JP6854672B2 - A masterbatch, a method for producing the same, and a method for producing foamable thermoplastic resin particles. - Google Patents

Description

The present invention relates to a masterbatch, a method for producing the same, and a method for producing foamable thermoplastic resin particles. More specifically, the present invention relates to a masterbatch containing graphite and a thermoplastic resin, a method for producing the masterbatch, and a method for producing foamable thermoplastic resin particles.

The styrene resin foam molded product obtained by using the foamable styrene resin particles is a foam having an excellent balance of light weight, heat insulating property, cushioning property, etc., and has been conventionally used for food containers, cold storage boxes, and cushioning. It is widely used as a material and as a heat insulating material for houses and the like.

In recent years, in relation to various problems such as global warming, energy saving by improving the heat insulating property of buildings such as houses has been aimed at, and demand for styrene resin foam molded products is expected to increase. At the same time, various studies have been made on further improvement of the heat insulating property of the styrene resin foam molded product.

On the other hand, the styrene resin foam molded product is in a competitive market with other materials such as glass wool as a heat insulating material. Therefore, in the production of styrene-based resin foam molded products, thorough cost reduction is required. In a styrene resin foam molded product having a foaming ratio of 40 times or more, the larger the foaming ratio, the higher the thermal conductivity and the worse the heat insulating property. Therefore, it is desired to lower the thermal conductivity of the styrene resin foamed molded product. It is rare. A styrene-based resin foam molded product having a lower thermal conductivity can obtain the same heat insulating properties as a conventional styrene-based resin foam molded product having a lower foaming ratio even when the foaming ratio is increased. The amount of certain foamable styrene resin particles used can be reduced. Therefore, a heat insulating material including a styrene-based resin foam molded product can be manufactured at low cost.

Further, a foaming agent such as butane or pentane contained in the styrene resin foam molded product has an effect of reducing the thermal conductivity, but such a foaming agent deviates from the styrene resin foam molded product with the passage of time. It is known that the thermal conductivity of the styrene-based resin foam molded product increases with the passage of time because it is dispersed and replaced with the atmosphere (air), and therefore the heat insulating property deteriorates with the passage of time. Therefore, it is required to maintain the thermal conductivity of the styrene resin foam molded product at a low level even after the foaming agent such as butane or pentane contained in the styrene resin foam molded product is replaced with air.

As a method of maintaining a low thermal conductivity, a method of using a radiant heat transfer inhibitor such as graphite for a styrene resin foam molded product is known. The radiant heat transfer inhibitor is a substance that can suppress radiant heat transfer among the heat transfer mechanisms transmitted in the foamed molded body, and is an additive-free system having the same resin, foaming agent, cell structure, and density. It has the effect of lowering the thermal conductivity as compared with the foam molded product.

For example, Patent Document 1 proposes effervescent styrene resin particles that can produce a foam having a density of 35 g / L or less by treatment and contain graphite powder that is evenly distributed. ..

Patent Document 2 describes 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 contained in an amount of 0.05 to 9% by weight. , Aspect ratio of 5 or more, volume average particle size (50% particle size) of 0.1 to 100 μm, specific surface area of 0.7 m ² / cm ³ or more, 90% particle size divided by 10% particle size 1 A styrene-based resin foam molded product of ~ 20 is described.

In Patent Document 3, a resin composition containing a polystyrene resin, a flame retardant, graphite, and a volatile foaming agent is melt-kneaded in an extruder, and the obtained melt-kneaded product is extruded from a die into pressurized water. A method for producing foamable styrene resin particles by cutting the extruded melt-kneaded product has been proposed.

Patent Document 4 proposes effervescent styrene resin particles containing 0.1 to 25% by mass of graphite having an average particle size of more than 50 μm.

Patent Document 5 states that the thermal conductivity is less than 0.032 W / mK and the density is 25 g, which is polymerized in a suspended aqueous solution in the presence of graphite and a nonionic surfactant and measured at 10 ° C. according to DIN 52612. A method for producing foamable styrene resin particles having a value of less than / L has been proposed.

In Patent Document 6, a masterbatch of graphite is used, and the thermal conductivity measured by the heat flow metering method according to JIS A 1412-: 1999 at an average temperature of 23 ° C. and a temperature difference of 20 ° C. is less than 0.032 W / mK. , And a method for producing foamable styrene resin particles having a density of less than 15 g / L has been proposed.

Special table 2001-525001 JP-A-2005-2268 Japanese Unexamined Patent Publication No. 2013-75941 Special table 2002-530450 Special Table 2008-502750 WO2015 / 137363 A1

Although the inventions of Patent Documents 1 to 5 achieve both foamability and heat insulating properties by adding graphite to the foamable resin particles, there is a demand for further improvement in foamability and heat insulating properties.

In general, the larger the specific surface area of graphite, the greater the probability of absorbing or reflecting heat radiation, and therefore the greater the effect of suppressing radiant heat transfer. Therefore, although it is usually preferable to use graphite having a small average particle size, graphite having a small average particle size is not only difficult to handle, but also has a problem that the manufacturing cost is high. Therefore, in the invention of Patent Document 6, excellent foaming property and heat insulating property are realized by using graphite having a specific surface area of a specific value or more even if the average particle size is large. However, from the viewpoint of mass productivity, further reduction of manufacturing cost is required, and there is room for improvement.

Therefore, an object of the present invention is to provide a method for producing foamable styrene-based resin particles capable of providing a styrene-based resin foam-molded article having a high foaming ratio and low thermal conductivity and also having a cost advantage. To do.

As a result of diligent studies to solve the above-mentioned problems, the inventors of the present application remarkably improve the dispersibility of graphite in the masterbatch when graphite having a specific particle size is masterbatched at a high concentration. This has led to the completion of the present invention.

That is, in the first invention of the present invention, in the method for producing a masterbatch containing graphite and a thermoplastic resin, the average particle size D50 of the graphite is 2 to 9 μm, and the content of the graphite is the following formula ( Satisfy 1)
Equation (1): M _min ≤ M ≤ 80 [% by weight]
(Here, in the above formula (1), when 2 ≦ D50 <5, M _min = 41, and when 5 ≦ D50 ≦ 9, M _min = 419 × C ^1.34 . M is in 100% by weight of the masterbatch. The graphite content [% by weight], C indicates the bulk density of graphite [g / cm ³ ]), and the mixture containing the graphite and the thermoplastic resin is kneaded by a kneader equipped with a biaxial stirrer. , A method for producing a masterbatch (hereinafter, may be referred to as "a method for producing a masterbatch of the present invention").

In the method for producing a masterbatch of the present invention, the laser scattering intensity per concentration of the graphite unit solution in the masterbatch is preferably 5.5 {% / (mg / ml)} /% by weight or more.

In the method for producing a masterbatch of the present invention, the laser scattering intensity per concentration of the graphite unit solution in the masterbatch is preferably 6.0 {% / (mg / ml)} /% by weight or more.

In the method for producing a masterbatch of the present invention, it is preferable that the graphite content satisfies the following formula (2).
Equation (2): M _min2 ≤ M ≤ 80 [% by weight]
(Here, in the above equation (2), when 2 ≦ D50 <7.5, M _min2 = 51, and when 7.5 ≦ D50 ≦ 9, M _min2 = 419 × C ^1.34 . M is a master batch. Graphite content at 100% by weight [% by weight], C indicates the bulk density of graphite [g / cm ³ ])
In the method for producing a masterbatch of the present invention, the graphite content is preferably 61% by weight or more and 80% by weight or less.

In the method for producing a masterbatch of the present invention, the above kneading is carried out under a load: 3.5 kgf / cm ² or more, a resin temperature: Tg + 50 ° C. or more (where Tg is a glass transition temperature of a thermoplastic resin), and a kneading time. : It is preferable to carry out in 10 minutes or more.

In the method for producing a masterbatch of the present invention, it is preferable that the thermoplastic resin is a styrene resin.

The second invention in the present invention is a masterbatch containing graphite and a thermoplastic resin having an average particle size D50 of 2 to 9 μm.
The masterbatch satisfies the following equation (1),
Equation (1): M _min ≤ M ≤ 80 [% by weight]
(Here, in the above formula (1), when 2 ≦ D50 <5, M _min = 41, and when 5 ≦ D50 ≦ 9, M _min = 419 × C ^1.34 . M is 100% by weight of the master batch. In, the graphite content [% by weight] and C indicate the bulk density of graphite [g / cm ³ ]), and
A masterbatch in which the laser scattering intensity per concentration of a graphite unit solution in the masterbatch is 5.5 {% / (mg / ml)} / wt% or more (hereinafter, referred to as "masterbatch of the present invention"). There is.)

In the master batch of the present invention, the laser scattering intensity per graphite unit solution concentration is preferably 6.0 {% / (mg / ml)} / wt% or more.

In the masterbatch of the present invention, it is preferable that the graphite content satisfies the following formula (2).
Equation (2): M _min2 ≤ M ≤ 80 [% by weight]
(Here, in the above equation (2), when 2 ≦ D50 <7.5, M _min2 = 51, and when 7.5 ≦ D50 ≦ 9, M _min2 = 419 × C ^1.34 . M is a master batch. Graphite content at 100% by weight [% by weight], C indicates the bulk density of graphite [g / cm ³ ])
In the master batch of the present invention, the graphite content is preferably 61% by weight or more and 80% by weight or less.

In the masterbatch of the present invention, it is preferable that the thermoplastic resin is a styrene resin.

A third invention of the present invention comprises a masterbatch obtained by the method for producing a masterbatch of the present invention, a masterbatch of the present invention, and a step of melt-kneading a thermoplastic resin with an extruder. The present invention relates to a method for producing resin particles (hereinafter, may be referred to as “a method for producing foamable thermoplastic resin particles of the present invention”).

In the method for producing foamable thermoplastic resin particles of the present invention, a melt containing a foaming agent is extruded into a cutter chamber filled with circulating water through a die having a large number of small holes attached after the extruder. Immediately after extrusion, it is preferable to further include a step of cutting with a rotary cutter in contact with the die.

In the method for producing foamable thermoplastic resin particles of the present invention, a step of extruding the melt through a die having a plurality of small holes attached after the extruder and cutting it with a cutter to obtain thermoplastic resin particles, and the above-mentioned It is preferable to further include a step of suspending the thermoplastic resin particles in water and impregnating the foaming agent.

In the method for producing foamable thermoplastic resin particles of the present invention, the graphite content is preferably 2 to 8% by weight based on 100% by weight of the foamable thermoplastic resin particles.

In the method for producing effervescent thermoplastic resin particles of the present invention, the laser scattering intensity per graphite unit solution concentration in the effervescent thermoplastic resin particles is 6.5 {% / (mg / ml)} / wt% or more. It is preferable to have.

In the method for producing foamable thermoplastic resin particles of the present invention, it is preferable that the thermoplastic resin is a styrene resin.

In the method for producing foamable thermoplastic resin particles of the present invention, the foaming agent contains at least two types selected from the group of hydrocarbons having 4 to 6 carbon atoms, and at least one of the two types has 4 carbon atoms. Alternatively, it is preferably a hydrocarbon of 5.

The method for producing the pre-foamed thermoplastic resin particles of the present invention includes a step of pre-foaming the foamable thermoplastic resin particles produced by the method for producing the foamable thermoplastic resin particles of the present invention to produce the pre-foamed resin particles. ..

The method for producing a foamed molded article of the present invention includes a step of molding the prefoamed thermoplastic resin particles produced by the method for producing prefoamed resin particles of the present invention.

According to the present invention, a masterbatch having excellent dispersibility can be obtained. Therefore, when the masterbatch of the present invention is used for foamable thermoplastic resin particles, it is possible to obtain foamable thermoplastic resin particles having excellent dispersibility of graphite.

According to the present invention, it is possible to provide foamable thermoplastic resin particles capable of providing a resin foam molded product having a high foaming ratio and a low thermal conductivity. Further, since the foamable thermoplastic resin particles obtained in the present invention are excellent in the dispersibility of graphite, low thermal conductivity can be realized even if the graphite content is reduced.

According to the present invention, graphite that can be obtained at low cost can be used, and high heat insulation can be realized while suppressing the graphite content, so that it is excellent in cost advantage in mass production.

Hereinafter, embodiments of the masterbatch of the present invention, a method for producing the same, and a method for producing the foamable styrene-based resin particles of the present invention will be described in detail.

[Master Badge]
The masterbatch of the present invention contains a thermoplastic resin and graphite having an average particle size of 2 to 9 μm.

(Thermoplastic resin)
The thermoplastic resin used in the master batch of the present invention is not particularly limited, but for example, polystyrene (PS), styrene-acrylonitrile copolymer (AS), styrene- (meth) acrylic acid copolymer. (Heat-resistant PS), styrene- (meth) acrylic acid ester copolymer, styrene-butadiene copolymer (HIPS), N-phenylmaleimide-styrene-maleic anhydride three-dimensional copolymer, and alloy with AS. Styrene-based resin such as (IP); Vinyl-based resin such as polymethylmethacrylate, polyacrylonitrile-based resin, polyvinyl chloride-based resin; polypropylene, polyethylene, ethylene-propylene copolymer, ethylene-propylene-butene ternary copolymer , Cycloolefin-based (co) polymers and other polyolefin-based resins and leologic-controlled polyolefin-based resins by introducing branched and crosslinked structures into these; nylon 6, nylon 66, nylon 11, nylon 12, MXD nylon, etc. Polyamide resin: Polyethylene terephthalate, polybutylene terephthalate, polyarylate, polyester resin such as polycarbonate, aliphatic polyester resin such as polylactic acid; polyphenylene ether resin (PPE), modified polyphenylene ether resin (modified PPE), poly Examples thereof include oxymethylene resins, polyphenylene sulfide resins, polyphenylene sulfide resins, aromatic polyether resins, engineering plastics such as polyether ether ketone resins, and the like. These may be used alone or in combination of two or more. Among these, a styrene-based resin is preferable from the viewpoint of obtaining foamable resin particles that are inexpensive and easy to foam-mold.

(Graphite)
The masterbatch of the present invention contains graphite having an average particle size of 2-9 μm.

By containing graphite in the foamable thermoplastic resin particles as a radiant heat transfer inhibitor, a thermoplastic resin foam molded product having high heat insulating properties can be obtained. The radiant heat transfer inhibitor referred to here refers to a substance having a property of reflecting, scattering or absorbing light in the near infrared or infrared region.

As the graphite used in the masterbatch of the present invention, known graphite can be used, and examples thereof include scaly graphite, earthy graphite, spheroidal graphite, and artificial graphite. In addition, in this specification, the term "scaly" also includes scaly, flaky or plate-like ones. 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 when used in a foamed molded product.

The graphite used in the masterbatch of the present invention has an average particle size of 2-9 μm. From the viewpoint of handleability during masterbatch production and radiant heat transfer suppressing effect when used in a foam molded product, it is preferably 2 to 6 μm, and more preferably 3 to 6 μm. In the present specification, the average particle size of graphite is measured and analyzed by the laser diffraction scattering method based on the Mie theory based on ISO13320: 2009 and JIS Z8825: 2013, and the cumulative volume with respect to the volume of all particles is 50%. The particle size D50 (volume average particle size by the laser diffraction scattering method) at the time of becoming the average particle size is defined as the average particle size.

The larger the average particle size of graphite, the lower the manufacturing cost. In particular, graphite having an average particle size of 2 μm or more is very inexpensive because the production cost including the cost of pulverization is low, and the cost of the master batch and the foamable styrene resin particles using the same can be reduced. Further, when the average particle size of graphite is 2 μm or more, the bulk density of graphite is relatively large, so that the handling property at the time of masterbatch production is excellent, and when used for foamable resin particles, the foaming property has good heat insulating property. It becomes possible to manufacture a molded product. When the average particle size is 9 μm or less, the cell film is less likely to be torn when used for the foamable styrene resin particles, and further when the pre-foamed particles and the foamed molded product are produced, so that high foaming is easy. There is a tendency that the ease of molding increases and the compressive strength of the foam molded product increases.

When the average particle size of graphite is 2 μm or more, lower thermal conductivity and therefore higher heat insulating properties can be obtained when applied to a foam molded product. Further, when the average particle size of graphite is 6 μm or less, the surface beauty of the molded product is excellent, and a lower thermal conductivity and therefore a higher heat insulating property can be obtained.

The graphite used in the masterbatch of the present invention is not particularly limited, but from the viewpoint of handleability during masterbatch production ^{, the bulk density is preferably 0.10 g / cm 3} or more, and the bulk density is high. More preferably 0.15 g / cm ³ or more.

In the masterbatch of the present invention, graphite is contained so as to satisfy the relational expression of the following formula (1).
Equation (1): M _min ≤ M ≤ 80 [% by weight]
Here, in the above equation (1), when 2 ≦ D50 <5, M _min = 41, and when 5 ≦ D50 ≦ 9, M _min = 419 × C ^1.34 . M indicates the graphite content [% by weight] in 100% by weight of the masterbatch (hereinafter, may be referred to as “graphite content M”), and C indicates the bulk density of graphite [g / cm ³ ].

In the masterbatch of the present invention, if the graphite content M is M _min % by weight or more, low thermal conductivity can be easily obtained. That is, it is presumed that when the graphite content is increased to some extent, collisions between graphites efficiently occur in the resin during kneading, and the dispersion and miniaturization of graphite are remarkably promoted. As a result, the radiant heat transfer suppressing effect of graphite can be efficiently exhibited, the amount of graphite added to the foamable resin particles can be reduced, and graphite having a large average particle size, which is cheaper, can be used. However, it is possible to obtain a foamable resin molded product having high heat insulating performance. In addition, since the amount of graphite added can be reduced, the risk of foam breakage due to graphite during foaming can also be suppressed, and a higher foaming ratio can be aimed at. In addition, the high graphite content can reduce running costs and labor costs during masterbatch production.

When the graphite content M at the time of producing the masterbatch is M _min % by weight or more, the handling property at the time of producing the masterbatch is inferior due to the large volume of graphite, so that it is not usually handled positively. Further, for the same reason, it is a general idea that the smaller the bulk density of graphite, the lower the graphite content, that is, the concentration at the time of masterbatch production. However, in the present invention, it has been found that by intentionally setting the graphite content M to M _min % by weight or more, the dispersibility of graphite is remarkably improved and the effect of suppressing radiant heat transfer of graphite is sufficiently exhibited. Further, if the graphite content M in producing the masterbatch exceeds 80% by weight, the graphite surface is not sufficiently wetted with the resin and the dispersion of graphite in the resin does not proceed, so that the effect of suppressing radiant heat transfer of graphite can be obtained. It cannot be fully expressed.

In the master batch of the present invention, the graphite content M is more preferably contained so as to satisfy the relational expression of the following formula (2) from the viewpoint of stably exhibiting a high radiant heat transfer suppressing effect. It is more preferable that it is contained so as to satisfy the relational expression of the formula (3).
Equation (2): M _min2 ≤ M ≤ 80 [% by weight]
Equation (3): 61 ≤ M ≤ 80 [% by weight]
(Here, in the above formula (2), when 2 ≦ D50 <7.5, M _min2 = 51, and when 7.5 ≦ D50 ≦ 9, M _min2 = 419 × C ^1.34 . C is graphite. The bulk density [g / cm ³ ] is shown.)
In addition to the above-mentioned thermoplastic resin and graphite, the masterbatch of the present invention may contain additives. For example, plasticizers, dispersants, mold release agents, lubricants and the like can be mentioned.

The masterbatch of the present invention contains the above graphite, the above thermoplastic resin, and other additives if necessary, and is kneaded by a kneading device equipped with a biaxial stirrer as a mixture satisfying the following relational expression (1). Can be made.
Equation (1): M _min ≤ M ≤ 80 [% by weight]
Here, in the above equation (1), when 2 ≦ D50 <5, M _min = 41, and when 5 ≦ D50 ≦ 9, M _min = 419 × C ^1.34 . M indicates the graphite content [% by weight] in 100% by weight of the masterbatch, and C indicates the bulk density [g / cm ³ ] of graphite.

In the present invention, a mixture containing a thermoplastic resin and graphite satisfying the above formula (1) is kneaded by a kneading device equipped with a biaxial stirrer to obtain a laser scattering intensity indicating the amount of light scattered. Increased, that is, the radiation suppression performance of graphite is increased, so that the thermal conductivity is reduced when used in a foamed molded product. Further, it is presumed that during kneading, the dispersion, miniaturization, and exfoliation of graphite occur in a complex manner, and the number of graphite particles is increasing.

As a kneading device equipped with a biaxial stirrer, a known kneading device can be used. For example, an intensive mixer, an internal mixer, a Banbury mixer and the like can be mentioned. Of these, an internal mixer or a Banbury mixer is preferable from the viewpoint of improving the mixing property by applying a load.

The kneading of the mixture containing the thermoplastic resin and graphite by a kneading device equipped with a biaxial stirrer is preferably kneaded while applying a load, specifically, for 10 minutes or more with a ^{load of 3.5 kgf / cm 2 or more.} It is preferable to knead the mixture at a resin temperature of Tg + 50 ° C. or higher, and it is more preferable to knead the mixture at a load of 4 kgf / cm ^{2 or higher for 15 minutes or longer and finish the kneading at a resin temperature of Tg + 50 ° C. or higher.} The resin temperature is preferably 300 ° C. or lower from the viewpoint of avoiding decomposition of the thermoplastic resin. In a kneading device such as a Banbury mixer, the mixing property can be increased by applying a load. Further, by kneading for 15 minutes or more, the viscosity of the thermoplastic resin in the Banbury mixer can be adjusted to a viscosity that makes it easy to mix with graphite, and graphite is sufficiently dispersed in the master batch, so that the foamed molded product It is easy to obtain low thermal conductivity when set to.

When the load is 4 kgf / cm ² or more, it is easy to obtain low thermal conductivity. That is, the graphite in the thermoplastic resin is sufficiently kneaded, and the laser scattering intensity can be increased.

It is also preferable that the stirring step for producing the masterbatch described above is ^{kneading at a load of 5 kgf / cm 2} or more for 20 minutes or more.

Kneading with a load of 5 kgf / cm ² or more is preferable because low thermal conductivity can be easily obtained. That is, the laser scattering intensity can be stably increased. Further, kneading for 20 minutes or more is preferable because low thermal conductivity can be easily obtained. That is, it is possible to stably increase the laser scattering intensity.

As a preferred embodiment of the present invention, when a masterbatch is prepared using a styrene resin as a thermoplastic resin, kneading by a kneading device equipped with a biaxial stirrer has a load of 3.5 kgf / cm ² or more. It is preferable to knead the mixture for 10 minutes or more and finish the kneading at a resin temperature of 160 ° C. or higher, and it is more preferable to knead the kneading at a load of 4 kgf / cm ² or higher for 15 minutes or longer and finish the kneading at a resin temperature of 170 ° C. or higher. It is more preferable to knead at cm ² or more for 20 minutes or more. In order to obtain a viscosity at which graphite can be easily dispersed in the styrene resin, it is preferable to mix the resin until the resin temperature reaches 170 ° C. or higher.

(Laser scattering intensity)
The master batch of the present invention preferably has a laser scattering intensity of 5.5 {% / (mg / ml)} /% by weight or more per graphite unit solution concentration. When this laser scattering intensity is 5.5 {% / (mg / ml)} / wt% or more, it is possible to obtain a high thermal conductivity reducing effect with respect to the graphite content when the foamed molded product is formed. Become. That is, when used for foamable resin particles, it is possible to obtain a high foaming ratio, a low thermal conductivity, and therefore a high heat insulating property. The laser scattering intensity per graphite unit solution concentration is more preferably 6.0 {% / (mg / ml)} / wt% or more, and more preferably 10 {% / (mg / ml)} / wt% or less. Is even more preferable. When the laser scattering intensity is 6.0% or more, a more sufficient effect of reducing the thermal conductivity can be obtained, that is, a lower thermal conductivity and therefore a higher heat insulating property can be obtained. Further, when the laser scattering intensity is 10 {% / (mg / ml)} / wt% or less, the average particle size of graphite does not become too small due to kneading, and the effect of improving the thermal conductivity can be easily obtained.

The laser scattering intensity per graphite unit solution concentration in the present invention is determined as follows. First, the intensity Lb of transmitted light when a He-Ne laser light having a wavelength of 632.8 nm is irradiated to a solvent that does not contain a measurement target (master batch, foamable thermoplastic resin particles described later), and the measurement target is a solvent. The laser scattering intensity Ob (%) is expressed by the formula: Ob = (1-Ls / Lb) × from the intensity Ls of the transmitted light when the solution dispersed by a predetermined weight is irradiated with He-Ne laser light having a wavelength of 632.8 nm. Calculate from 100. Next, the laser scattering intensity per unit solution concentration to be measured is obtained from the obtained laser scattering intensity Ob. Then, the laser scattering intensity calculated by dividing the obtained laser scattering intensity per unit solution concentration by the content (% by weight) of graphite in the measurement target having a predetermined weight is the laser scattering intensity per graphite unit solution concentration. .. The solvent may be toluene when the resin in the foamable resin particles is a styrene resin, and may be any solvent as long as the resin can be dissolved when the resin is another resin.

[Effervescent thermoplastic resin particles]
The foamable thermoplastic resin particles of the present invention are characterized by being produced by using the masterbatch of the present invention described above.

The foamable thermoplastic resin particles of the present invention can similarly contain the components contained in general foamable thermoplastic resin particles, except that the masterbatch of the present invention is used. Specifically, it contains a thermoplastic resin and a foaming agent as components other than the masterbatch, and if necessary, from a radiant heat transfer inhibitor, a flame retardant, a heat stabilizer, a radical generator, and other additives. Can contain at least one optional component selected from the group. Preferably, it contains a thermoplastic resin, a foaming agent and a flame retardant, and may contain at least one of the above-mentioned optional components excluding the flame retardant, and more preferably, the thermoplastic resin, a foaming agent, a flame retardant and heat. It may contain a stabilizer and may contain at least one of the above-mentioned optional components excluding the flame retardant and the heat stabilizer, and more preferably, a thermoplastic resin, a foaming agent, a flame retardant, a heat stabilizer and a nucleating agent. May contain at least one of the above-mentioned optional components excluding flame retardants, heat stabilizers and nucleating agents.

(Thermoplastic resin)
The thermoplastic resin used for the foamable thermoplastic resin particles of the present invention is the same as the thermoplastic resin used in the above-mentioned masterbatch, and is preferably a styrene resin because it is inexpensive and easy to foam mold. ..

The styrene resin is not only a styrene homopolymer (polystyrene homopolymer), but also styrene and another monomer copolymerizable with styrene or a derivative thereof as long as the effect according to one embodiment of the present invention is not impaired. And may be copolymerized. However, the brominated styrene-butadiene copolymer described later is excluded.

Other monomers copolymerizable with styrene or derivatives thereof include, for example, methylstyrene, dimethylstyrene, ethylstyrene, diethylstyrene, isopropylstyrene, bromostyrene, dibromostyrene, tribromostyrene, chlorostyrene, dichlorostyrene, etc. And styrene derivatives such as trichlorostyrene; polyfunctional vinyl compounds such as divinylbenzene; (meth) acrylic acid esters such as methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, and butyl methacrylate. Compounds; 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-butylmaleimide, Examples thereof include N-alkyl-substituted maleimide compounds such as N-cyclohexylmaleimide, N-phenylmaleimide, N- (2) -chlorophenylmaleimide, N- (4) -bromophenylmaleimide, and N- (1) -naphthylmaleimide. .. These may be used alone or in combination of two or more.

The styrene-based resin is not limited to the above-mentioned styrene homopolymer and / or a copolymer of styrene and another monomer copolymerizable with styrene or a derivative thereof, and relates to one embodiment of the present invention. As long as the effect is not impaired, it may be a homopolymer of the above-mentioned other monomer or derivative, or a blend with a copolymer thereof.

For example, a diene-based rubber-reinforced polystyrene, an acrylic-based rubber-reinforced polystyrene, and / or a polyphenylene ether-based resin can be blended with the styrene-based resin.

Among styrene-based resins, it is relatively inexpensive, can be foam-molded with low-pressure steam, etc. without using a special method, and has an excellent balance of heat insulating properties, flame retardancy, and cushioning properties. -Acrylonitrile copolymer or styrene-butyl acrylate copolymer is preferable.

(Graphite)
The effervescent thermoplastic resin particles of the present invention contain graphite by using the masterbatch of the present invention.

The foamable thermoplastic resin particles of the present invention are obtained by kneading a masterbatch with a thermoplastic resin (new thermoplastic resin), but the thermoplastic resin contained in the masterbatch and the new thermoplastic resin May be the same or different. From the viewpoint of the dispersibility of graphite and the foamability, it is preferable that the thermoplastic resin contained in the masterbatch and the new thermoplastic resin have excellent compatibility with each other.

The graphite content of the foamable thermoplastic resin particles of the present invention can be easily controlled to the target foaming ratio, and from the viewpoint of the balance of the effect of reducing thermal conductivity and the like, 2 weights per 100% by weight of the foamable thermoplastic resin particles. It is desirable that it is% or more and 8% by weight or less. When the graphite content is 2% by weight or more, the effect of reducing the thermal conductivity tends to be sufficient, while when the graphite content is 8% by weight or less, when the pre-foamed particles and the foamed molded product are produced from the foamable thermoplastic resin particles. In addition, since the cell film is less likely to be torn, high foaming is easy, and the foaming ratio tends to be easily controlled.

The graphite content of the foamable thermoplastic resin particles is more preferably 3% by weight or more and 7% by weight or less. When the graphite content is 3% by weight or more, the thermal conductivity is lowered, and therefore higher heat insulating properties can be obtained. Further, when the graphite content is 7% by weight or less, the foamability and the surface beauty of the molded product are improved.

(Foaming agent)
The foaming agent used in the foamable thermoplastic resin particles of the present invention is not particularly limited, but volatile foamability is preferable from the viewpoint of having a good balance between foamability and product life and easily increasing the magnification in actual use. , Hydrocarbons having 4 to 6 carbon atoms are more preferable. When the number of carbon atoms of the foaming agent is 4 or more, the volatility becomes low and the foaming agent is less likely to disperse from the foamable thermoplastic resin particles. Therefore, a sufficient amount of the foaming agent remains in the foaming process during actual use. It is preferable because it is possible to obtain a sufficient foaming force and it is easy to increase the magnification. Further, when the number of carbon atoms is 6 or less, the boiling point of the foaming agent is not too high, so that sufficient foaming power can be easily obtained by heating during pre-foaming, and high foaming tends to be easy. Examples of the hydrocarbon having 4 to 6 carbon atoms include hydrocarbons such as normal butane, isobutane, normal pentane, isopentane, neopentane, cyclopentane, normal hexane, and cyclohexane. These may be used individually by 1 type, and may be used in combination of 2 or more type. Of these, hydrocarbons having 4 carbon atoms and / or hydrocarbons having 5 carbon atoms are more preferably contained. In particular, since it is easy to increase the magnification, the foaming agent contains at least two types selected from the group of hydrocarbons having 4 to 6 carbon atoms, and at least one of the two types is a hydrocarbon having 4 or 5 carbon atoms. It is preferably hydrogen.

In the foamable thermoplastic resin particles of the present invention, the amount of the foaming agent added is 4 to 10 parts by weight with respect to 100 parts by weight of the mixture consisting of the thermoplastic resin containing no foaming agent, the masterbatch, and other additives. Is preferable. Within the above range, the balance between the foaming speed and the foaming force is better, and the effect that the magnification is more stable and higher is easily obtained. When the amount of the foaming agent added is 4 parts by weight or more, the foaming force required for foaming is sufficient, so that high foaming tends to be easy, and it tends to be easy to produce a foamed molded product having a high foaming ratio of 50 times or more. .. Further, when the amount of the foaming agent is 10 parts by weight or less, the flame retardant performance is improved and the manufacturing time (molding cycle) when manufacturing the foamed molded product is shortened, so that the manufacturing cost tends to be low. Become. The amount of the foaming agent added is more preferably 4.5 to 9 parts by weight, still more preferably 5 to 8 parts by weight, based on 100 parts by weight of the thermoplastic resin.

(Flame retardants)
The flame retardant used in the foamable thermoplastic resin particles of the present invention is not particularly limited, and any flame retardant conventionally used in foamed molded products can be used. Among them, bromine, which has a high flame retardant imparting effect, can be used. Flame retardants are desirable. Examples of the bromine-based flame retardant 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)) or 2,2-bis [4- (2,3-dibromopropoxy) -3,5-dibromophenyl] propane (also known as tetrabromobisphenol A-bis (2,2)) 3-Dibromopropyl ether)) brominated bisphenol compounds, tetrabromocyclooctane, tris (2,3-dibromopropyl) isocyanurate, brominated styrene / butadiene block copolymer, brominated random styrene / butadiene copolymer Examples thereof include a coalesced or a brominated butadiene / vinyl aromatic hydrocarbon copolymer such as a brominated styrene / butadiene graft copolymer (for example, disclosed in Japanese Patent Application Laid-Open No. 2009-516019). One of these brominated flame retardants may be used alone, or two or more thereof may be used in combination.

The bromine-based flame retardant has a bromine content of 0.8% by weight or more based on the total amount of the foamed molded product in terms of the balance of flame retardancy when graphite is added, while being easy to control the target foaming ratio. It is preferably 5.0% by weight or less. When the bromine content is 0.8% by weight or more, the flame retardancy imparting effect tends to be large, and when it is 5.0% by weight or less, the strength of the obtained foamed molded product tends to increase. The bromine content is more preferably 1.0 to 3.5% by weight and is added to the foamable thermoplastic resin particles.

(Heat stabilizer)
In the foamable thermoplastic resin particles of the present invention, further, by using a heat stabilizer in combination, deterioration of flame retardancy due to decomposition of the brominated flame retardant in the manufacturing process and deterioration of the foamable thermoplastic resin particles are suppressed. be able to.

The heat stabilizers are used in appropriate combinations according to the type and content of the thermoplastic resin used, the type and content of the foaming agent, the type and content of the radiant heat transfer inhibitor, the type and content of the brominated flame retardant, and the like. be able to.

As the heat stabilizer, a hindered amine compound, a phosphorus compound, or an epoxy compound is preferable from the viewpoint that the 1% weight loss temperature in the thermogravimetric analysis of the brominated flame retardant-containing mixture can be arbitrarily controlled. The heat stabilizer may be used alone or in combination of two or more. These heat stabilizers can also be used as light resistance stabilizers as described later.

(Radical generator)
The effervescent thermoplastic resin particles of the present invention can exhibit high flame retardant performance by further containing a radical generator and used in combination with a bromine-based flame retardant.

The radical generator can be appropriately combined and used according to the type and content of the thermoplastic resin to be used, the type and content of the foaming agent, the type and content of the radiant heat transfer inhibitor, and the type and content of the brominated flame retardant. ..

Examples of the radical generator include cumene hydroperoxide, dicumyl peroxide, t-butyl hydroperoxide, 2,3-dimethyl-2,3-diphenylbutane, poly-1,4-isopropylbenzene and the like. Be done. The radical generator may be used alone or in combination of two or more.

(Other additives)
The foamable thermoplastic resin particles of the present invention are, if necessary, a radiant heat transfer inhibitor, a processing aid, a light resistance stabilizer, a nucleating agent, a foaming aid, and an antistatic agent, 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 an inhibitor and a colorant such as a pigment.

Examples of the processing aid include sodium stearate, magnesium stearate, calcium stearate, zinc stearate, barium stearate, liquid paraffin and the like. Examples of the light resistance stabilizer include the above-mentioned hindered amines, phosphorus-based stabilizers, epoxy compounds, phenol-based antioxidants, nitrogen-based stabilizers, sulfur-based stabilizers, benzotriazoles and the like. Examples of the nucleating agent include silica, calcium silicate, wallastonite, kaolin, clay, mica, zinc oxide, calcium carbonate, sodium hydrogen carbonate, or an inorganic compound such as talc, a methyl methacrylate-based copolymer, or ethylene-. Polymer compounds such as vinyl acetate copolymer resin, olefin waxes such as polyethylene wax, or fatty acid bisamides such as methylene bisstearyl amide, ethylene bisstearyl amide, hexamethylene bispalmitic acid amide, and ethylene bisoleic acid amide. Can be mentioned. As the foaming aid, a solvent having a boiling point of 200 ° C. or lower under atmospheric pressure can be preferably used, and for example, an aromatic hydrocarbon such as styrene, toluene, ethylbenzene, or xylene, or an alicyclic such as cyclohexane or methylcyclohexane. Examples thereof include formula hydrocarbons, or acetates such as ethyl acetate and butyl acetate. As the radiant heat transfer inhibitor, antistatic agent and colorant, those used in various resin compositions can be used without particular limitation. These other additives may be used alone or in combination of two or more.

[Manufacturing method of foamable thermoplastic resin particles]
As a method for producing the foamable resin particles of the present invention, a graphite masterbatch (masterbatch of the present invention) or a thermoplastic resin and various components are melt-kneaded using an extruder and then cut into particles. There are two melt-kneading methods, the first melt-kneading method and the second melt-kneading method, which can be appropriately selected.

As the first melt-kneading method, a thermoplastic resin and a graphite masterbatch, and if necessary, additives such as a flame retardant, a radical generator, and a heat stabilizer are melt-kneaded with an extruder, and the foaming agent is melt-kneaded with the extruder. Alternatively, it is dissolved and dispersed in the melt by a mixing facility provided after the extruder, and then extruded into a cutter chamber filled with pressurized circulating water through a die having many small holes attached after the extruder, and immediately after extrusion. There is a method of cutting with a rotary cutter and cooling and solidifying with pressurized circulating water. At this time, the melt kneading by the extruder is performed when a single extruder is used, when a plurality of extruders are connected, and a second kneader such as a static mixer or a stirrer without a screw is used in combination with the extruder. In some cases, it can be selected as appropriate.

As a second melt-kneading method, a thermoplastic resin, a graphite masterbatch, and, if necessary, additives such as a flame retardant, a radical generator, and a heat stabilizer are melt-kneaded with an extruder to have a large number of small holes. A method in which thermoplastic resin particles are obtained by extruding through a die and then cutting with a cutter (cold cut method or hot cut method), and then the resin particles are suspended in water and the resin particles contain a foaming agent. There is.

The set temperature of the melt-kneading portion of the extruder in the first and second melt-kneading methods is preferably 100 ° C. to 250 ° C. Further, it is preferable that the residence time in the extruder from the supply of the resin and various components to the extruder to the end of melt-kneading is 10 minutes or less.

When the set temperature in the melt-kneading part of the extruder is 250 ° C. or less, and / or when the residence time in the extruder until the end of melt-kneading is 10 minutes or less, decomposition of the brominated flame retardant is unlikely to occur, which is desirable. It is possible to obtain the flame retardancy of the above, and it is possible to obtain the effect that it is not necessary to add an excessive amount of the flame retardant in order to impart the desired flame retardancy.

On the other hand, when the set temperature in the melt-kneading portion of the extruder is 100 ° C. or higher, the load on the extruder becomes small and the extrusion becomes stable.

Here, the melt-kneading portion of the extruder means from the feed portion to the tip of the final extruder on the downstream side when the extruder is composed of a single-screw or twin-screw screw. When a second kneader such as a static mixer or a stirrer without a screw is used in combination with the first extruder, it means from the feed portion of the first extruder to the tip of the second kneader. ..

In the extruder, a foaming agent, a radiant heat transfer inhibitor, and if necessary, other additives such as a brominated flame retardant, a heat stabilizer, and a nucleating agent are dissolved or uniformly dispersed in the resin, and if necessary. The molten resin (molten kneaded product) cooled to an appropriate temperature is extruded into pressurized cooling water from a die having a plurality of small holes.

As the extruder used in the first and second melt-kneading methods, a known extruder can be used, and it may be a single-screw extruder, a twin-screw extruder, or a single-screw extruder. It may have a tandem type configuration in which a machine and / or a twin-screw extruder are combined. In the step of melt-kneading a mixture containing a masterbatch and a thermoplastic resin with an extruder, when a masterbatch having a graphite content of 60% by weight or more is used, it is recommended to use a twin-screw extruder from the viewpoint of graphite dispersion. Is preferable. In a single-screw extruder, graphite dispersion may be poor, especially when a masterbatch with a graphite content of 70% by weight or more is used. However, kneading performance can be improved by installing a static mixer after the single-screw extruder. By improving, graphite may be sufficiently dispersed.

The dies used in the first and second melt-kneading methods are not particularly limited, and examples thereof include those having small holes having a diameter of 0.3 mm to 2.0 mm, more preferably 0.4 mm to 1.0 mm. Be done.

In the first melt-kneading method, the temperature of the molten resin immediately before being extruded from the die is Tg + 40 ° C. or higher, where Tg is the glass transition temperature of the thermoplastic resin in a state where the foaming agent is not contained. Preferably, it is Tg + 40 ° C. to Tg + 100 ° C., more preferably Tg + 50 ° C. to Tg + 70 ° C.

When the temperature of the molten resin immediately before being extruded from the die is Tg + 40 ° C. or higher, the viscosity of the extruded molten resin becomes low, the small holes are less likely to be clogged, and the actual small hole opening ratio is lowered. The resin particles to be made are less likely to be deformed. On the other hand, when the temperature of the molten resin immediately before being extruded from the die is Tg + 100 ° C. or less, the extruded molten resin tends to solidify and foaming is suppressed. Further, the viscosity of the extruded molten resin does not become too low, the rotary cutter can stably cut the extruded molten resin, and the extruded molten resin is less likely to wind around the rotary cutter.

The cutting device for cutting the molten resin extruded into the circulating pressurized cooling water in the first melt-kneading method is not particularly limited. Examples thereof include a device that is transferred to a centrifugal dehydrator to dehydrate and consolidate without foaming in the pressure circulation cooling water.

The advantage of the first melt-kneading method is that the running cost is lower than that of the second melt-kneading method because even the foamable resin particles can be produced in the same equipment.

The advantage of the second melt-kneading method is that the resin particles can be impregnated with the foaming agent using the equipment used for producing general foamable resin particles, so that no large capital investment or equipment change is required, and , The production stability of the resin particles is high even if the amount of graphite, the particle size of graphite, etc. are changed.

The foamable thermoplastic resin of the present invention can also be produced by seed polymerization used for producing general foamable resin particles. Specifically, the thermoplastic resin and the masterbatch (graphite masterbatch) of the present invention are melt-kneaded with an extruder, extruded through a die having small pores, and cut with a cutter to obtain graphite-containing resin seed particles. After that, the graphite-containing resin seed particles are suspended in water, and seed polymerization is performed by supplying a resin monomer, an initiator, and if necessary, other additives such as a brominated flame retardant and a nucleating agent. , A method of impregnating the foaming agent before and / or during and / or after the polymerization.

The advantage of the polymerization method is that the polymerization and the foaming agent can be impregnated using the equipment used for producing general foamable resin particles, so that no large capital investment or equipment change is required.

In the method for producing foamable thermoplastic resin particles of the present invention, the foamable heat obtained by melt-kneading a masterbatch having an excellent dispersion state of graphite (highly dispersibility and contained in a high concentration) with a thermoplastic resin is obtained. The thermoplastic resin particles have excellent dispersibility of graphite and can exhibit excellent heat insulating properties. Specifically, a solution in which foamable thermoplastic resin particles were dispersed in a solvent was measured by a laser diffraction scattering method using laser light having a wavelength of 632.8 nm, and the laser scattering intensity per unit solution concentration of graphite was 6. It is preferably 0.0 {% / (mg / ml)} /% by weight or more, and more preferably 6.5 {% / (mg / ml)} /% by weight or more.

[Preliminary foamed particles and foamed molded product]
The foamable thermoplastic resin particles of the present invention are foamed 10 to 110 times by a conventionally known pre-foaming step, for example, heated steam to obtain pre-foamed resin particles, which are cured for a certain period of time if necessary, and then molded. used. The obtained preliminary foamed resin particles are molded by steam (for example, in-mold molding) using a conventionally known molding machine to produce a foamed molded product. Depending on the shape of the mold used, it is possible to obtain a molded product having a complicated shape or a block-shaped molded product.

According to the effervescent thermoplastic resin particles of the present invention, even if the effervescent molded product has a high effervescence ratio of 80 times (cm ³ / g), it can have very low thermal conductivity. Specifically, it is preferable to exhibit a very low thermal conductivity A of 0.0306 W / mK or less at a foaming magnification of 80 times, which will be described later. Further, after storage for 30 days at a temperature of 50 ° C. at which the foaming agent easily volatilizes, the thermal conductivity B at a foaming magnification of 80 times, which will be described later, is preferably very low at 0.0324 W / mK or less, and in this case, it is extremely low for a long period of time. In addition, low thermal conductivity and thus high heat insulation can be maintained. At a foaming magnification of 50 times, it is preferable that the thermal conductivity A is 0.0284 W / mK or less and the thermal conductivity B is 0.0306 W / mK or less.

Further, since the amount of the foamable thermoplastic resin particles used as a raw material decreases as the foaming ratio increases in the foamed molded product, according to the present invention, the foamed molded product having a high foaming ratio can be produced at low cost. ..

The styrene-based resin foam molded product according to the embodiment of the present invention has low thermal conductivity, self-extinguishing property, and can be adjusted to an oxygen index of 26 or more. It can be particularly preferably used as a heat insulating material.

The foaming ratio of the foam molded product is preferably 70 times (cm ³ / g) or more, more preferably 80 times (cm ³ / g) or more. According to the present invention, low thermal conductivity can be achieved even when the foamed molded product is 80 times or more, so that the manufacturing cost is low and the weight is also advantageous, and the foamed molded product with higher foaming is also high. High performance heat insulation can be exhibited.

In addition, in this specification, the foaming ratio is ^{shown in the unit of "times" or "cm 3} / g", but these have the same meaning.

The average cell diameter of the foam molded product is preferably 70 to 250 μm, more preferably 90 to 200 μm, and even more preferably 100 to 180 μm. When the average cell diameter is in the above range, the foam molded product has higher heat insulating properties. When the average cell diameter is 70 μm or more, the closed cell ratio of the foamed molded product increases, and when it is 250 μm or less, the thermal conductivity decreases. The average cell diameter can be adjusted, for example, by appropriately selecting the amount of the nucleating agent.

[Use]
Since the foam molded product obtained by using the foamable thermoplastic resin particles of the present invention can have a low thermal conductivity after a long period of time, it is used as a heat insulating material for buildings, fish, etc. used for floors, walls, roofs, etc. It can be used for various purposes such as agricultural and marine products boxes such as boxes for transporting marine products such as vegetables and agricultural products such as vegetables, heat insulating materials for bathrooms, and heat insulating materials for hot water storage tanks.

The present invention is not limited to the above-described embodiments, and various modifications can be made within the scope of the claims, and the embodiments obtained by appropriately combining the technical means disclosed in the different embodiments. Is also included in the technical scope of the embodiment of the present invention.

Hereinafter, one embodiment of the present invention will be specifically described based on Examples and Comparative Examples, but the present invention is not limited thereto.

The measurement method and evaluation method in the following Examples and Comparative Examples are as follows.

(Measurement of Thermal Conductivity A of Styrene-based Resin Foam Mold)
It is generally known that the larger the measured average temperature of thermal conductivity, the larger the value of thermal conductivity, and it is necessary to determine the measured average temperature in order to compare the heat insulating properties. In this specification, 23 ° C. defined by JIS A9511: 2006R, which is a standard for foamed plastic heat insulating materials, is adopted as a standard.

In the following Examples and Comparative Examples, the thermal conductivity A is obtained by cutting out a thermal conductivity measurement sample from a styrene-based resin foam molded body, allowing the sample to stand at a temperature of 50 ° C. for 48 hours, and further at a temperature of 23 ° C. The measurement was carried out after allowing the mixture to stand for 24 hours.

More specifically, a sample having a length of 300 mm, a width of 300 mm, and a width of 25 mm was cut out from the styrene-based resin foam molded product. In the thickness direction, the thickness of the styrene resin foam molded product of 25 mm was used as it was. Therefore, the two surfaces of the sample having a length of 300 mm and a width of 300 mm remain the same as the surfaces of the styrene-based resin foam molded product when molded. Such a molded surface is generally called a "surface skin" and is defined in the specification as a "surface layer". 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 using a thermal conductivity measuring device (HC-074, manufactured by Eiko Seiki Co., Ltd.). The thermal conductivity A was measured by a heat flow metering method in accordance with JIS A 1412-2: 1999 at an average temperature of 23 ° C. and a temperature difference of 20 ° C.

(Measurement of thermal conductivity B of styrene resin foam molded product after annealing)
In order to evaluate the thermal conductivity B when the foaming agent is replaced with air after a long period of time, a thermal conductivity measurement sample is cut out from the styrene resin foamed molded product, and the sample is allowed to stand at a temperature of 50 ° C. for 30 days. Further, after allowing to stand at a temperature of 23 ° C. for 24 hours, the thermal conductivity B was 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 body is 0.5% or less, and the thermal conductivity is reduced. The effect on the rate is minor, and the thermal conductivity B when the styrene resin foam molded product is used at room temperature for a long period of time can be evaluated almost accurately.

More specifically, 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 product in the same manner as in the measurement of the thermal conductivity A. 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, and then using a thermal conductivity measuring device (HC-074, manufactured by Eiko Seiki Co., Ltd.). The thermal conductivity B was measured by a heat flow metering method in accordance with JIS A 1412-2: 1999 at an average temperature of 23 ° C. and a temperature difference of 20 ° C.

(Measurement of bulk density of graphite)
With a 200 ml graduated cylinder tilted 30 ° from an upright position, 145 to 155 ml of graphite is gradually added to the graduated cylinder using a spoon. Next, the measuring cylinder is dropped 30 times from a height of 3 cm with the graduated cylinder upright, and after repeating this operation until the volume change of graphite becomes less than 0.5 ml during the subsequent 30 drops, the mass of graphite And measure the volume. At this time, the bulk density of graphite is calculated by the following formula.

Graphite bulk density [g / cm ³ ] = graphite mass [g] / graphite volume [cm ³ ].

(Measurement of graphite content)
About 10 mg of the graphite masterbatch obtained in Examples and Comparative Examples and the effervescent styrene resin particles were collected and used as samples. This sample was continuously subjected to the following I to III using a thermogravimetric measuring device (TG / DTA 220U manufactured by SII Nanotechnology Co., Ltd.) equipped with a thermal analysis system: EXSTAR6000, and the weight was reduced in III. The amount was taken as the weight of graphite and expressed as a percentage of the weight of the test piece.
I. After raising the temperature from 40 ° C to 600 ° C at 20 ° C / min under a nitrogen stream of 200 mL / min, hold at 600 ° C for 10 minutes.
II. After lowering the temperature from 600 ° C to 400 ° C at 10 ° C / min under a nitrogen stream of 200 mL / min, hold at 400 ° C for 5 minutes.
III. The temperature is raised from 400 ° C. to 800 ° C. at 20 ° C./min under an air flow of 200 mL / min, and then held at 800 ° C. for 15 minutes.

(Measurement of average particle size D50 (μm) and laser scattering intensity (%) of graphite)
(1) Sample solution preparation conditions (a) When the measurement target is effervescent styrene resin particles 500 mg of the sample is dissolved and dispersed in 20 mL of a 0.1% (w / w) span 80 toluene solution.
(B) When the measurement target is graphite before kneading, that is, graphite itself as a raw material 20 mg of graphite and 480 mg of styrene resin (A) are dissolved and dispersed in 20 mL of a 0.1% (w / w) span 80 toluene solution.
(C) When the measurement target is a graphite masterbatch 40 mg of the graphite masterbatch was dissolved and dispersed in 20 mL of a 0.1% (w / w) span 80 toluene solution.
In (a) to (c), the dispersion means a state in which the resin is dissolved and graphite is dispersed.

Next, the sample solution is irradiated with ultrasonic waves using an ultrasonic cleaner to alleviate the aggregation of graphite.
(2) Ultrasonic irradiation conditions Equipment used: Ultrasonic cleaner manufactured by AS ONE Corporation Model number USM
Oscillation frequency: 42kHz
Irradiation time: 10 minutes Temperature: Room temperature.

(3) Particle size measurement condition Measuring device: Laser diffraction type particle size distribution measuring device manufactured by Malvern Co., Ltd. Mastersizer 3000
Light source: 632.8 nm red He-Ne laser and 470 nm blue LED
Dispersion unit: Wet dispersion unit Hydro MV
The analysis was carried out with the following settings, and the volume distribution was obtained by measurement and analysis by the laser diffraction / scattering method based on the Mie theory based on ISO13320: 2009 and JIS Z8825: 2013, and the average particle size D50 of graphite in the sample was determined. Calculated.
Particle type: Non-spherical graphite Refractive index: 2.42
Graphite absorption rate: 1.0
Dispersion medium: 0.1% (w / w) span 80 toluene solution Refractive index of dispersion medium: 1.49
Number of agitation in the dispersion unit: 2500 rpm
Analytical model: General purpose, maintain single mode Measurement temperature: Room temperature.

(4) Measurement procedure 120 mL of a 0.1% (w / w) span 80 toluene solution was injected into the dispersion unit and stirred at 2500 rpm for stabilization. The intensity of the light measured by the central detector when the sample solution sample was not present in the measurement cell and the laser beam of 632.8 nm red He-Ne was irradiated in the state of only the dispersion medium was defined as the intensity Lb of the transmitted light. Then, 2 mL of the sonicated sample solution was collected and added to the dispersion unit. The intensity of the light measured by the central detector when the sample solution was added and irradiated with 632.8 nm red He-Ne laser light 1 minute later was defined as the intensity Ls of the transmitted light. At the same time, D50 was measured. From the obtained Ls and Lb, the laser scattering intensity Ob of the sample solution was calculated by the following formula.

Ob = (1-Ls / Lb) x 100 (%)
The central detector is a detector located in front of the laser beam output, and the light detected here is a measure of transmitted light that was not used for scattering. Laser scattering intensity is a measure of the amount of laser light lost when a sample is scattered by the laser of an analyzer.

(5) Calculation of Laser Scattering Intensity per Unit Solution Concentration of Effervescent Styrene Resin Particles The laser scattering intensity per unit solution concentration of effervescent styrene resin particles was calculated by the following formula.

Effervescent Styrene-based Resin Particles Laser Scattering Intensity per Unit Solution Concentration (% / (mg / ml)) = Laser Scattering Intensity (Ob) / {Sample Weight (500 mg) / Toluene Amount (20 mL) x Sample Injection Amount (2 mL) / Total amount of toluene in the dispersion unit (120 mL + 2 mL)}.

The laser scattering intensity per unit solution concentration is a value obtained by dividing the measured laser scattering intensity by the sample concentration in toluene. Since this measuring device is a device that needs to measure with a solution, the sample concentration in the toluene solution is kept constant, and the measured value at a constant sample amount is obtained.

(6) Calculation of Laser Scattering Intensity Per Graphite Unit Solution Concentration in Effervescent Styrene Resin Particles The laser scattering intensity per graphite unit solution concentration contained in the effervescent styrene resin particles is calculated by the following formula. did.

Laser scattering intensity per graphite unit solution concentration in effervescent styrene resin particles {% / (mg / ml)} / wt% = Laser scattering intensity per effervescent styrene resin particle unit solution concentration (% / (mg / mg /) ml)) / Graphite content (% by weight) of the effervescent styrene resin particles.

It is an essence of one embodiment of the present invention that even if the weight of graphite is the same, the heat insulating property can be improved by adjusting the state of graphite contained in the foamable styrene resin particles, that is, the dispersed concentration. One embodiment of the present invention can be expressed by using the laser scattering intensity per graphite unit solution concentration.

(7) Calculation of laser scattering intensity per unit solution concentration of mixture of graphite and styrene resin before kneading Laser scattering per unit solution concentration of mixture of graphite and styrene resin before kneading by the following formula. The strength was calculated.

Laser scattering intensity per unit solution concentration of mixture of graphite and styrene resin before kneading {% / (mg / ml)} = Laser scattering intensity (Ob) / [{Graphite weight (20 mg) + styrene resin (480 mg) )} / Toluene amount (20 mL) x sample injection amount (2 mL) / total toluene amount in the dispersion unit (120 mL + 2 mL)].

(8) Laser Scattering Intensity Per Graphite Unit Solution Concentration Before Kneading The laser scattering intensity per kneading graphite, that is, the raw material graphite unit solution concentration was calculated by the following formula.

Laser scattering intensity per unit solution concentration of graphite before kneading {% / (mg / ml)} / wt% = Laser scattering intensity per unit solution concentration of graphite and styrene resin before kneading (% / (mg) / Ml)) / Graphite content in the mixture of graphite and styrene resin before kneading (20/500 x 100 = 4% by weight)
(9) Calculation of Laser Scattering Intensity per Graphite Master Batch Unit Solution Concentration The laser scattering intensity per graphite master batch unit solution concentration was calculated by the following formula.

Laser scattering intensity per graphite master batch unit solution concentration (% / (mg / ml)) = laser scattering intensity (Ob) / {master batch weight (40 mg) / toluene amount (20 mL) x sample injection amount (2 mL) / dispersion Total amount of toluene in the unit (120 mL + 2 mL)}.

(10) Calculation of Laser Scattering Intensity per Graphite Unit Solution Concentration in Graphite Master Batch The laser scattering intensity per graphite unit solution concentration in the graphite master batch was calculated by the following formula.

Laser scattering intensity per graphite unit solution concentration in Graphite Master batch {% / (mg / ml)} / wt% = Laser scattering intensity per graphite master batch unit solution concentration (% / (mg / ml)) / Graphite Master Batch graphite content (% by weight).

(Measurement of bromine content)
The content of bromine was determined by performing a quantitative analysis of bromine by an ion chromatography method (hereinafter referred to as IC method) after performing an oxygen flask combustion method.

(1) Oxygen Flask Combustion Method A sample (styrene resin foam molded product 5 mg) was placed in the center of the filter paper having a fire-conducting portion, and the filter paper was folded in three in the vertical direction with the fire-conducting portion fixed. Then, the filter paper was folded in three in the horizontal direction, and the filter paper containing the sample was placed in a platinum basket attached to a stopper (glass stopper) of a 500 ml combustion flask. On the other hand, the Erlenmeyer flask of the combustion flask was filled with oxygen by adding 25 ml of an absorbent solution (ultrapure water to which 1 drop of saturated hydrazine was added dropwise).

The ignition part of the filter paper was ignited, a platinum basket to which the filter paper was fixed was inserted into the Erlenmeyer flask, and the sample was burned inside the Erlenmeyer flask. After the completion of combustion, the combustion flask was tilted and shaken for 2 minutes, and then left for 1 hour to absorb the bromine generated by the combustion into the absorbing liquid.

(2) IC method The amount of bromine ions was measured by the IC method with respect to the absorbed liquid obtained by the oxygen flask combustion method.
Equipment used: ICS-2000 manufactured by Nippon Dionex
Column: IonPac AG18, AS18 (4 mmφ x 250 mm)
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 formula.

Bromine concentration (%) in the sample = [{IC measurement result (mg / l) of styrene resin foam molded product-background test result (mg / l)} x 25 (ml) x 1000] / {Sample collection amount (Mg) x 10000}.

(Measurement of foaming ratio and evaluation of foaming performance and molding performance)
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 product in the same manner as in the case of measuring the thermal conductivity. The weight (g) of the sample was measured, and 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 of the measured dimensions, and the foaming ratio was calculated according to the following formula.

Foaming magnification (cm ³ / g) = sample volume (cm ³ ) / sample weight (g)
As described above, the expansion ratio "times" of the styrene resin foam molded product is customarily expressed as "cm ³ / g".

Further, the surface of the obtained molded product 80 times larger was observed, and it was determined that the one having few voids between particles had good surface beauty and the one having conspicuous voids had poor surface beauty.

The foaming / molding performance of the styrene resin foam was evaluated based on the measured foaming ratio and the beauty of the surface of the molded product. The foaming and molding performance was evaluated according to the following criteria.
◯: A beautiful molded product that can be foamed 80 times was obtained.
Δ: It was possible to foam 80 times, but a beautiful molded product could not be obtained.
X: It was impossible to foam 80 times.

(Evaluation of flame retardancy)
The foamed molded product was allowed to stand at a temperature of 60 ° C. for 48 hours, and further allowed to stand at a temperature of 23 ° C. for 24 hours, and then the oxygen index was measured according to JIS K7201.

(Evaluation method of average cell diameter of styrene resin foam molded product)
A styrene resin foam molded product having a foaming magnification of 50 times is cut with a razor, and a cross section thereof is photographed using an optical microscope (DIGITAL MICROSCOPE VHX-900 manufactured by KEYENCE) at an observation magnification of 100 times. The number of cells existing in the range of 1000 μm × 1000 μm square at the center of the foamed particles existing in the cross section is counted. Using the number of cells, the cell diameter was calculated based on the following formula.
Cell diameter (μm) = 2 x [1000 μm x 1000 μm / (number of cells x pi)] ^0.5
The above operation was carried out on five foamed particles existing in the cross section of the styrene resin foam molded product, and the average value of the obtained five cell diameters was taken as the average cell diameter.

The raw materials used in Examples and Comparative Examples are shown below.

(Styrene resin)
(A) Styrene homopolymer [manufactured by PS Japan Corporation, 680]
(Graphite)
(B1) Graphite [Scale graphite SGP-40B, manufactured by Marutoyo Casting Co., Ltd.]
Average particle size D50: 5.8 μm
Laser scattering intensity per graphite unit solution concentration: 4.0 {% / (mg / ml)} / wt%
(B2) Graphite [Scale graphite BF-3AK, manufactured by Chuetsu Graphite Industry Co., Ltd.]
Average particle size D50: 3.2 μm
Laser scattering intensity per graphite unit solution concentration: 5.8 {% / (mg / ml)} / wt%
(B3) Graphite [Scale graphite BF-10AK, manufactured by Chuetsu Graphite Industry Co., Ltd.]
Average particle size D50: 9.6 μm
Laser scattering intensity per graphite unit solution concentration: 3.2 {% / (mg / ml)} / wt%
(B4) Graphite [Scale graphite UCP, manufactured by Nippon Graphite Industry Co., Ltd.]
Average particle size D50: 13.3 μm
Laser scattering intensity per graphite unit solution concentration: 3.6 {% / (mg / ml)} /% by weight.

(Brominated flame retardant)
(C1) 2,2-bis [4- (2,3-dibromo-2-methylpropoxy) -3,5-dibromophenyl] propane [manufactured by Dai-ichi Kogyo Seiyaku Co., Ltd., SR-130, bromine content = 66% by weight].

(Heat stabilizer)
(D1) Tetrakis (2,2,6,6-tetramethylpiperidyloxycarbonyl) butane [LA-57 manufactured by ADEKA Corporation]
(D2) Bis (2,6-di-t-butyl-4-methylphenyl) pentaerythritol diphosphite [PEP-36 manufactured by ADEKA Corporation].

(Foaming agent)
(E1) Normal pentane [manufactured by Wako Pure Chemical Industries, Ltd., reagent product]
(E2) Isopentane [manufactured by Wako Pure Chemical Industries, Ltd., reagent product]
(E3) Isobutane [Mitsui Chemicals, Inc.].

(Other additives)
(F) Ethylene bisstearic acid amide [manufactured by NOF CORPORATION, Alflo H-50S].

(Example 1)
Raw materials are added to the Banbury mixer so that the total weight (A + B1 + F) of 49% by weight of the styrene resin (A), 50% by weight of the graphite (B1), and 1% by weight of the ethylene bisstearic acid amide (F) is 100% by weight. Then, the mixture was melt-kneaded for 20 minutes without heating and cooling under a load of 5 kgf / cm ^2. At this time, the resin temperature was measured and found to be 180 ° C. A strand-shaped resin supplied to a ruder and extruded at a discharge rate of 250 kg / hr through a die having a small hole attached to the tip was cooled and solidified in a water tank at 30 ° C., and then cut to obtain a master batch (I1). ..

(Example 2)
A graphite masterbatch (I2) was obtained in the same manner as in Example 1 (except that the styrene resin (A) was changed to 39% by weight and the graphite (B1) was changed to 60% by weight in Example 1).

(Example 3)
A graphite masterbatch (I3) was obtained in the same manner as in Example 1 except that the styrene resin (A) was changed to 29% by weight and the graphite (B1) was changed to 70% by weight in Example 1.

(Example 4)
A graphite masterbatch (I4) was obtained in the same manner as in Example 1 except that the styrene resin (A) was changed to 49% by weight and the graphite (B2) was changed to 50% by weight in Example 1.

(Example 5)
A graphite masterbatch (I5) was obtained in the same manner as in Example 4 except that the styrene resin (A) was changed to 39% by weight and the graphite (B2) was changed to 60% by weight in Example 4.

(Example 6)
A graphite masterbatch (I6) was obtained in the same manner as in Example 1 except that the styrene resin (A) was changed to 29% by weight and the graphite (B3) was changed to 70% by weight in Example 1.

(Comparative Example 1)
A graphite masterbatch (I7) was obtained in the same manner as in Example 1 except that the styrene resin (A) was changed to 59% by weight and the graphite (B1) was changed to 40% by weight in Example 1.

(Comparative Example 2)
A graphite masterbatch (I8) was obtained in the same manner as in Example 1 except that the styrene resin (A) was changed to 9% by weight and the graphite (B1) was changed to 90% by weight in Example 1.

(Comparative Example 3)
A graphite masterbatch (I9) was obtained in the same manner as in Example 1 except that the styrene resin (A) was changed to 29% by weight and the graphite (B4) was changed to 70% by weight in Example 1.

(Comparative Example 4)
A graphite masterbatch (I10) was obtained in the same manner as in Example 6 except that the styrene resin (A) was changed to 49% by weight and the graphite (B3) was changed to 50% by weight in Example 6.

For the master batches (I1) to (I10) obtained in Examples 1 to 6 and Comparative Examples 1 to 4, the graphite content, the average particle size D50 of graphite, and the laser scattering intensity were measured according to the above-mentioned measuring methods. The measurement results and evaluation results are shown in Table 1.

(Masterbatch of a mixture of brominated flame retardant and heat stabilizer)
(J1) After supplying the styrene resin (A) to the twin-screw extruder and melt-kneading it, a mixture of the brominated flame retardant (C1), the stabilizer (D1) and (D2) is supplied from the middle of the extruder. Then, it was further melt-kneaded. However, the weight ratio of each material is (A) :( C1) :( D1) :( D2) = 70: 28.5: 0.6: 0.9, (A) + (C1) + (D1). + (D2) = 100% by weight. A strand-shaped resin extruded at a discharge rate of 300 kg / hr is cooled and solidified in a water tank at 20 ° C. through a die having a small hole attached to the tip of the extruder, and then cut to form a brominated flame retardant and a heat stabilizer. A masterbatch of the mixture was obtained. At this time, the set temperature of the extruder was 170 ° C. The bromine content in the masterbatch was 18.8% by weight.

(Example 7)
[Preparation of foamable styrene resin particles]
The styrene resin (A), the master batch (J1), and the graphite master batch (I1) were each put into a blender and blended for 10 minutes to obtain a resin mixture. The weight ratio of each material was (A) :( J1) :( I1) = 83.65: 8.35: 8.00, (A) + (J1) + (I1) = 100% by weight.

The obtained resin mixture is supplied to a tandem type two-stage extruder in which a same-direction twin-screw extruder (first extruder) having a diameter of 40 mm and a single-screw extruder (second extruder) having a diameter of 90 mm are connected in series. Then, melt-kneading was performed at a set temperature of 190 ° C. and a rotation speed of 150 rpm of an extruder having a diameter of 40 mm. From the middle of the 40 mm diameter extruder (first extruder), 4 mixed pentane [a mixture of 80% by weight of normal pentane (E1) and 20% by weight of isopentane (E2)] was added to 100 parts by weight of the resin composition. .3 parts by weight and isobutane (E3) were press-fitted at a ratio of 2.2 parts by weight. Then, it was supplied to a 90 mm diameter extruder (second extruder) through a continuous pipe set at 200 ° C.

After cooling the molten resin to a resin temperature of 160 ° C with a 90 mm diameter extruder (second extruder), the diameter is 0.65 mm and the land length is 3 attached to the tip of the second extruder set at 250 ° C. A die having 60 small holes of 0.0 mm was extruded into pressurized circulating water at a temperature of 60 ° C. and 0.8 MPa at a discharge rate of 50 kg / hour. The extruded molten resin is cut and granulated under the condition of 1500 rpm using a rotary cutter having 10 blades in contact with the die, and transferred to a centrifugal dehydrator to obtain foamable styrene resin particles. It was. At this time, the residence time in the first extruder was 2 minutes, and the residence time in the second extruder was 5 minutes.

0.08 part by weight of zinc stearate was dry-blended with respect to 100 parts by weight of the obtained foamable styrene resin particles, and then stored at 15 ° C.

[Preparation of preliminary foamed particles]
Two weeks after the effervescent styrene resin particles were prepared and stored at 15 ° C., the effervescent styrene resin particles were put into a prefoaming machine [BHP-300, manufactured by Daikai Kogyo Co., Ltd.], and 0.08 MPa of water vapor was used. Was introduced into a pre-foaming machine and foamed to obtain pre-foamed particles having a foaming ratio of 80 times.

Preliminary foamed particles having a foaming ratio of 50 times were obtained in the same manner as described above.

[Preparation of styrene resin foam molded product]
Inside the in-mold molding die (length 450 mm x width 310 mm x thickness 25 mm) in which the obtained pre-foamed particles with a foaming ratio of 80 times were attached to a styrofoam molding machine [KR-57, manufactured by Daisen Kogyo Co., Ltd.]. Was filled with water vapor of 0.06 MPa and foamed in the mold, and then water was sprayed on the mold for 3 seconds to cool the mold. After holding the styrene resin foam molded product in the mold until the pressure at which the styrene resin foam molded product pushes the mold becomes 0.015 MPa (gauge pressure), the styrene resin foam molded product is taken out and the rectangular styrene is taken out. A based resin foam molded product was obtained. The foaming ratio was 80 times.

In the same manner as described above, a styrene resin foam molded product having a foaming ratio of 50 times was obtained.

(Example 8)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 85.65% by weight and the graphite masterbatch (I2) was changed to 6.00% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Example 9)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 87.08% by weight and the graphite masterbatch (I3) was changed to 4.57% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Example 10)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 83.65% by weight and the graphite masterbatch (I4) was changed to 8.00% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Example 11)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 84.65% by weight and the graphite masterbatch (I4) was changed to 7.00% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Example 12)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 86.48% by weight and the graphite masterbatch (I5) was changed to 5.17% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Example 13)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 85.85% by weight and the graphite masterbatch (I6) was changed to 5.80% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Example 14)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 75.65% by weight and the graphite masterbatch (I1) was changed to 16.00% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Comparative Example 5)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 81.65% by weight and the graphite masterbatch (I7) was changed to 10.00% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Comparative Example 6)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 87.15% by weight and the graphite masterbatch (I8) was changed to 4.50% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Comparative Example 7)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 85.65% by weight and the graphite masterbatch (I9) was changed to 6.00% by weight. A styrene-based resin foam molded product was produced by the above treatment.

(Comparative Example 8)
Same as in Example 7 except that in [Preparation of foamable styrene resin particles] of Example 7, the styrene resin (A) was changed to 83.65% by weight and the graphite masterbatch (I10) was changed to 8.00% by weight. A styrene-based resin foam molded product was produced by the above treatment.

With respect to the foamable styrene resin particles obtained in Examples 7 to 14 and Comparative Examples 5 to 8, the styrene resin foamed molded product had a graphite content, an average graphite particle size D50, and laser scattering according to the above-mentioned measurement method. Strength, bromine content, styrene, average cell diameter, moldability, oxygen index, and thermal conductivity A and B were measured. The measurement results and evaluation results are shown in Table 2.

As shown in Table 2, in Examples 7 to 9 and Examples 11 to 12, if the graphite masterbatch satisfies the requirements of the present invention, the higher the graphite content in the masterbatch, the more the graphite unit solution. The laser scattering intensity per concentration is also excellent, that is, the dispersibility of graphite is higher. Therefore, it is possible to reduce the graphite content in the foamable resin particles while maintaining the low thermal conductivity of the foamed molded product. Therefore, in the case of mass production, it can be expected that a foam molded product having both a high foaming ratio and high heat insulating performance can be produced while suppressing the raw material cost and the processing cost.

All of the above-described embodiments are illustrative and not limited to one embodiment of the present invention, and one embodiment of the present invention shall be implemented in various other modifications and modifications. Can be done. Therefore, the scope of one embodiment of the present invention is defined only by the claims and their equivalents.

Claims (22)

In the method for producing a masterbatch containing graphite and a thermoplastic resin,
The average particle size D50 of the graphite is 2-9 μm.
The graphite content satisfies the following formula (1).
Equation (1): M _min ≤ M ≤ 80 [% by weight]
(Here, in the above formula (1), when 2 ≦ D50 <5, M _min = 41, and when 5 ≦ D50 ≦ 9, M _min = 419 × C ^1.34 . M is 100% by weight of the master batch. Graphite content [% by weight], C indicates graphite bulk density [g / cm ³ ])
A method for producing a masterbatch in which a mixture containing the graphite and the thermoplastic resin is kneaded by a kneading device equipped with a biaxial stirrer. The method for producing a masterbatch according to claim 1, wherein the laser scattering intensity per concentration of the graphite unit solution in the masterbatch is 5.5 {% / (mg / ml)} / wt% or more. The masterbatch according to any one of claims 1 and 2, wherein the laser scattering intensity per concentration of the graphite unit solution in the masterbatch is 6.0 {% / (mg / ml)} / wt% or more. Production method. The method for producing a masterbatch according to any one of claims 1 to 3, wherein the graphite content satisfies the following formula (2).
Equation (2): M _min2 ≤ M ≤ 80 [% by weight]
(Here, in the above equation (2), when 2 ≦ D50 <7.5, M _min2 = 51, and when 7.5 ≦ D50 ≦ 9, M _min2 = 419 × C ^1.34 . M is a master batch. Graphite content at 100% by weight [% by weight], C indicates the bulk density of graphite [g / cm ³ ]) The method for producing a masterbatch according to any one of claims 1 to 4, wherein the graphite content is 61% by weight or more and 80% by weight or less. The kneading is carried out with a load of 3.5 kgf / cm ² or more.
Resin temperature: Tg + 50 ° C. or higher (where Tg is the glass transition temperature of the thermoplastic resin), kneading time: 10 minutes or longer.
The method for producing a masterbatch according to any one of claims 1 to 5. The method for producing a masterbatch according to any one of claims 1 to 6, wherein the thermoplastic resin is a styrene resin. A masterbatch containing graphite and a thermoplastic resin having an average particle size D50 of 2 to 9 μm.
The masterbatch satisfies the following equation (1),
Equation (1): M _min ≤ M ≤ 80 [% by weight]
(Here, in the above formula (1), when 2 ≦ D50 <5, M _min = 41, and when 5 ≦ D50 ≦ 9, M _min = 419 × C ^1.34 . M is 100% by weight of the master batch. In, the graphite content [% by weight] and C indicate the bulk density of graphite [g / cm ³ ]), and
A masterbatch in which the laser scattering intensity per concentration of the graphite unit solution in the masterbatch is 5.5 {% / (mg / ml)} /% by weight or more. The masterbatch according to claim 8, wherein the laser scattering intensity per concentration of the graphite unit solution in the masterbatch is 6.0 {% / (mg / ml)} /% by weight or more. The masterbatch according to any one of claims 8 and 9, wherein the masterbatch satisfies the following formula (2).
Equation (2): M _min2 ≤ M ≤ 80 [% by weight]
(Here, in the above equation (2), when 2 ≦ D50 <7.5, M _min2 = 51, and when 7.5 ≦ D50 ≦ 9, M _min2 = 419 × C ^1.34 . M is a master batch. Graphite content at 100% by weight [% by weight], C indicates the bulk density of graphite [g / cm ³ ]) The masterbatch according to any one of claims 8 to 10, wherein the graphite content is 61% by weight or more and 80% by weight or less. The masterbatch according to any one of claims 8 to 11, wherein the thermoplastic resin is a styrene resin. A method for producing foamable thermoplastic resin particles, comprising a masterbatch obtained by the method for producing a masterbatch according to any one of claims 1 to 7 and a step of melt-kneading the thermoplastic resin with an extruder. .. A method for producing foamable thermoplastic resin particles, comprising the master batch according to any one of claims 8 to 12 and a step of melt-kneading the thermoplastic resin with an extruder. A step of extruding a melt containing a foaming agent into a cutter chamber filled with circulating water through a die having a large number of small holes attached after the extruder, and immediately after extruding, cutting with a rotary cutter in contact with the die is further performed. Prepare, prepare
The method for producing foamable thermoplastic resin particles according to any one of claims 13 and 14. A step of extruding the melt through a die having a plurality of small holes attached after the extruder and cutting it with a cutter to obtain thermoplastic resin particles, and
Further comprising a step of suspending the thermoplastic resin particles in water and impregnating with a foaming agent.
The method for producing foamable thermoplastic resin particles according to any one of claims 13 and 14. The method for producing foamable thermoplastic resin particles according to any one of claims 13 to 16, wherein the graphite content is 2 to 8% by weight based on 100% by weight of the foamable thermoplastic resin particles. The laser scattering intensity per graphite unit solution concentration in the foamable thermoplastic resin particles is 6.5 {% / (mg / ml)} / wt% or more.
The method for producing foamable thermoplastic resin particles according to any one of claims 13 to 17. The method for producing foamable thermoplastic resin particles according to any one of claims 13 to 18, wherein the thermoplastic resin is a styrene resin. The foaming agent comprises at least two selected from the group of hydrocarbons having 4 to 6 carbon atoms, and at least one of the two species is a hydrocarbon having 4 or 5 carbon atoms.
The method for producing foamable thermoplastic resin particles according to any one of claims 15 to 19. Preliminary foaming heat comprising a step of pre-foaming the foamable thermoplastic resin particles produced by the method for producing foamable thermoplastic resin particles according to any one of claims 13 to 20 to produce pre-foamed resin particles. A method for producing thermoplastic resin particles. A method for producing a foamed molded article, comprising a step of molding the prefoamed thermoplastic resin particles produced by the method for producing prefoamed resin particles according to claim 21.