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A method for preparing hierarchically porous zeolite in one step without secondary template

A technology of pore zeolite and sub-template, which is applied in the direction of crystalline aluminosilicate zeolite, borocarbane silicone crystalline aluminosilicate zeolite, etc., to achieve reduced synthesis cost, high acid site accessibility, and high acid site accessibility Effect

Inactive Publication Date: 2019-03-08
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] The purpose of the present invention is to provide a method for preparing hierarchically porous zeolite in one step without a secondary template, so as to solve the problems existing in the preparation of hierarchically porous zeolite by the post-treatment method and the template method. Hierarchical zeolite with pore or macroporous structure

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  • A method for preparing hierarchically porous zeolite in one step without secondary template
  • A method for preparing hierarchically porous zeolite in one step without secondary template
  • A method for preparing hierarchically porous zeolite in one step without secondary template

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Embodiment 1

[0019] According to SiO 2 :Al 2 o 3 :NaOH:TPA + :H 2 O = 1:0.025:0.153:0.105:22.322 molar ratio, weigh 5.01g tetrapropylammonium bromide, 0.46gγ-Al at room temperature 2 o 3 , Dissolve 1.1g of sodium hydroxide in 51mL of distilled water, stir and clarify, slowly add 21mL of silica sol with a mass fraction of 40% dropwise, mix well, transfer to a stainless steel reaction kettle with a volume of 100mL, and crystallize at 140°C for 5 days , the resulting solid product was washed with distilled water until neutral, filtered, dried, and then calcined in a muffle furnace at 550° C. with air for 5 hours to obtain a hierarchically porous ZSM-5 zeolite.

[0020] figure 1 The SEM images of the obtained ZSM-5 crystals show that the obtained ZSM-5 crystals present a core-shell structure, and the shell layer is formed by the interlaced growth of strip-shaped ZSM-5 zeolites. Pore ​​and macroporous structure; TEM shows that there are obvious mesopore and macroporous structure between...

Embodiment 2

[0022] According to SiO 2 :Al 2 o 3 :NaOH:TPA + :H 2 The mol ratio of O=1.000: 0.033: 0.279: 0.210: 22.322, at room temperature 10.02g tetrapropylammonium bromide, 0.86g pseudo-boehmite (70%Al 2 o 3 , 30%H 2O), 2g of sodium hydroxide were dispersed in 41mL of distilled water, after stirring and clarification, 31mL of silica sol with a mass fraction of 30% was slowly added dropwise. The resulting solid product was washed with distilled water to neutrality, filtered, dried, and then calcined in a muffle furnace at 550° C. for 5 hours with air to obtain a hierarchically porous ZSM-5 zeolite.

[0023] SEM showed that the interior of the spherical ZSM-5 zeolite crystal was formed by the accumulation of nanocrystals, and there were obvious mesopores and macropores; figure 2 The TEM shows that the crystal lattice orientation of the nanocrystals is inconsistent, and obvious mesopore and macropore structure can be observed between the grains; N 2 The adsorption-desorption resu...

Embodiment 3

[0025] According to SiO 2 :Al 2 o 3 :NaOH:TPA + :H 2 O = 1.000: 0.025: 0.204: 0.084: 19.222 molar ratio, 4.65g tetrapropylammonium bromide, 0.81g aluminum hydroxide, 1.7g sodium hydroxide were dissolved in 48mL distilled water at room temperature, stirred and clarified, slowly dripped Add 24mL of silica sol with a mass fraction of 40%, mix well, transfer to a stainless steel reaction kettle with a volume of 100mL, crystallize at 170°C for 2 days, wash the obtained solid product with distilled water until neutral, filter, dry, and then The multi-level porous ZSM-5 zeolite was obtained by calcining in a muffle furnace at 550°C for 5 hours with air flowing through it.

[0026] SEM showed that the spherical ZSM-5 zeolite crystal was formed by the accumulation of nano-grains, and there were obvious mesopores and macropores; TEM showed that there were obvious mesoporous structures between the nano-grains; image 3 N 2 In the adsorption-desorption curve, the as-prepared ZSM-5 z...

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Abstract

The invention provides a secondary template-free one-step preparation method of a multistage porous zeotile. The method is as below: using with TPA<+> as a template, slowly adding a silicon source into an water solution dissolved with a template, an aluminum source and sodium hydroxide and evenly mixing, conducting hydrothermal reaction at 140 to 200 DEG C, roasting the solid product to obtain multistage ZSM-5 zeolite with intergranular mesoporous and macroporous structure. The molar ratio of the materials is as below: SiO2: Al2O3: NaOH: TPA<+>: H2O = 1: 0.003 to 0.033: 0.153 to 0.279: 0.042 to 0.210: 19.222 to 25.423. This invention uses silicon aluminum source and microporous template for conventional zeolite synthesis; through fine control of the preparation conditions, multistage porous ZSM-5 zeotile accumulated by nanocrystals through one-step hydrothermal method; and the method ensures the connectivity of mesopores tunnel with the inherent pore tunnel, improve acid bit accessibility of zeolite and has great application prospect in the fields of fine chemicals, petrochemical and other industrial production.

Description

technical field [0001] The present invention relates to a preparation method of multi-stage porous zeolite, in particular to a silicon-alumina source and template agent synthesized by traditional microporous zeolite, without adding secondary template, one-step hydrothermal synthesis with intercrystalline mesopores and macropores Method for the structure of the ZSM-5 zeolite. Background technique [0002] Due to the adjustable acid properties, regular pore structure and high hydrothermal stability, zeolite materials are widely used in the fields of catalysis, adsorption and separation technology. Especially in the field of catalysis, the unique shape-selective catalytic effect of zeolite materials has brought revolutionary progress. However, the crystal size of zeolite is much larger than its pore diameter, which makes it have a large mass transfer resistance in the reaction. When it comes to macromolecular reactants or products, zeolite catalysts suffer from severe diffusi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/40
CPCC01B39/40C01P2004/03
Inventor 潘梦张勇郑家军白亚东刘芝平李瑞丰王广帅
Owner TAIYUAN UNIV OF TECH