Preparation method for high-dispersion zeolite molecular sieves
A zeolite molecular sieve and molecular sieve technology, applied in the direction of crystalline aluminosilicate zeolite, etc., can solve the problems of prolonged crystallization time, dispersion, low hydrothermal stability, etc., and achieve inhibition of system transformation, large external specific surface area, and reduced condensation. the effect of reunion
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Embodiment 1
[0138] Repeat comparative example 1, water glass (SiO 2 ), water, sulfuric acid, aluminum sulfate (Al 2 o 3 ), isopropanol (IPA) and n-butylamine (NBA) in molar ratio as SiO 2 / Al 2 o 3 =178,OH - / SiO 2 =0.58, NBA / SiO 2 =0.40, IPA / SiO 2 =0.01,H 2 O / SiO 2 =15 prepared into a homogeneous gel, and added its SiO to the gel 2 Total weight 2% ZSM-5 molecular sieve seed crystals. After the reaction gel was emulsified by an emulsifier for 15 minutes, it was transferred to a high-pressure hydrothermal kettle, stirred and aged at 100°C for 24 hours, and then heated to 170°C for crystallization for 23 hours. Wherein 23h is the crystallization end time of the zeolite molecular sieve determined by examining the crystallization curve of the zeolite molecular sieve. When the zeolite molecular sieve crystallization time reaches 23h, trimethylchlorosilane (by mass ratio R / SiO 2 =0.5 meter) into the crystallization kettle with the crystallization compound, stirred evenly, and react...
Embodiment 2
[0140] Repeat implementation 1, but replace trimethylchlorosilane with methyltrichlorosilane and methylhydrogendichlorosilane of the same quality respectively, then the obtained products are proved to be pure ZSM-5 molecular sieves through X-ray diffraction analysis, and their relative crystallinity The degrees are 86% and 90% respectively. Characterized by SEM, the product is dispersed nano zeolite. via N 2 Characterized by physical adsorption, the BET external area is 70m 2 / g, 65m 2 / g, and the product filtration rate is 10 times that of Comparative Example 1.
Embodiment 3
[0142] Repeat Example 1, when the crystallization time of the zeolite molecular sieve reaches 23h, open the pressure reducing valve, so that part of the water, vaporizable isopropanol and n-butylamine in the crystallization material liquid are recovered through condensation, and the recovered liquid can be recycled . Pour trimethylchlorosilane into the kettle filled with the crystallization material liquid after decompression, stir evenly, and react at 100°C for 5h. The obtained solid product is filtered through a plate frame, washed, dried and roasted to obtain pure ZSM-5 molecular sieve. The relative crystallinity of the product is 93.0%. Characterized by SEM, the product is dispersed nanometer zeolite. via N 2 Physical adsorption characterization, its BET external area is 70m 2 / g, and the product filtration rate is 10 times that of Comparative Example 1.
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