KR101484615B1 - Method for manufacturing styrene-form with excellent insulation and non-deformation - Google Patents
Method for manufacturing styrene-form with excellent insulation and non-deformation Download PDFInfo
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- KR101484615B1 KR101484615B1 KR20130052662A KR20130052662A KR101484615B1 KR 101484615 B1 KR101484615 B1 KR 101484615B1 KR 20130052662 A KR20130052662 A KR 20130052662A KR 20130052662 A KR20130052662 A KR 20130052662A KR 101484615 B1 KR101484615 B1 KR 101484615B1
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- 238000009413 insulation Methods 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 238000000034 method Methods 0.000 title claims description 7
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000006260 foam Substances 0.000 claims abstract description 34
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 33
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 24
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims abstract description 21
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000003063 flame retardant Substances 0.000 claims abstract description 12
- 229910002804 graphite Inorganic materials 0.000 claims description 21
- 239000010439 graphite Substances 0.000 claims description 21
- DEIGXXQKDWULML-UHFFFAOYSA-N 1,2,5,6,9,10-hexabromocyclododecane Chemical compound BrC1CCC(Br)C(Br)CCC(Br)C(Br)CCC1Br DEIGXXQKDWULML-UHFFFAOYSA-N 0.000 claims description 16
- 239000004088 foaming agent Substances 0.000 claims description 13
- 229910021383 artificial graphite Inorganic materials 0.000 claims description 9
- 239000004794 expanded polystyrene Substances 0.000 claims description 7
- 239000004795 extruded polystyrene foam Substances 0.000 claims description 7
- 229920006327 polystyrene foam Polymers 0.000 claims description 7
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 claims description 6
- BHNZEZWIUMJCGF-UHFFFAOYSA-N 1-chloro-1,1-difluoroethane Chemical compound CC(F)(F)Cl BHNZEZWIUMJCGF-UHFFFAOYSA-N 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 229920005989 resin Polymers 0.000 claims description 5
- 239000011347 resin Substances 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000000155 melt Substances 0.000 claims description 4
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000001273 butane Substances 0.000 claims description 3
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 3
- 229910021382 natural graphite Inorganic materials 0.000 claims description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 239000000454 talc Substances 0.000 claims description 2
- 229910052623 talc Inorganic materials 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims 1
- 150000007513 acids Chemical class 0.000 claims 1
- 238000005469 granulation Methods 0.000 claims 1
- 230000003179 granulation Effects 0.000 claims 1
- 229920005990 polystyrene resin Polymers 0.000 abstract description 16
- 239000002667 nucleating agent Substances 0.000 abstract description 8
- 230000000052 comparative effect Effects 0.000 description 17
- 239000002245 particle Substances 0.000 description 13
- 239000004793 Polystyrene Substances 0.000 description 10
- 229920002223 polystyrene Polymers 0.000 description 10
- 239000006229 carbon black Substances 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 239000004604 Blowing Agent Substances 0.000 description 4
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 4
- 229910052794 bromium Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- -1 that is Inorganic materials 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 3
- 229920006248 expandable polystyrene Polymers 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000011324 bead Substances 0.000 description 2
- IADKAKQBSKWITE-UHFFFAOYSA-N bromocyclododecane Chemical compound BrC1CCCCCCCCCCC1 IADKAKQBSKWITE-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000003779 heat-resistant material Substances 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 208000019901 Anxiety disease Diseases 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 229920006328 Styrofoam Polymers 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000036506 anxiety Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000012757 flame retardant agent Substances 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000004620 low density foam Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011342 resin composition Substances 0.000 description 1
- 230000000979 retarding effect Effects 0.000 description 1
- 239000008261 styrofoam Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0004—Use of compounding ingredients, the chemical constitution of which is unknown, broadly defined, or irrelevant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/001—Combinations of extrusion moulding with other shaping operations
- B29C48/0012—Combinations of extrusion moulding with other shaping operations combined with shaping by internal pressure generated in the material, e.g. foaming
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/02—Halogenated hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
- C08L25/02—Homopolymers or copolymers of hydrocarbons
- C08L25/04—Homopolymers or copolymers of styrene
- C08L25/06—Polystyrene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2325/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Derivatives of such polymers
- C08J2325/02—Homopolymers or copolymers of hydrocarbons
- C08J2325/04—Homopolymers or copolymers of styrene
- C08J2325/06—Polystyrene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
- C08K2003/2237—Oxides; Hydroxides of metals of titanium
- C08K2003/2241—Titanium dioxide
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- Chemical & Material Sciences (AREA)
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- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
본 발명은 단열성이 우수하고 야외노출시 변형이 생기지 않는 압출 스티렌 발포체의 제조방법에 관한 것으로, 상기 방법은 폴리스티렌 수지에 흑연분말, 산화티탄, 난연제, 조핵제를 압출기에 투입하고, 용융한 다음, 발포제 투입하여 압출하는 것이며, 이를 통해 단열성이 우수하고 야외노출시 변형이 생기지 않는 압출 스티렌 폼을 제조할 수 있다.The present invention relates to a method for producing an extruded styrene foam which is excellent in heat insulation and does not cause deformation when exposed to the outside, and is characterized in that graphite powder, titanium oxide, a flame retardant and a nucleating agent are added to a polystyrene resin in an extruder, The extruded styrene foam is excellent in heat insulation property and does not cause deformation during outdoor exposure.
Description
본 발명은 단열성이 우수하고 야외 노출시 변형이 생기지 않는 압출 스티렌 발포체의 제조방법에 관한 것이고, 더욱 상세하게는 주 원료인 폴리스티렌 수지에 흑연과 함께 산화티탄을 사용하여 단열성이 우수하면서 야외 노출시 변형이 생기지 않는 압출 스티렌 발포체의 제조방법에 관한 것이다.
The present invention relates to a method for producing an extruded styrene foam which is excellent in heat insulation property and does not cause deformation during outdoor exposure. More specifically, the present invention relates to a method for producing an extruded styrene foam which is excellent in heat insulation by using titanium oxide together with graphite in a main raw material, To a method for producing an extruded styrene foam.
일반적으로 단열용으로 사용된 발포된 폴리스티렌 발포체 보드의 밀도는 약 30 g/ℓ인데, 그 이유는 팽창된 폴리스티렌 발포체의 열전도도가 상기 밀도에서 최소값을 갖기 때문이다.Generally, the density of foamed polystyrene foam boards used for thermal insulation is about 30 g / l because the thermal conductivity of the expanded polystyrene foam has a minimum value at that density.
재료 및 공간을 절약하기 위하여, 보다 낮은 밀도, 특히 15 g/ℓ 미만을 갖는 발포체 보드를 단열을 위해 사용하는 것이 바람직하며, 이와 같은 발포체의 제조는 기술적으로는 문제점이 없다.To save material and space, it is desirable to use foam boards with lower density, especially less than 15 g / l, for insulation, and the production of such foams is not technically problematic.
그러나, 상기 낮은 밀도를 갖는 발포체 보드는 단열 성능을 급격하게 감소시켜 열전도도 등급 035 (DIN 18 164, 1부)의 필요조건을 만족시키지 않는다.However, the low density foam board drastically reduces the insulation performance and does not meet the requirements of the thermal conductivity grade 035 (DIN 18 164, part 1).
발포체의 열전도도는 카본 블랙, 금속 산화물, 금속 분말 또는 안료와 같은 무열 재료의 혼입에 의해 감소될 수 있음은 공지되어 있다.It is known that the thermal conductivity of the foam can be reduced by the incorporation of heat-resistant materials such as carbon black, metal oxides, metal powders or pigments.
따라서, 유럽 특허 공개 공보 제372 343호에는 카본 블랙 1 내지 25 중량%를 함유하는 폴리스티렌 발포체가 기재되어 있으며, 이 경우 카본 블랙의 입도는 10 내지 100 ㎚이다. 상기 문헌에 기재된 폴리스티렌 발포체는 주로 압출법에 의해 제조되고, 바람직하게 밀도는 32 내지 40g/ℓ이다. 또한, 폴리스티렌 중 카본 블랙 농축물을 발포제와 함께 폴리스티렌 용융물로 혼합하고, 상기 혼합물을 압출하고 결정화하여 발포제를 함유하는 미립자상 폴리스티렌을 제조하는 방법이 기재되어 있으나, 이는 제조방법이 매우 복잡하다.Thus, EP-A 372 343 describes polystyrene foams containing from 1 to 25% by weight of carbon black, in which case the particle size of the carbon black is between 10 and 100 nm. The polystyrene foam described in the above document is produced mainly by extrusion, and preferably has a density of 32 to 40 g / l. Also disclosed is a method for producing fine-particle polystyrene containing a foaming agent by mixing a carbon black concentrate in polystyrene with a foaming agent with a polystyrene melt, and extruding and crystallizing the mixture to produce fine-particle polystyrene containing a foaming agent.
국제 특허 공개 공보 제94/13721호에는 카본 블랙의 입도가 150㎚ 초과인 유사 발포체가 기재되어 있다.International Patent Publication No. 94/13721 describes a similar foam having a particle size of carbon black of more than 150 nm.
유럽 특허 공개 공보 제620 246호에는 미립자상 무열 재료, 특히 카본 블랙과 또한 흑연을 함유하는 팽창된 폴리스티렌 발포체 성형물이 기재되어 있으며, 여기서 성형물의 밀도는 20g/ℓ 미만이다.EP-A-620 246 describes an expanded polystyrene foam molding comprising particulate heat-resistant materials, especially carbon black and also graphite, wherein the density of the molding is less than 20 g / l.
입자를 성형물에 혼입시키는 것은 바람직하게는 예비발포화된 폴리스티렌 비드의 표면을 코팅하거나 또는 아직 발포화되지 않은 폴리스티렌 입자체에 매립시킴으로써 수행된다. 그러나 폴리스티렌 입자의 표면 상에 입자를 분포시키는 것은 예비발포화된 비드의 접착을 대단히 손상하여 저품질의 발포체를 유발하며, 또한 입자는 성형물의 표면에서 벗겨질 수 있다. 두 경우 모두에서 입자는 폴리스티렌 입자의 내부에 균일하게 분포되지 않는다.The incorporation of the particles into the molding is preferably carried out by coating the surface of the prefoamed polystyrene beads or by embedding them in the polystyrene sieve which has not yet been foamed. However, distributing the particles on the surface of the polystyrene particles greatly impairs adhesion of the prefoamed beads, resulting in low-quality foams, and the particles can also be peeled from the surface of the molding. In both cases, the particles are not uniformly distributed within the polystyrene particles.
상기와 같은 무열입자가 혼입된 성형물은 열전도도를 감소시키기는 하지만 야외에 노출될 경우 색상이 검어서 적외선 흡수가 용이하여 성형물의 위아래 온도차에 따라 수축, 팽창 및/또는 휨이 발생하는 문제가 생긴다. 즉, 도 1에 따르면, 무열입자, 즉 흑연이 혼입되지 않은 성형물과 흑연이 혼입된 성형물의 색상과 이들의 표면온도를 측정한 것으로, 흑연이 혼입된 성형물은 검은색 색상이여서 표면온도가 혼입되지 않는 것에 비해 높았으며, 이로 인해 장기간 야외 노출시 휨이 발생할 수 있게 되는 것이다.Although the molded article having the above-mentioned non-heat-absorbing particles reduces the thermal conductivity, when the resin is exposed to the outdoors, the color is black and the infrared ray is easily absorbed, causing a problem of shrinkage, expansion and / or warping depending on the temperature difference between the upper and lower parts of the molded article . That is, according to FIG. 1, the color of the non-heat-treated particles, that is, the color of the molded article in which the graphite is not mixed with the graphite, and the surface temperature thereof are measured. The molded article containing the graphite has a black color, , Which may cause warpage in long-term outdoor exposure.
이에 본 발명자들은 기존 성형물의 야외 노출시 온도에 따른 변형을 감소시키기 위한 방안을 연구하면서, 흑연과 함께 산화티탄을 첨가하는 경우, 야외 노출시 적외선, 자외선 등을 반사하여 발포체 온도 상승을 줄여 줌으로써 압출 스티렌 발포체의 변형이 생기지 않음을 밝히고 본 발명을 완성하였다.
Accordingly, the present inventors have studied a method for reducing deformation according to the temperature of outdoor moldings of existing moldings and, when titanium oxide is added together with graphite, reflect infrared rays and ultraviolet rays during outdoor exposure to reduce the temperature rise of the foam, Styrene foam is not deformed and the present invention has been completed.
따라서, 본 발명이 해결하고자 하는 과제는 단열성이 우수하고 야외 노출시 변형이 생기지 않는 압출 스티렌 발포체 제조방법를 제공하는 것이다.
Accordingly, a problem to be solved by the present invention is to provide a method for producing an extruded styrene foam which is excellent in heat insulation and does not cause deformation during outdoor exposure.
상기 과제를 해결하기 위하여, 본 발명은In order to solve the above problems,
폴리스티렌 수지에 상기 수지의 중량대비 흑연분말 0.1 내지 5중량%, 산화티탄 0.1 내지 1중량%, 난연제는 브롬계 HBCD(Hexa bromocyclo dodecane) 1 내지 5중량%, 조핵제 0.3 내지 4중량%를 혼합하여 용융하는 단계; 및0.1 to 5% by weight of graphite powder and 0.1 to 1% by weight of titanium oxide, 1 to 5% by weight of bromine-based bromocyclo dodecane (HBCD) and 0.3 to 4% by weight of a nucleating agent are mixed in a polystyrene resin with respect to the weight of the resin, Melting; And
상기 용융물에 상기 수지의 중량대비 발포제 3 내지 15중량%를 투입하여 압출하는 단계를 포함하는 것을 특징으로 하는 단열성이 우수하고 야외 노출시 변형이 생기지 않는 압출 스티렌 발포체의 제조방법을 제공한다.And 3 to 15% by weight of a blowing agent based on the weight of the resin is injected into the melt to extrude the extruded styrene foam. The extruded styrene foam is excellent in heat insulation and does not deform during outdoor exposure.
본 발명에 따른 압출 스티렌 발포체의 제조방법에 있어서, 상기 산화티탄은 0.4 내지 1.2 g/mℓ의 밀도를 갖는 백색 분말인 것이 바람직하고, 상기 흑연은 20 내지 40g/ℓ의 밀도를 갖는 것이 바람직하다.In the process for producing an extruded styrene foam according to the present invention, the titanium oxide is preferably a white powder having a density of 0.4 to 1.2 g / m, and the graphite preferably has a density of 20 to 40 g / l.
또한, 상기 흑연분말은 열전도도를 낮추면서, 발포체의 물리적 특성을 천연흑연 또는 합성흑연(인조흑연) 중 어느 하나이고, 상기 난연제인 브롬계 HBCD(Hexa bromocyclo dodecane)는 EPS(expanded polystyrene foam) 또는 XPS(extruded polystyrene foam)용 중에서 선택되는 어느 하나이며, 상기 조핵제는 TALC, 탄산칼슘 및 실리카로 이루어진 군에서 선택되고, 상기 발포제는 H2O, 알콜, 가압화하여 액화상태가 된 HCFC류(HCFC-22, HCFC-142b), 부탄, CO2 및 DME(CH3COCH3)로 이루어진 군에서 선택되는 것이 바람직하다.
In addition, the graphite powder may be one of natural graphite or synthetic graphite (artificial graphite), while physical properties of the foam may be reduced while thermal conductivity is lowered. The flame retardant HBCD (Hexa bromocyclo dodecane) may be expanded polystyrene foam XPS (extruded polystyrene foam), and the nucleating agent is selected from the group consisting of TALC, calcium carbonate and silica, and the blowing agent is selected from the group consisting of H 2 O, alcohol, HCFCs HCFC-22, HCFC-142b), butane, CO2, and DME (CH3COCH3).
상술한 바와 같은 본 발명에 따른 제조방법은 낮은 밀도 및 낮은 열전도도를 가지면서 양호한 가공 특성 및 양호한 물리적 특성을 갖고, 동시에 야외 노출시 변형이 생기지 않는 단열성이 우수한 압출 폴리스티렌 발포체를 제조할 수 있다.
The production method according to the present invention as described above can produce an extruded polystyrene foam having low density and low thermal conductivity, good processing characteristics and good physical properties, and at the same time having excellent heat insulation property without causing deformation during outdoor exposure.
도 1은 흑연이 혼입되지 않은 성형물과 흑연이 혼입된 성형물의 색상과 이들의 표면온도를 나타낸 사진이다.
도 2는 실시예 1 및 비교예 1 내지 2에서 얻은 스티렌 발포체의 상태를 나타낸 사진이다.Fig. 1 is a photograph showing the hue of the molded article in which graphite is not mixed with graphite and the surface temperature thereof.
2 is a photograph showing the states of the styrene foam obtained in Example 1 and Comparative Examples 1 and 2. Fig.
이하, 본 발명에 따른 단열성이 우수한 압출 스티렌 발포체 제조방법에 대한 바람직한 실시예를 참조하여 상세히 설명한다.Hereinafter, a method for producing an extruded styrene foam having excellent heat insulation properties according to the present invention will be described in detail with reference to preferred embodiments thereof.
본 발명은 폴리스티렌 수지에 상기 수지의 중량대비 흑연분말 0.1 내지 5중량%, 산화티탄 0.1 내지 1중량%, 난연제는 브롬계 HBCD(Hexa bromocyclo dodecane) 1 내지 5중량% 및 조핵제 0.3 내지 4중량%를 혼합하여 용융하는 단계; 및 상기 용융물에 상기 수지의 중량대비 발포제 3 내지 15중량%를 투입하여 압출하는 단계를 포함하는 것을 특징으로 하는 단열성이 우수하고 야외 노출시 변형이 생기지 않는 압출 스티렌 발포체 제조방법이다.The present invention relates to a polystyrene resin composition comprising 0.1 to 5% by weight of graphite powder and 0.1 to 1% by weight of titanium oxide, 1 to 5% by weight of bromine-based bromocyclo dodecane (HBCD) and 0.3 to 4% Mixing and melting the mixture; And 3 to 15% by weight of a blowing agent based on the weight of the resin to the melt, and extruding the extruded styrene foam. The extruded styrene foam is excellent in heat insulation and does not deform during outdoor exposure.
상기 용융 단계에서, 주재료인 폴리스티렌 수지(중합체)는 중량평균분자량이 20 내지 30만으로 압출용도에 쓰는 것을 사용하는 것이 바람직하다. 압출조건에 따라 재활용한 스티로폼 폴리스티렌 중합체도 주재료 중량대비 0.1 내지 50%에서 사용 할 수 있지만 개방셀(open cell)형성 등으로 인한 단열성 저하나 품질 불균일로 인한 공정불안 제기되지 않도록 하여야 한다.In the melting step, the main material, polystyrene resin (polymer), preferably has a weight average molecular weight of 20 to 300,000 and is used for extrusion use. The styrofoam polystyrene polymer recycled according to the extrusion conditions can be used at 0.1 to 50% of the weight of the main material. However, it is necessary to prevent the process anxiety due to the deterioration of the heat insulation due to the open cell formation or the quality unevenness.
단열성을 개선시키고 양호한 물리적 특성을 가질 수 있도록 첨가되는 첨가제인 흑연분말은 천연흑연 또는 합성흑연(인조흑연)중 어느 것을 사용해도 가능하며, 이는 폴리스티렌 수지 중량대비 0.1 내지 5중량%의 범위 내에서 사용되는 것이 바람직하다. 여기서 0.1중량% 미만으로 사용되는 경우 단열성 개선여부가 나타나지 않고, 5중량%를 초과하여 사용되는 경우 셀을 개방시키는 것을 포함 셀 구조에 영향을 미쳐 열전도율 하락보다는 열전도율을 상승시키기 때문에 바람직하지 않다.The graphite powder, which is an additive added to improve the heat insulation property and good physical properties, can be either natural graphite or synthetic graphite (artificial graphite), which is used in a range of 0.1 to 5% by weight based on the weight of the polystyrene resin . If it is used in an amount of less than 0.1% by weight, it is not preferable to improve the heat insulating property, and if it is used in an amount exceeding 5% by weight, it is not preferable because it affects the cell structure including opening the cell and increases the thermal conductivity rather than the decrease in thermal conductivity.
또한, 사용되는 흑연은 그의 밀도가 20 내지 40g/ℓ인 것이 바람직하며, 흑연의 밀도가 20g/ℓ미만에서는 저밀도로 제품형상을 유지하기 어렵고, 40g/ℓ초과하는 고밀도에서 제조원가 상승으로 비경제적이다.The graphite used preferably has a density of 20 to 40 g / l, and when the density of graphite is less than 20 g / l, it is difficult to maintain the product shape with a low density, and it is uneconomical to increase the manufacturing cost at a high density exceeding 40 g / .
상기 합성흑연 즉, 인조흑연이라 함은 석유정제후 남은 찌꺼기인 석유코크나 석탄에서 추출되는 코크(coke)등을 2,500℃이상에서 가열하면 정향배열 구조를 바꾸는 흑연 화(graphiteization)과정을 거친 것을 인조흑연(합성흑연)이라고 한다.The synthetic graphite, that is, artificial graphite refers to graphite which has undergone a graphiteization process when the coke or the like extracted from petroleum coke or coal, which is remnant after petroleum refining, is heated at 2,500 ° C. or higher, Graphite (synthetic graphite).
야외 노출시 발생되는 휨 현상을 감소시키기 위해 사용되는 산화티탄은 백색분말로 야외 노출시 자외선, 적외선 등을 반사시켜 성형물에 온도를 높이지 않은 역할을 함으로써 발포체의 변형을 방지한다.The titanium oxide used to reduce warpage caused by outdoor exposure is white powder, which protects the foam from deformation by reflecting ultraviolet rays, infrared rays,
상기 산화티탄은 원석 알루미나마이트를 산화반응시켜 제조한 것으로 산화금속(또는 수산화물)로 표면코팅이 되어있고, 폴리히드릭 알콜(Polyhydric aclcohols), 알카놀아민(alkcanolamines) 또는 실록산(siloxanes) 등의 유기물질로 또 다른 표면처리가 되어 있다.The titanium oxide is prepared by oxidizing gemite aluminumite and is surface-coated with a metal oxide (or hydroxide). The titanium oxide is an organic compound such as polyhydric alcohols, alkanolamines, siloxanes, The surface is treated with another material.
상기 산화티탄으로는 구상구조인 루틸(rutile)과 면상구조인 아나타제(anatase)의 2가지 다른 결정형이 있으며, 이중에서 안정화되어 활성이 약하고, 투과성이 상대적으로 작은 구상구조인 루틸을 사용하는 것이 바람직하다.As the titanium oxide, there are two different crystal forms of rutile, which is a spherical structure, and anatase, which is a planar structure. Of these, rutile, which is stabilized and weak in activity and has a relatively small permeability, is preferably used Do.
산화티탄의 사용량은 폴리스티렌 수지의 중량대비 0.1 내지 1중량%의 범위 내에서 사용되는 것이 바람직하며, 0.1중량% 미만에서는 사용량이 작아 휨개선 효과가 없고, 1중량% 초과시는 단열성이 떨어져 흑연 사용 효과가 반감된다.The amount of titanium oxide to be used is preferably within a range of 0.1 to 1% by weight based on the weight of the polystyrene resin. When the amount is less than 0.1% by weight, the amount of titanium oxide used is small and the effect of improving warpage is not exhibited. .
사용되는 산화티탄의 밀도는 0.4 내지 1.2 g/mℓ의 범위 내인 것이 바람직하며, 산화티탄의 밀도가 0.4g/mℓ미만인 경우 입자상이 작아 발포체에 분산이 어렵고, 1.2g/mℓ를 초과하는 경우 차폐력이 떨어지고 발포체 의 셀에 나쁘게 영향을 미치며 비경제적이다.It is preferable that the density of the titanium oxide used is in the range of 0.4 to 1.2 g / mℓ. When the density of the titanium oxide is less than 0.4 g / mℓ, the particle size is small and it is difficult to disperse in the foam. When the density is more than 1.2 g / Degrade and adversely affect the cells of the foam and are uneconomical.
난연제는 브롬계를 사용하는 것이 바람직하며, 이는 발포 폴리스티렌 폼 보드에 브롬이 들어감으로 해서 불연성가스 생성소화 작용 등 난연 메카니즘으로 자기 소화성을 갖게 되기 때문이다. 상기 난연제는 분말형태로 투입하거나 투입 전 폴리스티렌수지와 혼합(마스터뱃치) 펠렛 형태로 사용할 수 있고, 그의 사용량은 폴리스티렌 수지의 중량대비 1 내지 5중량%의 범위 내인 것이 바람직하며, 1중량% 미만의 경우 KS M 3808 연소성 기준을 맞출 수 없고, 5중량% 초과시는 고가 난연제 사용으로 비경제적이며 제품물성 강도, 열전도율을 저하시키기 때문에 바람직하지 않다.It is preferable to use a bromine-based flame retardant because bromine enters the foamed polystyrene foam board, and self-extinguishing property is obtained by a flame retarding mechanism such as a nonflammable gas generating and extinguishing function. The flame retardant may be used in the form of a powder or in the form of a pellet mixed with a polystyrene resin before the addition (master batch). The amount of the flame retardant used is preferably in the range of 1 to 5% by weight based on the weight of the polystyrene resin, , The flammability standard of KS M 3808 can not be met, and when it exceeds 5 wt%, use of a high-flame retardant agent is not economical, and the strength and thermal conductivity of the product are lowered.
상기와 같이 사용되는 브롬계 난연제로는 HBCD(Hexa bromocyclo dodecane)가 바람직하며, 상기 HBCD(Hexa bromocyclo dodecane)는 헥사브로모시클로도데칸(Hexabromocyclododecane)의 유기 할로겐계 난연제로 폴리스티렌을 기본으로 하는 EPS(expanded polystyrene foam)에나 XPS(extruded polystyrene foam)등에 주로 사용한다.The brominated flame retardant is preferably HBCD (Hexa bromocyclo dodecane), and the HBCD (Hexa bromocyclo dodecane) is an organic halogen-based flame retardant of hexabromocyclododecane. The polystyrene-based EPS expanded polystyrene foam) or extruded polystyrene foam (XPS).
또 다른 첨가제인 조핵제는 압출법 발포성 폴리스티렌 중합체 제조시 단열성을 보완하기 위해 사용됨과 동시에 발포 셀 크기를 작게 하거나 균일하게 만들어 주기 위해 사용되는 것으로 그의 사용량은 폴리스티렌 수지의 중량대비 0.3 내지 4.0중량% 투입됨이 바람직하다.Another additive, a nucleating agent, is used to complement the heat insulation property in the production of the expandable polystyrene polymer by extrusion, and at the same time, it is used to make the size of the foamed cell small or uniform. Its usage is 0.3 to 4.0% by weight based on the weight of the polystyrene resin .
상기와 같이 폴리스티렌 수지에 첨가제인 흑연분말, 산화티탄, 난연제 및 조핵제를 압출기에 투입하여 용융시킨다. 여기서, 압출기로는 이 분야에 일반적으로 사용되는 압출기가 사용될 수 있으며, 또한, 상기 투입물이 모두 용융될 수 있도록 180 내지 240℃에서 용융시키는 것이 바람직하다.As described above, graphite powder, titanium oxide, a flame retardant, and a nucleating agent, which are additives to the polystyrene resin, are put into an extruder and melted. As the extruder, an extruder generally used in this field can be used, and it is also preferable to melt at 180 to 240 캜 so that all of the input materials can be melted.
이어서, 상기 용융시킨 용융물에 발포제를 투입하여 압출하는 단계가 진행된다.Subsequently, a step of putting the foaming agent into the molten melt and extruding is carried out.
여기서, 상기 발포제로는 폴리스티렌 수지를 충분히 발포시키기 위하여 사용되며, 상기 발포제는 폴리스티렌 수지 중량대비 3 내지 15중량%의 범위내에서 사용되는 것이 바람직하다. 3중량% 미만으로 발포제가 사용되는 경우, 폴리스티렌 수지를 충분히 발포할 수 없으므로 제품의 밀도를 상승시킬 수 있으며, 15중량%를 초과하면 발포제 손실이 발생하여 비경제적이며 평평한 판상을 얻기 어렵다.Here, the foaming agent is used for sufficiently foaming the polystyrene resin, and the foaming agent is preferably used in a range of 3 to 15% by weight based on the weight of the polystyrene resin. When the foaming agent is used in an amount of less than 3% by weight, the polystyrene resin can not be sufficiently foamed to increase the density of the product. When the amount of the foaming agent is more than 15% by weight, a loss of foaming agent occurs.
상기 압출은 이 분야에 일반적인 방법으로 통해 압출되어질 수 있으며, 이 때 온도는 100 내지 140℃에서 진행되는 것이 바람직하다.The extrusion may be extruded through a conventional method in this field, preferably at a temperature of from 100 to 140 < 0 > C.
상기 발포제로는 H2O, 알콜, 가압화여 액화상태가 된 HCFC류 (HCFC-22, HCFC-142b), 부탄, CO2 , DME(CH3OCH3) 중 어느 하나이고, 상기 HCFC류, 즉 HCFC-22는 모노클로로디플루오르 메탄(Monochloro difluoro methane)이고, HCFC-142b는 모노클로로디플루오르 에탄(Monochloro difluoro ethane)이다.
The blowing agent is any one of H 2 O, alcohol, pressurized and liquefied HCFCs (HCFC-22, HCFC-142b), butane, CO 2 and DME (CH 3 OCH 3 ) Is monochloro difluoro methane, and HCFC-142b is Monochloro difluoro ethane.
이하 본 발명을 실시예를 들어 상세히 설명하지만, 본 발명이 하기 실시예로 한정되는 것은 아니다.Hereinafter, the present invention will be described in detail with reference to Examples. However, the present invention is not limited to the following Examples.
비교예Comparative Example 1 One
압출기에 투입된 폴리스티렌 수지(LG화학 25HRE) 100kg에 첨가제로 난연제(HBCD) 3kg 및 조핵제 1kg를 혼합 투입하여 220℃에서 용융시키고, 이어서 발포제 HCFC-22를 6kg 투입하고, CO2를 1kg 투입하여 120℃로 냉각 압출하여 스티렌 발포체를 만들었다.3 kg of a flame retardant (HBCD) and 1 kg of a nucleating agent were mixed and injected into 100 kg of a polystyrene resin (LG Chem 25HRE) injected into an extruder and melted at 220 ° C. Then 6 kg of foaming agent HCFC-22 was added and 1 kg of CO 2 was added to 120 Lt; 0 > C to form a styrene foam.
비교예Comparative Example 2 2
압출기에 투입된 폴리스티렌 수지(LG화학 25HRE) 100kg에 첨가제로 흑연분말(30g/ℓ의 밀도) 0.3kg, 난연제(HBCD) 3kg 및 조핵제 1kg를 혼합 투입하여 220℃에서 용융시키고, 이어서 발포제 HCFC-22를 6kg 투입하고, CO2를 1kg 투입하여 120℃로 냉각 압출하여 스티렌 발포체를 만들었다.0.3 kg of graphite powder (density of 30 g / l) as an additive, 3 kg of flame retardant (HBCD) and 1 kg of a nucleating agent were mixed and injected into 100 kg of a polystyrene resin (LG Chem 25HRE) put into an extruder and then melted at 220 캜. And 1 kg of CO 2 was added thereto. The mixture was cooled and extruded at 120 ° C to prepare a styrene foam.
실시예Example 1 One
압출기에 투입된 폴리스티렌 수지(LG화학 25HRE) 100kg에 첨가제로 흑연분말(30g/ℓ의 밀도) 0.3kg, 산화티탄(독일허츠만 TR28) 0.2kg, 난연제(HBCD) 3kg 및 조핵제 1kg를 혼합 투입하여 220℃에서 용융시키고, 이어서 발포제 HCFC-22를 6kg 투입하고, CO2를 1kg 투입하여 120℃로 냉각 압출하여 스티렌 발포체를 만들었다.0.3 kg of graphite powder (30 g / l density), 0.2 kg of titanium oxide (Germany Hertzman TR28), 3 kg of flame retardant (HBCD) and 1 kg of a nucleating agent were added to 100 kg of polystyrene resin (LG Chem 25HRE) Then, 6 kg of foaming agent HCFC-22 was added, 1 kg of CO 2 was added, and the mixture was cooled and extruded at 120 ° C to prepare a styrene foam.
시험예Test Example 1 One
상기 비교예 1(흑연 및 산화티탄 무첨가), 비교예 2(흑연만 첨가), 실시예 1(흑연 및 산화티탄 첨가)에서 얻은 스티렌 발포체에 대하여 밀도를 측정하고, 열전도율을 측정하여 그 결과를 하기 표 1에 나타내었다.The density of the styrene foam obtained in Comparative Example 1 (no graphite and titanium oxide), Comparative Example 2 (graphite only) and Example 1 (graphite and titanium oxide added) were measured and the thermal conductivity was measured. Table 1 shows the results.
열전도율 시험방법 : 평균온도 20± 5℃에서 KS L 9016으로 측정Thermal conductivity test method: Measured with KS L 9016 at an average temperature of 20 ± 5 ℃
시험예Test Example 2 2
상기 비교예 1, 비교예 2 및 실시예 1에서 얻은 스티렌 발포체를 두께 50mm 폭 900mm 길이 1800mm인 보드로 만든 후, 이들을 사진 촬영하여 이를 도 2에 나타내고, 야외 노출 시간에 경과에 따른 휨량(mm)를 측정하였다. 야외 노출 54시간 경과시 보드의 길이방향으로 비교예 1(무첨가)는 2mm, 비교예 2(흑연입자 투입)는 8mm, 실시예 1(흑연입자+산화티탄 투입)는 3.5mm 벤딩이 생겼다. 자세한 것은 하기 표 2에 나타내었다.The styrene foam obtained in Comparative Example 1, Comparative Example 2 and Example 1 was made into a board having a thickness of 50 mm, a width of 900 mm, and a length of 1800 mm, and these were photographed and shown in FIG. 2. The deflection (mm) Were measured. Comparative Example 2 (charging of graphite particles) was 8 mm, and Example 1 (charging of graphite particles + titanium oxide) resulted in 3.5 mm bending in Comparative Example 1 (no addition) in the longitudinal direction of the board when 54 hours elapsed from exposure to the outside. The details are shown in Table 2 below.
(측정시외부온도)Elapsed time
(External temperature in measurement)
상기 표 1 및 표 2로부터 흑연과 산화티탄을 동시에 사용한 실시예 1의 경우 비교예 1에 비하여 열전도율이 낮으며, 비교예 2에 비해서는 휨양이 월등히 낮았으며, 흑연만 첨가된 비교예 2와는 열전도율 면에서 유사함을 확인할 수 있었고, 또한, 흑연이 첨가되지 않은 비교예 1과 휨양에 있어서 유사함을 확인할 수 있었다.From the above Tables 1 and 2, the thermal conductivity of Example 1 using graphite and titanium oxide at the same time was lower than that of Comparative Example 1, and the deflection was significantly lower than that of Comparative Example 2, and the thermal conductivity And it was confirmed that they were similar to those of Comparative Example 1 in which no graphite was added.
또한 도 2에서 보여지는 바와 같이, 본 발명에 따른 실시예 1의 보드가 비교예 2의 보드에 비해 휨이 없음을 확인할 수 있었다.Also, as shown in FIG. 2, it can be seen that the board of Example 1 according to the present invention has no warpage as compared with the board of Comparative Example 2.
Claims (4)
상기 용융물에 상기 수지의 중량대비 발포제 3 내지 15중량%를 투입하여 압출하는 단계를 포함하고,
상기 산화티탄은 0.4 내지 1.2g/mℓ의 밀도를 갖는 백색 분말인 것을 특징으로 하는 단열성이 우수하고 야외노출시 변형이 생기지 않는 압출스티렌 발포체의 제조방법.0.1 to 5% by weight of graphite powder and 0.1 to 1% by weight of graphite powder, 0.1 to 1% by weight of graphite powder, 0.1 to 1% by weight of flame retardant, 1 to 5% by weight of HBCD (Hexa bromocyclo dodecane) and 0.3 to 4% Melting; And
Adding 3 to 15% by weight of a foaming agent to the melt to the weight of the resin, and extruding the melt,
Wherein the titanium oxide is a white powder having a density of 0.4 to 1.2 g / m < 2 >. The method for producing an extruded styrene foam according to any one of claims 1 to 3,
상기 흑연는 20 내지 40g/ℓ의 밀도를 갖는 것을 특징으로 하는 단열성이 우수하고 야외노출시 변형이 생기지 않는 압출 스티렌 발포체의 제조방법.The method according to claim 1,
Wherein the graphite has a density of 20 to 40 g / l. The method for producing an extruded styrene foam according to claim 1,
상기 흑연분말은 천연흑연 또는 합성흑연(인조흑연) 중 어느 하나이고, 상기 난연제인 HBCD(Hexa bromocyclo dodecane)는 EPS(expanded polystyrene foam) 또는 XPS(extruded polystyrene foam)용 중에 어느 하나이며, 상기 조핵제는 TALC, 탄산칼슘 및 실리카로 이루어진 군에서 선택되고, 상기 발포제는 H2O, 알콜, 가압화하여 액화상태가 된 HCFC류(HCFC-22, HCFC-142b), 부탄, CO2 및 DME(CH3COCH3)로 이루어진 군에서 선택되는 것을 특징으로 하는 단열성이 우수하고 야외노출시 변형이 생기지 않는 압출 스티렌 발포체의 제조방법.The method according to claim 1,
Wherein the graphite powder is one of natural graphite or synthetic graphite (artificial graphite), and the flame retardant HBCD (Hexa bromocyclo dodecane) is any one of expanded polystyrene foam (EPS) or extruded polystyrene foam (XPS) is TALC, is selected from the group consisting of calcium carbonate and silica, the foaming agent is H 2 O, an alcohol, pressure granulation to a liquefied state HCFC acids (HCFC-22, HCFC-142b ), butane, CO2 and DME (CH3COCH3) Wherein the extruded styrene foam is excellent in heat insulation and does not cause deformation during outdoor exposure.
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US5710186A (en) * | 1996-05-31 | 1998-01-20 | The Dow Chemical Company | Foams containing treated titanium dioxide and processes for making |
KR20010075179A (en) * | 1998-09-16 | 2001-08-09 | 휴스톤 로버트 엘 | Process for producing styrenic foam |
KR100750626B1 (en) | 2006-12-29 | 2007-08-20 | 주식회사 벽산 | Styrene-form with excellent insulation and a manufacturing method thereof |
WO2009148445A1 (en) | 2008-06-04 | 2009-12-10 | Owens Corning Intellectual Capital, Llc | Extruded polystyrene foam containing propylene carbonate, ethylene carbonate or butylene carbonate as a process aids |
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US5710186A (en) * | 1996-05-31 | 1998-01-20 | The Dow Chemical Company | Foams containing treated titanium dioxide and processes for making |
KR20010075179A (en) * | 1998-09-16 | 2001-08-09 | 휴스톤 로버트 엘 | Process for producing styrenic foam |
KR100750626B1 (en) | 2006-12-29 | 2007-08-20 | 주식회사 벽산 | Styrene-form with excellent insulation and a manufacturing method thereof |
WO2009148445A1 (en) | 2008-06-04 | 2009-12-10 | Owens Corning Intellectual Capital, Llc | Extruded polystyrene foam containing propylene carbonate, ethylene carbonate or butylene carbonate as a process aids |
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KR20220141178A (en) | 2021-04-12 | 2022-10-19 | 김선희 | Method for preparing flame retardant expanded polystyrene panel and the blind therefrom |
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