Vanadium catalysis system for combined polymerization of ethylene, propylene, and diolefin, and application

A catalytic system and diene technology, applied in the field of vanadium catalytic system, can solve the problems of difficulty in post-processing of rubber, secondary pollution of polymers, insufficient activity, etc., and achieve lower production catalyst cost, improved ternary copolymerization activity, and easy removal. Effect

Inactive Publication Date: 2007-12-26
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But at the same time, the above-mentioned vanadium compounds have the disadvantage that the activity is not high enough in the process of ternary copolymerization of ethylene, propylene and diene
For this reason, in order to increase the yield, a large amount of main catalyst must be added, which will greatly increase the vanadium content in the polymer, which will cause difficulties in the post-treatment of rubber, and because the catalyst residue content in the separated copolymer is high, so Its use is subject to certain restrictions
In addition, most of these vanadium compounds themselves are sensitive to air, water, acid, alkali, etc., and there are many changes in production, storage and use.
[0003] Japanese patent 1973-71492 uses vanadium oxychloride as the main catalyst, and greatly improves the catalytic efficiency of V-Al catalyst by adding anthraquinone oxides as activators, but the compatibility of anthraquinone oxides is not good; USP4181790 With vanadium compound as the main catalyst and 2,3,4,4-tetrachloro-3-butenoic acid ester as the activator, the activity of ethylene-propylene copolymerization is improved and the gel is reduced, but the main catalyst used is sensitive to air , water sensitive, inconvenient to use; CN85108910 uses vanadium oxychloride as the main catalyst, uses alkylaluminum chloride as a co-catalyst, and simultaneously adds silicon tetrachloride or trichlorofluoromethane to carry out the copolymerization of ethylene and α-olefins, which improves the Copolymerization activity, but the silicon tetrachloride used is easy to cause secondary pollution to the polymer; CN1099395 uses vanadium trichloride as the main catalyst, diethylaluminum chloride as the cocatalyst, and ethyl trichloroacetate as the activator Ethylene-propylene copolymerization, the polymerization activity is obviously improved; US4598132 discloses a vanadium catalyst system containing an ester-based polymer, and the synthesis of EPDM with the system formed by this catalyst and aluminum alkyl only improves the gel problem, and the catalytic efficiency does not increase significantly ; US5122493 mainly solves the problem of molecular weight distribution, by using branched dihydroxyl hydrocarbons, the polymer molecular weight is formed into a narrow distribution, VO (acac) 2 Although the catalyst is insensitive to air, water, etc., the catalyst is insoluble in inert solvents (such as hexane), and it is difficult to use when inert solvents such as hexane are used as polymerization solvents

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Prepare ethylene, propylene, and hydrogen through a mixing device according to 1: (1.5-4.5): (0.15-0.45), and then fully mix them evenly through a circulating compressor. The polymerization is carried out in a 5L polymerization kettle, and the 5L polymerization kettle Perform anhydrous and oxygen-free treatment under vacuum for 1 hour, the inert gas used is high-purity nitrogen, then add 2000ml of dry hexane (water content≤10ppm) to it, which contains 10ml of norbornene (ENB), and start the cycle compression machine, feed the mixed gas into the polymerization kettle to make the mixed gas dissolved in hexane reach saturation, and then add 10ml (0.4mmol) of bis (diisooctyl phosphate) vanadyl (V-P 204 ) of hexane solution, 10ml of sesquialuminum, so that the Al / V ratio is 20 / 1, and finally add activator ethyl trichloroacetate (ETCA), so that ETCA / V is 5 / 1, and the polymerization temperature is 30°C. The pressure is 0.5MPa, and the polymerization reaction time is 1 hour. Af...

Embodiment 2

[0038] Change the add-on of ethyl trichloroacetate (ETCA), make ETCA / V be 3 / 1, other conditions are identical with embodiment 1, make Al / V ratio be 10 / 1, get dry glue 118g, polymerization catalytic efficiency 5784g glue / g vanadium. Through gel permeation chromatography analysis, the number average relative molecular mass is 40,000, the relative molecular mass distribution is 2.7, and the propylene content is 40%.

Embodiment 3

[0040] Other conditions are identical with embodiment 1, change the add-on of ethyl trichloroacetate (ETCA), make ETCA / V be 8 / 1, make Al / V ratio be 40 / 1, get dry glue 120g, polymerization catalytic efficiency 5882g glue / g vanadium. Through gel permeation chromatography analysis, the number average relative molecular mass is 31,000, the relative molecular mass distribution is 3.0, and the propylene content is 39%.

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PUM

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Abstract

This invention relates to a vanadium catalyst system for preparing rubber elastomers. This invention introduces an activation promoter into the traditional vanadium catalyst system to form a new active catalyst system, which is composed of vanadium compound, cocatalyst and activation promoter. The vanadium catalyst system can be used in ternary polymerization of ethylene, propylene and diene, and has such advantages as high catalytic activity, low consumption and easy removal of vanadium during post treatment.

Description

technical field [0001] The invention relates to a vanadium catalyst system for preparing rubber elastic body by copolymerization of ethylene, propylene and diene and its application. Background technique [0002] It is a well-known method in the industry that vanadium system Ziegler-Natta catalysts are used for terpolymerization of ethylene, propylene and dienes to prepare rubber elastomers. A representative main catalyst is VOCl 3 ,, VCl 3 ,, VCl 4 ,, V(acac) 3 etc., the other component is a Group I-III organometallic compound (such as an aluminum alkyl). Such V-alkylaluminum systems have played a major role in the synthesis of ethylene / propylene / ethylene norbornene terpolymer (EPDM) elastomers. But at the same time, the above-mentioned vanadium compound has the disadvantage that the activity is not high enough in the terpolymerization process of ethylene, propylene and diene. For this reason, in order to increase the yield, a large amount of main catalyst must be add...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F210/18C08F4/68
Inventor 王笑海邹向阳赵秀红王萍佟瑶彩吴运良
Owner PETROCHINA CO LTD
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