Method for preparing 1-ethene under ethene oligomerizating catalyst system

A technology for ethylene oligomerization and catalysts, applied in chemical instruments and methods, organic chemistry, hydrocarbons, etc., can solve problems such as uneven mass and heat transfer, high local temperature, and the influence of complex catalysts on the catalytic effect, and achieve Good heat transfer effect and uniform mixing effect

Inactive Publication Date: 2004-04-21
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But still can not meet the requirements, people hope to further improve the performance of the catalyst, in order to improve the catalytic activity
[0005] Above ethylene oligomerization method all lays particular emphasis on the research to catalyst, although WO 99 / 19380 has carried out research to ethylene oligomerization method, similar with other patents, reaction is carried out in common autoclave basically, and thereby Problems with uneven mass and heat transfer
Since the reaction is a strong exothermic reaction, and the heat release rate is faster at the initial stage of the reaction, the local temperature is often too high due to the slow heat transfer rate, causing part of the catalyst to be deactivated, which affects the efficiency of the catalyst; and because in this reaction The mass transfer rate in the kettle is slow, which affects the catalytic effect of the complex catalyst, reduces the catalytic activity, and often takes a long reaction time, resulting in increased energy consumption

Method used

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  • Method for preparing 1-ethene under ethene oligomerizating catalyst system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] In the reactor (6) with the agitator (7) driven by the motor (5), a distributor (8) of stainless steel pipes with evenly distributed apertures is installed on the wall below the agitator. The ratio of the small hole diameter of the distributor to the diameter of the stainless steel pipe is 50%. The distributor is connected to the premixer (4). The premixer is composed of two stainless steel pipes. filler. The feed port of the premixer is connected with the solvent (2) and the raw material ethylene (1) tank, and the raw material ethylene (1) tank is directly connected with the top of the reactor, and the overflow tank (9) connected with the separation device (10) is connected with the reaction tank. The discharge port in the middle of the device is connected, and the catalyst inlet (3) is arranged between the distributor and the premixer.

[0031] After the assembled reactor was cleaned with cyclohexane, it was vacuum-dried at 100°C for 1 hour, cooled to room temperatur...

Embodiment 2-7

[0033] The process conditions and results are shown in Table 1.

[0034] Reality

[0035] Catalyst a

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PUM

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Abstract

A process for preparing 1-hexene under existance of ethylene oligonerizing catalyst includes such steps as premixing part of ethylene gas with solvent, mixing with the components in catalyst system, including chromic compound, pyrrol derivative, alkylaluminium and improver, loading in reactor via gas distributor, directly loading the rest of ethylene gas in reactor, discharging the resultant liquid, adding catalysis stopping agent, and separating. Its advantages are high selectivity of 1-hexene and high catalytic activity.

Description

technical field [0001] The present invention relates to a method for preparing 1-hexene in the presence of an ethylene oligomerization catalyst system. Background technique [0002] EP 0608447A1 reports a chromium-based catalyst composition as a catalyst for ethylene oligomerization and / or copolymerization, wherein a chromium-containing compound is used as one of the components of the catalyst composition; pyrrole compound is used as a chromium-based catalyst combination The second component of the material; a Lewis acid and / or metal alkyl compound is used as the third component of the catalyst composition as an activator; it is also pointed out that a halogen can also be selected in the catalyst system As the fourth component of the catalyst composition, the halogen source can be either an inorganic halide or many types of organic halides. The catalyst has a higher selectivity to 1-hexene, but its catalytic activity not tall. [0003] Sn(OSO 2 f 3 ) 2 The compound repl...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C2/08C07C2/26C07C11/107
CPCY02P20/52
Inventor 王刚吴林美王斯晗曲家波张宝军李玉龙袁宗胜胡凯文刘龙陈谦韩雪梅李建忠王桂芝杨玉和李洪涛王路海马建英赵景红
Owner PETROCHINA CO LTD
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