KR20120002393A - Method of producing highly flowable and flame retardant modified polyethylene powder for metal coating - Google Patents

Method of producing highly flowable and flame retardant modified polyethylene powder for metal coating Download PDF

Info

Publication number
KR20120002393A
KR20120002393A KR1020100086321A KR20100086321A KR20120002393A KR 20120002393 A KR20120002393 A KR 20120002393A KR 1020100086321 A KR1020100086321 A KR 1020100086321A KR 20100086321 A KR20100086321 A KR 20100086321A KR 20120002393 A KR20120002393 A KR 20120002393A
Authority
KR
South Korea
Prior art keywords
modified
density polyethylene
resin
powder
weight
Prior art date
Application number
KR1020100086321A
Other languages
Korean (ko)
Other versions
KR101237741B1 (en
Inventor
정화영
윤경준
김대인
박종철
Original Assignee
주식회사 투에이취켐
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 주식회사 투에이취켐 filed Critical 주식회사 투에이취켐
Publication of KR20120002393A publication Critical patent/KR20120002393A/en
Application granted granted Critical
Publication of KR101237741B1 publication Critical patent/KR101237741B1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D123/00Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers
    • C09D123/26Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers modified by chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/03Powdery paints
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/18Fireproof paints including high temperature resistant paints
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/41Organic pigments; Organic dyes
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/66Additives characterised by particle size
    • C09D7/69Particle size larger than 1000 nm
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/80Processes for incorporating ingredients
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C26/00Coating not provided for in groups C23C2/00 - C23C24/00
    • C23C26/02Coating not provided for in groups C23C2/00 - C23C24/00 applying molten material to the substrate

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Nanotechnology (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Paints Or Removers (AREA)

Abstract

PURPOSE: A manufacturing method of modified polyethylene powder is provided not to generate volatile organic compound during coating film formation, to prevent environment contamination, and to secure the safety of a worker. CONSTITUTION: A manufacturing method of modified polyethylene powder comprises: a step(S10) of manufacturing modified resin by reacting and extruding high density polyethylene which has the high flexability of 60-100 melt index, and 0.5-1.5 parts by weight maleic anhydride on the basis of total modified resin(P1); a step(S20) of manufacturing resin composition(P2) by mixing 10-40 parts by weight the modified resin(P1), 30-85 parts by weight adhesive resin, and 5-30 parts by weight flame retardant; and an additional step(S30) of manufacturing powder by pulverizing the resin composition(P2) to the size of 10-300 micron.

Description

고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법 {Method of producing highly flowable and flame retardant modified polyethylene powder for metal coating} Method of producing modified polyethylene powder for metal coating having high flowability and flame retardancy {Method of producing highly flowable and flame retardant modified polyethylene powder for metal coating}

본 발명은 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법에 관한 것이다.The present invention relates to a method for producing modified polyethylene powder for metal coating having high fluidity and flame retardancy.

일반적으로 금속부품의 코팅은 도료를 표면에 마감하여 금속부품이 산화되는 것을 방지하고, 내구성 및 심미적 효과를 높이는 것을 목적으로 한다. 종래의 액상 도료는 폴리머 레진, 바인더, 안료 등이 휘발성 유기용제에 혼합된 것으로 도포후 유기용제의 휘발에 의해 도막이 형성되는데 이때 사용되는 대부분의 유기용제는 VOC 유해물질로 대기, 수질, 폐기물 환경에 직접 또는 간접적으로 영향을 미치는 문제점이 있다.
In general, the coating of metal parts aims to prevent the metal parts from oxidizing by finishing the paint on the surface, and to increase durability and aesthetic effect. Conventional liquid paints are a mixture of polymer resins, binders, and pigments in volatile organic solvents. After coating, the coating film is formed by volatilization of organic solvents. Most of the organic solvents used are hazardous substances of VOC. There is a problem that affects directly or indirectly.

한편, 휘발성 유기화합물이 발생하지 않는 종래의 열가소성 파우더 코팅제는 폴리에틸렌, 폴리프로필렌, 에틸렌 비닐 아세테이트 등의 비극성 폴리올레핀을 주수지로 한 분말상 코팅제가 주류를 이루고 있는데 비극성임에 따라 금속표면과의 접착성이 없어 단순 점착코팅되며, 도막의 일부분이 파손되면 코팅도막 전체로 들뜸현상이 쉽게 확산되어 내구성이 부족한 문제가 있다.
On the other hand, conventional thermoplastic powder coatings which do not generate volatile organic compounds are mainly powdered coatings made of non-polar polyolefin such as polyethylene, polypropylene, ethylene vinyl acetate, etc. There is no simple adhesive coating, and if a part of the coating is broken, there is a problem that the lifting phenomenon is easily spread to the entire coating film and the durability is insufficient.

상기의 분말 도료의 특징으로 한번의 도장으로 100~500 두께를 가진 도막을 형성할 수 있는 장점이 있으나, 용융흐름지수(Melt flow index)가 낮아 피도물에 대한 젖음성이 나쁘고 접착성이 없어 열과 습기가 많은 외부 환경에 빈번이 노출되는 금속구조물(에어컨 실외기, 냉장고 후면 트레이 및 옥외용 메쉬 팬스 등)에 코팅될 경우 도막의 들뜸이나 크랙(crack)이 발생하고 지속적으로 진행되어 박리된 부위의 녹 발생이 가속화되는 문제점을 안고 있다.
As a characteristic of the powder coating, there is an advantage of forming a coating film having a thickness of 100 to 500 with one coating. However, since the melt flow index is low, the wettability to the coating is poor and the adhesiveness is low, which causes heat and moisture. When coated on metal structures (such as air conditioners, refrigerator rear trays, and outdoor mesh pans) that are frequently exposed to many external environments, the coating may be lifted or cracked, and it may continue to accelerate the rusting of the peeled areas. I have a problem.

또한, 분말 도료는 액상 도료에 비해 흐름성이 현저하게 낮기 때문에 균일한 도막형성에 어려움이 있으므로 피도물에 분말 도료를 도포시 도막 두께를 일정하게 조절하기 어려운 문제점을 가지므로 작업성 및 적용성이 액상 도료에 비하여 한정적으로 사용되고 있는 실정이며, 무기 첨가제를 함유한 분말 도료는 도막 표면에 오렌지필이나 핀홀과 같은 도장불량 발생율이 높아 레벨링제 및 표면개선제등의 첨가제류를 필수적으로 사용해야 하는 경제적 부담이 있다.
In addition, since the powder coating is significantly lower in flowability than the liquid coating, it is difficult to form a uniform coating film. Therefore, when the powder coating is applied to the coating material, it is difficult to constantly adjust the coating film thickness. It is used more limitedly than paints, and powder coatings containing inorganic additives have a high economic burden due to the high incidence of poor coating such as orange peel and pinholes on the surface of the coating film, which requires the use of additives such as leveling agents and surface improving agents. .

최근 국내외적으로 도료의 사용량이 증가함에 따라 환경성과 안정성에 대한 관심과 요구가증가되고 있는 추세이며, 이에 따라 화재 발생시 연소 및 지연의 효과를 나타낼 수 있는 환경친화적인 난연제 조성물과 이를 첨가한 분말 도료에 대한 관심이 높아지고 있는 실정이다.Recently, as the amount of paint is increased at home and abroad, there is a growing interest and demand for environmental stability and stability. Accordingly, an environmentally friendly flame retardant composition and powder coating containing the same can exhibit the effects of combustion and delay in the event of a fire. Interest in the situation is increasing.

본 발명은 고유동성과 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더의 제조방법으로 금속의 부식방지 및 심미적 외관을 충족하며 도막 형성시 액상 도료의 경우처럼 휘발성 유기화합물이 전혀 발생하지 않으므로 환경오염을 방지하고 작업자의 안전을 도모한다. 또한 변성 폴리에틸렌을 주수지로 함으로 기존의 분말 도료와 비교하여 접착성능을 향상하고 고유동성에 따른 원활한 도막을 형성하는 것과 난연성을 부여하는 것을 목적으로 한다.The present invention is a method of manufacturing a modified polyethylene powder for metal coating having a high flowability and flame retardancy to meet the corrosion protection and aesthetic appearance of the metal and to prevent environmental pollution since no volatile organic compounds occur at all when forming a coating film Promote the safety of workers. In addition, by using modified polyethylene as the main resin, the purpose of the present invention is to improve the adhesive performance, form a smooth coating film according to high fluidity, and to impart flame retardance as compared with the conventional powder coating.

본 발명의 금속피복용 변성 폴리에틸렌 파우더 제조방법은, 용융지수가 60~100인 고유동성을 가진 고밀도폴리에티렌(HDPE, High Density Polyethylene)과 총 변성수지(P1)의 0.5~1.5 중량부의 무수말레인산을 반응압출하여 변성수지(P1)를 제조하는 단계(S10)와;In the method of manufacturing modified polyethylene powder for metal coating of the present invention, 0.5 to 1.5 parts by weight of maleic anhydride of high density polyethylene (HDPE, High Density Polyethylene) having a melt index of 60 to 100 and total modified resin (P1) Reaction extrusion to prepare a modified resin (P1) (S10);

상기 변성수지(P1) 10~40중량부와, 고밀도폴리에틸렌(HDPE), 저밀도폴리에틸렌(LDPE, low density polyethylene), 선형저밀도폴리에틸렌(LLDPE, linear low density polyethylene), 중간밀도폴리에틸렌(MDPE, medium density polyethylene), 폴리카보네이트(PC, polycarbonate), 에틸렌비닐아세테이트(EVA, ethylene vinyl acetate), 폴리에틸렌테레프탈레이트(PET, polyethylene terephthalate), 에틸렌프로필렌디엔모노머(EPDM, ethylene propylene diene monomer), 스틸렌부타디엔스틸렌(SBS, stylene butadiene stylene), 스틸렌부타디엔러버(SBR, stylene butadiene rubber), 스틸렌에틸렌부타디엔스틸렌(SEBS, styrene etylene butadiene styrene), 부타디엔러버(BR, butadien rubber) 중에서 선택된 적어도 하나 이상의 물질로 구성된 접착성 수지제 30~85중량부와, 5~30중량부의 난연제를 혼합하여 수지조성물(P2)을 제조하는 단계(S20);를 포함하여 구성된다.The modified resin (P1) 10 to 40 parts by weight, high density polyethylene (HDPE), low density polyethylene (LDPE, low density polyethylene), linear low density polyethylene (LLDPE, linear low density polyethylene), medium density polyethylene (MDPE, medium density polyethylene) ), Polycarbonate (PC, polycarbonate), ethylene vinyl acetate (EVA, ethylene vinyl acetate), polyethylene terephthalate (PET, polyethylene terephthalate), ethylene propylene diene monomer (EPDM, ethylene propylene diene monomer), styrene butadiene styrene (SBS, Adhesive resin composed of at least one material selected from stylene butadiene stylene (SBR), styrene butadiene rubber (SBR), styrene ethylene butadiene styrene (SEBS), butadiene rubber (BR) It comprises a; step (S20) to produce a resin composition (P2) by mixing ~ 85 parts by weight, and 5 to 30 parts by weight of the flame retardant.

본 발명에 따른 경우, 금속의 부식방지 및 심미적 외관을 충족하며 도막 형성시 액상 도료의 경우처럼 휘발성 유기화합물이 전혀 발생하지 않으므로 환경오염을 방지하고 작업자의 안전을 도모하고, 또한 변성 폴리에틸렌을 주수지로 함으로 기존의 분말 도료와 비교하여 접착성능을 향상하고 고유동성에 따른 원활한 도막을 형성하는 것과 난연성을 부여할 수 있는 고유동성과 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더의 제조방법이 제공된다.According to the present invention, it satisfies the corrosion protection and aesthetic appearance of the metal and does not generate any volatile organic compounds as in the case of the liquid coating when forming the coating film, thereby preventing environmental pollution and promoting the safety of the worker, and also modified resin polyethylene The present invention provides a method for producing modified polyethylene powder for metal coating having high flowability and flame retardancy, which can improve adhesion performance and form a smooth coating film according to high flowability as compared with conventional powder coating.

도 1은 본 발명의 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법 공정도.1 is a process chart of the modified polyethylene powder for metal coating having a high flowability and flame retardancy of the present invention.

이하에서 본 발명의 일실시예에 따른 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법에 대하여 상세하게 설명한다. 도 1은 본 발명의 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법 공정도이다.
Hereinafter, a method for preparing modified polyethylene powder for metal coating having high fluidity and flame retardancy according to an embodiment of the present invention will be described in detail. 1 is a process chart of the modified polyethylene powder for metal coating having a high flowability and flame retardancy of the present invention.

도 1에 도시된 바와 같이, 본 발명의 일실시예에 따른 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법은, 1차로 변성수지(P1)를 제조하는 단계(S10)와, 2차로 수지조성물(P2)을 제조하는 단계(S20)와, 3차로 파우더를 제조하는 단계(S30)를 포함하여 구성된다.
As shown in FIG. 1, the method of manufacturing modified polyethylene powder for metal coating having high flowability and flame retardancy according to an embodiment of the present invention includes the steps of preparing modified resin (P1) in the first step (S10) and secondly. It comprises a step (S20) of preparing a resin composition (P2), and a step (S30) of preparing a powder in the third.

먼저, 변성수지(P1)를 제조하는 단계(S10)에서, 용융지수가 60~100인 고유동성을 가진 고밀도폴리에티렌(HDPE, High Density Polyethylene)과 총 변성수지(P1)의 0.5~1.5 중량부의 무수말레인산을 반응압출한다.
First, in the step of manufacturing the modified resin (P1) (S10), 0.5 ~ 1.5 weight of the high-density polyethylene (HDPE, High Density Polyethylene) and total modified resin (P1) having a high melt melt index of 60 ~ 100 Reaction extruded negative maleic anhydride.

무수말레인산이 0.5 중량부보다 낮을 경우 접착성 수지제에 혼합되었을때 접착성이 낮아 효과가 떨어지며, 1.5 중량부 이상에서는 미반응물질이 많이 생성되어 오히려 반응압출되는 효과가 떨어지기 때문이다.
When maleic anhydride is lower than 0.5 parts by weight, the effect is low when the adhesive is mixed with the adhesive resin, the effect is lowered, more than 1.5 parts by weight of the unreacted substances are generated, rather the effect of the reaction extrusion is reduced.

최초 변성 수지와 첨가되는 HDPE의 용융지수가 60~100로 높은 이유는 제조단계별로 유동지수가 낮아지게 됨으로, 최종 개발 조성물의 유동지수가 20~40 범위를 갖기 위해서이다. 즉, 초기 용융지수가 높은 고밀도폴리에틸렌을 사용한 이유는 최종 조성물(변성수지+접착성 수지제+난연제)로 제조하였을때 용융지수가 낮아져서 20~40의 용융지수를 갖게 하게 위해서이다.
The reason why the melt index of the first modified resin and the added HDPE is 60 to 100 is high because the flow index is lowered according to manufacturing stages, so that the flow index of the final development composition is in the range of 20 to 40. That is, the reason for using high density polyethylene having a high initial melt index is that the melt index is lowered when the final composition (modified resin + adhesive resin + flame retardant) is prepared to have a melt index of 20 to 40.

다음으로, 수지조성물(P2)을 제조하는 단계(S20)에서, 전 단계(S10)에서 제조된 변성수지(P1) 10~40중량부와, 고밀도폴리에틸렌(HDPE), 저밀도폴리에틸렌(LDPE, low density polyethylene), 선형저밀도폴리에틸렌(LLDPE, linear low density polyethylene), 중간밀도폴리에틸렌(MDPE, medium density polyethylene), 폴리카보네이트(PC, polycarbonate), 에틸렌비닐아세테이트(EVA, ethylene vinyl acetate), 폴리에틸렌테레프탈레이트(PET, polyethylene terephthalate), 에틸렌프로필렌디엔모노머(EPDM, ethylene propylene diene monomer), 스틸렌부타디엔스틸렌(SBS, stylene butadiene stylene), 스틸렌부타디엔러버(SBR, stylene butadiene rubber), 스틸렌에틸렌부타디엔스틸렌(SEBS, styrene etylene butadiene styrene), 부타디엔러버(BR, butadien rubber) 중에서 선택된 적어도 하나 이상의 물질로 구성된 접착성 수지제 30~85중량부와, 5~30중량부의 난연제를 혼합하여 수지조성물(P2)을 제조한다. 이때 혼합은 압출기를 사용한다.
Next, in the step of preparing a resin composition (P2) (S20), 10 to 40 parts by weight of the modified resin (P1) prepared in the previous step (S10), high density polyethylene (HDPE), low density polyethylene (LDPE, low density) polyethylene), linear low density polyethylene (LLDPE), medium density polyethylene (MDPE), polycarbonate (PC, polycarbonate), ethylene vinyl acetate (EVA), polyethylene terephthalate (PET) , polyethylene terephthalate, ethylene propylene diene monomer (EPDM), styrene butadiene styrene (SBS, stylene butadiene stylene), styrene butadiene rubber (SBR, stylene butadiene rubber), styrene ethylene butadiene styrene (SEBS, styrene etylene butadiene 30 to 85 parts by weight of an adhesive resin composed of at least one material selected from styrene) and butadien rubber (BR), and 5 to 30 parts by weight of a flame retardant. Combined to produce a resin composition (P2). At this time, the mixing is performed using an extruder.

1차 컴파운드 변성수지(P1)가 10중량% 보다 적을 경우 분말 도료 수지조성물의 접착력이 약하고 40중량% 이상일 경우에는 수지간에 가교도의 과잉 상승으로 인하여 최종 난연제를 포함하는 분말 도료 조성물의 용융지수가 낮아져 균일한 용융 코팅성능을 발현하기 어려운 문제점이 있다.
If the primary compound modified resin (P1) is less than 10% by weight, the adhesive strength of the powder coating resin composition is weak and when the weight is more than 40% by weight, the melt index of the powder coating composition including the final flame retardant is lowered due to the excessive increase in the crosslinking degree between the resins. There is a problem in that it is difficult to express uniform melt coating performance.

접착성 수지제는 반응압출된 변성 고밀도폴리에틸렌 수지와 혼합되어서 접착성 및 기계적물성을 나타낼 수 있게 해주는 역할을 한다. 변성 고밀도폴리에틸렌 수지를 단독으로 반응하는 이유는 고밀도폴리에틸렌과 무수말레인산과의 반응성을 높이기 위한 것이다.
The adhesive resin agent is mixed with the reaction extruded modified high density polyethylene resin and serves to exhibit adhesiveness and mechanical properties. The reason for reacting the modified high density polyethylene resin alone is to increase the reactivity of the high density polyethylene with maleic anhydride.

변성 고밀도 폴리에틸렌과 접착성 수지제가 함께 혼합되어야만 접착성이 부여된다. 또한 접착성 수지조성물을 사용함으로서 최종개발제품이 코팅제로서 역할을 할 수 있도록 코팅특성을 보완해주는 역할을 한다.
Adhesiveness is imparted only when the modified high density polyethylene and the adhesive resin are mixed together. In addition, by using the adhesive resin composition serves to complement the coating properties so that the final product can act as a coating agent.

상기 난연제는 유기계 혼합 난연제가 바람직하며, 최종 개발제품(수지조성물(P2))의 난연제의 함유량은 5~30중량부이며, 5중량부이하인 경우 난연성의 부족으로 연소되는 문제점이 있으며, 30중량부이상에는 난연성은 우수하나 코팅제의 코팅물성을 저하하는 문제점을 안고 있어서 사용이 제한적이다. 난연성과 코팅물성을 고려하여 바람직하게는 20중량부 이하로 난연제의 함유량을 맞추어 사용하는 것이 좋다. 멜라민폴리포스페이트(MPP, Melamine poly phosphate 인함량 14~17% , 질소함량 40~44% , 평균입도 3.5~4.5μm )와 Red Phosphate(평균입도 10 μm이하)의 유기계 혼합 난연제가 사용될 수 있다.
The flame retardant is preferably an organic mixed flame retardant, the content of the flame retardant of the final product (resin composition (P2)) is 5 to 30 parts by weight, if less than 5 parts by weight, there is a problem of combustion due to lack of flame retardancy, 30 parts by weight The flame retardancy is excellent but has a problem of reducing the coating properties of the coating agent is limited in use. In consideration of flame retardancy and coating properties, it is preferable to adjust the content of the flame retardant to 20 parts by weight or less. Organic mixed flame retardants of melamine polyphosphate (MPP, Melamine poly phosphate phosphorus 14-17%, nitrogen content 40-44%, average particle size 3.5-4.5μm) and Red Phosphate (average particle size 10μm or less) may be used.

본 발명의 본 발명의 일실시예에 따른 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법은, 수지조성물(P2)은 펠렛 형태로 제조되고, 상기 수지조성물(P2)을 제조하는 단계(S20) 이후에, 조분쇄/미분쇄 단계를 거쳐 수지조성물(P2)을 10~300 μm로 분쇄하여 파우더를 제조하는 단계(S30)를 더 포함하여 구성되는 것이 바람직하다.
Method for producing a modified polyethylene powder for metal coating having a high flowability and flame retardancy according to an embodiment of the present invention, the resin composition (P2) is prepared in the form of pellets, the step of preparing the resin composition (P2) S20), preferably, further comprising the step (S30) of preparing a powder by grinding the resin composition (P2) to 10 ~ 300 μm through the coarsely pulverized / finely ground step.

본 발명의 본 발명의 일실시예에 따른 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법에 있어서, 변성수지(P1)를 제조하는 단계(S10)는, 펠릿 형태의 고밀도 폴리에틸렌과 파우더 상의 무수말레인산을 180~220℃ 조건에서 압출기로 그라프팅(grafting) 하여 진행되는 것이 바람직하다.
In the method of manufacturing a modified polyethylene powder for metal coating having high flowability and flame retardancy according to an embodiment of the present invention, the step of preparing the modified resin (P1) (S10), the pellet form of high density polyethylene and powder It is preferable to proceed by grafting maleic anhydride with an extruder at 180-220 degreeC conditions.

상기 온도 범위는 반응압출로 고밀도 폴리에틸렌의 에틸렌 결과을 끊고 무수말레인산이 결합될 수 있는 조건이다. 180~220도는 원료투입부에서 반응되어 나오는 부분까지의 압출기 존(zone)이 단계적으로 승온되는 조건을 나타내는 것이다.
The temperature range is a condition under which ethylene of the high density polyethylene is terminated by reaction extrusion and maleic anhydride can be bound. 180 to 220 degrees shows a condition in which the extruder zone from the raw material input part to the reacted part is elevated in stages.

본 발명의 본 발명의 일실시예에 따른 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법의 변성수지(P1)를 제조하는 단계(S10)에서 산화방지제 또는 개시제 중 적어도 하나가 추가로 혼합되는 것이 바람직하다. 산화방지제는 페놀와 포스페이트화합물 중에서 선택된 하나이며, 개시제는 과산화디쿠밀(DCP, dicumyl peroxide)인 것이 바람직하다.
At least one of an antioxidant or an initiator is additionally mixed in the step (S10) of preparing a modified resin (P1) of the modified polyethylene powder for metal coating method having a high fluidity and flame retardancy according to an embodiment of the present invention. It is preferable to be. The antioxidant is one selected from phenol and phosphate compounds, and the initiator is preferably dicumyl peroxide (DCP).

본 발명의 본 발명의 일실시예에 따른 수지조성물(P2)의 용융지수는 20~40 인 것이 바람직하다. 최종 제품의 용융지수가 20 미만인 경우, 흐름성 및 젖음성이 부족하여 코팅성이 낮은 문제점이 있고, 40이상으로 높은 경우는 유동성이 높아 코팅시 도막두께를 일정하게 맞추는 것이 힘들기 때문이다.
The melt index of the resin composition (P2) according to an embodiment of the present invention of the present invention is preferably 20 to 40. If the melt index of the final product is less than 20, there is a problem of low coating properties due to the lack of flowability and wettability, and high to 40 or more because it is difficult to uniformly adjust the coating film thickness during coating.

또한, 수지조성물(P2)을 제조하는 단계(S20)에서, 이산화티나늄(titanium dioxide), 카본블랙(carbon black), 프탈로사이아닌(phthalocyanine) 중에서 선택된 착색안료가 수지조성물(P2) 총 중량의 1~5중량% 이 더 혼합되는 것이 바람직하다.
In addition, in the step (S20) of preparing the resin composition (P2), the coloring pigment selected from titanium dioxide (carbon dioxide), carbon black (carbon black), phthalocyanine (phthalocyanine) is the total weight of the resin composition (P2) It is preferable that 1 to 5% by weight of is further mixed.

본 발명의 고유동성 및 난연성을 갖는 금속피복용 변성 폴리에틸렌 파우더 제조방법에 대하여 좀 더 구체적으로 설명한다.
It will be described in more detail with respect to the method of producing a modified polyethylene powder for metal coating having a high flowability and flame retardancy of the present invention.

본 발명은 용융흐름지수(MI, 190도, 2.16kg 조건)가 80 이상 고유동성을 가진 고밀도폴리에티렌(HDPE, High Density Polyethylene)에 무수말레인산을 반응압출하여 접착성을 부여하고 이를 주수지로 사용한다.
In the present invention, the melt flow index (MI, 190 degrees, 2.16kg conditions) is 80% high-density polystyrene (HDPE, High Density Polyethylene) has a high fluidity reaction extruded to give adhesion to the maleic anhydride and give it as the main resin use.

또한, 본 발명은 주수지에 더하여, 용도 및 요구물성에 따른 코팅특성을 가질 수 있도록 고밀도폴리에티렌(HDPE, 저밀도폴리에틸렌(LDPE, low density polyethylene), 선형저밀도폴리에틸렌(LLDPE, linear low density polyethylene), 중간밀도폴리에틸렌(MDPE, medium density polyethylene), 폴리카보네이트(PC, polycarbonate), 에틸렌비닐아세테이트(EVA, ethylene vinyl acetate), 폴리에틸렌테레프탈레이트(PET, polyethylene terephthalate), 에틸렌프로필렌디엔모노머(EPDM, ethylene propylene diene monomer), 스틸렌부타디엔스틸렌(SBS, stylene butadiene stylene), 스틸렌부타디엔러버(SBR, stylene butadiene rubber), 스틸렌에틸렌부타디엔스틸렌(SEBS, styrene etylene butadiene styrene), 부타디엔러버(BR, butadien rubber) 중 어느 하나 이상을 포함하는 금속피복용 변성 폴리에틸렌 수지 조성물을 제조하는 것이다.
In addition, the present invention, in addition to the main resin, high density polyethylene (HDPE, low density polyethylene (LDPE, low density polyethylene), linear low density polyethylene (LLDPE) so as to have a coating characteristic according to the use and required properties , Medium density polyethylene (MDPE), polycarbonate (PC, polycarbonate), ethylene vinyl acetate (EVA, ethylene vinyl acetate), polyethylene terephthalate (PET), ethylene propylene diene monomer (EPDM, ethylene propylene diene monomer), styrene butadiene styrene (SBS), styrene butadiene rubber (SBR, stylene butadiene rubber), styrene ethylene butadiene styrene (SEBS), butadiene rubber (BR, butadien rubber) It manufactures the modified polyethylene resin composition for metal coatings containing the above.

이때, 첨가제로 무수말레인산 외에도 개시제인 과산화디쿠밀(DCP, dicumyl peroxide)이 첨가될 수 있으며, 고밀도폴리에틸렌의 반응압출 공정에는 산화방지제로서 페놀, 포스페이트화합물 중 적어도 어느 하나 이상을 포함하는 것이 좋다.
In this case, in addition to maleic anhydride, an initiator, dicumyl peroxide (DCP, dicumyl peroxide) may be added, and the reaction extrusion process of high density polyethylene may include at least one or more of a phenol and a phosphate compound as an antioxidant.

상기 제조 공정중 1차 컴파운드(변성수지, P1) 제조단계는 반응압출을 통해 변성 고밀도폴리에틸렌 수지를 제조하는 것으로, 2차 컴파운드에 1차 컴파운드(변성수지) 사용량은 10~40중량% 처방하는 것이 바람직하다.
The primary compound (modified resin, P1) manufacturing step of the manufacturing process is to produce a modified high-density polyethylene resin through the reaction extrusion, the primary compound (modified resin) is used to formulate 10 to 40% by weight of the secondary compound desirable.

또한, 변성되어 개질된 주수지(변성주지)와 수지 조성물의 2차 컴파운딩 공정에는 최종 코팅제 조성물의 착색을 위해 화학적으로 반응성이 없고 내열성이 우수한 이산화티나늄(titanium dioxide), 카본블랙(carbon black), 프탈로사이아닌(phthalocyanine) 등의 착색안료가 수지 조성물 총 중량의 1~5중량% 첨가될 수 있으며 1~20㎛ 크기의 분말이 바람직하다.
In addition, in the secondary compounding process of the modified and modified main resin (modified resin) and the resin composition, titanium dioxide and carbon black, which are not chemically reactive and have excellent heat resistance, for coloring the final coating composition. ), And colored pigments such as phthalocyanine may be added in an amount of 1 to 5% by weight of the total weight of the resin composition, and a powder having a size of 1 to 20 μm is preferable.

본 발명에서는 난연성을 부여하고자 유무기계 난연제를 혼합하여 사용하였으며, 유기인계 난연제로는 인함량이 약 25~30%인 암모늄폴리포스페이트(APP, ammonium polyphosphate), 멜라민포스페이트(MP, melamine phosphate), 유기인산에스터(organophorus ester), 멜라민폴리포스페이트(MPP, Melamine poly phosphate), 적인 (Red Phosphate) 등의 군에 속하는 것 중 1종 내지 2종 이상이 선택될 수 있으며, 최종 파우더 코팅제 조성물의 입자크기가 50 μm이하임을 감안하여 유기인계 난연제의 입자크기는 1~20μm인 것을 특징으로 하며, 보다 바람직하게는 5~10μm인 것이 좋다.
In the present invention, a flame retardant having a non-mechanical machine was used in order to impart flame retardancy, and as an organophosphorus flame retardant, ammonium polyphosphate (APP, ammonium polyphosphate), melamine phosphate (MP, melamine phosphate), and organic phosphoric acid having a phosphorus content of about 25 to 30% Organophorus ester, melamine polyphosphate (MPP), red phosphate (Red Phosphate) and the like belonging to the group of one or more may be selected, the particle size of the final powder coating composition 50 The particle size of the organophosphorous flame retardant is 1-20 μm in consideration of the fact that it is less than μm, and more preferably 5-10 μm.

또한, 무기계 난연제로는 수산화알루미늄, 수산화마그네슘, 수산화칼슘, 붕산아연 화합물, 몰리브덴 화합물로 이루어진 군에서 적어도 1종 내지 2종 이상이 사용될 수 있으며 이때 무기계 난연제의 입자크기는 1~20μm인 것, 보다 바람직하게는 5~10μm인 것이 적합하다.
In addition, as the inorganic flame retardant, at least one or two or more kinds may be used in the group consisting of aluminum hydroxide, magnesium hydroxide, calcium hydroxide, zinc borate compound, and molybdenum compound, wherein the particle size of the inorganic flame retardant is 1-20 μm, more preferably. Preferably it is 5-10 micrometers.

또한, 무기첨가제로 탄산칼슘, 탈크 등이 사용될 수 있으며, 도막의 표면경도가 향상되는 효과가 있다.
In addition, calcium carbonate, talc, or the like may be used as the inorganic additive, and the surface hardness of the coating film may be improved.

상기 유기계 혼합 난연제의 입자크기가 1 미만일 경우 주수지와 컴파운드 혼합시 압출기내 부하량이 높아져 작업성이 저하되거나 뭉침현상에 의한 균일 분산이 어려울 수 있으며, 입자크기가 20 μm보다 클 경우 코팅 물성이 고르지 못해 외관품질을 저하 시키는 원인이 되므로 바람직하지 못하다.
When the particle size of the organic mixed flame retardant is less than 1, the load in the extruder increases when the main resin and the compound are mixed, and thus, workability may be degraded or uniform dispersion due to agglomeration may be difficult. When the particle size is larger than 20 μm, coating properties may be uneven. It is not preferable because it may cause the appearance quality to deteriorate.

또한, 상기 난연제는 열분해 과정에서 탄소성 char를 형성하여 연소를 어렵게 하는 특성이 있으며, 혼합 사용시 보다 적은량으로 효과적인 난연성을 발현할 수 있으므로, 본 발명에서는 상기의 유기계 혼합 난연제를 사용한다.
In addition, since the flame retardant has a property of making carbonaceous char difficult to burn during pyrolysis, and can express effective flame retardancy in a smaller amount when mixed, the organic-based mixed flame retardant is used in the present invention.

상기의 비할로겐 유기계 혼합 난연제는 전체 조성물 대비 5~30중량%를 첨가하며, 바람직하게는 5~20중량%를 사용하는 것이 좋다. 상기 난연조성물의 함량이 5중량% 이하이면 난연성을 기대하기 어려우며, 반면에 20중량%를 초과하는 경우에는 2축 압출기에서의 컴파운드 작업이 어려워 주수지인 플라스틱제의 기계적 물성을 저하시키는 우려가 있다.
The non-halogen organic mixed flame retardant is added to 5 to 30% by weight relative to the total composition, preferably 5 to 20% by weight is used. If the content of the flame retardant composition is 5% by weight or less, it is difficult to expect flame retardancy, while if it exceeds 20% by weight, compounding in a twin screw extruder is difficult, which may lower the mechanical properties of the plastic, which is the main resin. .

최종적으로 변성 고밀도폴리에틸렌 주수지와 수지 첨가물 및 난연제의 배합조성물은 컴파운드 공정을 통해 펠렛 형태로 제조되며, 분말 도료로 사용되기 위해 기계적 분쇄방식을 통해 1차 분말화 단계로 조분쇄되어 500 μm 정도가되고, 2차 분말화 단계인 미분쇄에서는 10~300 μm정도의 입자크기의 범위를 갖도록 분쇄된다.
Finally, the modified high-density polyethylene main resin, resin additive, and flame retardant compound composition are manufactured in pellet form through compounding process, and then used as a powder paint to be coarsely pulverized in the first powdering step through mechanical grinding to obtain 500 μm. In the pulverization, which is the second powdering step, the powder is pulverized to have a particle size in the range of about 10 to 300 μm.

압출공정Extrusion process 내용 및 작업조건 Content and working condition

1단계 : Stage 1 : 반응압출에In reaction extrusion 의한  by 주수지Main resin 제조 단계 Manufacturing stage

- 내용 : HDPE와 무수말레인산을 2축 twin 압출기를 이용하여 그라프팅한다. HDPE 자체는 비극성으로 접착력이 없다. 따라서 무수말레인산과 그라프팅하여 HDPE에 극성기(-COOH) 도입하는 것이다.
-Content: HDPE and maleic anhydride are grafted using twin screw twin extruder. HDPE itself is nonpolar and non-adhesive. Therefore, grafting with maleic anhydride introduces a polar group (-COOH) into HDPE.

개시제인 과산화디쿠밀(DCP)은 반응압출시 HDPE의 에틸렌 결합을 끊고 radical을 형성하고 여기에 무수말레인산의 극성기가 그라프팅 되도록 한다.
Dicumyl peroxide (DCP), an initiator, breaks down the ethylene bond of HDPE and forms radicals upon reaction extrusion, thereby allowing the polar group of maleic anhydride to be grafted thereto.

HDPE는 pellet, 무수말레인산과 DCP는 powder 형태로 압출기의 호퍼에서 혼합되어 투입된다. 실제 제조공정은 screw가 2개인 2축 twin 압출기를 통하여 제조되며, 작업조건은 압출기의 호퍼에서 다이스(입구부분)까지 온도를 승온하는 조건, 즉 180~220℃로 setting한다.
HDPE is pellet, maleic anhydride and DCP are mixed in powder form in the hopper of the extruder. The actual manufacturing process is made through a twin screw extruder with two screws, and the working conditions are set to 180 ~ 220 ℃ to raise the temperature from the hopper to the die (inlet).

2단계 : 코팅제 조성물(수지 조성물, Step 2: coating composition (resin composition, P2P2 ) 제조 단계A) manufacturing steps

- 내용 : 본 발명은 분말 코팅제를 제조하는 것을 목적으로 하기 때문에 상기의 1단계에서 제조된 반응물을 주수지로 하고 여기에 코팅제로서의 물성을 갖게 하기 위한 다른 수지물들과 첨가제를 혼련하여 코팅조성물을 제조하는 단계를 거친다. -Contents: Since the present invention aims to produce a powder coating agent, the reaction product prepared in step 1 is used as a main resin, and other resins and additives are kneaded to give physical properties as a coating agent, thereby preparing a coating composition. Go through the steps.

2단계에서는 용도 및 요구물성에 따른 코팅특성을 가질수 있도록 1단계에서 제조된 변성 고밀도폴리에틸렌(HDPE)에, 고밀도폴리에틸렌(HDPE), 저밀도폴리에틸렌(LDPE, low density polyethylene), 선형저밀도폴리에틸렌(LLDPE, linear low density polyethylene), 중간밀도폴리에틸렌(MDPE, medium density polyethylene), 폴리카보네이트(PC, polycarbonate), 에틸렌비닐아세테이트(EVA, ethylene vinyl acetate), 폴리에틸렌테레프탈레이트(PET, polyethylene terephthalate), 에틸렌프로필렌디엔모노머(EPDM, ethylene propylene diene monomer), 스틸렌부타디엔스틸렌(SBS, stylene butadiene stylene), 스틸렌부타디엔러버(SBR, stylene butadiene rubber), 스틸렌에틸렌부타디엔스틸렌(SEBS, styrene etylene butadiene styrene), 부타디엔러버(BR, butadien rubber) 중 어느 하나 이상을 포함하는 금속피복용 변성 폴리에틸렌 수지 조성물을 제조하며 여기에 기능성을 부여하기 위해 난연제, 착색안료 및 무기첨가제를 첨가한다.
In the second stage, the modified high density polyethylene (HDPE) prepared in the first stage, high density polyethylene (HDPE), low density polyethylene (LDPE, low density polyethylene), linear low density polyethylene (LLDPE, linear) to have coating characteristics according to the use and required properties low density polyethylene), medium density polyethylene (MDPE), polycarbonate (PC, polycarbonate), ethylene vinyl acetate (EVA, ethylene vinyl acetate), polyethylene terephthalate (PET), ethylene propylene diene monomer ( EPDM, ethylene propylene diene monomer, styrene butadiene stylene (SBS), styrene butadiene rubber (SBR, stylene butadiene rubber), styrene ethylene butadiene styrene (SEBS), butadiene rubber (BR, butadien rubber) To prepare a modified polyethylene resin composition for metal coating comprising any one or more of Flame retardants, coloring pigments and inorganic additives are added to impart functionality.

접착성 수지제는, 고밀도폴리에틸렌(HDPE), 저밀도폴리에틸렌(LDPE, low density polyethylene), 선형저밀도폴리에틸렌(LLDPE, linear low density polyethylene), 중간밀도폴리에틸렌(MDPE, medium density polyethylene), 폴리카보네이트(PC, polycarbonate), 에틸렌비닐아세테이트(EVA, ethylene vinyl acetate), 폴리에틸렌테레프탈레이트(PET, polyethylene terephthalate), 에틸렌프로필렌디엔모노머(EPDM, ethylene propylene diene monomer), 스틸렌부타디엔스틸렌(SBS, stylene butadiene stylene), 스틸렌부타디엔러버(SBR, stylene butadiene rubber), 스틸렌에틸렌부타디엔스틸렌(SEBS, styrene etylene butadiene styrene), 부타디엔러버(BR, butadien rubber) 중에서 선택된 적어도 하나 이상의 물질로 구성된다.
Adhesive resins include high density polyethylene (HDPE), low density polyethylene (LDPE, low density polyethylene), linear low density polyethylene (LLDPE, linear low density polyethylene), medium density polyethylene (MDPE, medium density polyethylene), polycarbonate (PC, polycarbonate), ethylene vinyl acetate (EVA), polyethylene terephthalate (PET, polyethylene terephthalate), ethylene propylene diene monomer (EPDM), styrene butadiene styrene (SBS, stylene butadiene stylene), styrene butadiene It is composed of at least one material selected from rubber (SBR, stylene butadiene rubber), styrene ethylene butadiene styrene (SEBS), butadiene rubber (BR, butadien rubber).

2단계의 작업조건은 1단계 상동하며 압출기를 통해 제조되므로 pellet형태로 생산된다.
The working conditions of the second stage are the same as the first stage and are produced in pellet form because they are manufactured through an extruder.

3단계 : 변성 폴리에틸렌 분말 코팅제로 활용하기 위한 분쇄공정Step 3: Grinding process for use as modified polyethylene powder coating

- 내용 : 상기의 1, 2단계는 코팅제의 기본적인 물성과 난연제를 혼련하여 pellet형태로 제조하기 위한 단계이며, 본 단계는 분말 코팅제로 활용하기위해 분쇄하는 단계를 뜻한다. 분쇄는 1차 조분쇄를 통해 500㎛ 이하로 제조되고 2차 미분쇄를 통해 10~300㎛의 범위를 갖도록 분쇄된다. 바람직하게는 250㎛의 크기를 갖는 변성 폴리에틸렌 분말 코팅제를 제조한다.
-Contents: Steps 1 and 2 above are for preparing pellets by mixing the basic properties of the coating agent with the flame retardant, and this step means grinding to use as a powder coating agent. Grinding is made to 500㎛ or less through the first coarse grinding, and grinding to have a range of 10 ~ 300㎛ through the second fine grinding. Preferably, a modified polyethylene powder coating having a size of 250 μm is prepared.

본 발명은 상기에서 언급한 바람직한 실시예와 관련하여 설명됐지만, 본 발명의 범위가 이러한 실시예에 한정되는 것은 아니며, 본 발명의 범위는 이하의 특허청구범위에 의하여 정하여지는 것으로 본 발명과 균등 범위에 속하는 다양한 수정 및 변형을 포함할 것이다.Although the present invention has been described in connection with the above-mentioned preferred embodiments, the scope of the present invention is not limited to these embodiments, and the scope of the present invention is defined by the following claims, and equivalent scope of the present invention. It will include various modifications and variations belonging to.

아래의 특허청구범위에 기재된 도면부호는 단순히 발명의 이해를 보조하기 위한 것으로 권리범위의 해석에 영향을 미치지 아니함을 밝히며 기재된 도면부호에 의해 권리범위가 좁게 해석되어서는 안될 것이다.The reference numerals set forth in the claims below are merely to aid the understanding of the present invention, not to affect the interpretation of the scope of the claims, and the scope of the claims should not be construed narrowly.

P1 : 변성수지, 1차 컴파운드
P2 : 수지조성물, 2차 컴파운드
P1: Modified resin, 1st compound
P2: Resin Composition, Secondary Compound

Claims (7)

용융지수가 60~100인 고유동성을 가진 고밀도폴리에티렌(HDPE, High Density Polyethylene)과 총 변성수지(P1)의 0.5~1.5 중량부의 무수말레인산을 반응압출하여 변성수지(P1)를 제조하는 단계(S10)와;
상기 변성수지(P1) 10~40중량부와, 고밀도폴리에틸렌(HDPE), 저밀도폴리에틸렌(LDPE, low density polyethylene), 선형저밀도폴리에틸렌(LLDPE, linear low density polyethylene), 중간밀도폴리에틸렌(MDPE, medium density polyethylene), 폴리카보네이트(PC, polycarbonate), 에틸렌비닐아세테이트(EVA, ethylene vinyl acetate), 폴리에틸렌테레프탈레이트(PET, polyethylene terephthalate), 에틸렌프로필렌디엔모노머(EPDM, ethylene propylene diene monomer), 스틸렌부타디엔스틸렌(SBS, stylene butadiene stylene), 스틸렌부타디엔러버(SBR, stylene butadiene rubber), 스틸렌에틸렌부타디엔스틸렌(SEBS, styrene etylene butadiene styrene), 부타디엔러버(BR, butadien rubber) 중에서 선택된 적어도 하나 이상의 물질로 구성된 접착성 수지제 30~85중량부와, 5~30중량부의 난연제를 혼합하여 수지조성물(P2)을 제조하는 단계(S20);를 포함하여 구성되는 것을 특징으로 하는 금속피복용 변성 폴리에틸렌 파우더 제조방법.
A step of preparing a modified resin (P1) by reacting and extruding high density polyethylene (HDPE, High Density Polyethylene) having a melt index of 60 to 100 and 0.5 to 1.5 parts by weight of maleic anhydride of the total modified resin (P1). (S10);
The modified resin (P1) 10 to 40 parts by weight, high density polyethylene (HDPE), low density polyethylene (LDPE, low density polyethylene), linear low density polyethylene (LLDPE, linear low density polyethylene), medium density polyethylene (MDPE, medium density polyethylene) ), Polycarbonate (PC, polycarbonate), ethylene vinyl acetate (EVA, ethylene vinyl acetate), polyethylene terephthalate (PET, polyethylene terephthalate), ethylene propylene diene monomer (EPDM, ethylene propylene diene monomer), styrene butadiene styrene (SBS, Adhesive resin composed of at least one material selected from stylene butadiene stylene (SBR), styrene butadiene rubber (SBR), styrene ethylene butadiene styrene (SEBS), butadiene rubber (BR) Containing ~ 85 parts by weight, 5 to 30 parts by weight of the flame retardant to prepare a resin composition (P2); Method for producing a modified polyethylene powder for metal coating, characterized in that.
제1항에 있어서,
상기 난연제는 입자크기는 1~20 μm인 것을 특징으로 하는 금속피복용 변성 폴리에틸렌 파우더 제조방법.
The method of claim 1,
The flame retardant is a method for producing a modified polyethylene powder for metal coating, characterized in that the particle size is 1 ~ 20 μm.
제1항 또는 제2항에 있어서,
상기 수지조성물(P2)은 펠렛 형태로 제조되고, 상기 수지조성물(P2)을 제조하는 단계(S20) 이후에,
상기 수지조성물(P2)을 10 ~ 300 μm로 분쇄하여 파우더를 제조하는 단계(S30);를 더 포함하여 구성되는 것을 특징으로 하는 금속피복용 변성 폴리에틸렌 파우더 제조방법.
The method according to claim 1 or 2,
The resin composition (P2) is prepared in the form of a pellet, after the step of preparing the resin composition (P2) (S20),
Method for producing a modified polyethylene powder for metal coating, characterized in that it further comprises; (S30) to produce a powder by grinding the resin composition (P2) to 10 ~ 300 μm.
제1항에 있어서,
상기 변성수지(P1)를 제조하는 단계(S10)는,
펠릿 형태의 고밀도 폴리에틸렌과 파우더 상의 무수말레인산을 180~220℃ 조건에서 압출기로 그라프팅(grafting) 하여 진행되는 것을 특징으로 하는 금속피복용 변성 폴리에틸렌 파우더 제조방법.
The method of claim 1,
The step of preparing the modified resin (P1) (S10),
Method for producing a modified polyethylene powder for metal coating, characterized in that the grafting of high density polyethylene in the form of pellets and maleic anhydride on a powder in an extruder at 180 ~ 220 ℃ condition.
제1항에 있어서,
상기 변성수지(P1)를 제조하는 단계(S10)에서 산화방지제 또는 개시제 중 적어도 하나가 추가로 혼합되되,
상기 산화방지제는 페놀와 포스페이트화합물 중에서 선택된 하나이며,
개시제는 과산화디쿠밀(DCP, dicumyl peroxide)인 것을 특징으로 하는 금속피복용 변성 폴리에틸렌 파우더 제조방법.
The method of claim 1,
At least one of an antioxidant or an initiator is further mixed in the step of preparing the modified resin (P1),
The antioxidant is one selected from phenol and phosphate compounds,
Initiator is dicumyl peroxide (DCP, dicumyl peroxide) characterized in that the method for producing a modified polyethylene powder for metal coating.
제1항 또는 제2항에 있어서,
상기 수지조성물(P2)의 용융지수는 20~40 인 것을 특징으로 하는 금속피복용 변성 폴리에틸렌 파우더 제조방법.
The method according to claim 1 or 2,
Melt index of the resin composition (P2) is a metal coating modified polyethylene powder manufacturing method, characterized in that 20 to 40.
제1항에 있어서,
상기 수지조성물(P2)을 제조하는 단계(S20)에서,
이산화티나늄(titanium dioxide), 카본블랙(carbon black), 프탈로사이아닌(phthalocyanine) 중에서 선택된 착색안료가 수지조성물(P2) 총 중량의 1~5중량% 이 더 혼합되는 것을 특징으로 하는 금속피복용 변성 폴리에틸렌 파우더 제조방법.



The method of claim 1,
In the step of preparing the resin composition (P2) (S20),
Metal pigments, characterized in that 1 to 5% by weight of the total weight of the resin composition (P2) is further mixed with a pigment selected from titanium dioxide, carbon black, and phthalocyanine. How to prepare modified polyethylene powder.



KR1020100086321A 2010-06-30 2010-09-03 Highly flowalbe and flame-retardant modified polyethylene resin composition for metal coating, modified polyethylene powder for metal coating, and mehtod of manufacturing the same KR101237741B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR20100062445 2010-06-30
KR1020100062445 2010-06-30

Publications (2)

Publication Number Publication Date
KR20120002393A true KR20120002393A (en) 2012-01-05
KR101237741B1 KR101237741B1 (en) 2013-02-26

Family

ID=45609819

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020100086321A KR101237741B1 (en) 2010-06-30 2010-09-03 Highly flowalbe and flame-retardant modified polyethylene resin composition for metal coating, modified polyethylene powder for metal coating, and mehtod of manufacturing the same

Country Status (1)

Country Link
KR (1) KR101237741B1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101418786B1 (en) * 2012-10-10 2014-07-11 주식회사 투에이취켐 Polyolefin powder and method for manufacturing the same
CN104610800A (en) * 2015-02-02 2015-05-13 芜湖市宝艺游乐科技设备有限公司 Thermal-insulating and fire-retardant polyethylene powder coating containing graphene oxide grated activated superfine aluminum silicate and preparation method of polyethylene powder coating
KR20230072429A (en) 2021-11-17 2023-05-24 가부시키가이샤 알박 Etching method and etching device

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101440032B1 (en) 2013-09-26 2014-09-24 주식회사 투에이취켐 Powder coating material and method for manufacturing the same
CN103773125A (en) * 2014-01-15 2014-05-07 芜湖市宝艺游乐科技设备有限公司 High-hardness polypropylene powder coating
KR101664271B1 (en) 2015-05-15 2016-10-11 류성걸 Polyethylene Powder for steel pipe coating manufacturing methods and polyethylene powder manufactured by someone
KR20180061682A (en) 2016-11-30 2018-06-08 배진성 Method for Preparing High Density Polyethylene Powder

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3148149B2 (en) * 1997-04-25 2001-03-19 カワサキ ケミカル ホールディング シーオー.,アイエヌシー. Polycarbonate / polyolefin resin composition, method for producing the same, and molded article
KR20000067127A (en) * 1999-04-23 2000-11-15 권문구 Component element of merterial for resistance to flame
KR100428558B1 (en) * 1999-12-07 2004-04-28 재단법인 포항산업과학연구원 A method for preparing a modified polyethyene with good adhesion and low viscosity for thermal spray
KR100627512B1 (en) * 2005-01-31 2006-09-22 엘에스전선 주식회사 Composition for production flame retardant insulating material of halogen free type with low temperature resistance properties

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101418786B1 (en) * 2012-10-10 2014-07-11 주식회사 투에이취켐 Polyolefin powder and method for manufacturing the same
CN104610800A (en) * 2015-02-02 2015-05-13 芜湖市宝艺游乐科技设备有限公司 Thermal-insulating and fire-retardant polyethylene powder coating containing graphene oxide grated activated superfine aluminum silicate and preparation method of polyethylene powder coating
KR20230072429A (en) 2021-11-17 2023-05-24 가부시키가이샤 알박 Etching method and etching device

Also Published As

Publication number Publication date
KR101237741B1 (en) 2013-02-26

Similar Documents

Publication Publication Date Title
KR101237741B1 (en) Highly flowalbe and flame-retardant modified polyethylene resin composition for metal coating, modified polyethylene powder for metal coating, and mehtod of manufacturing the same
CN104086894A (en) A polarity-modified polypropylene composite material and a preparing method thereof
CN104693604A (en) Halogen-free flame retardant glass-fiber reinforced polypropylene composite material and preparation method thereof
CN103298876A (en) High filler loaded polymer composition
CN109734990A (en) Two-dimensional material nano modification flame-proof ethylene-vinyl acetate copolymer method
MX2013009026A (en) Flame retardant compositions.
US9346946B2 (en) Composite materials and shaped articles
CN110317399A (en) Expanded flame-retardant polypropylene lightweighting materials and its continuous extrusion foaming preparation method
CN101613505B (en) Environment-friendly fire retardant polypropylene material of non-precipitating fire retardant and method for preparing same
WO2015021148A1 (en) Biohydrogenated plastics
CN110498968A (en) Polypropylene thermoplastic elastomer composite material and preparation method thereof
CN101550242A (en) Darkcoloured halogen-free expandable polyolefine fire retardant and preparation method thereof
CN113480806A (en) Composite resin material with improved properties and use thereof in automotive trim materials
CN102295797B (en) Zero-halogen flame-retardant polyolefin material and preparation method as well as application thereof
CN101358000A (en) Phosphorus series non-halogen composite flame retardant for polyolefin, preparation method thereof and flame retardant polyolefin
CA3139602C (en) Polypropylene board and method for preparing same
CN110938257B (en) Low-VOC (volatile organic compound) volatilization and high-flame-retardant TPO (thermoplastic polyolefin) composite material and preparation method thereof
KR20120119859A (en) Polypropylene based powder coatings containing hot-melt type flame retardant and production method there of
CN102924797B (en) Weathering resistance polyethylene agriculture film resin composition and preparation method thereof
KR100988249B1 (en) Manufacturing method of thermoplastic powder coating material containing non-halogen hybrid flame retardant
CN114213711A (en) Preparation method of halogen-free composite flame retardant, flame-retardant polyolefin and preparation method thereof
JPS61276840A (en) Propylene polymer resin composition
CN116041823B (en) Halogen-free intumescent flame-retardant antistatic thermoplastic elastomer composite foaming material and preparation method thereof
JPH0841274A (en) Propylene-based resin composition for coating
CN112759883B (en) Slush molding grade TPE material and preparation method and application thereof

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20171228

Year of fee payment: 6

FPAY Annual fee payment

Payment date: 20190110

Year of fee payment: 7

FPAY Annual fee payment

Payment date: 20200206

Year of fee payment: 8