KR20230158162A - Manufacturing method of eco-friendly container with excellent chemical resistance - Google Patents

Manufacturing method of eco-friendly container with excellent chemical resistance Download PDF

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KR20230158162A
KR20230158162A KR1020220057422A KR20220057422A KR20230158162A KR 20230158162 A KR20230158162 A KR 20230158162A KR 1020220057422 A KR1020220057422 A KR 1020220057422A KR 20220057422 A KR20220057422 A KR 20220057422A KR 20230158162 A KR20230158162 A KR 20230158162A
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eco
friendly
weight
chemical resistance
parts
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KR1020220057422A
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Korean (ko)
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정재우
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대흥 아이 비 엔 주식회사
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    • 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
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/02Combined blow-moulding and manufacture of the preform or the parison
    • B29C49/06Injection blow-moulding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B11/00Making preforms
    • B29B11/06Making preforms by moulding the material
    • B29B11/08Injection moulding
    • 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
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/18Feeding the material into the injection moulding apparatus, i.e. feeding the non-plastified material into the injection unit
    • 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
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/18Feeding the material into the injection moulding apparatus, i.e. feeding the non-plastified material into the injection unit
    • B29C45/1866Feeding multiple materials
    • 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
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/76Measuring, controlling or regulating
    • B29C45/77Measuring, controlling or regulating of velocity or pressure of moulding material
    • 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
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/0005Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor characterised by the material
    • 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
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/64Heating or cooling preforms, parisons or blown articles
    • 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
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/06PE, i.e. polyethylene
    • B29K2023/0608PE, i.e. polyethylene characterised by its density
    • B29K2023/065HDPE, i.e. high density polyethylene
    • 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
    • B29K2027/00Use of polyvinylhalogenides or derivatives thereof as moulding material
    • B29K2027/12Use of polyvinylhalogenides or derivatives thereof as moulding material containing fluorine
    • B29K2027/18PTFE, i.e. polytetrafluorethene, e.g. ePTFE, i.e. expanded polytetrafluorethene
    • 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
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0032Pigments, colouring agents or opacifiyng agents
    • 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
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0044Stabilisers, e.g. against oxydation, light or heat
    • 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
    • B29K2503/00Use of resin-bonded materials as filler
    • B29K2503/04Inorganic materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00Other particular articles
    • B29L2031/712Containers; Packaging elements or accessories, Packages

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Containers Having Bodies Formed In One Piece (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

본 발명은 내약품성이 우수한 친환경 용기의 제조방법에 관한 것으로, 더욱 상세하게는 고밀도폴리에틸렌, 친환경 충전재 및 착색제를 혼합하는 원료혼합단계, 상기 원료혼합단계를 통해 제조된 혼합물을 사출블로우성형기에 투입하고 용융하는 용융단계, 상기 용융단계를 통해 용융된 혼합물을 사출하는 사출단계, 상기 사출단계를 통해 사출된 혼합물을 블로우성형하는 블로우성형단계 및 상기 블로우성형단계를 통해 제조된 성형물을 냉각하는 냉각단계로 이루어진다.
상기의 과정을 통해 제조되는 용기는 기계적 물성, 내약품성 및 외관품질이 우수할 뿐만 아니라, 계란껍질로 제조된 탄산칼슘이 사용되어 친환경적인 효과를 나타낸다.
The present invention relates to a method of manufacturing an eco-friendly container with excellent chemical resistance, and more specifically, to a raw material mixing step of mixing high-density polyethylene, eco-friendly filler and colorant, and injecting the mixture prepared through the raw material mixing step into an injection blow molding machine. A melting step, an injection step of injecting the molten mixture through the melting step, a blow molding step of blow molding the mixture injected through the injection step, and a cooling step of cooling the molded product manufactured through the blow molding step. It comes true.
Containers manufactured through the above process not only have excellent mechanical properties, chemical resistance, and appearance quality, but also have an environmentally friendly effect because calcium carbonate made from eggshell is used.

Description

내약품성이 우수한 친환경 용기의 제조방법 {MANUFACTURING METHOD OF ECO-FRIENDLY CONTAINER WITH EXCELLENT CHEMICAL RESISTANCE}Method for manufacturing eco-friendly containers with excellent chemical resistance {MANUFACTURING METHOD OF ECO-FRIENDLY CONTAINER WITH EXCELLENT CHEMICAL RESISTANCE}

본 발명은 내약품성이 우수한 친환경 용기의 제조방법에 관한 것으로, 더욱 상세하게는 기계적 물성, 내약품성 및 외관품질이 우수할 뿐만 아니라, 계란껍질로 제조된 탄산칼슘이 사용되어 친환경적인 용기를 제공하는 내약품성이 우수한 친환경 용기의 제조방법에 관한 것이다.The present invention relates to a method of manufacturing an eco-friendly container with excellent chemical resistance, and more specifically, to provide an eco-friendly container that not only has excellent mechanical properties, chemical resistance, and appearance quality, but also uses calcium carbonate made from eggshells. This relates to a method of manufacturing eco-friendly containers with excellent chemical resistance.

화학물질이나 약품을 담는 용도로는 내약품성이 우수한 폴리에틸렌 용기가 주로 사용되는데, 그 내용물로는 예를 들면 불산, 황산, 염산, 질산, 인산, 과산화수소, 암모니아수, 페놀 등과 같은 용매나 세정에 이용되는 고순도 약품, 부동액, 유화제, 글리세롤, 글리세린, 라텍스, 폴리비닐알코올, 염료 등과 같은 비위험성 약품 및 과일 쥬스, 간장, 식초, 중성세제 등의 일상 생활에 이용되는 화학물질 등이 있다.Polyethylene containers with excellent chemical resistance are mainly used to contain chemicals or drugs. Their contents include solvents and cleaning agents such as hydrofluoric acid, sulfuric acid, hydrochloric acid, nitric acid, phosphoric acid, hydrogen peroxide, aqueous ammonia, and phenol. These include non-hazardous chemicals such as high-purity chemicals, antifreeze, emulsifiers, glycerol, glycerin, latex, polyvinyl alcohol, and dyes, as well as chemicals used in daily life such as fruit juice, soy sauce, vinegar, and neutral detergents.

이러한 약품을 담는 용기는 성분의 변화없이 장기간 보존할 수 있도록 하는 내약품성이 요구되며, 또한 용기로서 기본적 물성이라 할 수 있는 우수한 낙하 내충격성이 요구되는데, 이는 고순도 약품이 담긴 용기의 취급시 파손되는 경우 인체에 미칠 수 있는 위험성과 주변환경의 오염 또는 그 제거가 그리 용이하지 않다는 점 때문이다. 이에 따라, 낙하 내충격성을 높이기 위하여 용융장력, 중량평균분자량을 증가시키기 위한 노력이 이루어져 왔다.Containers containing these chemicals require chemical resistance that allows them to be stored for a long period of time without changing the composition, and also require excellent drop resistance, which is a basic physical property of the container, which can prevent damage when handling containers containing high-purity chemicals. This is because of the risk it may pose to the human body and the fact that it is not easy to pollute the surrounding environment or remove it. Accordingly, efforts have been made to increase melt tension and weight average molecular weight to increase drop impact resistance.

한국특허공개 제10-2002-0049130호에는 고순도 약품을 담는 중공성형체의 재질로 사용되는 폴리에틸렌계 수지조성물로서, 고하중(216kg, 190℃) 용융흐름지수(ASTM D1238 기준) 20g/10분 미만인 지글러 촉매 또는 크롬촉매에 의해 제조된 폴리에틸렌계 수지 65~95중량%와, 고하중 용융흐름지수 2~50g/10분 범위인 메타로 센촉매에 의해 제조된 폴리에틸렌계 수지 35~5중량%로 구성되는 이종 촉매에 의한 폴리에틸렌계 수지 조성물이 기재되어 있으며, Korean Patent Publication No. 10-2002-0049130 describes a polyethylene-based resin composition used as a material for hollow molds containing high-purity chemicals, and has a high load (216 kg, 190°C) melt flow index (ASTM D1238 standard) of less than 20 g/10 minutes. It consists of 65 to 95% by weight of polyethylene resin produced by a catalyst or chromium catalyst and 35 to 5% by weight of polyethylene resin produced by a metarosene catalyst with a high load melt flow index in the range of 2 to 50 g/10 minutes. A polyethylene-based resin composition using a heterogeneous catalyst is described,

한국특허공개 제10-2003-0066409호에는 밀도와 평균분자량을 증가시킨 고밀도폴리에틸렌을 제조하여 충격강도를 높이는 기술에 기재되어 있는데, 상기 수지는216kg하중으로 측정한 MFR과 216kg하중으로 측정한 MFR의 비(MFR216kg/MFR 216kg)가 200이하가 되도록 하였다.Korean Patent Publication No. 10-2003-0066409 describes a technology to increase impact strength by manufacturing high-density polyethylene with increased density and average molecular weight. The resin has MFR measured with a load of 216 kg and MFR measured with a load of 216 kg. The ratio (MFR216kg/MFR 216kg) was set to be less than 200.

그러나 상기와 같은 기술들은 비록 충격강도가 향상되는 장점을 갖는 반면, 용기 표면의 광택성을 향상시키지는 못하였고, 낙하충격강도 이외에 동적강성(Stiffness)을 향상되지 못하여 용기의 외관이 불량한 문제점이 있었다.However, although the above technologies have the advantage of improving impact strength, they do not improve the glossiness of the surface of the container, and they do not improve dynamic stiffness other than drop impact strength, so there is a problem that the appearance of the container is poor.

한국특허공개 제10-2002-0049130호(2002.06.26.)Korean Patent Publication No. 10-2002-0049130 (June 26, 2002) 한국특허등록 제10-0525702호(2005.10.26.)Korean Patent Registration No. 10-0525702 (2005.10.26.)

본 발명의 목적은 기계적 물성, 내약품성 및 외관품질이 우수할 뿐만 아니라, 계란껍질로 제조된 탄산칼슘이 사용되어 친환경적인 용기를 제조하는 내약품성이 우수한 친환경 용기의 제조방법을 제공하는 것이다.The purpose of the present invention is to provide a method for manufacturing an eco-friendly container that not only has excellent mechanical properties, chemical resistance, and appearance quality, but also has excellent chemical resistance by using calcium carbonate made from eggshells to manufacture an eco-friendly container.

본 발명의 목적은 고밀도폴리에틸렌, 친환경 충전재 및 착색제를 혼합하는 원료혼합단계, 상기 원료혼합단계를 통해 제조된 혼합물을 사출블로우성형기에 투입하고 용융하는 용융단계, 상기 용융단계를 통해 용융된 혼합물을 사출하는 사출단계, 상기 사출단계를 통해 사출된 혼합물을 블로우성형하는 블로우성형단계 및 상기 블로우성형단계를 통해 제조된 성형물을 냉각하는 냉각단계로 이루어지며, 상기 친환경 충전재는 계란껍질로 제조된 탄산칼슘인 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법을 제공함에 의해 달성된다.The purpose of the present invention is to include a raw material mixing step of mixing high-density polyethylene, eco-friendly filler and colorant, a melting step of feeding the mixture prepared through the raw material mixing step into an injection blow molding machine and melting it, and injection of the melted mixture through the melting step. It consists of an injection step, a blow molding step of blow molding the mixture injected through the injection step, and a cooling step of cooling the molded product manufactured through the blow molding step, and the eco-friendly filler is calcium carbonate made from eggshell. This is achieved by providing a method of manufacturing an eco-friendly container characterized by excellent chemical resistance.

본 발명의 바람직한 특징에 따르면, 상기 원료혼합단계는 고밀도폴리에틸렌 100 중량부, 친환경 충전재 40 내지 60 중량부 및 착색제 5 내지 15 중량부로 이루어지는 것으로 한다.According to a preferred feature of the present invention, the raw material mixing step is comprised of 100 parts by weight of high-density polyethylene, 40 to 60 parts by weight of eco-friendly filler, and 5 to 15 parts by weight of colorant.

본 발명의 더 바람직한 특징에 따르면, 상기 원료혼합단계에서는 상기 고밀도폴리에틸렌 100 중량부 대비 산화방지제 0.05 내지 0.2 중량부가 더 함유되며, 상기 산화방지제는 옥타데실-3-(3,5-디-터트-부틸-4-하이드록시페닐)프로피오네이트 및 트리스(2,4-디-터트-부틸페닐)포스파이트 및 옥시다이즈드 비스(하이드로제네이티드탈로우알킬)아민으로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것으로 한다.According to a more preferred feature of the present invention, in the raw material mixing step, an antioxidant of 0.05 to 0.2 parts by weight is further contained relative to 100 parts by weight of the high-density polyethylene, and the antioxidant is octadecyl-3-(3,5-di-tert- At least one selected from the group consisting of butyl-4-hydroxyphenyl)propionate and tris(2,4-di-tert-butylphenyl)phosphite and oxidized bis(hydrogenated tallowalkyl)amine. It is said to be done.

본 발명의 더욱 바람직한 특징에 따르면, 상기 원료혼합단계에서는 상기 고밀도폴리에틸렌 100 중량부 대비 테프론계 수지 0.5 내지 3 중량부가 더 함유되는 것으로 한다.According to a more preferred feature of the present invention, in the raw material mixing step, 0.5 to 3 parts by weight of Teflon-based resin is added compared to 100 parts by weight of the high-density polyethylene.

본 발명의 더욱 더 바람직한 특징에 따르면, 상기 테프론계 수지는 폴리테트라플루오로에틸렌, 에틸렌테트라플루오로에틸렌 공중합체 및 플루오르화에틸렌프로필렌 공중합체로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것으로 한다.According to an even more preferred feature of the present invention, the Teflon-based resin is made of at least one selected from the group consisting of polytetrafluoroethylene, ethylenetetrafluoroethylene copolymer, and fluorinated ethylenepropylene copolymer.

본 발명의 더욱 더 바람직한 특징에 따르면, 상기 친환경 충전재는 70 내지 80℃의 온도에서 40 내지 60분 동안 건조하여 사용되는 것으로 한다.According to an even more preferred feature of the present invention, the eco-friendly filler is used by drying at a temperature of 70 to 80° C. for 40 to 60 minutes.

본 발명의 더욱 더 바람직한 특징에 따르면, 상기 사출단계는 상기 용융단계를 통해 용융된 혼합물을 300 내지 400Psi의 압력으로 6 내지 8초 동안 사출금형에 주입하여 이루어지는 것으로 한다.According to an even more preferred feature of the present invention, the injection step is performed by injecting the mixture melted through the melting step into the injection mold for 6 to 8 seconds at a pressure of 300 to 400 Psi.

본 발명에 따른 내약품성이 우수한 친환경 용기의 제조방법은 기계적 물성, 내약품성 및 외관품질이 우수할 뿐만 아니라, 계란껍질로 제조된 탄산칼슘이 사용되어 친환경적인 용기를 제공하는 탁월한 효과를 나타낸다.The method of manufacturing an eco-friendly container with excellent chemical resistance according to the present invention not only has excellent mechanical properties, chemical resistance, and appearance quality, but also shows an excellent effect of providing an eco-friendly container by using calcium carbonate made from eggshell.

도 1은 본 발명에 따른 내약품성이 우수한 친환경 용기의 제조방법을 나타낸 순서도이다.Figure 1 is a flowchart showing a method of manufacturing an eco-friendly container with excellent chemical resistance according to the present invention.

이하에는, 본 발명의 바람직한 실시예와 각 성분의 물성을 상세하게 설명하되, 이는 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자가 발명을 용이하게 실시할 수 있을 정도로 상세하게 설명하기 위한 것이지, 이로 인해 본 발명의 기술적인 사상 및 범주가 한정되는 것을 의미하지는 않는다.Below, preferred embodiments of the present invention and the physical properties of each component are described in detail, but are intended to be described in detail so that those skilled in the art can easily practice the invention. This does not mean that the technical idea and scope of the present invention are limited.

본 발명에 따른 내약품성이 우수한 친환경 용기의 제조방법은 고밀도폴리에틸렌, 친환경 충전재 및 착색제를 혼합하는 원료혼합단계(S101), 상기 원료혼합단계(S101)를 통해 제조된 혼합물을 사출블로우성형기에 투입하고 용융하는 용융단계(S103), 상기 용융단계(S103)를 통해 용융된 혼합물을 사출하는 사출단계(S105), 상기 사출단계(S105)를 통해 사출된 혼합물을 블로우성형하는 블로우성형단계(S107) 및 상기 블로우성형단계(S107)를 통해 제조된 성형물을 냉각하는 냉각단계(S109)로 이루어진다.The method of manufacturing an eco-friendly container with excellent chemical resistance according to the present invention includes a raw material mixing step (S101) of mixing high-density polyethylene, eco-friendly fillers, and colorants, and the mixture prepared through the raw material mixing step (S101) is input into an injection blow molding machine. A melting step (S103) of melting, an injection step (S105) of injecting the mixture melted through the melting step (S103), a blow molding step (S107) of blow molding the mixture injected through the injection step (S105), and It consists of a cooling step (S109) of cooling the molded product manufactured through the blow molding step (S107).

상기 원료혼합단계(S101)는 고밀도폴리에틸렌, 친환경 충전재 및 착색제를 혼합하는 단계로, 고밀도폴리에틸렌 100 중량부, 친환경 충전재 40 내지 60 중량부 및 착색제 5 내지 15 중량부로 이루어지는 것이 바람직한다.The raw material mixing step (S101) is a step of mixing high-density polyethylene, eco-friendly filler, and colorant, and is preferably comprised of 100 parts by weight of high-density polyethylene, 40 to 60 parts by weight of eco-friendly filler, and 5 to 15 parts by weight of colorant.

상기 고밀도폴리에틸렌은 고하중 용융흐름지수는 50g/10분 이하이고, 중량평균분자량이 250000 내지 450000이며, 분자량분포도가 12 내지 25이고, MI216/MI216는 50~200이며, 밀도는 0.950g/㎤ 이상인 것을 사용하는 것이 바람직하다.The high-density polyethylene has a high-load melt flow index of 50 g/10 minutes or less, a weight average molecular weight of 250,000 to 450,000, a molecular weight distribution of 12 to 25, MI216/MI216 of 50 to 200, and a density of 0.950 g/cm3 or more. It is desirable to use

또한, 상기 고밀도폴리에틸렌은 에틸렌 호모 중합체 또는 에틸렌과 1종 이상의 단량체의 공중합체가 사용되는 것이 바람직하며, 상기 단량체로는, 4 내지 6개의 탄소원자를 함유하는 선형 또는 분지형 알파 올레핀, 예를 들어, 부텐-1, 헥센-1 및 4-메틸펜텐-1 등을 사용할 수 있다.In addition, the high-density polyethylene is preferably an ethylene homopolymer or a copolymer of ethylene and one or more monomers, and the monomers include linear or branched alpha olefins containing 4 to 6 carbon atoms, for example, Butene-1, hexene-1, and 4-methylpentene-1 can be used.

상기 고하중 용융흐름지수가 50g/10분을 초과하면, 용융장력이 저하되거나, 또는 성형품의 두께 균일성이 악화되거나, 용기(Bottle)의 성형불량을 일으키므로 바람직하지 않고, 상기 중량평균분자량이 250000 미만이면 용기 내충격성이 약화되어 바람직하지 않고, 450000을 초과하면 가공성이 저하되어 외관 불량을 야기시키므로 바람직하지 않으며, 상기 분자량분포가 12 미만이면 최종 수지조성물의 목표 분자량분포를 얻기 곤란하여 유동성 저하로 외관이 만족되지 않으므로 바람직하지 않고, 25를 초과하면 저분자량 성분이 많아져 패리슨 쳐짐이나 용기적재성 저하를 야기시키므로 바람직하지 않다. 또한, 상기 MI216/MI216이 50미만이면, 가공시 수지의 유동성이 나빠져서 수지가 발열되고 멜트프랙쳐를 일으키기 쉬워 바람직하지 않고, 200을 초과하면, 성형품의 기계적 물성이 저하되어 적절한 용기적 재성을 갖지 못하여 바람직하지 않으며, 밀도가 0.950g/㎤ 미만이면 중공성형 용기의 강도가 저하되어 바람직하지 않다.If the high load melt flow index exceeds 50 g/10 min, it is undesirable because the melt tension decreases, the thickness uniformity of the molded product deteriorates, or molding defects in the bottle occur, and the weight average molecular weight If it is less than 250,000, it is undesirable because the impact resistance of the container is weakened. If it exceeds 450,000, it is undesirable because it reduces processability and causes appearance defects. If the molecular weight distribution is less than 12, it is difficult to obtain the target molecular weight distribution of the final resin composition, resulting in lower fluidity. This is undesirable because the appearance is not satisfactory, and if it exceeds 25, the amount of low molecular weight components increases, causing sagging of the parison and deterioration of container loadability, which is undesirable. In addition, if the MI216/MI216 is less than 50, the fluidity of the resin deteriorates during processing, which is undesirable because the resin generates heat and is prone to causing melt fractures, and if it exceeds 200, the mechanical properties of the molded product deteriorate and do not have appropriate container properties. This is undesirable, and if the density is less than 0.950 g/cm3, the strength of the hollow molded container decreases, which is undesirable.

상기 친환경 충전재는 40 내지 60 중량부가 함유되며, 본 발명을 통해 제조되는 내약품성이 우수한 친환경 용기의 기계적 물성을 향상시키는 역할을 하는데, 이때, 상기 친환경 충전재는 계란껍질로 제조된 탄산칼슘을 사용하는 것이 바람직하다.The eco-friendly filler contains 40 to 60 parts by weight and serves to improve the mechanical properties of the eco-friendly container with excellent chemical resistance manufactured through the present invention. In this case, the eco-friendly filler uses calcium carbonate made from eggshell. It is desirable.

상기의 친환경 충전재로 사용되는 계란껍질로 제조된 탄산칼슘은 폐기 처분되는 계란 껍데기를 수거하여 화염처리를 거친 후 분쇄하는 과정을 통해 제조되기 때문에 친환경적인 효과를 나타낸다.Calcium carbonate made from eggshells used as the above-mentioned eco-friendly filler is environmentally friendly because it is manufactured through a process of collecting discarded eggshells, flame-treating them, and then pulverizing them.

또한, 상기 친환경 충전재는 70 내지 80℃의 온도에서 40 내지 60분 동안 건조하여 사용되는 것이 바람직한데, 상기의 온도와 시간동안 건조된 충전재는 수분의 함량이 현저하게 줄어들기 때문에 용기가 성형되는 과정이나 성형후에 수분으로 인해 물성이 저하되는 현상을 억제할 수 있다.In addition, the eco-friendly filler is preferably used by drying at a temperature of 70 to 80°C for 40 to 60 minutes. Since the moisture content of the filler dried at the above temperature and time is significantly reduced, the process of forming the container However, it is possible to suppress the phenomenon of physical properties being deteriorated due to moisture after molding.

상기 친환경 충전재의 건조온도가 70℃ 미만이거나 건조온도가 40분 미만이면 수분의 제거가 효율적으로 이루어지지 못하며, 상기 친환경 충전재의 건조온도가 80℃를 초과하거나 건조시간이 60분을 초과하면 에너지 효율성 측면에서 바람직하지 못하다.If the drying temperature of the eco-friendly filler is less than 70℃ or the drying temperature is less than 40 minutes, moisture cannot be removed efficiently, and if the drying temperature of the eco-friendly filler exceeds 80℃ or the drying time exceeds 60 minutes, energy efficiency From this point of view, it is not desirable.

상기 친환경 충전재의 함량이 40 중량부 미만이면 상기의 효과가 미미하며, 상기 친환경 충전재의 함량이 60 중량부를 초과하게 되면 상기의 효과는 크게 향상되지 않으면서 용기의 기계적 강도가 오히려 저하되고 외관품질이 불량해지기 때문에 바람직하지 못하다.If the content of the eco-friendly filler is less than 40 parts by weight, the above effect is minimal, and if the content of the eco-friendly filler exceeds 60 parts by weight, the above effect is not significantly improved, but the mechanical strength of the container is lowered and the external quality is deteriorated. It is undesirable because it becomes defective.

상기 착색제는 5 내지 15 중량부가 함유되며, 고밀도폴리에틸렌 100 중량부에 안료 10 내지 20 중량부를 혼합하여 이루어진 마스터배치 형태로 적용되는 것이 바람직하며, 상기 안료로는 백색을 부여하는 안료인 산화타이타늄, 산화아연, 리토폰(lithopone) 및 연백으로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것이 바람직하다.The colorant contains 5 to 15 parts by weight, and is preferably applied in the form of a masterbatch made by mixing 10 to 20 parts by weight of pigment with 100 parts by weight of high-density polyethylene. The pigment includes titanium oxide and oxidation, which are pigments that impart white color. It is preferably made of at least one selected from the group consisting of zinc, lithopone and lead white.

상기 착색제의 함량이 5 중량부 미만이면 용기전체에 고른 색상이 부여되지 못하며, 상기 착색제의 함량이 15 중량부를 초과하게 되면 상대적으로 고밀도폴리에틸렌이나 충전재의 함량이 지나치게 줄어들기 때문에 바람직하지 못하다.If the content of the colorant is less than 5 parts by weight, a uniform color cannot be imparted to the entire container, and if the content of the colorant exceeds 15 parts by weight, the content of high-density polyethylene or filler is relatively reduced, which is undesirable.

또한, 상기 원료혼합단계(S101)에서는 상기 고밀도폴리에틸렌 100 중량부 대비 산화방지제 0.05 내지 0.2 중량부가 더 함유될수도 있는데, 상기와 같이 산화방지제가 함유되면 제조되는 용기의 산화방지 효과 뿐만 아니라, 내약품성이 더욱 향상될 수 있다.In addition, in the raw material mixing step (S101), an additional 0.05 to 0.2 parts by weight of antioxidant may be added compared to 100 parts by weight of high-density polyethylene. When the antioxidant is contained as described above, not only the antioxidant effect of the manufactured container but also the chemical resistance is improved. It can be improved further.

이때, 상기 산화방지제는 옥타데실-3-(3,5-디-터트-부틸-4-하이드록시페닐)프로피오네이트 및 트리스(2,4-디-터트-부틸페닐)포스파이트 및 옥시다이즈드 비스(하이드로제네이티드탈로우알킬)아민으로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것이 바람직하다.At this time, the antioxidants include octadecyl-3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate, tris(2,4-di-tert-butylphenyl)phosphite, and oxidase. Ized bis(hydrogenated tallowalkyl)amine is preferably composed of at least one selected from the group consisting of amines.

상기 산화방지제의 함량이 0.05 중량부 미만이면 상기의 효과가 미미하며, 상기 산화방지제의 함량이 0.2 중량부를 초과하면 제조되는 용기의 기계적 물성이 저하될 수 있다.If the content of the antioxidant is less than 0.05 parts by weight, the effect is minimal, and if the content of the antioxidant exceeds 0.2 parts by weight, the mechanical properties of the manufactured container may be reduced.

또한, 원료혼합단계(S101)에서는 상기 고밀도폴리에틸렌 100 중량부 대비 테프론계 수지 0.5 내지 3 중량부가 더 함유될 수도 있는데, 테프론계 수지가 함유되면 용기의 표면 광택도를 더욱 향상시킬 수 있으며, 성형과정에서 원료의 점도를 적절하게 조절하여 적당한 멜트텐션(melt tension)을 유지하면서 표면의 샥스킨을 줄여주는 역할을 한다.In addition, in the raw material mixing step (S101), 0.5 to 3 parts by weight of Teflon-based resin may be added compared to 100 parts by weight of high-density polyethylene. When Teflon-based resin is contained, the surface gloss of the container can be further improved, and the molding process It plays a role in reducing shock skin on the surface while maintaining appropriate melt tension by appropriately controlling the viscosity of the raw materials.

이때, 상기 테프론계 수지는 폴리테트라플루오로에틸렌(PTFE, polytetrafluoroethylene), 에틸렌 테트라플루오로에틸렌 공중합체(ETFE, ethylene tetrafluoroethylene copolymer) 및 플루오르화 에틸렌 프로필렌 공중합체(FEP, fluorinated ethylene propylene copolymer)로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것이 바람직하다.At this time, the Teflon-based resin is a group consisting of polytetrafluoroethylene (PTFE), ethylene tetrafluoroethylene copolymer (ETFE), and fluorinated ethylene propylene copolymer (FEP). It is preferable that it consists of one or more selected from.

상기 테프론계 수지의 함량이 0.5 중량부 미만이면 상기의 효과가 미미하며, 상기 테프론계 수지의 함량이 3 중량부를 초과하게 되면 원료의 점도가 지나치게 증가하여 성형성이 저하될 수 있다.If the content of the Teflon-based resin is less than 0.5 parts by weight, the above effect is minimal, and if the content of the Teflon-based resin exceeds 3 parts by weight, the viscosity of the raw material increases excessively, which may reduce moldability.

상기 용융단계(S103)는 상기 원료혼합단계(S101)를 통해 제조된 혼합물을 사출블로우성형기에 투입하고 용융하는 단계로, 상기 원료혼합단계(S101)를 통해 제조된 혼합물을 5개의 히터밴드가 장착된 스크류로 통과시켜 용융하는데, 상기 히터밴드는 첫번째가 190 내지 195℃, 두번째가 210 내지 220℃, 세번째가 220 내지 230℃, 네번째가 210 내지 220℃, 5번째가 230 내지 250℃를 나타내도록 설정하여 용융을 진행하는 것이 바람직하다.The melting step (S103) is a step of putting the mixture prepared through the raw material mixing step (S101) into an injection blow molding machine and melting it. The mixture prepared through the raw material mixing step (S101) is equipped with five heater bands. It is melted by passing it through a screw, and the heater band is set at 190 to 195°C for the first, 210 to 220°C for the second, 220 to 230°C for the third, 210 to 220°C for the fourth, and 230 to 250°C for the fifth. It is desirable to proceed with melting by setting it.

또한, 히터 밴드의 손상을 방지하기 위하여 스크류 상단과 하단 외부에 냉각수 순환 커버를 장착하여 외부의 온도가 고온이 되지 않도록 한는 것이 바람직하다.Additionally, in order to prevent damage to the heater band, it is desirable to install coolant circulation covers on the outside of the top and bottom of the screw to prevent the outside temperature from becoming high.

상기 사출단계(S105)는 상기 용융단계(S103)를 통해 용융된 혼합물을 사출하는 단계로, 상기 용융단계(S103)를 통해 용융된 혼합물을 사출금형에 주입하여 이루어지는데, 혼합물이 사출틀 안에 투입되기 전에 사출틀이 완전히 닫는 힘을 가질 수 있도록 투입 시간 전에 대기 시간을 0.5 내지 0.8초를 기다릴 수 있도록 하는 것이 바람직하며, 이때 최소한의 사출틀이 닫힐 수 있는 시간인 최소 0.2초 이상을 반드시 확보해야 한다.The injection step (S105) is a step of injecting the mixture melted through the melting step (S103), and is performed by injecting the mixture melted through the melting step (S103) into an injection mold. The mixture is injected into the injection mold. It is desirable to allow a waiting time of 0.5 to 0.8 seconds before the injection time so that the injection mold has the force to completely close before the injection mold is closed. At this time, at least 0.2 seconds, which is the minimum time for the injection mold to be closed, must be secured. do.

또한, 사출틀에 혼합물이 완전히 투입될 수 있도록 6 내지 8초의 시간과 300psi 내지 400psi의 압력을 적용하고, 사출틀에 혼합물이 완전히 투입된 후에는 사출틀에 넘치지 않도록 투입 노즐이 압력에 의해 후진될 수 있도록 설계하는 것이 바람직하다.In addition, a time of 6 to 8 seconds and a pressure of 300 psi to 400 psi are applied to ensure that the mixture is completely injected into the injection mold, and after the mixture is completely injected into the injection mold, the injection nozzle can be retracted by pressure to prevent the mixture from overflowing into the injection mold. It is desirable to design it so that

또한, 사출틀 안에 투입된 혼합물이 고온으로 흘러내리지 않고 형상을 유지할 수 있도록 사출틀을 닫아 놓은 상태에서 1.5 내지 2.5초 동안 냉각을 진행한다. 이때 사출틀이 닫힌 상태로 혼합물을 냉각할 수 있도록 사출틀에 냉각수가 순환될 수 있도록 설계하는 것이 바람직하며, 사출틀 순환 냉각을 위한 온도는 용기 주입구 부분 30 내지 85℃, 몸통 부분 90 내지 100℃ 및 바닥 부분 85 내지 95℃로 설정하는 것이 바람직하다. In addition, cooling is performed for 1.5 to 2.5 seconds with the injection mold closed so that the mixture placed in the injection mold can maintain its shape without flowing down due to high temperature. At this time, it is desirable to design the injection mold to allow cooling water to circulate so that the mixture can be cooled while the injection mold is closed. The temperature for circulation cooling of the injection mold is 30 to 85°C at the container inlet and 90 to 100°C at the body. and the bottom portion is preferably set to 85 to 95°C.

상기 사출단계(S105)에서 혼합물의 투입압력이 300psi 미만이거나 사출시간이 6초 미만이면 사출틀에 혼합물이 완전하게 사출되지 못하며, 혼합물의 투입압력이 400psi를 초과하거나 사출시간이 8초를 초과하게 되면 사출틀에 혼합물이 사출량이 지나치게 증가하여 용기의 두께를 지나치게 증가시키며, 상기 블로우성형단계(S107)에서 진행되는 블로우성형이 제대로 진행되지 못한다.In the injection step (S105), if the mixture input pressure is less than 300 psi or the injection time is less than 6 seconds, the mixture cannot be completely injected into the injection mold. If the mixture input pressure exceeds 400 psi or the injection time exceeds 8 seconds, the mixture cannot be completely injected into the injection mold. If this happens, the injection amount of the mixture in the injection mold increases excessively, thereby excessively increasing the thickness of the container, and the blow molding performed in the blow molding step (S107) does not proceed properly.

상기 블로우성형단계(S107)는 상기 사출단계(S105)를 통해 사출된 혼합물을 블로우성형하는 단계로, 상기 사출단계(S105)를 통해 사출틀로 사출된 혼합물의 냉각이 진행된 후에, 냉각된 혼합물을 블로우 틀로 옮긴 후 블로우 틀을 닫는데, 이때 블로우 틀이 완전히 닫힌 힘이 생길 수 있도록 사출틀과 마찬가지로 0.5 내지 0.8초의 시간을 기다린 후에 블로우성형과정을 진행하는 것이 바람직하다.The blow molding step (S107) is a step of blow molding the mixture injected through the injection step (S105). After the mixture injected into the injection mold through the injection step (S105) is cooled, the cooled mixture is After transferring to the blow mold, the blow mold is closed. At this time, it is desirable to wait 0.5 to 0.8 seconds before proceeding with the blow molding process, as with the injection mold, so that the blow mold can be fully closed.

사출틀이 완전히 닫힌 후에는 블로우 틀에 7 내지 10초 동안 에어를 공급하여 블로우성형을 진행하는 것이 바람직하다.After the injection mold is completely closed, it is desirable to proceed with blow molding by supplying air to the blow mold for 7 to 10 seconds.

상기 냉각단계(S109)는 상기 블로우성형단계(S107)를 통해 제조된 성형물을 냉각하는 단계로, 상기 블로우성형단계(S107)를 통해 제조된 성형물을 1 내지 20℃의 온도로 냉각하는 과정으로 이루어진다.The cooling step (S109) is a step of cooling the molded product manufactured through the blow molding step (S107), and consists of cooling the molded product manufactured through the blow molding step (S107) to a temperature of 1 to 20 ° C. .

이때, 상기 냉각단계(S109)는 고온 상태의 성형물을 냉각시켜 용기의 수축을 최소화하기 위해 블로우 틀에 냉각수가 순환되어 성형물의 온도가 1 내지 20℃로 냉각될 수 있도록 블로우 틀을 설계하는 것이 바람직하다.At this time, in the cooling step (S109), in order to cool the molded product at a high temperature and minimize shrinkage of the container, it is desirable to design the blow mold so that the temperature of the molded product can be cooled to 1 to 20°C by circulating coolant in the blow mold. do.

이하에서는, 본 발명에 따른 내약품성이 우수한 친환경 용기의 제조방법 및 그 제조방법으로 제조된 친환경 용기의 물성을 실시예를 들어 설명하기로 한다.Hereinafter, the manufacturing method of an eco-friendly container with excellent chemical resistance according to the present invention and the physical properties of the eco-friendly container manufactured by the manufacturing method will be described using examples.

<실시예 1><Example 1>

고밀도폴리에틸렌 100 중량부, 친환경 충전재(계란껍질로 제조된 탄산칼슘) 50 중량부 및 착색제(고밀도폴리에틸렌 100 중량부 산화타이타늄 15 중량부가 혼합된 마스터배치) 10 중량부를 혼합하고, 5개의 히터밴드(첫번째 192℃, 두번째 215℃, 세번째 225℃, 네번째 215℃, 5번째 240℃)가 장착된 스크류가 구비된 사출블로우성형기에 투입하고 용융한 후에, 사출틀에 용융된 혼합물을 7초 동안 350psi의 압력으로 사출한 후에, 용기 주입구 부분 50℃, 몸통 부분 95℃ 및 바닥 부분 90℃로 2초 동안 냉각하고, 냉각된 혼합물은 블로우 틀로 옮긴 후 블로우 틀을 닫고 8.5 동안 에어를 공급하여 블로우성형하고, 블로우성형된 성형물을 10℃로 냉각하여 내약품성이 우수한 친환경 용기를 제조하였다.Mix 100 parts by weight of high-density polyethylene, 50 parts by weight of eco-friendly filler (calcium carbonate made from eggshell), and 10 parts by weight of colorant (masterbatch mixed with 100 parts by weight of high-density polyethylene and 15 parts by weight of titanium oxide), and add 5 heater bands (the first one). 192℃, second 215℃, third 225℃, fourth 215℃, fifth 240℃) and melted in an injection blow molding machine equipped with a screw. After melting, the molten mixture in the injection mold was pressured at 350 psi for 7 seconds. After injection, the container inlet is cooled to 50℃, the body is 95℃, and the bottom is 90℃ for 2 seconds. The cooled mixture is transferred to a blow mold, the blow mold is closed, air is supplied for 8.5 minutes, blow molded, and blown. The molded product was cooled to 10°C to produce an eco-friendly container with excellent chemical resistance.

<실시예 2><Example 2>

상기 실시예 1과 동일하게 진행하되, Proceed in the same manner as Example 1 above, but

상기 고밀도폴리에틸렌 100 중량부 대비 산화방지제{옥타데실-3-(3,5-디-터트-부틸-4-하이드록시페닐)프로피오네이트} 0.1 중량부를 더 함유하여 내약품성이 우수한 친환경 용기를 제조하였다.An eco-friendly container with excellent chemical resistance is manufactured by containing 0.1 parts by weight of antioxidant {octadecyl-3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate} compared to 100 parts by weight of high-density polyethylene. did.

<실시예 3><Example 3>

상기 실시예 1과 동일하게 진행하되, Proceed in the same manner as Example 1 above, but

상기 고밀도폴리에틸렌 100 중량부 대비 테프론계 수지(폴리테트라플루오로에틸렌) 2 중량부를 더 함유하여 내약품성이 우수한 친환경 용기를 제조하였다.An eco-friendly container with excellent chemical resistance was manufactured by adding 2 parts by weight of Teflon-based resin (polytetrafluoroethylene) compared to 100 parts by weight of high-density polyethylene.

<실시예 4><Example 4>

상기 실시예 1과 동일하게 진행하되, Proceed in the same manner as Example 1 above, but

상기 고밀도폴리에틸렌 100 중량부 대비 산화방지제{옥타데실-3-(3,5-디-터트-부틸-4-하이드록시페닐)프로피오네이트} 0.1 중량부 및 테프론계 수지(폴리테트라플루오로에틸렌) 2 중량부를 더 함유하여 내약품성이 우수한 친환경 용기를 제조하였다.0.1 part by weight of antioxidant {octadecyl-3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate} and Teflon-based resin (polytetrafluoroethylene) relative to 100 parts by weight of high-density polyethylene. By adding 2 parts by weight, an eco-friendly container with excellent chemical resistance was manufactured.

<비교예 1><Comparative Example 1>

고밀도폴리에틸렌 100 중량부, 탄산칼슘 20 중량부 및 착색제(고밀도폴리에틸렌 100 중량부 산화타이타늄 15 중량부가 혼합된 마스터배치) 10 중량부를 혼합하고, 5개의 히터밴드(첫번째 192℃, 두번째 215℃, 세번째 225℃, 네번째 215℃, 5번째 240℃)가 장착된 스크류가 구비된 사출블로우성형기에 투입하고 용융한 후에, 사출틀에 용융된 혼합물을 7초 동안 350psi의 압력으로 사출한 후에, 용기 주입구 부분 50℃, 몸통 부분 95℃ 및 바닥 부분 90℃로 2초 동안 냉각하고, 냉각된 혼합물은 블로우 틀로 옮긴 후 블로우 틀을 닫고 8.5 동안 에어를 공급하여 블로우성형하고, 블로우성형된 성형물을 10℃로 냉각하여 용기를 제조하였다.Mix 100 parts by weight of high-density polyethylene, 20 parts by weight of calcium carbonate, and 10 parts by weight of colorant (masterbatch mixed with 100 parts by weight of high-density polyethylene and 15 parts by weight of titanium oxide), and heat five heater bands (the first at 192℃, the second at 215℃, and the third at 225℃). ℃, fourth 215℃, fifth 240℃) and melted in an injection blow molding machine equipped with a screw, and then injected the molten mixture into the injection mold at a pressure of 350 psi for 7 seconds, and then injected the mixture into the injection mold at 50 psi. ℃, cool to 95℃ for the body and 90℃ for the bottom for 2 seconds, transfer the cooled mixture to the blow mold, close the blow mold, supply air for 8.5 and blow mold it, and cool the blow molded product to 10℃. A container was manufactured.

<비교예 2><Comparative Example 2>

상기 비교예 1과 동일하게 진행하되, 탄산칼슘 80 중량부를 혼합하여 용기를 제조하였다.The same procedure as in Comparative Example 1 was carried out, but a container was prepared by mixing 80 parts by weight of calcium carbonate.

상기 실시예 1 내지 4 및 비교예 1 내지 2를 통해 제조된 용기의 낙하내충격성, 적재강도 및 외관을 측정하여 아래 표 1에 나타내었다.The drop impact resistance, loading strength, and appearance of the containers manufactured through Examples 1 to 4 and Comparative Examples 1 to 2 were measured and are shown in Table 1 below.

{단, 낙하내충격성은 UN 기준에 의거 실시하였는데, 상온의 물을 20L 눈금까지 채우고 마개를 하여 일정 높이에서 5회 낙하하여 용기의 파손 및 누수를 확인하는 방법으로, 파손 및 누수가 1회도 나타나지 않은 최대 높이를 나타내는 방법을 이용하였다.{However, the drop impact resistance was conducted according to UN standards. This is a method of checking for damage or leakage of the container by filling it with room temperature water up to the 20L mark, putting a stopper on it, and dropping it 5 times from a certain height to check for damage or leakage. A method of indicating the maximum height was used.

또한, 적재강도는 40℃, 250kg 하중 하에서 28일간 방치 후 용기의 크랙 발생 여부를 확인하는 방법을 이용하였다.In addition, the loading strength was determined by checking whether cracks occurred in the container after leaving it for 28 days at 40℃ and under a load of 250kg.

또한, 외관은 육안으로 관찰하여 멜트프랙쳐나 다이라인의 발견 여부를 확인하여 양호 및 불량을 확인하는 방법을 이용하였다.}In addition, the appearance was observed with the naked eye to check whether melt fractures or die lines were found to determine whether it was good or bad.}

<표 1><Table 1>

상기 표 1에 나타낸 것처럼, 본 발명의 실시예 1 내지 4를 통해 제조된 친환경 용기는 기계적 강도가 우수할 뿐만 아니라, 외관 품질이 우수한 것을 알 수 있다. 특히, 테프론계 수진가 함유된 실시예 3 내지 4의 경우 외관품질이 더욱 우수한 것을 알 수 있다.As shown in Table 1, it can be seen that the eco-friendly containers manufactured through Examples 1 to 4 of the present invention not only have excellent mechanical strength, but also have excellent appearance quality. In particular, in the case of Examples 3 to 4 containing Teflon-based resin, it can be seen that the appearance quality is more excellent.

따라서, 본 발명에 따른 내약품성이 우수한 친환경 용기의 제조방법은 기계적 물성, 내약품성 및 외관품질이 우수할 뿐만 아니라, 계란껍질로 제조된 탄산칼슘이 사용되어 친환경적인 용기를 제공한다.Therefore, the method of manufacturing an eco-friendly container with excellent chemical resistance according to the present invention not only has excellent mechanical properties, chemical resistance, and appearance quality, but also provides an eco-friendly container by using calcium carbonate made from eggshell.

S101 ; 원료혼합단계
S103 ; 용융단계
S105 ; 사출단계
S107 ; 블로우성형단계
S109 ; 냉각단계
S101 ; Raw material mixing stage
S103 ; melting stage
S105 ; Injection stage
S107 ; Blow molding stage
S109 ; Cooling stage

Claims (7)

고밀도폴리에틸렌, 친환경 충전재 및 착색제를 혼합하는 원료혼합단계;
상기 원료혼합단계를 통해 제조된 혼합물을 사출블로우성형기에 투입하고 용융하는 용융단계;
상기 용융단계를 통해 용융된 혼합물을 사출하는 사출단계;
상기 사출단계를 통해 사출된 혼합물을 블로우성형하는 블로우성형단계; 및
상기 블로우성형단계를 통해 제조된 성형물을 냉각하는 냉각단계;로 이루어지며,
상기 친환경 충전재는 계란껍질로 제조된 탄산칼슘인 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법.
A raw material mixing step of mixing high-density polyethylene, eco-friendly fillers, and colorants;
A melting step of putting the mixture prepared through the raw material mixing step into an injection blow molding machine and melting it;
An injection step of injecting the molten mixture through the melting step;
A blow molding step of blow molding the mixture injected through the injection step; and
It consists of a cooling step of cooling the molded product manufactured through the blow molding step,
A method of manufacturing an eco-friendly container with excellent chemical resistance, wherein the eco-friendly filler is calcium carbonate made from eggshell.
청구항 1에 있어서,
상기 원료혼합단계는 고밀도폴리에틸렌 100 중량부, 친환경 충전재 40 내지 60 중량부 및 착색제 5 내지 15 중량부로 이루어지는 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법.
In claim 1,
The raw material mixing step is a method of manufacturing an eco-friendly container with excellent chemical resistance, characterized in that it consists of 100 parts by weight of high-density polyethylene, 40 to 60 parts by weight of eco-friendly filler, and 5 to 15 parts by weight of colorant.
청구항 1 또는 2에 있어서,
상기 원료혼합단계에서는 상기 고밀도폴리에틸렌 100 중량부 대비 산화방지제 0.05 내지 0.2 중량부가 더 함유되며,
상기 산화방지제는 옥타데실-3-(3,5-디-터트-부틸-4-하이드록시페닐)프로피오네이트 및 트리스(2,4-디-터트-부틸페닐)포스파이트 및 옥시다이즈드 비스(하이드로제네이티드탈로우알킬)아민으로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법.
In claim 1 or 2,
In the raw material mixing step, 0.05 to 0.2 parts by weight of antioxidant is additionally contained relative to 100 parts by weight of the high-density polyethylene,
The antioxidants include octadecyl-3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate, tris(2,4-di-tert-butylphenyl)phosphite, and oxidized A method of manufacturing an eco-friendly container with excellent chemical resistance, characterized in that it is made of at least one selected from the group consisting of bis(hydrogenated tallow alkyl)amine.
청구항 1 또는 2에 있어서,
상기 원료혼합단계에서는 상기 고밀도폴리에틸렌 100 중량부 대비 테프론계 수지 0.5 내지 3 중량부가 더 함유되는 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법.
In claim 1 or 2,
A method for manufacturing an eco-friendly container with excellent chemical resistance, characterized in that in the raw material mixing step, 0.5 to 3 parts by weight of Teflon-based resin is added compared to 100 parts by weight of high-density polyethylene.
청구항 4에 있어서,
상기 테프론계 수지는 폴리테트라플루오로에틸렌, 에틸렌테트라플루오로에틸렌 공중합체 및 플루오르화에틸렌프로필렌 공중합체로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법.
In claim 4,
A method of manufacturing an eco-friendly container with excellent chemical resistance, wherein the Teflon-based resin is made of at least one selected from the group consisting of polytetrafluoroethylene, ethylenetetrafluoroethylene copolymer, and fluorinated ethylenepropylene copolymer.
청구항 1 또는 2에 있어서,
상기 친환경 충전재는 70 내지 80℃의 온도에서 40 내지 60분 동안 건조하여 사용되는 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법.
In claim 1 or 2,
A method of manufacturing an eco-friendly container with excellent chemical resistance, characterized in that the eco-friendly filler is dried for 40 to 60 minutes at a temperature of 70 to 80 ° C.
청구항 1에 있어서,
상기 사출단계는 상기 용융단계를 통해 용융된 혼합물을 300 내지 400Psi의 압력으로 6 내지 8초 동안 사출금형에 주입하여 이루어지는 것을 특징으로 하는 내약품성이 우수한 친환경 용기의 제조방법.
In claim 1,
The injection step is a method of manufacturing an eco-friendly container with excellent chemical resistance, characterized in that the mixture molten through the melting step is injected into an injection mold for 6 to 8 seconds at a pressure of 300 to 400 Psi.
KR1020220057422A 2022-05-10 2022-05-10 Manufacturing method of eco-friendly container with excellent chemical resistance KR20230158162A (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020049130A (en) 2000-12-19 2002-06-26 전승호 High Pure Polyethylene Resin Composition and Its Hollow Bodies
KR100525702B1 (en) 2002-02-01 2005-11-03 미쯔이가가꾸가부시끼가이샤 Polyethylenes Resin for Blow Mold and Blow Mold Comprising the Same

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020049130A (en) 2000-12-19 2002-06-26 전승호 High Pure Polyethylene Resin Composition and Its Hollow Bodies
KR100525702B1 (en) 2002-02-01 2005-11-03 미쯔이가가꾸가부시끼가이샤 Polyethylenes Resin for Blow Mold and Blow Mold Comprising the Same

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