KR920021585A - Method for preparing catalyst composition for ethylene polymerization and method for preparing ethylene homopolymer or copolymer using same - Google Patents

Method for preparing catalyst composition for ethylene polymerization and method for preparing ethylene homopolymer or copolymer using same Download PDF

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KR920021585A
KR920021585A KR1019910008944A KR910008944A KR920021585A KR 920021585 A KR920021585 A KR 920021585A KR 1019910008944 A KR1019910008944 A KR 1019910008944A KR 910008944 A KR910008944 A KR 910008944A KR 920021585 A KR920021585 A KR 920021585A
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aliphatic
compound
formula
carbon atoms
aromatic hydrocarbon
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KR1019910008944A
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KR940000410B1 (en
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지용채
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박원배
한양화학 주식회사
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Priority to JP4140301A priority patent/JP2518581B2/en
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Priority to US08/215,414 priority patent/US5597770A/en

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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

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

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Description

에틸렌 중합용 촉매 조성물의 제조방법 및 이를 이용한 에틸렌 호모 중합체 또는 공중합체의 제조방법Method for preparing catalyst composition for ethylene polymerization and method for preparing ethylene homopolymer or copolymer using same

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

Claims (9)

하기 일반식(II)의 전구체 조성물을 불활성 담체물질로 희석시킨 다음, 하기 일반식(III)의 적어도 하나 이상의 알킬 알루미늄 화합물로 부분 활성화시킨 다음 하기 일반식(IV)의 할로겐화 붕소화합물로 처리하는 것을 특징으로 하는 하기 일반식(I)로 표시될 수 있는 에틸렌 중합용 촉매 조성물의 제조방법.Diluting the precursor composition of formula (II) with an inert carrier material, then partially activating with at least one alkyl aluminum compound of formula (III) and then treating with a halogenated boron compound of formula (IV) A method for producing a catalyst composition for ethylene polymerization, which can be represented by the following general formula (I). MgaTi(OR)bXcAld(R")eX'fHg[ED]hBiRv jX"3i-j(I)Mg a Ti (OR) b X c Al d (R ") e X ' f H g [ED] h B i R v j X" 3i-j (I) MgaTi(OR)bAl0.33Xc[ED]h(II)Mg a Ti (OR) b Al 0.33 X c [ED] h (II) Ald(R")eX'fHg (III)Al d (R ") e X ' f Hg (III) BiRv jX"3-j(IV)B i R v j X " 3-j (IV) 상기식에서, R은 탄소수 l 내지 14개를 갖는 지방족 혹은 방향족 탄화수소 라디칼 또는 COR' (여기서 R'는 탄소원자 l 내지 14개를 갖는 지방족 또는 방향족 탄화수소 라디칼임)이고, R"는 탄소원자 1 내지 14개를 갖는 지방족 또는 방향족 탄화수소 라디칼 또는 OR"'(여기서 R"'는 탄소원자 1 내지 14개를 갖는 지방족 또는 방향족 탄화수소 라디칼임)이고, X는 C1, Br, I 및 이의 혼합물로 이루어진 군에서 선택된 것이고, ED는 지방족산과 방향족산의 알킬에스테르, 지방족 에테르, 환상에테르 및 지방족 케톤으로 이루어진 군에서 선택된 유기 전자공여체 화합물이고, a는 0.5 내지 56의 수이고, b는 0,1 또는 2이고, c는 2 내지 116의 수이고, d는 d'+0.33(단 d'는 l 내지 33의 수)이고, 는 0 내지 1.5의수이고, g는 0 또는 이고, e는 상기 e+f+g이 3이 되도록 하는 수이고, h는 2 내지 85의 수이고, X'는 Cl 또는 OR"이고, 상기 R" 및 R는 같거나 다른 탄소원자 1 내지 14개를 갖는 지방족 또는 방향족 탄화수소 라디칼이고, X"는 C1, Br 및 이들의 혼합물로 이루어진 군에서 선택된 것이고, i는 0.1 내지 1의 수이며, j는 상기 Rv가 지방족 또는 방향족 탄화수소라디칼인 경우에는 0 또는 1i이고, Rv가 OR일 경우에는 0, 1i 또는 2i이며, H는 수소이다.Wherein R is an aliphatic or aromatic hydrocarbon radical having 1 to 14 carbon atoms or COR 'wherein R' is an aliphatic or aromatic hydrocarbon radical having 1 to 14 carbon atoms, and R "is 1 to 14 carbon atoms Is an aliphatic or aromatic hydrocarbon radical having a dog or OR "'wherein R"' is an aliphatic or aromatic hydrocarbon radical having 1 to 14 carbon atoms and X is selected from the group consisting of C1, Br, I and mixtures thereof ED is an organic electron donor compound selected from the group consisting of alkyl esters of aliphatic and aromatic acids, aliphatic ethers, cyclic ethers and aliphatic ketones, a is a number from 0.5 to 56, b is 0,1 or 2, c Is a number from 2 to 116, d is d '+ 0.33 (where d' is a number from l to 33), is a number from 0 to 1.5, g is 0 or and e is e + f + g is 3 Is a number such that h is from 2 to 85 And X ′ is Cl or OR ″, wherein R ″ and R are aliphatic or aromatic hydrocarbon radicals having 1 to 14 carbon atoms, the same or different, and X ″ in the group consisting of C1, Br and mixtures thereof I is selected, i is a number from 0.1 to 1, j is 0 or 1i when R v is an aliphatic or aromatic hydrocarbon radical, 0, 1 i or 2 i when R v is OR, and H is hydrogen. 제1항에 있어서, 하기식(V)를 갖는 적어도 하나의 마그네슘 화합물과 하기 일반식(VI)를 갖는 적어도 하나의 티탄화합물을 적어도 하나의 액상 유기전자공여체 화합물중에 용해시켜 이 전자공여체 화합물 중에 상기 일반식(II)을 갖는 전구물질 조성물의 용액을 형성시키고, 이 전구물질 조성물을 불활성 담체에 희석시킨 다음, 상기 일반식(III)의 적어도 하나이상의 알킬알루미늄 화합물로 부분활성화시킨 다음, 상기 일반식(IV)의 할로겐화 붕소 화합물로 처리하는 것을 특징으로 하는 하기 일반식(I)로 표시될 수 있는 에틸렌 중합용 촉매 조성물의 제조방법.The method according to claim 1, wherein at least one magnesium compound having formula (V) and at least one titanium compound having formula (VI) are dissolved in at least one liquid organic electron donor compound to A solution of the precursor composition having formula (II) is formed, the precursor composition is diluted with an inert carrier, and then partially activated with at least one alkylaluminum compound of formula (III), and then A process for producing a catalyst composition for ethylene polymerization which can be represented by the following general formula (I), which is treated with a boron halide compound of (IV). MgX2(V)MgX 2 (V) Tiw(OR)xAlyXz(VI)Ti w (OR) x Al y X z (VI) 상기 일반식에서, R은 탄소원자 1 내지 14개를 갖는 지방족 또는 방향족 탄화수소 라디칼 또는 COR'(여기서 R'는 탄소원자 1 내지 14개를 갖는 지방족 또는 방향족 탄화수소 라디칼임)이고, w는 1이고, x는 0,1 또는 2이고, y는 1/3이며, z는 2 내지 116이고, X는 Cl, Br, 1 및 이의 혼합물로 이루어진 군에서 선택된 것이다.Wherein R is an aliphatic or aromatic hydrocarbon radical having 1 to 14 carbon atoms or COR 'wherein R' is an aliphatic or aromatic hydrocarbon radical having 1 to 14 carbon atoms, w is 1, x Is 0,1 or 2, y is 1/3, z is 2 to 116 and X is selected from the group consisting of Cl, Br, 1 and mixtures thereof. 제1항 또는 제2항에 있어서, 상기 전구체 조성물이 TiC13·1/3AlC13, 무수 MgCl2및 테트라하이드로퓨란으로부터 제조되는 것을 특징으로 하는 촉매조성물의 제조방법.The method of claim 1 or 2, wherein the precursor composition is prepared from TiC1 3 · 1/3 AlC1 3 , anhydrous MgCl 2 and tetrahydrofuran. 제1항에 있어서, 상기 불활성 담체물질로 희석된 상기 일반식(II)의 전구체 조성물을 상기 일반식(III)으로 부분활성화시킬때 상기 알킬 알미늄 화합물과 티탄화합물의 몰비가 4:1 이하인 것을 특징으로 하는 촉매조성물의 제조방법.The method of claim 1, wherein the molar ratio of the alkyl aluminum compound and the titanium compound is 4: 1 or less when the precursor composition of the general formula (II) diluted with the inert carrier material is partially activated with the general formula (III). Method of producing a catalyst composition. 제4항에 있어서, 상기 몰비가 2:1 이하에서 0.1:1인 것을 특징으로 하는 촉매조성물의 제조방법.The method of claim 4, wherein the molar ratio is less than 2: 1 0.1: 1. 제1항 또는 제2항에 있어서, 상기 불활성 담체물질로 희석된 상기 일반식(II)의 전구체 조성물을 상기 일반식(III)으로 부분활성화시킬때 전자공여체 화합물과 상기 알루미늄 화합물의 몰비가 1:0.325 이상인 것을 특징으로 하는 촉매조성물의 제조방법.The molar ratio of the electron donor compound to the aluminum compound according to claim 1 or 2, when the precursor composition of formula (II) diluted with the inert carrier material is partially activated with the formula (III). Method for producing a catalyst composition, characterized in that 0.325 or more. 제1항에 있어서, 상기 일반식(III)으로 부분활성화된 촉매전구물질을 다시 상기 일반식(IV)의 할로겐화 화합물로 처리시 상기 할로겐화 붕소화합물과 상기 촉매 전구물질중의 전자공여체 화합물의 몰비가 0.1:1 내지 0.7:1인 것을 특징으로 하는 촉매 조성물의 제조방법.The molar ratio of the boron halide compound and the electron donor compound in the catalyst precursor when the catalyst precursor material partially activated by the general formula (III) is again treated with the halogenated compound of the general formula (IV). Method for producing a catalyst composition, characterized in that 0.1: 1 to 0.7: 1. 에틸렌과 에틸렌 또는 탄소원자 3 내지 8개를 갖는 적어도 하나의 알파올레핀과의 혼합물을 제1항 내지 제7항의 어느 한 항에 의해 제조된 촉매조성물과 2,000psig 이하의 압력, 약 80 내지 약 90℃ 및 적절한 수소 존재하에 슬러리 상으로 반응시키는 것을 특징으로 하는 에틸렌 호모 중합체 또는 공중합체의 제조방법.A mixture of ethylene and at least one alphaolefin having 3 to 8 carbon atoms is combined with the catalyst composition prepared by any one of claims 1 to 7 with a pressure of up to 2,000 psig, about 80 to about 90 ° C. And reacting in slurry phase in the presence of suitable hydrogen. 제8항에 있어서, 에틸렌 호모 중합체 또는 공중합체의 용융물 유량비가 32 내지 40이고 밀도가 0.91 내지 0.97g/cm2인 것을 특징으로 하는 에틸렌 호모 중합체 또는 공중합체의 제조 방법.The method of claim 8, wherein the melt flow rate ratio of the ethylene homo polymer or copolymer is 32 to 40 and the density is 0.91 to 0.97 g / cm 2 . ※ 참고사항:최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019910008944A 1991-05-30 1991-05-30 Process for the preparation of catalyst composition for ethylene polymerization and process for the preparation of ethylene homo and copolymer using same KR940000410B1 (en)

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Application Number Priority Date Filing Date Title
KR1019910008944A KR940000410B1 (en) 1991-05-30 1991-05-30 Process for the preparation of catalyst composition for ethylene polymerization and process for the preparation of ethylene homo and copolymer using same
JP4140301A JP2518581B2 (en) 1991-05-30 1992-06-01 Process for producing catalyst composition for ethylene polymerization and process for producing ethylene homopolymer and copolymer using the same
US08/215,414 US5597770A (en) 1991-05-30 1994-03-21 Titanium-based catalyst composition for polymerizing ethylene

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KR1019910008944A KR940000410B1 (en) 1991-05-30 1991-05-30 Process for the preparation of catalyst composition for ethylene polymerization and process for the preparation of ethylene homo and copolymer using same

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KR920021585A true KR920021585A (en) 1992-12-18
KR940000410B1 KR940000410B1 (en) 1994-01-20

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JPH06172416A (en) 1994-06-21
KR940000410B1 (en) 1994-01-20

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