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Method for preparing hexene through C4 disproportionation

A hexene and disproportionation technology, which is applied in the field of carbon four disproportionation to produce hexene, can solve the problem of low utilization rate of carbon four raw materials, and achieve the effect of improving utilization rate and good technical effect

Active Publication Date: 2015-05-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The technical problem to be solved by the present invention is the low utilization rate of carbon four raw materials existing in the prior art, and a new method for producing hexene by carbon four disproportionation is provided

Method used

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  • Method for preparing hexene through C4 disproportionation
  • Method for preparing hexene through C4 disproportionation
  • Method for preparing hexene through C4 disproportionation

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Experimental program
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Embodiment 1

[0023] according to figure 1 In the process flow shown, the extractant is a mixed solvent of nitrogen-formylmorpholine and methyl ethyl ketone, the weight ratio is 1:1; the catalyst in the isomerization reactor is 12%Ni / Al 2 o 3 , operating conditions: reaction temperature 50°C, reaction pressure 1.5MPa in absolute pressure, mass space velocity of C4 2h -1 ; The adsorbent in the impurity processor is BASF Selexsorb CD and COS, the weight ratio of the two is 2:1, and the disproportionation catalyst in the disproportionation reactor is 8%WO 3 / SiO 2 , the operating conditions are: reaction temperature 350°C, reaction pressure 3MPa in absolute pressure, mass space velocity of C4 2h -1 . The operating conditions of the extraction process are shown in Table 2, and the material balance of the reaction is shown in Table 3.

Embodiment 2~6

[0025] React by each condition and step of embodiment 1, just change different operating parameters, its reaction condition is listed in table 1, the operating condition of extraction process is as shown in table 2, and the mass balance of reaction is as shown in table 3.

[0026] Table 1

[0027]

[0028] Note: The data of isomerization catalyst and disproportionation catalyst are the mass percentage of active components.

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Abstract

The present invention relates to a method for preparing hexene through C4 disproportionation, wherein the problem of not high C4 utilization rate in the prior art is mainly solved with the present invention. According to the present invention, 1-butene is adopted as a raw material, the C4 raw material respectively be subjected to an extraction process and passes through an isomerization reactor to obtain a 1-butene-rich C4 olefin stream, and the C4 olefin stream passes through a disproportionation reactor and a separation device to obtain the product hexene. The method can be used for industrial production of hexene preparation through C4 disproportionation.

Description

technical field [0001] The invention relates to a method for producing hexene by carbon four disproportionation. Background technique [0002] As a high value-added olefin product, the synthesis of hexene has attracted much attention. At present, the conventional preparation method of hexene in industry is to generate 1-hexene through ethylene polymerization, and the catalyst used is an alkylated metal catalyst. Through olefin disproportionation technology, relatively excess low-value-added C4 olefins can be converted into high-value-added hexene and ethylene. [0003] Olefin disproportionation (Olefin metathesis) is a conversion process of olefins. Under the action of transition metal catalysts (such as W, Mo, Re, etc.), the C=C double bond in olefins is broken and reformed, so that new olefin products can be obtained. We can simply express the disproportionation process of alkenes from the following reaction formula: [0004] Catal. [0005] …...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/107C07C6/04
Inventor 宣东刘苏董静
Owner CHINA PETROLEUM & CHEM CORP