会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明申请
    • PROCESS TO CONTROL OUTPUT AND QUALITY OF ETHYLENE-BASED POLYMER FORMED BY HIGH PRESSURE FREE RADICAL POLYMERIZATION
    • 通过高压自由基聚合形成的基于乙烯的聚合物的输出和质量控制方法
    • WO2016109266A1
    • 2016-07-07
    • PCT/US2015/066860
    • 2015-12-18
    • DOW GLOBAL TECHNOLOGIES LLCDOW BRASIL SUDESTE INDUSTRIAL LTDA.
    • HOSMAN, Cornelis J.F.BERBEE, Otto J.GONCALVES, Sergio E.DANG, Nhi
    • C08F2/01C08F2/34
    • C08F2/01C08F2/34Y02P20/582
    • The invention provides a process to prepare an ethylene-based polymer, said process comprising polymerizing ethylene in the presence of at least one initiator system selected from the following: a) class 1 initiator system, b) class 2 initiator system, c) class 3 initiator system, or d) a combination thereof; and at a inlet pressure (P 2 ) greater than, or equal to, 1000 Bar (100 MPa); and in a reactor system comprising at least one hyper compressor and a reactor configuration comprising at least one reactor, which comprises at least one reaction zone; and wherein the inlet pressure (P 2 ) is reduced by at least 200 Bar, as compared to a similar polymerization, in the same reactor system, except it is operated at a higher inlet pressure (P 1 ), and at a different hyper compressor throughput, and at a different maximum temperature for at least one reaction zone, and optionally, at a different amount of CTA system fed to the reactor configuration; and wherein, for the process, the "Ratio of total reactor consumption of the highest temperature class initiator system(s) (Y)" meets the following Equation D: 0.95 * x^((P 1 -P 2 )/10MPa) 1 -P 2 )/10MPa) (Eqn. D), wherein x is greater than, or equal to, 0.97; and wherein z is less than, or equal to, 1.03. The invention also provides a process to prepare an ethylene-based polymer, said process comprising polymerizing ethylene in the presence of at least one initiator system selected from the following: a) a class 1 initiator system, b) a class 2 initiator system, c) a class 3 initiator system, or d) a combination thereof; and at an inlet pressure (P 2 ) greater than, or equal to, 1000 Bar (100 MPa); and in a reactor system comprising a reactor configuration comprising at least one reactor, which comprises at least one reaction zone; and wherein the inlet pressure (P 2 ) is reduced by at least 200 Bar, as compared to a similar polymerization, in the same reactor configuration, except it is operated at a higher inlet pressure (P 1 ), and at a different maximum temperature for at least one reaction zone, and optionally, at a different amount of CTA system fed to the reactor configuration; and wherein, for the process, the "Ratio of total reactor consumption of the highest temperature class initiator system(s) (Y)" meets the following Equation D: 0.95 * x^((P 1 -P 2 )/10MPa) 1 -P 2 )/10MPa) (Eqn. D), wherein x is greater than, or equal to, 0.97; and wherein z is less than, or equal to, 1.03.
    • 本发明提供一种制备乙烯基聚合物的方法,所述方法包括在至少一种选自以下的引发剂体系的存在下聚合乙烯:a)1类引发剂体系,b)2类引发剂体系,c)3类 引发剂体系,或d)其组合; 并且在大于或等于1000巴(100MPa)的入口压力(P2)下; 以及包括至少一个超压缩机和包括至少一个反应器的反应器构型的反应器系统,所述反应器包括至少一个反应区; 并且其中在相同的反应器系统中,与相似的聚合相比,入口压力(P2)除了至少200巴,除了其在较高的入口压力(P1)下运行,并且在不同的超压缩机生产量下, 并且在不同的最高温度下对于至少一个反应区,以及任选的不同量的进料到反应器构型的CTA体系; 并且其中,对于该方法,“最高温度级引发剂体系(Y)”的总反应器消耗量的比例满足以下等式D:0.95 * x ^((P1-P2)/ 10MPa)