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Dual catalyst on a single support

Active Publication Date: 2006-06-08
NOVA CHEM (INT) SA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0014] (c) altering the partial pressure of one or more of the C2-8 olefins in the reaction mixture by not less than 10 psi (68.94 KPa); and
[0015] (d) altering the amount of no

Problems solved by technology

The patent does not teach the use of mixed catalysts systems for bimodal resins nor does it teach process control to adjust the polymer characteristics such as bimodality and comonomer incorporation.
Further the reference fails to teach or suggest the molecular weight distribution of the components in the resulting polymer may be altered or controlled by altering or controlling the reaction conditions.

Method used

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  • Dual catalyst on a single support
  • Dual catalyst on a single support
  • Dual catalyst on a single support

Examples

Experimental program
Comparison scheme
Effect test

example 1

Preparation of Catalyst A

[0155] In a glovebox, 1.95 g of silica-supported MAO prepared above was slurried in 15 mL of toluene. Separately, 35 mg of catalyst component 1 was dissolved in 20 mL of toluene, and 12 mg of (tBu3PN)(n-butyl indenyl)TiCl2 was dissolved in 20 mL of toluene. Both catalyst solutions were added simultaneously to the silica slurry. After 1 hour of stirring, the slurry was filtered, yielding a clear filtrate. The solid component was washed twice with toluene, and once with heptane. The final product was dried in vacuo to 300 mtorr (40 Pa) and stored under nitrogen until use.

Polymerization

[0156] A 2 L stirred autoclave reactor was heated at 100° C. for 1 hour and thoroughly purged with nitrogen. 160 g of NaCl predried in an oven at 160° C. for at least a week was added in the reactor which was subsequently pressure purged three times with nitrogen and twice with ethylene at 100° C. The reactor was then cooled to 90° C. and an aliquot of 25 weight % triisobuty...

example 2

Preparation of Catalyst B

[0158] In a glovebox, 1.95 grams of silica-supported MAO prepared above was slurried in 15 mL of toluene. Separately, 26 mg of catalyst component 1 was dissolved in 20 mL of toluene, and 21 mg of (tBu3PN)(C6F5CH2Cp)TiCl2 was dissolved in 20 mL of toluene. Both catalyst solutions were added simultaneously to the silica slurry. After one hour of stirring, the slurry was filtered, yielding a clear filtrate. The solid component was washed twice with toluene, and once with heptane. The final product was dried in vacuo to 300 mTorr and stored under nitrogen until use.

Polymerization

[0159] The polymerization was the same as Example 1, except that 26.7 mg of Catalyst B was used for polymerization, producing 46.8 g of polymer.

[0160] As seen in FIG. 2, the GPC-FTIR plot shows that the polymer is bimodal with most of comonomer incorporation in the high molecular weight fraction.

example 3

Preparation of Catalyst C

[0161] In a glovebox, 2.92 grams of silica-supported MAO prepared above was slurried in 30 mL of toluene. Separately, 63.0 mg of catalyst component 1 was dissolved in 25 mL of toluene, and 13.3 mg of (tBU3PN)(C6F5)(n-Bu)CpTiCl2 was dissolved in 10 mL of toluene. Both catalyst solutions were added simultaneously to the silica slurry. After one hour of stirring, the slurry was filtered, yielding a clear filtrate. The solid component was washed twice with toluene, and once with heptane. The final product was dried in vacuo to 300 mTorr (40 102 Pa) and stored under nitrogen until use.

Polymerization

[0162] The polymerization was the same as Example 1, except that 20.9 mg of Catalyst C was used for polymerization, producing 45.8 g of polymer

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Abstract

Bimodal polyolefins having a reverse or partial reversed comonomer incorporation may be prepared in the presence of a dual catalyst on the same support wherein each catalyst has a different response to temperature, ethylene partial pressures, partial pressure of non-polymerizable hydrocarbons present in the reaction mixture and hydrogen partial pressure.

Description

FIELD OF THE INVENTION [0001] The present invention relates to a dual catalyst system on the same support. BACKGROUND OF THE INVENTION [0002] The original single site catalysts of the mid 1980's, such as metallocene catalysts, produced resin having a narrow polydispersity (Mw / Mn) typically in the range from about 2.5 to 3.5. Early on it was recognized that either blending such resins or the use of different metallocene catalysts in the same reactor could produce bimodal resins, each component having a narrow polydispersity and the blend having a broader polydispersity. It was felt such resins would provide a good balance of processability and physical properties such as resin toughness. There are an increasing number of patents and applications in this field. [0003] U.S. Pat. No. 4,530,914 issued Jul. 23, 1985 to Ewen et al., assigned to EXXON Research & Engineering Co. teaches the use in the same reactor of two metallocene catalysts each having different propagation and termination...

Claims

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Application Information

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IPC IPC(8): C08F4/02
CPCC07F7/006C07F17/00C08F4/65912C08F4/65916C08F4/6592C08F10/00C08F210/16C08F2410/04C08F4/65904C08F210/14C08F2500/05C08F4/64048C07F7/003
Inventor HOANG, PETER PHUNG MINHBAAR, CLIFF ROBERTZORICAK, PETERBAXTER, GAIL
Owner NOVA CHEM (INT) SA
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