JP2013203470A - Container for carrying glass - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a container for carrying glass formed of a foamed molding which is impact-resistant, antistatic, and has favorable appearance even if a foaming rate is high.SOLUTION: A problem is solved by a glass carrying container. The glass carrying container is formed of a polystyrene based resin having a plurality of bubbles and bubble films dividing them and in which the bubble films form a continuous phase and polyacrylic alkyl ester resin particulates dispersed in the continuous phase and forming a disperse phase. In the glass carrying container, the polystyrene based resin is composed of a complex polystyrene-based resin foamed molding product which is complexed with polyacrylic alkyl ester resin particulates, and a plurality of the disperse phases exist in a state of lamellas in the thickness direction of the bubble films in the bubble film cross-sections of the complex polystyrene resin foam.

Description

The present invention relates to a glass transport container. ADVANTAGE OF THE INVENTION According to this invention, the container for glass conveyance which consists of a foaming molding which is excellent in impact resistance, antistatic property, and the external appearance also with high expansion ratio can be provided.
The glass transport container of the present invention can be used for transporting and storing glass substrates for liquid crystal displays and plasma displays, glass substrates for touch panels, and other thin glass substrates, in addition to base glass.

In containers for transporting glass products such as thin film glass for liquid crystal panels, impact resistance and impact relaxation properties to prevent damage to glass products from external impact, antistatic properties to prevent glass products from being charged, Various performances such as durability that can withstand repeated use are required.
In order to satisfy these requirements, containers of various structures and materials have been proposed.

For example, Japanese Unexamined Patent Application Publication No. 2009-269610 (Patent Document 1) and Japanese Unexamined Patent Application Publication No. 2011-255912 (Patent Document 2) are made of a synthetic resin foam having a specific shape that matches the shape of a plate-like body and a glass product. A plate-shaped body and a glass substrate transport container that can prevent compression deformation and breakage, have excellent durability, and can be used repeatedly are disclosed.
Japanese Patent Application Laid-Open No. 2008-222940 (Patent Document 3) discloses a continuous antistatic foam obtained by foaming a resin mixture containing an ethylene-vinyl acetate copolymer and conductive carbon black.

JP 2009-269610 A JP 2011-255912 A JP 2008-222940 A

However, there is a need for glass transport containers that have performances that exceed the prior art containers described above.
On the other hand, researches on foamed molded articles such as polystyrene-based resins, polypropylene-based resins, and rubber-modified styrene-based resins have been actively conducted, but each has advantages and disadvantages and is not sufficient as a material for glass transport containers.
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to solve the above-mentioned problems and to provide a glass transport container made of a foamed molded article that is excellent in impact resistance even at a high expansion ratio, and has good antistatic properties and appearance.

Thus, according to the present invention, a glass transport container,
The glass transport container has a plurality of bubbles and a bubble film partitioning them, and a polystyrene resin in which the bubble film forms a continuous phase, and a polyacryl dispersed in the continuous phase to form a dispersed phase An acid alkyl ester resin fine particle, and the polystyrene resin is composed of a composite polystyrene resin foam molded body in which the polyacrylic acid alkyl ester resin fine particle is combined,
There is provided a glass transport container, wherein the dispersed phase is present in a plurality of layers in the thickness direction of the bubble film cross section of the composite polystyrene resin foam molded article.

ADVANTAGE OF THE INVENTION According to this invention, the container for glass conveyance which consists of a foaming molding which is excellent in impact resistance also in high foaming magnification, and is excellent in antistatic property and external appearance can be provided.
That is, the composite polystyrene resin foam particles used as the material for the glass transport container of the present invention are foam particles made of a composite polystyrene resin in which polyacrylic acid alkyl ester resin fine particles are dispersed in a continuous phase of the polystyrene resin. When the foam film of the expanded particles is viewed in the cross section in the thickness direction, the polyacrylic acid alkyl ester resin fine particles have a distribution structure in which a plurality of the polyacrylic acid alkyl ester resin particles are present in the thickness direction.

Therefore, when a glass conveying container made of a foamed molded product is manufactured by filling this into a mold cavity and heating and foam-molding in the mold, the polyacrylic acid alkyl ester resin fine particles are in the thickness direction of the cell membrane. In other words, the polyacrylic acid alkyl ester resin fine particles are well oriented in the bubble film, and the polyacrylic acid alkyl ester resin fine particles are exposed from the bubble film surface without causing the bubbles to communicate. In order to keep the retention of the volatile foaming agent good, it is possible to provide a glass transport container comprising a composite polystyrene-based resin foam molded article excellent in all of mechanical strength, moldability and impact resistance.
The glass transport container of the present invention can be used for transporting and storing glass substrates for liquid crystal displays and plasma displays, glass substrates for touch panels, and other mainly thin glass substrates, in addition to base glass. It can be used suitably for conveyance of thin glass for liquid crystal display (panel).

  Further, according to the present invention, the dispersed phase has a dimension in the bubble film thickness direction (thickness of the polyacrylic acid alkyl ester resin fine particles) and a dimension in the bubble film surface direction (the thickness of the polystyrene resin resin expanded particles). When the length of the polyacrylic acid alkyl ester resin fine particles is c and d, respectively, the machine has an aspect ratio (d / c) of 7 or more and 60 or less, preferably 20 or more and 50 or less. It is possible to provide a glass transport container comprising a composite polystyrene-based resin foam molding having strength, moldability and impact resistance.

  Further, according to the present invention, the polystyrene resin has a weight average molecular weight (MW) of 200,000 to 350,000 and a ratio of the Z average molecular weight (MZ) to the weight average molecular weight (MW) (MZ / MW) of 2 to 4. When it has, it can provide the container for glass conveyance which consists of a composite polystyrene-type resin foaming molding which has more outstanding mechanical strength, a moldability, and impact resistance.

  According to the present invention, when the polyacrylic acid alkyl ester resin fine particles are formed from a polymer of ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, or a mixture thereof, polyacrylic acid is further added. When the alkyl ester resin fine particles are 5 to 100 parts by weight with respect to 100 parts by weight of the polystyrene resin, it is composed of a composite polystyrene resin foam molded article having better mechanical strength, moldability and impact resistance. A glass transport container can be provided.

Further, according to the present invention, when the composite polystyrene resin expanded particles further contain a component derived from polybutadiene terminal acrylate, the polystyrene resin and the polyacrylate resin are compatibilized to further improve the impact resistance. It is possible to provide a glass transport container made of the composite polystyrene-based resin foam molded article.
Here, compatibilization does not mean that the polyacrylic ester resin fine particles are present in the polystyrene resin simply by phase separation, but some or all of them are bonded by some bond, for example, a graft bond. This means that it exists in a mixture and is thought to contribute to the improvement of impact resistance.
Further, according to the present invention, when the composite polystyrene-based resin expanded particles have a bulk density of 0.015 g / cm ³ or more and 0.1 g / cm ³ or less, more excellent mechanical strength, moldability and impact resistance. It is possible to provide a glass transport container comprising a composite polystyrene-based resin foam-molded article having

Further, according to the present invention, the composite polystyrene-based resin foam molded article has a falling ball impact value of 11 cm or more according to JIS K7211, a bending break point displacement amount according to JIS K7221-1 of 12 mm or more, and a crack amount due to JIS Z0235 of less than 50%. When it has, it can provide the container for glass conveyance which consists of a composite polystyrene-type resin foaming molding which has more outstanding mechanical strength, a moldability, and impact resistance.
Further, according to the present invention, when the composite polystyrene resin foamed particles are surface-coated with an antistatic agent-containing component, the composite polystyrene system has excellent antistatic performance (surface resistivity of 1 × 10 ¹² Ω or less). A glass transport container made of a resin foam molded article can be provided.

(A) Scanning electron microscope (SEM) photograph of the cross section of the expanded particle of Example 1, (b) Transmission electron microscope (TEM) photograph of the cross section of the foamed particle bubble film. It is a transmission electron microscope (TEM) photograph for demonstrating the measuring method of the aspect-ratio of a foam particle foam film cross section. It is the schematic for demonstrating the measuring method of the crack amount of a foaming molding. It is a scanning electron microscope (SEM) photograph of the expanded particle cross section of Example 13. It is a scanning electron microscope (SEM) photograph of the expanded particle cross section of Example 14. 18 is a scanning electron microscope (SEM) photograph of a cross-section of expanded particles of Example 15. It is a transmission electron microscope (TEM) photograph of the cross section of the foamed molded product of Example 14.

The glass transport container of the present invention has a plurality of bubbles and a bubble film that partitions them, and the bubble film is dispersed in the continuous phase to form a dispersed phase by forming a continuous phase with the bubble film. Polyacrylic acid alkyl ester-based resin fine particles, and the polystyrene resin is composed of a composite polystyrene-based resin foam molded product obtained by combining the polyacrylic acid alkyl ester-based resin fine particles,
A plurality of the dispersed phases are present in the form of a plurality of layers in the thickness direction of the bubble film in the cross section of the bubble film of the composite polystyrene-based resin foam molded article.
That is, the container for transporting glass of the present invention is obtained by impregnating a composite polystyrene resin with a foaming agent to obtain expandable composite polystyrene resin particles, and pre-expanding the obtained expandable particles to obtain a composite polystyrene resin. It consists of a composite polystyrene-based resin foam molding obtained by obtaining foam particles (hereinafter also referred to as “foam particles”) and foam-molding the obtained foam particles.
Here, the “composite polystyrene resin” in the foamed particles of the present invention means a resin obtained by combining (compositing) a polystyrene resin and a polyacrylic acid alkyl ester resin.
In addition, the “composite polystyrene resin” is a form in which a dispersoid composed of polyacrylic acid alkyl ester resin fine particles is dispersed in a dispersion medium composed of a polystyrene resin. Is called “dispersed phase”.

The size and shape of the glass to be transported in the glass transport container of the present invention are not particularly limited as long as the container can be produced and the effects of the present invention can be obtained.
For example, a glass substrate for glass such as a liquid crystal television or a plasma television, or a base plate glass, in which one or both of the vertical and horizontal lengths exceed 1000 mm.
The effect of the present invention can be obtained by producing the glass transport container of the present invention in a desired shape by a known method using a foamed molded body described below as a constituent material.
Hereinafter, the constituent materials of the glass transport container of the present invention will be described in the order of resin particles, expandable resin particles, resin foam particles, and foamed molded article.

(Polystyrene resin particles: continuous phase)
The polystyrene resin constituting the continuous phase of the composite polystyrene resin foamed particles of the present invention is not particularly limited as long as it is a resin mainly composed of a styrene monomer, and a styrene or styrene derivative homopolymer or copolymer. Is mentioned.
Examples of the styrene derivative include α-methyl styrene, vinyl toluene, chlorostyrene, ethyl styrene, isopropyl styrene, dimethyl styrene, bromostyrene, and the like. These styrenic monomers may be used alone or in combination.

The polystyrene resin may be a combination of a vinyl monomer copolymerizable with a styrene monomer.
Examples of the vinyl monomer include divinylbenzene such as o-divinylbenzene, m-divinylbenzene and p-divinylbenzene, alkylene glycol di (meth) acrylate such as ethylene glycol di (meth) acrylate and polyethylene glycol di (meth) acrylate. Multifunctional monomers such as (meth) acrylate; α-methylstyrene, (meth) acrylonitrile, methyl (meth) acrylate, butyl (meth) acrylate and the like. Among these, polyfunctional monomers are preferable, ethylene glycol di (meth) acrylate, polyethylene glycol di (meth) acrylate having n of 4 to 16 and divinylbenzene are more preferable, and divinylbenzene and ethylene glycol di (meth) acrylate are more preferable. Particularly preferred. In addition, the monomer used together may be used independently or may be used together.
Moreover, when using the monomer used together, it is preferable that the content is set so that it may become the quantity (for example, 50 weight% or more) which a styrene-type monomer becomes a main component.
In the present invention, “(meth) acryl” means “acryl” or “methacryl”.

The polystyrene resin preferably has a weight average molecular weight (MW) of 200,000 to 350,000 and a ratio of the Z average molecular weight (MZ) to the weight average molecular weight (MW) (MZ / MW) of 2 to 4.
When the weight average molecular weight (MW) is less than 200,000, the polyacrylic acid alkyl ester resin fine particles in the cell membrane are difficult to be oriented, and the impact resistance may be lowered when a foamed molded product is obtained. On the other hand, when the weight average molecular weight (MW) exceeds 350,000, the foamability is lowered when foaming the composite polystyrene resin foamed particles, the elongation of the surface of the foamed molded product is insufficient, and the appearance of the foamed molded product is inferior. Sometimes.
Specific MWs are, for example, 200,000, 250,000, 300,000 and 350,000.

In addition, when the ratio (MZ / MW) of the Z average molecular weight (MZ) to the weight average molecular weight (MW) is less than 2, the polyacrylic acid alkyl ester resin fine particles in the bubble film are difficult to be oriented, and a foam molded article is obtained. Sometimes the impact resistance is reduced. On the other hand, when the ratio (MZ / MW) of the Z average molecular weight (MZ) to the weight average molecular weight (MW) exceeds 4, the foamability of the foamed composite polystyrene resin particles is reduced, and the surface of the foam molded product is reduced. In some cases, the appearance of the foamed molded article is inferior due to insufficient elongation.
A more preferable weight average molecular weight (MW) is 230,000 to 330,000, and a ratio of a Z average molecular weight (MZ) to a more preferable weight average molecular weight (MW) (MZ / MW) is 2 to 3.
Specific MZ / MW is, for example, 2.0, 2.5, 3.0, or the like.

(Polyacrylic acid alkyl ester resin fine particles: dispersed phase)
The polyacrylic acid alkyl ester resin fine particles constituting the dispersed phase of the composite polystyrene resin foamed particles of the present invention are not particularly limited as long as the resin is mainly composed of an acrylic acid alkyl ester monomer, for example, Examples include methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, pentyl acrylate, 2-ethylhexyl acrylate, hexyl acrylate, etc. Among them, ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate Is preferred. These alkyl acrylate monomers may be used alone or in combination. In addition, carbon number of the said "alkyl" means 1-30.
Therefore, the polyacrylic acid alkyl ester resin fine particles are preferably formed from a polymer of ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, or a mixture thereof.

The polyacrylic acid alkyl ester resin fine particles are preferably 5 to 100 parts by weight with respect to 100 parts by weight of the polystyrene resin.
When the weight ratio of the resin fine particles is within the above range, a composite polystyrene resin foam molded article having more excellent mechanical strength, moldability and impact resistance can be provided.
When the resin fine particles are less than 5 parts by weight based on 100 parts by weight of the polystyrene resin, the effect of improving the impact resistance of the obtained composite polystyrene resin foam molded article may not be sufficiently obtained. On the other hand, if the resin fine particle exceeds 100 parts by weight with respect to 100 parts by weight of the polystyrene resin, it is difficult to foam the obtained expandable composite polystyrene resin particles at a high magnification, and the density of the foamed molded product cannot be reduced. There is. More preferable resin fine particles are 10 to 70 parts by weight with respect to 100 parts by weight of the polystyrene resin.
Specific polyacrylic acid alkyl ester resin fine particles are, for example, 5, 10, 15, 20, 25, 30, 50, 70, 75, and 100 parts by weight with respect to 100 parts by weight of the polystyrene resin.
In the present invention, the ratio of the raw material resin and monomer is substantially the same as the ratio of the expanded particles and the expanded molded body.

The dispersed phase of the composite polystyrene resin foamed particles of the present invention has a plurality of polyacrylic acid alkyl ester resin fine particles in the thickness direction in a layered manner when the cell membrane of the composite polystyrene resin foamed particles is viewed in the cross section in the thickness direction. It is an existing structure.
In the present invention, it is considered that the fine particles are dispersed substantially uniformly when viewed in terms of the foam film and the foam film unit in the foam molded article. From this point of view, the distribution state of the fine particles in the dispersed phase is as follows. It is substantially uniform in the foamed molded product.

When the cell phase of the foamed particles is viewed in a cross section in the thickness direction, the dispersed phase has a size in the thickness direction of the dispersed phase (resin fine particle thickness a) and a size in the direction of the cell phase of the dispersed phase (resin fine particle size). It is preferable to have an aspect ratio (b / a) of 7 or more and 60 or less when the length is b).
If the aspect ratio (b / a) is less than 7, the resin fine particles are easily exposed from the bubble film surface, and the retention of the foaming agent gas may be lowered. On the other hand, if the aspect ratio (b / a) exceeds 60, the resin fine particles become too flat, become thin and difficult to suppress the propagation of cracks, and the impact resistance of the foamed molded product may be lowered. A more preferable aspect ratio (b / a) is 10 or more and 60 or less, and a more preferable aspect ratio (b / a) is 20 or more and 50 or less.
Specific b / a is, for example, 10, 15, 20, 25, 30, 35, 45, 50, 55 and 60.
The same applies to the foam molded body, and the thickness a and the length b of the foamed particles are replaced with c and d, respectively.
The aspect ratio and the measuring method thereof will be described in detail in Examples.

In the present invention, the shape of the resin fine particles in the composite polystyrene resin particles before foaming is not particularly limited, and may be, for example, spherical, elliptical spherical, indefinite shape, or the like.
In addition, the shape of the resin fine particles in the cell membrane cross section of the foamed particles after foaming is not particularly limited, and may be, for example, a circle, an ellipse, an indeterminate shape, or the like.

Moreover, it is preferable that the average particle diameter of the resin fine particle in the composite polystyrene resin particle before foaming is 100 to 1000 nm.
When the average particle size of the resin fine particles is less than 100 nm, the impact resistance of the obtained foamed molded product may be insufficient. On the other hand, when the average particle diameter of the resin fine particles exceeds 1000 nm, the dissipation rate of the foaming agent may be increased. A more preferable average particle size of the resin fine particles is 200 to 500 nm.
Specific average particle diameters are, for example, 100, 200, 250, 500, 750, and 1000 nm.

(Composite polystyrene resin particles)
In the present invention, the shape of the composite polystyrene resin particles is not particularly limited, and may be, for example, spherical, elliptical spherical, cylindrical or the like. Preferably, it is spherical.
When the composite polystyrene-based resin particles of the present invention are spherical, the average particle size thereof is then expanded into the mold of the expanded particles obtained by further expanding the expandable composite polystyrene-based resin particles impregnated with the volatile foaming agent. In consideration of filling properties and the like, the thickness is preferably 0.3 to 2.0 mm, more preferably 0.5 to 1.5 mm.
Specific average particle diameters are, for example, 0.3, 0.5, 0.8, 1.0, 1.5, and 2.0 mm.

(Polybutadiene terminated acrylate)
The composite polystyrene resin particles preferably further contain a component derived from polybutadiene terminal acrylate.
Thereby, the polystyrene and the polyacrylic acid ester are made compatible, and the composite polystyrene-type resin foaming molded object which improved the impact resistance further can be provided.

  For the polybutadiene-terminated acrylate, a monomer having a structure in which one or more (meth) acryloyl groups are bonded to a polybutadiene molecule containing 80% or more of 1,2-bonds and 1,4-bonds can be used. This monomer preferably has a structure in which a (meth) acryloyl group is introduced at the polybutadiene molecular end. Specifically, the polybutadiene-terminated acrylate is composed of a polybutadiene molecule containing the following repeating unit (1) having 1,2-bonds and the following repeating unit (2) having 1,4-bonds, and one or both ends of the polybutadiene molecule. It is a monomer having a functional group ((meth) acryloyl group) represented by the following formula (3) at the terminal.

The molar ratio between the units (1) and (2) is preferably (1) / [(1) + (2)] ≧ 0.8. The unit (2) may be a trans structure or a cis structure. Units (1) and (2) can be present in the monomer in various repeating forms such as random, block, and alternating.
In formula (3), R is preferably a hydrogen atom or a lower alkyl group having 1 to 4 carbon atoms. The functional groups of formula (3) are preferably located at both ends of the polybutadiene molecule.
As the polybutadiene-terminated acrylate, for example, trade names BAC-45 and BAC-15 available from Osaka Organic Chemical Industry can be used. In addition, those newly synthesized by the following known methods can also be used.

That is, a method of introducing a (meth) acryl group into a polybutadiene structure by reacting a hydroxyl group-containing polybutadiene with a compound having a (meth) acryl group.
Examples of the above method include (i) a method in which a hydroxyl group of a hydroxyl group-containing polybutadiene and a carboxyl group of a compound having a (meth) acryl group are subjected to a dehydration reaction using a dehydration catalyst such as p-toluenesulfonic acid. ii) A method in which a transesterification reaction between a (meth) acrylic acid ester and a hydroxyl group of polybutadiene is performed using a transesterification catalyst such as a titanium catalyst or a tin catalyst.
Examples of the compound having a (meth) acrylic group include (meth) acrylic acid, methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate, butyl (meth) acrylate, and the like. (Propyl and butyl include structural isomers).

The polybutadiene terminated acrylate preferably has a number average molecular weight in the range of 200 to 10,000. If the number average molecular weight is less than 200, the elasticity of the composite polystyrene resin particles may be lowered. If it exceeds 10,000, it may be difficult to charge and dissolve in the reaction system. A more preferred number average molecular weight is in the range of 2500 to 3000. The number average molecular weight here is a value obtained by measurement with a gel permeation chromatograph.
Specific number average molecular weights are, for example, 200, 1000, 1500, 2000, 2500, 3000, 3500, 5000, and 10,000.

  The polybutadiene-terminated acrylate preferably has a viscosity (25 ° C.) in the range of 500 to 9000 Pa · s. When the viscosity is less than 500 Pa · s, the elasticity of the composite polystyrene resin particles may be lowered. If it exceeds 9000 Pa · s, it may be difficult to charge and dissolve in the reaction system. A more preferable viscosity is in the range of 4000 to 8000 Pa · s. The viscosity here is a value obtained by measuring with a rotary viscometer.

The component derived from the polybutadiene-terminated acrylate is preferably contained in the composite polystyrene resin particles in the range of 0.1 to 3.0 parts by weight with respect to 100 parts by weight of the composite polystyrene resin particles. If the content of this component is less than 0.1 parts by weight, the elasticity of the composite polystyrene resin particles may be lowered. If it exceeds 3.0 parts by weight, it may be difficult to be absorbed by the composite polystyrene resin particles. A more preferred content is in the range of 0.1 to 2.0 parts by weight, particularly in the range of 0.5 to 1.0 parts by weight.
Specific polybutadiene-terminated acrylates are, for example, 0.1, 0.3, 0.5, 0.8, 1.0, 1.5, 2.0 and 3 with respect to 100 parts by weight of the composite polystyrene resin particles. 0.0 part by weight (unit omitted).

(Composite polystyrene resin foam particles)
In the present invention, the composite polystyrene-based resin expanded particles preferably have a bulk density of 0.015 g / cm ³ or more and 0.1 g / cm ³ or less.
When the bulk density of the expanded particles is within the above range, a composite polystyrene resin foam molded article having more excellent mechanical strength, moldability and impact resistance can be provided.
When the bulk density of the expanded particles is less than 0.015 g / cm ³ , the impact resistance of the expanded molded article may be lowered. On the other hand, when the bulk density of the foamed particles exceeds 0.1 g / cm ³ , the foamed molded product becomes large in weight when used as a packaging material or a cushioning material, which may be economically disadvantageous. The bulk density of the preferred foam particles is less 0.018 g / cm ³ or more 0.05 g / cm ^3.
Specific bulk densities are, for example, 0.015, 0.018, 0.02, 0.03, 0.04, 0.05, 0.08, and 0.1.

  In the present invention, the resin fine particles in the cross section of the foam film of the foam particles have a specific flat shape because the polystyrene system that forms a continuous phase in the process of foaming the resin, that is, in the process of stretching the foam film as the foam expands This means that the resin fine particles in the dispersed phase are appropriately stretched with the elongation of the resin. This means that the viscoelasticity of the polystyrene resin forming the continuous phase, that is, the molecular weight needs to be in a specific range. Accordingly, the polystyrene-based resin preferably has a weight average molecular weight (MW) and a ratio of the Z average molecular weight (MZ) to the weight average molecular weight (MW) (MZ / MW) in the above range.

The composite polystyrene resin foamed particles of the present invention are prepared by preliminarily preparing the foamable composite polystyrene resin particles impregnated with a volatile foaming agent to a predetermined bulk density (for example, 0.015 to 0.1 g / cm3) by a known method. It can be manufactured by foaming.
The foamable composite polystyrene resin particles of the present invention, for example, polymerize a monomer mixture after absorbing a monomer mixture containing an alkyl acrylate ester into seed particles made of polystyrene resin in an aqueous medium. Then, a step of dispersing and forming the polyacrylic acid alkyl ester resin fine particles in the seed particles, followed by adding a styrene monomer to the seed particles in which the polyacrylic acid alkyl ester resin fine particles are dispersed and formed in the aqueous medium. After the monomer mixture is absorbed, the monomer mixture may be polymerized to further grow polystyrene resin particles, and to be produced by a step of impregnating a foaming agent after the polymerization or in the middle of the polymerization. it can.

  More specifically, the expandable composite polystyrene resin particle of the present invention is based on 100 parts by weight of seed particles made of polystyrene resin in a dispersion obtained by dispersing seed particles made of polystyrene resin in water. A first polymerization step in which 10 to 90 parts by weight of an acrylic acid alkyl ester monomer is supplied, and this acrylic acid alkyl ester monomer is absorbed and polymerized by seed particles to grow polystyrene resin particles; A second polymerization step in which a styrene monomer is supplied into the dispersion, and this is absorbed and polymerized into seed particles to further grow polystyrene resin particles; a step of impregnating a foaming agent after the polymerization or in the middle of the polymerization Can be manufactured.

  The alkyl acrylate ester monomer used in the first polymerization step and the amount of use thereof and the styrene monomer used in the second polymerization step are (polyacrylic acid alkyl ester resin fine particles) and (polystyrene resin particles). ).

(Seed particles)
The seed particles made of polystyrene resin are not particularly limited and can be produced by a known method. For example, a suspension polymerization method or a method in which a raw material resin is melt-kneaded with an extruder, extruded into a strand shape, and cut with a desired particle diameter can be mentioned. In addition, a part or all of a polystyrene resin-recovered product can be used, and particles obtained by a suspension polymerization method or a cutting method are used as they are, or styrene monomers are added to the particles in an aqueous medium. Particles obtained by impregnation and polymerization may be used.
The particle diameter of the seed particles can be adjusted as appropriate according to the average particle diameter of the composite polystyrene resin particles to be prepared. For example, when preparing composite polystyrene resin particles having an average particle diameter of 1 mm, the average particle diameter is 0.4. It is preferable to use seed particles of about 0.7 mm.
The weight average molecular weight of the seed particles is not particularly limited, but is preferably 150,000 to 700,000, more preferably 200,000 to 500,000.
(Other ingredients)
In addition, additives such as plasticizers, anti-binding agents, bubble regulators, crosslinking agents, fillers, flame retardants, flame retardant aids, lubricants, and colorants are added to the seed particles within the range that does not impair the physical properties. May be.

(Polymerization initiator)
The polymerization initiator used in the above production method is not particularly limited as long as it is conventionally used for the polymerization of styrene monomers. For example, benzoyl peroxide, lauryl peroxide, t-butylperoxy Benzoate, t-butyl peroxy-2-ethylhexanoe, t-butyl peroxide, t-butyl peroxypivalate, t-butyl peroxyisopropyl carbonate, t-butyl peroxyacetate, 2,2-bis (t -Butylperoxy) butane, t-butylperoxy-3,3,5-trimethylhexanoate, di-t-butylperoxyhexahydroterephthalate, 2,2-di-t-butylperoxybutane, di- Organic peroxides such as t-hexyl peroxide and dicumyl peroxide and azobis Sobuchironitoriru, azo compounds such as azo-bis-dimethylvaleronitrile and the like. These may be used alone or in combination, but it is preferable to use a plurality of types of polymerization initiators having a decomposition temperature of 60 to 130 ° C. for obtaining a half-life of 10 hours.

(Suspension stabilizer)
In the above production, a suspension stabilizer may be used in order to stabilize the dispersibility of the styrene monomer droplets and the polystyrene resin seed particles. Such a suspension stabilizer is not particularly limited as long as it is conventionally used for suspension polymerization of a styrene monomer, and examples thereof include water-soluble substances such as polyvinyl alcohol, methyl cellulose, polyacrylamide, and polyvinyl pyrrolidone. And poorly soluble inorganic compounds such as tribasic calcium phosphate and magnesium pyrophosphate.
Moreover, when using a poorly soluble inorganic compound, an anionic surfactant is used together normally.

  Examples of such anionic surfactants include fatty acid soaps, N-acyl amino acids or salts thereof, carboxylates such as alkyl ether carboxylates, alkylbenzene sulfonates, alkyl naphthalene sulfonates, and dialkyl sulfosuccinate esters. Sulfates such as alkyl sulfoacetates, α-olefin sulfonates, higher alcohol sulfates, secondary higher alcohol sulfates, alkyl ether sulfates, polyoxyethylene alkylphenyl ether sulfates, etc. And phosphoric acid ester salts such as alkyl ether phosphoric acid ester salts and alkyl phosphoric acid ester salts.

(Other ingredients)
Addition of plasticizers, anti-binding agents, bubble regulators, cross-linking agents, fillers, flame retardants, flame retardant aids, lubricants, colorants, etc. to the composite polystyrene resin particles within the range that does not impair the physical properties. An agent may be added.
Moreover, powdery metal soaps such as zinc stearate may be applied to the surface of the expandable composite polystyrene resin particles described later. By this coating, it is possible to reduce the bonding between the expanded particles in the pre-expanding step of the expandable polystyrene resin particles.

The composite polystyrene resin particles can contain a plasticizer having a boiling point of more than 200 ° C. under 1 atm in order to maintain good foam moldability even when the pressure of water vapor used during heat foaming is low.
Examples of the plasticizer include glycerin fatty acid esters such as phthalic acid esters, glycerin diacetomonolaurate, glycerin tristearate, and glycerin diacetomonostearate, adipic acid esters such as diisobutyl adipate, and plasticizers such as coconut oil. .
The content of the plasticizer in the composite polystyrene resin particles is less than 2% by weight.

The foamed composite polystyrene resin particles of the present invention are preferably surface-coated with an antistatic agent-containing component.
Examples of the surface coating include a method of applying an antistatic agent to the surface of the composite polystyrene resin particles. Specifically, it is preferable to stir the composite polystyrene resin particles together with the antistatic agent in a stirrer. As the stirrer, a stirrer such as a tumbler mixer or a Redige mixer is used.

  Antistatic agents include, for example, nonionic surfactants such as hydroxyalkylamines, hydroxyalkyl monoetheramines, glycerin fatty acid esters, polyoxyethylene alkyl ethers, and anionic surfactants such as alkylsulfonates and alkylbenzenesulfonates. Agents, cationic surfactants such as tetraalkylammonium salts and trialkylbenzylammonium salts. Nonionic surfactants such as hydroxyalkylamine, hydroxyalkyl monoetheramine, glycerin fatty acid ester, polyoxyethylene alkyl ether and the like can be mentioned.

  Specific examples of such an antistatic agent include, for example, N, N-bis (hydroxyethyl) dodecylamine, N, N-bis (hydroxyethyl) tetradecylamine, and N, N-bis (hydroxyethyl) hexadecylamine. N, N-bis (hydroxyethyl) octadecylamine, N-hydroxyethyl-N- (2-hydroxytetradecyl) amine, N-hydroxyethyl-N- (2-hydroxyhexadecyl) amine, N-hydroxyethyl- N- (2-hydroxyoctadecyl) amine, N-hydroxypropyl-N- (2-hydroxytetradecyl) amine, N-hydroxybutyl-N- (2-hydroxytetradecyl) amine, N-hydroxypentyl-N- ( 2-hydroxytetradecyl) amine, N-hydroxypentyl-N- ( -Hydroxyhexadecyl) amine, N-hydroxypentyl-N- (2-hydroxyoctadecyl) amine, N, N-bis (2-hydroxyethyl) dodecylamine, N, N-bis (2-hydroxyethyl) tetradecylamine N, N-bis (2-hydroxyethyl) hexadecylamine, N, N-bis (2-hydroxyethyl) octadecylamine, glycerol monostearate, glycerol distearate, sodium dodecylbenzenesulfonate, sodium alkylbenzenesulfonate Polyethylene glycol, polyoxyethylene oleyl ether, lauryltrimethylammonium chloride, stearyltrimethylammonium chloride, laurylbetaine, stearylbetaine and the like. These antistatic agents may be used alone or in combination.

The antistatic agent is preferably in the range of 0.5 to 5.0 parts by weight with respect to 100 parts by weight of the composite polystyrene resin particles.
If the coating amount of the antistatic agent is small and less than 0.5 part by weight, sufficient antistatic performance may not be obtained. On the other hand, when the coating amount of the antistatic agent exceeds 5.0 parts by weight, the fusion-bonding property of the foamed molded product may be impaired. A more preferable content is in the range of 0.8 to 2.0 parts by weight, and a further preferable content is in the range of 0.9 to 1.5 parts by weight.
Specific antistatic agents are, for example, 0.5, 0.8, 0.9, 1.0, 1.5, 2.0, and 5.0 with respect to 100 parts by weight of the composite polystyrene resin particles. It is.

(Expandable composite polystyrene resin particles)
The expandable composite polystyrene resin particles of the present invention include composite polystyrene resin particles and a volatile foaming agent, and are produced by impregnating a volatile foaming agent after the polymerization in the second polymerization step or during the polymerization. be able to.
If the temperature at which the volatile foaming agent is impregnated is low, the impregnation takes time, and the production efficiency of the expandable polystyrene resin particles may be lowered. On the other hand, if it is high, a large amount of coalescence between the expandable polystyrene resin particles may occur, so 70 to 130 ° C is preferable, and 80 to 120 ° C is more preferable.

(Volatile foaming agent)
The volatile foaming agent is not particularly limited as long as it is conventionally used for foaming polystyrene resins. For example, carbon such as isobutane, n-butane, n-pentane, isopentane, neopentane, and cyclopentane. Examples include volatile foaming agents such as aliphatic hydrocarbons of several tens or less, and in particular, butane-based foaming agents and pentane-based foaming agents are preferable, and volatile foaming agents containing pentane as a main component (for example, 50% by weight or more). Particularly preferred. In addition, pentane can be expected to act as a plasticizer.

The content of the volatile foaming agent in the foamable composite polystyrene resin particles is usually in the range of 2 to 10% by weight, preferably in the range of 3 to 10% by weight, and particularly preferably in the range of 3 to 8% by weight.
When the content of the volatile foaming agent is small, for example, less than 2% by weight, a low-density composite polystyrene resin foam molding may not be obtained from the foamable composite polystyrene resin particles, and at the time of in-mold foam molding Since the effect of increasing the secondary foaming power cannot be obtained, the appearance of the composite polystyrene resin foamed molded product may be deteriorated. On the other hand, if the content of the volatile foaming agent is large, for example, if it exceeds 10% by weight, the time required for the cooling process in the production process of the composite polystyrene resin foamed product using the composite polystyrene resin foam particles becomes long, and the productivity is increased. May decrease.

(Foaming aid)
The foamed composite polystyrene resin particles of the present invention can contain a foaming aid together with a volatile foaming agent.
The foaming aid is not particularly limited as long as it is conventionally used for foaming polystyrene resins. For example, aromatic organic compounds such as styrene, toluene, ethylbenzene, xylene, cyclohexane, methylcyclohexane, etc. Examples thereof include solvents having a boiling point of 200 ° C. or less under 1 atm, such as cycloaliphatic hydrocarbons, ethyl acetate, and butyl acetate.

The content of the foaming aid in the composite polystyrene resin particles is usually in the range of 0.2 to 2.5% by weight, and preferably in the range of 0.3 to 2% by weight.
When the content of the foaming aid is small, for example, less than 0.2% by weight, the plasticizing effect of the polystyrene resin may not be exhibited. On the other hand, if the content of the foaming auxiliary agent is large and exceeds 2.5% by weight, shrinkage or melting occurs in the composite polystyrene resin foam molded product obtained by foam molding of the foamable composite polystyrene resin particles. The appearance may be deteriorated, or the time required for the cooling step in the production process of the composite polystyrene resin foam molded article using the composite polystyrene resin foam particles may be long.

Next, the foamable composite polystyrene resin particles impregnated with the volatile foaming agent are pre-foamed to a predetermined bulk density (for example, 0.015 to 0.1 g / cm ³ ) by a known method, whereby The composite polystyrene resin expanded particles of the invention can be obtained.
In the pre-foaming, air may be introduced simultaneously with steam when foaming as necessary.

The pre-foaming conditions may be appropriately selected depending on the resin particles to be used and desired physical properties. For example, the pressure is about 0.01 to 0.04 MPa, more preferably 0.01 to 0.03 MPa, and still more preferably 0.015 to 0.02 MPa. Specific examples include 0.01 MPa, 0.015 MPa, 0.02 MPa, 0.03 MPa, and 0.04 MPa.
Further, the time is about 30 to 240 seconds, more preferably 60 to 180 seconds, and still more preferably 90 to 150 seconds. Specific examples include 30 seconds, 60 seconds, 90 seconds, 120 seconds, 150 seconds, 180 seconds, and 240 seconds.

The composite polystyrene resin expanded particles of the present invention preferably have a bulk density of 0.015 g / cm ³ or more and 0.1 g / cm ³ or less.
When the bulk density of the expanded particles is within the above range, a composite polystyrene resin foam molded article having more excellent mechanical strength, moldability and impact resistance can be provided.
When the bulk density of the expanded particles is less than 0.015 g / cm ³ , the impact resistance of the expanded molded article may be lowered. On the other hand, when the bulk density of the foamed particles exceeds 0.1 g / cm ³ , the foamed molded product becomes large in weight when used as a packaging material or a cushioning material, which may be economically disadvantageous. The bulk density of the preferred foam particles is less 0.018 g / cm ³ or more 0.05 g / cm ^3.
Specific bulk densities are, for example, 0.015, 0.018, 0.02, 0.03, 0.04, 0.05, 0.08, and 0.1 (unit omitted).

  Accordingly, the composite polystyrene resin foam particles of the present invention include foamable composite polystyrene resin particles containing 2 to 10% by weight of a volatile foaming agent mainly composed of pentane with respect to the foamable composite polystyrene resin particles. A pre-foamed one is preferred.

(Composite polystyrene resin foam molding)
The composite polystyrene resin foam molded article of the present invention can be obtained by treating the composite polystyrene resin foam particles of the present invention by a known method, and the composite polystyrene resin foam particles of the present invention are incorporated in a molding machine. It is preferable to obtain it by fusing and integrating in a mold. Specifically, the composite polystyrene resin foamed particles of the present invention are filled in a mold of a foam molding machine and heated again, so that the foamed particles are thermally fused together while foaming to form a foamed molded product. Is obtained.

The conditions for foam molding may be appropriately selected depending on the resin particles to be used, desired physical properties, and the like. For example, the pressure is about 0.06 to 0.10 MPa, more preferably 0.07 to 0.09 MPa, and still more preferably 0.075 to 0.08 MPa. Specific examples include 0.06 MPa, 0.07 MPa, 0.075 MPa, 0.08 MPa, 0.09 MPa, and 0.10 MPa.
The heating time is about 20 to 60 seconds, more preferably 25 to 50 seconds, and further preferably 30 to 40 seconds. Specific examples include 20 seconds, 25 seconds, 30 seconds, 40 seconds, 50 seconds, 60 seconds, and the like.

The composite polystyrene-based resin foamed molded article of the present invention preferably has a falling ball impact value of 11 cm or more according to JIS K7221, a bending break point displacement amount according to JIS K7221-1 of 12 mm or more, and a crack amount according to JIS Z0235 of less than 50%. .
The falling ball impact value, the bending break point displacement amount, and the crack amount are more preferably 13 cm or more, 14 mm or more and less than 45%, respectively.
These measurement methods will be described in detail in Examples.

  Hereinafter, specific examples of the present invention will be described by way of examples. However, the following examples are merely illustrative of the present invention, and the present invention is not limited to the following examples. In the following, “part” and “%” are based on weight unless otherwise specified.

In the following Examples and Comparative Examples, the average particle diameter of the composite polystyrene resin particles, the bulk density and the bulk multiple of the composite polystyrene resin foam particles, the aspect ratio of the polyacrylic acid alkyl ester resin fine particles in the foamed particle bubble membrane cross section, Molecular weight of composite polystyrene resin foamed particles, aspect ratio, molecular weight, falling ball impact value, displacement at bending break point, cracking amount and molding of polyacrylic acid alkyl ester resin fine particles in the cell membrane cross section of foam molded product with 50 times the bulk size The properties were measured and evaluated according to the following measurement methods and evaluation criteria.
Further, the surface resistivity of the foamed molded product was measured by the following method to evaluate the antistatic property.

<Average particle diameter of composite polystyrene resin particles>
The average particle diameter is a value expressed by D50.
Specifically, using a low-tap type sieve shaker (manufactured by Iida Seisakusho), sieve openings are 4.00 mm, 3.35 mm, 2.80 mm, 2.36 mm, 2.00 mm, 1.70 mm, 1.40 mm. 1.18mm, 1.00mm, 0.85mm, 0.71mm, 0.60mm, 0.50mm, 0.425mm, 0.355mm, 0.300mm, 0.250mm, 0.212mm and 0.180mm JIS About 50 g of the sample is classified with a standard sieve for 10 minutes, and the sample weight on the sieve mesh is measured. A cumulative weight distribution curve is created from the obtained results, and the particle diameter (median diameter) at which the cumulative weight is 50% is defined as the average particle diameter.

<Bulk density and bulk multiple of composite polystyrene resin expanded particles>
The bulk density and bulk multiple of the composite polystyrene resin foamed particles are measured as follows.
The weight (a) of about 5 g of expanded particles is weighed at the second decimal place, and the measured expanded particles are put into a 500 cm ³ graduated cylinder having a minimum memory unit of 5 cm ³ . Next, a pressing tool, which is a round resin plate slightly smaller than the diameter of the graduated cylinder, with a rod-shaped resin plate having a width of about 1.5 cm and a length of about 30 cm standing upright and fixed at the center thereof. Apply the volume (b) of the foamed particles.
From the weight (a) of the obtained expanded particles and the volume (b) of the expanded particles, the bulk density of the expanded particles (g / cm ³ ) = (a) / (b)
Bulk multiple = reciprocal of bulk density = (b) / (a)
Ask for.

<Aspect Ratio of Polyacrylic Acid Alkyl Ester Resin Fine Particle in Cross Section of Foamed Particle Bubble Film>
Slice the foamed particles, cut out a section from the vicinity of the center of the foamed particles, embed the section in an epoxy resin, and use the ultra-microtome (LEICA ULTRACUT UCT, manufactured by Leica Microsystems) for the epoxy resin containing the foamed particle section. Process to make ultrathin sections. Ruthenium tetroxide is used as the staining agent.
Next, the ultrathin section is photographed with a transmission electron microscope (manufactured by Hitachi High-Technologies Corporation, H-7600) at a magnification of 5000 times (in some cases, 10,000 times or 20000 times). The photographed photograph was enlarged and printed on an A4 sheet so as to form one image, and 30 particles were selected in order from the longest polyacrylic acid alkyl ester resin fine particles that can be confirmed at both ends in the range of 150 mm × 200 mm in the image. Then, the thickness a (dimension in the bubble film thickness direction) and the length b (dimension in the bubble film surface direction) of these particles are measured, and the aspect ratio (b / a) is calculated. Each dimension is the longest part. That is, the distance between both ends of the particle that can be confirmed even when the particle is curved is defined as b, and the distance between the line connecting the both ends of the particle and the longest portion in the vertical direction is defined as a. The total average aspect ratio is calculated from the obtained aspect ratio, and is defined as the aspect ratio of the polyacrylic acid alkyl ester resin fine particles in the composite polystyrene resin foamed particles (see FIG. 2).

<Aspect Ratio of Polyacrylic Acid Alkyl Ester Resin Fine Particle in Cross Section of Foam Molded Cell Bubble Film>
The skin is removed from the foamed molded product, a section is cut out from the vicinity of the center of the surface from which the skin has been removed, the section is embedded in an epoxy resin, and the epoxy resin containing the section is made into an ultramicrotome (Leica Microsystems, LEICA). Ultrathin sections are processed by using ULTRACUT UCT). Ruthenium tetroxide is used as the staining agent.
Next, the ultrathin section is photographed with a transmission electron microscope (manufactured by Hitachi High-Technologies Corporation, H-7600) at a magnification of 5000 times (in some cases, 10,000 times or 20000 times). The photographed photograph was enlarged and printed on an A4 sheet so as to form one image, and 30 particles were selected in order from the longest polyacrylic acid alkyl ester resin fine particles that can be confirmed at both ends in the range of 150 mm × 200 mm in the image. Then, the thickness c (dimension in the bubble film thickness direction) and the length d (dimension in the bubble film surface direction) of these particles are measured, and the aspect ratio (d / c) is calculated. Each dimension is the longest part. That is, the distance between both ends of the particle that can be confirmed even when the particle is curved is d, and the distance between the line connecting the both ends of the particle and the longest portion in the vertical direction is c. The total average aspect ratio is calculated from the obtained aspect ratio and is defined as the aspect ratio of the polyacrylic acid alkyl ester resin fine particles in the composite polystyrene resin foam molded article.

<Molecular weight of composite polystyrene resin expanded particles>
The molecular weight means an average molecular weight in terms of polystyrene (PS) measured using a gel permeation chromatography (GPC) method (internal standard method).
Divide it into two so as to pass through the center of the expanded particles, dissolve 30 mg ± 3 mg of the divided expanded particles in 4 mL of chloroform containing 0.1 wt% BHT (butylhydroxytoluene), and filter through a non-aqueous 0.45 μm chromatodisc. The obtained filtrate is measured using a chromatograph under the following conditions. The average molecular weight of the sample is obtained from a standard polystyrene calibration curve that has been measured and prepared in advance.
Measuring apparatus: Tosoh HPLC (pump DP-8020, autosampler AS-8020, detector UV-8020, RI-8020)
Column: 2 GPC K-806L (φ8.0 × 300 mm, manufactured by Shodex) Guard column: 1 GPC K-LG (φ8.0 × 50 mm, manufactured by Shodex) Test number: 2
Measurement conditions: column temperature (40 ° C.), mobile phase (chloroform), mobile phase flow rate (1.2 mL / min), pump temperature (room temperature), detector temperature (room temperature), measurement time (25 minutes), detection wavelength ( UV254nm), injection volume (50μL)
Standard polystyrene for calibration curve: manufactured by Showa Denko KK, trade name “Shodex”, weight average molecular weight (Mw): 5,620,000, 3,120,000, 1,250,000, 442,000, 131,000, 54,000, 20,000, 7,590, 3,450, 1,320
The ratio MZ / MW is determined from the obtained weight average molecular weight MW and Z average molecular weight MZ.

<Molecular weight of composite polystyrene resin foam molding>
The molecular weight means an average molecular weight in terms of polystyrene (PS) measured using a gel permeation chromatography (GPC) method (internal standard method).
A sample of 30 mg ± 3 mg was taken from the foam molded article, this sample was dissolved in 4 mL of chloroform containing 0.1 wt% BHT (butylhydroxytoluene), filtered through a non-aqueous 0.45 μm chromatodisc, and the obtained filtrate was Measure using a chromatograph under the following conditions. The average molecular weight of the sample is obtained from a standard polystyrene calibration curve that has been measured and prepared in advance.
Measuring apparatus: Tosoh HPLC (pump DP-8020, autosampler AS-8020, detector UV-8020, RI-8020)
Column: 2 GPC K-806L (φ8.0 × 300 mm, manufactured by Shodex) Guard column: 1 GPC K-LG (φ8.0 × 50 mm, manufactured by Shodex) Test number: 2
Measurement conditions: column temperature (40 ° C.), mobile phase (chloroform), mobile phase flow rate (1.2 mL / min), pump temperature (room temperature), detector temperature (room temperature), measurement time (25 minutes), detection wavelength ( UV254 nm), injection amount: 50 μL
Standard polystyrene for calibration curve: manufactured by Showa Denko KK, trade name “Shodex”, weight average molecular weight (Mw): 5,620,000, 3,120,000, 1,250,000, 442,000, 131,000, 54,000, 20,000, 7,590, 3,450, 1,320
The ratio MZ / MW is determined from the obtained weight average molecular weight MW and Z average molecular weight MZ.

<Falling ball impact value of foam molding>
The falling ball impact strength is measured in accordance with the method described in JIS K7211: 1976 “General Rules for Hard Plastic Drop Weight Impact Test Method”.
The obtained foamed molded product having a bulk multiple of 50 times is dried at a temperature of 50 ° C. for 1 day, and then a 40 mm × 215 mm × 20 mm (thickness) test piece (six skins on both sides) is cut out from the foamed molded product.
Next, both ends of the test piece are fixed with clamps so that the distance between the fulcrums is 150 mm, and a hard ball having a weight of 321 g is dropped from a predetermined height onto the center of the test piece to check whether the test piece is broken or not. Observe.
The test piece was tested by changing the falling height (test height) of the hard sphere at 5 cm intervals from the lowest height at which all five specimens were destroyed to the highest height at which all were not destroyed, and the falling ball impact value (cm), ie 50% The fracture height is calculated by the following formula.

H50 = Hi + d [Σ (i · ni) /N±0.5]
The symbols in the formula mean the following:
H50: 50% fracture height (cm)
Hi: Test height (cm) when the height level (i) is 0, and the height at which the test piece is expected to break d: Height interval (cm) when the test height is raised or lowered
i: Height level when Hi is 0 and increases or decreases by 1 (i =... -3, -2, -1, 0, 1, 2, 3,...)
ni: Number of specimens destroyed (or not destroyed) at each level, whichever data is used (if the number is the same, either may be used)
N: The total number of specimens that were destroyed (or not destroyed) (N = Σni), whichever data is used (in the case of the same number, either may be used)
± 0.5: Use a negative number when using destroyed data, and a positive number when using data that was not destroyed

The obtained falling ball impact value is evaluated according to the following criteria. The larger the falling ball impact value, the greater the impact resistance of the foamed molded product.
◎ (excellent): Falling ball impact value is 13 cm or more. ○ (Good): Falling ball impact value is in the range of 11 cm to less than 13 cm. △ (possible): Falling ball impact value is in the range of 9 cm to less than 11 cm. Less than 9cm

<Displacement of bending break point of foamed molded product>
The bending strength is measured in accordance with the method described in JIS K7222-1: 2006 “Rigid foamed plastics—Bending test—Part 1: Bending test”.
The obtained foam molded article having a bulk multiple of 50 times is dried at a temperature of 50 ° C. for 1 day, and then a test piece of 25 mm × 130 mm × 20 mm (thickness) is cut out from the foam molded article.
Next, press wedge 5R and support base 5R are mounted on the universal testing machine (Orientec, Tensilon (registered trademark) UCT-10T) as the tip jig, and the test piece is set at a distance of 100 mm between the fulcrums, and the compression speed is 10 mm. Bending test is performed under the conditions of / min. In this test, the fracture detection sensitivity was set to 0.5%, and when the decrease exceeded the set value of 0.5% compared to the previous load sampling point, the previous sampling point was changed to the bending fracture point displacement ( mm).

The obtained bending fracture point displacement is evaluated according to the following criteria. It shows that the flexibility of a foaming molding is so large that a bending fracture point displacement amount is large.
◎ (excellent): Bending fracture point displacement is 14 mm or more. ○ (good): Bending fracture point displacement is in the range of 12 mm to less than 14 mm. △ (possible): Bending fracture point displacement is in the range of 10 mm to less than 12 mm. ): Bending fracture displacement is less than 10 mm

<Crack amount of foamed molded product>
The amount of cracks is measured according to the method described in JIS Z0235: 1976 “Packaging Buffer Material—Evaluation Test Method”.
The obtained foam molded article having a bulk multiple of 50 times is dried at a temperature of 50 ° C. for 1 day, and then a test piece of 75 mm × 300 mm × 50 mm (thickness) is cut out from the foam molded article.
Next, the test piece was lightly fixed on the center of the base of the shock absorber for impact shock absorber (manufactured by Yoshida Seiki Co., Ltd., CST-320S) so that it does not move when impacted, as shown in FIG. The weight of 13.5 kg was dropped from a height of 60 cm so as to cover the entire lengthwise direction of the test piece and the entire width direction, and the cracks of the test piece generated at this time were observed. The amount of cracks (%) is calculated by the following formula.

S = H / T × 100
The symbols in the formula mean the following:
S: Crack amount (%)
H: Crack size (mm)
T: Test piece thickness (mm)
The amount of cracks obtained is evaluated according to the following criteria. It shows that the impact resistance of a foaming molding is so large that the amount of cracks is small.
◎ (excellent): crack amount less than 45% ○ (good): crack amount range from 45% to less than 50% △ (possible): crack amount range from 50% to less than 55% × (impossible): crack amount 55% or more

<Moldability of foam molding>
After pre-foaming, an expanded bead automatic molding machine (Sekisui) equipped with a molding die having a rectangular parallelepiped cavity with an internal dimension of 300 mm x 400 mm x 50 mm (thickness) is obtained by aging the foamed particles 50 times in bulk at room temperature for 24 hours. KACE MFG Co., Ltd., ACE-3SP) is filled into the cavity, and after heating and cooling under the following conditions, the foamed molded product is taken out from the mold and the appearance of the foamed molded product is evaluated.
(Molding conditions) Mold heating: 5 seconds
Heating on the other hand: 10 seconds
Reverse one-side heating: 5 seconds
Double-sided heating: 20 seconds
Water cooling: 10 seconds
Set steam pressure: 0.06, 0.07, 0.08 MPa

◎ (excellent): There is no expanded particle with the surface of the molded body sufficiently stretched and melted (there is no gap between the expanded particles, the surface of the molded body is very smooth, and the appearance of the molded body is very good)
○ (good): The gap between the expanded particles is very small, the surface of the molded product is almost smooth, and the appearance of the molded product is good. △ (Yes): The expanded surface of the molded product is insufficiently stretched or there are expanded particles whose surface is melted. , There are innumerable gaps on the surface of the molded body, and the appearance of the molded body is poor (impact resistance is not affected)
X (impossible): The surface of the molded body is not stretched or the molded body is contracted to such an extent that impact resistance is affected or impact resistance evaluation is difficult.

<Antistatic property>
The surface resistivity is measured according to the method described in JIS K6911: 1995 “General Test Method for Thermosetting Plastics”.
The obtained foamed molded article having a bulk multiple of 50 times is dried at a temperature of 50 ° C. for 1 day, and then 10 test pieces of 100 mm × 100 mm × original thickness (10 mm or less) are cut out from the same foamed molded article.
Next, using a digital ultrahigh resistance / microammeter and a resiliency chamber (Advantest Co., Ltd., R8340 and R12702A), an electrode is crimped to the sample piece with a load of about 30 N, and a voltage of 500 V is applied for 1 minute. After charging, the resistance value of the sample piece is measured, and the surface resistivity is calculated by the following formula.

ρs = π (D + d) / (D−d) × Rs
The symbols in the formula mean the following:
ρs: Surface resistivity (MΩ)
D: Inner diameter (cm) of the annular electrode on the surface
d: outer diameter of inner circle of surface electrode (cm)
Rs: Surface resistance (MΩ)
The obtained surface resistivity (average value of 10 test pieces) is evaluated according to the following criteria.
○ (With antistatic property): Surface resistivity is 1 × 10 ¹² Ω or less × (No antistatic property): Surface resistivity exceeds 1 × 10 ¹² Ω

Example 1
(Manufacture of seed (nuclear PS) particles)
40 kg of water, 100 g of tribasic calcium phosphate as a suspension stabilizer and 2.0 g of sodium dodecylbenzenesulfonate as an anionic surfactant are fed into a polymerization vessel equipped with a stirrer with an internal volume of 100 liters, and 40 kg of styrene monomer and polymerization are started while stirring. After adding 96.0 g of benzoyl peroxide and 28.0 g of t-butylperoxybenzoate as agents, the temperature was raised to 90 ° C. to polymerize. And it hold | maintained at this temperature for 6 hours, and also, after heating up to 125 degreeC, it cooled after 2 hours and obtained the polystyrene-type resin seed particle (A).
The polystyrene resin seed particles (A) are sieved, and the polystyrene resin seed particles (B-1) having a particle diameter of 0.5 to 0.71 mm (average particle diameter D50 = 0.66 mm) as the seed particles are used. Polystyrene resin seed particles (B-2) of 0.71 to 1.18 mm (average particle diameter D50 = 0.99 mm) were obtained.

(Manufacture of composite polystyrene resin particles)
Next, in a polymerization vessel equipped with a stirrer having an internal volume of 5 liters, 2000 g of water, 500 g of the polystyrene resin seed particles (B-1), 10.0 g of magnesium pyrophosphate as a suspension stabilizer, and dodecylbenzene as an anionic surfactant Sodium sulfonate 0.4g was supplied and it heated up at 75 degreeC, stirring.
Next, 200 g of butyl acrylate in which 0.6 g of dicumyl peroxide was dissolved as a polymerization initiator was supplied to the 5 liter polymerization vessel, and then absorbed into the seed particles, held at 75 ° C. for 60 minutes, and then 130 The temperature was raised to ° C. and held for 2 hours.
Thereafter, the temperature is lowered to 75 ° C., and 200 g of styrene monomer in which 5.2 g of benzoyl peroxide and 0.75 g of t-butylperoxybenzoate are dissolved as a polymerization initiator is supplied to the 5 liter polymerization vessel, and then seed particles. The styrene monomer was absorbed therein and kept at 75 ° C. for 60 minutes.
Subsequently, while the temperature of the reaction liquid was raised from 75 ° C. to 120 ° C. over 180 minutes, 1100 g of styrene monomer was supplied in a certain amount into the polymerization vessel from 75 ° C. to 115 ° C. over 160 minutes. Subsequently, after heating up to 120 degreeC, it heated up further to 140 degreeC, and it cooled after 2 hour passage, and obtained the composite polystyrene-type resin particle (C).

(Production of expandable composite polystyrene resin particles)
Next, 2200 g of water, 1800 g of composite polystyrene resin particles (C), 7.2 g of magnesium pyrophosphate and 0.36 g of sodium dodecylbenzenesulfonate were supplied as a suspension stabilizer to a polymerization vessel equipped with a stirrer having an internal volume of 5 liters. The temperature was raised to 100 ° C. with stirring. Next, 144 g of n-pentane / isopentane = 75/25 to 85/15 pentane (gas type a: product name pentane, manufactured by Cosmo Oil Co., Ltd.) was injected into the 5 liter polymerization vessel as a foaming agent and held for 3 hours. Then, it cooled to 30 degrees C or less, and took out from the inside of a polymerization container. Subsequently, it was dried and left in a thermostatic chamber at 13 ° C. for 7 days to obtain expandable composite polystyrene resin particles.

(Manufacture of composite polystyrene resin foam particles)
Subsequently, 1500 g of expandable composite polystyrene resin particles were coated with a surface treatment agent consisting of 1.2 g of zinc stearate, 1.2 g of hydroxystearic acid triglyceride and 0.75 g of polyethylene glycol (MW = 300). After the treatment, the foamable composite polystyrene resin particles are put into a normal pressure pre-foaming machine preheated with steam, and steam is introduced at a setting of about 0.03 MPa while stirring, and the volume is 50 times in about 2-3 minutes. It was pre-foamed to a multiple.

(Manufacture of foam moldings)
Automatic foam bead equipped with a molding die having a rectangular parallelepiped cavity of 300 mm × 400 mm × 50 mm (thickness) inside a composite polystyrene resin expanded particle with a bulk ratio of 50 times aged for 24 hours after pre-expanding It filled in the cavity of the molding machine (Sekisui Machinery Co., Ltd. make, ACE-3SP), and after heating and cooling with the following conditions, the foaming molding was taken out from the metal mold | die and the foaming molding was obtained.
(Molding conditions) Mold heating: 5 seconds
Heating on the other hand: 10 seconds
Reverse one-side heating: 5 seconds
Double-sided heating: 20 seconds
Water cooling: 10 seconds
Set steam pressure: 0.06, 0.07, 0.08 MPa
The obtained composite polystyrene resin particles, composite polystyrene resin foam particles and foamed molded article were measured and evaluated by the above methods. The results are shown in Tables 1 and 2.
FIG. 1 shows a scanning electron microscope (SEM) photograph (a) of a cross section of the composite polystyrene-based resin foamed particles and a transmission electron microscope (TEM) photograph (b) of the internal cell membrane.

Example 2
In the production of composite polystyrene resin particles, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene were used in the same manner as in Example 1 except that 2-ethylhexyl acrylate was used instead of butyl acrylate. System resin foamed particles and foamed molded products were obtained and measured and evaluated. The results are shown in Tables 1 and 2.

Example 3
In the production of composite polystyrene resin particles, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene resin were used in the same manner as in Example 1 except that ethyl acrylate was used instead of butyl acrylate. Foamed particles and a foamed molded article were obtained and measured and evaluated. The results are shown in Tables 1 and 2.

Example 4
(Manufacture of composite polystyrene resin particles)
In a polymerization vessel with an internal volume of 5 liters equipped with a stirrer, 2000 g of water, 600 g of the polystyrene resin seed particles (B-1), 10.0 g of magnesium pyrophosphate as a suspension stabilizer and sodium dodecylbenzenesulfonate as an anionic surfactant 0.4 g was supplied and the temperature was raised to 75 ° C. while stirring.
Next, 400 g of butyl acrylate in which 1.2 g of dicumyl peroxide was dissolved as a polymerization initiator was supplied to the 5 liter polymerization vessel, and then absorbed into the seed particles, held at 75 ° C. for 60 minutes, and then 130 The temperature was raised to ° C. and held for 2 hours.
Thereafter, the temperature is lowered to 75 ° C., and 200 g of styrene monomer in which 4.0 g of benzoyl peroxide and 0.7 g of t-butylperoxybenzoate are dissolved as a polymerization initiator is supplied to the 5 liter polymerization vessel. And absorbed at 75 ° C. for 60 minutes.
Subsequently, the reaction solution was heated from 75 ° C. to 120 ° C. over 180 minutes, and 800 g of styrene monomer was supplied from 75 ° C. to 115 ° C. into the polymerization vessel in a fixed amount over 160 minutes. After raising the temperature to 120 ° C., the temperature was further raised to 140 ° C. and cooled after 2 hours to obtain composite polystyrene resin particles (C).
In the same manner as in Example 1, the foamable composite polystyrene resin particles, the composite polystyrene resin foam particles, and the foam molded article were obtained, measured, and evaluated. The results are shown in Tables 1 and 2.

Example 5
In the production of composite polystyrene resin particles, the polystyrene resin seed particles (B-2) were used instead of the polystyrene resin seed particles (B-1), and 4.0 g of benzoyl peroxide was changed to 3.0 g. Except that, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene resin foam particles and foamed molded articles were obtained, measured and evaluated in the same manner as in Example 4. The results are shown in Tables 1 and 2.

Example 6
In the production of composite polystyrene resin particles, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene series are the same as in Example 1 except that 5.2 g of benzoyl peroxide is changed to 6.5 g. Resin foam particles and a foam-molded article were obtained and measured and evaluated. The results are shown in Tables 1 and 2.

Example 7
In the production of composite polystyrene resin particles, 200 g of butyl acrylate in which 0.2 g of divinylbenzene was dissolved in addition to 0.6 g of dicumyl peroxide as a polymerization initiator was supplied to a 5-liter polymerization vessel, and benzoyl peroxide was added. Except having changed 2g to 7.15g, it carried out similarly to Example 1, and obtained the composite polystyrene-type resin particle, the expandable composite polystyrene-type resin particle, the composite polystyrene-type resin foam particle, and the foaming molding, and measured and evaluated. . The results are shown in Tables 1 and 2.

Example 8
In the production of composite polystyrene resin particles, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene resin were used in the same manner as in Example 1 except that 5.2 g of benzoyl peroxide was changed to 2.6 g. Resin foam particles and a foam-molded article were obtained and measured and evaluated. The results are shown in Tables 1 and 2.

Example 9
In the production of expandable composite polystyrene resin particles, n-butane / isopentane = 75/25 to 85/15 pentane (gas species a: product name pentane manufactured by Cosmo Oil Co., Ltd.) is used as a blowing agent. i-butane = 60/40 to 70/30 butane (Gas species b: Cosmo Oil Co., Ltd., product name Cosmobutane Silver) was used in the same manner as in Example 1 to obtain composite polystyrene resin particles and foam Porous polystyrene resin particles, composite polystyrene resin foam particles, and foamed molded articles were obtained and measured and evaluated. The results are shown in Tables 1 and 2.

Example 10
Example 4 except that 400 g of butyl acrylate in which 1.0 g of divinylbenzene was dissolved in addition to 1.2 g of dicumyl peroxide as a polymerization initiator was supplied to a 5-liter polymerization vessel in the production of composite polystyrene resin particles. In the same manner as above, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene resin foam particles, and foamed molded articles were obtained and measured and evaluated. The results are shown in Tables 1 and 2.

Example 11
In the production of composite polystyrene resin particles, a composite polystyrene system was used in the same manner as in Example 1 except that 6.5 g of t-butylperoxy-2-ethylhexanoate was used instead of 5.2 g of benzoyl peroxide. Resin particles, expandable composite polystyrene resin particles, composite polystyrene resin foam particles and a foamed molded article were obtained, and measured and evaluated. The results are shown in Tables 1 and 2.

Example 12
In the production of composite polystyrene resin particles, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene resin were used in the same manner as in Example 1 except that 5.2 g of benzoyl peroxide was changed to 9.1 g. Foamed particles and a foamed molded article were obtained and measured and evaluated. The results are shown in Tables 1 and 2.

Comparative Example 1
(Manufacture of polystyrene resin particles)
In a polymerization vessel equipped with a stirrer having an internal volume of 5 liters, 2000 g of water, 500 g of the above polystyrene resin seed particles (B-1), 8.0 g of magnesium pyrophosphate as a suspension stabilizer and sodium dodecylbenzenesulfonate as an anionic surfactant 0.4 g was supplied and the temperature was raised to 75 ° C. while stirring.
Next, 100 g of styrene monomer in which 6.0 g of benzoyl peroxide and 0.75 g of t-butylperoxybenzoate were dissolved as a polymerization initiator was supplied to the 5 liter polymerization vessel, and the styrene monomer was absorbed into the seed particles. And kept at 75 ° C. for 30 minutes.
Subsequently, while the temperature of the reaction solution was raised from 75 ° C. to 120 ° C. over 180 minutes, 1400 g of styrene monomer was supplied from 75 ° C. to 115 ° C. into the polymerization vessel in a fixed amount over 160 minutes. Subsequently, after heating up to 120 degreeC, it heated up at 130 degreeC, and it cooled after 2 hours passage, and obtained the polystyrene-type resin particle (C).

(Manufacture of expandable polystyrene resin particles)
Next, 2200 g of water, 1800 g of polystyrene resin particles (C), 7.2 g of magnesium pyrophosphate and 0.36 g of sodium dodecylbenzenesulfonate were supplied as a suspension stabilizer to a polymerization vessel equipped with a stirrer having an internal volume of 5 liters. The temperature was raised to 100 ° C. with stirring. Next, 126 g of butane of n-butane / i-butane = 60/40 to 70/30 (gas type b: product name Cosmobutane Silver, manufactured by Cosmo Oil Co., Ltd.) as a blowing agent was injected into the 5-liter polymerization vessel. After holding for 3 hours, it was cooled to 30 ° C. or lower and taken out from the polymerization vessel. Subsequently, it was dried and left in a thermostatic chamber at 13 ° C. for 7 days to obtain expandable polystyrene resin particles.
The polystyrene resin foam particles and the foam molded article were produced according to the production of the composite polystyrene resin foam particles and the foam molded article of Example 1, and a foam molded article was obtained, measured and evaluated. The results are shown in Tables 1 and 2.

Comparative Example 2
(Manufacture of rubber-modified polystyrene resin particles)
A styrene-butadiene block copolymer having a butadiene component of 60% by weight was dissolved in a styrene monomer to obtain a 14.5% by weight solution. To 100 parts by weight of this solution, 5 parts by weight of ethylbenzene, 0.05 part by weight of 1,1-bis (t-butylperoxy) cyclohexane and 0.05 part by weight of t-dodecyl mercaptan were added to obtain a polymerization raw material liquid.
Subsequently, the obtained polymerization raw material liquid was supplied to a polymerization vessel equipped with a stirrer having an internal volume of 5 liters, and polymerization was performed under the following conditions. Polymerization temperature is 105 ° C. for 3 hours, temperature is raised to 130 ° C. for 2 hours, temperature is further raised and polymerization is conducted at 145 ° C. for 1 hour. Then, ethylbenzene was removed to obtain a polymer.
The obtained polymer was supplied to an extruder, kneaded, a strand was drawn from the pores of the die, immediately cooled with water, and then cut into pellets having a diameter of about 1 mm and a length of about 1.5 mm. The content of the butadiene component in the obtained pellet-like rubber-modified polystyrene resin particles was 10.5% by weight as calculated from the mass balance of styrene-butadiene block copolymer and styrene.

(Manufacture of expandable rubber-modified polystyrene resin particles)
Next, 2200 g of water, 1800 g of rubber-modified polystyrene resin particles, 7.2 g of magnesium pyrophosphate and 0.36 g of sodium dodecylbenzenesulfonate are supplied as a suspension stabilizer to another polymerization vessel equipped with a stirrer having an internal volume of 5 liters. The temperature was raised to 125 ° C. with stirring. Next, 144 g of n-pentane / isopentane = 75/25 to 85/15 pentane (gas type a: product name pentane, manufactured by Cosmo Oil Co., Ltd.) as a blowing agent is injected into the 5 liter polymerization vessel and held for 5 hours. Thus, expandable rubber-modified polystyrene resin particles were obtained. After the holding, the foamed rubber-modified polystyrene resin particles were taken out from the polymerization container after being cooled to 30 ° C. or lower, dried, and left in a thermostatic chamber at 13 ° C. for 5 days.

(Manufacture of rubber-modified polystyrene resin expanded particles and expanded molded products)
Production of the rubber-modified polystyrene resin foamed particles and the foamed molded product was carried out in accordance with the production of the composite polystyrene resin foamed particles and foamed molded product of Example 1, to obtain, measure and evaluate the foamed molded product. The results are shown in Tables 1 and 2.

Example 13
(Manufacture of composite polystyrene resin particles)
In a polymerization vessel equipped with a stirrer having an internal volume of 5 liters, 2000 g of water, 500 g of the polystyrene resin particles (B-1) obtained in Example 1 as seed particles, 10.0 g of magnesium pyrophosphate as a suspension stabilizer and an anion interface 1.6 g of sodium dodecylbenzenesulfonate as an activator was supplied and heated to 75 ° C. while stirring.
Next, 200 g of butyl acrylate in which 0.6 g of dicumyl peroxide and 10 g of polybutadiene terminal acrylate (manufactured by Osaka Organic Chemical Industry Co., Ltd., product name: BAC-45) are dissolved as a polymerization initiator is supplied to the 5 liter polymerization vessel. Then, butyl acrylate was absorbed in the seed particles, held at 75 ° C. for 60 minutes, then heated to 130 ° C. and held for 2 hours.
Thereafter, the mixture was cooled to 75 ° C., and 200 g of a styrene monomer in which 7.0 g of benzoyl peroxide and 0.75 g of t-butylperoxybenzoate were dissolved as a polymerization initiator was supplied to the 5 liter polymerization vessel. A styrene monomer was absorbed in the particles, and polymerized by holding at 75 ° C. for 60 minutes to obtain a reaction solution.
Subsequently, while the temperature of the reaction solution was raised from 75 ° C. to 120 ° C. over 180 minutes, 1100 g of styrene monomer was supplied into the polymerization vessel in a certain amount in 160 minutes. Subsequently, after heating up to 120 degreeC, it heated up to 140 degreeC and cooled after 2 hours progress, and the composite polystyrene-type resin particle (C) was obtained.

(Production of expandable composite polystyrene resin particles)
Next, in another polymerization vessel equipped with a stirrer having an internal volume of 5 liters, 2200 g of water, 1800 g of composite polystyrene resin particles (C), 7.2 g of magnesium pyrophosphate as suspension stabilizer and 1.44 g of sodium dodecylbenzenesulfonate were added. The temperature was raised to 125 ° C. while feeding and stirring. Next, 144 g of pentane of n-pentane / i-pentane = 75/25 to 85/15 (gas type a: product name pentane, manufactured by Cosmo Oil Co., Ltd.) as a blowing agent was injected into the 5 liter polymerization vessel for 3 hours. After being held, it was cooled to 30 ° C. or lower and taken out from the polymerization vessel. Subsequently, it was dried and left in a thermostatic chamber at 13 ° C. for 5 days to obtain expandable composite polystyrene resin particles.

(Manufacture of composite polystyrene resin expanded particles and expanded molded products)
In the same manner as in Example 1, pre-expanded particles and a foam-molded product were obtained from the obtained expandable particles, and measured and evaluated. The results are shown in Tables 3 and 4.

Example 14
In the production of the composite polystyrene resin particles, the composite polystyrene resin particles, the expandable composite polystyrene resin particles, the composite polystyrene resin foam particles, and the composite polystyrene resin particles, except that 10 g of the polybutadiene terminal acrylate is 16 g, and A foamed molded product was obtained and measured and evaluated. The results are shown in Tables 3 and 4.

Example 15
In the production of composite polystyrene resin particles, except that 10 g of polybutadiene terminal acrylate is changed to 20 g, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene resin foam particles and A foamed molded product was obtained and measured and evaluated. The results are shown in Tables 3 and 4.

Example 16
In the production of the composite polystyrene resin particles, the composite polystyrene resin particles, the expandable composite polystyrene resin particles, the composite polystyrene resin foam particles, and the composite polystyrene resin particles, except that 10 g of the polybutadiene terminal acrylate is 40 g, and A foamed molded product was obtained and measured and evaluated. The results are shown in Tables 3 and 4.

Example 17
(Coating of expandable particles)
The foamable composite polystyrene resin particles 1500 g were charged into a tumbler mixer having an internal volume of 20 L. Next, 1.2 g of zinc stearate, 1.2 g of hydroxystearic acid triglyceride, 0.75 g of glycerol monostearate, and polyoxyethylene hydroxyalkylamine (trade name Antistar 80FS, manufactured by Tanaka Chemical Laboratory) as an antistatic agent 15 0.0 g was added sequentially and stirred for 15 minutes. Next, 0.75 g of polyethylene glycol (MW = 300) and 0.45 g of diisobutyl adipate were added and stirred for 15 minutes to coat the surface treatment agent on the surface of the expandable polystyrene resin particles.
Except for the above, in the same manner as in Example 13, composite polystyrene resin particles, expandable composite polystyrene resin particles, composite polystyrene resin foam particles, and foamed molded articles were obtained and measured and evaluated. The results are shown in Tables 3 and 4.
Moreover, the scanning electron microscope (SEM) photograph of the foamed particle cross section of Examples 13-15 is respectively shown in FIGS. 4-6, and the transmission electron microscope (TEM) photograph of the foam molded body cross section of Example 14 is shown in FIG. Show.

Example 18
(Preparation of glass transport container)
In the production of the composite polystyrene-based resin expanded particles, the composite polystyrene-based resin particles, the expandable composite polystyrene-based resin particles, and the composite polystyrene-based resin expanded particles are obtained in the same manner as in Example 1 except that the bulk multiple is 40 times. Obtained.
After pre-foaming, the composite polystyrene resin foamed particles with a bulk ratio of 40 times aged at room temperature for 24 hours are filled into the cavities of a foamed bead automatic molding machine equipped with a molding die having a cavity of the following shape, and steam heating and After cooling, the foamed molded product was removed from the mold to obtain a glass transport container.
(Main unit) Outer dimensions 1580mm x 980mm x 119mm
Internal dimensions 1369mm x 785mm x 69mm
(Lid) Outer dimensions 1580mm x 980mm x 90mm
45mm thickness

(Short edge drop test)
20 sheets of 1357 mm × 774 mm × 1.48 mm (thickness) 60-inch SOF-attached panels were placed in the obtained glass transport container. The total weight of the panel was 80 kg.
The container for transporting glass in a packed state was placed on a pallet (1600 mm × 1000 mm × 150 mm (thickness)), and this was dropped from a height of 15 cm by a short ridge.
The state of the glass transport container and panel is evaluated according to the following criteria.
○ (Good): Panel and container are not damaged and can be used in a returnable manner. △ (Yes): Panel is not damaged, but the container is damaged and can be used if it is one-way. Damaged and unusable The result of the short ridge drop test in Example 18 was ○.

Example 19
Except having used the composite polystyrene-type resin particle of Example 13, it carried out similarly to Example 18, and obtained the composite polystyrene-type resin expanded particle and the container for glass conveyance, and measured and evaluated.
The result of the short ridge drop test in Example 19 was ○.

Comparative Example 3
Except having used the polystyrene-type resin particle of the comparative example 1, it carried out similarly to Example 18, and obtained the polystyrene-type resin foam particle and the container for glass conveyance, and measured and evaluated.
The result of the short ridge drop test in Comparative Example 3 was x.

  The container for glass conveyance produced using the foaming molding manufactured in each Example has physical properties as shown in Table 2 and Table 4, and the short ridge drop test of Examples 18 and 19 and Comparative Example 3 From the results, it can be seen that it is useful compared to conventional containers.

a Thickness of polyacrylic acid alkyl ester resin fine particles b Length of polyacrylic acid alkyl ester resin fine particles in the bubble film surface direction g Polyacrylic acid alkyl ester resin fine particles t Bubble film thickness 1 Test piece 2 Weight 3 Crack H Crack size T Test piece thickness

Claims (10)

A glass transport container,
The glass transport container has a plurality of bubbles and a bubble film partitioning them, and a polystyrene resin in which the bubble film forms a continuous phase, and a polyacryl dispersed in the continuous phase to form a dispersed phase An acid alkyl ester resin fine particle, and the polystyrene resin is composed of a composite polystyrene resin foam molded body in which the polyacrylic acid alkyl ester resin fine particle is combined,
A container for transporting glass, wherein the dispersed phase is present in a plurality of layers in the direction of the thickness of the bubble film in the cross section of the bubble film of the composite polystyrene resin foam molded article.   The dispersed phase has dimensions in the cell membrane thickness direction (thickness of polyacrylic acid alkyl ester resin fine particles) and cell membrane surface direction dimensions (polyacrylic acid alkyl ester) in the cell membrane cross section of the composite polystyrene resin foam molded article. The container for glass conveyance of Claim 1 which has an aspect-ratio (d / c) of 7 or more and 60 or less, when c and d are respectively the length of a system resin fine particle).   The polystyrene-based resin has a weight average molecular weight (MW) of 200,000 to 350,000 and a ratio of a Z average molecular weight (MZ) to a weight average molecular weight (MW) (MZ / MW) of 2 to 4. The container for glass conveyance as described in 2.   The container for glass conveyance according to claim 2 or 3, wherein the aspect ratio (d / c) is 20 or more and 50 or less.   The glass according to any one of claims 1 to 4, wherein the polyacrylic acid alkyl ester resin fine particles are formed from a polymer of ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, or a mixture thereof. Transport container.   The glass transport container according to any one of claims 1 to 5, wherein the polyacrylic acid alkyl ester resin fine particles are 5 to 100 parts by weight with respect to 100 parts by weight of the polystyrene resin.   The container for glass conveyance according to any one of claims 1 to 6, wherein the composite polystyrene-based resin foam molded article further includes a component derived from a polybutadiene terminal acrylate. The container for glass conveyance according to any one of claims 1 to 7, wherein the composite polystyrene-based resin foam molded article has a bulk density of 0.015 g / cm ³ or more and 0.1 g / cm ³ or less.   The composite polystyrene resin foam molded article has a falling ball impact value according to JIS K7221 of 11 cm or more, a bending break point displacement amount according to JIS K7221-1 of 12 mm or more, and a crack amount according to JIS Z0235 of less than 50%. The container for glass conveyance as described in any one of these.   The container for glass conveyance as described in any one of Claims 1-9 in which the said composite polystyrene-type resin foaming molding is foam-molded the composite polystyrene-type resin foaming particle surface-coated with the antistatic agent containing component.