KR100829345B1 - Expandable polystyrene type resin particles, a method for preparing the same, and expanded articles using the same resin particles - Google Patents

Abstract

The present invention relates to an expandable styrene resin particle containing charcoal, a method for manufacturing the same, and a foamed molded article made of the resin particle, wherein the resin particle comprises a styrene resin, charcoal, and a blowing agent. The expandable styrene resin particles including the charcoal of the present invention have the advantage of excellent thermal insulation even at low density, and have the advantage of expressing the charcoal function beneficial to the human body, such as a filtration effect and a humidity control effect.

Suspension, Charcoal, Foam, Styrene, Copolymer, Density, Thermal Conductivity, Insulation

Description

Expandable polystyrene type resin particles, a method for preparing the same, and expanded articles using the same resin particles}

The present invention relates to an expandable styrene resin particle containing charcoal, a method of manufacturing the same, and an expanded molded article made of the resin particle. More specifically, an expandable styrene resin including charcoal having excellent thermal insulation even at low density. The present invention relates to a resin particle, a method for producing the same, and a foam molded article made of the resin particle.

Expandable polystyrene (EPS) generally contains a polymerization initiator and a blowing agent such as a hydrocarbon gas such as pentane and butane or a halogenated hydrocarbon compound in a styrene monomer, thereby suspending polymerization with water to produce 0.2-3.0 mm spherical particles ( Beads, bead) foamed styrene resin particles are obtained. The obtained expanded styrene resin particles (beads) are washed, dried, and sieved to form a foam molded article.

Method for producing a molded foam is as follows. The expanded styrene resin particles impregnated with the blowing agent in the styrene resin are heated to a softening point or more by steam or the like to prepare particulate pre-expanded particles having independent bubbles therein, and are aged for a predetermined time in a aging storage tank. The foamed particles thus produced have a white color. The pre-expanded particles may be further heated by steam or the like in a closed mold capable of heating the inside of the preliminary foamed particles to be fused to each other by volume expansion of the foamed particles to prepare EPS foamed products. The foam molded article is a resource-saving material in which 98% of the volume is air and the remaining 2% is resin. Foamed molded products using EPS have excellent buffering, waterproofing, warmth and insulation properties, and are used as packaging materials for household appliances, agricultural and marine products boxes, aquaculture riches, and building insulation materials. When used as a heat insulator, depending on the thickness and width of the building wall, the molded part can be easily cut and used with heated copper wire.

EPS foam molded articles used for thermal insulation generally have the best thermal insulation at a specific gravity of about 30 g / l, but are preferably used at lower specific gravity to save material and space. However, as the specific gravity decreases, the thermal conductivity of the EPS foamed molded article increases, so that the insulation does not satisfy the requirements of the insulation 'ga' group standard (KSM 3808).

It is known that the thermal conductivity of foams can be reduced by the incorporation of heatless materials such as graphite, carbon black, metal oxides, metal powders or pigments. In WO 00/43442, a polystyrene resin was melted in an extruder together with aluminum platelets, mixed with pentane, and granulated by a strand granulator to prepare expanded styrene resin particles. Such is a rather complicated process and economically disadvantageous compared to suspension polymerization. EP 620246 describes a method of coating particulate heatless materials, in particular carbon black or graphite, on the surface of prefoamed EPS foam or on the surface of EPS particles that have not yet been foamed. However, distributing the heatless material on the surface of the EPS particles may inhibit fusion during molding and may also peel off from the surface of the molding. In both cases, the heatless material is not evenly distributed inside the polystyrene particles.

WO 98/51734 describes expandable styrene particles having excellent thermal conductivity containing graphite particles by suspension polymerization of styrene in an aqueous phase in the presence of graphite particles. The particle size of graphite is 1-50 micrometers. However, graphite has a disadvantage of human hazards such as causing dusting when inhaling dust over a long period of time.

As a result of long researches by the present inventors to compensate for the disadvantages of the prior art, it has been provided a foamed styrene resin particles including char.

Charcoal has various beneficial effects such as filtration effect, humidity control effect, negative ion generation effect, far-infrared ray heating effect, odor removal effect, harmful electromagnetic wave blocking effect, and is widely used in various fields such as bedding, household goods, beauty, decoration and props. It is also used for food.

Particularly, if charcoal is included in the EPS foam molded article used for thermal insulation, it is only natural that it is expected to have several effects at the same time.

Accordingly, an object of the present invention is to provide a foamed styrene resin particle containing charcoal having excellent thermal insulation even at low density, and a method of manufacturing the same and a foamed molded article made of the resin particle.

Another object of the present invention is to provide an expandable styrene resin particle containing charcoal capable of expressing a charcoal function beneficial to the human body, such as a filtering effect and a humidity control effect, a method of manufacturing the same, and a foam molded article made of the resin particle. .

In order to achieve the above object, the present invention is a) 100 parts by weight of a styrene resin; b) 0.1 to 15 parts by weight of charcoal; And c) provides a foamable styrene resin particles comprising a char, comprising a blowing agent.

The present invention also comprises the step of suspending the styrene-based monomer in the water phase in the presence of char, and the timing of addition of the blowing agent is before the suspension polymerization, during the suspension polymerization or after completion of suspension polymerization, effervescent comprising char Provided are methods for producing styrene resin particles.

The present invention also provides a method for producing expandable styrene resin particles comprising char, comprising the step of suspending styrene resin particles in an aqueous phase and impregnating the suspended styrene resin particles with charcoal and a blowing agent.

The present invention also comprises the steps of a) melt-mixing styrene resin particles with charcoal in an extruder; b) granulating the styrenic resin melt mixture; c) suspending granulated styrenic resin particles in an aqueous phase, and impregnating the suspended styrene resin particles with a blowing agent; provides a method for producing expandable styrene resin particles including charcoal.

The present invention also provides a foam molded article made of expandable styrene resin particles containing the char.

Hereinafter, the present invention will be described in more detail.

Expandable styrene resin particles comprising char according to the present invention includes a) 100 parts by weight of styrene resin; b) 0.1 to 15 parts by weight of charcoal; And c) a blowing agent.

The styrene-based resin is a polymer matrix of the expanded styrene resin particles of the present invention and includes a homopolystyrene resin as well as a copolymer of styrene and a monomer copolymerizable with styrene. Examples of the monomer copolymerizable with styrene may include ethylenically unsaturated comonomers, and more specifically, alkyl styrene alpha-methylstyrene, alpha-ethylstyrene, and alpha- such as ethyl styrene, dimethyl styrene, and para-methyl styrene. Alkyl acrylate divinylbenzene acrylonitrile butadiene isobutyl, such as halogenated styrene methylacrylate, alkyl methacrylate, and methyl methacrylate, such as alpha-alkyl styrene chlorostyrene and bromostyrene, such as propyl styrene and alpha-butyl styrene Ethylene vinyl isoprene or a mixture thereof.

In the styrene copolymer, the content of the repeating unit of the monomer (comonomer) copolymerized with styrene is preferably 30% by weight or less based on the entire styrene copolymer.

As charcoal included in the expandable styrene resin particles of the present invention, charcoal which is commonly used may be used, and examples thereof include, but are not limited to, gum charcoal, white charcoal, activated charcoal, and the like. The content of the charcoal is determined according to the desired thermal conductivity of the expandable styrenic resin, preferably 0.1 to 15 parts by weight, more preferably 0.1 to 10 parts by weight, most preferably 100 parts by weight of the expanded styrene resin. 1 to 5 parts by weight. If the content of charcoal is less than 0.1 part by weight, the effect of improving thermal conductivity is insignificant, and if it exceeds 15 parts by weight, the effect as a heat-free material is no longer improved, and it is economically disadvantageous without special advantages, and there is a problem in dispersion stability.

As the blowing agent included in the expandable styrenic resin particles of the present invention, a blowing agent conventionally used to prepare expandable styrene resin particles may be used, and it is a gas or liquid at room temperature and atmospheric pressure, and is a volatile organic compound which does not dissolve resin particles. Any compound can be used without limitation. Non-limiting examples may include cyclic aliphatic hydrocarbon halogenated hydrocarbon compounds such as aliphatic hydrocarbons such as propane, isobutane, normal butane, isopentane, normalpentane, cyclohexane, and cyclohexane, or mixtures thereof. The content of the blowing agent is preferably 3 to 15 parts by weight, more preferably 3 to 10 parts by weight based on 100 parts by weight of the expandable styrene resin. If the content of the blowing agent is less than 3 parts by weight, the foaming effect is insignificant, and if it exceeds 15 parts by weight, it is only economically disadvantageous without improving the special foaming effect.

The average particle diameter of the expandable styrene resin particles of the present invention is preferably 0.2 to 3 mm.

The first method for producing expandable styrenic resin particles comprising char according to the present invention comprises the step of suspending polymerization of a styrene monomer in an aqueous phase in the presence of char, and the addition time of the blowing agent is before suspension polymerization. In progress or after completion of suspension polymerization. The addition before the suspension polymerization means that the blowing agent is added before the initiator is added to the suspension containing the styrene monomer.

Styrene-based monomers include styrene monomers as well as comonomers copolymerizable with styrene monomers. The comonomer copolymerizable with the styrene monomer is the same as the comonomer which can be copolymerized to form the expandable styrene resin particles.

The addition amount of the comonomer copolymerizable with a styrene monomer is 30 weight% or less with respect to the whole styrene monomer.

Charcoal and blowing agent are the same as charcoal and blowing agent which are components of the expandable styrene resin particles including the present invention charcoal.

This step can be carried out by a conventional suspension polymerization, the addition time of the blowing agent is before the suspension polymerization, during the suspension polymerization or after completion of suspension polymerization

A polymerization initiator commonly used to carry out this step may be added, and preferably, it is dissolved in a styrene monomer and an initiator having a half life of 10 hours at 50 to 120 ° C. Specifically, organic peroxides such as cumenehydroxy peroxide, zcumyl peroxide, t-butyl peroxy 2-ethylhexanoate, t-butyl peroxy benzoate, benzoyl peroxide, lauroyl peroxide, and azobis isoiso Azo compounds, such as butyl nitrile, or a mixture thereof can be illustrated. The total amount of the polymerization initiator is preferably 0.01 to 2 parts by weight based on 100 parts by weight of the styrene monomer.

Suspension stabilizers commonly used to carry out this step may be added, and hydrophilic polymers such as polyvinyl alcohol, methyl cellulose, polyvinyl pyrrolidone, and poorly water-soluble inorganic substances such as tricalcium phosphate and magnesium pyrophosphoric acid Salts, or mixtures thereof.

In order to perform this step, a surfactant commonly used with the suspension stabilizer may be used in combination, and an anionic surfactant such as sodium alkyl sulfonate or sodium dodecyl benzene sulfonate may be used in combination when a poorly water-soluble inorganic salt is used as the suspension stabilizer. can do.

The amount of the suspension stabilizer is preferably used in an amount of 0.01 to 5 parts by weight based on 100 parts by weight of the styrene monomer, and in the case of using a poorly water-soluble inorganic salt and an anionic surfactant together, the water-soluble inorganic material is hardly contained in 100 parts by weight of the styrene monomer. It is preferable to use the salt at 0.05 to 3 parts by weight and the anionic surfactant at 0.0001 to 0.5 part by weight.

In order to perform this step, a flame retardant such as hexabromocyclododecane, a flame retardant such as 2,3-dimethyl 2,3-diphenyl butane, a cell regulator such as polyethylene wax and silica, a plasticizer, a chain during polymerization of the monomer Additives commonly used for the production of expandable styrene resin particles such as a transfer agent can be added.

In addition, foaming styrene resin particles prepared in advance to perform this step may be recycled and added, and the recycled resin particles to be added are preferably 10 parts by weight or less based on 100 parts by weight of the styrene monomer.

Process temperature and pressure of this step is the temperature and pressure of the conventional suspension polymerization, it is determined according to the boiling point of the reaction solvent, the reaction rate, for example, the process temperature is 90 to 130 ℃. The reaction time is not particularly limited as long as the reaction can be sufficiently performed.

A second method for producing expandable styrenic resin particles comprising char according to the present invention comprises the steps of suspending the styrenic resin particles in an aqueous phase and impregnating the suspended styrene resin particles with charcoal and a blowing agent.

The styrene resin particles suspended in the water phase are the same as the styrene resin particles which are the matrix resin particles of the expandable styrene resin particles of the present invention. Therefore, the homopolystyrene resin, as well as a copolymer of styrene and a monomer copolymerizable with styrene, and in the styrene copolymer, the content of the repeating unit of the monomer (comonomer) copolymerized with styrene is preferred for the entire styrene copolymer Preferably 30% by weight or less.

Styrene-based resin particles are styrene and, if necessary, a comonomer of 30% by weight or less is polymerized by a conventional suspension polymerization process, for example, 50% to 100%, and more specifically, 70% to 100% by polymerization. It may be styrene resin particles.

Flame retardants such as hexabromocyclododecane, flame retardants such as 2,3-dimethyl 2,3-diphenyl butane, cell regulators such as polyethylene wax and silica, plasticizers, chain transfer agents, etc. Additives used in the production of conventional expanded styrene resin particles are added, and the styrene resin obtained by polymerizing 70% to 100% at a conversion rate is suspended in an aqueous phase containing a suspension stabilizer. The obtained suspension is impregnated with charcoal and a blowing agent to produce expanded styrene resin particles.

The step of suspending the styrenic resin particles of this step in an aqueous phase and impregnating the suspended styrene resin particles with charcoal and a blowing agent can be carried out in a conventional manner.

A third method for producing expandable styrenic resin particles comprising charcoal according to the present invention comprises the steps of: a) melt mixing styrene resin particles with charcoal in an extruder; b) granulating the styrenic resin melt mixture; c) suspending the granulated styrene resin particles in the water phase and impregnating the suspended styrene resin particles with a blowing agent.

As the styrene resin particles, the same ones as the styrene resin particles of the second method may be used.

a) Melting and mixing the styrene resin particles with charcoal in an extruder may be carried out in a conventional manner, for example, styrene resin particles, charcoal and flame retardants such as hexabromocyclododecane, if necessary, 2 A flame retardant aid such as, 3-dimethyl 2,3-diphenyl butane, a cell regulator such as polyethylene wax and silica, and a plasticizer may be carried out together by melt mixing in an extruder.

b) Granulating the styrenic resin melt mixture may be carried out in a conventional granulation process, for example using a conventional strand granulation apparatus.

c) Suspending the granulated styrenic resin particles in an aqueous phase and impregnating the suspended styrene resin particles with a blowing agent may be carried out by conventional suspension and impregnation processes.

The suspension of expandable styrenic resin particles obtained by the above methods is made into particles having a water content of, for example, 0.3 wt% or less through a conventional dehydration and drying process. The prepared resin particles may be coated with a surface coating agent, and examples of the surface coating agent are conventionally used for preparing expandable styrenic resin particles, for example, glycidyl tristearate, glycidyl mono stearate, zinc Stearates, antistatic agents and the like.

The foaming process of the expandable styrenic resin particles including the charcoal of the present invention for producing a molding according to the present invention can be carried out in a conventional foaming process, for example, it can be carried out using steam, hot air, hot water and the like. have.

Hereinafter, the present invention will be described in more detail with reference to the following examples, but the scope of the present invention is not limited to the examples.

Example 1

Add 10 kg of styrene monomer to the pre-melting tank 1, add 600 g of charcoal (4 parts by weight relative to 15 kg of the total monomers added to the preliminary sea baths 1 and 2) while stirring at 200 rpm, and then add 15 g of polyethylene wax and maintain the mixture for 60 minutes. After dissolving, the mixture was allowed to stand at room temperature and cooled.

In pre-dissolution tank 2, 75 g of benzoyl peroxide (BPO), 8 g of t-butyl peroxy benzoate, and 45 g of zucyl peroxide as a polymerization initiator, 3.75 g of divinylbenzene (DVB) as a crosslinking agent, and 5 kg of styrene monomer were added thereto. After stirring for 30 minutes to dissolve, the solution made in the pre-dissolution tank 1 was poured and stirred for another 30 minutes.

Separately, 15 kg of pure water was added to a 40 L pressure vessel, 25 g of tricalcium phosphate and 5 g of sodium dodecyl benzene sulfonate were added as an anionic surfactant to prepare a suspension, and the solution made in the predissolution bath was poured and stirred at 300 rpm for 30 minutes. Thereafter, the polymerization was carried out until the polymerization rate reached 70% while maintaining the temperature of the reactor at 90 ° C.

Thereafter, 1200 g of pentane was introduced at a rate of 40 g / min while the pressure resistant polymerization tank was sealed and then heated to 110 ° C. After the addition was completed and the temperature reached 110 ℃ was maintained for 2 hours, then cooled to 45 ℃ to obtain expanded styrene resin particles.

After the obtained resin particles were dehydrated, the fluidized bed was dried so that the moisture on the surface of the particles was 0.3% or less, and the particles were sorted by particle size. Among them, a polymer resin having a particle size of 0.9 mm to 1.0 mm was placed in a mixer, and 500 ppm polyethylene glycol, 2000 ppm glycidyl tristearate, and 1000 ppm zinc stearate were added to the polymerization resin, and the mixture was stirred for 20 minutes. .

The foamed styrene resin particles thus obtained were foamed and molded at 60 times magnification, and then thermal conductivity was measured by the KSL 9016 measuring method. The thermal conductivity was 0.0319 W / mK.

Example 2

Styrene Polymer Manufacturing Steps

10 kg of styrene monomer was added to the pre-dissolution tank 1, and 15 g of polyethylene wax was added thereto while stirring at 200 rpm. The temperature was raised to 60 ° C. and maintained for 60 minutes to dissolve the additives, and the mixture was allowed to stand at room temperature and cooled.

In pre-dissolution tank 2, 75 g of benzoyl peroxide (BPO), 8 g of t-butyl peroxy benzoate, and 45 g of zucyl peroxide as a polymerization initiator, 3.75 g of divinylbenzene (DVB) as a crosslinking agent, and 5 kg of styrene monomer were added thereto. After stirring for 30 minutes to dissolve, the solution made in the pre-dissolution tank 1 was poured and stirred for another 30 minutes.

Separately, 15 kg of pure water was added to a 40 L pressure vessel, 25 g of tricalcium phosphate and 5 g of sodium dodecyl benzene sulfonate were added as an anionic surfactant to prepare a suspension, and the solution made in the predissolution bath was poured and stirred at 300 rpm for 30 minutes.

Thereafter, the temperature of the reactor was maintained at 90 ° C. and the polymerization was carried out until the polymerization rate became 70%. After the reaction at 125 ° C. for 1 hour, the reaction mixture was cooled and then discharged, dehydrated, and dried to obtain a polystyrene polymer.

Containing charcoal Expanded styrene  Resin Particle Manufacturing Step

The styrene polymers obtained were selected by particle size.

15 kg of polymer having a particle size of 0.9 mm to 1.0 mm was placed in a 40 L pressure vessel and 15 kg of pure water, 600 g of charcoal, 1200 g of pentane, 75 g of toluene, 25 g of tricalcium phosphate, and 5 g of sodium dodecyl benzene sulfonate as an anionic surfactant. After the pressure-resistant polymerization tank was sealed and stirred at 300 rpm for 30 minutes. The reactor was then heated to 120 ° C. After reaching 120 ° C., it was maintained for 2 hours, and then cooled to 45 ° C. to obtain expanded styrene resin particles.

After the obtained resin particles were dehydrated, the fluidized bed was dried so that the moisture on the surface of the particles became 0.3% or less. The resulting expanded styrene resin particles were added to the polymerization resin with 500 ppm polyethylene glycol, 2000 ppm glycidyl tristearate and 1000 ppm zinc stearate, followed by stirring for 20 minutes.

The foamed styrene resin particles thus obtained were foamed and molded at 60 times magnification, and then thermal conductivity was measured by the KSL 9016 measuring method. The thermal conductivity was 0.0320 W / mK.

Example 3

Styrene polymer manufacturing step comprising char

15 kg of the styrene polymer obtained in the step of preparing the styrene polymer of Example 2 and 600 g of charcoal were stirred with a stirrer and then granulated in a Twin extruder to obtain a styrene polymer particle including char having an average diameter of 1.2 mm.

blowing agent Impregnation  step

15 kg of styrene polymer particles containing the obtained charcoal were charged with 15 kg of pure water in a 40 L pressure reactor, 1200 g of pentane, 25 g of tricalcium phosphate, and 5 g of dodecyl benzene sulfonate as anionic surfactant were added, and then the pressure resistant tank was sealed. Stirred at 300 rpm for min. The reactor was then heated to 120 ° C. After reaching 120 ° C., it was maintained for 2 hours, and then cooled to 45 ° C. to obtain expanded styrene resin particles.

After the obtained expanded styrene resin particles were dehydrated, the fluidized bed was dried so that the moisture on the surface of the particles became 0.3% or less. The resulting expanded styrene resin particles were added to the polymerization resin with 500 ppm polyethylene glycol, 2000 ppm glycidyl tristearate and 1000 ppm zinc stearate, followed by stirring for 20 minutes.

The foamed styrene resin particles thus obtained were foamed and molded at 60 times magnification, and then thermal conductivity was measured by the KSL 9016 measuring method. The thermal conductivity was 0.0319 W / mK.

[Comparative Example]

A foamable styrene resin particle was obtained by the same method as Example 1 except not using charcoal. After foaming and molding the obtained expanded styrene polymer at 60 times magnification, the thermal conductivity was measured by the KS L9016 measuring method. The thermal conductivity was 0.034 W / mK.

As described in the above Examples and Comparative Examples, it was confirmed that the thermal conductivity of the expanded styrene resin particles including the charcoal according to the present invention was significantly reduced and the thermal insulation was remarkably improved.

Therefore, the expandable styrene resin particles including the charcoal of the present invention have the advantage of excellent thermal insulation even at low density, and have the advantage of expressing the function of charcoal beneficial to the human body.

Claims (9)

delete delete delete delete delete delete Suspending the styrenic resin particles in the water phase, and the step of impregnating the suspended styrene resin particles with a charcoal and a foaming agent, foamed styrene resin containing 100 parts by weight of styrene-based resin, 0.1 to 15 parts by weight of charcoal and blowing agent A method for producing expandable styrene resin particles comprising char, wherein the particles are obtained. a) melt-mixing styrene resin particles with charcoal in an extruder; b) granulating the styrenic resin melt mixture; c) suspending the granulated styrene resin particles in an aqueous phase and impregnating the suspended styrene resin particles with a blowing agent; Including, 100 parts by weight of the styrenic resin, 0.1 to 15 parts by weight of charcoal and foaming styrene resin particles comprising a blowing agent, characterized in that the method for producing expandable styrene resin particles comprising a char. delete