KR840005466A - Ethylene Polymerization Method - Google Patents

Ethylene Polymerization Method Download PDF

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KR840005466A
KR840005466A KR1019830003344A KR830003344A KR840005466A KR 840005466 A KR840005466 A KR 840005466A KR 1019830003344 A KR1019830003344 A KR 1019830003344A KR 830003344 A KR830003344 A KR 830003344A KR 840005466 A KR840005466 A KR 840005466A
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compound
general formula
carbon atoms
reaction product
ethylene
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KR1019830003344A
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KR900004669B1 (en
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다께후미 야노 (외 3)
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시미즈 야스오
우베고오산 가부시끼가이샤
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    • 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
    • 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
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F10/02Ethene

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  • 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)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

내용 없음No content

Description

에틸렌의 중합방법Ethylene Polymerization Method

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음As this is a public information case, the full text was not included.

Claims (12)

(1)할로겐화 알루미늄을 다음 일반식(II)로 표시되는 규소화합물과 반응시키고, (2) 그 반응생성물을 다음 일반식(III)으로 표시되는 그리냐르(Grignard)화합물과 반응시켜 담체를 만들고, 그 다음 (3) 그 담체를 다음 일반식(IV)으로 표시되는 티탄화합물과 접촉시켜 얻은(A) 고체촉매성분과 다음 일반식(I)로 표시되는 (B)유기 알루미늄화합물과로부터 얻은 촉매의 존재하에 에틸렌 또는 에틸렌과 적어도 탄소원자수 3개의 α-올레핀과의 혼합물을 중합시키는 것을 특징으로 하는 에틸렌 중합방법.(1) the aluminum halide is reacted with a silicon compound represented by the following general formula (II), and (2) the reaction product is reacted with a Grignard compound represented by the following general formula (III) to form a carrier, (3) the catalyst obtained from (A) a solid catalyst component obtained by contacting the carrier with a titanium compound represented by the following general formula (IV) and an organic aluminum compound represented by the following general formula (I): Ethylene polymerization process characterized by polymerizing ethylene or a mixture of ethylene and at least three carbon atoms of -olefin in the presence of. 상기식에서, R1,R2,R3및 R4는 탄소원자수 1 내지 8의 알킬기, 탄소원자수 7 내지 10의 페닐기나 아르알킬기이고, R5는 탄소원자수 1 내지 6의 알킬기이고, X1및 X2는 할로겐원자이고, ℓ =1및 m은 0,1,2 또는 3이고, n은 1 또는 2이다.Wherein R 1 , R 2 , R 3 and R 4 are alkyl groups of 1 to 8 carbon atoms, phenyl or aralkyl groups of 7 to 10 carbon atoms, R 5 is an alkyl group of 1 to 6 carbon atoms, X 1 and X 2 is a halogen atom, l = 1 and m are 0,1,2 or 3 and n is 1 or 2. 제1항에 있어서, 할로겐화 알루미늄과 일반식(II)의 유기 규소화합물과의 상기 반응을 규소화합물의 몰당 0.25 내지 10몰의 할로겐화 알루미늄을 사용하여 -50 내지 100℃의 온도에서 0.1 내지 2시간동안 불활성 유기용제중에서 행하는 것을 특징으로 하는 방법.The method of claim 1, wherein the reaction of the aluminum halide with the organosilicon compound of general formula (II) is carried out at a temperature of -50 to 100 ° C. for 0.1 to 2 hours using 0.25 to 10 moles of aluminum halide per mole of silicon compound. The method characterized by the above-mentioned inert organic solvent. 제1항에 있어서, 상기 할로겐화 알루미늄이 염화알루미늄인 것을 특징으로 하는 방법.The method of claim 1 wherein the aluminum halide is aluminum chloride. 제1항에 있어서, 일반식(II)의 상기 유기 규소화합물이 메틸트리에톡시실란, 디메틸디에톡시실란, 테트라에톡시실란, 페닐트리에톡시실란, 테트라이소펜톡시실란, 또는 페닐트리펜톡시실란인 것을 특징으로 하는 방법.The compound of claim 1, wherein the organosilicon compound of formula (II) is methyltriethoxysilane, dimethyldiethoxysilane, tetraethoxysilane, phenyltriethoxysilane, tetraisopentoxysilane, or phenyltripentoxy And silane. 제1항에 있어서, 할로겐화 알루미늄과 일반식(II)의 규소화합물과의 반응생성물을 상기 반응생성물 제조에 사용된 규소화합물의 몰당 0.05 내지 4몰의 일반식(III)의 그리냐르화합물과 반응시키되, 상기 반응생성물을 불활성 유기용매에 녹인 용액과 에테르중에나 에테르와 방향족 유기용매와의 혼합용매중에 그리냐르화합물을 녹인 용액을 상호 점차적으로 혼합시키는 방식으로 하며, 상기 에테르는 다음 일반식(V)로 표시되는 것을 특징으로 하는 방법.The reaction product of claim 1, wherein the reaction product of the aluminum halide with the silicon compound of general formula (II) is reacted with 0.05 to 4 moles of Grignard compound of the general formula (III) per mole of silicon compound used to prepare the reaction product. The reaction product is dissolved in an inert organic solvent and a solution of a Grignard compound dissolved in an ether or a mixed solvent of an ether and an aromatic organic solvent is gradually mixed with each other, and the ether is represented by the following general formula (V). Method represented by. R6-O-R7(V)R 6 -OR 7 (V) 상기식에서 R6과 R7은 독립적으로 탄소원자수 2 내지 8의 알킬기를 표시한다.Wherein R 6 and R 7 independently represent an alkyl group having 2 to 8 carbon atoms. 제1항에 있어서, 상기 일반식(III)의 그리냐르 화합물은 염화알킬마그네슘인 것을 특징으로 하는 방법.The method according to claim 1, wherein the Grignard compound of the general formula (III) is magnesium alkyl chloride. 제1항에 있어서, 할로겐화 알루미늄과 일반식(II)의 규소화합물과의 반응생성물과 일반식(III)의 그리냐르 화합물과의 반응에 의해 생성된 담체를, 일반식(IV)의 티탄화합물과의 접촉처리전에, 불활성 유기 용매로 세척하는 것을 특징으로 하는 방법.The carrier produced by the reaction product of the aluminum halide with the silicon compound of general formula (II) and the Grignard compound of the general formula (III) is a titanium compound of general formula (IV). Before contact treatment, characterized in that the washing with an inert organic solvent. 제1항에 있어서, 상기 담체를, 상기 담체의 제조에 사용된 그리냐르 화합물의 몰당 적어도 1몰의 티탄화합물과 접촉시키는 것을 특징으로 하는 방법.The method of claim 1, wherein the carrier is contacted with at least one mole of titanium compound per mole of Grignard compound used to prepare the carrier. 제1항에 있어서, 상기 유기 알루미늄화합물(B)의 양이 고체촉매성분(A)에 함유된 티탄의 그램원자당 1 내지 1,000몰의 범위에 드는 것을 특징으로 하는 방법.The method according to claim 1, wherein the amount of the organoaluminum compound (B) is in the range of 1 to 1,000 moles per gram atom of titanium contained in the solid catalyst component (A). 제1항에 있어서, 상기 유기 알루미늄화합물(B)이 수소화 디이소부틸 알루미늄인 것을 특징으로 하는 방법.The method according to claim 1, wherein the organoaluminum compound (B) is diisobutyl aluminum hydride. 제1항에 있어서, 에틸렌 또는 에틸렌과 적어도 탄소원자수 3의 α-올레핀과의 혼합물을 1 내지 3000kg/㎠의 압력하에서 30 내지 300℃의 온도에서 사실상 무수(water-free) 및 무산소(oxygen-free) 상태에서 중합시키는 것을 특징으로 하는 방법.The process of claim 1 wherein the mixture of ethylene or ethylene and at least 3 carbon atoms of -olefins at a temperature of 30 to 300 ° C. under a pressure of 1 to 3000 kg / cm 2 is substantially water-free and oxygen-free. And polymerizing in a) state. 제1항에 있어서, 액체 탄화수소 중합매질을 사용하여 액상에서 또한 고체촉매성분(A)의 양이 중합매질 리터당 티탄으로서 0.0005 내지 10mg원자의 범위이고 유기 알루미늄화합물(B)의 양이 중합매질의 리터당 0.001 내지 1,000밀리몰의 범위에 드는 양의 촉매를 사용하여 중합을 행하는 것을 특징으로 하는 방법.The method according to claim 1, wherein the amount of solid catalyst component (A) in the liquid phase using a liquid hydrocarbon polymerization medium is in the range of 0.0005 to 10 mg atoms as titanium per liter of the polymerization medium and the amount of the organoaluminum compound (B) per liter of the polymerization medium. The polymerization is carried out using a catalyst in an amount in the range of 0.001 to 1,000 mmol. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019830003344A 1982-07-28 1983-07-20 Preparation for ethylene KR900004669B1 (en)

Applications Claiming Priority (2)

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JP57130513A JPS5922909A (en) 1982-07-28 1982-07-28 Polymerization of ethylene
JP130513 1982-07-28

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KR840005466A true KR840005466A (en) 1984-11-12
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CA (1) CA1233948A (en)
FR (1) FR2531090B1 (en)
GB (1) GB2125053B (en)

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KR101236596B1 (en) * 2010-12-24 2013-02-22 삼성토탈 주식회사 Method of preparation of solid catalyst and method of gas-phase polymerization of ethylene using solid catalyst prepared by the same

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CA1104298A (en) * 1978-02-23 1981-06-30 Akinobu Shiga Catalysts for the polymerization of olefins
JPS5817204B2 (en) * 1979-09-21 1983-04-05 宇部興産株式会社 α-olefin polymerization method
JPS5817206B2 (en) * 1979-10-11 1983-04-05 宇部興産株式会社 Ethylene polymerization method
JPS5825363B2 (en) * 1980-05-22 1983-05-27 宇部興産株式会社 Production method of α-olefin polymer

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FR2531090B1 (en) 1987-02-20
CA1233948A (en) 1988-03-08
KR900004669B1 (en) 1990-07-02
FR2531090A1 (en) 1984-02-03
GB8319780D0 (en) 1983-08-24
JPS5922909A (en) 1984-02-06
GB2125053A (en) 1984-02-29
GB2125053B (en) 1986-01-02
JPH0153889B2 (en) 1989-11-16

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