Noble metal modified titanium-silicon molecular sieve and preparation method and application thereof, and method for direct oxidation of olefins
A titanium-silicon molecular sieve and precious metal technology, applied in molecular sieve catalysts, chemical instruments and methods, organic chemistry, etc., can solve the problems of poor stability and low catalyst activity of titanium-silicon materials, and achieve good catalytic effect.
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preparation example Construction
[0028] Therefore, as previously mentioned, the present invention provides a method for preparing the noble metal-modified titanium-silicon molecular sieve of the present invention, the method comprising:
[0029] (1) mixing the unloading agent with the acid solution for beating, carrying out the first heat treatment on the obtained slurry, and separating and obtaining the first solid, wherein the unloading agent is the unloading agent of a reaction device using titanium silicon molecular sieve as a catalyst, The acid solution contains peroxide and nitric acid;
[0030] (2) The second heat treatment is performed after mixing the first solid, the titanium source, the noble metal source and the alkali source in the presence of an aqueous solvent.
[0031] In the present invention, the unloading agent of the reaction device using titanium-silicon molecular sieve as the catalyst can be the unloading agent unloaded from various devices using titanium-silicon molecular sieve as the c...
Embodiment approach
[0044] According to a preferred embodiment of the present invention, the preferred stage (1) and stage (3) meet one or both of the following conditions:
[0045] 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;
[0046] 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.
[0047] 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.
[0048] 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
[0112] This example illustrates the methods and products provided by the invention.
[0113] Under normal temperature (20 DEG C, all the other comparative examples are the same as the examples) and normal pressure (0.1MPa, all the other comparative examples are the same as the examples), the deactivated cyclohexanone oximation catalyst SH-2 and acid solution (containing nitric acid and the aqueous solution of hydrogen peroxide, the concentrations of nitric acid and hydrogen peroxide are both 4mol / L) mixed and beaten, and then the mixed slurry was mixed and stirred at 80°C for 12h; after solid-liquid separation, the solid, precious metal source palladium chloride, titanium After mixing the source titanium sulfate and sodium hydroxide aqueous solution (pH 12), put the mixed solution into a stainless steel sealed reaction kettle, and go through the first stage at 140°C for 6h, then cool the mixture down to 30°C and go through the second stage for 2h, then continue Go through the ...
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Abstract
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