A kind of regeneration method of titanium-silicon molecular sieve catalyst deactivated by oxidation reaction
A titanium-silicon molecular sieve and oxidation reaction technology, which is applied in molecular sieve catalysts, catalyst regeneration/reactivation, physical/chemical process catalysts, etc., can solve the problem of high energy consumption, and achieve high energy consumption, complex regeneration process, and high cost.
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Embodiment 1
[0040] 5g of the deactivated catalyst was mixed and washed with 50g of formic acid and 50g of hydrogen peroxide (30wt%) at 90°C under normal pressure for 8h, followed by washing, filtering and drying. The dried regenerant is then calcined for 6 hours by mixing water vapor and oxygen at 1:1 at 300°C. The evaluation experiment shows that the selectivity of propylene oxide is 97.52%, and the conversion rate of hydrogen peroxide is 42.00%.
Embodiment 2
[0042] 5g of the deactivated catalyst was mixed and washed with 50g of formic acid and 50g of hydrogen peroxide (30wt%) at 90°C under normal pressure for 8h, followed by washing, filtering and drying. The dried regenerant is then calcined for 12 hours by mixing water vapor and oxygen at 300°C in a ratio of 1:1. The evaluation experiment shows that the selectivity of propylene oxide is 98.02%, and the conversion rate of hydrogen peroxide is 43.00%.
Embodiment 3
[0044] 5g of the deactivated catalyst was mixed and washed with 50g of formic acid and 50g of hydrogen peroxide (30wt%) at 80°C under normal pressure for 8h, followed by washing, filtering and drying. The dried regenerant is then calcined with a 1:1 mixture of water vapor and oxygen at 300°C for 6 hours. The evaluation experiment shows that the selectivity of propylene oxide is 97.40%, and the conversion rate of hydrogen peroxide is 40.50%.
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