include 31, 32, 33, 34, 35, 38, 40, 43, 44, 45, 46, 47, 48, 49, 50, and the like. Detailed blackness measurement methods are described in the Examples.

  The foamed molded product may further contain a flame retardant. As the flame retardant, the same ones described for the above expandable particles can be used, but tetrabromocyclooctane or tetrabromobisphenol A-bis (2,3-dibromo-2-methylpropyl ether) is particularly preferred. preferable. Content of a flame retardant is 0.5-10 mass parts with respect to 100 mass parts of foaming moldings, Preferably it is 2-8 mass parts. Specific values of the flame retardant content include 0.5, 1, 2, 3, 4, 5, 6, 7, 8, 9, 10 parts by mass, and the like.

  Preferably, the foam-molded article is a heat insulating material for living space in which the total content of aromatic organic compounds composed of a styrene monomer, ethylbenzene, isopropylbenzene, normal propylbenzene, xylene, toluene, and benzene is less than 2000 ppm. If the total content of the aromatic organic compound is less than 2000 ppm, it is possible to cope with sick house syndrome, which has been recently requested, and to provide a more comfortable living space. More preferably, it is 1750 ppm or less, More preferably, it is 1500 ppm or less, Most preferably, it is 500 ppm or less, Most preferably, it is 300 ppm or less. By selecting a resin raw material with a low content of aromatic organic compound consisting of styrene monomer, ethylbenzene, isopropylbenzene, normal propylbenzene, xylene, toluene, benzene as the raw material polystyrene resin, during the manufacturing process Thus, it is possible to obtain styrene resin foamable particles, foamed particles, foamed molded products, and heat insulating materials for living spaces without mixing the aromatic organic compound. In the case of foamed particles, foamed molded products, and heat insulating materials for living spaces obtained from the same styrenic resin foamable particles, the total content of the aromatic organic compounds is a comparable value. Styrenic resin expandable particles having a total content of the aromatic organic compound of less than 2000 ppm are suitable for producing a heat insulating material for living spaces. In addition, a melt extrusion method is preferable as a production method for obtaining styrene resin expandable particles having a small total content of the aromatic organic compound. Detailed methods for measuring the total content of aromatic organic compounds are described in the Examples.

The foamed molded body preferably has a density of 0.010 to 0.400 g / cm ³ . If the density is greater than 0.400 g / cm ³ , the lightness may be reduced. When the density is less than 0.010 g / cm ³ , the heat insulating performance and mechanical strength may be lowered. A more preferable density is 0.011 to 0.100 g / cm ³ , an even more preferable density is 0.012 to 0.04 g / cm ³ , and a still more preferable density is 0.0125 to 0.033 g / cm ³ . The most preferable density is 0.015 to 0.030 g / cm ³ . Specific bulk density values are 0.009, 0.010, 0.011, 0.012, 0.0125, 0.013, 0.014, 0.015, 0.02, 0.03, It may be 0.033, 0.035, 0.04, 0.1, 0.2, 0.3, 0.4 g / cm ³ or the like.

  It is preferable that the average diameter (average bubble diameter) of the bubbles constituting the foamed molded product is 50 to 1000 μm. When the average cell diameter is less than 50 μm, the heat insulating property may be lowered. When the average bubble diameter is larger than 1000 μm, the mechanical strength may be lowered. The average cell diameter is more preferably from 100 to 600 μm, still more preferably from 200 to 300 μm. Specific values of the average cell diameter may be 50, 100, 150, 200, 250, 300, 350, 400, 500, 600, 700, 800, 900, 1000 μm, and the like.

  The foamed molded article preferably exhibits a thermal conductivity of 0.034 W / mk or less. When the thermal conductivity exceeds 0.034 W / mk, it may not be possible to provide a foamed molded article having sufficient heat insulation. More preferable thermal conductivity is 0.033 W / mk or less, and still more preferable thermal conductivity is 0.32 W / mk or less. Specific values of thermal conductivity are 0.0340, 0.0339, 0.0338, 0.0337, 0.0336, 0.0335, 0.0334, 0.0333, 0.0332, 0.0331. 0.0330, 0.0329, 0.0328, 0.0327, 0.0326, 0.0325, 0.0324, 0.0323, 0.0322, 0.0321, 0.0320, 0.0319, 0 0.0318, 0.0317, 0.0316, 0.0315, 0.0314, 0.0313, 0.0312, 0.0311, 0.0310, 0.0309, 0.0308, 0.0307, 0.0306 , 0.0305, 0.0304, 0.0303, 0.0302, 0.0301, 0.0300, and the like.

The foamed molded product preferably exhibits a water absorption of less than 0.5 g / 100 cm ² . When the amount of water absorption exceeds 0.5 g / 100 cm ² , the heat insulating property may be lowered. More preferable water absorption is less than 0.4 g / 100 cm ² , still more preferable water absorption is less than 0.3 g / 100 cm ² , and even more preferable water absorption is less than 0.2 g / 100 cm ² . Specific water absorption values include 0.5, 0.45, 0.4, 0.35, 0.3, 0.25, 0.2, 0.15, 0.1, 0.05, etc. Is mentioned.

Preferably, the foamed molded article exhibits a ratio A / B of 0.8 to 2.0 in absorbance A at a wave number of 1000 cm ⁻¹ and absorbance B at a wave number of 500 cm ⁻¹ obtained by transmission infrared analysis. When the absorbance ratio A / B <0.8 or when the absorbance ratio A / B> 2.0, sufficient heat insulation may not be obtained. (1) The absorbance ratio A / B can be reduced by increasing the amount of carbon material added. (2) Increasing the absorbance ratio A / B can be achieved by increasing the amount of carbon material added, reducing the bubble diameter, or the like. A more preferred absorbance ratio A / B is 0.81 to 1.80, and a further preferred absorbance ratio A / B is 0.82 to 1.75. Specific values of the absorbance ratio A / B are 0.8, 0.81, 0.82, 0.83, 0.84, 0.85, 0.9, 0.95, 1.0, 1 .1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.75, 1.76, 1.77, 1.78, 1.79, 1.8 1.85, 1.9, 1.95, 2.0 and the like.

Absorbance A means the absorbance at a wave number of 1000 cm ⁻¹ obtained by transmission infrared analysis. The preferred absorbance A is 0.8 or more. When the absorbance A is less than 0.8, the heat insulation is poor. More preferable absorbance A is 0.95 or more. Specific values of absorbance A include 0.8, 0.81, 0.82, 0.83, 0.84, 0.85, 0.86, 0.87, 0.88, 0.89, 0.9, 0.91, 0.92, 0.93, 0.94, 0.95, 0.96, 0.97, 0.98, 0.99 and the like.

Further, the absorbance B means the absorbance at a wave number of 500 cm ⁻¹ obtained by transmission infrared analysis. The preferred absorbance B is 0.5 or more. When the absorbance B is less than 0.5, the heat insulating property is lowered. More preferable absorbance B is 0.55 or more. Specific values of absorbance B include 0.5, 0.51, 0.52, 0.53, 0.54, 0.55, 0.56, 0.57, 0.58, 0.59, 0.6, 0.65, 0.7 and the like.
Detailed methods for measuring absorbances A and B are described in the Examples.

For example, the foamed molded body is filled with foamed particles in a closed mold having a large number of small holes, heated and foamed with a heat medium (for example, pressurized water vapor) to fill the voids between the foamed particles, and It can manufacture by fusing together and integrating. At that time, the density of the foamed molded product can be adjusted, for example, by adjusting the filling amount of the pre-expanded particles in the mold.
Heating foaming can be performed, for example, by heating for 5 to 50 seconds with a heat medium of 110 to 150 ° C. Under these conditions, good fusing property between the expanded particles can be secured. More preferably, the heat-foaming molding can be performed by heating for 10 to 50 seconds with a heating medium (for example, water vapor) at a molding vapor pressure (gauge pressure) of 0.06 to 0.08 MPa and 90 to 120 ° C. .

  The foamed molded product can be used for various applications that require heat insulation. For example, wall insulation, floor insulation, roof insulation, automotive insulation, warm water tank insulation, piping insulation, solar system insulation, water heater insulation, food and industrial products, etc. It can be used for containers, packing materials for fish and agricultural products, embankment materials, tatami core materials, etc. The foamed molded product can take a shape corresponding to the intended use. In particular, it can be suitably used as a heat insulating material for living spaces such as a heat insulating material for walls, a heat insulating material for floors, a heat insulating material for roofs, and a heat insulating material for automobiles.

  EXAMPLES Next, although an Example is given and this invention is demonstrated in more detail, this invention is not limited to these.

<Volume resistivity of carbon material measured using polyethylene resin>
Volume resistivity here is the raw material carbon material, or when the raw material carbon material is added to the masterbatch, expandable particles, expanded particles, and foamed molded product, the masterbatch, expandable particles, The carbon material taken out by removing the styrene resin in the foamed particles and the foamed molded article with toluene as an organic solvent was melt kneaded with the polyethylene resin (carbon material: polyethylene resin = 1: 4 (mass ratio). )), The value obtained by measuring the surface of the kneaded product.
Specifically, a polyethylene resin and a carbon material that are sufficiently melt-kneaded using an extruder and formed into a film shape are measured by the method described in JIS K6911: 1995 “General Test Method for Thermosetting Plastics”. To do. That is, using a test apparatus (advantest digital ultra-high resistance / microammeter R8340 and resiliency chamber R12702A), an electrode is crimped to a sample sample with a load of about 30 N, and the resistance after charging at 500 V for 1 minute. The value is measured and calculated by the following formula. The sample sample has a width of 100 × length of 100 × original thickness (10 or less) mm. After conditioning for 24 hours or more at a temperature of 20 ± 2 ° C. and a humidity of 65 ± 5%, the test environment is measured at a temperature of 20 ± 2 ° C. and a humidity of 65 ± 5%. The number of test pieces is five, and the average value is the volume resistivity (Ω · cm) of the carbon material.
ρv = (πd ² / 4t) × Rv
ρv: Volume resistivity (Ω · cm)
d: outer diameter of inner circle of surface electrode (cm)
t: thickness of test specimen (cm)
Rv: Volume resistance (Ω)

<Volume resistivity of carbon material measured using polystyrene resin>
Volume resistivity here is the raw material carbon material, or when the raw material carbon material is added to the masterbatch, expandable particles, expanded particles, and foamed molded product, the masterbatch, expandable particles, The carbon material taken out by removing the styrene resin in the foamed particles and the foamed molded article with toluene as an organic solvent was melt kneaded with the polystyrene resin (carbon material: polystyrene resin = 1: 4 (mass ratio). )), The value obtained by measuring the surface of the kneaded product.
Specifically, a resistivity test using a four-probe method of conductive plastic is performed on a plate-like molded body of a kneaded product of carbon material and polystyrene resin (carbon material: polystyrene resin = 1: 4 (mass ratio)). Measurement is performed in accordance with the method (JIS K7194). The test apparatus uses a low resistivity meter Lorester GP MCP-T600 manufactured by Mitsubishi Chemical Corporation, and the sample sample has a width of 80 × length of 50 × original thickness (20 or less) mm. The sample sample is conditioned at a temperature of 20 ± 2 ° C. and a humidity of 65 ± 5% for 24 hours or more, and then measured as a test environment at a temperature of 20 ± 2 ° C. and a humidity of 65 ± 5%. The volume resistivity is calculated from the following equation by measuring the resistance values at five measurement positions according to JIS K 7194 on the surface of the sample. The average value is defined as the volume resistivity (Ω · cm) of the carbon material.
ρv = V / I × RCF × t
ρv: Volume resistivity (Ω · cm)
V / I: Resistance (Ω)
RCF: Correction coefficient depending on measurement position and sample thickness t: Thickness of test piece (cm)

<Weight average molecular weight>
A weight average molecular weight means the polystyrene (PS) conversion average molecular weight measured using gel permeation chromatography (GPC). Specifically, 3 mg of the sample was allowed to stand and dissolved in 10 mL of tetrahydrofuran (THF) for 72 hours (complete dissolution), and the resulting solution was subjected to a non-aqueous 0.45 μm chromatodisc (13N) manufactured by Kurashiki Boseki Co., Ltd. Filter and measure. The average molecular weight of the sample is determined from a standard polystyrene calibration curve measured and prepared in advance. The chromatographic conditions are as follows.

(Measurement condition)
Equipment used: High-speed GPC equipment: HLC-8320GPC EcoSEC system manufactured by Tosoh Corporation (with built-in RI detector)
Guard column: Tosoh TSKguardcolumn SuperHZ-H (4.6 mm ID × 2 cmL) × 1 Column: Tosoh TSKgel SuperHZM-H (4.6 mm ID × 15 cmL) × 2 Column temperature: 40 ° C.
System temperature: 40 ° C
Mobile phase: Tetrahydrofuran Mobile phase flow rate: Sample side 0.175 mL / min, Reference side 0.175 mL / min Detector: RI detector Sample concentration: 0.3 g / L
Injection volume: 50 μL
Measurement time: 0-25 minutes Runtime: 25 minutes Sampling pitch: 200 msec

(Create a calibration curve)
As standard polystyrene samples for calibration curves, the weight average molecular weights of trade names “TSK standard POLYSTYRENE” manufactured by Tosoh Corporation are 5,480,000, 3,840,000, 355,000, 102,000, 37,900, 9 , 100, 2,630, and 500, and standard polystyrene samples having a weight average molecular weight of 1,030,000 with a trade name “Shodex STANDARD” manufactured by Showa Denko KK are used.

  The method of creating a calibration curve is as follows. The above standard polystyrene samples for calibration curves are group A (with a weight average molecular weight of 1,030,000), group B (weight average molecular weights of 3,840,000, 102,000, 9,100, 500) and group C. (The weight average molecular weight is 5,480,000, 355,000, 37,900, 2,630). Group A is weighed 5 mg and then dissolved in 20 mL of tetrahydrofuran, Group B is also weighed 5 to 10 mg each and then dissolved in 50 mL of tetrahydrofuran, and Group C is also weighed 1 to 5 mg each and then dissolved in 40 mL of tetrahydrofuran. The standard polystyrene calibration curve was prepared by injecting 50 μL of the prepared A, B, and C solutions, and using the retention time obtained after the measurement, a calibration curve (third-order equation) was transferred to the HLC-8320GPC dedicated data analysis program GPC workstation (EcoSEC-WS). The measurement curve is obtained by using the calibration curve.

<Measuring method of average primary particle diameter (average particle diameter)>
Using a cutter knife, the center of the expandable particles is cut out, and the skin portion of the expanded particles and the expanded molded body is cut out as a measurement sample. After the cut sample is fixed to the cryosample table with an adhesive, it is ultrathin using an ultramicrotome (LEICA ULTRACUT UCT manufactured by Leica Microsystems) and a frozen section preparation system (LEICA EM FCS manufactured by Leica Microsystems). A section (thickness 90 nm) is prepared. Next, using a transmission electron microscope (H-7600, manufactured by Hitachi High-Technologies Corporation), an ultrathin section is photographed (photographing magnification: 50,000 times). At least 200 carbon materials are photographed per sample, the diameter of each particle is measured, and the average value thereof is calculated. In addition, it is desirable to measure the part which can be recognized clearly as a primary particle, without an outer edge missing.

<Measurement method of amount of carbon material in resin>
The amount of carbon material in the resin is measured using a differential thermothermal gravimetric simultaneous measurement apparatus TG / DTA6200 type (manufactured by SII Nano Technology). For example, in the case of foamable particles, foamed particles, foamed molded products, etc. containing a foaming agent or an organic solvent in the resin, the foaming agent in the resin can be left in a constant temperature bath at 120 ° C. for 2 hours. Samples from which organic solvents have been removed are used as measurement samples. About 15 mg of the sample is filled so that there is no gap at the bottom of the platinum measurement container, and the measurement is performed using alumina as a reference material. As temperature conditions, the temperature is raised from 30 ° C. to 520 ° C. at a rate of 10 ° C./min and a nitrogen gas flow rate of 230 mL / min, and then raised from 520 ° C. to 800 ° C. at a rate of 10 ° C./min and an Air flow rate of 160 mL / min. A TG curve (vertical axis: TG (%), horizontal axis: temperature (° C)) is obtained, and based on this, the weight loss of the sample when the temperature is raised from 520 ° C to 800 ° C is calculated, and the carbon material amount w (mass%) ).
At this time, the mass ratio between the carbon material and the styrene resin has the following relationship.
Carbon material: Styrenic resin = 1: (100 / w-1)
w: The value of mass% of the carbon material obtained from the measurement result In addition, if the foamed particles, the foamed molded product, and the heat insulating material for living space obtained from the same styrenic resin foamable particles, the carbon material and the styrenic resin The mass ratio is a similar value.

<Bulk density of expanded particles>
The bulk density of the expanded particles is measured according to JIS K6911: 1995 “General Test Method for Thermosetting Plastics”. Specifically, first, Wg is collected using the expanded particles as a measurement sample, and the measurement sample is naturally dropped into a measuring cylinder. The volume Vcm ³ of the measurement sample dropped into the graduated cylinder is measured using an apparent density measuring instrument based on JIS K6911. By substituting Wg and Vcm ³ into the following formula, the bulk density of the expanded particles is calculated.
Bulk density of expanded particles (g / cm ³ ) = mass of measurement sample (W) / volume of measurement sample (V)

<Density of foam molding>
The mass (a) and volume (b) of a test piece (example 75 × 300 × 30 mm) cut out from a foamed molded product (after being molded and dried at 40 ° C. for 20 hours or more) each have three or more significant figures. Then, the density (g / cm ³ ) of the foamed molded product is obtained by the formula (a) / (b).

<Average bubble diameter>
The average cell diameter is measured according to the test method of ASTM D2842-69. Using a razor blade, obtain a cross-section of the molded body of the foamed particles and any part of the foamed molded body. Using this scanning plane, a scanning electron microscope (JSM-6360LV, manufactured by NEC Corporation) is used to create an image magnified 100 times.
Next, a straight line of 60 mm is drawn at an arbitrary position in the range of 20% in the radial direction of the expanded particle from the expanded particle interface on the image of the cut surface. The number of bubbles on the straight line is counted, and the average chord length (t) of the bubbles is calculated by the following equation.
Average chord length t (μm) = 60 / (number of bubbles × magnification multiple of image)
The average bubble diameter (D) of this bubble is calculated by the following formula.
Average bubble diameter D (μm) = t / 0.616
The above operation is performed with N number of 10, and the average value is defined as the average bubble diameter.

<Thermal conductivity of foamed molded product>
A test piece having a rectangular parallelepiped shape having a length of 200 mm, a width of 200 mm, and a thickness of 30 mm is cut out from the foamed molded body. Next, the cut out test piece is allowed to stand for 72 hours in a constant temperature bath at 60 ° C. to remove the foaming agent contained in the foamed molded product. Thereafter, curing is performed for 24 hours or more at a temperature of 23 ° C. ± 1 ° C. and a humidity of 50 ± 10% to obtain a test piece for measuring thermal conductivity. The thermal conductivity (W / m · K) of the test specimen for measurement is measured at a measurement temperature of 23 ° C. by a flat plate heat flow meter method according to JIS A1412-2 (1999 “Foamed plastic insulation material”). Rate is an indicator of thermal insulation.
From the value of the obtained thermal conductivity (W / m · K), the heat insulation is evaluated according to the following criteria.
0.0310 (W / m · K) or less: Thermal insulation is further improved (A)
0.0310 and 0.0320 or less: better thermal insulation (B)
More than 0.0320 and 0.0340 or less: Excellent heat insulation (C)
Exceeds 0.0340 (W / m · K): poor heat insulation (D)
In the present invention, the value of the thermal conductivity of the foamed molded product is a value after removing the foaming agent contained in the foamed molded product. When measured without removing the foaming agent in the foamed molded product, the thermal conductivity of the foaming agent such as butane and pentane is lower than the thermal conductivity of air, so the value of the thermal conductivity of the foamed molded product is , About 0.002 (W / m · K).

<Specific surface area>
The specific surface area (m ² / g) of the carbon material is measured according to ASTM D-6556.

<Longest diameter of agglomerates of carbon material in foamable particles, foamed particles and foamed molded product>
Using a cutter knife, the expandable particles are cut out at the center of the particles, and the expanded particles and the expanded molded body are cut out of the skin portion to be used as a measurement sample. After the cut sample is fixed to the cryosample table with an adhesive, it is ultrathin using an ultramicrotome (LEICA ULTRACUT UCT manufactured by Leica Microsystems) and a frozen section preparation system (LEICA EM FCS manufactured by Leica Microsystems). A section (thickness 90 nm) is prepared. Subsequently, using a transmission electron microscope (H-7600, manufactured by Hitachi High-Technologies Corporation), an ultrathin section is photographed (imaging magnification: 10,000 times). Photograph at least 200 independent separate aggregates per sample. In the photographed image, the longest diameter of the distance between any two points on the outer edge of the aggregate that the primary particles of the carbon material appear to overlap was taken as the longest diameter of the aggregate, and the average value thereof was calculated. The longest diameter connecting the two points is set so as to always overlap the primary particles on the photograph. That is, the longest diameter does not pass through the background of the photograph.

<Blackness of foam molding>
The blackness ΔE ′ of the foamed molded product is evaluated by color difference measurement based on JIS Z8729-2004 “Color Display Method—L ^* a ^* b ^* Color System”.
For the measurement, a color difference meter (manufactured by Konica Minolta, model: CR-400) and a standard white plate calibration plate (Y: 94.3, x: 0.3144, y: 0.3208) are used for standardization.
Specifically, from any 10 points on the vertical and horizontal surfaces of the foamed molded product, the measurement area was measured as φ8 mm, and the average value was calculated from the lightness L ^* value, color coordinate a ^* value, and b ^* value. ΔE ′ is calculated as the degree.
ΔE ′ = L ^* + | a ^* | + | b ^* |
From the obtained ΔE ′, the blackness is evaluated according to the following criteria.
31 ≦ ΔE ′ ≦ 50: Good (◯)
ΔE ′ <31 and 50 <ΔE ′: Defect (×)

<Measurement method of absorbance>
A sample having a thickness of 1.0 mm ± 0.1 mm is obtained from an arbitrary portion of the obtained foamed molded article. Next, the absorbance of the transmitted infrared of the sample is measured by the following method.
・ Fourier transform infrared spectroscopic analyzer NICOLET iS5 (manufactured by Thermo Fisher Scientific)
Measurement method: Transmission method Measurement wave number region: 4000 cm ^{−1 to} 400 cm ⁻¹
-Wave number dependence of measurement depth: No correction-Detector: DTGSKBr
・ Resolution: 4cm ^-1
・ Number of integration: 16 times (same for background measurement)

<Measurement method of water absorption>
The water absorption of the foamed molded product was measured according to JIS A9511: 2006R foamed plastic heat insulating material measuring method B. Three test pieces having a 100 × 100 × 25 mm full-cut surface were immersed in fresh water for 10 seconds, then immersed in ethanol for 10 seconds, and further allowed to stand at room temperature (23 ° C.) for 60 minutes. The reference mass (m0) And Next, after immersing in fresh water again and allowing it to absorb water for 24 hours, the mass (m1) is measured by the same method as the reference mass measurement.
For each of the three test pieces, W is calculated by the following formula, and the average value is defined as the water absorption (g / 100 cm ² ).
W = (m1-m0) / A × 100
m1 (g): Mass after absorbing water for 24 hours m0 (g): Reference mass A (cm ² ): Total surface area

<Measurement method and evaluation of flame retardancy of foamed molded product>
Five test pieces having a rectangular parallelepiped shape having a length of 200 mm, a width of 25 mm, and a height of 10 mm are cut out from the obtained foamed molded article with a vertical cutter. After the cut material is cured in an oven at 60 ° C. for 1 day, the individual flame-out time is measured according to the measurement method A of JIS A9511-2006. The average value of the individual flame extinguishing times of 5 test pieces is taken as the flame extinguishing time. In addition, the flame retardance was evaluated according to the following criteria from the flame-out time.
Good (◯): Flame extinguishing time 1.5 seconds or more and less than 3.0 seconds Very good (◎): Flame extinguishing time less than 1.5 seconds Not measured (-): No measurement

<Total content of aromatic organic compound>
The total content of the aromatic organic compound is a value measured by the following << Method for measuring volatile organic compound (VOC) content >>.
<< Measurement Method of Volatile Organic Compound (VOC) Content >>
Weigh accurately 1 g of foamed molded product, add 1 mL of dimethylformamide solution containing 0.1% by volume of cyclopentanol as an internal standard solution, and then add dimethylformamide to the dimethylformamide solution to prepare 25 mL of the measurement solution. Then, 1.8 μL of this measurement solution was supplied to a 230 ° C. sample vaporization chamber, and a gas chromatograph (manufactured by Shimadzu Corporation, trade name “GC-14A”) was detected for each volatile organic compound under the following measurement conditions. Based on the calibration curve of each volatile organic compound measured in advance, the amount of volatile organic compound is calculated from each chart, and the amount of volatile organic compound in the foamed molded product is calculated. When calculating the amount of the volatile organic compound in the expandable particles, 1 g of the expandable particles is precisely weighed and measured in the same manner.
Detector: FID
Column: GL Sciences (3mmφ × 2.5m)
Liquid phase: PEG-20M PT 25%
Carrier; Chromosorb W AW-DMCS
Mesh: 60/80
Column temperature: 100 ° C
Detector temperature: 230 ° C
DET temperature: 230 ° C
Carrier gas (nitrogen)
Carrier gas flow rate (40mL / min)
In addition, among the volatile organic compound (VOC) content described above, the total amount of each volatile organic compound corresponding to the aromatic organic compound is defined as “total content of aromatic organic compound”.

Example 1
With respect to 95 parts by mass of virgin polystyrene having a weight average molecular weight of 200,000 (Toyo Styrene Co., Ltd., trade name “HRM-10N”: resin), acetylene black (manufactured by Denki Kagaku Kogyo Co., Ltd., Denka Black granular grade, average primary particle size) 35 nm, specific surface area 69 m ² / g) 5 parts by mass, 0.5 parts by mass of fine powder talc as an inorganic foam nucleating agent, and 5 parts by mass of triphenyl phosphate (phosphorus component 9.5% by mass) as a phosphorus flame retardant, 150 kg per hour was continuously supplied to a single screw extruder having a diameter of 90 mm. The temperature inside the extruder was set to a maximum temperature of 220 ° C., and the resin was melted. Then, 6 parts by mass of isopentane was used as a blowing agent with respect to 100 parts by mass of the resin, and was injected from the middle of the extruder. The resin and foaming agent are kneaded and cooled in the extruder, the resin temperature at the tip of the extruder is kept at 170 ° C., the pressure at the resin introduction part of the die is kept at 15 MPa, the land length is 0.6 mm in diameter. From the die in which 200 small holes of 3.0 mm are arranged, the foaming agent-containing molten resin is extruded into a cutting chamber connected to the discharge side of this die and circulating water at 30 ° C., and at the same time 10 in the circumferential direction. The extrudate was cut with a high-speed rotating cutter having a single blade to obtain particles. While the cut particles were cooled with circulating water, they were conveyed to a particle separator, and the particles were separated from the circulating water. Further, the collected particles were dehydrated and dried to obtain styrene resin foamable particles. The obtained styrene resin expandable particles were acetylene black: styrene resin = 1: 19 (mass ratio). The obtained styrenic resin expandable particles were substantially spherical with no deformation or beard, and the average particle size was about 1.1 mm.

Polyethylene glycol 0.03 parts by mass, zinc stearate 0.15 parts by mass, stearic acid monoglyceride 0.05 parts by mass, hydroxystearic acid triglyceride 0.05 parts by mass with respect to 100 parts by mass of the obtained styrenic resin expandable particles. The portion was uniformly coated on the entire surface of the styrene resin expandable particles. The obtained styrene resin expandable particles were heated to be pre-expanded to a bulk density of 0.019 g / cm ³ to obtain pre-expanded particles. The pre-expanded particles were aged at 20 ° C. for 24 hours. Next, the pre-expanded particles were filled in a mold and heated and foamed to obtain a foamed molded product having a length of 400 mm × width of 300 mm × thickness of 30 mm. The foamed molded product was dried in a drying chamber at 50 ° C. for 6 hours, and then the density of the foamed molded product was measured and found to be 0.020 g / cm ³ . The foamed molded article was excellent in appearance without shrinkage, and the thermal conductivity of the foamed molded article was 0.032 w / mk.
Further, the flame retardancy of the foamed molded article was evaluated as “◯” with a flame extinguishing time of 0.9 seconds.

(Example 2 : Reference example )
Styrenic resin foamability in the same manner as in Example 1 except that 3 parts by mass of tetrabromobisphenol A-bis (2,3-dibromo-2-methylpropyl ether) and 3 parts by mass of triphenyl phosphate are used as the flame retardant. Particles were obtained. The obtained styrene resin expandable particles were acetylene black: styrene resin = 1: 19 (mass ratio). The obtained styrenic resin expandable particles were substantially spherical with no deformation or beard, and the average particle size was about 1.1 mm.
Further, a foamed molded product was obtained in the same manner as in Example 1. The obtained foamed molded product had a density of 0.020 g / cm ³ . The foamed molded article was excellent in appearance without shrinkage, and the thermal conductivity of the foamed molded article was 0.032 w / mk.
Further, the flame retardancy of the foam molded article was evaluated as “◯” with a flame extinguishing time of 1.0 second.

  Tables 2 and 3 show the evaluation results of the expandable particles, the expanded particles and the expanded molded body of Examples 1 and 2.

Claims (5)

Including styrenic resin, carbon material, foaming agent and flame retardant,
The flame retardant includes a phosphorus-based flame retardant having a phosphorus content of 7% by mass or more,
The phosphorus-based flame retardant is included in an amount of 5 to 10 parts by mass with respect to 100 parts by mass of the styrene resin .
The carbon material is a conductive carbon black having a volume resistivity of 1.0 × 10 ⁴ Ω · cm or less and a volume resistivity of 1.0 × 10 ⁻¹ Ω · cm or more,
The primary particles of the carbon material have an average primary particle size of 18 to 125 nm,
The average value of the longest diameter of the aggregate in which a plurality of primary particles are aggregated is 180 to 500 nm,
Styrene resin expandable particles the ratio of the longest diameter of the mean value for the average primary particle diameter is characterized 4.0-10.0 der Rukoto. The styrene resin expandable particle according to claim 1, wherein the flame retardant contains the phosphorus flame retardant and a bromine flame retardant. The flame retardant contains 0.5 to 10 parts by mass of a brominated flame retardant which is tetrabromobisphenol A-bis (2,3-dibromo-2-methylpropyl ether) with respect to 100 parts by mass of a styrene resin. Item 3. The styrene resin expandable particle according to Item 1 or 2. Including styrenic resin, carbon material and flame retardant,
The flame retardant includes a phosphorus-based flame retardant having a phosphorus content of 7% by mass or more,
The phosphorus-based flame retardant is included in an amount of 5 to 10 parts by mass with respect to 100 parts by mass of the styrene resin .
The carbon material is a conductive carbon black having a volume resistivity of 1.0 × 10 ⁴ Ω · cm or less and a volume resistivity of 1.0 × 10 ⁻¹ Ω · cm or more,
The primary particles of the carbon material have an average primary particle size of 18 to 125 nm,
The average value of the longest diameter of the aggregate in which a plurality of primary particles are aggregated is 180 to 500 nm,
The expanded styrene resin beads the ratio of the longest diameter of the mean value for the average primary particle diameter is characterized 4.0-10.0 der Rukoto. A foamed molded article comprising a plurality of styrene resin foam particles fused together, containing a styrene resin, a carbon material and a flame retardant,
The flame retardant includes a phosphorus-based flame retardant having a phosphorus content of 7% by mass or more,
The phosphorus-based flame retardant is included in an amount of 5 to 10 parts by mass with respect to 100 parts by mass of the styrene resin .
The carbon material is a conductive carbon black having a volume resistivity of 1.0 × 10 ⁴ Ω · cm or less and a volume resistivity of 1.0 × 10 ⁻¹ Ω · cm or more,
The primary particles of the carbon material have an average primary particle size of 18 to 125 nm,
The average value of the longest diameter of the aggregate in which a plurality of primary particles are aggregated is 180 to 500 nm,
Foamed molded ratio of the longest diameter of the mean value for the average primary particle diameter is characterized 4.0-10.0 der Rukoto.