KR20030088670A - Method for preparing of polyethylene foam by rotational molding - Google Patents
Method for preparing of polyethylene foam by rotational molding Download PDFInfo
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- KR20030088670A KR20030088670A KR1020020026493A KR20020026493A KR20030088670A KR 20030088670 A KR20030088670 A KR 20030088670A KR 1020020026493 A KR1020020026493 A KR 1020020026493A KR 20020026493 A KR20020026493 A KR 20020026493A KR 20030088670 A KR20030088670 A KR 20030088670A
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- polyethylene foam
- granules
- powder
- producing
- foam
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- 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
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/02—Shaping 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
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- 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
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/02—Shaping 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
- B29C44/04—Shaping 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 consisting of at least two parts of chemically or physically different materials, e.g. having different densities
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- 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
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/02—Shaping 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
- B29C44/04—Shaping 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 consisting of at least two parts of chemically or physically different materials, e.g. having different densities
- B29C44/0423—Shaping 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 consisting of at least two parts of chemically or physically different materials, e.g. having different densities by density separation
- B29C44/043—Shaping 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 consisting of at least two parts of chemically or physically different materials, e.g. having different densities by density separation using a rotating mould
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- 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
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/3415—Heating or cooling
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- 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
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/58—Moulds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/06—PE, i.e. polyethylene
- B29K2023/0608—PE, i.e. polyethylene characterised by its density
- B29K2023/0633—LDPE, i.e. low density polyethylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/06—PE, i.e. polyethylene
- B29K2023/0608—PE, i.e. polyethylene characterised by its density
- B29K2023/065—HDPE, i.e. high density polyethylene
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Moulding By Coating Moulds (AREA)
Abstract
Description
[산업상 이용분야][Industrial use]
본 발명은 폴리에틸렌 발포체의 제조 방법에 관한 것으로, 더욱 상세하게는 기존의 연질 및 경질 폴리에틸렌 플라스틱에 발포성을 부가하여 단열재 및 방음재 등에 사용할 수 있는 폴리에틸렌 발포체의 제조 방법에 관한 것이다.The present invention relates to a method for producing a polyethylene foam, and more particularly to a method for producing a polyethylene foam that can be used to heat insulation and sound insulation by adding foamability to existing soft and hard polyethylene plastics.
[종래 기술][Prior art]
일반적으로 외피는 경질이고, 내피는 연질인 2층 구조의 플라스틱 폼 수지를 구조적인 폼 수지(structural foam resin)라고 한다. 이러한 구조적인 폼 수지는 천연 목재의 성질과 유사하여 일명 합성 목재라 한다.In general, a two-layered plastic foam resin with a hard outer shell and a soft inner shell is called a structural foam resin. This structural foam resin is called synthetic wood because it is similar to that of natural wood.
이러한 구조적인 폼 수지는 먼저 발포체를 사용하지 않는다는 점에서 기존의 폼 수지와는 상이하고, 그 물성에 있어서 견고도가 높고, 싱크 마크(sink mark)가 없으며 재료를 절감할 수 있다는 장점이 있다.This structural foam resin is different from the conventional foam resin in that it does not use a foam first, and has the advantages of high rigidity in physical properties, no sink mark, and material saving.
종래 이러한 2층 구조의 구조적인 폼 수지는 저압 발포 및 고압 발포 등으로 사출 성형 공정으로 제조하는 것이 일반적이었다.Conventionally, such a two-layered structural foam resin has been generally manufactured by injection molding by low pressure foaming and high pressure foaming.
그러나, 이상과 같은 사출성형 공정에 의한 구조적인 폼 수지의 제조는 제조된 수지의 물성이 나쁘거나 후처리 공정 등이 필요함에 따라 제조 원가가 상승한다는 단점이 있었다.However, the production of the structural foam resin by the injection molding process as described above has a disadvantage in that the manufacturing cost increases due to bad physical properties of the produced resin or post-treatment process.
이와 같은 단점을 해결하기 위하여 회전성형(rotational molding) 공정이 개발되었다.In order to solve this disadvantage, a rotational molding process has been developed.
종래의 회전성형공정은 플라스틱 분말을 사용하고, 이것을 밀폐시킨 금형에 투입하여 2축으로 회전하면서 열풍 등으로 가열하는 것이지만 2축 회전이기 때문에 넓은 장소를 요구하고 비효율적이고 또한 열풍이 현저히 높은 온도이기 때문에 금형 온도가 부분적으로 다르고, 성형된 성형체에 균열이 발생하며 강도가 불충분하므로 바람을 받기 쉬운 부분이 열등에 의해 열화되기 때문에 복잡한 형태와 구조의 성형 발포체 및 복합 성형체의 제조가 불가능하였다.The conventional rotational molding process uses plastic powder, and puts it in a sealed mold and heats it with hot air while rotating in two axes, but since it is biaxial rotation, it requires a large place and is inefficient and has a significantly high temperature. Since the mold temperature is partially different, cracks are formed in the molded body, and the strength is insufficient, it is impossible to manufacture molded foams and composite molded bodies having a complicated shape and structure because the vulnerable parts are degraded by inferiority.
미국 특허 제3,814,778호에서는 분말 플라스틱과 10 메쉬보다 큰 가교 발포성의 입상체를 금형에 약 90 % 이하로 투입하여 회전속도가 0.1 내지 1.5 m/분의 속도로 회전하면서 가열하고, 분말 플라스틱에 의해 표피와 그 내측에 발포체가 충만된 복합 성형체의 제조 방법을 개시하고 있다. 그러나, 이 방법은 제조된 복합성형체의 제조 방법이지만 특수한 복합성형체의 제조에 한정되는 것이다.In U.S. Patent No. 3,814,778, powdered plastics and crosslinked foamable granules larger than 10 mesh are introduced into the mold at about 90% or less, and the rotating speed is heated at a speed of 0.1 to 1.5 m / min. And a method for producing a composite molded article filled with a foam therein. However, this method is a method for producing the manufactured composite molded product, but is limited to the production of a special composite molded product.
미국 특허 제3,914,361호에서는 분말 플라스틱과 입경이 30배 이상인 발포 입상체를 밀폐시킨 밸브를 갖는 금형에 투입하고 15 m/분 이하의 속도로 금형을 회전시키고 외부보다 높은 온도의 수증기로 100 내지 250 ℃로 가열하고, 분말 플라스틱에 의해 표피를 생성시키고, 발포 입상체를 발포시키고, 내부에 있는 가스를밸브에 의해 분산시켜서 냉각한 발포 입상체의 제조 방법을 개시하고 있다. 그러나, 이 특허에서도 제조된 복합성형체의 제조 방법이지만 특정의 복합성형체의 제조 방법에 한정된다는 단점이 있다.U.S. Patent No. 3,914,361 discloses a mold having a valve sealing a powdered plastic and a foamed granule having a particle diameter of 30 times or more, rotating the mold at a speed of 15 m / min or less and steaming at a temperature of 100 to 250 DEG C with a higher temperature than the outside. A method for producing a foamed granule is disclosed, which is heated by heating to form a skin by powdered plastic, foamed foamed granules, and gas dispersed therein by a valve. However, this patent also has a disadvantage in that the method for producing a composite molded product is limited to a method for producing a specific composite molded product.
본 발명은 위에서 설명한 바와 같은 문제점을 해결하기 위하여 안출된 것으로서, 본 발명의 목적은 회전 성형 공정을 이용하여 폴리에틸렌 성형 발포체를 제조하기 위한 방법을 제공하는 것이다.SUMMARY OF THE INVENTION The present invention has been made to solve the problems as described above, and an object of the present invention is to provide a method for producing polyethylene molded foam using a rotational molding process.
본 발명은 상기한 목적을 달성하기 위하여, 본 발명은The present invention to achieve the above object, the present invention
고밀도 폴리에틸렌 분말과 저밀도 폴리에틸렌 입상체를 10 : 1 내지 1 : 10 의 비율로 금형에 동시에 투입하는 단계;Simultaneously injecting the high density polyethylene powder and the low density polyethylene granules into the mold at a ratio of 10: 1 to 1:10;
상기 분말과 입상체를 3.0 내지 5.0 RPM의 속도로 회전시키면서 온도 110 내지 160 ℃ 로 10 내지 20 분 동안 가열 용융시키는 단계; 및Heating and melting the powder and granules at a temperature of 110 to 160 ° C. for 10 to 20 minutes while rotating at a speed of 3.0 to 5.0 RPM; And
상기 속도를 유지하면서 상기 분말과 입상체의 가열 용융 온도를 160 내지 200 ℃로 하여 10 내지 20 분 동안 가열 용융시키는 단계Heating and melting the powder and the granules at a temperature of 160 to 200 ° C. for 10 to 20 minutes while maintaining the speed;
를 포함하는 것을 특징으로 하는 폴리에틸렌 발포체의 제조 방법을 제공한다.It provides a method for producing a polyethylene foam comprising a.
이하, 본 발명을 첨부한 도면을 참조하여 상세히 설명한다.Hereinafter, with reference to the accompanying drawings, the present invention will be described in detail.
본 발명에서는 고밀도 폴리에틸렌(HDPE)과 저밀도 폴리에틸렌(LDPE)을 혼합사용하여 고밀도 폴리에틸렌의 분말과 저밀도 폴리에틸렌 입상체를 회전 성형함으로써 폴리에틸렌 발포체를 얻을 수 있다.In the present invention, a polyethylene foam can be obtained by rotationally molding a powder of high density polyethylene and a low density polyethylene granule using a mixture of high density polyethylene (HDPE) and low density polyethylene (LDPE).
본 발명에 의한 폴리에틸렌 발포체는 다음과 같이 제조된다.The polyethylene foam according to the invention is produced as follows.
먼저, 고밀도 폴리에틸렌(High Density Polyethylene: HDPE)의 분말과 저밀도 폴리에틸렌(Low Density Polyethylene: LDPE)의 입상체를 동시에 금형에 넣어서 금형을 회전하면서 가열한다.First, the powder of high density polyethylene (HDPE) and the granules of low density polyethylene (LDPE) are simultaneously put into a mold and heated while rotating the mold.
분말과 입상체를 동시에 넣어서 회전시키면서 편석 효과와 입상체의 표면적의 크기에 따른 열전도의 차이가 심한 것을 이용하여 분말은 금형에서 열에 의해 용융되고 입상체는 나중에 용융되면서 발포가 이루어지므로 2중 성형이 자연스럽게 이루어진다.The powder is melted by heat in the mold and foamed while the granules are melted later by using the one with a large difference in segregation effect and the size of the surface area of the granules while rotating the powder and the granules at the same time. It happens naturally.
따라서, 고밀도 폴리에틸렌과 저밀도 폴리에틸렌의 층을 구별하여 성형할 수 있다.Therefore, the layer of high density polyethylene and low density polyethylene can be distinguished and shape | molded.
이때, 저온에서 고온으로 고밀도 폴리에틸렌은 130 내지 200 ℃에서 발포가 이루어지고, 저밀도 폴리에틸렌은 110 내지 180 ℃에서 발포가 이루어지므로, 약 110 내지 200 ℃로 저온에서 고온으로 약 10 내지 40분간 가열하는 것이 바람직하다. 더욱 바람직하기로는 약 110 내지 160 ℃의 온도에서 약 10 내지 20분간 가열한 후, 160 내지 200 ℃의 온도에서 약 10 내지 20분간 가열하는 것이 바람직하다.At this time, since the high-density polyethylene is foamed at a low temperature to a high temperature at 130 to 200 ℃, low-density polyethylene is foamed at 110 to 180 ℃, it is about 10 to 40 minutes to heat to a high temperature at a low temperature from about 110 to 200 ℃ desirable. More preferably, the heating is performed at a temperature of about 110 to 160 ° C. for about 10 to 20 minutes, and then at a temperature of 160 to 200 ° C. for about 10 to 20 minutes.
그리고, 고밀도 폴리에틸렌과 저밀도 폴리에틸렌의 투입 비율은 10 : 1 내지 1 : 10이 바람직하며, 더욱 바람직하기로는 약 3 : 1인 것이 바람직하다.In addition, the addition ratio of the high density polyethylene and the low density polyethylene is preferably from 10: 1 to 1:10, more preferably from about 3: 1.
또한, 가열 방법은 버너의 화염을 직접 금형에 가열하여 금형을 달구어서 온도를 높이고, 사용되는 연료는 주로 LPG 또는 LNG를 사용한다.In addition, the heating method is to heat the flame of the burner directly to the mold to heat the mold to increase the temperature, the fuel used is mainly LPG or LNG.
한편, 금형의 주위에 원형의 레일을 만들어서 모터에 의해 회전시키면 축은 없으나 회전의 중심이 축의 역할을 하므로 회전성형이 가능하게 된다. 따라서, 금형을 180 내지 360 °로 회전시키면서 금형 전체가 열을 받아 성형되도록 한다. 바람직하기로는 금형 회전의 중심이 좌우 45 °씩 경사각을 이루도록 하여 전체 금형이 열을 받아 성형될 수 있도록 하는 구조를 채택하는 것이 바람직하다.On the other hand, when a circular rail is made around the mold and rotated by a motor, there is no axis, but rotational rotation is possible because the center of rotation plays a role of the axis. Therefore, the entire mold is formed by receiving heat while rotating the mold at 180 to 360 °. Preferably, it is preferable to adopt a structure in which the center of the mold rotation forms an inclination angle of 45 ° left and right so that the entire mold can be molded by receiving heat.
그리고, 성형 발포체의 성상을 향상시키기 위하여, 용도에 따라 산화방지제, 자외선 차단제, 대전 방지제, 착색제, 충진제등을 더욱 첨가하여 제조할 수 있다.And in order to improve the property of a molded foam, it can manufacture by adding an antioxidant, a sunscreen, an antistatic agent, a coloring agent, a filler, etc. according to a use.
상기 산화방지제는 0.1 내지 1 %, 자외선 차단제는 0.1 내지 2 %, 대전 방지제는 2 내지 4 %, 착색제는 5 내지 10 %, 충진제는 10 내지 25 %를 사용하는 것이 바람직하다.0.1 to 1% of the antioxidant, 0.1 to 2% of the sunscreen, 2 to 4% of the antistatic agent, 5 to 10% of the colorant, 10 to 25% of the filler is preferably used.
본 발명에 따른 제조 방법을 채용하는 경우에는 동시에 2중 재질의 폴리에틸렌 발포체의 성형이 가능하게 된다. 또한, 제조된 발포체 표피의 두께는 1 내지 10 mm이고, 발포체 내부의 두께는 발포체의 용도에 따라 10 내지 200 mm가 가능하다.In the case of employing the production method according to the present invention, it is possible to simultaneously mold the polyethylene foam of the double material. In addition, the thickness of the prepared foam skin is 1 to 10 mm, and the thickness inside the foam may be 10 to 200 mm depending on the use of the foam.
이하, 본 발명의 바람직한 일실시예를 제시한다. 다만, 하기하는 실시예는 본 발명의 이해를 돕기 위하여 제시되는 것일 뿐 본 발명이 하기하는 실시예에 한정되는 것은 아니다.Hereinafter, a preferred embodiment of the present invention. However, the following examples are only presented to aid the understanding of the present invention, and the present invention is not limited to the following examples.
실시예 1Example 1
용량이 400 ℓ인 회전 성형 금형에 고밀도 폴리에틸렌과 저밀도 폴리에틸렌의 비가 3 : 1로 하여 전체 혼합량이 금형의 10 %가 되도록 투입하였다. 그리고나서, 회전 금형의 경사각을 수직축을 중심으로 하여 45 °로 하여 110 내지 120 ℃에서 약 5 RPM으로 약 20분간 가열한 후 180 내지 190 ℃에서 20분간 가열하였다.A high density polyethylene and a low density polyethylene ratio of 3: 1 were placed in a rotary molding die having a capacity of 400 L so that the total mixing amount was 10% of the mold. Then, the inclination angle of the rotating die was set at 45 ° about the vertical axis and heated at 110 to 120 ° C. for about 20 minutes at about 5 RPM, followed by heating at 180 to 190 ° C. for 20 minutes.
실시예 2Example 2
실시예 1과 동일한 방법으로 발포체를 제조하였으나, 자외선 차단제 0.5 %, 산화방지제 0.3 %, 착색제 10 %를 배합하여 첨가제 혼합물을 제조하고 이 혼합물을 고밀도 폴리에틸렌과 저밀도 폴리에틸렌의 혼합물의 5 %를 투입하여 발포체를 제조하였다.A foam was prepared in the same manner as in Example 1, except that 0.5% of a sunscreen, 0.3% of an antioxidant, and 10% of a colorant were mixed to prepare an additive mixture, and 5% of a mixture of high density polyethylene and low density polyethylene was added to the foam. Was prepared.
이상과 설명한 바와 같이, 본 발명에 의한 발포체 제조 방법으로 성형 발포체를 제조하는 경우 플라스틱 표피가 있는 단열재, 방음재를 제조할 수 있으며, 이에 따라 충격에 의해 표피가 쉽게 부숴지지 않고, 내습성, 흡음 및 차음 효과 등이 우수하며, 성형물의 크기에 따른 성형이 용이하며 구조가 간단하거나 복잡해도 성형을 용이하게 제조할 수 있다.As described above, when the molded foam is manufactured by the foam manufacturing method according to the present invention, it is possible to manufacture a heat insulating material and a sound insulation with a plastic skin, so that the skin is not easily broken by impact, and moisture resistance, sound absorption and It is excellent in sound insulation effect, and the molding is easy according to the size of the molding, even if the structure is simple or complicated, the molding can be easily produced.
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KR20140146169A (en) * | 2012-04-23 | 2014-12-24 | 도요세이칸 그룹 홀딩스 가부시키가이샤 | Foamed stretched plastic bottle |
KR101720207B1 (en) | 2015-10-22 | 2017-03-27 | 유한회사 가야미 | Tractor for loop using a foaming rotational molding and method for manufacturing the same |
KR20170070407A (en) * | 2015-12-14 | 2017-06-22 | 현대자동차주식회사 | Urea tank integrated with feul tank and method for manufacturing it |
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JPH0232836A (en) * | 1988-07-22 | 1990-02-02 | Mitsubishi Petrochem Co Ltd | Preparation of multi-layered molded item containing foamed layer by means of rotational molding |
JPH08224746A (en) * | 1995-02-21 | 1996-09-03 | Tadaaki Shiina | Production of foamed composite having sections |
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US3542912A (en) * | 1967-12-12 | 1970-11-24 | Nypel Inc | Rotational molding method for forming multilayered articles |
US3814778A (en) * | 1971-08-26 | 1974-06-04 | Furukawa Electric Co Ltd | Method for producing a composite foamed article |
JPH0232836A (en) * | 1988-07-22 | 1990-02-02 | Mitsubishi Petrochem Co Ltd | Preparation of multi-layered molded item containing foamed layer by means of rotational molding |
JPH08224746A (en) * | 1995-02-21 | 1996-09-03 | Tadaaki Shiina | Production of foamed composite having sections |
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Publication number | Priority date | Publication date | Assignee | Title |
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KR20140146169A (en) * | 2012-04-23 | 2014-12-24 | 도요세이칸 그룹 홀딩스 가부시키가이샤 | Foamed stretched plastic bottle |
KR101720207B1 (en) | 2015-10-22 | 2017-03-27 | 유한회사 가야미 | Tractor for loop using a foaming rotational molding and method for manufacturing the same |
KR20170070407A (en) * | 2015-12-14 | 2017-06-22 | 현대자동차주식회사 | Urea tank integrated with feul tank and method for manufacturing it |
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