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    • 3. 发明申请
    • CATALYST COMPOSITION FOR OLIGOMERIZATION OF ETHYLENE AND PROCESSES OF OLIGOMERIZATION
    • 乙烯低聚化催化剂组合物及其低分子化方法
    • US20130018214A1
    • 2013-01-17
    • US13637976
    • 2011-03-30
    • Mingfang ZhengWeizhen LiHuaijie WangJun LiuHaiying ZhangYu ZhouTonglin LiLan ZhaoJilong WangHongfei WuYuling PiaoJunlong Sui
    • Mingfang ZhengWeizhen LiHuaijie WangJun LiuHaiying ZhangYu ZhouTonglin LiLan ZhaoJilong WangHongfei WuYuling PiaoJunlong Sui
    • B01J31/12C07C2/26
    • C08F10/02B01J31/143B01J31/183B01J2231/20B01J2531/842B01J2531/845B01J2531/847C07C2/32C07C2531/14C07C2531/22C08F110/02Y02P20/52C08F4/7042C08F2500/02C07C11/02C08F210/02
    • The present invention provides a catalyst composition for the ethylene oligomerization, which comprises 2-imino-1,10-phenanthroline coordinated iron (II), cobalt (II) or nickel (II) chloride as main catalyst and triethylaluminum as cocatalyst. The present invention also provides a process for oligomerization of ethylene is provided, wherein a catalyst composition comprising 2-imino-1,10-phenanthroline coordinated iron (II), cobalt (II) or nickel (II) chloride as main catalyst and triethylaluminum as cocatalyst is used, and the molar ratio of aluminum in the cocatalyst to central metal in the main catalyst ranges from 30 to less than 200. According to the present invention, another process for oligomerization of ethylene is also provided, wherein a catalyst composition comprising 2-imino-1,10-phenanthroline coordinated iron (II), cobalt (II) or nickel (II) chloride as main catalyst and triethylaluminum as cocatalyst is used, and the temperature of ethylene oligomerization ranges from −10 to 19° C. According to the present invention, the price of cocatalyst i.e. triethylaluminum, is low, just a fraction of that of methylaluminoxane, the amount of cocatalyst is therefore significantly reduced, with the catalytic activity is still acceptable, thus the cost of ethylene oligomerization is significantly reduced. In view of both the catalytic activity and the cost, the present invention is highly applicable in industry.
    • 本发明提供了一种用于乙烯低聚的催化剂组合物,其包含2-亚氨基-1,10-菲咯啉配位的铁(II),钴(II)或氯化镍(II)作为主要催化剂,三乙基铝作为助催化剂。 本发明还提供了一种乙烯低聚方法,其中包含2-亚氨基-1,10-菲咯啉配位的铁(II),钴(II)或氯化镍(II)作为主要催化剂的催化剂组合物和三乙基铝作为 助催化剂,主催化剂中助催化剂与中心金属之间的铝的摩尔比为30至小于200.根据本发明,还提供了另一种乙烯低聚方法,其中催化剂组合物包含2 - 亚氨基-1,10-菲咯啉配位的铁(II),钴(II)或氯化镍(II)为主催化剂,三乙基铝为助催化剂,乙烯齐聚温度为-10〜19℃。 对于本发明,助催化剂即三乙基铝的价格低,仅仅是甲基铝氧烷的一部分,因此助催化剂的量显着降低,催化活性为 仍然是可接受的,因此乙烯低聚的成本显着降低。 鉴于催化活性和成本两方面,本发明在工业上是高度适用的。
    • 9. 发明授权
    • Determining a data flow metric
    • 确定数据流量度
    • US08767557B1
    • 2014-07-01
    • US13619916
    • 2012-09-14
    • Daniel VivancoYu ZhouShahzada RasoolMuhammad Ahsan Naim
    • Daniel VivancoYu ZhouShahzada RasoolMuhammad Ahsan Naim
    • H04W72/04H04L12/26H04W4/00H04W28/10
    • H04L43/10H04L43/0876
    • In a system and method of determining a data flow metric in a wireless communication system, sending a plurality of test packets to a plurality of wireless devices in communication with an access node, determining a first inter-arrival gap and a first physical resource block-to-transmission time interval (PRB-TTI) ratio for each wireless device during a first time period, and a first comparison of the first inter-arrival gap to the first PRB-TTI ratio for each wireless device, determining a second inter-arrival gap and a second PRB-TTI ratio for each wireless device during a second time period, and a second comparison of the second inter-arrival gap to the second PRB-TTI ratio for each wireless device, and determining whether a data flow metric of the access node meets a data flow criteria based on the first and second comparisons.
    • 在确定无线通信系统中的数据流量度量的系统和方法中,向与接入节点通信的多个无线设备发送多个测试分组,确定第一到达间隙间隔和第一物理资源块 - 在第一时间段期间每个无线设备的传输时间间隔(PRB-TTI)比率以及针对每个无线设备的第一到达间隙与第一PRB-TTI比率的第一比较,确定第二到达间 间隙和第二PRB-TTI比率,以及第二时间间隔与第二PRB-TTI比率对于每个无线设备的第二比较,以及确定是否有数据流量度量 访问节点基于第一和第二比较满足数据流标准。