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Method for isomerizing butene-2 into butene-1

A butene and isomerization technology, applied in the direction of isomerization of hydrocarbons, chemical instruments and methods, organic chemistry, etc., can solve the problems of high reaction temperature and low catalyst activity, so as to reduce the reaction temperature, help reduce energy consumption, The effect of good technical effects

Active Publication Date: 2016-01-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] The technical problem to be solved by the present invention is that there are problems of low catalyst activity and high reaction temperature in the prior art, and a new method for isomerizing butene-2 ​​to butene-1 is provided

Method used

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  • Method for isomerizing butene-2 into butene-1

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] According to 1Al 2 o 3 :20SiO2 2 :0.02Na 2 O:5R:2000H 2 The molar ratio of O, sodium silicate, aluminum nitrate, ethylenediamine, and sodium hydroxide were added to deionized water respectively, and the pH value was adjusted to 10-13 by sulfuric acid, stirred for 2 hours, and the resulting gel was placed in an autoclave at After crystallization at 170°C for 68 hours, take it out, filter, wash until neutral, and dry to obtain the raw molecular sieve powder, which is ZSM-35 molecular sieve through XRD detection. see results figure 1 , SEM photo see figure 2 .

[0030] The raw molecular sieve powder is sodium type, and ammonium exchange is carried out according to the known technology, 0.5 mol / liter ammonium nitrate solution, 80 ° C for 2 hours, and exchanged three times. After drying, it was calcined at 550°C for 6 hours to obtain hydrogen ZSM-35 molecular sieve. The finished catalyst product A is obtained.

[0031] The prepared catalysts were evaluated on a 10m...

Embodiment 2

[0033] According to 1Al 2 o 3 :25SiO2 2 :0.1Na 2 O:6.3R:2500H 2 The molar ratio of O, sodium silicate, aluminum nitrate, ethylenediamine, and sodium hydroxide were added to deionized water respectively, the pH value was adjusted to 10-13 by sulfuric acid, stirred for 2 hours, and the resulting gel was placed in an autoclave Crystallize at 150°C for 5 days, take it out, filter, wash until neutral, and dry to obtain the raw molecular sieve powder, which is ZSM-35 molecular sieve through XRD detection.

[0034] The raw molecular sieve powder is sodium type, and ammonium exchange is carried out according to the known technology, 0.5 mol / liter ammonium nitrate solution, 80 ° C for 2 hours, and exchanged three times. After drying, it was calcined at 550°C for 6 hours to obtain hydrogen ZSM-35 molecular sieve. The finished catalyst product B is obtained.

[0035] Carry out catalyst B evaluation by [embodiment 1], the result is listed in table 2.

Embodiment 3

[0037] According to 1Al 2 o 3 :30SiO2 2 :0.2K 2 O:6.3R:2500H 2 The molar ratio of O is to add sodium silicate, aluminum nitrate, ethylenediamine and potassium hydroxide to deionized water respectively, adjust the pH value to 10-13 by sulfuric acid, stir for 2 hours, and put the resulting gel in an autoclave Crystallize at 200°C for 6 days, take it out, filter, wash until neutral, and dry to obtain the raw molecular sieve powder, which is ZSM-35 molecular sieve through XRD detection.

[0038] The raw molecular sieve powder is sodium type, and ammonium exchange is carried out according to the known technology, 0.5 mol / liter ammonium nitrate solution, 80 ° C for 2 hours, and exchanged three times. After drying, it was calcined at 550°C for 6 hours to obtain hydrogen ZSM-35 molecular sieve. That is, the finished catalyst product C is obtained.

[0039] Carry out catalyst C evaluation by [embodiment 1], the result is listed in table 2.

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Abstract

The present invention relates to a method for isomerizing butene-2 into butene-1. A purpose of the present invention is mainly to solve the problems of low catalyst activity and high reaction temperature in the prior art. The technical scheme of the present invention comprises that butene-2 or a butene-2-rich mixture is adopted as a reaction raw material, and the reaction raw material contacts a catalyst to produce a butene-2 double bond isomerization reaction so as to generate butene-1, wherein the used catalyst is at least one selected from ZSM-35 zeolite, ZSM-5 zeolite or ZSM-11 zeolite. With the technical scheme, the problems in the prior art are well solved, and the method can be used for butene-1 preparation through butene-2 in the industrial production.

Description

technical field [0001] The invention relates to a method for isomerizing butene-2 ​​into butene-1. Background technique [0002] C4 is one of the products from refinery FCC unit or cracking ethylene unit, the main composition is isobutene, butene-1 and butene-2 ​​(cis and trans isomers). [0003] Butene-1 is the raw material for the production of linear low-density polyethylene (LLDPE), and many manufacturers often cannot meet the needs of production. Butene-1 is also the raw material for disproportionation to produce hexene-1. Generally, butene-1 is produced by using It can be obtained by separation and purification in mixed C4 products, and can also be obtained by dimerization of ethylene. The use of butene-2 ​​is relatively small, mainly used in the production of alkylate, methyl ethyl ketone and disproportionation to produce propylene. Butene-2 ​​is produced through double bond isomerization to produce butene-1, which can meet the demand for butene in industrial product...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C5/25C07C11/08B01J29/65B01J29/40B01J29/80
Inventor 金照生李亚男许茗喆
Owner CHINA PETROLEUM & CHEM CORP