KR20000066740A - Propylene-ethylene-butene-1 copolymer for heat sealing film and resin composition comprising the same - Google Patents

Propylene-ethylene-butene-1 copolymer for heat sealing film and resin composition comprising the same Download PDF

Info

Publication number
KR20000066740A
KR20000066740A KR1019990014048A KR19990014048A KR20000066740A KR 20000066740 A KR20000066740 A KR 20000066740A KR 1019990014048 A KR1019990014048 A KR 1019990014048A KR 19990014048 A KR19990014048 A KR 19990014048A KR 20000066740 A KR20000066740 A KR 20000066740A
Authority
KR
South Korea
Prior art keywords
group
butene
ethylene
propylene
cyclopentenyl
Prior art date
Application number
KR1019990014048A
Other languages
Korean (ko)
Other versions
KR100607538B1 (en
Inventor
전은진
김미옥
Original Assignee
유현식
삼성종합화학 주식회사
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 유현식, 삼성종합화학 주식회사 filed Critical 유현식
Priority to KR1019990014048A priority Critical patent/KR100607538B1/en
Publication of KR20000066740A publication Critical patent/KR20000066740A/en
Application granted granted Critical
Publication of KR100607538B1 publication Critical patent/KR100607538B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/02Ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/02Polymerisation in bulk
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/18Suspension polymerisation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/34Polymerisation in gaseous state
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/04Monomers containing three or four carbon atoms
    • C08F210/06Propene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/04Monomers containing three or four carbon atoms
    • C08F210/08Butenes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/642Component covered by group C08F4/64 with an organo-aluminium compound
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/646Catalysts comprising at least two different metals, in metallic form or as compounds thereof, in addition to the component covered by group C08F4/64
    • C08F4/6465Catalysts comprising at least two different metals, in metallic form or as compounds thereof, in addition to the component covered by group C08F4/64 containing silicium
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE: Provided is a propylene-ethylene-butene-1 copolymer resin for a heat-adhesive film, which is excellent in a blocking-resistance and is used for a food packing. CONSTITUTION: The propylene-ethylene-butene-1 copolymer resin having a melting temperature of 127-135°C and a melting calorie of 65-83 J/g is produced by polymerizing propylene, ethylene, and butene-1 by a gas phase or a bulk slurry polymerization in the presence of a solid complex titanium catalyst, an organo aluminum cocatalyst, and an organo silicon compound as an outer electron donor (formula SiR1R2(OR3)2) having bulky two alkyl groups and two alkoxy groups. The ratio of the ethylene/the butene-1 is less than 1. In the formula, R1 is cyclopentyl, 3-propylpentyl, 1-cyclopentylpropyl, etc., R2 and R3 are an alkyl, a cycloalkyl, an aryl.

Description

열접착성 필름용 프로필렌-에틸렌-부텐-1 공중합체 및 이를 포함하는 수지 조성물{PROPYLENE-ETHYLENE-BUTENE-1 COPOLYMER FOR HEAT SEALING FILM AND RESIN COMPOSITION COMPRISING THE SAME}Propylene-ethylene-butene-1 copolymer for heat-adhesive film and resin composition comprising same {PROPYLENE-ETHYLENE-BUTENE-1 COPOLYMER FOR HEAT SEALING FILM AND RESIN COMPOSITION COMPRISING THE SAME}

본 발명은 고체 착물 티타늄 촉매, 유기 알루미늄 조촉매, 외부전자공여체로서 두 개의 알킬기와 두 개의 알콕시기를 갖는 유기규소 화합물의 존재하에 프로필렌, 에틸렌, 부텐-1 각각의 모노머를 용매를 사용하지 않는 기상 혹은 벌크 슬러리 중합공정을 사용하여 중합시켜 제조되는 프로필렌-에틸렌-부텐-1 공중합체 수지 및 이를 포함하는 수지 조성물에 관한 것이다.The present invention provides a gaseous phase without using a solvent for each monomer of propylene, ethylene, butene-1 in the presence of a solid complex titanium catalyst, an organoaluminum promoter, an organosilicon compound having two alkyl groups and two alkoxy groups as external electron donors. The present invention relates to a propylene-ethylene-butene-1 copolymer resin prepared by polymerization using a bulk slurry polymerization process and a resin composition comprising the same.

무연신 폴리프로필렌계 필름은 가격이 저렴하고 열접착 특성이 우수하여 식품포장에 널리 사용되고 있다. 포장시 생산속도를 높이면 열접착에 소요되는 시간이 감소하므로 고온에서 접착하거나 열접착층에 사용되는 폴리머의 열접착온도가 낮아야 한다. 그러나 고온에서 접착하면 열에 의해 필름이 손상될 수 있고, 열접착온도를 낮추기 위하여 낮은 용융온도의 폴리머, 예를 들어 프로필렌-에틸렌-부텐-1 공중합체를 열접착층에 적용하는 경우 블록킹이 발생하여 생산속도를 높이는데 한계가 있다. 이 경우 블록킹의 원인은 저분자량의 저결정성 성분의 표면전이에 의한 것으로 알려져 있다.Unstretched polypropylene-based films are widely used in food packaging because of their low cost and excellent thermal adhesive properties. Increasing the production speed during packaging reduces the time required for thermal bonding, so the thermal bonding temperature of the polymer used at the high temperature or the thermal bonding layer should be low. However, adhesion at high temperatures may damage the film due to heat, and in the case of applying a low melting temperature polymer, such as propylene-ethylene-butene-1 copolymer, to the thermal bonding layer to lower the thermal bonding temperature, blocking occurs. There is a limit to speeding up. In this case, the cause of blocking is known to be due to the surface transition of low crystalline components of low molecular weight.

종래 이와 같은 문제점을 해결하기 위하여 여러 가지 방법이 사용되어 왔다. 예로서 열접착용 수지에 블록킹 방지제를 혼합하는 방법이 그것이다. 사용되는 블록킹 방지제로는 이산화실리콘이 가장 널리 사용되며(EP-A-27 586, EP-A-189 242), 경화된 실리콘(EP-A-242 055), 폴리아미드-6, 폴리아미드-6,6, 폴리에틸렌 테레프탈레이트, 폴리에틸렌 벤조에이트(DE-A-2 244) 등이 사용되기도 한다. 그러나 블록킹 방지제를 과도하게 사용하면 필름의 투명성이나 광택성이 저하하고 적게 사용하면 블록킹이 발생하는 단점이 있다. 또한 용매 슬러리 중합에 의해서 제조된 프로필렌-에틸렌-부텐-1 삼원공중합체가 기상 또는 벌크 슬러리 중합에 의한 공중합체에 비해 내블록킹성은 우수하지만 제조비용이 높은 단점이 있다.Conventionally, various methods have been used to solve this problem. An example is a method of mixing a blocking agent with a resin for thermal bonding. As the blocking agent used, silicon dioxide is the most widely used (EP-A-27 586, EP-A-189 242), cured silicone (EP-A-242 055), polyamide-6, polyamide-6 , 6, polyethylene terephthalate, polyethylene benzoate (DE-A-2 244) and the like may be used. However, excessive use of the antiblocking agent has a disadvantage in that the transparency or glossiness of the film is lowered, and in the case of less use, blocking occurs. In addition, the propylene-ethylene-butene-1 terpolymer prepared by solvent slurry polymerization has better blocking resistance than the copolymer by gas phase or bulk slurry polymerization, but has a disadvantage of high manufacturing cost.

본 발명의 목적은 상기와 같은 문제점을 개선하기 위한 것으로서, 기상 또는 벌크 슬러리 중합을 하므로써 제조 비용이 저렴하고, 중합공정에서 특정의 외부전자공여체를 사용하므로써 낮은 용융온도에서도 결정화도가 높고 표면전이되는 물질이 적어 열처리시 흐림도 변화가 낮고, 열접착 온도가 낮으면서 내블록킹성이 우수하여 고속포장시에도 효과적으로 적용이 가능한 열접착성 필름용 프로필렌-에틸렌-부텐-1 공중합체 수지 및 이를 포함하는 수지 조성물을 제공하는 것이다.An object of the present invention is to improve the above problems, the production cost is low by gas phase or bulk slurry polymerization, the crystallinity is high and the surface transition even at low melting temperature by using a specific external electron donor in the polymerization process Propylene-ethylene-butene-1 copolymer resin for heat-adhesive film which has low change of cloudiness during heat treatment, low blocking temperature and excellent blocking resistance and can be effectively applied even at high speed packaging. It is to provide a composition.

본 발명의 프로필렌-에틸렌-부텐-1 공중합체 수지는 고체 착물 티타늄 촉매, 유기 알루미늄 조촉매, 외부전자공여체로서 두 개의 알킬기와 두 개의 알콕시기를 갖는 유기규소 화합물의 존재하에 프로필렌, 에틸렌, 부텐-1 각각의 모노머를 용매를 사용하지 않는 기상 혹은 벌크 슬러리 중합공정을 사용하여 중합시켜 제조되는 것을 특징으로 한다.The propylene-ethylene-butene-1 copolymer resin of the present invention is a propylene, ethylene, butene-1 in the presence of a solid complex titanium catalyst, an organoaluminum promoter, an organosilicon compound having two alkyl groups and two alkoxy groups as external electron donors. Each monomer is characterized in that it is prepared by polymerizing using a gas phase or bulk slurry polymerization process without using a solvent.

상기와 같이 제조된 본 발명의 프로필렌-에틸렌-부텐-1 공중합체는 에틸렌/부텐-1의 몰비가 1.0 이하이고, 용융온도가 127∼135℃, 용융열량이 65∼83J/g이며, 이러한 특성에 의하여 기존의 프로필렌-에틸렌-부텐-1 공중합체에 비하여 열접착온도를 낮게 유지하면서 내블록킹성이 향상된 장점을 갖는다.The propylene-ethylene-butene-1 copolymer of the present invention prepared as described above has a molar ratio of ethylene / butene-1 of 1.0 or less, a melting temperature of 127 to 135 ° C and a heat of fusion of 65 to 83 J / g. As compared to the existing propylene-ethylene-butene-1 copolymer has the advantage of improved blocking resistance while maintaining a low thermal bonding temperature.

프로필렌-에틸렌-부텐-1 공중합체의 에틸렌/부텐-1의 몰비가 1.0을 초과하면 열접착성 필름제조후 숙성시 저결정성 성분이 표면으로 전이하여 블록킹이 발생한다. 에틸렌/부텐-1의 몰비가 1.0 이하라도 용융온도가 135℃를 넘으면 열접착온도가 높아지고 용융온도가 127℃ 미만이면 블록킹이 발생한다.If the molar ratio of ethylene / butene-1 of the propylene-ethylene-butene-1 copolymer exceeds 1.0, the low crystalline component transfers to the surface during aging after the production of the heat-adhesive film, and blocking occurs. Even if the molar ratio of ethylene / butene-1 is 1.0 or less, the thermal bonding temperature is high when the melting temperature exceeds 135 ° C, and blocking occurs when the melting temperature is less than 127 ° C.

본 발명의 프로필렌-에틸렌-부텐-1 공중합체 수지의 제조에 사용되는 고체 착물 티타늄 촉매는 마그네슘 화합물과 티탄 화합물을 접촉시킴으로써 제조되고 이때 티탄 화합물은 테트라 할로겐화 티탄이 바람직하다.The solid complex titanium catalyst used in the production of the propylene-ethylene-butene-1 copolymer resin of the present invention is prepared by contacting a magnesium compound with a titanium compound, wherein the titanium compound is preferably tetrahalogenated titanium.

이러한 고체 착물 티타늄 촉매로는 특별한 제한은 없고, 공지의 것을 선택하여 사용할 수 있다. 또한 중합공정시 조촉매로는 고체 착물 티타늄 촉매와 함께 사용될 수 있는 것으로 공지된 유기 알루미늄 화합물들을 선택, 사용할 수 있다.There is no restriction | limiting in particular as such a solid complex titanium catalyst, A well-known thing can be selected and used. In addition, as a cocatalyst in the polymerization process, an organoaluminum compound known to be used together with a solid complex titanium catalyst may be selected and used.

본 발명의 프로필렌-에틸렌-부텐-1 공중합체 수지의 제조에 사용되는 외부전자공여체로는 두 개의 알킬기와 두 개의 알콕시기를 가지는 일반식(Ⅰ)과 같이 표시되는 유기규소 화합물을 사용한다.As an external electron donor used in the preparation of the propylene-ethylene-butene-1 copolymer resin of the present invention, an organosilicon compound represented by formula (I) having two alkyl groups and two alkoxy groups is used.

SiR1R2(OR3)2---------------- (Ⅰ)SiR 1 R 2 (OR 3 ) 2 ---------------- (Ⅰ)

위의 식에서 R1은 시클로펜틸기, 2-메틸시클로펜틸기, 3-메틸시클로펜틸기, 2-에틸시클로펜틸기, 3-프로필펜틸기, 3-이소프로필시클로펜틸기, 3-부틸시클로펜틸기, 3-터셔리부틸시클로펜틸기, 2,2-디메틸시클로펜틸기, 2,3-디메틸시클로펜틸기, 2,5-디메틸시클로펜틸기, 2,2,5-트리메틸시클로펜틸기, 2,3,4,5-테트라메틸시클로펜틸기, 2,2,5,5-테트라메틸시클로펜틸기, 1-시클로펜틸프로필기, 1-메틸-1-시클로펜틸에테프기, 시클로펜테닐기, 2-시클로펜테닐기, 3-시클로펜테닐기, 2-메틸-1-시클로펜테닐기, 2-메틸-3-시클로펜테닐기, 3-메틸-3-시클로펜테닐기, 2-에틸-3-시클로펜테닐기, 2,4-디메틸-3-시클로펜틸기, 2,5-디메틸-3-시클로펜테닐기, 2,3-4,5-테트라메틸-3-시클로펜테닐기, 2,2,5,5-테트라메틸-3-시클로펜테닐기, 1,3-시클로펜타디에닐기, 2,4-시클로펜타디에닐기, 1,4-시클로펜타디에닐기, 2-에틸-2,4-시클로펜타디에닐기, 2,2-디메틸-2,4-시클로펜타디에닐기, 2,3-디메틸-2,4-시클로펜타디에닐기, 2,5-디메틸-2,4-시클로펜타디에닐기, 2,3,4,5-테트라메틸-2,4-시클로펜타디에닐기 등이고, R2는 알킬기, 시클로알킬기, 아릴기 등이며, R3는 알킬기, 시클로알킬기, 아릴기 등인데, 특히 R1과 R2가 모두 시클로펜틸기이고 R3은 메틸기 또는 에틸기인 유기 규소 화합물을 사용하는 것이 바람직하다. 고리 탄소수 6 이상의 벌키한 시클로알킬기 한 개와 고리 화합물이 아닌 알킬기 한 개 그리고 두 개의 알콕시기를 가지는 유기규소 화합물을 외부전자공여체로서 사용하는 경우에는 생성되는 폴리머의 결정화도(용융열량)가 낮아 블록킹이 발생한다.In the above formula, R 1 is a cyclopentyl group, 2-methylcyclopentyl group, 3-methylcyclopentyl group, 2-ethylcyclopentyl group, 3-propylpentyl group, 3-isopropylcyclopentyl group, 3-butylcyclophene Tyl group, 3-tertarybutylcyclopentyl group, 2,2-dimethylcyclopentyl group, 2,3-dimethylcyclopentyl group, 2,5-dimethylcyclopentyl group, 2,2,5-trimethylcyclopentyl group, 2 , 3,4,5-tetramethylcyclopentyl group, 2,2,5,5-tetramethylcyclopentyl group, 1-cyclopentylpropyl group, 1-methyl-1-cyclopentylethane group, cyclopentenyl group, 2-cyclopentenyl group, 3-cyclopentenyl group, 2-methyl-1-cyclopentenyl group, 2-methyl-3-cyclopentenyl group, 3-methyl-3-cyclopentenyl group, 2-ethyl-3-cyclopentene Neyl group, 2,4-dimethyl-3-cyclopentyl group, 2,5-dimethyl-3-cyclopentenyl group, 2,3-4,5-tetramethyl-3-cyclopentenyl group, 2,2,5,5 -Tetramethyl-3-cyclopentenyl group, 1,3-cyclopentadienyl group, 2,4-cyclopentadienyl group, 1,4- Clopentadienyl group, 2-ethyl-2,4-cyclopentadienyl group, 2,2-dimethyl-2,4-cyclopentadienyl group, 2,3-dimethyl-2,4-cyclopentadienyl group, 2, 5-dimethyl-2,4-cyclopentadienyl group, 2,3,4,5-tetramethyl-2,4-cyclopentadienyl group and the like, R 2 is an alkyl group, a cycloalkyl group, an aryl group and the like, and R 3 is It is an alkyl group, a cycloalkyl group, an aryl group, etc. It is preferable to use the organosilicon compound especially whose R <1> and R <2> are both cyclopentyl groups and R <3> is a methyl group or an ethyl group. When an organosilicon compound having one bulky cycloalkyl group having 6 or more ring carbon atoms, one alkyl group and two alkoxy groups which are not cyclic compounds is used as an external electron donor, blocking occurs due to low crystallinity (melt heat amount) of the produced polymer. .

본 발명의 프로필렌-에틸렌-부텐-1 공중합체 수지의 중합방식은 수율을 향상시키고 제조비용을 절감하기 위하여 기상 또는 벌크 슬러리 중합공정을 사용한다.The polymerization method of the propylene-ethylene-butene-1 copolymer resin of the present invention uses a gas phase or bulk slurry polymerization process to improve the yield and reduce the production cost.

본 발명의 열접착성 필름용 수지 조성물은 상기한 프로필렌-에틸렌-부텐-1 공중합체 수지에 내열안정제, 블록킹 방지제, 중화제 등과 같은 통상의 열접착용 수지 조성물용 각종 첨가제를 첨가하여 제조된다.The resin composition for heat-adhesive films of the present invention is prepared by adding various additives for common heat-adhesive resin compositions such as heat stabilizers, antiblocking agents, neutralizing agents, and the like to the above propylene-ethylene-butene-1 copolymer resins.

본 발명의 수지 조성물을 제조하는 방법에 있어서는 특별한 제한이 없고 보편적으로 알려진 폴리프로필렌 수지 조성물을 제조하는 방법을 이용할 수 있다. 공중합체 수지와 각 첨가제 성분들을 원하는 순서에 따라 자유롭게 선택하여 혼합할 수 있다. 통상 공중합체 수지와 각 성분들을 필요한 양으로 첨가하여 니더, 롤, 반바리 믹서 등의 혼련기와 1축 또는 2축 압출기 등을 사용하여 혼련하는 방법이 이용될 수 있다.There is no restriction | limiting in particular in the method of manufacturing the resin composition of this invention, The method of manufacturing the polypropylene resin composition generally known can be used. The copolymer resin and each additive component can be freely selected and mixed in a desired order. Usually, a method of kneading using a kneader such as a kneader, a roll, a short-barrier mixer, and a single or twin screw extruder by adding a copolymer resin and each component in a required amount may be used.

본 발명의 공중합체 수지와 수지 조성물은 열접착용 플라스틱 필름의 재료로 사용된다.The copolymer resin and resin composition of this invention are used as a material of the plastic film for thermal bonding.

본 발명의 공중합체 수지 자체 또는 이를 포함하는 수지 조성물을 이용하여 제조되는 열접착성 플라스틱 필름은 통상의 T-다이법에 의해 성형될 수 있다. 또한 플라스틱 필름의 형태로는 단층의 플라스틱 필름 외에 양쪽 최외층 혹은 한쪽 최외층에 본 발명의 수지 조성물을 사용한 다층 필름의 형태로 적용하는 것도 가능하다. 필름제조시 코로나 방전처리, 화염처리 등으로 표면처리를 하여 젖음성을 향상시킬 수도 있다.The heat-adhesive plastic film produced using the copolymer resin itself or the resin composition containing the same of the present invention can be molded by a conventional T-die method. Moreover, as a form of a plastic film, it is also possible to apply in the form of the multilayer film using the resin composition of this invention in both outermost layers or one outermost layer other than a single plastic film. Wetness may be improved by surface treatment such as corona discharge treatment or flame treatment during film production.

본 발명은 하기의 실시예 및 비교예에 의하여 보다 구체적으로 이해될 수 있으며, 하기의 실시예는 본 발명을 예시하기 위한 예에 지나지 않으며 본 발명의 보호범위를 제한하고자 하는 것은 아니다.The present invention can be understood in more detail by the following examples and comparative examples, the following examples are only examples for illustrating the present invention and are not intended to limit the protection scope of the present invention.

각 실시예 및 비교예에 있어서의 제반물성의 측정방법은 다음과 같다.The measuring method of the physical properties in each Example and a comparative example is as follows.

- 에틸렌 함량/부텐-1 함량 : 적외선 흡수 스펙트럼법-Ethylene Content / Butene-1 Content: Infrared Absorption Spectroscopy

- MI : ASTM D1238, 230℃, 2.16㎏-MI: ASTM D1238, 230 ℃, 2.16㎏

- 용융온도/용융열량 : 퍼킨엘머사 DSC-7형을 사용하여 0.1mm의 프레스 쉬트를 일단 200℃까지 가열하고 10℃/분으로 25℃까지 냉각한 후에 10℃/분의 승온속도로 25∼200℃까지 측정하여 최대 흡열피크를 나타내는 온도 Tm을 DSC 융점으로, 70℃ 용융완료 온도 까지의 열량을 용융열량으로 하였다.-Melting temperature / melting heat amount: Using a Perkin Elmer DSC-7 type, 0.1mm press sheet is heated to 200 ° C once, cooled to 25 ° C at 10 ° C / min, and then 25 to 25 ° C at a heating rate of 10 ° C / min. The temperature Tm which measured to 200 degreeC and shows the maximum endothermic peak was DSC melting | fusing point, and the heat amount to 70 degreeC melting | fusing completion temperature was made into the heat of fusion.

- 열처리시 흐림도 변화 : 통상의 실험실용 무연신 필름기를 사용하여 공중합체 수지를 30㎛의 필름으로 성형하고 이 필름을 100℃ 오븐에서 1시간 열처리후 ASTM D1003에 의하여 흐림도를 측정하여 열처리 전의 흐림도 변화와의 차이값을 흐림도 변화로 하였다.-Cloudiness change during heat treatment: Copolymer resin is formed into 30㎛ film using normal draw-free film machine for laboratory, and this film is heat treated in 100 ℃ oven for 1 hour and then measured by cloudiness according to ASTM D1003. The difference value with the blurring degree was made into the blurring degree.

- 블록킹력 : 상기 필름을 면적 10㎠로 절단후 두장의 필름을 겹쳐 두장의 유리판 사이에 놓고 500g/㎠의 무게를 가한후 40℃ 오븐에서 7일간 열처리후 필름의 박리강도를 측정하였다. 블록킹력이 낮을수록 내블록킹성이 우수하다.-Blocking force: The film was cut into an area of 10 cm 2, two films were overlapped, placed between two glass plates, and weighed 500 g / cm 2, and then the peel strength of the film was measured after heat treatment in an oven at 40 ° C. for 7 days. The lower the blocking force, the better the blocking resistance.

- 열접착 온도 : 두장의 필름을 12㎛의 폴리에틸렌 테레프탈레이트 필름 사이에 넣고 2㎏f의 하중하에, 1.5초간 접착한다. 접착된 필름을 폭 10mm로 재단하여 필름의 계면 박리강도를 측정한다. 박리강도가 600g일때의 접착온도를 열접착온도로 한다.Heat bonding temperature: Two films are put between 12 micrometers polyethylene terephthalate films, and they adhere for 1.5 second under a load of 2 kgf. The bonded film is cut to a width of 10 mm to measure the interfacial peel strength of the film. The bonding temperature when the peel strength is 600 g is the thermal bonding temperature.

각 실시예 및 비교예를 표 1에 나타내었다.Each Example and the comparative example are shown in Table 1.

실시예Example

실시예의 프로필렌-에틸렌-부텐-1 공중합체 수지의 중합방법은 다음과 같다.The polymerization method of the propylene-ethylene-butene-1 copolymer resin of the Example is as follows.

용량 2리터의 고압 반응기를 프로필렌으로 세정한 다음 고체 착물 티타늄 촉매 27mg(티타늄 원자로서 환산시의 티타늄 성분은 0.02밀리몰)을 유리 바이알(vial)에 담아 반응기 안에 장착한 후 반응기 안을 질소/진공 상태로 3회 반복하여 진공상태로 만들었다. 조촉매로서 트리에틸알루미늄 10밀리몰과 외부전자공여체로서 고리 탄소수 5인 두 개의 벌키한 시클로알킬기와 두 개의 알콕시기를 가지는 유기 규소 화합물인 디시클로펜틸디메톡시실란 0.1밀리몰을 n-헥산 1000㎖와 함께 반응기에 주입하였다. 헥산이 주입된 후 수소 100N㎖를 투입하였다. 에틸렌과 부텐-1은 반응기와 연결된 별도의 용기내에서 반응에 적용할 몰비(표 1 참조)로 충분히 교반한 뒤 반응기로 주입하였다. 주입한 후 온도를 70℃로 상승시킨 후 프로필렌 가스를 주입하여 프로필렌이 기체-액체 평형 상태가 될 때 교반기로 반응기 안에 장착된 바이알을 깨어서 반응을 시작하였다. 반응은 30분을 행하였고 반응이 끝난 후 고압물의 내용물을 실온으로 냉각시킨 후 에탄올을 10㎖정도 주입하여 촉매 활성점을 제거하였다. 이때 생성되는 중합체를 여벌 수집하고 50℃의 진공오븐에서 6시간 정도 건조시켜 프로필렌-에틸렌-부텐-1 공중합체를 백색 분말로서 얻었다.A 2 liter high pressure reactor was washed with propylene, and then 27 mg of a solid complex titanium catalyst (0.02 mmol of titanium in terms of titanium atoms) were placed in a glass vial and placed in a reactor in a nitrogen / vacuum state. The vacuum was repeated three times. 0.1 mmol of dicyclopentyldimethoxysilane, an organosilicon compound having 10 mmol of triethylaluminum as cocatalyst and two bulky cycloalkyl and two alkoxy groups having 5 ring carbon atoms as external electron donor, together with 1000 ml of n-hexane Injected into. After hexane was injected, 100Nml of hydrogen was added thereto. Ethylene and butene-1 were sufficiently stirred at a molar ratio (see Table 1) to be applied to the reaction in a separate vessel connected to the reactor and then injected into the reactor. After the injection, the temperature was raised to 70 ° C., followed by injection of propylene gas, and the reaction was started by breaking the vial mounted in the reactor with the stirrer when the propylene became a gas-liquid equilibrium. The reaction was carried out for 30 minutes and after the reaction was completed, the contents of the high pressure product was cooled to room temperature, and about 10 ml of ethanol was injected to remove the catalyst active site. The polymer produced at this time was collected extraly and dried in a vacuum oven at 50 ° C. for about 6 hours to obtain a propylene-ethylene-butene-1 copolymer as a white powder.

비교예Comparative example

표 1에 나타낸 바와 같이 외부전자공여체로서 실시예에서 사용한 디시클로펜틸디메톡시실란 또는 고리 탄소수 6개인 벌키한 시클로알킬기 한 개와 고리 화합물이 아닌 알킬기 한 개 및 두 개의 알콕시기를 갖는 유기 규소 화합물인 시클로헥실메틸디메톡시 실란을 사용하고, 에틸렌과 부텐-1의 함량을 변경시킨 것 이외에 다른 과정은 실시예와 동일한 과정으로 중합을 실시하였다.As shown in Table 1, cyclohexyl, an organosilicon compound having one dicyclopentyldimethoxysilane or a bulky cycloalkyl group having 6 ring carbon atoms and an alkyl group and two alkoxy groups other than a cyclic compound, used in the examples as an external electron donor The polymerization was carried out in the same manner as in Example except that methyldimethoxy silane was used and the contents of ethylene and butene-1 were changed.

A : Dicyclopentyl dimethoxy silaneA: Dicyclopentyl dimethoxy silane

B : Cyclohexyl methyl dimethoxy silaneB: Cyclohexyl methyl dimethoxy silane

표 1에서 알 수 있는 바와 같이, 실시예 1과 2는 비교예 1과 용융온도와 열접착온도는 동일하나 용융열량(결정화도)이 높아 열처리시 흐림도 변화 및 블록킹력이 낮다.As can be seen from Table 1, Examples 1 and 2 have the same melting temperature and thermal bonding temperature as Comparative Example 1, but the heat of melting (crystallinity) is high, the cloudiness change and the blocking force are low during heat treatment.

그리고 중합시 동일한 외부전자공여체를 사용한 경우에도, 용융온도와 용융열량이 본 발명의 범위보다 높은 비교예 2는 용융온도와 용융열량이 본 발명의 범위내인 실시예 1에 비해 열접착온도가 높다.In addition, even when the same external electron donor was used in the polymerization, Comparative Example 2, in which the melting temperature and the heat of fusion were higher than the range of the present invention, has a higher thermal bonding temperature compared to Example 1, in which the melting temperature and the heat of fusion were within the range of the present invention. .

또한 비교예 3은 실시예 1, 2와 사용된 외부전자공여체와 용융온도 및 용융열량이 같으나 에틸렌/부텐-1의 비가 1.0 이상으로 높아 열처리시 흐림도 변화 및 블록킹력이 높으며, 비교예 4는 실시예 1, 2와 사용된 외부전자공여체가 같고 에틸렌/부텐-1의 비도 낮으나 용융온도와 용융열량이 너무 낮아 블록킹력이 높다.In addition, Comparative Example 3 has the same melting temperature and the heat of fusion as the external electron donors used in Examples 1 and 2, but the ratio of ethylene / butene-1 is higher than 1.0, so that the cloudiness change and the blocking force are high during the heat treatment. The external electron donors used in Examples 1 and 2 are the same, and the ratio of ethylene / butene-1 is low, but the melting temperature and the amount of heat of melting are so low that the blocking force is high.

이상에서 볼 수 있는 바와 같이 본 발명에 의해 제조된 프로필렌-에틸렌-부텐-1 공중합체는 결정화도가 높은 폴리프로필렌 수지 조성물을 제조할 수 있는 외부전자공여체를 사용하여 기상 또는 벌크 슬러리 중합에 의하여 제조되므로써 제조비용이 저렴하며, 낮은 용융온도에서도 결정화도가 높고, 표면전이 되는 물질이 적어 열처리시 흐림도 변화가 낮고, 열접착 온도도 낮게 유지하면서 내블록킹성이 우수한 효과를 갖는다.As can be seen from the above, the propylene-ethylene-butene-1 copolymer prepared by the present invention is prepared by gas phase or bulk slurry polymerization using an external electron donor capable of producing a polypropylene resin composition having high crystallinity. Inexpensive manufacturing cost, high crystallinity even at low melting temperature, low surface transition material, low cloudiness change during heat treatment, and excellent thermal resistance while maintaining low thermal bonding temperature.

Claims (4)

고체 착물 티타늄 촉매와 유기 알루미늄 조촉매 및 외부전자공여체로서 벌키한 두 개의 알킬기와 두 개의 알콕시기를 갖는 유기 규소 화합물의 존재하에 프로필렌, 에틸렌, 부텐-1 각각의 모노머를 용매를 사용하지 않는 기상 혹은 벌크 슬러리 중합공정으로 중합하여 제조되며, 에틸렌/부텐-1의 몰비가 1.0 이하이고, 용융온도가 127∼135℃, 용융열량이 65∼83J/g인 것을 특징으로 하는 열접착성 필름용 프로필렌-에틸렌-부텐-1 공중합체 수지.In the presence of a solid complex titanium catalyst, an organoaluminum promoter and an organosilicon compound having two alkyl groups and two alkoxy groups bulked as external electron donors, each of propylene, ethylene and butene-1 monomers is a gaseous or bulk-free solvent. Produced by polymerization in a slurry polymerization process, the propylene-ethylene for heat-adhesive film, characterized in that the molar ratio of ethylene / butene-1 is 1.0 or less, the melting temperature is 127 ~ 135 ℃, the heat of fusion 65 ~ 83J / g Butene-1 copolymer resin. 제 1항에 있어서, 상기 외부전자공여체는 하기의 일반식(Ⅰ)으로 표시되는 유기규소 화합물이고The method of claim 1, wherein the external electron donor is an organosilicon compound represented by the following general formula (I) SiR1R2(OR3)2---------------- (Ⅰ)SiR 1 R 2 (OR 3 ) 2 ---------------- (Ⅰ) 여기에서 R1은 시클로펜틸기, 2-메틸시클로펜틸기, 3-메틸시클로펜틸기, 2-에틸시클로펜틸기, 3-프로필펜틸기, 3-이소프로필시클로펜틸기, 3-부틸시클로펜틸기, 3-터셔리부틸시클로펜틸기, 2,2-디메틸시클로펜틸기, 2,3-디메틸시클로펜틸기, 2,5-디메틸시클로펜틸기, 2,2,5-트리메틸시클로펜틸기, 2,3,4,5-테트라메틸시클로펜틸기, 2,2,5,5-테트라메틸시클로펜틸기, 1-시클로펜틸프로필기, 1-메틸-1-시클로펜틸에테프기, 시클로펜테닐기, 2-시클로펜테닐기, 3-시클로펜테닐기, 2-메틸-1-시클로펜테닐기, 2-메틸-3-시클로펜테닐기, 3-메틸-3-시클로펜테닐기, 2-에틸-3-시클로펜테닐기, 2,4-디메틸-3-시클로펜틸기, 2,5-디메틸-3-시클로펜테닐기, 2,3-4,5-테트라메틸-3-시클로펜테닐기, 2,2,5,5-테트라메틸-3-시클로펜테닐기, 1,3-시클로펜타디에닐기, 2,4-시클로펜타디에닐기, 1,4-시클로펜타디에닐기, 2-에틸-2,4-시클로펜타디에닐기, 2,2-디메틸-2,4-시클로펜타디에닐기, 2,3-디메틸-2,4-시클로펜타디에닐기, 2,5-디메틸-2,4-시클로펜타디에닐기 또는 2,3,4,5-테트라메틸-2,4-시클로펜타디에닐기이고,R 1 is a cyclopentyl group, 2-methylcyclopentyl group, 3-methylcyclopentyl group, 2-ethylcyclopentyl group, 3-propylpentyl group, 3-isopropylcyclopentyl group, 3-butylcyclopentyl group , 3-tertarybutylcyclopentyl group, 2,2-dimethylcyclopentyl group, 2,3-dimethylcyclopentyl group, 2,5-dimethylcyclopentyl group, 2,2,5-trimethylcyclopentyl group, 2, 3,4,5-tetramethylcyclopentyl group, 2,2,5,5-tetramethylcyclopentyl group, 1-cyclopentylpropyl group, 1-methyl-1-cyclopentylethp group, cyclopentenyl group, 2 -Cyclopentenyl group, 3-cyclopentenyl group, 2-methyl-1-cyclopentenyl group, 2-methyl-3-cyclopentenyl group, 3-methyl-3-cyclopentenyl group, 2-ethyl-3-cyclopentenyl group , 2,4-dimethyl-3-cyclopentyl group, 2,5-dimethyl-3-cyclopentenyl group, 2,3-4,5-tetramethyl-3-cyclopentenyl group, 2,2,5,5- Tetramethyl-3-cyclopentenyl group, 1,3-cyclopentadienyl group, 2,4-cyclopentadienyl group, 1,4-hour Lopentadienyl group, 2-ethyl-2,4-cyclopentadienyl group, 2,2-dimethyl-2,4-cyclopentadienyl group, 2,3-dimethyl-2,4-cyclopentadienyl group, 2, 5-dimethyl-2,4-cyclopentadienyl group or 2,3,4,5-tetramethyl-2,4-cyclopentadienyl group, R2는 알킬기, 시클로알킬기 또는 아릴기이며,R 2 is an alkyl group, a cycloalkyl group or an aryl group, R3는 알킬기, 시클로알킬기 또는 아릴기인 것을 특징으로 하는 열접착성 필름용 프로필렌-에틸렌-부텐-1 공중합체 수지.R 3 is an alkyl group, a cycloalkyl group or an aryl group, wherein the propylene-ethylene-butene-1 copolymer resin for heat-adhesive film. 제 1항에 있어서, 외부전자공여체는 고리 탄소수 5인 두 개의 벌키한 시클로알킬기와 두 개의 알콕시기를 가지는 유기규소 화합물인 것을 특징으로 하는 열접착성 필름용 프로필렌-에틸렌-부텐-1 공중합체 수지.The propylene-ethylene-butene-1 copolymer resin for heat adhesive film according to claim 1, wherein the external electron donor is an organosilicon compound having two bulky cycloalkyl groups and two alkoxy groups having 5 ring carbon atoms. 제 1항 내지 제 3항중 어느 한 항에 따른 프로필렌-에틸렌-부텐-1 공중합체 수지와 내열안정제, 블록킹 방지제, 중화제와 같은 통상의 첨가제로 이루어진 것을 특징으로 하는 열접착성 필름용 수지 조성물.A resin composition for a heat-adhesive film, comprising a propylene-ethylene-butene-1 copolymer resin according to any one of claims 1 to 3, and common additives such as a heat stabilizer, an antiblocking agent, and a neutralizing agent.
KR1019990014048A 1999-04-20 1999-04-20 Propylene-ethylene-butene-1 copolymer for heat sealing film and resin composition comprising the same KR100607538B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019990014048A KR100607538B1 (en) 1999-04-20 1999-04-20 Propylene-ethylene-butene-1 copolymer for heat sealing film and resin composition comprising the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019990014048A KR100607538B1 (en) 1999-04-20 1999-04-20 Propylene-ethylene-butene-1 copolymer for heat sealing film and resin composition comprising the same

Publications (2)

Publication Number Publication Date
KR20000066740A true KR20000066740A (en) 2000-11-15
KR100607538B1 KR100607538B1 (en) 2006-08-02

Family

ID=19581118

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019990014048A KR100607538B1 (en) 1999-04-20 1999-04-20 Propylene-ethylene-butene-1 copolymer for heat sealing film and resin composition comprising the same

Country Status (1)

Country Link
KR (1) KR100607538B1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100549106B1 (en) * 1999-04-20 2006-02-06 삼성토탈 주식회사 Polypropylene resin composition for metallizing
KR100572915B1 (en) * 1999-11-30 2006-04-24 삼성토탈 주식회사 Polypropylene resin composition for extrusion coating
KR101431910B1 (en) * 2012-12-06 2014-08-26 삼성토탈 주식회사 Polypropylene resin with high transparency and impact resistance, and process for their manufacture

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4242479A (en) * 1976-12-23 1980-12-30 Showa Yuka Kabushiki Kaisha Process for producing an improved ethylenic polymer
JPS5883006A (en) * 1981-11-13 1983-05-18 Mitsui Petrochem Ind Ltd Polymerization of olefin
KR920002488B1 (en) * 1988-06-17 1992-03-26 미쓰이 세끼유 가가꾸 고오교오 가부시끼가이샤 Process for polymerizing olefins and polymerization catalyst therefor
KR930001064B1 (en) * 1988-09-13 1993-02-15 미쓰이 세끼유 가가꾸 고오교오 가부시끼가이샤 Olefin polymerization catalyst component process for production thereof olefin polymerization catalyst and process for polymerizing olefins
KR920002488A (en) * 1990-07-03 1992-02-28 박판규 Method of manufacturing pads and nonwoven fabrics for processing bio-ceramic
US5302675A (en) * 1992-09-08 1994-04-12 Rexene Corporation High tensile strength amorphous 1-butene/propylene copolymers
JPH06234811A (en) * 1993-02-10 1994-08-23 Mitsui Petrochem Ind Ltd Production of ultra-high-molecular weight polyolefin
KR950008513A (en) * 1993-09-28 1995-04-17 유충식 3-Pyrrolidinylthio-1-azabicyclo (3,2,0) hepta-2-ene-2-carboxylic acid and preparation method thereof
TW442528B (en) * 1996-12-02 2001-06-23 Chisso Corp Polypropylene composition
KR100549106B1 (en) * 1999-04-20 2006-02-06 삼성토탈 주식회사 Polypropylene resin composition for metallizing

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100549106B1 (en) * 1999-04-20 2006-02-06 삼성토탈 주식회사 Polypropylene resin composition for metallizing
KR100572915B1 (en) * 1999-11-30 2006-04-24 삼성토탈 주식회사 Polypropylene resin composition for extrusion coating
KR101431910B1 (en) * 2012-12-06 2014-08-26 삼성토탈 주식회사 Polypropylene resin with high transparency and impact resistance, and process for their manufacture

Also Published As

Publication number Publication date
KR100607538B1 (en) 2006-08-02

Similar Documents

Publication Publication Date Title
CA1237649A (en) Laminated polypropylene film
KR101107825B1 (en) Propylene resin composition for packaging material
WO1999037711A2 (en) Polyolefins and uses thereof
JP5300482B2 (en) Low gloss elastoplastic plastic polyolefin composition
JP2004530781A (en) Polymer film containing propylene random copolymer
KR101813706B1 (en) Unstretched polypropylene film
JP5260846B2 (en) Propylene resin composition for packaging materials
WO1986002595A1 (en) Heat sealable plastics laminate
JP2009511683A6 (en) Low gloss elastoplastic plastic polyolefin composition
KR101288710B1 (en) Resin composition and meltable bag
KR101423945B1 (en) Polyolefin compositions having low hardness and low gloss
CA2424335A1 (en) Melt-moldable, thermoplastic norbornene-based resin composition, and molded article or optical film using the same
JP5422000B2 (en) Multilayer heat shrinkable film
KR100607538B1 (en) Propylene-ethylene-butene-1 copolymer for heat sealing film and resin composition comprising the same
JP4204676B2 (en) Propylene-based resin and film and laminate using the same
JP2009516758A (en) Polyolefin composition having low gloss
KR19990014180A (en) Propylene block copolymer
KR100572915B1 (en) Polypropylene resin composition for extrusion coating
JP5342115B2 (en) Propylene resin composition for packaging materials
KR100549106B1 (en) Polypropylene resin composition for metallizing
CN101589102B (en) Polyolefin compositions having low hardness and low gloss
JP3277678B2 (en) Polyester film
KR102219073B1 (en) Preparing method for the Petroleum Resin and the Hot-melt Compostion using the same method
JPH09324014A (en) Polypropylene resin
JP4574279B2 (en) Polypropylene composition and sealant film obtained therefrom

Legal Events

Date Code Title Description
N231 Notification of change of applicant
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: 20130624

Year of fee payment: 8

FPAY Annual fee payment

Payment date: 20140703

Year of fee payment: 9

FPAY Annual fee payment

Payment date: 20150626

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20160628

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20180626

Year of fee payment: 13

EXPY Expiration of term