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Catalyst component and catalyst for olefin polymerization

A technology of olefin polymerization and solid catalyst, which is applied in the application of catalysts in olefin polymerization and the application field of olefin homopolymerization and copolymerization, and can solve the problems of low catalytic activity, difficulty in industrial application of internal electron donor compound synthesis process, polymer Narrow relative molecular mass distribution, etc.

Active Publication Date: 2011-08-10
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In industrial applications, these internal electron donors have certain defects in practical applications: for example, the catalytic activity of catalysts using aromatic diester compounds is lower than that of diether compounds; catalysts using diether compounds Although the catalytic activity is high and has good hydrogen tuning sensitivity, the relative molecular mass distribution of the resulting polymer is narrow; although the succinate ester compound of 2,3-dihydrocarbyl has a wide relative molecular mass distribution, there is this inner molecular mass distribution. Difficulties in industrial application of electron donor compound synthesis process; Patent CN1242780A uses C with ω-cyano group 2 ~C 5 Monobasic acid ester compounds are catalysts for internal electron donors, and there are also ω-cyano C 3 ~C 5 Difficulties in the synthesis of monobasic acid ester compounds, although C containing ω-cyano 2 Monobasic acid ester compounds (that is: cyanoacetate compounds containing substituents) are easier to synthesize, but compared with the catalysts of aromatic diester compounds, the C of ω-cyano 2 ~C 5 Monobasic acid ester compounds are less active catalysts for internal electron donors, and the resulting polymer is also poor in isotacticity, etc.

Method used

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  • Catalyst component and catalyst for olefin polymerization
  • Catalyst component and catalyst for olefin polymerization
  • Catalyst component and catalyst for olefin polymerization

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] (1) Preparation of catalyst solid components

[0058] In the reactor fully replaced by high-purity nitrogen, 4.8g of magnesium chloride, 95ml of toluene, 4ml of epichlorohydrin, and 12.5ml of tributyl phosphate (TBP) were sequentially added, and the temperature was raised to 50°C under stirring and maintained for 2.5 hours. After complete dissolution, 1.4 g of phthalic anhydride was added and maintained for 1 hour. Cool the solution to below -25°C and add TiCl dropwise within 1 hour 4 56ml, slowly warming up to 80°C, during the heating process, the solid matter is gradually precipitated, and the 2,3-diisopropyl-2-cyanobutanediol prepared according to the method described in the patent application specification of China Invention Patent Application No. 200910077779.6 is added Acetate diethyl ester 5mmol, maintain the temperature for 1 hour, after filtration, add toluene 70ml, wash twice to obtain a solid precipitate. Then add toluene 60ml, TiCl 4 40ml, heat up to 100°...

Embodiment 2

[0071] (1) The preparation of the catalyst solid component is the same as in Example 1, except that the 2,3-diisopropyl-2-cyano-succinic acid prepared by the method described in the patent application description of China Invention Patent Application No. 200910077779.6 - 1-isobutyl-4-ethyl ester (5 mmol) in place of diethyl 2,3-diisopropyl-2-cyanosuccinate (5 mmol).

[0072] (2) The propylene polymerization method is the same as that of Example 1, and the test results are shown in Table 1.

Embodiment 3

[0074] (1) preparation of catalyst solid component, with embodiment 2.

[0075] (2) Propylene polymerization

[0076] In a 5L autoclave, 5ml of a hexane solution of triethylaluminum (the concentration of triethylaluminum is 0.5mmol / ml), 1.25ml of cyclohexylmethyldimethoxysilane (CHMMS ) hexane solution (the concentration of CHMMS is 0.1mmol / ml), 10ml of anhydrous hexane and 10mg of the solid catalyst component obtained in Example 1 above. Close the autoclave, introduce 6 L of hydrogen gas (standard volume) and 2.3 L of liquid propylene, raise the temperature to 70° C., and polymerize for 1 hour. The test results are shown in Table 1.

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Abstract

The invention relates to a catalyst component and a catalyst for olefin polymerization, and application thereof in olefin homopolymerization and copolymerization. Alpha-cyanosuccinic acid ester compounds with a special structure or a composite donor system consisting of the alpha-cyanosuccinic acid ester compounds is used as an internal donor to synthesize the catalyst, the catalyst has higher catalytic activity during propylene polymerization, a polymerization product has high isotacticity and wide molecular weight distribution. The alpha-cyanosuccinic acid ester compounds are easier to prepare and more suitable for industrial production compared with the conventional 2,3-dialkyl succinic acid ester compounds.

Description

technical field [0001] The present invention relates to a catalyst component and catalyst for olefin polymerization, and its application in olefin homopolymerization and copolymerization. More specifically, it relates to a solid catalyst component containing a compound of general formula (I) as an internal electron donor, and the application of the catalyst containing this component in olefin polymerization. Background technique [0002] In this field, it is well known that Ziegler-Natta catalyst consists of at least two parts: the active component containing transition metal, also known as the main catalyst, the more transition metal compounds used in practice are titanium and vanadium, generally with carrier magnesium chloride Together to form a solid catalyst component; and a metal organic compound containing elements of Group I A to IIIA of the periodic system, also known as a co-catalyst, mainly an alkyl aluminum or an alkyl aluminum halide. In some cases, especially w...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F4/651C08F12/00C08F4/654C08F10/00C08F36/02C08F4/649C08F10/06
Inventor 谢伦嘉凌永泰田宇冯再兴赵思源胡青亢宇
Owner CHINA PETROLEUM & CHEM CORP
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