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公开(公告)号:EP3263606A1
公开(公告)日:2018-01-03
申请号:EP16177220.7
申请日:2016-06-30
发明人: VATER, Marcus , WENDLER, Ulrich , BARTKE, Michael
IPC分类号: C08F2/02
摘要: The present invention is directed at a bulkpolymerisation process for the preparation of a polymer (P) comprising the steps of:
(i) providing at least one diene monomer (DM) and optionally at least one comonomer (COM);
(ii) contacting the at least one diene monomer (DM) and optionally the at least one comonomer (COM) with a catalyst system (CS) forming a reaction mixture (RM);
(iii) polymerizing the reaction mixture (RM) comprising the at least one diene monomer (DM) and optionally the at least one comonomer (COM) in at least one reactor vessel (RV);
(iv) isolating the polymer (P) obtained from the at least one reactor vessel (RV); wherein the reaction mixture (RM) comprises solvent, diluent and/or dispersant in an amount of ≤ 10 wt.-%, based on the weight of the reaction mixture (RM); and
wherein the conversion rate of the diene monomer (DM) and optionally the comonomer (COM) is ≥ 80 %.摘要翻译: 本发明涉及用于制备聚合物(P)的本体聚合方法,其包括以下步骤:(i)提供至少一种二烯单体(DM)和任选的至少一种共聚单体(COM); (ii)使所述至少一种二烯单体(DM)和任选的所述至少一种共聚单体(COM)与形成反应混合物(RM)的催化剂体系(CS)接触; (iii)在至少一个反应器容器(RV)中使包含至少一种二烯单体(DM)和任选的至少一种共聚单体(COM)的反应混合物(RM)聚合; (iv)分离从至少一个反应器容器(RV)获得的聚合物(P); 其中基于所述反应混合物(RM)的重量,所述反应混合物(RM)包含≤10重量%的溶剂,稀释剂和/或分散剂; 并且其中二烯单体(DM)和任选的共聚单体(COM)的转化率≥80%。
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公开(公告)号:EP3478726B1
公开(公告)日:2020-05-27
申请号:EP17733474.5
申请日:2017-06-29
发明人: VATER, Marcus , WENDLER, Ulrich , BARTKE, Michael
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公开(公告)号:EP3478726A1
公开(公告)日:2019-05-08
申请号:EP17733474.5
申请日:2017-06-29
发明人: VATER, Marcus , WENDLER, Ulrich , BARTKE, Michael
摘要: The present invention is directed at a bulkpolymerisation process for the preparation of a polymer (P) comprising the steps of: (i) providing at least one diene monomer (DM) and optionally at least one comonomer (COM); (ii) contacting the at least one diene monomer (DM) and optionally the at least one comonomer (COM) with a catalyst system (CS) forming a reaction mixture (RM); (iii) polymerizing the reaction mixture (RM) comprising the at least one diene monomer (DM) and optionally the at least one comonomer (COM) in at least one reactor vessel (RV); (iv) isolating the polymer (P) obtained from the at least one reactor vessel (RV); wherein the reaction mixture (RM) comprises solvent, diluent and/or dispersant in an amount of ‰¤ 10 wt.-%, based on the weight of the reaction mixture (RM); and wherein the conversion rate of the diene monomer (DM) and optionally the comonomer (COM) is ‰¥ 80 %.
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