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Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins

一种烯烃聚合、催化剂的技术,应用在制备固体金属茂催化剂体系以及该催化剂体系在烯烃聚合中的应用领域,能够解决降低催化剂体系形态学、预聚合增加成本、结片等问题

Inactive Publication Date: 2013-01-16
北欧化工公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0019] Also, the use of these highly reactive fluorinated compounds is considered problematic in terms of HS&E (Health, Safety and Environment), so the future availability of these compounds cannot be ensured
[0020] Many prior art catalyst systems have the disadvantage that in slurry reactors they tend to dissolve to some extent in the desired polymerization medium, thus degrading the morphology of the catalyst system, which in turn causes condensation in the reactor. Scale and flakes
Besides being a sensitive step, prepolymerization adds cost on an industrial scale

Method used

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  • Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins
  • Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins
  • Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0291] Example 1: Preparation of liquid clathrates; variant B

[0292] 250 mg of racemic cyclohexyl(methyl)silanediyl-bis(2-methyl-4-(4'-tert-butylphenyl)indene- 1-yl) zirconium dichloride was reacted with 15 mL of 30 wt% MAO solution in toluene to form a catalyst solution. Al / Zr is 370 mol / mol.

[0293] 0.97 mL of clathrate reagent octamethyltrisiloxane (OMTS) was added to this solution, and the solution thus obtained was placed in a glove box overnight while mixing. After adding OMTS, the red mixture turned orange. On day 2, mixing was stopped and the liquid separated into a toluene phase and a catalyst phase. Use 5 mL of bottom catalyst phase. The liquid has now changed its color to dark red, and the top phase also has a reddish color.

Embodiment 2

[0294] Example 2: Preparation of liquid clathrates; variant A

[0295] 0.97 mL of the clathrate reagent octamethyltrisiloxane (OMTS) was added to 15 mL of a 30 wt% MAO solution in toluene, and the resulting slurry was stirred overnight. Stirring was then stopped and two separate phases formed. Discard the upper phase.

[0296] Add 5 mL of the lower layer containing the clathrated MAO to 179 mg of racemic cyclohexyl(methyl)silanediyl-bis(2-methyl-4-(4'-tert-butylphenyl)indene-1 - base) zirconium dichloride. The resulting solution was stirred for 1 hour and had a dark red color.

[0297] Al / Zr is 235 mol / mol.

Embodiment 3

[0299] 5mL of the catalyst solution prepared according to Example 1 was added into a 30mL GPL 106 in a 50 mL emulsion glass reactor equipped with "open baffles" and a stirrer suspended below the oil surface. Mixing was then started for 15 minutes with a tip speed of 0.75 m / s (mixing speed 250 rpm).

[0300] Argon was then turned on to evaporate the toluene. The residual catalyst / oil slurry was siphoned into a septum bottle with argon flushing continued for 120 minutes before mixing was stopped.

[0301] catalyst

[0302] PSD: 5-15μm (based on SEM image)

[0303]The catalyst productivity was 5 kgPP / g catalyst·h.

[0304] from figure 1 with figure 2 As can be seen in , perfectly spherical particles with smaller particle sizes are formed.

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Abstract

A process for the preparation of a solid olefin polymerisation catalyst system, comprising an organometallic compound of a transition metal of Group 3 to 10 of the Periodic Table (IUPAC 2007) in the form of solid particles comprising the steps of I) generating an emulsion by dispersing a liquid clathrate in a solvent (S) wherein (i) the solvent (S) constitutes the continuous phase of the emulsion and comprises a nonreactive fluorinated synthetic oil having a viscosity at 20 DEG C according to ASTM D445 of at least 10 cSt up to 2000 cSt, (ii) the liquid clathrate constitutes in form of droplets the dispersed phase of the emulsion, II) solidifying said dispersed phase to convert said droplets to solid particles and III) optionally recovering said particles to obtain said catalyst system, wherein the liquid clathrate comprises (a) a lattice being the reaction product of a1); a transition metal compound of formula (I) LmRnTXq wherein T is a transition metal of anyone of the groups 3 to 10 of the periodic table (IUPAC2007), preferably a transition metal of anyone of the groups 4 to 6 of the periodic table (IUPAC2007), more preferably titanium (Ti), zirconium (Zr) or hafnium (Hf), i.e. zirconium (Zr) or hafnium (Hf), each X is independently a monovalent sigma-ligand, each L is independently an organic ligand which coordinates to the transition metal (T), R is a bridging group linking said organic ligands (L), m is 2 or 3, preferably 2, n is 0, 1 or 2, preferably 1, q is 1, 2 or 3, preferably 2, m+q is equal to the valency of the transition metal (T), a2) a cocatalyst comprising aluminoxane a3) a compound being effective to form the lattice with the transition metal compound and / or the aluminoxaneand b) a hydrocarbon solvent (HS).

Description

technical field [0001] The invention relates to an improved method for preparing a solid metallocene catalyst system by emulsification / solidification technology, and the application of the catalyst system in olefin polymerization. [0002] In particular, the present invention describes the use of emulsification / solidification techniques for the preparation of solid metallocene catalyst systems in which the liquid clathrate constitutes the dispersed phase of the emulsion and has a viscosity at 20°C according to ASTM D445 of at least A non-reactive fluorinated synthetic oil of 10 cSt (centistokes) was used as the continuous phase. Background technique [0003] Many catalysts and processes are known for preparing olefin polymers. For example, Ziegler-Natta (ZN) catalyst compositions and chromium oxide compounds have been found useful in the preparation of polyolefins. [0004] Further, the use of metallocene catalysts in olefin polymerization has been known for many years and...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/00C08F4/659C07F5/06C08G65/00C08F4/6592
CPCC08F10/00B01J2531/49C08F4/65922B01J31/0268B01J2531/90B01J31/143B01J31/2295B01J2531/94B01J31/128B01J2531/46C08F4/6592C08F2410/01B01J31/26B01J31/0239B01J31/124B01J2531/48C08F4/65912
Inventor 詹尼·瓦洛宁玛丽亚·穆斯托宁
Owner 北欧化工公司
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