Titanium silicalite molecular sieve, synthetic method and application of titanium silicalite molecular sieve, and cyclic ketone oxidation method
A technology of titanium-silicon molecular sieve and synthesis method, which is applied in the direction of molecular sieve catalysts, molecular sieves and base exchange compounds, chemical instruments and methods, etc., and can solve the problems of large grains of titanium-silicon molecular sieves, low activity, difficulty in separation of small grains, poor preparation repeatability, etc. problems, to achieve the effect of easy industrial application, good catalytic effect and high utilization rate
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[0030] In the present invention, as long as the titanium-silicon molecular sieve has the aforementioned characteristics, the purpose of the present invention can be achieved, and its synthesis method can be various, as long as the titanium-silicon molecular sieve with the aforementioned characteristics can be synthesized. For the present invention, the titanium-silicon molecular sieve is preferably Silicon molecular sieves are synthesized as follows, the method comprising:
[0031] (1) mixing and contacting a precious metal source, an ammonia source, and optionally water to obtain a first mixture;
[0032] (2) In the presence of a templating agent, mixing a titanium source, an organosilicon source, the first mixture, and optionally water to obtain a second mixture;
[0033] (3) performing the first hydrothermal crystallization on the second mixture to obtain a mixed slurry A with a solid content not higher than 20% by weight;
[0034] (4) Concentrating the mixed slurry A to o...
Embodiment approach
[0046] According to a preferred embodiment of the present invention, the preferred stage (1) and stage (3) meet one or both of the following conditions:
[0047] Condition 1: the temperature of stage (1) is lower than the temperature of stage (3), preferably, the temperature of stage (1) is 10-50°C lower than the temperature of stage (3), preferably 20-40°C lower;
[0048] Condition 2: the time of stage (1) is less than the time of stage (3), preferably, the time of stage (1) is 5-24 hours shorter than the time of stage (3), preferably 6-12 hours shorter.
[0049] According to a preferred embodiment of the present invention, the temperature in stage (2) is lowered to not higher than 50°C, preferably 30-50°C, and the residence time is at least 1 hour, preferably 1-5h.
[0050] According to the method of the present invention, the heating rate and cooling rate for adjusting the temperature to the temperature of each stage can be selected according to the type of the reactor used...
Embodiment 1
[0109] (1) Mixing and contacting noble metal source palladium chloride and ammonia water (concentration is 20% by weight) to obtain a mixture; noble metal source: ammonia source (weight ratio)=2:20, solute content is 1% by weight, and the conditions for mixing and contacting include: 30°C, normal pressure, 4h;
[0110] (2) Then mix the mixture with tetrabutyl titanate, tetraethyl orthosilicate, and tetrapropylammonium hydroxide; after mixing, perform the first hydrothermal crystallization at a temperature of 120°C for 72 hours to obtain a mixed slurry A (solid content is 18% by weight); silicon source: titanium source: precious metal source: templating agent: water (mol)=100:2:1:15:1000;
[0111] (3) Filtrating the mixed slurry A to obtain mixed slurry B (solid content is 40% by weight) and liquid phase C;
[0112] (4) The mixed slurry B was subjected to the second hydrothermal crystallization at a temperature of 170° C. for 24 hours, filtered, washed, dried, roasted and reco...
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