JP6555251B2 - Styrenic resin foam molding and method for producing the same - Google Patents

Description

  The present invention relates to expandable styrene resin particles, a method for producing the same, pre-expanded particles obtained by pre-expanding expandable styrene-based resin particles, a styrene resin foam-molded article obtained by molding pre-expanded particles, and a method for producing the same.

  Styrenic resin foam molded products obtained by using expandable styrene resin particles have been conventionally used as a food product box, a cold box, a cushioning material, and a foam having an excellent balance of light weight, heat insulation, buffering properties, and the like. It is widely used as a heat insulating material for houses.

  In recent years, related to various problems such as global warming, energy saving is being promoted by improving the heat insulation of buildings such as houses, and the demand for styrene resin foam moldings is expected to increase, and further improvement of heat insulation is expected. Various studies have been made.

  On the other hand, styrene resin foam molded products are a competitive market with other materials such as glass wool as a heat insulating material, and thorough cost reduction is required. Styrenic resin foam moldings with an expansion ratio of 40 times or more have higher thermal conductivity as the expansion ratio increases and deteriorates the heat insulation properties. Therefore, the styrene resin has a high expansion ratio of 40 times or more and low thermal conductivity. A foamed molded body has been desired. If it is a styrene resin foam molded article with lower thermal conductivity, even if the expansion ratio is increased, the heat insulation equivalent to that of a conventional styrene resin foam molded article with a low expansion ratio can be obtained, and the expandable styrene is the raw material. The heat insulating material can be manufactured at low cost because the amount of the resin particles used can be reduced.

  In addition, foaming agents such as butane and pentane, which have a thermal conductivity reducing effect, contained in the styrenic resin foam moldings dissipate from the styrene resin foam moldings over time and are replaced with the atmosphere (air). Furthermore, it is known that the thermal conductivity of the styrene resin foam molded article increases with the passage of time, and the heat insulation properties deteriorate with the passage of time.

  Therefore, it is required to keep the thermal conductivity low even after the foaming agent such as butane and pentane contained in the styrene resin foam molded article is replaced with air.

Regarding the heat insulation improvement of the styrenic resin foam molded article, for example, Patent Document 1 discloses a foaming agent for styrene resin particles having a weight average molecular weight of 300 to 600,000 and an expansion ratio during melt flow measurement within a predetermined range. Expandable styrene resin particles that contain a styrene resin foam molded article having a bulk density of 0.02 to 0.009 g / cm ³ and an average cell thickness of 0.8 to 2.5 μm have been proposed. .

  According to the invention of Patent Document 1, a low thermal conductivity can be obtained as compared with a conventional styrenic resin foam molded article, but the thermal insulation property that satisfies the market demand has not been achieved.

  In addition, a method of using a radiation heat transfer inhibitor such as graphite in a styrene resin foam molded article is known. A radiant heat transfer inhibitor is a substance that can suppress radiant heat transfer among heat transfer mechanisms that travel through the foam molded body, and has the same resin, foaming agent, cell structure, and density. In this case, it refers to a substance having an effect of lowering the thermal conductivity by adding a radiant heat transfer inhibitor as compared with an additive-free system.

  Patent Document 2 discloses an expandable styrenic resin particle characterized in that it can provide a foam having a density of 35 g / L or less by treatment and contains uniformly distributed graphite powder. Proposed. As a problem when using graphite powder, there is a decrease in flame retardancy. On the other hand, as a flame retardant, an organic bromine compound having a bromine content of 70% by weight or more is used as the foamable styrene resin. Techniques for inclusion in particles have been proposed.

Patent Document 3 discloses that the density is 10 to 100 kg / m ³ , the closed cell ratio is 60% or more, the average cell diameter is 20 to 1000 μm, and the graphite powder is 0.05 to 9% by weight. The aspect ratio is 5 or more, the volume average particle diameter (50% particle diameter) is 0.1 to 100 μm, the specific surface area is 0.7 m ² / cm ³ or more, and the value obtained by dividing the 90% particle diameter by the 10% particle diameter is 1 to 20. A styrenic resin foam molded article is suggested. However, graphite used in the most preferred is an embodiment example of Patent Document 3 is 1.50 m ² / cm ³ at maximum specific surface area, than the specific surface area of 1.50 m ² / cm ³ in Patent Document 3 There is no mention of the use of graphite.

  Patent Document 4 discloses a foaming property in which a styrene monomer is seed-polymerized into a styrene resin micropellet containing graphite particles in the presence of an aromatic hydrocarbon having 6 to 10 carbon atoms, and at the same time, a foaming agent is added. A method for producing styrene resin particles has been proposed.

  In Patent Document 5, a resin composition containing a polystyrene-based resin, a flame retardant, graphite, and a volatile foaming agent is melt-kneaded in an extruder, and the resulting melt-kneaded product is extruded from a die into pressurized water and extruded. There has been proposed a method of producing expandable styrene resin particles by cutting the melt-kneaded product.

  Patent Document 6 proposes expandable styrene resin particles containing 0.1 to 25% by mass of graphite having an average particle size of more than 50 μm. Patent Document 7 proposes expandable styrene resin particles in which the flame retardant content in the surface layer is greater than the overall flame retardant content. Patent Document 8 proposes expandable styrene resin particles containing 0.1 to 25% by mass of graphite and a volatile foaming agent that is a mixture of pentane and water and having a bulk density exceeding 600 g / L. Patent Document 9 proposes expandable styrenic resin particles containing 3 to 15% by weight of graphite and having an overall graphite content larger than that of the surface layer portion.

  Patent Document 10 discloses a method in which styrene and, if necessary, a monomer compound copolymerizable with styrene are polymerized in a suspension aqueous liquid in the presence of graphite particles, and a foaming agent is added before, during or after polymerization. Has proposed a method for producing conductive styrene resin particles. Patent Document 11 is polymerized in a suspension aqueous solution in the presence of graphite and a nonionic surfactant, and has a thermal conductivity of less than 32 mW / m · K and a density of 25 g / m as measured at 10 ° C. according to DIN52612. A method for producing expandable styrene-based resin particles that is less than L is proposed.

  In invention of patent documents 2-11, thermal conductivity is reduced rather than the conventional styrene resin foaming molding by containing graphite which controls propagation of heat, and heat insulation is improved. However, a thorough cost reduction of the styrene resin foam molded body is required in the market, and a styrene resin foam molded body having a high expansion ratio and low thermal conductivity is required. In particular, there is a need for a styrenic resin foam molded article having low thermal conductivity even when butane, pentane or the like is replaced with air after a long period of time, and these inventions do not meet this expectation.

  On the other hand, as a method for producing a styrene resin foam molded product from expandable styrene resin particles, the resin particles are expanded to a predetermined expansion ratio to obtain pre-expanded particles, and the preliminary expansion is performed using the pre-expanded particles. The foaming method is common.

This pre-foaming method is roughly classified into a continuous method and a batch method. In the continuous method, the foamable styrene resin particles are continuously put into the can of the pre-foaming machine under stirring at atmospheric pressure, and the resin particles are predetermined by supplying water vapor from the lower part of the pre-foaming machine into the can. The pre-expanded particles having the expansion ratio are taken out from the upper part of the pre-expander. In the batch method, expandable styrene resin particles are introduced into a can of a pre-foaming machine, and the resin particles are preliminarily provided with a predetermined expansion ratio by supplying water from the lower part of the pre-foaming machine to the can while stirring the can. After forming the expanded particles, the water vapor supply is stopped, the air is blown in, and the mixture is cooled and dried, and the obtained preliminary expanded particles are taken out from the preliminary expanded machine. The batch method includes an atmospheric pressure foaming method in which pre-foaming is performed under atmospheric pressure, and a pressure foaming method in which pre-foaming is performed with the inside of the can of the pre-foaming machine being pressurized. Unless otherwise specified below, pressure means gauge pressure.

However, in the case of using the expandable styrene resin particles containing graphite having a radiation heat transfer suppressing effect in order to further reduce the thermal conductivity of the styrene resin foam molded article in the conventional preliminary foaming method, It is very difficult to obtain pre-expanded particles having a foaming ratio of 65 cm ³ / g or more because the cell membrane in the pre-expanded particles is easily opened during the pre-expanding mainly due to graphite. Further, even when pre-expanded particles having an expansion ratio of 65 cm ³ / g or more are obtained by adjusting the foaming conditions, there is a problem that the styrenic resin foam-molded article obtained by foam-molding the pre-expanded particles is inferior in surface beauty. The reduction in the expansion ratio also impairs the lightness of the styrene resin foam molded article.

  As a technique for obtaining pre-expanded particles having a high expansion ratio, a two-stage expansion method is known. In the two-stage foaming method, the first stage of pre-foaming is applied to the expandable styrenic resin particles to obtain expanded particles with a certain expansion ratio, and after curing and introducing air into the second stage, This is a method for obtaining pre-expanded particles having a further increased expansion ratio by the pre-expansion. In the two-stage foaming method, after completion of the first stage pre-foaming, the obtained foam particles are cured in a can of the pre-foaming machine, and after the obtained foam particles are once taken out from the pre-foaming machine and cured, There is a method of charging again into the preliminary foaming machine.

If the two-stage foaming method is used, pre-expanded particles having an expansion ratio of 65 cm ³ / g or more can be easily obtained even when expandable styrene resin particles made of a styrene resin composition containing graphite are used. . However, since the number of air bubbles having holes in the cell membrane in the pre-expanded particles is remarkably increased by the two-stage pre-expanding (heated foaming), the styrene resin foam-molded article obtained by molding the pre-expanded particles Exhibits a relatively high thermal conductivity based on a decrease in closed cell ratio, etc., and also has problems such as a decrease in surface aesthetics and a decrease in mechanical properties due to poor fusion between pre-expanded particles inside. doing.

Therefore, when the expandable styrene resin particles made of a styrene resin having a relatively high content of 3 to 8% by weight of graphite are used to produce a styrene resin foam molded article by the conventional prefoaming method, low thermal conductivity or Remarkably excellent heat insulation based on high closed cell ratio, etc. and extremely high light weight based on high foaming ratio (particularly foaming ratio of 65 cm ³ / g or more), etc., and low thermal conductivity is maintained over a long period of time, It is very difficult to obtain a styrenic resin foam molded article having good surface aesthetics. Moreover, the present condition is that such a styrene-type resin foam molding is not on the market.

Japanese Patent Laid-Open No. 2002-284817 Special table 2001-525001 gazette JP 2005-2268 A JP-T 2009-536687 JP 2013-75941 A Japanese translation of PCT publication No. 2002-530450 JP 2004-346281 A JP 2005-506390 A JP 2013-209608 A JP-T-2001-522383 Special table 2008-502750 gazette

  An object of the present invention is to produce expandable styrene resin particles, pre-expanded particles, and expandable styrene resin particles that can give a styrene resin foam molded article with higher expansion ratio, lower thermal conductivity, and higher heat insulation. It is to provide a method, and a styrenic resin foam-molded article having a high heat insulating property with a higher expansion ratio and a lower thermal conductivity, and a method for producing the same.

  As a result of intensive studies to solve the above problems, the present inventors have found a styrenic resin foam molded article having a very low thermal conductivity over a long period of time from the beginning of manufacture and a high heat insulating property and a method for producing the same, The present invention has been completed. In particular, according to the method for producing a styrenic resin foam molded article of the present invention, the inventors of the present invention do not use the expandable styrenic resin particles having a high content of 3 to 8% by weight of graphite. By pre-foaming under conditions, the increase in thermal conductivity over time is significantly suppressed with high foaming ratio, high closed cell ratio, and low thermal conductivity without impairing the surface beauty of the styrene resin foam. It was found that a styrenic resin foam molded article having high heat insulation properties over the long term can be obtained.

  That is, the present invention relates to (1) to (4) expandable styrene resin particles, (5) pre-expanded particles, (6) styrene resin foam molded articles, and (7) to (10) expandability. The manufacturing method of a styrene resin particle, the manufacturing method of the styrene resin foam molding of (11)-(17), and the styrene resin foam molding of (18)-(31) are provided.

(1) Expandable styrene resin particles obtained by adding a foaming agent to styrene resin particles, wherein the expandable styrene resin particles contain 3 to 8% by weight of graphite, and the graphite has an average particle diameter of 3 to 7 μm. The expandable styrene resin particles have a specific surface area of 1.55 m ² / cm ³ or more.
(2) The expandable styrenic resin particles of (1) above, wherein a value obtained by dividing 90% particle size by 10% particle size of graphite is 2.5 or more.
(3) The expandable styrene resin according to (1) or (2) above, which contains a brominated flame retardant and has a bromine content of 0.8 to 2.5% by weight in the case of a styrene resin foam molded article. particle.
(4) Any of the above (1) to (3), wherein the foaming agent comprises a hydrocarbon having 4 to 5 carbon atoms, and the content of the foaming agent is 4 to 10 parts by weight with respect to 100 parts by weight of the styrene resin. Expandable styrene resin particles.
(5) Pre-expanded particles obtained by pre-expanding the expandable styrenic resin particles according to any one of (1) to (4) above.
(6) A styrene resin foam molded article obtained by molding the pre-expanded particles of (5) above.
(7) The manufacturing method of the expandable styrene resin particle in any one of said (1)-(4).
(8) The method for producing expandable styrene resin particles according to (7) above, wherein styrene resin and graphite are melt-kneaded with an extruder to obtain styrene resin pellets using a cold cut method or a hot cut method. And then, suspending the styrene resin pellets in water and containing a foaming agent, a method for producing expandable styrene resin particles.
(9) The method for producing expandable styrene resin particles according to (7) above, wherein the styrene resin, graphite and foaming agent are melt-kneaded with an extruder and have a small hole attached to the tip of the extruder. A process for producing expandable styrenic resin particles, which is extruded into a cutter chamber filled with pressurized circulating water through, cut with a rotary cutter immediately after extrusion, and cooled and solidified with pressurized circulating water.
(10) The method for producing expandable styrene-based resin particles according to (7) above, wherein styrene is polymerized in an aqueous suspension in the presence of graphite, and before and / or during and / or after polymerization, the foaming agent A method for producing expandable styrene resin particles, characterized by impregnating with water.

(11) A styrene resin foam molded article produced by pre-expanding foamable styrene resin particles into pre-expanded particles, and molding the pre-expanded particles in-mold, wherein the styrene resin foam molded article comprises graphite. Between 3 to 8% by weight, measured between a thermal conductivity A (W / m · K) and an expansion ratio B (cm ³ / g) of a styrene resin foam molded article measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. A styrenic resin foam molded article having the relationship of Formula 1.
Formula 1: A ≦ 0.0251 + 0.0000776 × B
(12) A styrene resin foam molded article produced by pre-expanding expandable styrene resin particles into pre-expanded particles, and molding the pre-expanded particles in-mold, wherein the styrene resin foam molded article is made of graphite. The thermal conductivity C (W / m · K) and the expansion ratio D measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. after drying the styrene resin foam molded body at 50 ° C. for 30 days. A styrene-based resin foam molded article having a relationship of Formula 2 between (cm ³ / g).
Formula 2: C ≦ 0.0276 + 0.0000776 × D
(13) The styrene resin foam molded article according to (11) or (12), wherein the expansion ratio is 40 (cm ³ / g) or more.
(14) The styrene resin foam molded article according to any one of (11) to (13), wherein the expandable styrene resin particles contain graphite having an average particle diameter of 3 to 7 μm.
(15) The styrene resin foam molded article according to any one of (11) to (14), wherein the expandable styrene resin particles contain graphite having a specific surface area of 1.55 m ² / cm ³ or more.
(16) The styrene resin foam according to any one of (11) to (15) above, wherein the expandable styrene resin particles contain graphite having a value obtained by dividing 90% particle size by 10% particle size to 2.5 or more. Molded body.
(17) The styrene resin foam molded article according to any one of (11) to (16) above, which contains a brominated flame retardant and has a bromine content of 0.8 to 2.5% by weight.

(18) A styrenic system comprising a pre-foaming step for obtaining pre-foamed particles by introducing water vapor into expandable styrenic resin particles placed in a can of the pre-foaming machine, and a molding step for molding the pre-foamed particles in a mold. A method for producing a resin foam molded article, wherein the graphite content in the styrene resin foam molded article is 3 to 8% by weight, and the water vapor charging time in the pre-foaming step is 50 to 500 seconds. Obtaining a styrene-based resin foam molded article having a relationship of Formula 1 between a thermal conductivity A (W / m · K) measured at a temperature of 23 ° C. and a temperature difference of 20 ° C. and a foaming ratio B (cm ³ / g). A method for producing a styrene-based resin foam molded article.
Formula 1: A ≦ 0.0251 + 0.0000776 × B
(19) A styrenic system including a pre-foaming step for obtaining pre-foamed particles by introducing water vapor into the expandable styrenic resin particles placed in a can of the pre-foaming machine, and a molding step for molding the pre-foamed particles in a mold. A method for producing a resin foam molded article, wherein the graphite content in the styrene-based resin foam molded article is 3 to 8% by weight, and the water vapor charging time in the preliminary foaming step is 50 to 500 seconds, Styrene having a relationship of Formula 2 between thermal conductivity C (W / m · K) and foaming ratio D (cm ³ / g) measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. after drying at 30 ° C. for 30 days A method for producing a styrenic resin foam molded article, characterized in that a styrene resin foam molded article is obtained.
Formula 2: C ≦ 0.0276 + 0.0000776 × D
(20) The method for producing a styrene resin foam molded article according to (18) or (19), wherein the foaming styrene resin particles are prefoamed in one stage in the prefoaming step.
(21) The method for producing a styrene resin foam molded article according to any one of the above (18) to (20), wherein the expansion ratio of the styrene resin foam molded article is 65 to 80 cm ³ / g.
(22) The method for producing a styrene resin foam molded article according to any one of the above (18) to (21), wherein the water vapor charging time is 80 to 300 seconds.
(23) The method for producing a styrene resin foam molded article according to any one of the above (18) to (22), wherein the pressure in the can of the preliminary foaming machine at the time of introducing steam is 0.001 to 0.15 MPa in gauge pressure.
(24) The method for producing a styrene resin foam molded article according to any one of the above (18) to (23), wherein the temperature of water vapor exceeds 100 ° C and is 130 ° C or less.
(25) Production of the styrene resin foam molded article according to any one of (18) to (24) above, wherein in the prefoaming step, air is introduced into the expandable styrene resin particles placed in the can of the prefoaming machine together with water vapor. Method.
(26) The method for producing a styrene resin foam molded article according to any one of the above (18) to (25), wherein the average cell diameter of the styrene resin foam molded article is 70 to 250 μm.
(27) The method for producing a styrene resin foam molded article according to any one of the above (18) to (26), wherein the closed cell ratio of the styrene resin foam molded article is 97 to 100%.
(28) The method for producing a styrene resin foam molded article according to any one of the above (18) to (27), wherein the closed cell ratio of the pre-expanded particles is 97 to 100%.
(29) The method for producing a styrene resin foam molded article according to any one of (18) to (28), wherein the expandable styrene resin particles contain graphite having an average particle diameter of 3 to 7 μm.
(30) The method for producing a styrene resin foam molded article according to any one of (18) to (29), wherein the expandable styrene resin particles contain graphite having a specific surface area of 1.55 m ² / cm ³ or more.
(31) The styrene resin foam according to any one of (18) to (30), wherein the expandable styrene resin particles contain graphite having a value obtained by dividing 90% particle diameter by 10% particle diameter of 2.5 or more. Manufacturing method of a molded object.

  ADVANTAGE OF THE INVENTION According to this invention, the styrene resin foaming molding which has high heat insulation with a high expansion ratio and low thermal conductivity can be provided. As described above, according to the present invention, heat insulation equivalent to that of a conventional styrene resin foam molded article having a low expansion ratio can be obtained, and the expansion ratio of the expandable styrene resin particles as a raw material is extremely high. The amount used can be reduced and can be manufactured at low cost. Furthermore, it is possible to provide a styrene resin foam molded article having a low thermal conductivity even after a long time has elapsed. Further, it is possible to provide a styrene resin foam molded article having a high closed cell ratio and a high surface beauty.

It is a graph which shows the relationship between the expansion ratio B (cm < ³ > / g) of Examples 1-18 and Comparative Examples 1-3 and thermal conductivity A (W / m * K). It is a graph which shows the relationship between the expansion ratio D (cm < ³ > / g) of Examples 1-18 and Comparative Examples 1-3 and thermal conductivity C (W / m * K).

  Hereinafter, embodiments of the present invention will be described in more detail in the order of expandable styrene-based resin particles and a production method thereof, a styrene-based resin foam molded product, and a production method thereof.

[Expandable styrene resin particles]
The expandable styrene resin particles of the present invention are those in which a foaming agent and graphite are contained in styrene resin particles, and the content of graphite is 3 to 8% by weight of the total amount of expandable styrene resin particles. It is characterized by. The graphite preferably has an average particle size of ³ to 7 μm, more preferably an average particle size of ³ to 7 μm and a specific surface area of 1.55 m ² / cm ³ or more, an average particle size of 3 to 7 μm, More preferably, the specific surface area is 1.55 m ² / cm ³ or more, and the 90% particle size divided by 10% particle size (90% particle size / 10% particle size) is 2.5 or more.

  The expandable styrene resin particles of the present invention contain a styrene resin, graphite, and a foaming agent, and are selected from the group consisting of a flame retardant, a thermal stabilizer, a radical generator, and other additives as necessary. At least one optional component can be contained. The expandable styrene resin particles of the present invention preferably contain a styrene resin, graphite, a foaming agent and a flame retardant, and may contain at least one of the above-mentioned optional components excluding the flame retardant, more preferably. , A styrenic resin, graphite, a foaming agent, a flame retardant and a heat stabilizer, and may contain at least one of the optional components excluding the flame retardant and the heat stabilizer, more preferably a styrenic resin, It contains graphite, a foaming agent, a flame retardant, a heat stabilizer and a nucleating agent, and may contain at least one of the above-mentioned optional components excluding the flame retardant, the heat stabilizer and the nucleating agent.

  Hereinafter, the essential components and optional components contained in the expandable styrene resin particles of the present invention will be described in more detail.

(Styrene resin)
The styrene resin used in the present invention is a copolymer of not only a styrene homopolymer (polystyrene homopolymer) but also other monomers or derivatives thereof copolymerizable with styrene within a range not impairing the effects of the present invention. May be. However, the brominated styrene / butadiene copolymer described later is excluded.

  Examples of other monomers copolymerizable with styrene or derivatives thereof include, for example, methylstyrene, dimethylstyrene, ethylstyrene, diethylstyrene, isopropylstyrene, bromostyrene, dibromostyrene, tribromostyrene, chlorostyrene, dichlorostyrene, Styrene derivatives such as trichlorostyrene; polyfunctional vinyl compounds such as divinylbenzene; (meth) acrylic acid ester compounds such as methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, butyl methacrylate; Vinyl cyanide compounds such as (meth) acrylonitrile; diene compounds such as butadiene or derivatives thereof; unsaturated carboxylic acid anhydrides such as maleic anhydride and itaconic anhydride; N-methylmaleimide, N- N-alkyl substituted maleimide compounds such as tilmaleimide, N-cyclohexylmaleimide, N-phenylmaleimide, N- (2) -chlorophenylmaleimide, N- (4) -bromophenylmaleimide, N- (1) -naphthylmaleimide, etc. can give. These may be used alone or in combination of two or more.

  The styrene resin used in the present invention is not limited to the styrene homopolymer and / or a copolymer with other monomers copolymerizable with styrene or a derivative thereof, and does not impair the effects of the present invention. In the range, it may be a homopolymer of the other monomer or derivative, or a blend with the copolymer.

  For example, diene rubber reinforced polystyrene, acrylic rubber reinforced polystyrene, polyphenylene ether resin, or the like can be blended with the styrene resin used in the present invention.

  Among the styrenic resins used in the present invention, it is relatively inexpensive and can be foam-molded with low-pressure steam or the like without using a special method, and is excellent in the balance of heat insulation, flame retardancy, and buffering properties. Polystyrene homopolymer, styrene-acrylonitrile copolymer, and styrene-butyl acrylate copolymer are preferred.

(Graphite)
In the present invention, a styrene resin foam molded article having high heat insulating properties can be obtained by adding graphite to the expandable styrene resin particles as a radiation heat transfer inhibitor. The radiation heat transfer inhibitor refers to a substance having a characteristic of reflecting, scattering, or absorbing light in the near infrared or infrared region (for example, a wavelength region of about 800 to 3000 nm).

  Examples of the graphite used in the present invention include flaky graphite, earthy graphite, spherical graphite, and artificial graphite. In the present specification, the term “scale-like” also includes a scale-like, flaky or plate-like one. These graphites can be used alone or in combination of two or more. Among these, a graphite mixture containing scaly graphite as a main component is preferable, and scaly graphite is more preferable because it has a high effect of suppressing radiant heat transfer.

  The graphite used in the present invention preferably has an average particle size of 3 to 7 μm. Furthermore, 4-6 micrometers is more preferable. The average particle size of the graphite of the present invention is determined by dispersing the graphite in water and measuring the particle size distribution by the laser diffraction scattering method. The particle size when the cumulative volume with respect to the volume of all particles is 50% (volume by the laser diffraction scattering method) The average particle size was defined as the average particle size.

The production cost of graphite increases as the average particle size decreases. In particular, graphite having an average particle size of less than 3 μm is very expensive due to high production cost, and the cost of expandable styrene resin particles tends to be high. When the average particle diameter exceeds 7 μm, it tends to be difficult to make the specific surface area of graphite 1.55 m ² / cm ³ or more. In addition, when the average particle diameter exceeds 7 μm, the cell membrane is easily broken when producing pre-expanded particles and styrene-based resin foam molded products from expandable styrene-based resin particles. There is a tendency that the ease decreases and the compressive strength of the styrenic resin foam molding decreases.

In addition, the larger the specific surface area of the graphite in the styrene resin foam molded article, the greater the probability of absorbing or reflecting heat radiation, so the effect as a radiation heat transfer inhibitor is increased. The specific surface area of graphite tends to increase as the average particle size of graphite decreases, but as described above, the production cost of graphite increases as the average particle size decreases. In the prior art, graphite having a specific surface area of 1.55 m ² / cm ³ or more was not used from the viewpoint of balance between cost and performance.

The graphite used in the present invention preferably has a specific surface area of 1.55 m ² / cm ³ or more. When the specific surface area is less than 1.55 m ² / cm ³ , the effect of reducing the thermal conductivity tends to be insufficient. The specific surface area of the graphite is more preferably 1.60 m ² / cm ³ or more, more preferably 1.65 m ² / cm ³ or more. The specific surface area of the graphite of the present invention is measured by a laser diffraction scattering method by dispersing graphite in water in the same manner as the average particle diameter. If the specific surface area is large, the probability of absorbing or reflecting radiation increases, and the effect as a radiation heat transfer inhibitor increases.

If the specific surface area is 1.55 m ² / cm ³ or more in graphite having an average particle diameter of 3 to 7 μm, the present inventors greatly reduce the thermal conductivity of the styrene-based resin foam molding and improve the heat insulation. It was found that the effect to make is great. In particular, if graphite with an average particle size of 3 to 7 μm and a specific surface area of 1.65 m ² / cm ³ or more is used, the cost performance is higher than that of other heat insulating materials that are considered to have higher heat insulation than styrene resin foam moldings. It becomes an excellent heat insulating material.

The specific surface area of the graphite used in the present invention is preferably from ^{5 m} 2 / cm ³ or ^less, more preferably 3m 2 / cm ³ or less, 2.5 m ² / cm ³ or less is more preferred. In the graphite having an average particle diameter of 3 to 7 μm of the present invention, when the specific surface area is set to 5 m ² / cm ³ or more, a technique such as thinning of the graphite is required and the cost is increased. The range of the specific surface area of graphite is preferably 1.55 to ⁵ m ² / cm ³ , more preferably 1.60 to ³ m ² / cm ³ , and still more preferably 1.65 to ^2.5 m ² / cm ³ .

The quality of general graphite is considered to be higher when it has the desired particle size, the particle size distribution is a normal distribution due to purification during the production of graphite, and the value of 90% particle size / 10% particle size is obtained. Has been manufactured to be small. However, in the present invention, the specific surface area can be obtained even in graphite having an average particle size range that is available at a general price by using poorly purified graphite containing many small particles, which are generally regarded as poor in quality. Can be increased to 1.55 m ² / cm ³ or more, and it becomes possible to obtain a styrenic resin foam molded article having good heat insulation.

  The graphite used in the present invention preferably has a value obtained by dividing 90% particle size by 10% particle size to 2.5 or more, more preferably 3 or more, and further preferably 5 or more. Graphite is dispersed in water, the particle size distribution is measured by laser diffraction scattering method, the particle size when the cumulative volume from the smaller particle size to the total particle volume becomes 10% is 10% particle size, the cumulative volume is The 90% particle size was 90%.

  The larger the 90% particle size / 10% particle size value, the broader the particle size distribution, and the larger the 90% particle size / 10% particle size value is the graphite with the same average particle size. However, the thermal conductivity can be greatly reduced.

  The graphite content of the expandable styrene resin particles in the present invention is easily controlled to the target expansion ratio, and the resin particles are compared with the expandable styrene resin particles from the viewpoint of balance such as a thermal conductivity reduction effect. It is preferably 3% by weight or more and 8% by weight or less, more preferably 3% by weight or more and 6.5% by weight or less, and further preferably 3.5% by weight or more and 5.5% by weight or less. preferable. If the graphite content is less than 3% by weight, the effect of reducing the thermal conductivity tends to be insufficient, whereas if it exceeds 8% by weight, it is difficult to control the expansion ratio.

  In addition, in the conventional graphite-containing expandable styrene resin particles, graphite is present in the cell membrane, so if the expansion ratio is high, the cell membrane breaks down and the moldability deteriorates or the compressive strength decreases. There was a tendency to. However, in the present invention, 3 to 8 weights of the graphite having the predetermined average particle size or the predetermined average particle size and specific surface area or the predetermined average particle size, specific surface area and 90% particle size / 10% particle size. %, It is possible to obtain graphite-containing expandable styrene resin particles having good moldability even at a high expansion ratio, and low thermal conductivity that cannot be obtained with conventional graphite-containing expandable styrene resin particles. Styrene-based resin foam moldings can be provided.

(Foaming agent)
Although the foaming agent used by this invention is not specifically limited, A C4-C5 hydrocarbon is preferable. Examples of the hydrocarbon having 4 to 5 carbon atoms include hydrocarbons such as normal butane, isobutane, normal pentane, isopentane, neopentane, and cyclopentane. These may be used individually by 1 type and may be used in combination of 2 or more type.

  The addition amount of the foaming agent in the present invention is preferably 4 parts by weight or more and 10 parts by weight or less with respect to 100 parts by weight of the styrenic resin from the viewpoint that it is easy to control the target foaming ratio. It is more preferably 5 parts by weight or more and 9 parts by weight or less, and further preferably 5 parts by weight or more and 8 parts by weight or less. When the addition amount of the foaming agent is less than 4 parts by weight, it tends to be difficult to produce a styrene resin foam molded article having a high expansion ratio of 40 times or more. Since the manufacturing time (molding cycle) at the time of manufacturing becomes long, the manufacturing cost tends to increase.

(Flame retardants)
The flame retardant used in the present invention is not particularly limited, and any flame retardant conventionally used in styrene resin foam molded products can be used, but among them, the flame retardant imparting effect is high and synergistic with graphite. From the viewpoint that the foaming ratio can be easily controlled, a brominated flame retardant is preferable. Examples of the brominated flame retardant used in the present invention include 2,2-bis [4- (2,3-dibromo-2-methylpropoxy) -3,5-dibromophenyl] propane (also known as tetrabromobisphenol A). -Bis (2,3-dibromo-2-methylpropyl ether)), 2,2-bis [4- (2,3-dibromopropoxy) -3,5-dibromophenyl] propane (also known as: tetrabromobisphenol A-) Brominated bisphenol compounds such as bis (2,3-dibromopropyl ether)); brominated styrene / butadiene block copolymers, brominated random styrene / butadiene copolymers, brominated styrene / butadiene graft copolymers, etc. Brominated butadiene / vinyl aromatic hydrocarbon copolymer (for example, disclosed in JP-T 2009-516019) It has been that), and the like. These brominated flame retardants may be used alone or in combination of two or more.

  The brominated flame retardant is easy to control to the desired expansion ratio and has a bromine content with respect to the total amount of the styrene resin foam molded product from the viewpoint of balance such as flame retardancy when adding a radiation heat transfer inhibitor. Preferably it is mix | blended with an expandable styrene-type resin particle so that it may become 0.8 to 2.5 weight%, More preferably, it is 1.0 to 2.0 weight%.

(Heat stabilizer)
In the expandable styrene resin particles of the present invention, the 1% weight reduction temperature in the thermogravimetric analysis of the brominated flame retardant-containing mixture can be controlled by using a heat stabilizer in combination.

  The heat stabilizer in the present invention is appropriately selected according to the type of styrene resin used, the type and content of the foaming agent, the type and content of the radiation heat transfer inhibitor, the type and content of the brominated flame retardant, and the like. They can be used in combination.

  As the heat stabilizer used in the present invention, a hindered amine compound, a phosphorus compound, and an epoxy compound are preferable because the 1% weight loss temperature in the thermogravimetric analysis of the brominated flame retardant-containing mixture can be arbitrarily controlled. A heat stabilizer can be used individually by 1 type or in combination of 2 or more types. These heat stabilizers can also be used as light-resistant stabilizers as described later.

(Radical generator)
In the expandable styrene resin particles of the present invention, by further containing a radical generator, the 1% weight reduction temperature in the thermogravimetric analysis of the brominated flame retardant is controlled by using it together with the brominated flame retardant. Can do.

  The radical generator in the present invention is used in appropriate combination depending on the type of styrene resin used, the type and content of the foaming agent, the type and content of the radiation heat transfer inhibitor, and the type and content of the brominated flame retardant. be able to.

  Examples of the radical generator used in the present invention include cumene hydroperoxide, dicumyl peroxide, t-butyl hydroperoxide, 2,3-dimethyl-2,3-diphenylbutane, and poly-1,4-isopropyl. Examples include benzene. A radical generator can be used individually by 1 type or in combination of 2 or more types.

(Other additives)
The expandable styrenic resin particles of the present invention are, as necessary, a processing aid, a light-resistant stabilizer, an antistatic agent, a colorant such as a pigment, a nucleating agent, a foam as long as the effects of the present invention are not impaired. It may contain one or more other additives selected from the group consisting of auxiliaries. Examples of processing aids include sodium stearate, magnesium stearate, calcium stearate, zinc stearate, barium stearate, and liquid paraffin. Examples of the light resistance stabilizer include hindered amines, phosphorus stabilizers, and epoxy compounds described above, as well as phenol antioxidants, nitrogen stabilizers, sulfur stabilizers, and benzotriazoles. Examples of nucleating agents include silica, calcium silicate, wollastonite, kaolin, clay, mica, zinc oxide, calcium carbonate, sodium bicarbonate, talc and other inorganic compounds, methyl methacrylate copolymers, ethylene-vinyl acetate. Examples thereof include polymer compounds such as copolymer resins, olefinic waxes such as polyethylene wax, and fatty acid bisamides such as methylene bisstearyl amide, ethylene bisstearyl amide, hexamethylene bispalmitic acid amide, and ethylene bisoleic acid amide. As the foaming aid, a solvent having a boiling point of 200 ° C. or less under atmospheric pressure can be preferably used. For example, aromatic hydrocarbons such as styrene, toluene, ethylbenzene and xylene, and alicyclic carbonization such as cyclohexane and methylcyclohexane. Examples thereof include acetates such as hydrogen, ethyl acetate, and butyl acetate. In addition, as an antistatic agent and a coloring agent, what is used for various resin compositions can be used without limitation. These other additives can be used alone or in combination of two or more.

[Method for producing expandable styrene resin particles]
Examples of the method for producing the expandable styrene resin particles of the present invention include a melt kneading method in which a styrene resin and various components are melt-kneaded using an extruder and then cut into particles, and a styrene resin in the presence of graphite. Examples thereof include a polymerization method in which a monomer is subjected to suspension polymerization, and among these, a melt kneading method is preferable. Examples of the melt kneading method include the following two methods.

  In the first melt-kneading method, a styrene resin and graphite are melt-kneaded with an extruder to obtain a styrene resin pellet using a cold cut method or a hot cut method, and then the styrene resin pellet is suspended in water. There is a method of making the pellets contain a foaming agent while making it turbid.

  More specifically, styrene-based resin, graphite, and if necessary, each component such as brominated flame retardant, radical generator, heat stabilizer, and other additives are melt-kneaded with an extruder if necessary. After the styrenic resin particles are obtained by extruding through a die having a small hole and then cut with a cutter, the styrenic resin particles are suspended in water and a foaming agent made of hydrocarbon is supplied for foaming. The manufacturing method which obtains a functional styrene resin particle is mentioned.

  The temperature of the resin in the melt kneading part of the extruder in the first melt kneading method is preferably 160 ° C to 250 ° C. Moreover, it is preferable that the residence time in an extruder from supplying a material to an extruder until the end of melt-kneading is 7 minutes or less.

  When the resin temperature is higher than 250 ° C. and / or when the residence time in the extruder until the completion of melt kneading is longer than 7 minutes, the brominated flame retardant may be decomposed and desired flame retardancy can be obtained. Or the flame retardant must be added in excess to give the desired flame retardancy.

  On the other hand, when the resin temperature is lower than 160 ° C., the load on the extruder becomes large and the extrusion may become unstable, or the dispersibility of the component to be added may deteriorate. In addition, when extruding through a die immediately after melt kneading, the shear strain and elongation strain of the molten resin increase, resulting in uneven shape of the resin particles, and the degree of particle sticking and flatness in the foaming agent impregnation process In some cases, the process becomes unstable and the process becomes unstable, or the process becomes longer and the productivity is significantly reduced.

  Here, the melt-kneading part of the extruder means from the feed part to the tip of the extruder when it is composed of one extruder having a single screw or a twin screw, and in the case of a tandem extruder. It means from the feed section of the first extruder to the tip of the second extruder.

  The advantage of the first melt-kneading method is that a styrene resin particle can be impregnated with a foaming agent using an apparatus used for production of general expandable styrene resin particles, so that a large capital investment or equipment change is required. This is because the production stability of styrenic resin particles is high even if the amount of graphite, graphite particle size, etc. are changed. On the other hand, since the production of the styrene resin particles and the production of the expandable styrene resin particles are carried out in separate plants, the running cost is higher than that in the second melt-kneading method described later.

  In the second melt-kneading method, a styrene resin, graphite, and a foaming agent are melt-kneaded with an extruder, and the inside of a cutter chamber filled with pressurized circulating water through a die having a small hole attached to the tip of the extruder. There is a method of extruding, cutting with a rotary cutter immediately after extrusion, and cooling and solidifying with pressurized circulating water.

  More specifically, styrene resin, hydrocarbon foaming agent, graphite, bromine flame retardant as necessary, radical generator, heat stabilizer, and other additives, if necessary, melt kneaded in an extruder After cooling the resulting melt-kneaded product to a predetermined temperature, it is extruded through a die having small holes into a cutter chamber filled with pressurized circulating water, and immediately after extrusion, cut by a rotary cutter and pelletized. In addition, there is a production method in which the obtained pellets (resin particles) are cooled and solidified with pressurized circulating water to obtain expandable styrene resin particles.

  In the second melt-kneading method, the temperature of the resin in the melt-kneading part of the extruder is preferably 160 ° C to 250 ° C. Moreover, it is preferable that the residence time in an extruder from supplying a styrene resin and various components to an extruder until the end of melt kneading is 7 minutes or less.

  When the resin temperature is higher than 250 ° C. and / or when the residence time in the extruder until the end of melt kneading is longer than 7 minutes, the same problem as in the first melt kneading method may occur. On the other hand, when the resin temperature is lower than 160 ° C., the load on the extruder becomes large and the extrusion may become unstable, or the dispersibility of the component to be added may deteriorate. In addition, when the resin is extruded through a die immediately after melt-kneading, the shear strain and elongation strain of the molten resin increase, and the resulting resin particles may have irregular shapes. In the case where the shape of the resulting expandable styrene resin particles is not good, the moldability may be deteriorated.

  In the extruder, the foaming agent, radiation heat transfer inhibitor, and other additives such as brominated flame retardants, heat stabilizers, and nucleating agents are dissolved or uniformly dispersed in the styrene resin as appropriate. The molten resin (melt kneaded material) cooled to the temperature is extruded into pressurized cooling water from a die having a plurality of small holes.

  The die used in the present invention is not particularly limited, and examples thereof include those having a small hole with a diameter of 0.3 mm to 2.0 mm, preferably 0.4 mm to 1.0 mm.

  In the second melt-kneading method, the temperature of the molten resin immediately before being extruded from the die is the glass transition temperature of the styrene-based resin in the state containing no foaming agent + 40 ° C. to 100 ° C., more preferably the glass transition temperature + 50 ° C. It is preferable that it is -70 degreeC.

  When the temperature of the molten resin immediately before being extruded from the die is lower than the glass transition temperature + 40 ° C., the viscosity of the extruded molten resin becomes too high and the small holes are clogged. Therefore, the resin particles obtained may be deformed. On the other hand, when the temperature of the molten resin immediately before being extruded from the die is higher than the glass transition temperature + 100 ° C., the extruded molten resin is not completely solidified and foams, or the extruded molten resin In some cases, the viscosity becomes too low to be stably cut by the rotary cutter, and the extruded molten resin winds around the rotary cutter.

  The cutting device for cutting the molten resin extruded into the circulating pressurized cooling water in the second melt-kneading method is not particularly limited. For example, the cutting device is cut by a rotary cutter in contact with a die lip to be spheronized and pressurized. Examples include a device that is transported to a centrifugal dehydrator and dewatered and collected without foaming the circulating cooling water.

  The advantage of the second melt-kneading method is that the running cost is lower than that of the first melt-kneading method because even the expandable styrene resin particles can be produced with the same equipment. On the other hand, since the amount of graphite and the graphite particle size affect the small hole opening ratio of the die, the production stability of the second melt-kneading method is lower than that of the first melt-kneading method.

  On the other hand, as a polymerization method, a styrene monomer or a styrene monomer and a monomer copolymerizable therewith are polymerized in an aqueous suspension in the presence of graphite, and before and / or during polymerization and / or Alternatively, there is a method of impregnating a foaming agent after polymerization.

  As yet another polymerization method, styrene resin, graphite is melt-kneaded with an extruder, extruded through a die having small holes, and cut with a cutter to obtain graphite-containing styrene resin seed particles. Suspend graphite-containing styrene resin seed particles in water and supply seeds by supplying styrene monomers, initiators, and other additives such as brominated flame retardants and nucleating agents as necessary. And / or a method of impregnating the foaming agent during and / or after the polymerization.

  The advantage of the polymerization method is that it can be impregnated with the polymerization and foaming agent using the equipment used for the production of general expandable styrenic resin particles, so that no large capital investment or equipment change is required. On the other hand, in the polymerization method, since the styrene resin seed particles are suspended in water, a large amount of waste water is generated and a drying process is required, so that the influence on the environment is great.

[Pre-expanded particles]
The expandable styrenic resin particles of the present invention obtained as described above are expanded into a conventional well-known pre-foaming step, for example, 10 to 110 times by heated steam to obtain pre-foamed particles, and for a certain period of time as necessary. After curing, it is used for molding. The method for obtaining the styrene resin foam molded article using the expandable styrene resin particles of the present invention is not particularly limited, but preferably, the styrene resin of the present invention including a predetermined pre-foaming method described later. It implements according to the manufacturing method of a foaming molding.

(Molding)
The obtained pre-expanded particles are molded with heated steam using a conventionally known molding machine (for example, in-mold molding) to obtain the styrene resin foam molded article of the present invention. Depending on the shape of the mold used, it is possible to obtain a molded article having a complicated shape or a block-like molded article.

[Styrenic resin foam molding]
The styrene resin foam molded article of the present invention includes, for example, the following first to fourth embodiments.

The styrene resin foam molded article of the first embodiment contains a styrene resin, a foaming agent and graphite, has a graphite content of 3 to 8% by weight, an average particle diameter of graphite of 3 to 7 μm and a specific surface area. It is produced by pre-expanding expandable styrene resin particles having a size of 1.55 m ² / cm ³ or more and molding the resulting pre-expanded particles. The expandable styrene resin particles used here are the graphite-containing expandable styrene resin particles of the present invention described above.

In addition, since the styrenic resin foam molded article of the first embodiment has a characteristic that the thermal conductivity is very low while having a high expansion ratio, the following formula 1, 3 or 4 in the second embodiment is used. Relationship between thermal conductivity A (W / m · K) and expansion ratio B (cm ³ / g) shown, and / or thermal conductivity shown by Formula 2, Formula 5 or Formula 6 in the third embodiment below Satisfies the relationship between C (W / m · K) and expansion ratio D (cm ³ / g).

The foamed molded product of the second embodiment is produced by pre-expanding expandable styrene resin particles and molding the obtained pre-expanded particles in a mold, and contains a styrene resin, a foaming agent and graphite. The graphite content is 3 to 8% by weight of the total amount, the thermal conductivity A (W / m · K) and the expansion ratio B (cm ³ / g) measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. It has the relationship of following formula 1 between these.
Formula 1: A ≦ 0.0251 + 0.0000776 × B

In the foamed molded product of the second embodiment, the thermal conductivity A (W / m · K) and the expansion ratio B (cm ³ / g) preferably have the relationship of the following formula 3, more preferably the following formula: There are four relationships. The foamed molded product of the second embodiment has a characteristic that the thermal conductivity is very low while having a high foaming ratio, and Expressions 1, 3 and 4 represent the characteristics.
Formula 3: A ≦ 0.0248 + 0.0000776 × B
Formula 4: A ≦ 0.0245 + 0.0000776 × B

The foamed molded product of the third embodiment is produced by pre-expanding expandable styrene resin particles and molding the obtained pre-expanded particles in a mold, and contains a styrene resin, a foaming agent and graphite. The thermal conductivity C (W / m · K) and expansion ratio measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. after the graphite content is 3 to 8% by weight of the total amount and dried at 50 ° C. for 30 days. It has the relationship of following formula 2 between D (cm < ³ > / g), It is characterized by the above-mentioned.
Formula 2: C ≦ 0.0276 + 0.0000776 × D

In the foamed molded article of the third embodiment, the thermal conductivity C (W / m · K) and the expansion ratio D (cm ³ / g) preferably have the relationship of the following formula 5, more preferably the following formula: 6 relationships. The foamed molded product of the third embodiment has the characteristics that the thermal conductivity is very low and the low thermal conductivity is maintained over a long period of time while having a high foaming ratio. 6 represents the characteristic.
Formula 5: C ≦ 0.0270 + 0.0000776 × D
Formula 6: C ≦ 0.0267 + 0.0000776 × D

The foamed molded product of the fourth embodiment is produced by pre-expanding expandable styrene resin particles and molding the obtained pre-expanded particles in a mold, and contains a styrene resin, a foaming agent and graphite. The graphite content is 3 to 8% by weight of the total amount, the thermal conductivity A (W / m · K) and the expansion ratio B (cm ³ / g) measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. The thermal conductivity C (W / m · K) measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. after drying for 30 days at 50 ° C. and the expansion ratio D (cm ³ / g) and having the relationship of the above formula 2. In the foam molded article of the fourth embodiment, the relationship between the thermal conductivity A and the expansion ratio B may be the relationship of the above expression 3 or 4 instead of the above expression 1, and the thermal conductivity C and the expansion ratio D This relationship may be the relationship of the above formula 5 or 6 instead of the above formula 2.

  The styrenic resin foam molded article of the present invention has very low thermal conductivity even when the expansion ratio is as high as 40 times or more. For example, the foamed molded product of the first embodiment exhibits a very low thermal conductivity in the range of 0.025 to 0.028 W / m · K at a foaming ratio of 40 times, and the foaming agent of 50 ° C. is easily volatilized. Even after storage for 30 days under temperature, the thermal conductivity is as low as 0.0280 to 0.0310, and the thermal conductivity is kept low for a long period of time, and thus high thermal insulation.

In a conventional graphite-containing styrene resin foam molded article (hereinafter sometimes referred to as “conventional foam molded article”) obtained from conventional graphite-containing expandable styrene resin particles, graphite mainly has holes in the cell membrane. By reducing the closed cell ratio involved in the expansion ratio and thermal conductivity, a high expansion ratio (especially 65 cm ³ / g or more) cannot be achieved, and the styrene resin foam of the present invention can be achieved at each expansion ratio. It was not possible to achieve such a low thermal conductivity as the molded body.

  Although the styrene resin foam molded article of the present invention uses expandable styrene resin particles containing a high amount of graphite as a raw material, the resin particles are used as prefoamed particles by adopting predetermined prefoaming conditions. Thus, it is possible to suppress the graphite from opening a hole in the cell membrane. Therefore, according to the present invention, although the foaming ratio is higher than that of the conventional foamed molded article, the surface aesthetics are not impaired, and the heat insulation equivalent to or higher than that of the conventional foamed molded article can be obtained. Therefore, it is possible to provide a styrenic resin foam molded body having high heat insulation (low thermal conductivity) and high light weight (high expansion ratio) that has not been commercially available at lower cost.

  In addition, the conventional foamed molding obtained from the conventional foamable styrenic resin particles has been problematic in that the foaming agent dissipates over time, the thermal conductivity increases, and the heat insulation deteriorates. In the present invention, since the lower thermal conductivity can be exhibited even after the foaming agent has sufficiently dissipated, high heat insulation can be maintained even after a long time has elapsed.

  In addition, the higher the expansion ratio of the styrene resin foam molded article, the less the amount of the expandable styrene resin particles used as a raw material, the lower the production rate of the styrene resin foam molded article of the present invention. can do. In addition, in the conventional styrene-based resin foam molded article, when the expansion ratio is 40 times or more, the higher the expansion ratio, the higher the thermal conductivity, and there is a drawback that the heat insulation property deteriorates. However, the expandable styrene resin particles of the present invention and / or the styrene resin foam molded article obtained from the production method of the present invention described later have low thermal conductivity even when the expansion ratio is 40 times or more. Therefore, it is possible to supply a heat insulating material having high heat insulating properties, light weight, good handleability, and lower cost.

  The styrenic resin foam molded article of the present invention has low thermal conductivity, has self-extinguishing properties, and can be adjusted to an oxygen index of 26 or more. It can be used suitably.

The expansion ratio of the styrene resin foam molded article of the present invention is preferably 40 cm ³ / g or more, more preferably 50 cm ³ / g or more, still more preferably 60 cm ³ / g or more, particularly preferably 65 cm ³ / g or more, most Preferably it is 65-80 cm < ³ > / g. According to the present invention, a low thermal conductivity can be achieved even when a styrene resin foam molded article having a magnification of 40 times or more is obtained. It can be expressed. In particular, when the expansion ratio is set to 65 to 80 cm ³ / g, the styrenic resin of the present invention in which the heat insulating property, lightness, surface aesthetics, fusion property between the expanded particles therein, and the like are remarkably improved. A foamed molded product can be obtained. In the present specification, the expansion ratio is expressed in units of “times” or “cm ³ / g”, which have the same meaning.

  Since the styrene resin foam molded article of the first embodiment is produced using the above expandable styrene resin particles of the present invention, it contains the same components as those of the resin particles (excluding the foaming agent, etc.). Contains in a range of amounts. The preferred form, more preferred form, and further preferred form of each component are the same as the resin particles. In addition, the content of each component (excluding the foaming agent, etc.) in the foamed molded product is such that a part of the foaming agent is dissipated when the resin particles are prefoamed and molded. There is a tendency to increase compared to the content of each component. In particular, the amount of graphite relative to the weight of the foamed molded product is greater than the amount of graphite relative to the weight of the resin particles.

Moreover, the preferable form of the styrene resin, graphite, and the foaming agent and these components contained in the styrene resin foam molded article of the second to fourth embodiments is the above-described expandable styrene resin particle of the present invention. This is the same as described in the section. In addition, graphite preferably has an average particle diameter of 3 to 7 μm, more preferably an average particle diameter of 3 to 7 μm and a specific surface area of 1.55 m ² from the viewpoint of achieving both high expansion ratio and low thermal conductivity at a high level. The average particle diameter is ^{3 to 7} μm, the specific surface area is 1.55 m ² / cm ³ or more, and the value of (10% particle diameter / 90% particle diameter) is 2.5 or more. The graphite is preferably a graphite mixture containing scaly graphite as a main component, and more preferably scaly graphite. In addition, the preferable range of the average particle size, specific surface area, and (10% particle size / 90% particle size) value of graphite is the same as the range described in the above-mentioned section of expandable styrene resin particles of the present invention. is there. Further, the graphite content and the preferred range thereof in the styrene resin foam molded articles of the second to fourth embodiments are also in the same range as the above-described expandable styrene resin particles of the present invention.

  Moreover, the styrene resin foam molded article of the second to fourth embodiments is selected from the group consisting of a flame retardant, a heat stabilizer, a radical generator, and other additives, as long as the effects of the present invention are not impaired. At least one selected from the above can be contained as an optional component. The other additive is, for example, at least one selected from the group consisting of a processing aid, a light resistance stabilizer, an antistatic agent, a colorant such as a pigment, a nucleating agent, and a foaming aid. These optional components can be the same as those exemplified in the section of expandable styrene resin particles. Among them, a brominated flame retardant is preferable as the flame retardant, and the brominated flame retardant preferably has a bromine content in the styrene resin foam molded article of the second to fourth embodiments, preferably 0.8 to 2.5% by weight. More preferably, it is blended so as to be 1.0 to 2.0% by weight.

(Measurement of thermal conductivity)
In general, it is known that the higher the measurement average temperature of the thermal conductivity, the larger the value of the thermal conductivity. In order to compare the heat insulation, it is necessary to determine the measurement average temperature. In this specification, 23 ° C. defined in JIS A9511: 2006R, which is a standard for foamed plastic heat insulating materials, is adopted as a standard.

  In the present invention, the thermal conductivity A is determined by cutting out a thermal conductivity measurement sample from a styrene resin foam molded article, and allowing the sample to stand at a temperature of 50 ° C. for 48 hours, and further to stand at a temperature of 23 ° C. for 24 hours. Measure after.

  Further, in order to evaluate the thermal conductivity C when the foaming agent is replaced with air after a long period of time, a thermal conductivity measurement sample is cut out from the styrenic resin foam molded article, and the sample is allowed to stand at a temperature of 50 ° C. for 30 days. Furthermore, after leaving still for 24 hours under the temperature of 23 degreeC, the heat conductivity C is measured.

  By drying (annealing) at 50 ° C. for 30 days, the content of hydrocarbon-based foaming agents such as butane and pentane contained in the styrene-based resin foamed molded article is 0.5% or less, and heat conduction The influence on the rate is negligible, and the thermal conductivity C when the styrene resin foam molded article is used at room temperature for a long time can be evaluated almost accurately.

  The styrenic resin foam molded article of the present invention can be used for various applications as shown below, for example.

(Insulation for construction)
Since heat insulating materials such as houses are used for more than 10 years, maintaining heat insulation after a long period of time has become an important issue. Since the styrenic resin foam molded article obtained in the present invention can lower the thermal conductivity after a long period of time compared to conventional styrene resin foam molded articles, it can be used for floors, walls, roofs, etc. It can be suitably used as a heat insulating material.

(Agriculture and fishery box)
Since the styrenic resin foam molded article obtained in the present invention can lower the thermal conductivity after a long period of time compared to conventional styrene resin foam molded articles, boxes and vegetables for transporting fish and other marine products It can use suitably for the box which conveys agricultural products, such as. An agricultural and fishery box with high heat insulation can reduce the amount of ice when transporting fresh fish, and can maintain good freshness of vegetables and the like even in summer.

(Insulation for bathroom)
In recent years, heat insulating materials are sometimes used on bathroom walls, ceilings, floors, and bathtubs in order to prevent a decrease in bath temperature. Since the styrenic resin foam molded article obtained in the present invention can lower the thermal conductivity after a long period of time as compared with a conventional styrene resin foam molded article, it can be suitably used as a heat insulating material for bathrooms.

(Hot water storage tank insulation)
Insulating materials are used in hot water storage tanks such as Ecocute (trade name) in order to prevent a drop in hot water temperature. Since the styrenic resin foam molded article obtained in the present invention can lower the thermal conductivity after a long period of time compared to the conventional styrene resin foam molded article, it can be suitably used as a heat insulating material for hot water storage tanks. .

[Method for producing styrene resin foam molded article]
The manufacturing method of the 1st and 2nd styrene-type resin foam molding of this invention is characterized by including a predetermined | prescribed foaming process.
That is, the first method for producing a styrene resin foam molded article (hereinafter, simply referred to as “first production method”) is to introduce steam into the expandable styrene resin particles placed in the can of the preliminary foaming machine. A pre-foaming step for obtaining pre-foamed particles; and a molding step for molding the pre-foamed particles in-mold, adjusting the graphite content in the styrene resin foam molded article to 3 to 8% by weight, and the pre-foaming step By setting the water vapor charging time in 50 to 500 seconds, the styrene-based resin foam molding having the relationship of the above formula 1 between the thermal conductivity A (W / m · K) and the foaming ratio B (cm ³ / g) It is characterized by obtaining a body.

In addition, a method for producing a second styrenic resin foam molded article (hereinafter simply referred to as “second production method”) is a method in which water vapor is introduced into expandable styrenic resin particles placed in a can of a pre-foaming machine. A pre-foaming step for obtaining pre-foamed particles; and a molding step for molding the pre-foamed particles in-mold, adjusting the graphite content in the styrene resin foam molded article to 3 to 8% by weight, and the pre-foaming step By setting the water vapor input time in 50 to 500 seconds, the styrene resin foam molding having the relationship of the above formula 2 between the thermal conductivity C (W / m · K) and the foaming ratio D (cm ³ / g) It is characterized by obtaining a body.

  Hereinafter, the first and second manufacturing methods will be described in more detail in the order of the preliminary foaming step and the molding step.

(Pre-foaming process)
The pre-foaming step uses a pre-foaming machine, adjusts the graphite content in the finally obtained styrenic resin foam molded article to be 3 to 8% by weight, and sets the steam charging time in the pre-foaming step. Except for 50 to 500 seconds, it can be carried out in the same manner as the pre-foaming of conventional expandable styrene resin particles.

  As the pre-foaming machine, a known one can be used, for example, a can equipped with a stirrer and containing expandable styrenic resin particles, a steam chamber installed under the can and supplying water vapor to the can A pre-foaming machine including a pre-foamed particle discharge port is used. Steam is supplied to the steam chamber from the boiler. Steam and compressed air can be mixed and supplied to the steam chamber. In this specification, the water vapor temperature is the temperature of water vapor introduced into the vapor chamber, and more specifically, the temperature of water vapor 10 cm upstream from the water vapor inlet of the vapor chamber. In addition, the water supply time (seconds) is such that after the supply of water vapor to the expandable styrene resin particles placed in the can is started, the expandable styrene resin particles become pre-expanded particles. This is the time during which steam was added before taking it out of the can. When water vapor is introduced into the can of the pre-foaming machine in a plurality of times, the sum of the time during which the water is introduced is regarded as the water vapor introduction time.

  The can internal pressure (gauge pressure) can be controlled, for example, by adjusting the opening of the exhaust valve. In this specification, the internal pressure of the can is the internal pressure of the can during the introduction of water vapor, and when the internal pressure varies during the introduction of the water vapor, the internal pressure is measured every predetermined time (for example, 1 second). It is obtained as an arithmetic average value of the measured values. In the pressure foaming method, there are cases where water vapor is intermittently introduced. Even if the supply of water vapor from the steam chamber to the can is stopped, the water vapor atmosphere in the can continues, so in this case, the time during which the pressure inside the can is maintained above atmospheric pressure is the time when steam is supplied. Include in time.

  In the pre-foaming step, the water vapor input time is 50 seconds to 500 seconds, preferably 80 seconds to 300 seconds, and more preferably 100 seconds to 200 seconds. Due to the steam introduction time being within the above range, the expansion ratio and the independent expansion ratio are high, the styrenic system of the present invention that maintains a very low thermal conductivity over a long period of time from the beginning of manufacture, and also has excellent surface beauty. A resin foam molding can be obtained. The reason why such an effect can be obtained is not sufficiently clear at present, but it is presumed that, despite the high content of graphite, it is suppressed that the graphite perforates the cell membrane. It should be noted that the selection of the water vapor charging time in the pre-foaming step is normally performed, but it is not clear at present how the water vapor charging time affects a system containing a high amount of graphite.

When the water vapor charging time is less than 50 seconds, it is necessary to increase the water vapor temperature in order to make the expandable resin particles have a predetermined expansion ratio. It tends to occur and tends to reduce the prefoaming yield. If the water vapor input time exceeds 500 seconds, the resulting pre-expanded particles shrink significantly, making it difficult to obtain pre-expanded particles having a high expansion ratio, and a styrene system having a high expansion ratio (particularly 65 cm ³ / g or more). There exists a tendency for it to become difficult to obtain a resin foaming molding, or the surface beauty of the obtained foaming molding is impaired.

  Moreover, the graphite content in the finally obtained styrenic resin foam molded article can be adjusted, for example, by appropriately selecting the graphite content in the expandable styrene resin particles. In addition, the graphite content in the styrene-based resin foamed molded product tends to increase more than the graphite content in the expandable styrene-based resin particles due to volatilization of the foaming agent in the preliminary foaming step and the molding step. Considering this point, the graphite content of the expandable styrene resin particles may be selected.

The internal pressure (cage pressure) at the time of introducing steam is not particularly limited, but is preferably 0.001 to 0.15 MPa, more preferably 0.01 to 0.10 MPa, and further preferably 0.03 to 0.08 MPa. . If the pressure inside the can is less than 0.001 MPa, when a high expansion ratio (especially 65 cm ³ / g or more) is obtained, it takes a long time for pre-foaming, and it tends to be difficult to make the steam input time 500 seconds or less. is there. When the pressure inside the can exceeds 0.15 MPa, it is necessary to increase the pressure of water vapor. However, if this is done, the number of occurrences of blocking phenomenon increases, and the prefoaming yield tends to decrease. In addition, by mixing water vapor with air, it is possible to adjust the water vapor temperature, to easily control the time for adding water vapor until the pre-expanded particles reach a predetermined expansion ratio, and to increase the closed cell ratio of the pre-expanded particles. Can be.

  The water vapor temperature can be adjusted by mixing water vapor and air. By mixing water vapor and air, it is possible to easily control the time for adding water vapor until a predetermined expansion ratio is reached, and to increase the closed cell ratio of the pre-expanded particles.

Although the temperature of the water vapor introduced into the can is not particularly limited, it is preferably more than 100 ° C., 130 ° C. or less, more preferably 105 to 125 ° C., further preferably 105 to 120 ° C. When the water vapor temperature is 100 ° C. or lower, when obtaining a high expansion ratio (particularly 65 cm ³ / g or more), it takes a long time for pre-foaming, and it tends to be difficult to make the water vapor input time 500 seconds or less. is there. When the water vapor temperature exceeds 130 ° C., the number of blocking phenomena increases and the prefoaming yield tends to decrease.

Moreover, it is preferable to perform preliminary foaming of the expandable styrene resin particles in one stage. By performing pre-foaming in one stage, a styrenic resin foam molded article with not only excellent heat insulation and light weight but also improved surface beauty and fusion between foam particles inside is obtained. Can do. When pre-foaming is performed in two stages, a high foaming ratio (for example, 65 cm ³ / g or more) can be easily obtained, but there is a tendency that the surface aesthetics and the fusibility between the foamed particles inside are lowered. is there.

Further, the preliminary foaming step can be performed by either a continuous method or a batch method.
The continuous method is a method of continuously supplying the expandable styrene resin particles into the can and discharging the pre-expanded particles from the discharge port provided in the upper portion of the can. The expansion ratio of the pre-expanded particles can be adjusted, for example, by appropriately selecting the amount (weight) of the expandable styrenic resin particles that are charged per time into the can. In the case of the continuous process, the residence time in the pre-foaming machine can from when the expandable styrenic resin particles are supplied into the can until the pre-expanded particles are discharged is referred to as the steam input time.

  In the batch method, a predetermined amount of expandable styrenic resin particles is placed in a can, pre-expanded to a predetermined expansion ratio, and then the supply of water vapor is stopped. Then, if necessary, air is introduced into the can. This is a method in which the pre-foamed particles are blown, cooled and dried, and taken out from the can. The expansion ratio of the pre-expanded particles can be adjusted by appropriately selecting the input amount (weight) of the expandable styrene resin particles into the can per batch. The batch method is a method in which the expanded foamed styrene resin particles are pre-expanded to a predetermined volume. Therefore, as the input amount per batch is reduced, the expansion ratio of the obtained pre-expanded particles is increased.

  Next, in the molding step, a styrene resin foam molded article can be obtained in the same manner as in the conventional foam molding method except that the pre-expanded particles obtained above are used.

  The average cell diameter of the styrene resin foam molded article is preferably adjusted to 70 to 250 μm, more preferably 90 to 200 μm, and still more preferably 100 to 180 μm. When the average cell diameter is in the above range, a styrenic resin foam molded article having high heat insulation is obtained. When the average cell diameter is less than 70 μm, the closed cell ratio of the foamed molded product is lowered, and when it exceeds 250 μm, the heat insulating property is lowered. The average cell diameter can be adjusted, for example, by appropriately selecting the amount of the nucleating agent.

  Moreover, in this invention, it is preferable to adjust the closed cell rate of a pre-expanded particle and a styrene resin foaming molding to 97 to 100%, respectively. When the closed cell ratio of the pre-expanded particles is less than 97%, the surface aesthetics of the styrene resin foam molded article obtained using the pre-expanded particles tends to be lowered. Further, when the closed cell ratio of the styrene resin foam molded article is less than 97%, the heat insulating property tends to be lowered. The closed cell ratio can be adjusted, for example, by introducing a mixture of water vapor and air into a can or a molding die and appropriately selecting the ratio of water vapor in the mixture.

  EXAMPLES Hereinafter, the present invention will be specifically described with reference to examples and comparative examples, but is not limited thereto. In the following, unless otherwise specified, “part” and “%” represent “part by weight” and “% by weight”, respectively.

  In addition, the measuring method and evaluation method in an Example are as follows.

(1) Thermal conductivity A of styrenic resin foam molding
A sample having a length of 300 mm and a width of 300 mm was cut out from the styrene-based resin foam molding. For the thickness direction, the thickness of 25 mm of the styrene resin foam molded article was used as it was. Accordingly, the two surfaces of the sample length 300 mm × width 300 mm remain as they were when the styrene resin foam molded article was molded. Such a molded surface is generally called a surface skin. The sample was allowed to stand at a temperature of 50 ° C. for 48 hours, and further allowed to stand at a temperature of 23 ° C. for 24 hours, and then a thermal conductivity measuring device (Hidehiro Seiki Co., Ltd., HC-074) was used. The thermal conductivity A was measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. by a heat flow meter method in accordance with JIS A1412-2: 1999.

(2) Thermal conductivity C of styrenic resin foam molding after drying at 50 ° C. for 30 days
A sample having a length of 300 mm, a width of 300 mm, and a thickness of 25 mm was cut out from the styrenic resin foam molded article in the same manner as in (1). The sample was allowed to stand at a temperature of 50 ° C. for 30 days, and further allowed to stand at a temperature of 23 ° C. for 24 hours. Then, using a thermal conductivity measuring device (HC-074 manufactured by Eihiro Seiki Co., Ltd.), The thermal conductivity C was measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. by a heat flow meter method according to JIS A1412-2: 1999.

(3) Graphite content About 10 mg of expandable styrene resin particles were collected, or about 10 mg of a test piece was cut out from the styrene resin foam molded article to prepare a sample. This sample was continuously subjected to the following I to III using a thermogravimetric apparatus (TG / DTA 220U, manufactured by SII NanoTechnology Co., Ltd.) equipped with a thermal analysis system: EXSTAR6000. The amount is the graphite weight and is expressed as a percentage of the specimen weight.

I. I. Temperature was raised from 40 ° C. to 600 ° C. at 20 ° C./min under a nitrogen stream of 200 mL / min and then kept at 600 ° C. for 10 minutes II. Lower the temperature from 600 ° C. to 400 ° C. at 10 ° C./min under a nitrogen flow of 200 mL / min, and hold at 400 ° C. for 5 minutes III. The temperature was raised from 400 ° C. to 800 ° C. at 20 ° C./min under an air stream of 200 mL / min and then held at 800 ° C. for 15 minutes

(4) Measurement of average particle diameter (μm), specific surface area (m ² / cm ³ ) of graphite, 90% particle diameter and 10% particle diameter Laser diffraction / scattering particle size analyzer (manufactured by Nikkiso Co., Ltd., Microtrac MT3300) II). Graphite was dispersed in water, and the particle size distribution and specific surface area were measured by a laser diffraction scattering method. The average particle size was defined as the particle size when the cumulative volume from the smaller particle size with respect to the volume of all particles was 50%. In addition, the particle size when the cumulative volume from the smaller particle size with respect to the volume of all particles becomes 10% is 10%, the particle size when the cumulative volume from the smaller particle size is 90%. A value obtained by dividing the 90% particle diameter by the 10% particle diameter was calculated as 90% particle diameter, and the value was (90% particle diameter / 10% particle diameter).
Measurement conditions: solvent = water, solvent refractive index = 1.333, particle permeability = absorption

(5) Method for measuring bromine content The bromine content was determined by quantitative analysis of bromine by the following ion chromatography method (hereinafter abbreviated as "IC method") after the following oxygen flask combustion method.

[Oxygen flask combustion method]
A sample (styrene resin foamed molded article 5 mg) is placed in the center of the filter paper having the igniter, and the filter paper is folded in three in the vertical direction while the igniter is fixed. Thereafter, the filter paper is folded in three in the horizontal direction, and the filter paper containing the sample is put in a platinum basket attached to a stopper (glass stopper) of a 500 ml combustion flask. On the other hand, 25 ml of absorption liquid (ultra pure water with 1 drop of saturated hydrazine added) is added to the Erlenmeyer flask of the combustion flask and further filled with oxygen.

  The ignition part of the filter paper is ignited, a platinum basket with the filter paper fixed is inserted into the Erlenmeyer flask, and the sample is burned inside the Erlenmeyer flask. After the completion of combustion, the combustion flask is tilted and shaken for 2 minutes, and then left for 1 hour, so that bromine generated by the combustion is absorbed by the absorbent.

[IC method]
The amount of bromine ions was measured for the absorbent obtained by the oxygen flask combustion method by the ion chromatography method under the following conditions.

Model: manufactured by Dionex, ICS-2000
Column: IonPac AG18, AS18 (4mmφ × 250mm)
Eluent: KOH gradient (using eluent generator)
Volumetric flow rate: 1.0 ml / min Sample injection volume: 50 μl
Detector: Electrical conductivity detector The bromine concentration in the sample was calculated using the following equation.

  Bromine concentration in sample (%) = [{IC measurement result of styrene-based resin foam molded article (mg / l) -blank test result (mg / l)} × 25 (ml) × 1000] / {sample collection amount ( mg) × 10000}

(6) Foaming ratio A sample having a length of 300 mm, a width of 300 mm, and a thickness of 25 mm was cut out from the styrene-based resin foam molded article in the same manner as in (1). While measuring the weight (g) of the sample, the vertical dimension, the horizontal dimension, and the thickness dimension were measured using a caliper. The volume (cm ³ ) of the sample was calculated from each measured dimension, and the expansion ratio was calculated according to the following formula.

Foaming ratio (times) = sample volume (cm ³ ) / sample weight (g)
The expansion ratio (times) of styrenic resin foam molded products is conventionally determined in cm ³ / g.

(7) Evaluation method of flame retardancy of styrenic resin foam molding (self-extinguishing)
The obtained molded foam was allowed to stand for 48 hours at a temperature of 60 ° C., and further allowed to stand for 24 hours at a temperature of 23 ° C., followed by JIS A9511: 2006R (foamed plastic heat insulating material) measurement method A. A similar evaluation was performed.
○: Fire extinguishing time is within 3 seconds.
X: Fire extinguishing time exceeded 3 seconds or did not extinguish.
The obtained foamed molded article was allowed to stand for 48 hours at a temperature of 60 ° C. and further allowed to stand for 24 hours at a temperature of 23 ° C., and then the minimum oxygen index was measured according to JIS K7201.

(8) Evaluation Method of Average Cell Diameter of Styrenic Resin Foam Molded Article A styrene resin foam molded article was cut with a razor, and a cross section was observed with an optical microscope. The number of cells existing in the range of 1000 μm × 1000 μm square (100 mm × 100 mm square in a 100 × image) of the cross section was measured, and the value measured by the following formula (area average diameter) was taken as the average cell diameter. The average cell diameter of five samples was measured, and the average was taken as the average cell diameter.
Average cell diameter (μm) = 2 × (1000 μm × 1000 μm / number of cells) ^1/2

(9) Evaluation method of closed cell ratio of pre-expanded particles and styrene resin foam molded article Using the air comparison type hydrometer (manufactured by BECKMAN, Model 930), the obtained pre-expanded particles and styrene resin foam molded article The closed cell volume was calculated by dividing the closed cell volume by the apparent volume separately obtained by the ethanol immersion method.

(10) Evaluation method of surface beauty of styrenic resin foam molded article The surface beauty of styrene resin foam molded article is obtained by storing the molded styrene resin foam molded article in a drying room at about 35 ° C all day and night. The panel was visually observed by 10 panelists and evaluated according to the following 5 levels. The value of each panel was arithmetically averaged, and the evaluation value was obtained by rounding off the second decimal place.
5: It is beautiful with almost no particle gaps.
4; Some particle gaps are seen.
3; lowest level at which there is a particle gap but no practical problem.
2: There are many particle gaps and there is a problem.
1: Level that cannot be used

(11) Evaluation method of blocking amount at the time of pre-foaming Pre-foamed particles are passed through a 1 cm sieve and the weight of a block of several pre-foamed particles remaining on the sieve (blocking) is measured. The ratio with respect to the weight of the expandable styrenic resin particles used in the above was calculated by the following formula, and used as the blocking amount (%) at the time of preliminary foaming.
Blocking amount (%) = (X / Y) × 100.
[Wherein, X represents the weight of blocking, and Y represents the weight of expandable styrene resin particles. ]

  The raw materials used in the examples and comparative examples are shown below.

(Styrene resin)
(A) Polystyrene homopolymer [PS Japan Co., Ltd., 680]
(Foaming agent)
(B1) Normal pentane [Wako Pure Chemical Industries, Ltd., reagent product]
(B2) Isopentane [Wako Pure Chemical Industries, Ltd., reagent product]

(Graphite)
(C1) Graphite [manufactured by Maruho Castings Co., Ltd., scaly graphite SGP-40B]
(C2) Graphite [manufactured by Ito Graphite Industries Co., Ltd., scaly graphite W-5]
(C3) Graphite [manufactured by Nippon Graphite Industry Co., Ltd., scaly graphite J-CPB]
(C4) Graphite [manufactured by Ito Graphite Industry Co., Ltd., scaly graphite X-10]
(C5) Graphite [manufactured by Chuetsu Graphite Co., Ltd., scaly graphite BF-3AK]
(C6) Graphite [manufactured by Chuetsu Graphite Co., Ltd., scaly graphite BF-10AK]
(C7) Graphite [manufactured by Nippon Graphite Industry Co., Ltd., scaly graphite UCP]

(Brominated flame retardant)
(D) 2,2-bis [4- (2,3-dibromo-2-methylpropoxy) -3,5-dibromophenyl] propane [Daiichi Kogyo Seiyaku Co., Ltd., SR-130: 1% weight reduction Temperature = 231 ° C., bromine content = 66%]
(Heat stabilizer)
(E1) Tetrakis (2,2,6,6-tetramethylpiperidyloxycarbonyl) butane (E2) Bis (2,6-di-t-butyl-4-methylphenyl) pentaerythritol diphosphite [manufactured by Chemtura, Ultranox 626]
(A mixture of brominated flame retardant and heat stabilizer)
(F) 3 parts of (E1) and 2 parts (E2) were mixed as thermal stabilizers with 95 parts of brominated flame retardant (D).

(Nucleating agent)
(G) Talc [manufactured by Hayashi Kasei Co., Ltd., Talcan powder PK-S]

(Graphite masterbatch)
(H1) 100 parts of polystyrene homopolymer (A) and 67 parts of graphite (C1) are put into a Banbury mixer, melted and kneaded at a preset temperature of 220 ° C. for 10 minutes, and then supplied to the ruder and attached to the tip. The strand-shaped resin extruded through a die having a discharge rate of 300 kg / hr was cooled and solidified in a water bath at 20 ° C., and then cut to obtain a master batch. The graphite content in the masterbatch was 40%.

  (H2) A master batch was obtained in the same manner as (H1) except that graphite (C2) was used instead of graphite (C1). The graphite content in the masterbatch was 40%.

  (H3) A master batch was obtained in the same manner as (H1) except that graphite (C3) was used instead of graphite (C1). The graphite content in the masterbatch was 40%.

  (H4) A master batch was obtained in the same manner as (H1) except that graphite (C4) was used instead of graphite (C1). The graphite content in the masterbatch was 40%.

  (H5) A master batch was obtained in the same manner as (H1) except that graphite (C5) was used instead of graphite (C1). The graphite content in the masterbatch was 40%.

  (H6) A master batch was obtained in the same manner as (H1) except that graphite (C6) was used instead of graphite (C1). The graphite content in the masterbatch was 40%.

  (H7) A master batch was obtained in the same manner as (H1) except that graphite (C7) was used instead of graphite (C1). The graphite content in the masterbatch was 40%.

(Masterbatch of mixture of brominated flame retardant and heat stabilizer)
(I) After supplying 100 parts of polystyrene homopolymer (A) to a twin screw extruder and melt-kneading, 73 parts of a mixture (F) of a brominated flame retardant and a heat stabilizer is supplied from the middle of the extruder. Further, melt kneading was performed. The strand-shaped resin extruded at a discharge rate of 300 kg / hr is cooled and solidified in a water bath at 20 ° C. through a die having a small hole attached to the tip of the extruder, and then cut to obtain a brominated flame retardant and a thermal stabilizer. A master batch of the mixture was obtained. At this time, the set temperature of the extruder was 170 ° C. The brominated flame retardant content in the masterbatch was 40%.

  In the following, Examples 1 to 19 and Comparative Examples 1 to 5 relate to a styrene resin foam molded article of the present invention, and Examples 20 to 36 and Comparative Examples 6 to 14 show the expandable styrene resin particles of the present invention and the same. Examples 37 to 53 and Comparative Examples 15 to 25 relate to a method for producing a styrene resin foam molded article of the present invention, regarding the production method, pre-expanded particles using the expandable resin particles, and styrene resin foam.

Example 1
[Production of styrene resin particles]
Master batch (I) 5.95 parts of a mixture of a brominated flame retardant and a heat stabilizer, 8.75 parts of graphite master batch (H1), talc (G ) 0.2 part was put into a blender and blended for 10 minutes to obtain a resin composition.

  The obtained resin composition was supplied to a single screw extruder having a diameter of 90 mm, melted and kneaded in the extruder, and discharged through a die having 140 small holes with a diameter of 1.4 mm attached to the tip of the extruder. The strand-shaped resin extruded at 335 kg / hour was cooled and solidified in a 20 ° C. water tank, and then styrene resin particles were obtained with a strand cutter. At this time, the temperature of the resin at the tip of the extruder was 245 ° C., and the residence time in the extruder was 3 minutes.

[Production of expandable styrene resin particles]
In a 6 L autoclave with a stirrer, 200 parts of deionized water, 1 part of tricalcium phosphate, 0.03 part of sodium dodecylbenzenesulfonate, 4 parts of sodium chloride with respect to 100 parts of the resulting styrene resin particles The autoclave was sealed. Thereafter, after heating to 105 ° C. in 1 hour, 8 parts of mixed pentane [a mixture of 80% normal pentane (B1) and 20% isopentane (B2)] as a blowing agent was added to the autoclave over 25 minutes, The temperature was raised to 115 ° C. over 10 minutes and held there for 4 hours.

  Next, it is cooled to room temperature, and the resin particles impregnated with the blowing agent are taken out from the autoclave, pickled with hydrochloric acid, washed with water, dehydrated with a centrifuge, and the moisture adhering to the surface of the resin particles with an air dryer. Drying was performed to obtain expandable styrene resin particles.

  After dry blending 0.08 part of zinc stearate with respect to 100 parts of the obtained expandable styrene resin particles, it was stored at 15 ° C.

[Preparation of pre-expanded particles]
Two weeks after producing expandable styrene resin particles and storing them at 15 ° C., the expandable styrene resin particles were put into a pre-foaming machine [manufactured by Daikai Kogyo Co., Ltd., BHP-300], and steam of 0.08 MPa was used. Was introduced into a pre-foaming machine and foamed to obtain pre-foamed particles having a bulk magnification of 40 times.

  Similarly, pre-expanded particles of 50 times, 60 times, 70 times and 80 times in bulk magnification were obtained.

[Production of Styrenic Resin Foamed Molding]
Inside the in-mold molding die (length 450 mm × width 310 mm × thickness 25 mm) in which the obtained pre-expanded particles having a bulk magnification of 40 times were attached to a foamed polystyrene molding machine [manufactured by Daisen Industry Co., Ltd., KR-57] Then, 0.06 MPa of water vapor was introduced and foamed in the mold, and then the mold was sprayed with water for 3 seconds to cool. The styrenic resin foam molded product is held in the mold until the pressure at which the styrenic resin foam molded product presses the mold is 0.015 MPa (gauge pressure), and then the styrenic resin foam molded product is taken out and a rectangular solid with a beautiful appearance. A styrene-based resin foam molding was obtained. The expansion ratio was 40 times.

  Similarly, styrene-based resin foam molded articles were prepared from pre-expanded particles having a bulk magnification of 50 times, 60 times, 70 times, and 80 times. The expansion ratios were 50 times, 60 times, 70 times, and 80 times, respectively.

(Example 2)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 1 except that 83.85 parts of styrene resin (A) and 10 parts of graphite masterbatch (H1) were used. It was.

Example 3
In [Production of Styrenic Resin Particles], the styrenic resin foam molded article was prepared in the same manner as in Example 1 except that 81.35 parts of styrene resin (A) and 12.5 parts of graphite masterbatch (H1) were used. Got.

Example 4
In [Production of Styrenic Resin Particles], a styrene resin foamed molded article was prepared by the same operation as in Example 1 except that 76.35 parts of styrene resin (A) and 17.5 parts of graphite masterbatch (H1) were changed. Got.

(Example 5)
In [Production of styrene resin particles], the mixture was changed to 89.8 parts of styrene resin (A) and 10 parts of graphite masterbatch (H1), and a masterbatch (I) of a mixture of brominated flame retardant and heat stabilizer A styrene resin foam molded article was obtained by the same operation as in Example 1 except that was not used.

(Example 6)
A styrene resin foam molded article was obtained by the same operation as in Example 1 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 7)
A styrene resin foam molded article was obtained by the same operation as in Example 2 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 8)
A styrene resin foam molded article was obtained by the same operation as in Example 3 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

Example 9
A styrene resin foam molded article was obtained by the same operation as in Example 4 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 10)
A styrene resin foam molded article was obtained by the same operation as in Example 5 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 11)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 2 except that the graphite master batch (H1) was changed to the graphite master batch (H2).

(Example 12)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 4 except that the graphite master batch (H1) was changed to the graphite master batch (H2).

( Reference Example 13)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 2 except that the graphite master batch (H1) was changed to the graphite master batch (H3).

( Reference Example 14)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 4 except that the graphite master batch (H1) was changed to the graphite master batch (H3).

( Reference Example 15)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 2 except that the graphite master batch (H1) was changed to the graphite master batch (H4).

( Reference Example 16)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 4 except that the graphite master batch (H1) was changed to the graphite master batch (H4).

(Example 17)
[Production of expandable styrene resin particles]
Blender of bromine flame retardant and heat stabilizer mixture (F) 2.5 parts, graphite (C1) 4 parts, talc (G) 0.2 parts with respect to 93.3 parts of styrene resin (A) And blended for 10 minutes to obtain a resin composition. The obtained resin composition is supplied to a tandem type two-stage extruder in which a single screw extruder (first extruder) having a diameter of 65 mm and a single screw extruder (second extruder) having a diameter of 90 mm are connected in series. Melt kneading was performed at a set temperature of 220 ° C. in a 65 mm extruder. From the middle of the 65 mm caliber extruder (first extruder), press-fit at a rate of 8 parts of mixed pentane [mixture of 80% normal pentane (B1) and 20% isopentane (B2)] to 100 parts of the resin composition. did. Then, it supplied to the 90-mm-diameter extruder (2nd extruder) through the continuation pipe | tube set to 230 degreeC.

After cooling the molten resin to 167 ° C. with a 90 mm diameter extruder (second extruder), the diameter is 0.7 mm and the land length is 3.0 mm attached to the tip of the second extruder set at 275 ° C. A die lip having 40 small holes was extruded into pressurized circulating water at a temperature of 60 ° C. and 0.9 MPa at a discharge rate of 50 kg / hour. The extruded molten resin is cut and pulverized under a condition of 2500 rpm using a rotary cutter having 10 blades in contact with the die lip, and is transferred to a centrifugal dehydrator to obtain expandable styrene resin particles. It was. At this time, the residence time in the first extruder was 4 minutes.
After dry blending 0.08 part of zinc stearate with respect to 100 parts of the obtained expandable styrene resin particles, it was stored at 15 ° C.

[Preparation of pre-expanded particles]
Pre-expanded particles were obtained in the same manner as in Example 1.
[Production of Styrenic Resin Foamed Molding]
A styrene resin foam molded article was obtained in the same manner as in Example 1.

(Example 18)
In [Production of expandable styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 17 except that 90.3 parts of styrene resin (A) and 7 parts of graphite (C1) were changed. It was.
Table 1 shows the evaluation results of the styrenic resin foam molded articles obtained in Examples 1 to 12, 17, 18, and Reference Examples 13 to 16 . In Table 1, Examples 13 to 16 mean Reference Examples 13 to 16.

(Comparative Example 1)
In [Production of Styrenic Resin Particles], the styrene resin foam molding is carried out in the same manner as in Example 1 except that the styrene resin (A) is changed to 93.85 parts and the graphite masterbatch (H1) is not used. Got the body.

(Comparative Example 2)
In [Preparation of Styrenic Resin Particles], the styrene resin (A) is changed to 99.8 parts, and the master batch (I) of the graphite masterbatch (H1) and the mixture of brominated flame retardant and heat stabilizer is changed. A styrene resin foam molded article was obtained by the same operation as in Example 1 except that it was not used.

(Comparative Example 3)
In [Production of styrene resin particles], styrene resin foaming was carried out in the same manner as in Example 1 except that 87.6 parts of styrene resin (A) and 6.25 parts of graphite masterbatch (H1) were changed. A molded body was obtained.

(Comparative Example 4)
In [Production of styrene resin particles], the same operation as in Example 1 was carried out except that the styrene resin (A) was changed to 68.85 parts and the graphite master batch (H1) was changed to 25 parts. Since the gap between the foamed styrene resin particles on the surface of the body was not filled, the surface was not smooth, and the foamed molded product was greatly shrunk immediately after molding, so a sample that could be evaluated was not obtained.
Table 2 shows the evaluation results of the styrene resin foam molded articles obtained in Comparative Examples 1 to 4.

(Example 19)
The following No. 1-9 styrene resin particles and styrene resin foam molded articles were produced. No. Reference numerals 8 and 9 are reference examples.
<No. 1>
In [Production of Styrenic Resin Particles], expandable resin particles are obtained by the same operation as in Example 1 except that the styrene resin (A) is changed to 85.91 parts and the graphite masterbatch (H1) is 7.94 parts. Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrenic resin foam molded article was 3.1%.

<No. 2>
In [Production of Styrenic Resin Particles], expandable resin particles are obtained by the same operation as in Example 1 except that the styrene resin (A) is 79.76 parts and the graphite masterbatch (H1) is 14.09 parts. Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrenic resin foam molded article was 5.5%.

<No. 3>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained by the same operation as in Example 1 except that 77.19 parts of styrene resin (A) and 16.66 parts of graphite masterbatch (H1) were changed. Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrenic resin foam molded article was 6.5%.

<No. 4>
In [Production of Styrenic Resin Particles], expandable resin particles are obtained by the same operation as in Example 1 except that the styrene resin (A) is changed to 74.63 parts and the graphite masterbatch (H1) is changed to 19.22 parts. Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrene resin foam molded article was 7.5%.

<No. 5>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained by the same operation as in Example 1 except that 73.35 parts of styrene resin (A) and 20.50 parts of graphite masterbatch (H1) were changed. Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrenic resin foam molding was 8.0%.

<No. 6>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained in the same manner as in Example 2 except that the graphite master batch (H1) was changed to a graphite master batch (H5) using scaly graphite BF-3AK. In addition, a styrene resin foam molded article was obtained.

<No. 7>
In [Production of styrene resin particles], expandable resin particles were obtained in the same manner as in Example 4 except that the graphite master batch (H1) was changed to a graphite master batch (H5) using scaly graphite BF-3AK. In addition, a styrene resin foam molded article was obtained.

<No. 8>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained in the same manner as in Example 2, except that the graphite master batch (H1) was changed to a graphite master batch (H6) using scaly graphite BF-10AK. In addition, a styrene resin foam molded article was obtained.

<No. 9>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained in the same manner as in Example 4 except that the graphite master batch (H1) was changed to a graphite master batch (H6) using scaly graphite BF-10AK. In addition, a styrene resin foam molded article was obtained.

(Comparative Example 5)
The following No. 10 to 14 expandable resin particles and a styrene resin foam molded article were produced.
<No. 10>
In [Production of Styrenic Resin Particles], expandable resin particles are obtained by the same operation as in Example 1 except that the styrene resin (A) is changed to 91.29 parts and the graphite masterbatch (H1) is 2.56 parts. Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrene resin foam molded article was 1.0%.

<No. 11>
In [Production of Styrenic Resin Particles], expandable resin particles are obtained by the same operation as in Example 1 except that the styrene resin (A) is 88.73 parts and the graphite masterbatch (H1) is 5.13 parts. Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrene resin foam molded article was 2.0%.

<No. 12>
In [Preparation of Styrenic Resin Particles], the expandable resin particles were prepared in the same manner as in Example 1 except that they were changed to 72.07 parts of styrene resin (A) and 21.78 parts of graphite masterbatch (H1). Furthermore, a styrene resin foam molded article was obtained. The graphite content of the styrenic resin foam molded article was 8.5%.

<No. 13>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained by the same operation as in Example 2 except that the graphite master batch (H1) was changed to a graphite master batch (H7) using scaly graphite UCP. Furthermore, a styrene resin foam molded article was obtained.

<No. 14>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained by the same operation as in Example 4 except that the graphite master batch (H1) was changed to a graphite master batch (H7) using scaly graphite UCP. Furthermore, a styrene resin foam molded article was obtained.

  Table 3 shows the evaluation results of the styrene-based resin foam moldings obtained in Example 19 and Comparative Example 5. In addition, the graphite content shown to Tables 1-3 is a graphite content in a styrene resin foaming molding.

The relationship between the expansion ratio B (cm ³ / g) and the thermal conductivity A (W / m · K) in Examples 1 to 18 and Comparative Examples 1 to 3 is shown in FIG. The relationship between the expansion ratio D (cm ³ / g) and the thermal conductivity C (W / m · K) in Examples 1 to 18 and Comparative Examples 1 to 3 is shown in FIG. In FIG. 1, X: plot of the expansion ratio B and thermal conductivity A of Examples 1 to 18, and ▲: plot of the expansion ratio B and thermal conductivity A of Comparative Examples 1-3. The straight line represents Formula 1, the dotted line represents Formula 3, and the alternate long and short dash line represents Formula 4. In FIG. 2, x: plot of the expansion ratio D and thermal conductivity C of Examples 1 to 18, and ▲: plot of the expansion ratio D and thermal conductivity C of Comparative Examples 1 to 3, the straight line is the formula 2, dotted line Represents Formula 5, and the alternate long and short dash line represents Formula 6.

  As shown in FIG. 1, the styrene resin foam molded article of the present invention is a styrene resin foam molded article having a high expansion ratio and high heat insulation. As shown in FIG. 2, the styrene resin foam molded article of the present invention is a styrene resin foam molded article having a high expansion ratio and a long thermal insulation.

  As shown in Tables 1 to 3 and FIGS. 1 and 2, by using the styrene resin foam molded article of the present invention, high foaming ratio and A styrenic resin foam molded article having high heat insulation can be provided. That is, according to the present invention, as shown in FIG. 1, by setting A (X value) ≦ 0.0251 + 0.0000776 × B (Formula 1), the foaming molding of styrene resin having a high expansion ratio and high heat insulation property. A styrene-based resin foam molded article having a higher expansion ratio and higher heat insulation can be provided by setting A ≦ 0.0248 + 0.0000776 × B (formula 3), and A ≦ 0 By using 0.0245 + 0.0000776 × B (formula 4), it is possible to provide a styrene-based resin foam molded article having a particularly high expansion ratio and high heat insulation.

  In addition, as shown in FIG. 2, by setting C (Y value) ≦ 0.0276 + 0.0000776 × D (Formula 2), a styrene-based resin foam molded article having a high expansion ratio and a long thermal insulation property is provided. By setting C 1 ≦ 0.0270 + 0.0000776 × D (Formula 5), it is possible to provide a styrene-based resin foam molded body having a higher expansion ratio and higher heat insulation over a long period of time, and C 1 ≦ 0. By setting it as 0267 + 0.0000776 × D (formula 6), it is possible to provide a styrene-based resin foam molded article having a particularly high expansion ratio and a high thermal insulation property over a long period of time.

(Example 20)
[Production of styrene resin particles]
Master batch (I) 5.95 parts of a mixture of a brominated flame retardant and a heat stabilizer, 8.75 parts of graphite master batch (H1), talc (G ) 0.2 part was put into a blender and blended for 10 minutes to obtain a resin composition.

  The obtained resin composition was supplied to a single screw extruder having a diameter of 90 mm, melted and kneaded in the extruder, and discharged through a die having 140 small holes with a diameter of 1.4 mm attached to the tip of the extruder. The strand-shaped resin extruded at 335 kg / hour was cooled and solidified in a 20 ° C. water tank, and then styrene resin particles were obtained with a strand cutter. At this time, the temperature of the resin at the tip of the extruder was 245 ° C., and the residence time in the extruder was 3 minutes.

[Production of expandable styrene resin particles]
In a 6 L autoclave with a stirrer, 200 parts of deionized water, 1 part of tricalcium phosphate, 0.03 part of sodium dodecylbenzenesulfonate, 4 parts of sodium chloride with respect to 100 parts of the resulting styrene resin particles The autoclave was sealed. Thereafter, after heating to 105 ° C. in 1 hour, 8 parts of mixed pentane [a mixture of 80% normal pentane (B1) and 20% isopentane (B2)] as a blowing agent was added to the autoclave over 25 minutes, The temperature was raised to 115 ° C. over 10 minutes and held there for 4 hours.

  Next, it is cooled to room temperature, and the resin particles impregnated with the blowing agent are taken out from the autoclave, pickled with hydrochloric acid, washed with water, dehydrated with a centrifuge, and the moisture adhering to the surface of the resin particles with an air dryer. Drying was performed to obtain expandable styrene resin particles.

  After dry blending 0.08 part of zinc stearate with respect to 100 parts of the obtained expandable styrene resin particles, it was stored at 15 ° C.

[Preparation of pre-expanded particles]
2 days after producing expandable styrene resin particles and storing at 15 ° C., the expandable styrene resin particles were put into a pre-foaming machine [BHP-300, manufactured by Daikai Kogyo Co., Ltd.] Water vapor was introduced into a pre-foaming machine and foamed to obtain pre-foamed particles having a bulk magnification of 40 times. Similarly, pre-expanded particles of 50 times, 60 times, 70 times and 80 times in bulk magnification were obtained.

[Production of Styrenic Resin Foamed Molding]
Inside the in-mold molding die (length 450 mm × width 310 mm × thickness 25 mm) in which the obtained pre-expanded particles having a bulk magnification of 40 times were attached to a foamed polystyrene molding machine [manufactured by Daisen Industry Co., Ltd., KR-57] Then, 0.06 MPa of water vapor was introduced and foamed in the mold, and then the mold was sprayed with water for 3 seconds to cool. The styrenic resin foam molded product is held in the mold until the pressure at which the styrenic resin foam molded product presses the mold is 0.015 MPa (gauge pressure), and then the styrenic resin foam molded product is taken out and a rectangular solid with a beautiful appearance. A styrene-based foam molded article was obtained. The expansion ratio was 40 times.

  Similarly, styrene-based resin foam molded articles were prepared from pre-expanded particles having a bulk magnification of 50 times, 60 times, 70 times, and 80 times. The expansion ratios were 50 times, 60 times, 70 times, and 80 times, respectively. Table 3 shows the evaluation results of the obtained foamed molded articles.

(Example 21)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 20 except that 83.85 parts of styrene resin (A) and 10 parts of graphite masterbatch (H1) were used. It was.

(Example 22)
In [Production of Styrenic Resin Particles], the styrenic resin foam molded article was prepared in the same manner as in Example 20, except that the styrene resin (A) was changed to 81.35 parts and the graphite masterbatch (H1) was 12.5 parts. Got.

(Example 23)
In [Production of Styrenic Resin Particles], a styrene resin foam molded article was prepared by the same operation as in Example 20 except that 76.35 parts of styrene resin (A) and 17.5 parts of graphite masterbatch (H1) were used. Got.

(Example 24)
In [Production of styrene resin particles], the mixture was changed to 89.8 parts of styrene resin (A) and 10 parts of graphite masterbatch (H1), and a masterbatch (I) of a mixture of brominated flame retardant and heat stabilizer A styrene resin foam molded article was obtained by the same operation as in Example 20 except that was not used.

(Example 25)
A styrene resin foam molded article was obtained by the same operation as in Example 20 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 26)
A styrene resin foam molded article was obtained by the same operation as in Example 21 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 27)
A styrene resin foam molded article was obtained by the same operation as in Example 22 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 28)
A styrene resin foam molded article was obtained by the same operation as in Example 23 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 29)
A styrene resin foam molded article was obtained by the same operation as in Example 24 except that the mixed pentane was changed to 10 parts in [Production of expandable styrene resin particles].

(Example 30)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 21 except that the graphite master batch (H1) was changed to the graphite master batch (H2).

(Example 31)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 23, except that the graphite master batch (H1) was changed to the graphite master batch (H2).

(Example 32)
[Production of expandable styrene resin particles]
Blender of bromine flame retardant and heat stabilizer mixture (F) 2.5 parts, graphite (C1) 4 parts, talc (G) 0.2 parts with respect to 93.3 parts of styrene resin (A) And blended for 10 minutes to obtain a resin composition.

  The obtained resin composition is supplied to a tandem type two-stage extruder in which a single screw extruder (first extruder) having a diameter of 65 mm and a single screw extruder (second extruder) having a diameter of 90 mm are connected in series. Melt kneading was performed at a set temperature of 220 ° C. in a 65 mm extruder. From the middle of the 65 mm caliber extruder (first extruder), press-fit at a rate of 8 parts of mixed pentane [mixture of 80% normal pentane (B1) and 20% isopentane (B2)] to 100 parts of the resin composition. did. Then, it supplied to the 90-mm-diameter extruder (2nd extruder) through the continuation pipe | tube set to 230 degreeC.

  After cooling the molten resin to 167 ° C. with a 90 mm diameter extruder (second extruder), the diameter is 0.7 mm and the land length is 3.0 mm attached to the tip of the second extruder set at 275 ° C. A die lip having 40 small holes was extruded into pressurized circulating water at a temperature of 60 ° C. and 0.9 MPa at a discharge rate of 50 kg / hour. The extruded molten resin is cut and pulverized at 2500 rpm using a rotary cutter having 10 blades in contact with the die lip, and transferred to a centrifugal dehydrator to obtain expandable styrene resin particles. It was. At this time, the residence time in the first extruder was 4 minutes.

  After dry blending 0.08 part of zinc stearate with respect to 100 parts of the obtained expandable styrene resin particles, it was stored at 15 ° C.

[Preparation of pre-expanded particles]
Pre-expanded particles were obtained in the same manner as in Example 20.
[Production of Styrenic Resin Foamed Molding]
A styrene resin foam molded article was obtained in the same manner as in Example 20.

(Example 33)
In [Production of expandable styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 32 except that 90.3 parts of styrene resin (A) and 7 parts of graphite (C1) were changed. It was.

(Example 34)
[Production of styrene resin particles]
To 86.85 parts of styrene resin (A), 4.75 parts of brominated flame retardant (D), 8 parts of graphite (C1), and 0.4 part of talc (G) are put into a blender for 10 minutes. The resin composition was obtained by blending.

  The obtained resin composition was supplied to a single screw extruder having a diameter of 90 mm, melted and kneaded in the extruder, and discharged through a die having 140 small holes with a diameter of 1.4 mm attached to the tip of the extruder. The strand-shaped resin extruded at 335 kg / hour was cooled and solidified in a 20 ° C. water tank, and then styrene resin particles were obtained with a strand cutter. At this time, the temperature of the resin at the tip of the extruder was 245 ° C., and the residence time in the extruder was 3 minutes.

[Production of expandable styrene resin particles]
In a 6 L autoclave with a stirrer, 200 parts of deionized water, 1 part of tricalcium phosphate, 0.03 part of sodium dodecylbenzenesulfonate, 4 parts of sodium chloride with respect to 50 parts of the obtained styrene resin particles The autoclave was sealed. Thereafter, the temperature of the autoclave was raised to 90 ° C., and 0.125 part of benzoyl peroxide and 50 parts of styrene monomer in which 1,1-di (t-butylperoxy) cyclohexane was dissolved in the autoclave over 2 hours while stirring. The polymerization was promoted by dropwise addition. Next, the autoclave was heated to 105 ° C. over 30 minutes, and 8 parts of mixed pentane [a mixture of 80% normal pentane (B1) and 20% isopentane (B2)] as a blowing agent was added to the autoclave over 25 minutes. The temperature was raised to 115 ° C. over 10 minutes and held there for 4 hours.

  Next, it is cooled to room temperature, and the resin particles impregnated with the blowing agent are taken out from the autoclave, pickled with hydrochloric acid, washed with water, dehydrated with a centrifuge, and the moisture adhering to the surface of the resin particles with an air dryer. Drying was performed to obtain expandable styrene resin particles.

After dry blending 0.08 part of zinc stearate with respect to 100 parts of the obtained expandable styrene resin particles, it was stored at 15 ° C.
[Preparation of pre-expanded particles]
Pre-expanded particles were obtained in the same manner as in Example 20.
[Production of Styrenic Resin Foamed Molding]
A styrene resin foam molded article was obtained in the same manner as in Example 20.

(Example 35)
In [Production of styrene-based resin particles], a styrene-based resin foam molded article was obtained by the same operation as in Example 34 except that the styrene-based resin (A) was changed to 80.85 parts and the graphite (C1) was 14 parts.
Table 4 shows the evaluation results of the styrene resin foam molded articles obtained in Examples 20 to 35.

(Comparative Example 6)
In [Production of styrene resin particles], the styrene resin foam molding is carried out in the same manner as in Example 1 except that the styrene resin (A) is changed to 93.85 parts and the graphite master batch (H1) is not used. Got the body.

(Comparative Example 7)
In [Creation of Styrenic Resin Particles], the styrene resin (A) is changed to 99.8 parts, and the master batch (I) of the graphite masterbatch (H1) and the mixture of brominated flame retardant and heat stabilizer is changed. A styrene resin foam molded article was obtained by the same operation as in Example 1 except that it was not used.

(Comparative Example 8)
In [Production of styrene resin particles], styrene resin foaming was carried out in the same manner as in Example 20, except that the styrene resin (A) was changed to 87.6 parts and the graphite master batch (H1) was changed to 6.25 parts. A molded body was obtained.

(Comparative Example 9)
In [Production of Styrenic Resin Particles], the same operation as in Example 20 was carried out except that the styrene resin (A) was changed to 68.85 parts and the graphite masterbatch (H1) was changed to 25 parts. Since the gap between the foamed styrene resin particles on the surface of the body was not filled, the surface was not smooth, and the foamed molded product was greatly shrunk immediately after molding, so a sample that could be evaluated was not obtained.

(Comparative Example 10)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 21 except that the graphite master batch (H1) was changed to the graphite master batch (H3).

(Comparative Example 11)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 23, except that the graphite master batch (H1) was changed to the graphite master batch (H3).

(Comparative Example 12)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 21 except that the graphite master batch (H1) was changed to the graphite master batch (H4).

(Comparative Example 13)
In [Production of styrene resin particles], a styrene resin foam molded article was obtained by the same operation as in Example 23, except that the graphite master batch (H1) was changed to the graphite master batch (H4).
Table 5 shows the evaluation results of the styrene resin foam molded articles obtained in Comparative Examples 6 to 13.

(Example 36)
The following No. 1 to 7 styrene resin foam molded articles were produced.
<No. 1>
In [Production of Styrenic Resin Particles], the graphite content was changed in the same manner as in Example 1 except that 85.91 parts of styrene resin (A) and 7.94 parts of graphite masterbatch (H1) were used. 0% expandable resin particles were obtained, and a styrene resin foam molded article was obtained.

<No. 2>
In [Production of Styrenic Resin Particles], the graphite content was changed in the same manner as in Example 1 except that 79.76 parts of styrene resin (A) and 14.09 parts of graphite masterbatch (H1) were changed. 3% of expandable resin particles were obtained, and a styrene-based resin foam molded article was obtained.

<No. 3>
In [Preparation of Styrenic Resin Particles], the graphite content of 6.6 by the same operation as in Example 1 except that 77.19 parts of styrene resin (A) and 16.66 parts of graphite masterbatch (H1) were changed. 3% of expandable resin particles were obtained, and a styrene-based resin foam molded article was obtained.

<No. 4>
In [Production of Styrenic Resin Particles], the graphite content was changed by the same operation as in Example 1 except that 74.63 parts of styrene resin (A) and 19.22 parts of graphite masterbatch (H1) were used. 2% of expandable resin particles were obtained, and further, a styrenic resin foam molded article was obtained.

<No. 5>
In [Production of Styrenic Resin Particles], the graphite content was changed by the same operation as in Example 1 except that 73.35 parts of styrene resin (A) and 20.50 parts of graphite masterbatch (H1) were changed. 7% of expandable resin particles were obtained, and further, a styrenic resin foam molded article was obtained.

<No. 6>
In [Preparation of Styrenic Resin Particles], the expandable resin was obtained in the same manner as in Example 2 except that the graphite master batch (H1) was changed to a graphite master batch (H5) using scaly graphite BF-3AK. Particles were obtained, and a styrene resin foam molded article was obtained.

<No. 7>
In [Production of styrene resin particles], the expandable resin was obtained by the same operation as in Example 4 except that the graphite master batch (H1) was changed to a graphite master batch (H5) using scaly graphite BF-3AK. Particles were obtained, and a styrene resin foam molded article was obtained.

(Comparative Example 14)
The following No. 8-No. Fourteen styrene resin foamed molded articles were produced.
<No. 8>
In [Preparation of Styrenic Resin Particles], the graphite content was changed to 0.001 by the same operation as in Example 1 except that the styrene resin (A) was changed to 91.29 parts and the graphite masterbatch (H1) was 2.56 parts. 9% of expandable resin particles were obtained, and further, a styrenic resin foam molded article was obtained.

<No. 9>
[Production of styrene resin particles] In the same manner as in Example 1 except that the styrene resin (A) was changed to 88.73 parts and the graphite master batch (H1) was 5.13 parts, a graphite content of 1. 9% of expandable resin particles were obtained, and further, a styrenic resin foam molded article was obtained.

<No. 10>
In [Production of Styrenic Resin Particles], a graphite content of 8.07 parts by the same operation as in Example 1 except that 72.07 parts of styrene resin (A) and 21.78 parts of graphite masterbatch (H1) were used. 2% of expandable resin particles were obtained, and further, a styrenic resin foam molded article was obtained.

<No. 11>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained in the same manner as in Example 2 except that the graphite master batch (H1) was changed to a graphite master batch (H7) using scaly graphite UCP. Furthermore, a styrene resin foam molded article was obtained.

<No. 12>
In [Production of Styrenic Resin Particles], expandable resin particles were obtained in the same manner as in Example 4 except that the graphite master batch (H1) was changed to a graphite master batch (H7) using scaly graphite UCP. Furthermore, a styrene resin foam molded article was obtained.

<No. 13>
In [Preparation of Styrenic Resin Particles], the expandable resin was obtained in the same manner as in Example 2 except that the graphite master batch (H1) was changed to a graphite master batch (H6) using scaly graphite BF-10AK. Particles were obtained, and a styrene resin foam molded article was obtained.

<No. 14>
In [Production of Styrenic Resin Particles], a foamable resin was obtained by the same operation as in Example 4 except that the graphite master batch (H1) was changed to a graphite master batch (H6) using scaly graphite BF-10AK. Particles were obtained, and a styrene resin foam molded article was obtained.
Table 6 shows the evaluation results of the styrene resin foam molded articles obtained in Example 36 and Comparative Example 14.

As shown in Tables 4 to 6, according to the present invention, it is possible to provide a styrenic resin foam molded article that can achieve high heat insulation even at a high expansion ratio.
The present invention relates to expandable styrene resin particles, a method for producing the same, pre-expanded particles obtained by pre-expanding expandable styrene-based resin particles, a styrene resin foam-molded article obtained by molding pre-expanded particles, and a method for producing the same.

  In addition, when expandable styrene resin particles are pre-expanded into pre-expanded particles and further molded into a styrene-based resin foam molded article, the amount of the foaming agent contained in each step decreases. Therefore, even in the same experimental example, the graphite content of the expandable styrene resin particles is different from the graphite content of the styrene resin foam molding.

(Example 37)
[Production of styrene resin particles]
Master batch (I) 5.95 parts of a mixture of brominated flame retardant and heat stabilizer, graphite master batch (H1) 10 parts, talc (G) 0 with respect to 83.85 parts of styrene resin (A) 2 parts were put into a blender and blended for 10 minutes to obtain a resin composition.

  The obtained resin composition was supplied to a single screw extruder having a diameter of 90 mm, melted and kneaded in the extruder, and discharged through a die having 140 small holes with a diameter of 1.4 mm attached to the tip of the extruder. The strand-shaped resin extruded at 335 kg / hour was cooled and solidified in a 20 ° C. water tank, and then styrene resin particles were obtained with a strand cutter. At this time, the temperature of the resin at the tip of the extruder was 245 ° C., and the residence time in the extruder was 3 minutes.

[Production of expandable styrene resin particles]
In a 6 L autoclave with a stirrer, 200 parts of deionized water, 1 part of tricalcium phosphate, 0.03 part of sodium dodecylbenzenesulfonate, 4 parts of sodium chloride with respect to 100 parts of the resulting styrene resin particles The autoclave was sealed. Thereafter, after heating to 105 ° C. in 1 hour, 8 parts of mixed pentane [a mixture of 80% normal pentane (B1) and 20% isopentane (B2)] as a blowing agent was added to the autoclave over 25 minutes, The temperature was raised to 115 ° C. over 10 minutes and held there for 4 hours.

  Next, it is cooled to room temperature, and the resin particles impregnated with the blowing agent are taken out from the autoclave, pickled with hydrochloric acid, washed with water, dehydrated with a centrifuge, and the moisture adhering to the surface of the resin particles with an air dryer. Drying was performed to obtain expandable styrene resin particles. To 100 parts of the resulting expandable styrene resin particles, 0.08 part of zinc stearate was dry blended, and then stored at 15 ° C. for 2 weeks.

[Preparation of pre-expanded particles]
Expandable styrene resin particles were prepared and stored at 15 ° C., and two weeks after the expansion, the expandable styrene resin particles were pre-foamed with a pre-foaming machine [Daikai Kogyo Co., Ltd., BHP-300]. 1800 g of expandable styrene resin particles were put into a pre-foaming machine, and steam having a steam temperature of 120 ° C. was introduced into the can. The pressure inside the can was adjusted to 0.1 MPa by adjusting the exhaust valve. When the pre-expanded particles reached a predetermined bulk capacity, the introduction of water vapor was stopped. The steam input time was 50 seconds. Thereafter, compressed air was blown into the can for 60 seconds to dry the prefoamed particles, and then the prefoamed particles were taken out from the prefoaming machine. The expansion ratio was 60 times in bulk ratio.
By adjusting the weight of the expandable styrenic resin particles to be added, 70-fold and 80-fold pre-expanded particles were obtained by the same method. Water vapor temperature and can internal pressure were carried out under the conditions described in Table 7.

[Production of Styrenic Resin Foamed Molding]
Inside the in-mold molding die (length 450 mm × width 310 mm × thickness 25 mm) in which the obtained pre-expanded particles having a bulk magnification of 60 times are attached to a foamed polystyrene molding machine [manufactured by Daisen Industry Co., Ltd., KR-57] Then, 0.06 MPa of water vapor was introduced and foamed in the mold, and then the mold was sprayed with water for 3 seconds to cool. The styrenic resin foam molded product is held in the mold until the pressure at which the styrenic resin foam molded product presses the mold is 0.015 MPa (gauge pressure), and then the styrenic resin foam molded product is taken out and a rectangular solid with a beautiful appearance. A styrene-based foam molded article was obtained. The expansion ratio was 60 times.

Styrenic resin foam moldings were similarly produced from pre-expanded particles with a bulk magnification of 70 times and 80 times. The expansion ratio was 70 times and 80 times, respectively.
Table 7 shows the evaluation results of the obtained pre-expanded particles and the expanded molded body.

(Examples 38 to 53 and Comparative Examples 15 to 21)
The steam introduction time, the can internal pressure, and the steam temperature were changed as shown in Table 7 (Example) and Table 8, and Comparative Examples 17 to 19 were carried out in the same manner as Example 37 except that graphite was not used. did.

As shown in Table 7 and Table 8, if it is the manufacturing method of this invention, there will be little blocking amount, and the foaming molding which can be foamed to the foaming magnification 65cm < ³ > / g or more and was excellent in the surface beauty can be manufactured.

(Comparative Example 22)
<First stage of two-stage foaming>
In the same manner as in Example 37, expandable styrene resin particles were prepared and stored at 15 ° C. for 2 weeks, and then 1800 g of the expandable styrene resin particles were placed in a pre-foaming machine (BHP-300, manufactured by Daikai Industrial Co., Ltd.). Then, steam having a steam temperature of 114 ° C. was introduced into the can. The pressure inside the can was adjusted to 0.07 MPa by adjusting the exhaust valve. Steam injection was stopped at a steam injection time of 100 seconds, and after that, compressed air was blown into the can for 60 seconds to dry the pre-expanded particles, and then the pre-expanded particles were taken out from the pre-expander. The taken pre-expanded particles were stored at 20 ° C.

<Second stage of two-stage foaming>
Twenty-four hours after the first stage of foaming, pre-expanded particles having a bulk volume of 12 L were charged into the pre-foaming machine, and steam at a steam temperature of 120 ° C. was introduced into the pre-foaming machine with the exhaust valve released to perform two-stage foaming. The pre-expanded particles having a bulk magnification of 60 times were obtained by adjusting the time when the two-stage foamed steam was added. One-stage foaming was carried out at the can internal pressure, steam introduction temperature, and steam introduction time shown in Table 8, and two-stage foaming was carried out in the same manner as above to obtain 70-fold and 80-fold pre-expanded particles, respectively.

  Using the obtained pre-expanded particles, styrene-based resin foam molded articles having expansion ratios of 60 times, 70 times, and 80 times were produced in the same manner as in Example 37.

(Comparative Example 23)
Prefoaming and molding were carried out in the same manner as in Comparative Example 22 except that the water vapor charging time for the first stage foaming was changed to the conditions shown in Table 9.
Table 9 shows the evaluation results of Comparative Examples 22 and 23. For comparison, the evaluation results of Example 44 are shown again. As shown in Table 9, when the graphite content is high, the closed cell ratio is lowered when the two-stage foaming is used, and the surface beauty of the foamed molded product is lowered.

(Comparative Examples 24 and 25)
Using pre-expanded particles of 60 times, 70 times, 80 times produced by the same method as in Example 37,
Styrenic resin foam moldings were produced at the water vapor temperature and can pressure shown in Table 10. Table 10 shows the evaluation results. For comparison, the evaluation results of Example 44 are shown again. In addition, about the thing which does not reach a predetermined foaming ratio even if supply of water vapor | steam is continued, the average cell diameter, the closed cell rate, the surface beauty, and the amount of blocking were not able to be evaluated.

As shown in Table 10, it is difficult to foam 70 times or more when the internal pressure of the can is less than 0.001 MPa. On the other hand, if it exceeds 0.15 MPa, a large amount of blocking is generated and the yield is deteriorated, and the closed cell ratio is lowered to deteriorate the surface beauty of the foamed molded product. In particular, as in Comparative Example 24, when the internal pressure of the can was set to 0 MPa, the expansion ratios of 70 times and 80 times were not reached even when water vapor was continuously supplied.

Claims (24)

90. Expandable styrene resin particles obtained by adding a foaming agent to styrene resin particles, wherein the expandable styrene resin particles contain 3 to 8% by weight of graphite, and the graphite has an average particle diameter of 3 to 7 μm, Expandable styrenic resin particles having a value obtained by dividing% particle size by 10% particle size of 2.5 or more and a specific surface area of 1.55 m ² / cm ³ or more. 2. The expandable styrene resin particles according to claim 1, which contain a brominated flame retardant and have a bromine content of 0.8 to 2.5 wt% when a styrene resin foam molded article is formed. The foaming styrene type according to claim 1 or 2 , wherein the foaming agent comprises a hydrocarbon having 4 to 5 carbon atoms, and the content of the foaming agent is 4 to 10 parts by weight with respect to 100 parts by weight of the styrene resin. Resin particles. Pre-expanded particles obtained by pre-expanding the expandable styrenic resin particles according to any one of claims 1 to 3 . A styrene resin foam molded article obtained by molding the pre-expanded particles according to claim 4 . The manufacturing method of the expandable styrene-type resin particle as described in any one of Claims 1-3 . It is a manufacturing method of the expandable styrene resin particle according to claim 6 ,
Styrenic resin and graphite are melt kneaded with an extruder to obtain styrene resin pellets using a cold cut method or a hot cut method, and then the styrene resin pellets are suspended in water and contain a foaming agent. A process for producing expandable styrene-based resin particles. It is a manufacturing method of the expandable styrene resin particle according to claim 6 ,
Styrenic resin, graphite and foaming agent are melt-kneaded with an extruder, extruded into a cutter chamber filled with pressurized circulating water through a die with a small hole attached to the tip of the extruder, and immediately after extrusion by a rotary cutter. A method for producing expandable styrene resin particles, characterized by being cut and solidified by cooling with pressurized circulating water. It is a manufacturing method of the expandable styrene resin particle according to claim 6 ,
A method for producing expandable styrene resin particles, comprising polymerizing styrene in an aqueous suspension in the presence of graphite, and impregnating a foaming agent before and / or during and / or after the polymerization. The styrenic resin foam molded article according to claim 5 ,
The styrenic resin foam molded article has a thermal conductivity A (W / m · K) and a foaming ratio B (cm ³ / g) of the styrene resin foam molded article measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. A styrenic resin foam molded article having the relationship of Formula 1 between:
Formula 1: A ≦ 0.0251 + 0.0000776 × B The styrenic resin foam molded article according to claim 5 ,
The styrenic resin foamed molded product is obtained by drying the styrenic resin foamed molded product at 50 ° C. for 30 days and then measuring the thermal conductivity C (W / m · K) and the foaming measured at an average temperature of 23 ° C. and a temperature difference of 20 ° C. A styrene-based resin foam molded article having a relationship of Formula 2 between magnifications D (cm ³ / g).
Formula 2: C ≦ 0.0276 + 0.0000776 × D The styrene resin foam molded article according to claim 10 or 11 , wherein the expansion ratio is 40 (cm ³ / g) or more.   Styrenic resin foaming comprising: a pre-foaming step for obtaining pre-foamed particles by introducing water vapor into expandable styrenic resin particles placed in a can of a pre-foaming machine; and a molding step for molding the pre-foamed particles in-mold A method for producing a molded body, comprising:
  The graphite content in the styrene resin foam molded article is 3 to 8% by weight, and the graphite has an average particle size of 3 to 7 μm and a specific surface area of 1.55 m. ² / Cm ³ And the value obtained by dividing the 90% particle size by the 10% particle size is 2.5 or more, and
  A styrenic resin foam molded article is obtained by setting the water vapor charging time in the preliminary foaming step to 50 to 500 seconds,
  A method for producing a styrene resin foam molded article. A method for producing a styrenic resin foam molded article according to claim 13 ,
Average temperature 23 ° C., a styrene resin foamed molded product having a relationship of equation 1 between the thermal conductivity A measured temperature difference 20 ℃ (W / m · K ) and the expansion ratio B (cm 3 / ^g) A method for producing a styrene-based resin foam molded article.
Formula 1: A ≦ 0.0251 + 0.0000776 × B A method for producing a styrenic resin foam molded article according to claim 13 ,
5 0 ° C. The average temperature of 23 ° C. After drying for 30 days, the thermal conductivity was measured at a temperature difference 20 ° C. and C (W / m · K) the relationship of Equation 2 between the expansion ratio D ^(cm 3 / g) A method for producing a styrene resin foam molded article, comprising: obtaining a styrene resin foam molded article having the same.
Formula 2: C ≦ 0.0276 + 0.0000776 × D The method for producing a styrene resin foam molded article according to any one of claims 13 to 15, wherein in the preliminary foaming step, the foamable styrene resin particles are prefoamed in one stage. Method for producing a styrene resin foamed molded product according to any one of claims 13 to 16, the expansion ratio of the styrene resin foam molded body and 65~80cm 3 / ^g. The method for producing a styrene-based resin foam molded article according to any one of claims 13 to 17 , wherein the steam introduction time is 80 to 300 seconds. The method for producing a styrene-based resin foam molded body according to any one of claims 13 to 18 , wherein the pressure in the can of the preliminary foaming machine at the time of introducing steam is 0.001 to 0.15 MPa in gauge pressure. The method for producing a styrenic resin foam molded article according to any one of claims 13 to 19, wherein the temperature of the water vapor exceeds 100C and is 130C or less. 21. The styrene resin foam molded article according to any one of claims 13 to 20 , wherein, in the preliminary foaming step, air is introduced together with the water vapor into the expandable styrene resin particles placed in a can of the preliminary foaming machine. Manufacturing method. The method for producing a styrene resin foam molded article according to any one of claims 13 to 21 , wherein an average cell diameter of the styrene resin foam molded article is set to 70 to 250 µm. The method for producing a styrene resin foam molded article according to any one of claims 13 to 22 , wherein the closed cell ratio of the styrene resin foam molded article is 97 to 100%. The method for producing a styrene-based resin foam molded article according to any one of claims 13 to 23 , wherein the closed cell ratio of the pre-expanded particles is 97 to 100%.

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