申请人:Petrochina Company Limited
公开号:US07786336B2
公开(公告)日:2010-08-31
The present invention relates to a catalyst composition for ethylene oligomerization and the use thereof. Such catalyst composition includes chromium compound, ligand containing P and N, activator and accelerator; wherein the chromium compound is selected from the group consisting of acetyl acetone chromium, THF-chromium chloride and Cr(2-ethylhecanoate)3; general formula of the ligand containing P and N is shown as:
in which R1, R2, R3 and R4 are phenyl, benzyl, or naphthyl. R5 is isopropyl, butyl, cyclopropyl, cyclopentyl, cyclohexyl or fluorenyl; the activatior is methyl aluminoxane, ethyl aluminoxane, propyl aluminoxane and/or butyl aluminoxane; the accelerator is selected from the group consisting of 1,1,2,2,-tetrachloroethane, 1,1,2,2-tetrabromoethane, 1,1,2,2-tetrafluoroethane, and compounds having a formula of X1R6X2, in which X1 and X2 are F, Cl, Br, I or alkoxyl, R6 is alkylene or arylene group; the molar ratio of chromium compound, ligand containing P and N, activator and accelerator is 1:0.5˜10:50˜3000:0.5˜10. After mixing the four components mentioned previously under nitrogen atmosphere for 10 minutes, they are incorporated to the reactor, or these four components are incorporated directly into the reactor. Then ethylene is introduced for oligomerization. Such catalyst can be used in producing 1-octene through ethylene oligomerization. It is advantageous in high catalysing activity, high 1-octene selectivity, etc. The catalytic activity is more than 1.0×106 g product·ma−1 Cr·h−1, the fraction of C8 linear α-olefin is more than 70% by mass.
本发明涉及一种用于乙烯寡聚的催化剂组合物及其使用。该催化剂组合物包括铬化合物、含有P和N的配体、活性剂和加速剂;其中,铬化合物选自乙酰丙酮铬、THF-氯化铬和Cr(2-乙基庚酸)3等组中;含有P和N的配体的通用公式如下:其中,R1、R2、R3和R4为苯基、苄基或萘基。R5为异丙基、丁基、环丙基、环戊基、环己基或芴基;活化剂为甲基铝氧烷、乙基铝氧烷、丙基铝氧烷和/或丁基铝氧烷;加速剂选自1,1,2,2-四氯乙烷、1,1,2,2-四溴乙烷、1,1,2,2-四氟乙烷和具有X1R6X2公式的化合物,其中X1和X2为F、Cl、Br、I或烷氧基,R6为烷基或芳基;铬化合物、含有P和N的配体、活性剂和加速剂的摩尔比为1:0.5~10:50~3000:0.5~10。在氮气氛下混合前述四种组分10分钟后,它们被加入反应器,或者这四种组分直接被加入反应器。然后引入乙烯进行寡聚化反应。这种催化剂可用于通过乙烯寡聚生产1-辛烯。它具有高催化活性、高1-辛烯选择性等优点。催化活性大于1.0×106 g产物·ma−1 Cr·h−1,C8直链α-烯烃的质量分数大于70%。