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Catalyst for ethylene polymerization or copolymerization and its preparation and application

An ethylene polymerization and catalyst technology, which is applied to the catalyst, preparation and application fields of ethylene polymerization or copolymerization, can solve the problems of long heating time, toxicity, difficulty in production and operation, etc. The effect of increasing the polymerization activity

Active Publication Date: 2006-11-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Compounds such as organic acid anhydrides, organic acids, ethers, ketones have all been used in the catalyst systems disclosed by CN85100997 and CN1229092 as the precipitation aids. and heating rate, especially when catalyst solid nuclei are formed, the control of heating rate is more necessary, and generally requires a longer heating time, so the use of this kind of precipitation aid prolongs the preparation period of catalyst accordingly It is more difficult, and the precipitation aids used are generally phthalic anhydride compounds, which are also toxic to the body, etc.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] In the high-purity N 2 In the fully replaced reactor, add 4.0g of anhydrous MgCl successively 2 , 50ml toluene, 2.0ml epichlorohydrin, 3.0ml tributyl phosphate, heated up to 50°C under stirring, and maintained for 15 minutes, added 6.0ml ethanol, continued to react for 15 minutes, then added 0.4g of activated carbon (through a 100-mesh sieve ), the solution was cooled to -5°C, and 20ml of titanium tetrachloride was dropped into it, then heated to 40°C, filtered, washed with hexane four times, and dried in vacuum to obtain a solid catalyst.

[0037] Ethylene polymerization: a stainless steel kettle with a volume of 2 liters is passed through H 2 After sufficient replacement, add 1000ml of hexane, 1.5ml of triethylaluminum (1mol / l hexane solution), and 5.8mg of the solid catalyst component prepared above, and heat up to 70°C for hydrogenation at 0.18MPa (gauge pressure) , and then feed ethylene to make the kettle reach 0.73MPa (gauge pressure), and polymerize for 2 hour...

Embodiment 2

[0039] With embodiment 1, only the gac add-on is changed into 0.20g (crossing 100 mesh sieves).

[0040] Ethylene polymerization: a stainless steel kettle with a volume of 2 liters is passed through H 2 After sufficient replacement, add 1000ml of hexane, 1.5ml of triethylaluminum (1mol / l hexane solution), and 5.5mg of the solid catalyst component prepared above, and heat up to 70°C for hydrogenation at 0.18MPa (gauge pressure) , and then feed ethylene to make the kettle reach 0.73MPa (gauge pressure), and polymerize for 2 hours at 80°C. The polymerization results are shown in Table 1.

Embodiment 3

[0042] With embodiment 1, only the gac add-on is changed into 0.10g (crossing 140 mesh sieves).

[0043] Ethylene polymerization: a stainless steel kettle with a volume of 2 liters is passed through H 2 After sufficient replacement, add 1000ml of hexane, 1.5ml of triethylaluminum (1mol / l hexane solution), and 5.0mg of the solid catalyst component prepared above, and heat up to 70°C for hydrogenation at 0.18MPa (gauge pressure) , and then feed ethylene to make the kettle reach 0.73MPa (gauge pressure), and polymerize for 2 hours at 80°C. The polymerization results are shown in Table 1.

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PUM

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Abstract

The invention provides a catalyst component for ethylene polymerization or copolymerization and a preparation method thereof. Wherein the catalyst is formed by dissolving magnesium halide in organic epoxy compound, organic phosphorus compound and adding electron donor compound to form a homogeneous solution. The present invention uses a non-toxic inorganic carbon-containing solid precipitation aid to make the catalyst suitable for ethylene polymerization or co-precipitation. Polymerization has comparable or better catalytic performance than the above-mentioned catalytic system. Since it is neither dissolved nor swelled, the dissolution reaction step of the precipitation aid is omitted. At the same time, this type of solid substance can also be used as a catalyst for microcrystal growth in the system. Therefore, the particle shape of the final catalyst can also be adjusted by selecting and controlling the particles of this type of solid material, which increases the means of regulating the particle shape of the catalyst and overcomes the long heating time and long catalyst preparation cycle of the existing technology , production operations are more difficult and other disadvantages, and to a certain extent reduce pollution.

Description

technical field [0001] The present invention relates to a catalyst component for ethylene polymerization or copolymerization, its preparation method, and its application in olefin polymerization or copolymerization. Background technique [0002] In the late 1970s, companies such as Mitsui Petrochemical Corporation of Japan and Monai of the United States successfully developed titanium-magnesium high-efficiency carrier catalysts with magnesium chloride as the carrier. Because the carrier was used to improve the utilization rate of the active center of the titanium atom, the catalytic activity was improved. It is much higher than conventional catalysts and simplifies the polymerization process, so the world's polyolefin industry has developed rapidly. Conventional methods for preparing highly active supported catalysts are generally co-grinding, grinding and impregnating, spraying carrier forming and high-speed stirring carrier forming, etc. The main disadvantage of the catal...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F10/02C08F4/645
Inventor 王毅孙怡菁金茂筑邢宝泉马冬朱宝兰张立伟
Owner CHINA PETROLEUM & CHEM CORP
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