KR20000062119A - Expandable polystyrene resin and a method of producing the same - Google Patents

Expandable polystyrene resin and a method of producing the same Download PDF

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Publication number
KR20000062119A
KR20000062119A KR1019990033718A KR19990033718A KR20000062119A KR 20000062119 A KR20000062119 A KR 20000062119A KR 1019990033718 A KR1019990033718 A KR 1019990033718A KR 19990033718 A KR19990033718 A KR 19990033718A KR 20000062119 A KR20000062119 A KR 20000062119A
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South Korea
Prior art keywords
steam
mold
foam
temperature
polystyrene resin
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KR1019990033718A
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Korean (ko)
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강석환
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강석환
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Priority to KR1019990033718A priority Critical patent/KR20000062119A/en
Publication of KR20000062119A publication Critical patent/KR20000062119A/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/3415Heating or cooling
    • B29C44/3426Heating by introducing steam in the mould
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/02Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/3461Making or treating expandable particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/36Feeding the material to be shaped
    • B29C44/38Feeding the material to be shaped into a closed space, i.e. to make articles of definite length
    • B29C44/44Feeding the material to be shaped into a closed space, i.e. to make articles of definite length in solid form
    • B29C44/445Feeding the material to be shaped into a closed space, i.e. to make articles of definite length in solid form in the form of expandable granules, particles or beads
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/60Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2025/00Use of polymers of vinyl-aromatic compounds or derivatives thereof as moulding material
    • B29K2025/04Polymers of styrene
    • B29K2025/06PS, i.e. polystyrene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/04Condition, form or state of moulded material or of the material to be shaped cellular or porous
    • B29K2105/048Expandable particles, beads or granules

Abstract

PURPOSE: A method for preparing a polystyrene resin foam-molded body which and the polystyrene resin foam-molded body with high intensity prepared by foaming the polystrene resin with a low magnifying power are provided. CONSTITUTION: The method comprises steps of: (i) obtaining a pre-foamed bead by putting a foaming polystyrene resin in a foam container having a stirring device and then directly heating it with steam having a pressure of 0.1-0.5 kilogram/minute and a temperature of 180-230°C; (ii) drying the pre-foamed bead; (iii) filling up a pre-heated mold with the dried foamed bead; and (iv) heating the filled foamed bead with steam having a pressure of 0.5-2 kilogram/minute and a temperature of 180-230°C and exhausting air, cooling down and then releasing the foamed bead. The polystyrene resin foam molded body comprises an integrated bottom and side walls. In the bottom a pair of circular piercing holes are formed and inside edge portion, which is a boundary between the bottom and the side walls, is formed to bend at a regular center of curvature not to be transformed by internal stress and many reinforcing ribs are formed on the inside and outside of the side walls to reinforce the intensity.

Description

폴리스티렌 수지 발포 성형체와 그 제조방법{Expandable polystyrene resin and a method of producing the same}Expanded polystyrene resin and a method of producing the same

본 발명은 폴리스티렌 수지 발포 성형체의 제조에 관한 것으로, 더욱 상세하게는 폴리스티렌 수지를 저배율로 발포시켜서 제조되는 고강도의 폴리스티렌 수지 발포 성형체 및 이의 제조방법에 관한 것이다.The present invention relates to the production of a polystyrene resin foamed molded article, and more particularly, to a high-strength polystyrene resin foamed molded article produced by foaming a polystyrene resin at low magnification and a method for producing the same.

일반적으로, 폴리스티렌 수지는 스티렌의 중합체로서 무색투명의 견고한 열가소성 수지이며, 내수성, 굴절율, 투명성이 크고 고주파절연성이 우수하며, 성형품은 전기부품, 가정용품, 냉장고 부품 등에 사용된다. 이러한 폴리스티렌 수지는 발포성 폴리스티렌(Expandable Polystyrene; EPS) 원료를 발포 용기에 넣은후, 용기를 간접 가열하여 발포시킨 발포체로 성형한 발포 성형체를 사용해 왔다.In general, polystyrene resin is a polymer of styrene, a colorless transparent solid thermoplastic resin, has excellent water resistance, refractive index, transparency, high frequency insulation, and molded articles are used in electric parts, household goods, refrigerator parts, and the like. Such polystyrene resins have used foamed molded articles molded into foams in which an expandable polystyrene (EPS) raw material is placed in a foaming vessel and then foamed by indirectly heating the vessel.

그러나, 이러한 간접 가열 제조방식은 간접가열로 인한 연료소모가 심하고 대단위의 시설 투자가 필요한 단점이 있었다. 또한, 내부까지 골고루 가열하기가 어렵고 온도조절이 용이하지 않기 때문에, 이러한 방법으로 얻은 성형체는 5배 이상의 고배율로 발포되는 경우가 많아서 밀도가 떨어지고 강도가 약한 결점이 있었다.However, this indirect heating manufacturing method has a disadvantage in that fuel consumption due to indirect heating is severe and a large-scale facility investment is required. In addition, since it is difficult to uniformly heat up to the inside and the temperature control is not easy, the molded article obtained by this method is often foamed at a high magnification of 5 times or more, so that there is a defect in density and weak strength.

또한, 성형체의 두께가 전체적으로 균일하지 못하다. 예를 들면, 박스 형태의 성형체의 경우, 가장자리의 두꺼운 부분이 성형시에 제대로 점착이 되지 않아서 강도가 약화되는 등의 문제점이 있었다.In addition, the thickness of the molded body is not uniform throughout. For example, in the case of a box-shaped molded article, there is a problem that the thick portion of the edge is not adhered properly at the time of molding and the strength is weakened.

본 발명은 상기와 같은 종래의 문제점을 해결하기 위해 안출된 것으로, 본 발명의 제 1의 목적은 가열에 필요한 연료소모가 적고 방대한 시설투자가 필요하지 않을 뿐 아니라 온도조절이 용이하여 정확한 배율의 발포체를 제조할 수 있는 폴리스티렌 수지 발포 성형체의 제조방법을 제공하는데 있다.The present invention has been made to solve the conventional problems as described above, the first object of the present invention is to reduce the fuel consumption required for heating, do not require extensive facility investment, and easy to control the temperature of the foam of the correct magnification It is to provide a method for producing a polystyrene resin foam molded article that can be produced.

본 발명의 제 2의 목적은 밀도가 높은 고강도의 폴리스티렌 수지 발포 성형체를 제공하는데 있다.A second object of the present invention is to provide a high density polystyrene resin foam molded article having a high density.

도 1은 본 발명에서 사용되는 주형들 사이에 발포체가 위치된 상태를 개략적으로 나타낸 도면,1 is a view schematically showing a state in which a foam is located between the molds used in the present invention,

도 2는 본 발명에 의해서 제조된 폴리스티렌 수지 발포 성형체의 사시도,Figure 2 is a perspective view of a polystyrene resin foam molded article produced by the present invention,

도 3a는 도 2에 도시된 폴리스티렌 수지 발포 성형체의 평면도, 그리고3A is a plan view of the polystyrene resin foamed molded product shown in FIG. 2, and

도 3b는 도 2에 도시된 폴리스티렌 수지 발포 성형체의 저면도이다.3B is a bottom view of the polystyrene resin foam molded article shown in FIG. 2.

〈도면의 주요부분에 대한 부호의 설명〉<Explanation of symbols for main parts of drawing>

11 : 고정측 주형 12 : 이동측 주형11: fixed side mold 12: moving side mold

13, 14 : 스팀 통과 게이트 20 : 발포체13, 14: steam passing gate 20: foam

30 : 운송 박스 32 : 바닥30: transport box 32: bottom

34 : 측벽 36 : 관통공34 side wall 36 through hole

38 : 내측 모서리부 39 : 보강 리브38: inner edge portion 39: reinforcing rib

상기한 제 1의 목적을 달성하기 위하여, 본 발명은,In order to achieve the first object described above, the present invention,

교반 장치가 부착된 발포 용기에 발포성 폴리스티렌 수지를 넣고, 0.1∼0.5㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 직접 가열하여 발포시켜서 예비 발포 비이드를 얻는 단계(S1);Placing the expandable polystyrene resin in a foaming vessel with a stirring device, and foaming by directly heating with a pressure of 0.1 to 0.5 kg / cm 3 and steam at a temperature of 180 to 230 ° C. (S1);

상기 예비 발포 비이드를 건조로로 이송하여 건조시키는 단계(S2);Transferring the pre-expanded beads to a drying furnace to dry (S2);

건조된 발포 비이드를 예비 가열된 주형에 충전하는 단계(S3); 그리고Filling the dried foam beads into a preheated mold (S3); And

충전된 발포 비이드를 0.5∼2㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 가열한후 배기, 냉각 및 이형시키는 단계(S4)를 포함하는 것을 특징으로 하는 폴리스티렌 발포 성형체의 제조 방법을 제공한다.Method for producing a polystyrene foamed molded article comprising the step (S4) of heating the filled foam beads with a pressure of 0.5 ~ 2kg / cm 3 and steam at a temperature of 180 ~ 230 ℃ to provide.

또한, 상기한 제 2의 목적을 달성하기 위하여, 본 발명은,In addition, in order to achieve the above second object, the present invention,

발포 용기 내에 발포성 폴리스티렌 수지를 넣고, 0.1∼0.5㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 직접 가열하여 발포시켜서 예비 발포 비이드를 얻고, 이렇게 얻은 예비 발포 비이드를 건조시킨후, 예비 가열된 주형에 충전하여 0.5∼2㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 가열하고, 계속해서 배기, 냉각 및 이형시켜서 제조되며, 일체로 이루어진 바닥과 측벽을 포함하고, 상기 바닥에는 위치선정을 위한 한쌍의 원형 관통공이 형성되고, 상기 바닥과 상기 측벽의 경계가 되는 내측 모서리부는 응력 발생시의 변형방지를 위해서 일정한 곡률반경으로 만곡되게 형성되며, 상기 측벽의 내측과 외측에는 강도의 보강을 위한 다수의 보강 리브가 형성된 것을 특징으로 하는 폴리스티렌 발포 성형체를 제공한다.The foamed polystyrene resin was placed in a foaming vessel and foamed by directly heating with a pressure of 0.1 to 0.5 kg / cm 3 and steam at a temperature of 180 to 230 ° C. to obtain a preliminary foamed beads, and drying the thus obtained preliminary foamed beads, followed by preliminary It is prepared by filling a heated mold with a pressure of 0.5 to 2 kg / cm 3 and steam at a temperature of 180 to 230 ° C., followed by exhausting, cooling and releasing, and including an integral bottom and sidewalls. A pair of circular through-holes for positioning is formed, and inner corners, which border the bottom and the sidewalls, are curved to have a constant curvature radius to prevent deformation during stress generation, and strength reinforcement is provided inside and outside the sidewalls. It provides a polystyrene foam molded article characterized in that a plurality of reinforcing ribs are formed for.

이하, 첨부 도면들을 참조하여 본 발명을 보다 상세하게 설명한다.Hereinafter, the present invention will be described in more detail with reference to the accompanying drawings.

일반적으로, 발포성 폴리스티렌의 발포는 발포 용기의 외부를 가열하는 간접가열 방식에 의해 행해져 왔으며, 이 경우 폴리스티렌의 발포는 저배율 발포성 폴리스티렌 원료를 사용한다 하더라도 최소 5배에서 25배율로 발포된다. 따라서, 상대적으로 밀도가 낮고 강도가 약한 발포 성형체가 얻어지게 된다.In general, the foaming of the expandable polystyrene has been carried out by an indirect heating method of heating the outside of the foam container, in which case the foaming of the polystyrene is foamed at least 5 to 25 times even when using a low magnification foamable polystyrene raw material. Thus, a foamed molded article having a relatively low density and a weak strength is obtained.

강도가 낮은 고배율 발포체의 경우 충전제나 일회용 용기 등으로 사용하는 경우에는 별 문제가 없으나, 예를 들어 자동 이송 장치의 운송 박스와 같이 여러 차례 반복사용이 필요하고 내구성이 필요한 성형체의 경우에는 사용하기 어려웠다.High strength foams with low strength have no problems when used as fillers or disposable containers, but they are difficult to use for moldings that require repeated use several times and require durability, such as transport boxes for automatic transfer devices. .

이를 해결하기 위해서, 본 발명에서는 스팀을 사용한 직접 가열방식으로 온도를 적절하게 조절하면서 밀도를 측정하여 2.5∼3.5배의 발포체를 얻을 수 있게 되었다.In order to solve this problem, in the present invention, it is possible to obtain a foam of 2.5 to 3.5 times by measuring the density while appropriately adjusting the temperature by a direct heating method using steam.

이때, 분사되는 스팀의 압력은 0.1∼0.5㎏/㎤, 바람직하게는 0.2㎏/㎤, 온도는 180∼230℃ 정도로 조절한다. 스팀을 분사하는 노즐 부위의 온도는 80∼100℃, 바람직하게는 92℃로 조절하고, 발포 용기 내부의 온도는 70∼100℃, 바람직하게는 70∼90℃, 보다 바람직하게는 80℃로 조절한다. 이때, 스팀의 온도가 너무 낮으면 발포가 잘 이루어지지 않고, 온도가 지나치게 높으면 발포가 급격하게 이루어져서 발포배율을 조절하기가 어렵게 된다.At this time, the pressure of the steam injected is adjusted to 0.1 to 0.5 kg / cm 3, preferably 0.2 kg / cm 3, and the temperature is about 180 to 230 ° C. The temperature of the nozzle part for injecting steam is adjusted to 80 to 100 ° C, preferably 92 ° C, and the temperature inside the foam container is adjusted to 70 to 100 ° C, preferably 70 to 90 ° C, more preferably 80 ° C. do. At this time, if the temperature of the steam is too low, the foaming is not made well, if the temperature is too high, the foaming is made rapidly, it is difficult to control the expansion ratio.

발포가 진행되는 경우, 일정 시간 간격으로 밀도를 측정하여 발포 배율이 2.5∼3.5배로 발포되었을 때 건조로로 이송시키게 되면 더 이상의 발포는 진행되지 않게 된다. 즉, 발포는 일정한 진공압력과 스팀 가열 분위기 하에서만 진행되기 때문이다. 이때, 발포와 건조 작업은 연속적으로 수행된다.When the foaming proceeds, if the density is measured at regular intervals and the foaming ratio is 2.5 to 3.5 times when the foaming is transferred to the drying furnace, no further foaming proceeds. That is, the foaming proceeds only under a constant vacuum pressure and steam heating atmosphere. At this time, the foaming and drying operations are carried out continuously.

주형은 스팀으로 미리 예비 가열을 해 두고, 발포 비이드를 주형에 충전한다. 도 1은 본 발명에서 사용되는 주형들 사이에 발포체가 위치된 상태를 개략적으로 나타낸 도면이다. 도 1에 도시된 바와 같이, 본 발명에서 사용되는 주형은 고정측 주형(11)과 이동측 주형(12)으로 구성되고, 각각의 주형(11,12)은 주형(11,12) 사이에 배치되는 발포체(20)에 스팀을 공급하도록 규칙적으로 배열된 스팀 통과 게이트(111, 112)를 갖는다.The mold is preheated with steam and filled with foam beads. 1 is a view schematically showing a state in which a foam is located between the molds used in the present invention. As shown in FIG. 1, the mold used in the present invention is composed of a fixed side mold 11 and a moving side mold 12, and each mold 11, 12 is disposed between the molds 11, 12. It has steam passing gates 111, 112 arranged regularly to supply steam to the foam 20.

이때, 성형체의 투께가 얇은 부분은 스팀 통과 게이트(111)의 깊이도 주형의 두께와 동일하고 3∼5개 섹션으로 나누어져 있으나, 성형체의 두께가 두껍게 성형되어야 할 부분은 도면에 나타낸 바와 같이 스팀이 공급되는 입구쪽의 단면이 브이(V)자 모양이 되도록 입구를 넓히고 스팀 통과 게이트(112)의 깊이를 얕게 형성함과 동시에 하나의 구멍으로 형성함으로써, 스팀의 속도가 빠르고 더 많은 양의 스팀과 더 높은 온도의 스팀이 공급되도록 하였다. 그 결과, 성형체의 두께가 달라도 고른 점착 내지는 성형이 일어나서 강도가 균일하게 된다.At this time, the thin part of the molded body is the same as the thickness of the mold and the depth of the steam passing gate 111 is divided into 3 to 5 sections, but the part to be molded thick thickness of the molded body as shown in the drawing By expanding the inlet so that the cross section of the inlet side to be supplied is V-shaped, forming the depth of the steam passage gate 112 shallowly, and forming it as one hole, the speed of steam is faster and the amount of steam is increased. And higher temperature steam was supplied. As a result, even adhesion or shaping | molding occurs even if the thickness of a molded object differs, and intensity | strength becomes uniform.

충전된 예비 발포 비이드를 0.5∼2㎏/㎤, 바람직하게는 1㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 가열하는데, 고정측 주형(11)에서 이동측 주형(12)으로 3∼4분간 가열한 후 편석을 방지하기 위해 배기한다. 다시 이동측 주형(12)에서 고정측 주형(11)으로 3∼6분간 스팀을 공급하여 양면가열을 한후 배기하고, 이동측 주형(12)에서 고정측 주형(11)으로 3∼5분간 가열하는 보조가열의 3단계 가열방식으로 가열한다. 다음에는, 잔류하는 스팀을 완전히 제거하고 냉각수를 사용하여 냉각하며, 역으로 진공을 걸어서 방냉시킨 후 주형(11,12)에 공기를 분사하여 이형시키게 된다.The filled pre-expanded beads are heated with a pressure of 0.5 to 2 kg / cm 3, preferably 1 kg / cm 3 and steam at a temperature of 180 to 230 ° C., from the fixed side mold 11 to the moving side mold 12. After heating for 4 minutes, it is evacuated to prevent segregation. After supplying steam from the moving side mold 12 to the fixed side mold 11 for 3 to 6 minutes, the both sides are heated and then exhausted, and the moving side mold 12 is heated to the fixed side mold 11 for 3 to 5 minutes. Heat by 3 steps of heating method of auxiliary heating. Next, the remaining steam is completely removed and cooled using a cooling water, and the vacuum is allowed to stand to cool, and then air is injected into the molds 11 and 12 for release.

하기에서는 본 발명의 실시 예들을 간략하게 설명한다.Hereinafter, embodiments of the present invention will be briefly described.

〈실시예 1〉<Example 1>

입도 0.6∼0.9㎜의 저발포용 EPS(금호석유화학의 LEND-10) 40㎏을 상부에 호퍼와 내부 중심에 나선형 회전날개가 부착된 발포 용기에 넣고 압력 0.2㎏/㎤, 온도 200℃의 스팀을 공급하였다. 스팀을 분사하는 노즐 부위의 온도는 92℃로 조절하고, 발포 용기 내부의 온도는 80℃로 조절하였다. 10분마다 5,200㏄의 계량컵으로 계량하여 발포체의 무게를 재어 2.8배율이 되었을 때, 건조로로 이송시켜서 건조시켰다.40 kg of low-foaming EPS (LEND-10 from Kumho Petrochemical) with a particle size of 0.6 to 0.9 mm is placed in a foam container with a hopper and a spiral rotary wing attached to the inner center at the top of a steam of 0.2 kg / cm 3 and a temperature of 200 ° C. Was supplied. The temperature of the nozzle part which sprays steam was adjusted to 92 degreeC, and the temperature inside foaming container was adjusted to 80 degreeC. The foam was weighed every 5 minutes with a measuring cup of 5,200 mm 3, and when it reached 2.8 magnification, it was transferred to a drying furnace and dried.

주형은 스팀으로 미리 예비 가열을 해 두고, 발포 비이드를 주형에 충전하였다. 충전된 발포 비이드를 압력 1㎏/㎤, 온도 200℃의 스팀으로 가열하는데, 고정측 주형에서 이동측 주형으로 220초 가열 후 배기하고, 다시 이동측 주형에서 고정측 주형으로도 가열하는 보조가열을 180초간 시행하였다. 배기하여 잔류하는 스팀을 완전히 제거하고 냉각수를 사용하여 냉각하고, 역으로 진공을 걸어 방냉시킨 후 이동측 주형에 먼저 공기를 분사하여 주형을 열고 다시 고정측 주형에 공기를 분사하여 이형시켜 성형체를 제조하였다. 이렇게 제조된 성형체의 밀도는 0.357g/㏄였다.The mold was preheated with steam in advance and filled with foam beads. The filled foam beads are heated by steam having a pressure of 1 kg / cm 3 and a temperature of 200 ° C., which is heated for 220 seconds from the fixed mold to the movable mold and then evacuated, and is further heated from the movable mold to the fixed mold. Was performed for 180 seconds. Exhaust steam is completely removed by exhaust and cooled by using cooling water, and then vacuum is cooled by cooling. After that, air is first blown into the moving mold, the mold is opened, and then air is blown into the fixed mold to release the molded body. It was. The density of the molded product thus prepared was 0.357 g / cc.

〈실시예 2〉<Example 2>

입도 0.6∼0.9㎜의 저발포용 EPS(금호석유화학의 LEND-10) 40㎏을 상부에 호퍼와 내부 중심에 나선형 회전날개가 부착된 발포 용기에 넣고 압력 0.2㎏/㎤, 온도 200℃의 스팀을 공급하였다. 스팀을 분사하는 노즐 부위의 온도는 92℃로 조절하고, 발포 용기 내부의 온도는 80℃로 조절하였다. 10분마다 5,200㏄ 계량컵으로 계량하여 발포체의 무게를 재어 3.1배율이 되었을 때, 건조로로 이송시켜 건조시켰다.40 kg of low-foaming EPS (LEND-10 from Kumho Petrochemical) with a particle size of 0.6 to 0.9 mm is placed in a foam container with a hopper and a spiral rotary wing attached to the inner center at the top of a steam of 0.2 kg / cm 3 and a temperature of 200 ° C. Was supplied. The temperature of the nozzle part which sprays steam was adjusted to 92 degreeC, and the temperature inside foaming container was adjusted to 80 degreeC. The foam was weighed every 5 minutes by 5,200㏄ measuring cup, and when it reached 3.1 magnification, it was transferred to a drying furnace and dried.

주형은 스팀으로 미리 예비 가열을 해 두고, 발포 비이드를 주형에 충전하였다. 충전된 발포 비이드를 압력 1㎏/㎤, 온도 200℃의 스팀으로 가열하는데, 고정측 주형에서 이동측 주형으로 300초 가열 후 배기하고, 다시 이동측 주형에서 고정측 주형으로도 스팀을 공급하여 양면가열을 350초간 시행하고 배기한 후, 이동측 주형에서 고정측 주형으로 가열하는 보조가열을 250초간 시행하였다. 다음에는, 배기하여 잔류하는 스팀을 완전히 제거하고 냉각수를 사용하여 냉각하고, 역으로 진공을 걸어 방냉시킨 후 이동측 주형에 먼저 공기를 분사하여 주형을 열고 다시 고정측 주형에 공기를 분사하여 이형시켜 성형체를 제조하였다. 이렇게 제조된 성형체의 밀도는 0.320g/㏄였다.The mold was preheated with steam in advance and filled with foam beads. The filled foam beads are heated with steam at a pressure of 1 kg / cm 3 and a temperature of 200 ° C., and after 300 seconds of heating from the fixed side mold to the moving side mold, the steam is also supplied from the moving side mold to the fixed side mold. After 350 seconds of double-sided heating and evacuation, auxiliary heating was performed for 250 seconds from the moving mold to the fixed mold. Next, exhaust steam is completely removed, and the remaining steam is cooled and cooled by cooling. The vacuum is then allowed to cool, and then the air is first blown to the moving mold, the mold is opened, and then the air is blown to the fixed mold to release the mold. A molded article was prepared. The density of the molded product thus prepared was 0.320 g / cc.

도 2는 본 발명에 의해서 제조된 폴리스티렌 수지 발포 성형체의 사시도이고, 도 3a는 평면도이며, 도 3b는 저면도이다.2 is a perspective view of a polystyrene resin foam molded article produced by the present invention, FIG. 3A is a plan view, and FIG. 3B is a bottom view.

도 2 내지 도 3b에 도시된 바와 같이, 본 발명에 의해서 제조된 폴리스티렌 수지 발포 성형체인 자동 이송 장치의 운송 박스(30)는 일체로 이루어진 바닥(32)과 측벽(34)을 포함한다. 바닥(32)에는 자동 이송 라인에서의 운송 박스(30)의 위치선정을 위한 한쌍의 관통공(36)이 형성된다. 관통공(36)은 응력 발생시의 변형방지를 위해서 원형으로 형성된다. 관통공(36)이 사각형상으로 형성되면, 사각형상의 모서리 부분에 응력이 집중하게 되어 균열이 쉽게 발생하기 때문에, 관통공(36)은 원형으로 형성하는 것이 바람직하다.As shown in Figs. 2 to 3B, the transport box 30 of the automatic transport apparatus, which is a polystyrene resin foam molded article manufactured by the present invention, includes an integral bottom 32 and side walls 34. The bottom 32 is provided with a pair of through holes 36 for positioning the transport box 30 in the automatic transfer line. The through hole 36 is formed in a circular shape to prevent deformation during stress generation. When the through holes 36 are formed in a rectangular shape, the stress is concentrated on the rectangular corners, and cracks easily occur. Therefore, the through holes 36 are preferably formed in a circular shape.

운송 박스(30)의 내측에서, 바닥(32)과 측벽(34)의 경계가 되는 내측 모서리부(38)는 응력 발생시의 변형방지를 위해서 일정한 곡률반경(R)으로 만곡되게 형성된다. 내측 모서리부(38)를 만곡되게 형성하면, 내측 모서리부(38)에 가해지는 응력이 바닥(34)과 측벽(34) 쪽으로 분산되어 균열의 발생을 효과적으로 예방할 수 있게된다. 측벽(34)의 내측과 외측에는 강도의 보강을 위한 다수의 보강 리브(39)가 형성된다.Inside the transport box 30, the inner edge portion 38, which is the boundary between the bottom 32 and the side wall 34, is formed to be curved with a constant radius of curvature R to prevent deformation during stress generation. When the inner edge portion 38 is formed to be curved, the stress applied to the inner edge portion 38 is dispersed toward the bottom 34 and the side wall 34 to effectively prevent the occurrence of cracks. On the inside and outside of the side wall 34, a plurality of reinforcing ribs 39 are formed for reinforcing strength.

이와같이 형성된 자동 이송 장치의 운송 박스(30)는 종래의 운송 박스에 비해서 응력 발생시의 변형정도가 작으며, 운송 박스의 위치선정을 위한 관통공의 수가 적고 중앙 부위에 노치(notch)가 형성되어 있지 않아서 제조비용이 절감된다.The transport box 30 of the automatic transport device formed as described above has a smaller degree of deformation during stress generation than the conventional transport box, a small number of through holes for positioning the transport box, and a notch is formed in the center portion. Manufacturing cost is reduced.

이상에서 설명한 바와 같이, 본 발명에 따르면, 가열에 필요한 연료소모가 적고 방대한 시설투자가 필요하지 않을 뿐 아니라 온도조절이 용이하여 정확한 배율의 발포체를 제조할 수 있다. 또한, 성형체 전체의 밀도가 동일하게 되고 밀도가 높은 고강도의 성형체를 제조할 수 있다. 본 발명에 의해 제조된 폴리스티렌 발포 성형체는, 예를 들어 자동 이송 장치의 운송 박스와 같이 여러차례 반복사용이 필요하고 내구성이 필요한 성형체에 특히 유용하다.As described above, according to the present invention, the fuel consumption required for heating is low, a large amount of facility investment is not required, and the temperature can be easily controlled to produce a foam having an accurate magnification. Moreover, the density of the whole molded object becomes the same, and a high density molded object with high density can be manufactured. The polystyrene foamed molded article produced by the present invention is particularly useful for molded articles requiring repeated use several times and requiring durability, such as, for example, a transport box of an automatic transfer device.

상기에서는 본 발명의 바람직한 실시예를 참조하여 설명하였지만, 해당기술 분야의 숙련된 당업자는 하기의 특허 청구 범위에 기재된 본 발명의 사상 및 영역으로부터 벗어나지 않는 범위내에서 본 발명을 다양하게 수정 및 변경시킬 수 있음을 이해할 수 있을 것이다.Although the above has been described with reference to a preferred embodiment of the present invention, those skilled in the art will be able to variously modify and change the present invention without departing from the spirit and scope of the invention as set forth in the claims below. It will be appreciated.

Claims (4)

교반 장치가 부착된 발포 용기에 발포성 폴리스티렌 수지를 넣고, 0.1∼0.5㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 직접 가열하여 발포시켜서 예비 발포 비이드를 얻는 단계(S1);Placing the expandable polystyrene resin in a foaming vessel with a stirring device, and foaming by directly heating with a pressure of 0.1 to 0.5 kg / cm 3 and steam at a temperature of 180 to 230 ° C. (S1); 상기 예비 발포 비이드를 건조로로 이송하여 건조시키는 단계(S2);Transferring the pre-expanded beads to a drying furnace to dry (S2); 건조된 발포 비이드를 예비 가열된 주형에 충전하는 단계(S3); 그리고Filling the dried foam beads into a preheated mold (S3); And 충전된 발포 비이드를 0.5∼2㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 가열한후 배기, 냉각 및 이형시키는 단계(S4)를 포함하는 것을 특징으로 하는 폴리스티렌 발포 성형체의 제조 방법.A method of producing a polystyrene foamed molded article comprising the step (S4) of heating the filled foam beads with a pressure of 0.5 to 2 kg / cm 3 and steam at a temperature of 180 to 230 ° C. and then evacuating, cooling, and releasing. 제 1 항에 있어서, 상기 단계(S4)에서, 상기 충전된 발포 비이드를 상기 스팀으로 가열할 때, 원하는 성형체의 두께에 따라 상기 스팀의 양을 변화시키는 것을 특징으로 하는 폴리스티렌 발포 성형체의 제조방법.The method of manufacturing a polystyrene foam molded article according to claim 1, wherein in the step S4, when the filled foam beads are heated with the steam, the amount of the steam is changed in accordance with a desired thickness of the molded article. . 제 2 항에 있어서, 상기 주형은 고정측 주형과 이동측 주형으로 구성되고, 상기 고정측 주형과 상기 이동측 주형은 이들 사이에 배치되는 발포체에 스팀을 공급하도록 규칙적으로 배열된 스팀 통과 게이트를 가지며, 상기 성형체의 두께가 얇은 부분에 대응하는 스팀 통과 게이트의 깊이는 상기 주형의 두께와 동일하고, 상기 성형체의 두께가 두꺼운 부분에 대응하는 스팀 통과 게이트는 입구쪽의 단면이 브이(V)자 모양이 되도록 확장되는 것을 특징으로 하는 폴리스티렌 발포 성형체의 제조방법.3. The mold of claim 2 wherein the mold is comprised of a stationary side mold and a moving side mold, wherein the stationary side mold and the moving side mold have steam passing gates arranged regularly to supply steam to the foam disposed therebetween. The depth of the steam passing gate corresponding to the thin part of the molded body is equal to the thickness of the mold, and the steam passing gate corresponding to the thick part of the molded body has a V-shaped cross section at the inlet side. Method for producing a polystyrene foam molded article characterized in that it is expanded to be. 발포 용기 내에 발포성 폴리스티렌 수지를 넣고, 0.1∼0.5㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 직접 가열하여 발포시켜서 예비 발포 비이드를 얻고, 이렇게 얻은 예비 발포 비이드를 건조시킨후, 예비 가열된 주형에 충전하여 0.5∼2㎏/㎤의 압력과 180∼230℃ 온도의 스팀으로 가열하고, 계속해서 배기, 냉각 및 이형시켜서 제조되며, 일체로 이루어진 바닥과 측벽을 포함하고, 상기 바닥에는 위치선정을 위한 한쌍의 원형 관통공이 형성되고, 상기 바닥과 상기 측벽의 경계가 되는 내측 모서리부는 응력 발생시의 변형방지를 위해서 일정한 곡률반경으로 만곡되게 형성되며, 상기 측벽의 내측과 외측에는 강도의 보강을 위한 다수의 보강 리브가 형성된 것을 특징으로 하는 폴리스티렌 발포 성형체.The foamed polystyrene resin was placed in a foaming vessel and foamed by directly heating with a pressure of 0.1 to 0.5 kg / cm 3 and steam at a temperature of 180 to 230 ° C. to obtain a preliminary foamed beads, and drying the thus obtained preliminary foamed beads, followed by preliminary It is prepared by filling a heated mold with a pressure of 0.5 to 2 kg / cm 3 and steam at a temperature of 180 to 230 ° C., followed by exhausting, cooling and releasing, and including an integral bottom and sidewalls. A pair of circular through-holes for positioning is formed, and inner corners, which border the bottom and the sidewalls, are curved to have a constant curvature radius to prevent deformation during stress generation, and strength reinforcement is provided inside and outside the sidewalls. Polystyrene foam molded article characterized in that a plurality of reinforcing ribs are formed for.
KR1019990033718A 1999-03-29 1999-08-16 Expandable polystyrene resin and a method of producing the same KR20000062119A (en)

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Publication number Priority date Publication date Assignee Title
KR101045682B1 (en) * 2009-10-28 2011-07-01 (주)폴머 Method for molding expanded polystyrene pulverized product and press molded product using same
KR101982976B1 (en) 2018-07-27 2019-08-28 유삼석 Plate type-expanded polystyrene molding method and plate type-expanded polystyrene molding equipment
KR20220110944A (en) * 2021-02-01 2022-08-09 김현식 Plastic Box Packaging Device

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JPH06315992A (en) * 1993-05-07 1994-11-15 Ibiden Co Ltd Production of foamed styrol molded object
JPH09267348A (en) * 1996-03-29 1997-10-14 Mitsubishi Electric Corp Styrene foamed molded object, mold for producing the same and drain pan
JPH10180884A (en) * 1996-12-27 1998-07-07 Daisen Kogyo:Kk Core vent unit
JPH1158531A (en) * 1997-08-18 1999-03-02 Sekisui Plastics Co Ltd Expansion molding device and embedded member for concrete slab which is molded using the same

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6046230A (en) * 1983-08-25 1985-03-13 Kanegafuchi Chem Ind Co Ltd Preparation of composite foamed body
KR900003736A (en) * 1988-08-26 1990-03-27 아오이 죠이치 IC card data processing system and its data processing method
JPH06315992A (en) * 1993-05-07 1994-11-15 Ibiden Co Ltd Production of foamed styrol molded object
JPH09267348A (en) * 1996-03-29 1997-10-14 Mitsubishi Electric Corp Styrene foamed molded object, mold for producing the same and drain pan
JPH10180884A (en) * 1996-12-27 1998-07-07 Daisen Kogyo:Kk Core vent unit
JPH1158531A (en) * 1997-08-18 1999-03-02 Sekisui Plastics Co Ltd Expansion molding device and embedded member for concrete slab which is molded using the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101045682B1 (en) * 2009-10-28 2011-07-01 (주)폴머 Method for molding expanded polystyrene pulverized product and press molded product using same
KR101982976B1 (en) 2018-07-27 2019-08-28 유삼석 Plate type-expanded polystyrene molding method and plate type-expanded polystyrene molding equipment
KR20220110944A (en) * 2021-02-01 2022-08-09 김현식 Plastic Box Packaging Device

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