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Preparation method of hierarchically porous Y-type molecular sieve

A multi-level porous and molecular sieve technology, which is applied in the directions of octahedral crystalline aluminosilicate zeolite, crystalline aluminosilicate zeolite, etc., can solve the problems that the microporous template and the mesoporous template cannot be reasonably matched, connected and co-constructed. , to achieve the effect of high relative crystallinity, easy separation, and uniform mesopore size

Active Publication Date: 2018-01-09
CNOOC TIANJIN CHEM RES & DESIGN INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to overcome the deficiencies of the prior art and provide a method for preparing a multi-level porous Y molecular sieve, which uses an anionic surfactant as a mesoporous template to form an ordered mesoscopic structure, and uses a co-structure directing agent as a linking agent The bridge between the mesoporous structure and the microporous structure solves the problems that the microporous template and the mesoporous template cannot be reasonably matched, connected and co-built during the self-assembly process. Synthesis of hierarchically porous Y molecular sieves by one-step hydrothermal method

Method used

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  • Preparation method of hierarchically porous Y-type molecular sieve
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Examples

Experimental program
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Effect test

Embodiment 1

[0034] At 80°C, 8.2g of sodium metaaluminate (Al 2 o 3 The content is 41wt%, Na 2 O content is 28.7wt%) dissolved in 160g deionized water, add 46g sodium hydroxide (purity 96%) under mechanical stirring, continue to stir, make it dissolve completely, obtain high alkalinity sodium metaaluminate solution. At 30°C, under stirring, the above-mentioned high alkalinity sodium metaaluminate solution was added to 222g of water glass (SiO 2 The content is 26.2wt%, Na 2 The O content is 8.3wt%), stirred for 2 hours, and then aged at 15°C for 24 hours to prepare the seed glue.

[0035] At 80° C., 10.8 g of sodium metaaluminate was dissolved in 172 g of deionized water, 36 g of sodium hydroxide was added, and stirring was continued to completely dissolve to obtain a low-alkalinity sodium metaaluminate solution. In a stirring state, the gelling temperature is 30°C, the prepared seed glue is poured into 436g of water glass, mixed evenly, and then 235g of aluminum sulfate solution (Al 2...

Embodiment 2

[0038] Each raw material source is with embodiment 1.

[0039] Dissolve 8.8g of sodium metaaluminate in 160g of deionized water at 80°C, add 42g of sodium hydroxide under mechanical stirring, and continue stirring to completely dissolve it to obtain a high-basicity sodium metaaluminate solution. The high alkalinity sodium metaaluminate solution was added into 208g of water glass under stirring at 40°C, stirred for 3 hours, and then left to age at 25°C for 16 hours to prepare the seed glue.

[0040] At 80° C., 116 g of sodium metaaluminate was dissolved in 172 g of deionized water, 38 g of sodium hydroxide was added, and stirring was continued to completely dissolve to obtain a low-alkalinity sodium metaaluminate solution. Under stirring, the gelling temperature is 40°C, pour the prepared seed gel into 406g of water glass, mix well, then add 235g of aluminum sulfate solution and the low-alkalinity sodium metaaluminate solution obtained above, and stir for 2 hours , to obtain a...

Embodiment 3

[0043] Each raw material source is with embodiment 1.

[0044] Dissolve 10.3g of aluminum hydroxide in 160g of deionized water at 80°C, add 45g of sodium hydroxide under mechanical stirring, and continue stirring to completely dissolve it to obtain a high-basicity sodium metaaluminate solution. At 20°C under stirring, the above high alkalinity sodium metaaluminate solution was added into 193g of water glass, stirred for 4 hours, and then aged at 20°C for 36 hours to prepare the seed glue.

[0045] At 80° C., 106 g of aluminum hydroxide was dissolved in 172 g of deionized water, 48 g of sodium hydroxide was added, and stirring was continued to completely dissolve to obtain a low-alkalinity sodium metaaluminate solution. Under stirring, the gelling temperature is 20°C, pour the prepared seed gel into 383g of water glass, mix well, then add 245g of aluminum sulfate solution and the low-alkalinity sodium metaaluminate solution obtained above, and stir for 4 hours , to obtain a so...

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Abstract

The invention discloses a preparation method of a hierarchically porous Y-type molecular sieve. The method comprises the following steps: mixing a silicon source and an aluminium source at 5-60 DEG C,and standing and aging the mixture to prepare seed crystal glue; mixing the silicon source, the seed crystal glue and the aluminium source at 15-70 DEG C, and stirring the mixture to obtain sol; mixing the sol, a co-structure- directing agent and a template agent, stirring the mixture for 0.5-8 h, heating the obtained sol to 90-120 DEG C, crystallizing the sol for 6-72 h, and performing filtering, washing, drying and roasting to obtain the hierarchically porous Y-type molecular sieve. The co-structure directing agent and the template agent adopted in the preparation method are cheap, available and small in dosage and are easily separated from volume phase; the obtained hierarchically porous Y-type molecular sieve is high in relative crystallinity, mesoporous channels are regular, microporous channels and mesoporous channels intersect, and mesoporous diameter distribution is uniform.

Description

technical field [0001] The invention belongs to the field of molecular sieve materials and their preparation, and specifically relates to a method for preparing multi-stage Y molecular sieves through hydrothermal crystallization by using organosilane as a co-structure directing agent and anionic surfactant as a template. Background technique [0002] Because of its excellent pore structure and suitable surface acidity, Y-type molecular sieve has been widely used in the fields of adsorption, separation and catalysis. It has been used as the main active component of petrochemical catalysts in catalytic cracking and hydrocracking. With the increasingly heavy feed oil, improving the accessibility of the active center of refining catalysts and improving their catalytic conversion ability to macromolecules has become the focus of petrochemical catalyst development. With the continuous development of new synthetic techniques for molecular sieve materials, multi-level porous molecul...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/24
Inventor 王凌涛刘冠锋于海斌臧甲忠洪美花王海强洪鲁伟季超邱宇宋万仓
Owner CNOOC TIANJIN CHEM RES & DESIGN INST
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