KR20180137182A - 헤테로원자 리간드, 이를 포함하는 올리고머화 촉매 및 올리고머 제조방법 - Google Patents
헤테로원자 리간드, 이를 포함하는 올리고머화 촉매 및 올리고머 제조방법 Download PDFInfo
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Abstract
Description
| 촉매 | 활성 (kg/gCr/h) |
반응온도 (oC) |
C6 (중량%) |
C6 중 1-헥센 (중량%) |
C8 (중량%) | C8 중 1-옥텐 (중량%) |
C10-C14 (중량%) |
폴리머 (중량%) | 옥텐/헥센 (g비) |
| 실시예1 | 1150 | 45 | 21.1 | 39.1 | 63.9 | 96.9 | 10.9 | 4.1 | 3.0 |
| 비교예1 | 125 | 45 | 20.2 | 45.9 | 69.8 | 97.2 | 8.8 | 1.2 | 3.5 |
| 실시예2 | 870 | 45 | 21.7 | 34.3 | 63.3 | 95.7 | 10.2 | 4.8 | 2.9 |
| 비교예2 | 166 | 45 | 19.2 | 51.3 | 69.3 | 96.1 | 9.9 | 1.6 | 3.6 |
| 실시예3 | 981 | 45 | 22.0 | 36.4 | 64.3 | 95.2 | 9.8 | 4.0 | 2.9 |
| 비교예3 | 214 | 45 | 11.5 | 30.5 | 71.5 | 95.8 | 15.8 | 1.2 | 6.2 |
| 실시예4 | 1049 | 45 | 23.4 | 41.9 | 62.7 | 95.4 | 10.3 | 3.6 | 2.7 |
| 비교예4 | 446 | 45 | 13.1 | 34.2 | 70.8 | 96.5 | 15.9 | 0.2 | 5.4 |
| 실시예5 | 997 | 60 | 24.8 | 47.4 | 64.1 | 95.7 | 9.0 | 2.0 | 2.6 |
| 비교예5 | 575 | 60 | 23.0 | 51.7 | 68.6 | 97.0 | 7.6 | 0.8 | 3.0 |
| 실시예6 | 873 | 80 | 26.4 | 53.7 | 63.5 | 96.6 | 8.1 | 2.0 | 2.4 |
| 비교예6 | 388 | 80 | 18.1 | 67.7 | 65.8 | 97.6 | 16.1 | 0.1 | 3.6 |
| 실시예7 | 640 | 100 | 30.7 | 63.7 | 59.9 | 96.9 | 7.7 | 1.7 | 2.0 |
| 비교예7 | 239 | 100 | 29.0 | 67.6 | 61.8 | 97.2 | 7.7 | 1.6 | 2.1 |
Claims (15)
- 제 1항에 있어서,
상기 실세스퀴옥산 유도체는 하기 화학식 2로 표시되는 헤테로원자 리간드.
[화학식 2]
-(SiO3/2)q(R7)q -1
R7은 수소, 하이드록시, 할로겐, 하이드로카빌, 치환된 하이드로카빌, 헤테로하이드로카빌 또는 치환된 하이드로카빌이며,
q는 2, 4, 6, 8, 10, 12, 14, 16 또는 18 이다. - 제 2항에 있어서,
상기 R7은 C1-C10알킬인 헤테로원자 리간드. - 제 2항에 있어서,
상기 화학식 2에서 q는 8 인 헤테로원자 리간드. - 제 1항에 있어서,
상기 D는 치환되거나 비치환된 하이드로카빌렌 또는 치환되거나 비치환된헤테로하이드로카빌렌을 포함하는 유기 연결 그룹; 및 단일 원자 링크를 포함하는 무기 연결 그룹에서 선택되는 어느 하나인 헤테로원자 리간드. - 제 1항에 있어서,
상기 헤테로원자 리간드는 하기 화학식 3 내지 5에서 선택되는 것인 헤테로원자 리간드.
[화학식 3]
[화학식 4]
[화학식 5]
상기 화학식 3 내지 5에서,
Z는 실세스키옥산 유도체이며,
R11 내지 R14는 서로 독립적으로 하이드로카빌, 치환된 하이드로카빌, 헤테로하이드로카빌 또는 치환된 하이드로카빌이며;
R 및 R21는 서로 독립적으로 치환 또는 비치환된 C6-C20아릴렌, 치환 또는 비치환된 C6-C20아릴렌C1-C10알킬렌, 치환 또는 비치환된 C6-C20아릴렌C2-C10알케닐렌, 치환 또는 비치환된 C6-C20아릴렌C2-C10알키닐렌, 치환 또는 비치환된 C1-C10알킬렌, 치환 또는 비치환된 C2-C10알케닐렌, 치환 또는 비치환된 C2-C10알키닐렌 또는 치환 또는 비치환된 C3-C20헤테로아릴렌이며,
R22는 치환 또는 비치환된 C6-C20아릴렌, 치환 또는 비치환된 C6-C20아릴렌C1-C10알킬렌, 치환 또는 비치환된 C6-C20아릴렌C2-C10알케닐렌, 치환 또는 비치환된 C6-C20아릴렌C2-C10알키닐렌, 치환 또는 비치환된 C1-C10알킬렌, C2-C10알케닐렌, 치환 또는 비치환된 C2-C10알키닐렌, 치환 또는 비치환된 C3-C20헤테로아릴렌 또는 이다. - 제 7항에 있어서,
상기 실세스퀴옥산 유도체는 *-(SiO3/2)q(R7)q -1이며, 여기서, R7은 하이드로카빌, 치환된 하이드로카빌, 헤테로하이드로카빌 또는 치환된 하이드로카빌이며,
q는 서로 독립적으로 2, 4, 6, 8, 10, 12, 14, 16 또는 18인 헤테로원자 리간드. - 제 7항에 있어서,
상기 R11 내지 R14는 할로겐, C1-C10알킬, 할로C1-C10알킬, C2-C10알케닐, C2-C10알키닐, C1-C10알콕시 및 할로C1-C10알콕시에서 선택되는 어느 하나 이상으로 치환된 C6-C20아릴인 헤테로원자 리간드. - 제 1항 내지 제 9항에서 선택되는 어느 한 항의 헤테로원자 리간드 및 전이금속을 포함하는 올리고머화 촉매.
- 제 10항의 올리고머화 촉매를 반응기에 투입하는 단계;
올레핀을 상기 반응기에 투입하는 단계; 및
상기 올레핀을 상기 올리고머화 촉매와 반응시켜 올리고머화하는 단계를 포함하는 올리고머 제조방법. - 제 11항에 있어서,
상기 올레핀은 에틸렌이며, 상기 올리고머는 1-헥센 또는 1-옥텐인 올리고머 제조방법. - 제 11항 또는 제 12항 중 어느 한 항에 있어서,
상기 전이금속의 100 내지 5,000 몰배의 금속을 포함하는 조촉매를 상기 반응기에 투입하는 단계를 더 포함하는 올리고머 제조방법. - 제 13항에 있어서,
상기 조촉매는 유기 알루미늄 화합물, 유기 알루미녹산, 유기 붕소 화합물, 유기염 또는 이들의 혼합물인 올리고머 제조방법. - 제 14항에 있어서,
상기 조촉매는 메틸알루미녹산(MAO), 변형 메틸알루미녹산 (MMAO), 에틸알루미녹산(EAO), 테트라이소부틸알루미녹산(TIBAO), 이소부틸알루미녹산(IBAO), 트리메틸알루미늄(TMA), 트리에틸알루미늄(TEA), 트리이소부틸알루미늄(TIBA), 트리-n-옥틸알루미늄, 메틸알루미늄디클로라이드, 에틸알루미늄 디클로라이드, 디메틸알루미늄 클로라이드, 디에틸알루미늄 클로라이드, 알루미늄이소프로폭사이드, 에틸알루미늄 세스퀴클로라이드 및 메틸알루미늄 세스퀴클로라이드로 이루어진 군으로부터 선택되는 하나 또는 둘 이상의 혼합물인 올리고머 제조방법.
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| Application Number | Priority Date | Filing Date | Title |
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| KR1020170076510A KR102450815B1 (ko) | 2017-06-16 | 2017-06-16 | 헤테로원자 리간드, 이를 포함하는 올리고머화 촉매 및 올리고머 제조방법 |
| PCT/KR2018/005523 WO2018230846A1 (ko) | 2017-06-16 | 2018-05-15 | 헤테로원자 리간드, 이를 포함하는 올리고머화 촉매 및 올리고머 제조방법 |
| EP18818564.9A EP3640256B1 (en) | 2017-06-16 | 2018-05-15 | Heteroatom ligand, oligomerization catalyst containing same, and method for preparing oligomer |
| CN201880040080.XA CN110753695B (zh) | 2017-06-16 | 2018-05-15 | 杂原子配体、包含其的低聚催化剂及低聚物的制备方法 |
| US16/622,055 US11020729B1 (en) | 2017-06-16 | 2018-05-15 | Heteroatom ligand, oligomerization catalyst containing same, and method for preparing oligomer |
| JP2019568285A JP7179027B2 (ja) | 2017-06-16 | 2018-05-15 | ヘテロ原子リガンド、それを含むオリゴマー化触媒、およびオリゴマーの製造方法 |
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| US (1) | US11020729B1 (ko) |
| EP (1) | EP3640256B1 (ko) |
| JP (1) | JP7179027B2 (ko) |
| KR (1) | KR102450815B1 (ko) |
| CN (1) | CN110753695B (ko) |
| WO (1) | WO2018230846A1 (ko) |
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| CN113996343A (zh) * | 2021-11-19 | 2022-02-01 | 中化泉州石化有限公司 | 一种制备1-辛烯的催化剂组合物 |
| CN115672406B (zh) * | 2022-11-08 | 2024-05-03 | 万华化学集团股份有限公司 | 一种耐高温乙烯四聚催化剂及其应用 |
| US12364976B2 (en) | 2023-03-06 | 2025-07-22 | Saudi Arabian Oil Company | Catalyst systems suitable for the tetramerization of ethylene and methods of using the same |
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| WO2002004119A1 (en) | 2000-07-11 | 2002-01-17 | Bp Chemicals Limited | Olefin trimerisation using a catalyst comprising a source of chromium, molybdenum or tungsten and a ligand containing at least one phosphorous, arsenic or antimony atom bound to at least one (hetero)hydrocarbyl group |
| WO2004056479A1 (en) | 2002-12-20 | 2004-07-08 | Sasol Technology (Pty) Ltd | Tetramerization of olefins |
| WO2014181248A1 (en) | 2013-05-09 | 2014-11-13 | Sasol Technology (Proprietary) Limited | Oligomerisation of ethylene to mixtures of 1-hexene and 1-octene |
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| EP0967228A1 (en) | 1998-06-26 | 1999-12-29 | Dsm N.V. | Metal complex containing one or more silsesquioxane ligands |
| JP4228092B2 (ja) | 1998-09-02 | 2009-02-25 | 東ソー株式会社 | オレフィン重合体製造用触媒およびオレフィン重合体の製造方法 |
| AU6291999A (en) * | 1998-10-05 | 2000-04-26 | B.F. Goodrich Company, The | Catalyst and methods for polymerizing cycloolefins |
| BR112012022112A2 (pt) | 2010-03-01 | 2016-10-25 | Evonik Degussa Gmbh | processo para preparação de dronedarona ligantes ligados com silsesquioxano poli-hédrico oligomérico (poss) |
| EP2363402A1 (de) | 2010-03-01 | 2011-09-07 | Evonik Oxeno GmbH | Polyhedrale Oligomere Silsesquioxan (POSS)-verbundene Liganden und deren Verwendung |
| CN102617640B (zh) | 2012-03-12 | 2015-04-29 | 中国科学院化学研究所 | 磷硅协同阻燃剂及其制备方法与应用 |
| KR101606556B1 (ko) | 2014-03-17 | 2016-03-28 | 한국화학연구원 | 폴리실세스퀴옥산-표면개질된 유무기 나노세공체 및 이의 제조방법 |
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- 2018-05-15 CN CN201880040080.XA patent/CN110753695B/zh active Active
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| WO2002004119A1 (en) | 2000-07-11 | 2002-01-17 | Bp Chemicals Limited | Olefin trimerisation using a catalyst comprising a source of chromium, molybdenum or tungsten and a ligand containing at least one phosphorous, arsenic or antimony atom bound to at least one (hetero)hydrocarbyl group |
| WO2004056479A1 (en) | 2002-12-20 | 2004-07-08 | Sasol Technology (Pty) Ltd | Tetramerization of olefins |
| WO2014181248A1 (en) | 2013-05-09 | 2014-11-13 | Sasol Technology (Proprietary) Limited | Oligomerisation of ethylene to mixtures of 1-hexene and 1-octene |
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Also Published As
| Publication number | Publication date |
|---|---|
| JP2020524137A (ja) | 2020-08-13 |
| US20210146346A1 (en) | 2021-05-20 |
| JP7179027B2 (ja) | 2022-11-28 |
| EP3640256A4 (en) | 2021-02-24 |
| CN110753695A (zh) | 2020-02-04 |
| US11020729B1 (en) | 2021-06-01 |
| EP3640256A1 (en) | 2020-04-22 |
| WO2018230846A1 (ko) | 2018-12-20 |
| KR102450815B1 (ko) | 2022-10-05 |
| EP3640256B1 (en) | 2023-12-20 |
| CN110753695B (zh) | 2022-08-02 |
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