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Method for preparing polymer-grade piperylene

A technology for crude piperylene and pentadiene, which is applied in the field of refining and separating polymerization grade piperylene, can solve the problems of difficulty in realizing stable industrial operation, easy deactivation of adsorbents, etc., and achieves low energy consumption and simple process. Effect

Active Publication Date: 2016-05-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Patent US4031151 proposes to use adsorption separation technology to separate piperylene and other impurities, but the disadvantage of this method is that the surface acidity of the adsorbent has a catalytic effect on the polymerization of olefins and diolefins, and the adsorbent is easily deactivated
And this process is an unsteady material exchange process, it is difficult to achieve stable industrial operation

Method used

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  • Method for preparing polymer-grade piperylene
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  • Method for preparing polymer-grade piperylene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] The crude piperylene raw material enters the first extraction tower in the presence of a polymerization inhibitor, the operating pressure is normal pressure, the temperature of the tower tank is 70°C, and the extractant dimethylformamide is preheated to 40°C and added from the top of the tower, and the crude The pentadiene raw material weight ratio is 6:1, and the reflux ratio is 2, and the mixture material enriched in cyclopentene and cyclopentane is obtained at the top of the tower, and the material enriched in piperylene and extractant is obtained in the tower still; The top material of the first extraction tower enters the rectification tower, the operating pressure is normal pressure, the temperature of the tower bottom is 50°C, the temperature of the top of the tower is 35°C, and the reflux ratio is 5, cyclopentene is obtained from the top of the tower, and cyclopentane is obtained from the bottom of the tower; The material in the bottom of the first extraction tow...

Embodiment 2

[0034]The crude piperylene raw material enters the first extraction tower in the presence of a polymerization inhibitor, the operating pressure is 0.2MPa, the temperature of the bottom of the tower is 150°C, and the extraction agent dimethylformamide is preheated to 100°C and added from the top of the tower, and the crude The pentadiene raw material weight ratio is 20:1, and the reflux ratio is 30, and the mixture material enriched in cyclopentene and cyclopentane is obtained at the top of the tower, and the material enriched in piperylene and extractant is obtained in the tower still; The top material of the first extraction tower enters the rectification tower, the operating pressure is normal pressure, the temperature of the tower bottom is 60°C, the temperature of the top of the tower is 45°C, and the reflux ratio is 50, cyclopentene is obtained from the top of the tower, and cyclopentane is obtained from the bottom of the tower; The material in the bottom of the first extr...

Embodiment 3

[0036] The crude piperylene raw material enters the first extraction tower in the presence of a polymerization inhibitor, the operating pressure is 0.1MPa, the temperature of the bottom of the tower is 110°C, and the extraction agent dimethylformamide is preheated to 70°C and added from the top of the tower. The pentadiene raw material weight ratio is 13:1, and the reflux ratio is 16, and the mixture material enriched in cyclopentene and cyclopentane is obtained at the top of the tower, and the material enriched in piperylene and extractant is obtained in the tower still; The top material of the first extraction tower enters the rectification tower, the operating pressure is normal pressure, the temperature of the tower bottom is 55°C, the temperature of the top of the tower is 40°C, and the reflux ratio is 28, cyclopentene is obtained from the top of the tower, and cyclopentane is obtained from the bottom of the tower; The material in the bottom of the first extraction tower e...

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Abstract

The invention discloses a method for preparing polymer-grade piperylene. The method mainly comprises the following processes: 1) crude piperylene obtained by separation of a C5 fraction which is a byproduct of petroleum cracking for preparation of ethylene enters a first extractive distillation column to undergo extractive distillation, mixed materials rich in cyclopentene and cyclopentane are obtained at the top of the column, and materials rich in piperylene and an extraction agent are obtained at the bottom of the column; 2) the materials at the bottom of the column in the step 1) enter a first stripping column to remove a solvent, an extraction agent is obtained at the bottom of the column, and the extraction agent returns back to a first extraction column for recycling; 3) materials at the top of the column in the step 2) enter a dipolymer reactor to undergo a polymerization reaction, a dimerization reaction liquid enters a heavies removing column to undergo refining, heavy components such as dicyclopentadiene and the like are obtained at the bottom of the column, and materials rich in piperylene are obtained at the top of the column; 4) the materials at the top of the column in the step 3) enter a second extractive distillation column to undergo secondary extractive distillation, and a polymer-grade piperylene product is obtained at the top of the column; and 5) the materials at the bottom of the column in the step 4) enter a secondary stripping column to recover a solvent, an extraction agent is obtained at the bottom of the column, and the extraction agent returns back to a secondary extraction column for recycling.

Description

technical field [0001] The invention relates to a method for refining and separating polymerization-grade piperylene, in particular to a method for refining piperylene obtained by separating carbon five, a by-product of petroleum cracking to ethylene, to polymerization grade by using extractive distillation and dimerization reaction. Background technique [0002] In the process of producing ethylene from petroleum cracking, a considerable amount of C5 fraction is produced by-product, and the C5 fraction is rich in diolefins such as piperylene, isoprene and cyclopentadiene. These diolefins are active in chemical properties and are important resources for chemical utilization. The mixed carbon five (hereinafter referred to as crude piperylene) obtained by the carbon five separation process is composed of piperylene 65 ~ 75wt%, and the total content of cyclopentene and cyclopentane is 18 ~ 25wt%, about 2% cyclopentadiene and alkynes, a small amount of other C5 hydrocarbons and...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C11/20C07C13/10C07C13/12C07C7/04C07C7/08
Inventor 姚亚娟傅建松秦技强奚军吴忠平
Owner CHINA PETROLEUM & CHEM CORP
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