Double micro pore high silicon composite molecular sieve and its preparing method

A molecular sieve and high-silicon technology, applied in the direction of crystalline aluminosilicate zeolite, octahedral crystalline aluminosilicate zeolite, etc., can solve the problems of difficult post-treatment process and poor hydrothermal stability, and achieve good thermal and hydrothermal stability Effect

Inactive Publication Date: 2007-04-11
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The inventor has successfully prepared Y/Beta and Beta/Y composite molecular sieve catalytic materials (patent application numbers: 2

Method used

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  • Double micro pore high silicon composite molecular sieve and its preparing method
  • Double micro pore high silicon composite molecular sieve and its preparing method

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0014] Embodiment 1

[0015] In the first step, 13.0g of high-silicon Y zeolite powder and 90.0ml of NaOH (0.10mol / L) were mixed uniformly, stirred with magnetic stirring for 1 hour, and the mixed solution was loaded into a 150ml stainless steel reaction kettle, and dissolved in alkali at 180 ° C for 3 hours . Obtain high-silica Y zeolite with reduced crystallinity after alkali dissolution;

[0016] In the second step, the obtained high-silicon Y zeolite with reduced crystallinity after being dissolved in alkali is centrifuged with a centrifuge, and the supernatant is removed;

[0017] In the third step, 0.6g of sodium hydroxide, 10.0g of TEABr (tetraethylamine bromide), 10.0ml of concentrated ammonia, 28.0ml of silica sol ( [SiO 2 ]=5.80mol / L), 16.0ml of distilled water was mixed and stirred to form a uniform white jelly, loaded into a 150ml stainless steel reactor, crystallized at 140°C for 6 days, taken out, washed until the solution was neutral and then dried. The prep...

Example Embodiment

[0018] Embodiment 2

[0019] In the first step, 13.0g of high-silicon Y zeolite powder and 90.0ml of NaOH (0.10mol / L) were mixed uniformly, stirred for 1 hour with magnetic stirring, and the mixed solution was loaded into a 150ml stainless steel reaction kettle, and dissolved in alkali at 175 ° C for 4 hours . Obtain high-silica Y zeolite with reduced crystallinity after alkali dissolution;

[0020] In the second step, the obtained high-silicon Y zeolite with reduced crystallinity after being dissolved in alkali is centrifuged with a centrifuge, and the supernatant is removed;

[0021] In the third step, 0.4g sodium hydroxide, 10.0g TEABr (tetraethylamine bromide), 10.0ml concentrated ammonia water, 28.0ml silica sol ( [SiO 2 ]=5.80mol / L), 16.0ml of distilled water was mixed and stirred to form a uniform white jelly, loaded into a 150ml stainless steel reactor, crystallized at 140°C for 6 days, taken out, washed until the solution was neutral and then dried. The prepared s...

Example Embodiment

[0022] Embodiment 3

[0023] In the first step, 13.0g of high-silicon Y zeolite powder and 90.0ml of NaOH (0.10mol / L) were mixed uniformly, stirred with magnetic stirring for 1 hour, and the mixed solution was put into a 150ml stainless steel reaction kettle, and dissolved in alkali at 140 ° C for 20 Hours. Obtain high-silica Y zeolite with reduced crystallinity after alkali dissolution;

[0024] In the second step, the obtained high-silicon Y zeolite with reduced crystallinity after being dissolved in alkali is centrifuged with a centrifuge, and the supernatant is removed;

[0025] In the third step, 0.8g sodium hydroxide, 10.0g TEABr (tetraethylamine bromide), 10.0ml concentrated ammonia water, 28.0ml silica sol ( [SiO 2 ]=5.80mol / L), 16.0ml of distilled water was mixed and stirred to form a uniform white jelly, loaded into a 150ml stainless steel reactor, crystallized at 140°C for 8 days, taken out, washed until the solution was neutral and then dried. The prepared samp...

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Abstract

The present invention belongs to the field of fine chemical technology, and is especially the preparation process of double pore high silicon zeolite molecular sieve as one kind of composite molecular sieve. The present invention features that by using type-Y high silicon zeolite as silicon and aluminum source, and through dissolving the surface of the high silicon type-Y crystal grain, mixing with ammonia water solution of ammonium tetraethyl bromide, adding certain amount of silica gel via stirring, crystallizing at 140-170 deg.C for 5-10 days, washing, stoving and roasting to eliminate template agent, double pore high silicon zeolite molecular sieve with both type-Y and type-beta molecular sieve pore canals is obtained. The double pore high silicon zeolite molecular sieve has low synthesis cost and high hydrothermal stability, and may be used in petrochemical industry.

Description

1. Technical field [0001] The preparation method of the high-silicon double-microporous composite molecular sieve of the present invention relates to a preparation method of an inorganic porous catalytic material, belongs to the field of fine chemical industry, and more specifically relates to a Beta / high-silicon Y double-microporous composite zeolite molecular sieve Preparation. 2. Technical Background [0002] Y-type zeolite is formed by faujasite cages interpenetrating with each other along three crystal axis directions through twelve-membered rings. It is an excellent catalyst with high cracking activity and good selectivity. Therefore, the invention of Y-type zeolite has epoch-making significance in the field of catalytic cracking. And Y-type zeolite with high silicon-aluminum ratio obtained by subjecting Y-type zeolite to hydrothermal treatment, that is, high-silicon Y-type zeolite. Due to the good hydrothermal stability and acid stability of high silicon aluminum ra...

Claims

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Application Information

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IPC IPC(8): C01B39/02C01B39/24
Inventor 李瑞丰秦波张喜文郭群孙万付马静红
Owner TAIYUAN UNIV OF TECH
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