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Catalyst for ethylene polymerization or copolymerization and its prepn and application

An ethylene polymerization and catalyst technology, which is applied to the catalyst, preparation and application fields for ethylene polymerization or copolymerization, can solve the problems of toxicity, long heating time, and prolong the preparation period, and achieves improved polymerization activity, reduced pollution, and reduced effect of the process

Active Publication Date: 2005-12-14
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 present invention provides catalyst component for ethylene polymerization or copolymerization and its preparation process. The catalyst is homogeneous solution prepared through dissolving magnesium halide in organic epoxy compound or organic phosphorus compound and adding electron donor compound. The present invention has separation assistant of non-toxic inorganic carbon containing solid to result in high catalytic performance, and the separation assistant is not soluble and swollen, needs no dissolving step, and may be used as the nucleartor for catalyst microcrystal growth to control the shape of catalyst. The present invention is superior to available technology, which has long temperature raising time, long catalyst preparing period, hard production operation and other demerits.

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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IPC IPC(8): C08F10/02
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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