Catalytic system for preparation of wide-distribution polyolefin, and application of catalytic system

A catalytic system and polyolefin technology, which are applied in the field of catalytic systems for olefin polymerization and the preparation of catalytic systems for wide-distribution polyolefins, can solve the problems of low catalytic activity, narrow relative molecular mass distribution of polymers, and difficult synthesis.

Active Publication Date: 2017-08-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Each of these internal electron donors has certain defects in practical industrial applications: as the catalytic activity of catalysts using aromatic diester compounds is low, the relative molecular mass distribution of the resulting polymer is moderate; the catalysts of glycol ester compounds The sensitivity to hydrogen adjustment is not as good as that of catalysts using diether compounds, and the relative molecular mass distribution of the obtained polymers is generally not as good as the evaluation results of catalysts using 2,3-dihydrocarbyl succinate compounds; although catalysts using diether compounds High catalytic activity and good hydrogen tuning sensitivity, but the relative molecular mass distribution of the obtained polymer is narrow; although the relative molecular mass distribution of 2,3-dihydrocarbyl succinate compounds is wide, there are internal electron donor compounds The synthesis process is difficult in industrial application; use the C with ω-cyano group 2 ~C 5 Monobasic acid ester

Method used

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  • Catalytic system for preparation of wide-distribution polyolefin, and application of catalytic system
  • Catalytic system for preparation of wide-distribution polyolefin, and application of catalytic system
  • Catalytic system for preparation of wide-distribution polyolefin, and application of catalytic system

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preparation example Construction

[0063] The magnesium halide alcoholate of the general formula (3) in the present invention can be prepared by methods known in the industry, such as spray drying, spray cooling, high-pressure extrusion or high-speed stirring. The specific preparation method may include the following steps: in a closed container, the optional inert medium is heated to 100 ° C ~ 140 ° C, adding magnesium halide MgX 2 , Alcohol R 11 OH, after fully reacting, it forms a mixture containing molten magnesium halide alcoholate, which is quenched and formed by low-temperature inert medium after high shear, to form spherical magnesium halide alcoholate pellets. High-shear action can adopt conventional methods, such as high-speed stirring method (such as Chinese patent CN1330086), spraying method (such as US6020279) and high gravity rotating bed (such as CN1580136A) and emulsifier (CN1463990A) etc. The cooling medium can be an inert hydrocarbon solvent with a lower boiling point, such as pentane, hexane...

Embodiment 1

[0150] (1) Preparation of spherical catalyst solid components

[0151] Prepare spherical magnesium chloride alcoholate MgX with reference to the embodiment 1 method in Chinese patent CN1091748A 2 ·(R 11 Oh) m , where X=C1, R 11 =C 2 h 5 , m=2.4.

[0152] In a 300ml double-layer glass reaction bottle, add 100ml of titanium tetrachloride, cool to -20°C, add 8 grams of the above-mentioned spherical magnesium chloride alcoholate, heat up to 100°C, and add according to the Chinese invention patent application number during the heating process. 2,3-diisopropyl-2-cyanodiethyl succinate (ID1) 2.5mmol prepared by the method described in the patent application description of 200910077779.6, diisobutyl phthalate (ID2) 2.5mmol filter Remove liquid, wash twice with titanium tetrachloride, wash four times with hexane, and obtain spherical catalyst solid component after vacuum drying.

[0153] (2) Propylene polymerization

[0154] The 5L autoclave is heated and evacuated, air and wat...

Embodiment 2

[0156] The internal electron donor is 2,3-diisopropyl-2-cyanosuccinate (ID1) 4mmol, diisobutyl phthalate (ID2) 1mmol, and the external electron donor is diisopropyl Basepiperazine dimethoxysilane (ED1), the amount of hydrogenation is 300mmol, and others are the same as in Example 1. All test results are shown in Table 1.

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Abstract

The invention relates to a catalytic system for preparation of wide-distribution polyolefin, and application of the catalytic system. The catalytic system comprises a solid catalyst component (A), a cocatalyst (B) and a first external electron donor (ED1), wherein the component (A) is a magnesium halide loaded Ti solid component and contains a composite internal electron donor (ID); the first external electron donor (ED1) is selected from one or more of compounds as shown in a general formula (1), (the formula is as shown in the description); and the R1 is selected from C1-C6 alkyl, C3-C8 naphthenic base, C6-C14 aryl or C6-C14 ceteroary, R2 is selected the formulas as shown in the description, and R3 is selected from OR1, R2, C1-C6 alkyl and C3-C8 naphthenic base. When being applied to olefin polymerization, the catalytic system has various advantages: catalytic activity and hydrogen sensitivity are high; and the polymerization product is high in isotactic index, wide in molecular weight distribution and high in weight-average molecular weight.

Description

technical field [0001] The invention relates to a catalytic system for olefin polymerization, in particular to a catalytic system for preparing wide-distributed polyolefin and its application, and belongs to the field of catalysts. Background technique [0002] Ziegler-Natta catalyst systems for olefin polymerization are known in the art as catalyst systems for olefin polymerization. Generally, the catalytic system includes a main catalyst, an internal electron donor, a co-catalyst and an external electron donor. [0003] Among them, the main catalyst generally adopts transition metal halides, oxyhalides, acetylacetonate compounds, etc., and the commonly used transition metal compounds are titanium and vanadium. The co-catalyst generally adopts metal-organic compounds containing elements of group IA-IIIA of the periodic system, mainly aluminum alkyls or halides of aluminum alkyls. [0004] Second, internal electron donors are indispensable as components in catalytic system...

Claims

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Application Information

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IPC IPC(8): C08F10/00C08F4/649C08F4/646C08F110/06
CPCC08F10/00C08F110/06C08F4/649C08F4/6465
Inventor 李化毅马良兴王笃金张赪李倩赵唤群
Owner CHINA PETROLEUM & CHEM CORP
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