首页> 外国专利> Trivalent titanium component prepn. for Ziegler-Natta catalyst system - by grinding titanium tri:chloride complex with ester and reacting with alcohol

Trivalent titanium component prepn. for Ziegler-Natta catalyst system - by grinding titanium tri:chloride complex with ester and reacting with alcohol

机译:三价钛成分制备。用于齐格勒-纳塔催化剂体系-通过将三氯化钛络合物与酯研磨并与醇反应

摘要

In the prepn. of a new Ti(III)-component, (1), for Ziegler-Natta catalyst systems, a Ti-contg. cpd., (A), having formula TiCl3.nAlCl3 (where n is 0.01-1) is ground with a 2-34C ester, (B), having formula R1-O-CO-R2 or R1-O-CO-CR2=CHR2 (where R1 is 1-16C alkyl or 7-23C phenyl-alkyl in which the Ph gp. is opt. substd. by up to 5 1-4C alkyl gps.; R2 is H, 1-18C alkyl, 7-23C phenyl- alkyl or 7-23C alkyl-phenyl in which Pb is opt. substd. by up to 5 1-4C alkyl gps.). Specific grinding conditions are used. (B) is added to (A) in quantities corresponding to molar ratio Ti in (A) : (B) 1 : 1.5 to 1 : 0.01. A suspension of (i) 1 pt.wt. prod.; (ii) 0.5-20 pts.wt. hydrocarbon, (C), liq. under normal conditions and boiling below 150 deg.C; and (iii) a 1-20C alcohol, (D), having formula X(OH)y (where y is 1 or 2 and X is an aromatic, satd. aliphatic or cycloaliphatic hydrocarbyl gp.) is prepd. D-quantity is such as to set up molar ratio Ti in (A) : (D) 1 : 0.01 to 1 : 2. The suspension is then strongly stirred 5-120 min. at 40-140 deg.C and then cooled to 15-25 deg.C. The suspension is opt. mixed with an Al-contg cpd. (E) having formula Al(R8)x(Y)3-x (where x is 1-3; Y is Cl or R8; R8 is 1-12C alkyl). Quantities are such as to set up molar ratio OH gps. from (D) : alkyl gps. in (E) 1 : 0.005 to 1 : 2. The solid sepd. from the suspension is opt. washed with a hydrocarbon, liq. under normal conditions and boiling below 150 deg.C, and dried, to recover (I). The catalyst systems are used in 2-6C alpha-mono-olefin (co)polymerisation. Stereoregular polymers are obtd. in high yields. Fine grain proportion is reduced.
机译:在准备中。用于Ziegler-Natta催化剂系统的新型Ti(III)组分(1)的Ti-contg。 cpd。(A),具有式TiCl3.nAlCl3(其中n为0.01-1)与2-34C酯研磨,(B),具有式R1-O-CO-R2或R1-O-CO-CR2 = CHR2(其中R1是1-16C烷基或7-23C苯基-烷基,其中Ph gp。最优选被5个1-4C烷基gps取代; R2是H,1-18C烷基,7- 23 C苯基烷基或7-23 C烷基苯基,其中Pb优选被最多5个1-4 C烷基gps取代)。使用特定的研磨条件。将(B)以与(A):(B)为1∶1.5至1∶0.01的摩尔比Ti相对应的量添加至(A)。 (i)1 pt.wt.产品; (ii)0.5-20磅碳氢化合物(C)在正常条件下,沸点低于150℃; (iii)具有式X(OH)y(其中y为1或2且X为芳族,饱和脂族或脂环族烃基gp。)的1-20C醇(D)。 D量设定为在(A):(D)1∶0.01至1∶2中设定摩尔比Ti。然后将悬浮液强烈搅拌5-120分钟。在40-140℃下,然后冷却至15-25℃。暂停是可选的。与Al-contg cpd混合。 (E)具有式Al(R8)x(Y)3-x(其中x为1-3; Y为Cl或R8; R8为1-12C烷基)。数量可设置OH gps摩尔比。来自(D):烷基gps。在(E)中为1:0.005至1:2。选择暂停。用碳氢化合物洗涤。在正常条件下并在低于150℃下沸腾,干燥,以回收(I)。催化剂体系用于2-6Cα-单烯烃(共)聚合。立体球状聚合物被去除。高产。细粒比例降低。

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