Unlock instant, AI-driven research and patent intelligence for your innovation.

Catalyst component for olefin polymerization, preparation method of catalyst component, catalyst, method for preparing ultra-high molecular weight polyolefin and application of catalyst component

An olefin polymerization and catalyst technology, applied in the field of olefin polymerization catalysts, can solve the problems of inability to prepare ultra-high molecular weight polyethylene powder and the like

Pending Publication Date: 2022-05-13
CHINA PETROLEUM & CHEM CORP +1
View PDF10 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the above-mentioned spherical / ellipsoidal N-type polyethylene catalyst cannot prepare ultra-high molecular weight polyethylene powder with a viscosity-average molecular weight higher than 5 million

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Catalyst component for olefin polymerization, preparation method of catalyst component, catalyst, method for preparing ultra-high molecular weight polyolefin and application of catalyst component
  • Catalyst component for olefin polymerization, preparation method of catalyst component, catalyst, method for preparing ultra-high molecular weight polyolefin and application of catalyst component
  • Catalyst component for olefin polymerization, preparation method of catalyst component, catalyst, method for preparing ultra-high molecular weight polyolefin and application of catalyst component

Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0087] According to the second aspect of the present invention, the present invention provides the above-mentioned preparation method for the catalyst component of olefin polymerization, and this preparation method comprises the following steps:

[0088] S1, dissolving magnesium halide in a solvent system containing an organic epoxy compound and an organic phosphorus compound to form a uniform solution;

[0089] S2, reacting the solution obtained in step S1 with an organic acid anhydride compound and an acetate compound, then contacting with a titanium compound, and then raising the temperature to precipitate solid particles containing magnesium / titanium;

[0090] S3, adding electron donor a and electron donor b to the system obtained in step S2, and then treating at a constant temperature to obtain a mixture;

[0091] S4, removing unreacted substances and solvents from the mixture obtained in step S3, and washing to obtain a solid catalyst component.

[0092] Preferably, in ...

Embodiment 1

[0115] (1) Preparation of catalyst components

[0116] Add 4.8 grams of magnesium chloride, 90 mL of toluene, 5.0 mL of epichlorohydrin, and 15.0 mL of tri-n-butyl phosphate into the reaction kettle, and react for 2 hours at a stirring speed of 450 rpm and a temperature of 60 ° C. Add 1.1 g of o-phthalic acid Diformic anhydride and 0.7 mL of ethyl acetate were kept at constant temperature for 1 hour, then cooled to -40°C, 70 mL of titanium tetrachloride was added dropwise, the temperature was gradually raised to 90°C, and the temperature was kept at constant temperature for 1 hour. 1 mL of 2,2-dimethyl-1,3-diethoxy-propane and 0.2 g of compound A were added, and the temperature was maintained for 1 hour. The mother liquor was filtered off, washed several times with inert diluent toluene and organic solvent hexane, and then dried to obtain a solid catalyst component with good fluidity.

[0117] (2) Polymerization reaction

[0118] A stainless steel reaction kettle with a volu...

Embodiment 2

[0121] (1) Preparation of catalyst components

[0122] Add 4.8 grams of magnesium chloride, 90 mL of toluene, 5.0 mL of epichlorohydrin, and 15.0 mL of tri-n-butyl phosphate into the reaction kettle, and react for 2 hours at a stirring speed of 450 rpm and a temperature of 60 ° C. Add 1.1 g of o-phthalic acid Diformic anhydride and 0.7 mL of ethyl acetate were kept at constant temperature for 1 hour, then cooled to -40°C, 70 mL of titanium tetrachloride was added dropwise, the temperature was gradually raised to 90°C, and the temperature was kept at constant temperature for 1 hour. 1 mL of 1-ethoxy-3-methoxy-propane and 0.15 g of compound B were added and the temperature was continued for 1 hour. The mother liquor was filtered off, washed several times with inert diluent toluene and organic solvent hexane, and then dried to obtain a solid catalyst component with good fluidity.

[0123] (2) Polymerization reaction: with embodiment 1, polymerization result is shown in Table 1. ...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
Bulk densityaaaaaaaaaa
Login to View More

Abstract

The invention belongs to the technical field of olefin polymerization catalysts, and discloses a catalyst component for olefin polymerization, a preparation method of the catalyst component, a catalyst, a method for preparing ultra-high molecular weight polyolefin and application of the catalyst component. The catalyst component comprises a magnesium compound, an organic anhydride compound, an acetate compound, a titanium-containing compound, and a reaction product of an electron donor a and an electron donor b, the electron donor a is selected from at least one of compounds represented by a general formula (I) and a general formula (II), and the electron donor b is selected from at least one of compounds represented by a general formula (III) and a general formula (IV). The organic anhydride compound, the acetate compound, the electron donor a and the electron donor b are introduced into an N-type polyolefin catalyst preparation system to serve as compound electron donors, the spherical / ellipsoidal ultra-high molecular weight polyolefin with the viscosity average molecular weight larger than 7,000,000 can be obtained through olefin polymerization, and the spherical / ellipsoidal ultra-high molecular weight polyolefin is narrow in particle size distribution and high in stacking density.

Description

technical field [0001] The invention belongs to the technical field of olefin polymerization catalysts, and more specifically relates to a catalyst component for olefin polymerization and a preparation method thereof, a catalyst for olefin polymerization, a method for preparing ultra-high molecular weight polyolefins and its application. Background technique [0002] Ultra high molecular weight polyethylene (UHMWPE for short) is a special polyethylene variety with a molecular weight greater than 1.5 million. At present, most commercialized UHMWPE are prepared by Ziegler-Natta catalyst (referred to as Z-N catalyst), which has incomparable wear resistance, impact resistance, self-lubrication, corrosion resistance, low temperature resistance and sanitation of ordinary polyethylene and other engineering plastics. Non-toxic, not easy to adhere, not easy to absorb water, low density and other comprehensive properties. [0003] The compression molding process is one of the main pr...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C08F10/00C08F110/02C08F4/649
CPCC08F10/00C08F110/02C08F4/6494C08F2500/01C08F2500/18
Inventor 黄庭孙竹芳俸艳芸苟清强谢伦嘉郭子芳李颖杨红旭贺国强黄廷杰王毅马冬曹昌文梁云
Owner CHINA PETROLEUM & CHEM CORP