A kind of thioether oxidation method
A technology of thioether oxidation and thioether, which is applied in the fields of chemical instruments and methods, organic chemistry, chemical recovery, etc., can solve the problems of high cost of anodic oxidation, prolong the stable operation period, prolong the service life of a single pass, and reduce the regeneration frequency Effect
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Embodiment 11-14 and 16
[0093] Following examples 11-14 and 16 adopt the following method to measure the activity of catalyst:
[0094] Catalyst, 36% by weight of ammonia water (as NH 3 meter), 30% by weight of hydrogen peroxide (as H 2 o 2 ), tert-butanol and cyclohexanone by mass ratio = 1:7.5:10:7.5:10 and then stirred and reacted at 80°C under atmospheric pressure for 2h, filtered the reactant, and analyzed the obtained liquid phase by gas chromatography The composition of the catalyst is analyzed, and the conversion rate of cyclohexanone is calculated by the following formula and used as the activity of the catalyst,
[0095] The conversion rate (%) of cyclohexanone=[(the molar amount of cyclohexanone added−the molar amount of unreacted cyclohexanone) / the molar amount of cyclohexanone added]×100%.
Embodiment 1
[0098] The catalyst (being a spherical catalyst with a volume average particle diameter of 500 μm, the content of titanium-silicon molecular sieve TS-1 in the catalyst is 85% by weight, the content of silicon oxide is 15% by weight, and the density is 0.79g / cm 3 ) is packed in a fixed-bed reactor to form a catalyst bed, wherein the number of the catalyst bed is 1 layer, and the aspect ratio of the catalyst bed is 10.
[0099] Dimethyl sulfide, hydrogen peroxide (provided in the form of 30% by weight hydrogen peroxide) as an oxidizing agent and methanol as a solvent were mixed to form a liquid mixture which was fed from the bottom into a fixed bed reactor in parallel flow over the catalyst bed. Among them, in the liquid mixture, the molar ratio of dimethyl sulfide to hydrogen peroxide is 2:1, the molar ratio of dimethyl sulfide to methanol is 1:8, and the weight hourly space velocity of dimethyl sulfide is 2.5h -1 . The temperature in the catalyst bed was 40° C., and the pres...
Embodiment 2
[0103] The same method as in Example 1 is used to oxidize dimethyl sulfide, the difference is that ammonia (24% by weight) is also sent into the fixed-bed reactor, and the amount of ammonia added will be the pH of the liquid mixture in contact with the catalyst. Adjusted from 5.2 to 7.5.
[0104] During the 640 hours of reaction, the dimethyl sulfide feed was stopped 4 times. The results obtained for 0.5 hours and 640 hours of reaction are listed in Table 1.
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