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Catalyst for ethylene and alpha-olefin copolymerization and preparation method thereof

A technology of olefin copolymerization and catalyst, which is applied in the field of olefin polymerization catalysts, can solve the problems of not realizing the copolymerization of ethylene and 1-hexene, uneven distribution of 1-hexene, and difficult separation of catalyst solids, etc., and achieves low cost and good shape , the effect of convenient operation

Active Publication Date: 2014-12-24
BC P INC CHINA NAT PETROLEUM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The method of ethylene copolymerization disclosed in CN1229092A is to dissolve magnesium chloride in organic epoxy compounds, organic phosphorus compounds and then add electron donors to form a uniform solution, and then react with at least one precipitation aid and transition metal titanium halides and derivatives thereof and obtain; the catalyst catalyzes ethylene and 1-hexene copolymerization activity high, and the 1-hexene insertion rate in the copolymer is higher, but the mother liquor of this catalytic system is more viscous in the preparation process, and it is difficult to separate the catalyst solid from the mother liquor, and the copolymerization Uneven distribution of 1-hexene in the
CN1194993A discloses a kind of catalyst that is used for ethylene slurry polymerization, and it is dissolved in the homogeneous solution of organic epoxy compound, organic phosphorus compound and inert solvent by magnesium chloride, then adds electron donor, a kind of co-diluent and transition metal titanium prepared from the chloride of ethylene, the catalyst can also be used for the copolymerization of ethylene and α-olefin, but there is no example of the copolymerization of ethylene and 1-hexene to form LLDPE

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  • Catalyst for ethylene and alpha-olefin copolymerization and preparation method thereof

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Experimental program
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Effect test

Embodiment 1

[0039] This embodiment provides a catalyst for the copolymerization of ethylene and α-olefin, which is prepared by the following steps:

[0040] (1) Add 2 grams of anhydrous magnesium chloride, 60 milliliters of hexane and 6.5 milliliters of isobutanol into a three-necked flask replaced by argon, stir and heat to 70° C., then react for 3 hours to obtain a suspension;

[0041] (2) Add 0.18 ml of tributyl phosphate to the suspension, stir and react at 70°C for 1 hour, then add 0.6 ml of tetraethoxysilane, and stir and react at 70°C for 1 hour;

[0042] (3) Cool down to room temperature, slowly add 47 ml of titanium tetrachloride dropwise, the dropwise addition time is 90 minutes, gradually warm up to 70°C, the heating time is 2 hours, and then stir and react for 2 hours;

[0043] (4) Then press filter the supernatant, add 50 ml of n-hexane, heat up to 70°C, add 0.10 ml of tetraethoxysilane, stir for 1 hour, then add 0.12 ml of tributyl phosphate, stir for 1 hour ;

[0044] (5)...

Embodiment 2

[0048] This embodiment provides a catalyst for the copolymerization of ethylene and α-olefin, the preparation method of which is the same as that of Example 1, except that:

[0049] 12 milliliters of isobutanol consumptions in the step (1).

[0050] In step (2), diisobutyl phthalate is used to replace tributyl phosphate, and the consumption is 0.06 milliliters; tetraethoxysilane is replaced with isobutyltrimethoxysilane, and the consumption is 0.17 milliliters.

[0051] The amount of titanium tetrachloride used in step (3) was 83 milliliters, the time for dropping was 2 hours, and the reaction time was 1 hour.

[0052] In step (4), replace tetraethoxysilane with isobutyltrimethoxysilane, and its consumption is 0.03 milliliters, and the reaction time is 2 hours; Replace tributyl phosphate with diisobutyl phthalate, and its consumption is 0.22 milliliters , the reaction time is 2 hours.

[0053] In the step (5), the consumption of titanium tetrachloride is 42 milliliters, and ...

Embodiment 3

[0056] This embodiment provides a catalyst for the copolymerization of ethylene and α-olefin, the preparation method of which is the same as that of Example 1, except that:

[0057] In the step (1), the consumption of isobutanol is 4.30 milliliters.

[0058] In step (2), diethyl succinate was used to replace tributyl phosphate, and the amount was 0.30 ml; 3-chloropropyltriethoxysilane was used to replace tetraethoxysilane, and the amount was 0.21 ml.

[0059] In the step (3), the amount of titanium tetrachloride is 31 milliliters, the time for dropping is 2 hours, and the reaction time is 1 hour.

[0060] In step (4), replace tetraethoxysilane with 3-chloropropyltriethoxysilane, and its consumption is 0.04 milliliters, and the reaction time is 2 hours; Replace tributyl phosphate with diethyl succinate, and its consumption is 0.15 ml.

[0061] 15.50 milliliters of titanium tetrachloride consumptions in the step (5).

[0062] The titanium content of the prepared solid catalys...

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Abstract

The invention relates to a catalyst for ethylene and alpha-olefin copolymerization and a preparation method thereof. The catalyst comprises a magnesium compound, a titanium compound, an electron donor I and an electron donor II. The electron donor I is an ester compound. The electron donor II is a siloxane compound. The preparation method of the catalyst includes that the magnesium compound is dissolved in a hydrocarbon solvent and an alcohol solvent, and reacts for 2-4 hours under the temperature of 70-90 DEG C; the electron donor I is added and reacts for 0.5-2 hours, and then the electron donor II is added and reacts for 0.5-2 hours; the titanium compound is added dropwisely under the room temperature, and reactions undergo 1-3 hours under the temperature of 70-90 DEG C; the solvents are eliminated; the hydrocarbon solvent is added; after the electron donor II reacts for 1-2 hours, the electron donor I is added and reacts for 1-2 hours; the titanium compound is added and reacts for 1-3 hours; and filtering, washing and drying are carried out to produce the catalyst. According to the catalyst, the catalyst activity for the ethylene and the long-chain alpha-olefin copolymerization is high, so the inserting rate of the long-chain alpha-olefin of produced copolymer is high.

Description

technical field [0001] The present invention relates to a catalyst for the copolymerization of ethylene and alpha-olefins and a preparation method thereof, in particular to an electron donor-modified Ziegler-Natta catalyst for the copolymerization of ethylene and long-chain alpha-olefins and a preparation method thereof, The invention belongs to the field of olefin polymerization catalysts. Background technique [0002] Linear low-density polyethylene (LLDPE) is a copolymer of ethylene and α-olefins (ethylene and 1-butene, ethylene and 4-methyl-1-pentene) successfully developed in the 1970s, and its molecules have a linear structure , the density is 0.91-0.94g / cm 3 , which is similar to LDPE produced by high-pressure method, is called the third generation product of polyethylene. After the introduction of α-olefin monomers into the polymer, the resulting macromolecules contain a considerable amount of branched chains. These short-chained and long-chained branches will affe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F210/16C08F4/649C08F4/646C08F4/658
Inventor 米普科许胜李贺熊玉洁张志高孔晓娟朱玉玲李浩米怡璇陈建吴志祥任迎春冯才华何阳许鹄飞
Owner BC P INC CHINA NAT PETROLEUM CORP