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

Trivalent titanium component prepn. for Ziegler-Natta catalyst system - by grinding titanium tri:chloride complex with phosphorus cpd. and reacting with ether and/or ester

机译:三价钛成分制备。用于Ziegler-Natta催化剂系统-通过与磷cpd研磨三氯化钛络合物。与醚和/或酯反应

摘要

In the prepn. of a new Ti(III)-component (1) for Ziegler-Natta catalyst systems, a Ti-contg. cpd. having TiCl3.nAlCl3, (A), (where n is 0.01-1) is ground with a P-contg. cpd. having formula OmP(R1)3, (B), (where m is 0 or 1 ; R1 is R2, OR2 or N(R2)2 and R2 is 1-24C alkyl, aryl, alkaryl or aralkyl). Specific grinding conditions are used. (B) is added to (A) in quantities corresponding to molar ratio Ti in (A) : (B) 1 : 0.01 to 1 : 1. A suspension of (i) 1 pt.wt. of prod.; (ii) 0.5-20 pts.wt. hydrocarbon, (C), liq. under normal conditions and boiling below 150 deg.C; and (iii) an O-contg. cpd. (D) is prepd. (D) can be a 4-30C ether of formula R8-O-R8' (where R8 and R8' are 1-15C alkyl, Ph or 7-14C alkyl-phenyl) and/or a 2-34C ester having formula R9'-O-CO-R9 or R9'-O-CO-CR9=CHR9 (where R9 is H, 1-12C alkyl, 7-14C phenyl-alkyl in which Ph is opt. mono-alkyl substd., Ph or 7-14C alkyl-phenyl ; R9' is 1-8C alkyl, Ph or 7-14C phenyl-alkyl). (D)-quantities are such that molar ratio Ti in (A) to (D) is 1 : 0.01 to 1 : 2. The suspension is strongly stirred 5-120 min. at 40-140 deg. C and cooled to 15-25 deg.C. The solid separated from the suspension is opt. washed with a hydrocarbon, liq. under normal conditions and boiling below 150 deg.C and dried to recover the new Ti(III)-componentt (1). The catalyst systems are used in 2-6C alpha-mono-olefin (co)polymerisation. Stereoregular polymers are obtd. in high yields. The prods. have a low fine grain proportion.
机译:在准备中。用于齐格勒-纳塔催化剂体系的新型Ti(III)组分(1)的制备,包括Ti-contg。 cpd。将具有TiCl 3·nAlCl 3(A)(其中n为0.01-1)的P-contg研磨。 cpd。具有式OmP(R 1)3,(B)(其中m为0或1; R 1为R 2,OR 2或N(R 2)2且R 2为1-24C的烷基,芳基,烷芳基或芳烷基)。使用特定的研磨条件。将(B)以对应于(A):(B)1∶0.01至1∶1的摩尔比Ti的量加入(A)。(i)1磅重量的悬浮液。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)O-contg。 cpd。 (D)是准备。 (D)可以是式R8-O-R8'的4-30C醚(其中R8和R8'是1-15C烷基,Ph或7-14C烷基-苯基)和/或具有式R9的2-34C酯'-O-CO-R9或R9'-O-CO-CR9 = CHR9(其中R9是H,1-12C烷基,7-14C苯基烷基,其中Ph是单烷基取代基,Ph或7 -14C烷基-苯基; R9'是1-8C烷基,Ph或7-14C苯基-烷基)。 (D)的量应使得(A)与(D)的摩尔比Ti为1∶0.01至1∶2。将悬浮液强烈搅拌5-120分钟。在40-140度并冷却至15-25℃。从悬浮液中分离出的固体是优选的。用碳氢化合物洗涤。在正常条件下沸点低于150℃,干燥以回收新的Ti(III)-组分(1)。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。刺。细粒比例低。

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