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公开(公告)号:US20060223958A1
公开(公告)日:2006-10-05
申请号:US11386289
申请日:2006-03-22
申请人: D. Fischbuch
发明人: D. Fischbuch
IPC分类号: C08F2/00
CPC分类号: C08F110/02 , Y02P20/584 , Y10S526/901 , Y10S526/905 , C08F4/69 , C08F2/34 , C08F2500/07
摘要: Processes for reducing the ultra high molecular weight polymeric material content of a high density polyethylene produced with a bis-triarylsilyl chromate catalyst system are provided. Processes for reducing the gel content of articles produced from high density polyethylene are also provided. The gel content of the articles is reduced by using the high density polyethylene with reduced ultra high molecular weight polymeric material content to produce the articles. The processes described reduce the content of ultra high molecular weight polymeric material in comparison to conventional high density polyethylene by introducing at least one catalyst deactivator into a recycle gas line containing a recycle gas stream associated with the fluidized bed reactor. The at least one catalyst deactivator has a boiling point lower than the maximum temperature within the recycle gas line. In certain embodiments, the at least one catalyst deactivator is introduced in the portion of the recycle gas line upstream of a recycle gas cooler at a ratio of 0.0075 mole of the at least one catalyst deactivator per 1 million moles of make-up ethylene to about 0.12 mole of the at least one catalyst deactivator per 1 million moles of make-up ethylene in the reaction system. In certain embodiments, the at least one catalyst deactivator is oxygen.
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公开(公告)号:US20080045676A1
公开(公告)日:2008-02-21
申请号:US11975053
申请日:2007-10-17
申请人: Robert Hagerty , Kevin Stavens , Marc DeChells , D. Fischbuch , James Farley
发明人: Robert Hagerty , Kevin Stavens , Marc DeChells , D. Fischbuch , James Farley
IPC分类号: C08F4/76
CPC分类号: C08F210/16 , Y10S526/901 , C08F2/34 , C08F2/005 , C08F210/14 , C08F2500/12
摘要: The present invention relates to a continuous gas phase process comprising polymerizing one or more hydrocarbon monomer(s) in a fluidized bed reactor in the presence of a Ziegler-Natta-type catalyst system and a condensable fluid for a period of at least 12 hours where the bed temperature is less than the Critical Temperature and the dew point temperature of the gas composition in the reactor is within 25° C. of the bed temperature.
摘要翻译: 本发明涉及连续气相方法,其包括在齐格勒 - 纳塔型催化剂体系和可冷凝流体存在下在流化床反应器中聚合一种或多种烃单体至少12小时的时间, 床温低于临界温度,反应器中气体组成的露点温度在床温25℃以内。
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公开(公告)号:US20070265400A1
公开(公告)日:2007-11-15
申请号:US11433682
申请日:2006-05-12
申请人: D. Fischbuch , Robert Hagerty , Sandy Hinds , Douglas Holroyd , Ai Vey Ng , Diwaker Singh
发明人: D. Fischbuch , Robert Hagerty , Sandy Hinds , Douglas Holroyd , Ai Vey Ng , Diwaker Singh
IPC分类号: C08F2/00
CPC分类号: B01J8/1809 , B01J2208/00274 , B01J2219/00191 , C08F10/00 , C08F110/02 , C08F2400/02 , Y10S526/901 , C08F2/34 , C08F2/00
摘要: The present invention relates to a continuous gas phase process comprising passing a recycle stream through a fluidized bed in a gas phase fluidized bed reactor, wherein the recycle stream comprises a low molecular weight dew point increasing component and a high molecular weight component, polymerizing an alpha-olefin monomer in the presence of a catalyst, and controlling an amount of the low molecular weight dew point increasing component in the recycle stream such that a dew point approach temperature of the recycle stream is less than the dew point approach temperature when operating with the higher molecular weight dew point increasing component alone.
摘要翻译: 连续气相方法本发明涉及一种连续气相方法,包括使循环流通过气相流化床反应器中的流化床,其中再循环流包含低分子量露点增加组分和高分子量组分,聚合α 烯烃单体,并且控制再循环流中低分子量露点增加组分的量,使得当循环流中的露点接近温度小于露点接近温度时 较高分子量露点增加组分。
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公开(公告)号:US20070004878A1
公开(公告)日:2007-01-04
申请号:US11515525
申请日:2006-09-05
申请人: Robert Hagerty , Kevin Stavens , Marc DeChellis , D. Fischbuch , James Farley
发明人: Robert Hagerty , Kevin Stavens , Marc DeChellis , D. Fischbuch , James Farley
IPC分类号: C08F2/00
CPC分类号: C08F210/16 , Y10S526/901 , C08F2/34 , C08F2/005 , C08F210/14 , C08F2500/12
摘要: The present invention relates to a continuous gas phase process comprising polymerizing one or more hydrocarbon monomer(s) in a fluidized bed reactor in the presence of catalyst system or polymerization catalyst and a condensable fluid for a period of at least 12 hours where the bed temperature is less than the Critical Temperature and the dew point temperature of the gas composition in the reactor is within 25° C. of the bed temperature.
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