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Spherical mesoporous material for supported metallocene catalyst and manufacturing method thereof

A technology of metallocene catalysts and mesoporous materials, applied in the field of metallocene-loaded spherical mesoporous materials, can solve the problems of low ethylene polymerization activity, affecting loading effect, and pore wall collapse

Active Publication Date: 2013-03-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The main reason for the low ethylene polymerization activity of the mesoporous material MCM-41 after loading the catalyst is that the thermal and hydrothermal stability of the pore wall structure of MCM-41 is poor, and the pore wall partially collapses during the loading process, which affects the loading. effect, so that it affects the catalytic activity

Method used

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  • Spherical mesoporous material for supported metallocene catalyst and manufacturing method thereof
  • Spherical mesoporous material for supported metallocene catalyst and manufacturing method thereof
  • Spherical mesoporous material for supported metallocene catalyst and manufacturing method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Preparation of Spherical Mesoporous Materials Supporting Cocatalyst Methylaluminoxane (MAO) and Metallocene Catalyst Precursor Bis(1-Methyl-3-butyl-cyclopentadienyl)Zirconium Dichloride

[0031] In step 1, 2.0 grams of F108 (Fuka's trade name is Synperonic □ Substance F108) with 5.24 g K 2 SO 4 Add to 60 grams of 2N (2N) hydrochloric acid solution, stir at 38°C until F108 is completely dissolved;

[0032] In the second step, add 4.2 grams of ethyl orthosilicate to the above solution, stir at 38°C for 15 minutes, and stand at 38°C for 24 hours;

[0033] In the third step, the obtained solution was transferred to a polytetrafluoroethylene-lined reactor and crystallized at 100°C for 24 hours;

[0034] Step 4, obtain the original powder mesoporous material after adding 100 grams of deionized water to dilute, filter, wash and dry;

[0035] Step 5, wash the original powder mesoporous material with ethanol under reflux conditions for 24 hours, remove the template agent, an...

Embodiment 2

[0040] The application method of the spherical mesoporous material supporting cocatalyst methylaluminoxane (MAO) and main catalyst bis(1-methyl-3-butyl-cyclopentadienyl) zirconium dichloride in polyolefin.

[0041] Homopolymerization of ethylene

[0042] In a 2-liter stainless steel autoclave, replace three times with nitrogen and ethylene respectively, then add 200 milliliters of hexane solvent, raise the temperature of the kettle to 80 ° C, then add the remaining 800 milliliters of hexane solvent, with the addition of hexane, Add 2 ml of 1 mol / L triethylaluminum (TEA) hexane solution, then add 139 mg of FDU-MB, raise and maintain the pressure to 1.0 MPa, and react at 80°C for 1 hour. After the polymerization reaction finishes, collect polyethylene particle powder, weigh 139 grams, the efficient of catalyst is 876g PE / gcat h (26000000g PE / (mol Zr h)), bulk density (BD) is 0.255g / ml, Melt index: MI 2.16 = 0.016 g / 10 min.

Embodiment 3

[0044] Ethylene copolymerization

[0045] In a 2-liter stainless steel autoclave, replace three times with nitrogen and ethylene respectively, then add 200 milliliters of hexane solvent, raise the temperature of the kettle to 80 ° C, then add the remaining 800 milliliters of hexane solvent, with the addition of hexane, Add 2 ml of 1 mol / L triethylaluminum (TEA) hexane solution and 10 ml of hexene, then add 121 mg of FDU-MB, raise and maintain the pressure to 1.0 MPa, and react at 80°C for 1 hour. After the polymerization reaction was finished, the polyethylene particle powder was collected and weighed to obtain 139 grams. The efficiency of the catalyst was 952gPE / gcat h (28000000gPE / (mol Zr h)), and the bulk density (BD) was 0.176g / ml. Index: MI 2.16 = 0.176 g / 10 min.

[0046] figure 1 It is the XRD structure comparison chart of spherical mesoporous materials FDU and FDU-MB. Figure (1)a is the XRD spectrum of the spherical mesoporous material FDU, and Figure (1)b is the XR...

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Abstract

The invention relates to a spherical mesoporous material for a supported metallocene catalyst (Bis (1-methyl-3-butylcyclopentadienyl) zirconium dichloride). The spherical mesoporous material is a spherical mesoporous material with grain size ranging from 3 micrometers to 20 micrometers; a cocatalyst (methylaluminoxane (MAO)) and a metallocene catalyst precursor (Bis (1-methyl-3-butylcyclopentadienyl) zirconium dichloride) are supported on the outer surface and / or the inner hole wall of the spherical mesoporous material, so as to obtain a catalyst applicable to olefin polymerization; and the activity during the vinyl polymerization is far higher than that of the commonly-used supported and catalyzed mesoporous material MCM-41 reported in the literature.

Description

technical field [0001] The invention relates to a metallocene-loaded spherical mesoporous material, which belongs to the fields of catalytic synthesis and olefin polymerization. Background technique [0002] The development and application of metallocene catalysts is another major breakthrough in the field of olefin polymerization catalysts after the traditional Ziegler-Natta catalysts, especially in the 1980s, Kaminsky and Sinn et al. (Angew.Chem., 1980,19,390; Adv. .Organoment.Chem., 1980, 18, 99.) developed a high-efficiency cocatalyst methylaluminoxane (MAO), making the research on metallocene catalysts enter a stage of rapid development. Due to the large amount of MAO required for the homogeneous metallocene catalyst to achieve high activity, the production cost is high, and the obtained polymer has no particle shape, it cannot be used in the widely used slurry method or gas phase polymerization process, an effective solution to the above problems The way is to load th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/22C08F4/6592C08F4/02C08G65/336C08F10/02
CPCY02P20/52
Inventor 亢宇谢伦嘉邱波王彦强赵思源邓晓音郑刚刘长城
Owner CHINA PETROLEUM & CHEM CORP