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Catalyst component for olefin polymerization and use thereof and catalyst for olefin polymerization and use thereof and olefin polymerization method

An olefin polymerization and catalyst technology, applied in the field of catalyst components, can solve the problems of carrier adhesion, unstable preparation process, poor carrier molding effect, etc., and achieve the effect of increasing bulk density

Active Publication Date: 2016-05-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the catalyst carrier prepared by this method has the disadvantages of unstable preparation process, easy carrier adhesion, and poor carrier molding effect.

Method used

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  • Catalyst component for olefin polymerization and use thereof and catalyst for olefin polymerization and use thereof and olefin polymerization method
  • Catalyst component for olefin polymerization and use thereof and catalyst for olefin polymerization and use thereof and olefin polymerization method
  • Catalyst component for olefin polymerization and use thereof and catalyst for olefin polymerization and use thereof and olefin polymerization method

Examples

Experimental program
Comparison scheme
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Embodiment approach

[0047] According to a preferred embodiment of the present invention, the average particle diameter of the olefin polymerization catalyst carrier may be 10-100 microns, preferably 40-60 microns; the particle size distribution is less than 1.2, preferably 0.6-0.8. In this preferred embodiment, the catalyst prepared from the olefin polymerization catalyst support is capable of yielding olefin polymers with higher bulk density. In the present invention, the average particle diameter and particle size distribution of the olefin polymerization catalyst carrier can be measured by using a MasterSizer 2000 laser particle size analyzer (manufactured by Malvern Instruments Ltd).

[0048] According to the present invention, the water contained in the carrier of the olefin polymerization catalyst comes from the trace amount of water carried by the synthesis raw materials and the reaction medium.

[0049]In the present invention, the titanium compound may be various titanium compounds conve...

preparation example 1

[0086] This preparation example is used to illustrate the olefin polymerization catalyst carrier provided by the present invention and its preparation method.

[0087] In a 1.6L reactor, add 200mL white oil, 8.0g (0.08mol) magnesium chloride, 3g (0.01mol) octadecyl alcohol, 95mL (1.6mol) ethanol, 9.8mL (0.08mol) 2,2-dimethoxy base propane, heated to 90°C with stirring. After reacting at a constant temperature for 1 hour, the mixture was stirred at a low speed (400 rpm) to disperse for 30 minutes for emulsification. Add 35 mL (0.45 mol) of epichlorohydrin to the emulsified product above, react for half an hour and press filter for 9 minutes. The press-filtered product was washed 5 times with hexane, and press-filtered after each wash. The total time of the press-filtering process was 20 minutes. Finally, the product was vacuum-dried to obtain the olefin polymerization catalyst carrier Z1.

[0088] The average particle diameter (D50) of the olefin polymerization catalyst carr...

preparation example 2

[0090] This preparation example is used to illustrate the olefin polymerization catalyst carrier provided by the present invention and its preparation method.

[0091] In a 1.6L reactor, add 300mL white oil, 8.0g (0.08mol) magnesium chloride, 10.8g (0.04mol) stearyl alcohol, 28mL (0.48mol) ethanol, 1mL (0.008mol) 2,2-dimethoxy base propane, heated to 100°C with stirring. After reacting at a constant temperature for 0.5 hour, the mixture was stirred at a low speed (800 rpm) to disperse for 30 minutes for emulsification. Add 12.5 mL (0.16 mol) of epichlorohydrin to the above emulsified product, react for 20 minutes, and press filter for 10 minutes. The press-filtered product was washed 5 times with hexane, and press-filtered after each wash. The total time of the press-filtering process was 25 minutes. Finally, the product was vacuum-dried to obtain the olefin polymerization catalyst carrier Z2.

[0092] The average particle diameter (D50) of the olefin polymerization catalys...

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Abstract

The invention provides a catalyst component used for olefin polymerization and applications thereof. The catalyst component comprises a product of a reaction of an olefin polymerization catalyst carrier with a titanium compound. The olefin polymerization catalyst carrier comprises magnesium halide having a general formula of MgXY, a compound having a general compound of ROH, a compound having a general formula of R'OH, a dialkoxy hydrocarbon compound and an ethylene oxide type compound. The invention also provides a catalyst used for olefin polymerization, applications thereof and an olefin polymerization method. The bulk density of the polymer obtained by polymerization is increased when the catalyst is used as the catalyst of the olefin polymerization reaction.

Description

technical field [0001] The present invention relates to a catalyst component for olefin polymerization, the application of the catalyst component for olefin polymerization in a catalyst for olefin polymerization, a catalyst for olefin polymerization, the catalyst for olefin polymerization Use of catalysts in olefin polymerization and olefin polymerization processes. Background technique [0002] It is well known that the performance of Ziegler-Natta catalyst supported by magnesium chloride alcoholate is significantly better than that of catalysts supported by other supports when it is used for the polymerization of olefins (especially propylene). Therefore, most of the catalysts currently used for olefin polymerization are prepared by loading titanium halide on magnesium chloride alcoholate. In order to obtain a spherical carrier, it can be prepared by methods such as spray drying, spray cooling, high-pressure extrusion, high-speed stirring, emulsifying machine method, and ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F10/00C08F4/02C08F4/649C08F4/646C08F4/654
Inventor 凌永泰夏先知刘月祥李威莅张纪贵谭扬彭人琪高富堂赵瑾高平乔素珍
Owner CHINA PETROLEUM & CHEM CORP