KR940005683A - 폴리올레핀 왁스의 제조방법 - Google Patents
폴리올레핀 왁스의 제조방법 Download PDFInfo
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- C08F4/60—Metals; 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
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- Y10S585/00—Chemistry of hydrocarbon compounds
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- Y10S585/946—Product is waxy polymer
Abstract
메탈로센 촉매의 존재하에 저비점 현탁화제, 특히 프로판중에서 올레핀을 중합시키면 임의의 추가 후처리 단계없이 사용할 수 있는 폴리올레핀 왁스가 수득된다.
Description
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Claims (11)
- 올레핀 또는 디올레핀을 일반식(I)의 메탈로센 화합물과 공촉매를 포함하는 촉매와 현탁화제로서 작용하는 탄소수 3 또는 4의 저비점 탄화수소 또는 저비점 할로겐화 탄화수소의 존재하에 0.5 내지 120bar의 압력하에 -40 내지 100℃의 온도에서 현탁 중합 또는 현탁공중합시켜 폴리올레핀 왁스를 제조하는 방법.상기식에서, M1은 주기율표의 Ⅳb족, Ⅴb족 또는 Ⅵb족 금속이고, R1및 R2는 동일하거나, 상이하며, 수소원자, C1-C10-알킬 그룹, C1-C10-알콕시 그룹, C6-C10-아릴 그룹, C6-C10-아릴 옥시 그룹, C2-C10-알케닐 그룹, C7-C40-아릴알킬 그룹, C7-C40-알킬아릴 그룹, C8-C40-아릴알케닐 그룹 또는 할로겐 원자이고, R3및 R4는 동일하거나 상이하며, 중심원자 M1과 샌드위치 구조를 형성할 수 있는 단핵 또는 다핵 탄화수소 라디칼이거나, 라디칼 R3및 R4중의 하나는 치환된 질소원자이다.
- 제1항에 있어서, 메탈로센이 일반식(Ia)의 화합물인 방법.상기식에서, R1및 R2는 제1항에서 정의한 바와 같고, R5,R6,R7,R8,R9및 R10은 동일하거나 상이하며, 수소 원자, 할로겐 원자, C1-C10-알킬 그룹, C6-C10-아릴 그룹, C1-C10-알콕시 그룹 또는 -NR16 2, -SR16, -OSiR16 3, -SiR16 3또는 -PR16 2라디칼(여기서, R16는 C1-C10-알킬 그룹 또는 C6-C10-아릴 그룹 또는 C6-C10-아릴 그룹이거나, Si- 또는 P- 함유 라디칼의 경우에는 할로겐 원자이다)이거나, 임의의 2개의 인접한 라디칼 R5,R6,R7,R8,R9및 R10은 이들을 연결하는 탄소원자와 함께 환을 형성한다.
- 제1항에 있어서, 메틸로센이 일반식(Ⅰb)이 화합물인 방법.상기식에서, R1및 R2는 제1항에서 정의한 바와 같고, R5,R6,R7,R8,R9및 R16은 제2항에서 정의한 바와 같으며, R13은=BR17, AlR17, -Ge-, -Sn-, -O-, -S-, =SO, =SO2, =NR17, =CO, =PR17또는 =P(O)R17(여기서, R17, R18및 R19는 동일하거나 상이하며, 수소원자, 할로겐원자, C1-C30-알킬 그룹, C1-C10-플루오로알킬 그룹, C6-C10-플루오로아릴 그룹, C6-C10-아릴 그룹, C1-C10-알콕시 그룹, C2-C10-알케닐 그룹, C7-C40-아릴알킬 그룹, C8-C40-아릴알케닐 그룹 또는 C7-C40-알킬아릴 그룹이거나, R17과 R18또는 R17과 R19는 각각의 경우에 이들을 연결하는 원자와 함께 환을 형성하며, M2는 규소, 게르마늄 또는 주석이다)이고, R11과 R12는 동일하거나 상이하며, R17에 대해 정의한 바와 같고, m 및 n은 동일하거나, 상이하며, 0,1 또는 2이고, m과 n의 합은 0,1 또는 2, 바람직하게는 0 또는 1이다.
- 제1항에 있어서, 메탈로센이 일반식(Ic)의 화합물인 방법.상기식에서, R1및 R2는 제1항에서 정의한 바와 같고, R5및 R6은 제2항에서 정의한 바와 같으며, M2는 제3항에서 정의한 바와 같고, R14및 R15및 R17및 R18에 정의한 바와 같으며, R24는 R17에 대해 정의한 바와 같다.
- 제1항에 있어서, 공촉매가 선형의 경우에는 일반식(Ⅱa)의 알루민옥사이고/이거나 환형의 경우에는 일반식(Ⅱb)의 화합물인 방법.상기식에서, R20라디칼은 동일하거나 상이한 C1-C6-알킬 그룹이고, p는 4 내지 30의 정수이다.
- 제1항에 있어서, 현탁화제가 프로판 또는 부탄인 방법.
- 제6항에 있어서, 현탁화제가 프로판인 방법.
- 제1항에 있어서, 지지체 물질 위에 존재하는 촉매가 사용되는 방법.
- 제1항에 있어서, 에틸렌, 프로필렌, 1-부텐, 4-메틸-1-펜텐 또는 헥센이 중합되는 방법.
- 제1항에서 청구한 방법에 의해 제조된, 총 중합체에 대해 에틸렌 단위 100 내지 80중량%의 총 중합체에 대해 프로필렌, 1-부텐, 4-메틸-1-펜텐 또는 1-헥센으로부터 유도된 단위 0 내지 20중량%를 포함하고 분자량(Mw)이 약 500 내지 약 50,000이며 분자량 (Mw/Mn)가 약 1 내지 10이고 점도수가 2 내지 100㎤/g인 폴리에틸렌 왁스.
- 제1항에서 청구한 방법에 의해 제조된, 총 중합체에 대해 프로필렌 단위 80 내지 100중량%의 총 중합체에 대해 에틸렌 또는 다른 올레핀으로부터 유도된 단위 0 내지 20중량%를 포함하고 분자량(Mw)이 약 1,000 내지 약 50,000g/mol이며 다분산도 (Mw/Mn)가 약 1.5 내지 5.0이고 점도수가 2 내지 100㎤/g이며 융점이 50 내지 150℃이고 직점이 60 내지 150℃이며 170℃에서의 용융점도가 100 내지 80,000Pas이고 공단량체 단위가 중합체 쇄에 랜덤하게 분포되어 있는 폴리프로필렌 왁스.※참고사항:최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE4217378 | 1992-05-26 | ||
DEP4217378.7 | 1992-05-26 |
Publications (2)
Publication Number | Publication Date |
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KR940005683A true KR940005683A (ko) | 1994-03-22 |
KR100284211B1 KR100284211B1 (ko) | 2001-03-02 |
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Application Number | Title | Priority Date | Filing Date |
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KR1019930009025A KR100284211B1 (ko) | 1992-05-26 | 1993-05-25 | 폴리올레핀 왁스 및 이의 제조방법 |
Country Status (14)
Country | Link |
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US (1) | US5723705A (ko) |
EP (1) | EP0571882B1 (ko) |
JP (1) | JP3429334B2 (ko) |
KR (1) | KR100284211B1 (ko) |
AT (1) | ATE150037T1 (ko) |
AU (1) | AU663585B2 (ko) |
BR (1) | BR9302041A (ko) |
CZ (1) | CZ282810B6 (ko) |
DE (1) | DE59305691D1 (ko) |
ES (1) | ES2100388T3 (ko) |
HK (1) | HK1006720A1 (ko) |
SK (1) | SK280438B6 (ko) |
TW (1) | TW294674B (ko) |
ZA (1) | ZA933630B (ko) |
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NL9201970A (nl) * | 1992-11-11 | 1994-06-01 | Dsm Nv | Indenylverbindingen en katalysatorcomponenten voor de polymerisatie van olefinen. |
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DE1929863A1 (de) * | 1969-06-12 | 1970-12-17 | Hoechst Ag | Verfahren zur Polymerisation von Olefinen |
DE2329641C3 (de) * | 1973-06-09 | 1978-09-28 | Hoechst Ag, 6000 Frankfurt | Verfahren zur Polymerisation von ct-Olefinen |
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DE4004477A1 (de) * | 1990-02-14 | 1991-08-22 | Schering Ag | Verfahren zur herstellung von loesungen oligomerer methylaluminoxane |
-
1993
- 1993-05-18 DE DE59305691T patent/DE59305691D1/de not_active Expired - Fee Related
- 1993-05-18 EP EP93108106A patent/EP0571882B1/de not_active Expired - Lifetime
- 1993-05-18 AT AT93108106T patent/ATE150037T1/de not_active IP Right Cessation
- 1993-05-18 ES ES93108106T patent/ES2100388T3/es not_active Expired - Lifetime
- 1993-05-20 SK SK514-93A patent/SK280438B6/sk unknown
- 1993-05-24 CZ CZ93983A patent/CZ282810B6/cs not_active IP Right Cessation
- 1993-05-24 BR BR9302041A patent/BR9302041A/pt not_active IP Right Cessation
- 1993-05-25 AU AU38765/93A patent/AU663585B2/en not_active Ceased
- 1993-05-25 JP JP12247993A patent/JP3429334B2/ja not_active Expired - Fee Related
- 1993-05-25 ZA ZA933630A patent/ZA933630B/xx unknown
- 1993-05-25 KR KR1019930009025A patent/KR100284211B1/ko not_active IP Right Cessation
- 1993-06-18 TW TW082104894A patent/TW294674B/zh active
-
1995
- 1995-06-07 US US08/478,359 patent/US5723705A/en not_active Expired - Fee Related
-
1998
- 1998-06-23 HK HK98106073A patent/HK1006720A1/xx not_active IP Right Cessation
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US5723705A (en) | 1998-03-03 |
SK280438B6 (sk) | 2000-02-14 |
CZ98393A3 (en) | 1993-12-15 |
AU3876593A (en) | 1993-12-02 |
AU663585B2 (en) | 1995-10-12 |
EP0571882A3 (en) | 1994-07-06 |
DE59305691D1 (de) | 1997-04-17 |
KR100284211B1 (ko) | 2001-03-02 |
EP0571882B1 (de) | 1997-03-12 |
BR9302041A (pt) | 1993-11-30 |
JP3429334B2 (ja) | 2003-07-22 |
EP0571882A2 (de) | 1993-12-01 |
TW294674B (ko) | 1997-01-01 |
ZA933630B (en) | 1993-12-20 |
HK1006720A1 (en) | 1999-03-12 |
JPH0649129A (ja) | 1994-02-22 |
ATE150037T1 (de) | 1997-03-15 |
CZ282810B6 (cs) | 1997-10-15 |
ES2100388T3 (es) | 1997-06-16 |
SK51493A3 (en) | 1994-02-02 |
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