Molecular sieve catalyst as well as preparation method and application thereof
A technology of molecular sieve and catalyst, which is applied in the field of molecular sieve catalyst and its preparation, can solve the problems that the efficiency of decomposing formaldehyde into water and carbon dioxide cannot reach 100%, it is easy to fall off, and the activity is unstable.
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Embodiment 1
[0050]This embodiment provides a molecular sieve catalyst, and the molecular sieve catalyst was prepared by a method:
[0051](1) 2 g of Usy molecular sieve and 0.687 ml of hydrochloric acid were added to 39.313 ml of deionized water (0.2 M hydrochloric acid was 0.2 m), stirred at 30 ° C for 6 h, filtered, deionized water washed into neutral, 110 ° C for 12 h, resulting acid treatment Usy molecular sieve;
[0052](2) Take 0.025 g of pelinet with 0.025 g of pelinestation to 20 ml of deionized water to add 1 g of Usy molecular sieves of the acid treatment, mix stirred for 4 h, stir the excess moisture, 110 ° C dry 12h, will result Hype in the tube furnace2Restore, H2The flow rate was 20 ml / min, under 350 ° C, and 1 h was reduced to obtain the molecular sieve catalyst.
[0053]The conversion of the catalyst on formaldehyde is likefigure 1 Demolvedfigure 1 It can be seen that the catalyst of the present invention can remove formaldehyde 100%, exhibiting excellent catalytic activity, and the ca...
Embodiment 2
[0056]This embodiment provides a molecular sieve catalyst, and the molecular sieve catalyst was prepared by a method:
[0057](1) Take 2 g of USY molecular sieve and 0.927 ml of hydrochloric acid (0.25 m), 0.25 M hydrochloric acid concentration is 0.25 m), stirred at 32 ° C, filtered, deionized water washed into neutral, 120 ° C oven for 13 h, to obtain acid treatment Usy molecular sieve;
[0058](2) Add 0.056 g of nitrate and 0.0365 g of nitrate to 20 ml of deionized water to add 1 g of USY molecular sieves of the acid treatment, mix stirred for 6 h, stirring and removing excess moisture, 110 ° C drying 10h, The resulting sample is used in tubular furnace2Restore, H2The flow rate was 25 ml / min, under 360 ° C, 0.2 h was reduced to obtain the molecular sieve catalyst.
Embodiment 3
[0060]The present embodiment differs from the first embodiment only that the concentration of the acid solution is 0.1 m, and the other conditions and parameters are identical to the first embodiment.
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