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公开(公告)号:EP3789436B1
公开(公告)日:2024-11-06
申请号:EP19882345.2
申请日:2019-08-23
发明人: CHOI, Seung Won , JOO, Eun Jung
IPC分类号: C08F110/02 , C08K5/14 , C08L23/08
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2.
公开(公告)号:EP4455169A1
公开(公告)日:2024-10-30
申请号:EP23193732.7
申请日:2023-08-28
IPC分类号: C08F110/06 , C08F210/06
摘要: The present disclosure relates to a catalyst composition for polymerizing propylene and a method for producing polypropylene. The catalyst composition for polymerizing the propylene includes a modifying agent. The modifying agent is an ester compound having hydrophilic groups and hydrophobic groups. In the method for producing the polypropylene, a reverse microcellular structure is formed by the modifying agent during a propylene polymerization, in which the hydrophilic groups are inside the reverse microcellular structure, and the hydrophobic groups are outside the reverse microcellular structure, such that polar substances in a raw material are retained inside the reverse microcellular structure. Thus, poisoning of the catalyst is reduced. Besides, the modifying agent can maintain a valence state of titanium in an active site of the catalyst at positive trivalent, such that the propylene polymerization between the titanium and the monomer is facilitated, thereby enhancing an activity of the catalyst.
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3.
公开(公告)号:EP4453049A1
公开(公告)日:2024-10-30
申请号:EP22835723.2
申请日:2022-12-12
申请人: Borealis AG
发明人: BURYAK, Andrey , SUMERIN, Victor
IPC分类号: C08F210/16 , C08F110/02 , F16L9/00 , C08L23/06 , C08L23/08 , F16L9/12
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公开(公告)号:EP3980588B1
公开(公告)日:2024-10-09
申请号:EP20726419.3
申请日:2020-05-18
IPC分类号: D01F6/06 , C08F110/06
CPC分类号: C08F110/06 , D01F6/06
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5.
公开(公告)号:EP4438635A2
公开(公告)日:2024-10-02
申请号:EP24187350.4
申请日:2017-03-06
IPC分类号: C08F110/06
CPC分类号: C08F110/06
摘要: A solid precatalyst component for use in olefinic polymerization, includes titanium, magnesium, and an electron donor compound; wherein: the electron donor compound is at least one compound represented by Formula (I):
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公开(公告)号:EP4426670A1
公开(公告)日:2024-09-11
申请号:EP22850624.2
申请日:2022-12-01
IPC分类号: C07C1/24 , C07C11/04 , C07C31/08 , C07C29/151 , C07C2/32 , C07C11/10 , C07C11/02 , C08F110/00 , C12P3/00 , C25B3/00
CPC分类号: C07C1/24 , C07C29/1518 , C07C2/32 , C08F10/02 , C25B1/04 , C25B15/081 , C12P7/06
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公开(公告)号:EP4421149A2
公开(公告)日:2024-08-28
申请号:EP24155401.3
申请日:2024-02-01
发明人: ITO, Masaki , SAKAKIBARA, Katsumi
IPC分类号: C09K15/08 , C08F110/06 , C08F210/06 , C09K15/32
CPC分类号: C09K15/322 , C09K15/08 , C08F210/06 , C08F110/06
摘要: Provided is a method of storing an antioxidant mixture for producing a more thermally stable polymer.
A method of storing an antioxidant mixture, comprising storing an antioxidant mixture containing an antioxidant and an aluminum compound under a condition at a gauge pressure of 0.21 MPa or higher.-
公开(公告)号:EP4372012A3
公开(公告)日:2024-08-07
申请号:EP24159765.7
申请日:2014-02-25
发明人: YANG, Qing , MCDANIEL, Max P , CRAIN, Tony R , CLEAR, Kathy S
IPC分类号: C08F4/6592 , C08F10/02 , C08F110/02 , C08F4/02
CPC分类号: C08F10/02 , C08F2410/0720210101
摘要: Disclosed herein are polymerization processes for the production of olefin polymers. These polymerization processes use a catalyst system containing at least two activator-supports. One activator-support is a halided solid oxide, and the other activat-or-support is a sulfated solid oxide and/or phosphated solid oxide.
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公开(公告)号:EP3868796B1
公开(公告)日:2024-07-31
申请号:EP19874270.2
申请日:2019-10-15
IPC分类号: C08F10/06 , C08F4/649 , C08F4/654 , C08F110/06 , C08F10/00
CPC分类号: C08F10/00 , C08F110/06 , C08F2410/0620210101
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公开(公告)号:EP4389783A1
公开(公告)日:2024-06-26
申请号:EP22215204.3
申请日:2022-12-20
申请人: Borealis AG
IPC分类号: C08F110/06
CPC分类号: C08F110/06 , C08F4/65912 , C08F4/65916 , C08F2410/0520130101
摘要: A process for transitioning between two different catalysts during the production of polypropylene homo- or copolymers in a continuous multistage polymerisation reaction , the process comprising the steps of:
a) polymerising propylene and optionally comonomers in a multi stage polymerisation reactor system comprising a prepolymerization reactor, a subsequent slurry reactor and thereafter a gas phase reactor in the presence of a first catalyst;
b) discontinuing the feed of the first catalyst to the prepolymerization reactor;
c) subsequently introducing, propylene, optionally comonomers, and a second catalyst into the prepolymerization reactor, and further introducing an aluminium alkyl into the polymerization reactor simultaneously with the introduction of the second catalyst;
d) polymerising propylene and optionally comonomers in the multistage polymerisation reactor system in the presence of the second catalyst;
wherein the first catalyst is a Ziegler-Natta catalyst and the second catalyst is a single site catalyst; and
wherein the amount of aluminium alkyl fed in step c) is 0.5 to 10.0 g per ton of total propylene fed into the prepolymerisation reactor and the slurry reactor in steps c) and d).
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