Catalyst for methanol oxidation to methylal by one step, preparing method and applications thereof
A technology of oxidation synthesis and catalyst, which is applied in the preparation of organic compounds, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve the problems of high price and limited practical application of catalysts, and achieve high selectivity, long life and good stability Effect
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Embodiment 1
[0027] 0.25 g of phosphomolybdic acid and 2.5 g of SBA-16 molecular sieve were carefully ground and mixed, and then calcined at 350° C. for 5 hours to obtain a catalyst with a content of phosphomolybdic acid of 7.48 wt % and a content of SBA-15 of 92.52 wt %.
[0028] Catalyst in 10vol% O 2 / Ar atmosphere at 350°C for 4 hours, lowered to 180°C, and then introduced methanol vapor preheated at 140°C with Ar and O 2 The mixed gas, the raw gas composition is CH 3 OH / O 2 / Ar=6.3 / 9.4 / 84.3, the reaction pressure is normal pressure, and the reaction gas space velocity is 4000ml / g cat .h, the reactivity of the catalyst is shown in Table 1.
Embodiment 2
[0030] Grind and mix 0.13g of phosphomolybdic acid and 2.5g of MCM-41 molecular sieve carefully, and roast at 550°C for 5h to obtain a catalyst with a content of phosphomolybdic acid of 4.03wt% and an MCM-41 content of 95.97wt%.
[0031] Catalyst in 10vol% O 2 / Ar 550°C for 1h, lower to 180°C, feed methanol steam and air preheated at 140°C, the raw gas composition is CH 3 OH / O 2 / Ar=6.3 / 9.4 / 84.3, the reaction pressure is normal pressure, and the reaction gas space velocity is 4000ml / g cat .h, the reactivity of the catalyst is shown in Table 1.
Embodiment 3
[0033] Dissolve 3.3g of phosphotungstic acid in deionized water, add 5.0g of HZSM-5 molecular sieve (Si / Al=60), impregnate at 50°C to form a viscous precursor, dry at 70°C for 24h, and then bake in air (300°C , 7h), the content of phosphotungstic acid was 36.46wt%, and the content of HZSM-5 was 63.54wt%.
[0034] Treat the catalyst at 300°C for 5 hours in an air atmosphere, lower it to 170°C, feed methanol steam and air preheated at 140°C, and the composition of the raw gas is CH 3 OH / O 2 / N 2 =10.0 / 18.0 / 72.0, the reaction pressure is normal pressure, and the reaction gas space velocity is 2000ml / g cat .h, the reactivity of the catalyst is shown in Table 1.
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