Multilevel porous molecular sieve catalyst as well as preparation method and application thereof

A molecular sieve and catalyst technology, which is applied to the multi-stage porous molecular sieve catalyst and the fields of preparation and application, can solve the problems of poor product selectivity, low catalyst space velocity and low conversion rate, and achieve high activity, high product selectivity and long service life. Effect

Inactive Publication Date: 2014-12-24
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst has high selectivity and stability of toluene and xylene, and can solve the problems of low space velocity, low conversion rate, poor product selectivity and easy coking of current catalysts, so as to effectively and comprehensively utilize benzene and methanol resources to produce various values Higher chemical production, less impact on the environment

Method used

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  • Multilevel porous molecular sieve catalyst as well as preparation method and application thereof
  • Multilevel porous molecular sieve catalyst as well as preparation method and application thereof
  • Multilevel porous molecular sieve catalyst as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] In the first step, silicon source: tetraethyl orthosilicate (TEOS), aluminum source: aluminum tert-butoxide, organic template agent: tetrapropylammonium hydroxide (TBAOH), and mesoporous directing agent (HTS) are mixed. SiO 2 :Al 2 o 3 :TPAOH:HTS=50-180:1:0.3:0.01-0.05, the solvent used is ethanol. In the second step, 9 g of water and 1 g of TPAOH were added. The crystallization time is 3 days, and the temperature is 180° C., and the method obtains ZSM-5 zeolite with a multi-level pore structure.

Embodiment 2

[0043] In the first step, the silicon source, aluminum source, and TPAOH were mixed uniformly in ethanol and dried into a xerogel, and then the ethanol solution of HTS was mixed with it and dried in air to form SiO 2 :Al 2 o 3 :TPAOH:HTS=50-180:1:0.3:0.01-0.05, xerogel. In the second step, 9 g of water and 1 g of TPAOH were added. The crystallization time is 3 days, and the temperature is 180° C., and the method obtains ZSM-5 zeolite with a multi-level pore structure.

Embodiment 3

[0045] Weigh 7g of ordinary ZSM-5 molecular sieve purchased from Nanhua Catalyst Factory, add γ-Al 2 o 3 3g, after mixing evenly, add 4% dilute nitric acid for kneading, extrusion molding, put it into a constant temperature drying oven at 120°C and dry for 12 hours, then roast and crush the strip-shaped catalyst to 20-40 mesh particles, and finally roast Catalyst A is then obtained.

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Abstract

The invention relates to a multilevel porous molecular sieve catalyst as well as a preparation method and application thereof. The preparation method of the multilevel porous molecular sieve catalyst comprises the following steps: adding an organic template agent ethanol solution into an aluminum source, a silicon source and a silane ethanol solution to form gel, performing air drying on the gel to obtain dry gel, adding water and tetrapropylammonium hydroxide into the dry gel to obtain a mixture, putting the mixture into a high-pressure kettle, crystallizing the mixture for 3 days at the temperature of 180 DEG C to obtain a multilevel porous ZSM-5 molecular sieve, uniformly mixing the multilevel porous ZSM-5 molecular sieve with gamma-Al2O3, adding a dilute nitric acid solution, then performing mixed kneading, performing strip extruding for forming, drying and roasting in air so as to obtain a carrier; and soaking the carrier by utilizing a magnesium acetate solution, drying and roasting the carrier to obtain a phenylcarbinol alkylation catalyst. When the prepared catalyst is applied to the phenylcarbinol alkylation reaction, the catalyst has the advantages that coke and carbon are not easily generated, the activity is high, and the product selectivity is high. Compared with other catalysts in the prior art, for the catalyst disclosed by the invention, the activity and the reaction stability are high, and the service life is longer.

Description

technical field [0001] The invention relates to a multi-stage pore molecular sieve catalyst for benzene-methanol alkylation, as well as its preparation and application. Background technique [0002] Benzene is mainly derived from catalytic reforming, isomerization of aromatics, and by-products of coal tar and ethylene production processes. According to reports, 150,000 tons of benzene will be generated for every 800,000 tons of ethylene produced, and the growth of ethylene in my country will be over 2 million t / a, which will inevitably lead to a large surplus of benzene. Methanol, as a cheap and easy-to-obtain excellent reagent, has been extensively researched and applied in aspects such as esterification and etherification. However, as one of the important products of coal chemical industry, with the rapid development of coal chemical industry, the market The production of methanol will increase rapidly, and there will be a surplus situation. As one of the most important b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/40C07C15/06C07C15/08C07C2/88
CPCY02P20/52
Inventor 徐亚荣徐新良朱学栋冯丽梅樊金龙
Owner PETROCHINA CO LTD
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