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A catalyst for converting alcohol ethers into p-xylene and C2-C3 olefins and its preparation method

A C2-C3, p-xylene technology, applied in the chemical field, can solve the problems of low xylene selectivity, many alkanes, inability to convert, etc., and achieves the effects of cheap raw materials, reduced preparation cost, and not easy to fall off

Active Publication Date: 2016-02-24
TSINGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Moreover, the above patents can only convert methanol and dimethyl ether, but cannot convert methanol or dimethyl ether containing water and a small amount of other alcohols, ketones, acids, esters, polycyclic aromatic hydrocarbons and other impurities
In addition, the patent (ZL201010146915.5) reported a catalyst that can make the conversion of methanol >60%, but the selectivity of p-xylene is low, and at the same time, in the by-product gas phase hydrocarbons, C 2 -C 3 Many alkanes, C 2 -C 3 less olefins

Method used

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  • A catalyst for converting alcohol ethers into p-xylene and C2-C3 olefins and its preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] 0.2mol / L zinc nitrate was impregnated on ZSM-5 molecular sieve, dried at 110°C for 2 hours, and finally calcined at 700°C for 2 hours. The ZSM-5 molecular sieve loaded with zinc is immersed in the mixture of magnesium nitrate, iron nitrate and silane, treated at 20°C for 0.5 hours, then washed and filtered, dried at 90°C for 24 hours, and then calcined at 350°C for 24 hours to obtain The final product. The mass ratio of iron oxide: magnesium oxide and silicon oxide in the composite oxide layer (the three are evenly mixed) is 1:1:1. The mass ratio of ZSM-5, zinc and composite oxide layer in the catalyst is 30:10:59.

[0028] Use 100% methanol as the reaction raw material, control the reactor pressure to 0.1MPa, and methanol space velocity to 0.2h -1 , the temperature is 520°C, after methanol passes through the catalyst bed, the conversion rate is >99.9%, the total aromatics (carbon-based) yield reaches 70%, and the ratio of p-xylene in xylene is >92%. Ethylene / ethane ...

Embodiment 2

[0030] 2mol / L silver nitrate was impregnated on ZSM-5 molecular sieve, dried at 90°C for 24 hours, and finally calcined at 600°C for 10 hours. Immerse silver-loaded ZSM-5 molecular sieves in magnesium chloride, ferric chloride, and ethyl orthosilicate at 50°C for 0.5 hours, then wash and filter, dry at 100°C for 2 hours, and then roast at 500°C for 4 hours to obtain the final product . The mass ratio of iron oxide: magnesium oxide and silicon oxide in the composite oxide layer (the three are evenly mixed) is 10:60:30. The mass ratio of ZSM-5, silver and composite oxide layer is 40:1:39.

[0031] Use 100% dimethyl ether as the reaction raw material, control the pressure of the reactor to 3MPa, and the space velocity of dimethyl ether to 20h -1 . The temperature is 450°C. After dimethyl ether passes through the catalyst bed layer, the conversion rate>99.9%, the total (carbon-based) yield of aromatics reaches 75%, the ratio of p-xylene in xylene>93%, and ethylene / ethane (mass...

Embodiment 3

[0033] 1mol / L zinc acetate and 0.5mol / L cobalt nitrate were impregnated on ZSM-5 molecular sieves, dried at 100°C for 8 hours, and finally calcined at 650°C for 4 hours. Immerse the ZSM-5 molecular sieve loaded with zinc and cobalt in ferric chloride, magnesium chloride, and butyl orthosilicate at 20°C for 1 hour, wash, filter and dry at 110°C for 8 hours, and then roast at 550°C for 8 hours to obtain the final finished product. The mass ratio of iron oxide: magnesium oxide and silicon oxide in the composite oxide layer (the three are evenly mixed) is 30:69:1. The mass ratio of ZSM-5, zinc, cobalt and composite oxide layer is 51:3:7:39.

[0034] With 50% methanol, 40% dimethyl ether, and 10% formic acid as the reaction raw materials, the pressure in the control reactor is 0.3MPa, and the space velocity of dimethyl ether is 10h -1 . The temperature is 500°C. After the reaction raw materials pass through the catalyst bed, the alcohol ether conversion rate is >99.9%, the tota...

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Abstract

The invention discloses a catalyst for converting alcohol ether to dimethylbenzene and C2-C3 alkene and a preparation thereof. The ingredients of the catalyst comprise a ZSM-5 molecular sieve, metal loaded on the ZSM-5 molecular sieve and a composite oxide layer wrapped outside the ZSM molecular sieve and the metal, wherein the composite oxide layer is composed of silicon oxide, ferric oxide and magnesium oxide. The catalyst is prepared through loading the metal onto the ZSM-5 molecular sieve and wrapping the composite oxide layer. The catalyst is capable of converting carbinol or dimethyl ether raw materials containing water and a certain amount of higher alcohol, acid, ester, ketone or C3-C15 hydrocarbon impurities; under the conditions of 0.1-3Mpa, 450-520 DEG C and air speed of 0.2-30h<-1>, one time conversion rate of carbinol and dimethyl ether is greater than 99.9%; the total arene recycling rate is 69-80%; the weight percentage of p-xylene in the dimethylbenzene is greater than 90% and in the gas phase hydrocarbon, the mass ratio of ethylene to ethane is 3-10 and the mass ratio of propylene to propene is 3-10.

Description

technical field [0001] The invention belongs to the technical field of chemical industry, in particular to a method for converting alcohol ether into p-xylene and C 2 -C 3 Catalysts for olefins and methods for their preparation. Background technique [0002] Catalytic conversion of methanol or dimethyl ether directly into aromatics is an important chemical technology route at present, and it is a beneficial supplement to the traditional production route using petroleum as raw material. Among them, modifying ZSM-5 molecular sieve and loading metals can effectively prepare aromatics, and obtain mixed aromatics mainly composed of benzene, toluene and xylene, wherein the obtained xylene is a mixture, p-xylene, o-xylene and m-xylene It is in a balanced composition (mass percentage is 23:24:53). However, p-xylene has the greatest use. To obtain a relatively large amount of p-xylene, the industry still needs to rely on the traditional transposition and isomerization reaction bet...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/46B01J29/48C07C1/20C07C11/04C07C11/06C07C15/08
CPCY02P20/52Y02P30/20Y02P30/40
Inventor 骞伟中张鲁湘胡琼方孔垂岩苏倡王宁魏飞
Owner TSINGHUA UNIV