Process for preparing p-xylene and propylene from mixed alcohol ethers

A technology for para-xylene and alcohol ether, which is applied in the field of preparing para-xylene and propylene, can solve problems such as low conversion rate of alcohol ether, and achieve the effects of improving the conversion rate of alcohol ether, reducing production cost and prolonging life.

Active Publication Date: 2017-07-28
汕头市澄丽日化用品有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] P-xylene and propylene are important raw materials in chemical production. At present, a large number of journals, books, patents and other documents have recorded the scheme of using methanol and dimethyl ether to catalyze the production of propylene and xylene. Most of the catalysts used in the catalysis are ZSM -5 and its modified product

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0012] Example 1

[0013] Put ZSM-5 molecular sieve and ZSM-11 molecular sieve in sodium hydroxide solution for primary immersion modification, the mass concentration of sodium hydroxide solution is 5%, the temperature of primary immersion modification is 30~35℃, duration is 2.5 h, then use the acidic modification solution for secondary immersion modification in the kettle body. The acidic modification solution is a mixed aqueous solution of hydrochloric acid and fluorosilicic acid. The content of hydrochloric acid in the mixed aqueous solution is 2% (mass concentration, the same below), The content of fluorosilicic acid is 6%, the temperature of the secondary impregnation modification is 110℃, the duration is 2.5h, and the internal pressure of the sealed vessel is controlled to 0.25MPa. After the secondary impregnation modification, ZSM-5 molecular sieve and ZSM-11 molecular sieve are recovered and combined Wash and dry; mix ZSM-5 molecular sieve, ZSM-11 molecular sieve and clay ac

Example Embodiment

[0016] Example 2

[0017] Put ZSM-5 molecular sieve and ZSM-11 molecular sieve in sodium hydroxide solution for primary immersion modification, the mass concentration of sodium hydroxide solution is 5%, the temperature of primary immersion modification is 30~35℃, duration is 2.5 h, then use the acidic modification solution for secondary immersion modification in the kettle body. The acidic modification solution is a mixed aqueous solution of hydrochloric acid and fluorosilicic acid. The content of hydrochloric acid in the mixed aqueous solution is 2% (mass concentration, the same below), The content of fluorosilicic acid is 6%, the temperature of the secondary impregnation modification is 110℃, the duration is 2.5h, and the internal pressure of the sealed vessel is controlled to 0.25MPa. After the secondary impregnation modification, ZSM-5 molecular sieve and ZSM-11 molecular sieve are recovered and combined Wash and dry; mix ZSM-5 molecular sieve, ZSM-11 molecular sieve and clay ac

Example Embodiment

[0020] Example 3

[0021] Put ZSM-5 molecular sieve and ZSM-11 molecular sieve in sodium hydroxide solution for primary immersion modification, the mass concentration of sodium hydroxide solution is 5%, the temperature of primary immersion modification is 30~35℃, duration is 2.5 h, then use the acidic modification solution for secondary immersion modification in the kettle body. The acidic modification solution is a mixed aqueous solution of hydrochloric acid and fluorosilicic acid. The content of hydrochloric acid in the mixed aqueous solution is 2% (mass concentration, the same below), The content of fluorosilicic acid is 6%, the temperature of the secondary impregnation modification is 110℃, the duration is 2.5h, and the internal pressure of the sealed vessel is controlled to 0.25MPa. After the secondary impregnation modification, ZSM-5 molecular sieve and ZSM-11 molecular sieve are recovered and combined Wash and dry; mix ZSM-5 molecular sieve, ZSM-11 molecular sieve and clay ac

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PUM

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Abstract

The invention relates to a method for preparing paraxylene and propylene by using mixed alcohol ether. According to the method, alcohol ether mixed gas comes into contact with a catalyst in a fluidized bed reactor so as to carry out a catalytic reaction; in the catalytic reaction, the temperature in the fluidized bed reactor is controlled to be 490-500 DEG C, the pressure is controlled to be 1.5-2.0 MPa, the airspeed of the alcohol ether mixed gas is 4-4.5h<-1>, and the alcohol ether mixed gas comprises the following components in parts by weight: 32 parts of methanol, 65 parts of dimethyl ether, 1.5 parts of water and 2 parts of C6-C12 hydrocarbon. According to the scheme, the alcohol ether mixed gas is catalyzed in the fluidized bed reactor by virtue of the catalyst, so that the alcohol ether mixed gas can be converted into propylene and paraxylene at a high selectivity; detection on the treated oil phase and gaseous phase shows that the alcohol ether conversion rate is larger than 99 percent, the proportion of paraxylene in xylene is higher than 90 percent, a ratio of ethylene to ethane in the gaseous phase is larger than 8, a ratio of propylene to propane is larger than 8, and a ratio of propylene to ethylene is larger than 10.

Description

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Claims

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Application Information

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Owner 汕头市澄丽日化用品有限公司
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