Preparation method of anti-water-type low-temperature NH3-SCR catalyst, catalyst prepared therewith and application of the catalyst
A technology of catalysts and composite oxides, applied in the direction of physical/chemical process catalysts, metal/metal oxides/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problems of catalyst water resistance and achieve good NH3- The effects of SCR water resistance, simple and quick preparation method, and excellent catalytic performance
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Embodiment 1
[0024] Example 1. Mn 0.2 Ti 0.8 o 2 sample preparation
[0025] Dissolve 0.98g of manganese acetate tetrahydrate in 28mL of absolute ethanol, add 1mL of water and 1mL of glacial acetic acid under magnetic stirring, and stir evenly. 5 mL of tetrabutyl titanate was added to the above solution, and stirred for 30 min. The reaction solution was transferred to a stainless steel hydrothermal reaction kettle with a polytetrafluoroethylene liner of 50 mL, and placed in an oven at 180° C. for 24 h. Cool to room temperature, centrifuge, wash with water and ethanol three times, and dry overnight at 60°C. The obtained sample was calcined in a muffle furnace for 4 hours in an air atmosphere (calcination temperature 550 ° C, heating time 150 min), to obtain Mn 2 Ti 8 sample.
Embodiment 2
[0026] Example 2. Mn 0.2 Ti 0.8-x Si x o 2 Catalyst preparation
[0027] With the Mn prepared in embodiment 1 0.2 Ti 0.8 o 2 Disperse 1 g of the sample in 100 mL of n-hexane, add x mL of hexamethyldisiloxane (0.50.2 Ti 0.8-x Si x o 2 sample. The XRD results showed that the prepared catalysts were all in the anatase crystal form (such as figure 1 ). The BET results show that the pore volume of Si-treated samples increases (as shown in Table 1), and the pore diameter moves toward the large pores (as shown in Table 1). figure 2 ).
[0028] Table 1
[0029]
Embodiment 3
[0030] Example 3. NH of the catalyst 3 -SCR performance evaluation
[0031] The catalyst prepared in embodiment 1,2 is applied to NH 3 -SCR response, Mn 0.2 Ti 0.8-x Si x o 2 and Mn 0.2 Ti 0.8 o 2 The catalysts all showed good low-temperature catalytic activity, indicating that the introduction of the inert species Si did not reduce the activity of the catalyst, such as image 3 shown. The reaction is carried out on a micro-reaction catalytic device, and the reaction gas composition is 500ppmNH 3 , 500ppmNO, 5%O 2 , the residual gas is N 2 , the airspeed is 100,000h -1 , the amount of catalyst used is 0.1g, the temperature of the catalytic reaction is 25-350° C., and the NO conversion rate of the reaction is detected by an infrared method.
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