A kind of non-precious metal oxide catalyst with anti-water protection layer and preparation method
A non-precious metal and catalyst technology, which is applied in the field of non-precious metal oxide catalysts and preparation, can solve the problems of limited application, high price, deactivation, etc., and achieve the effect of simple preparation method, low cost, and activity recovery
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0028] Weigh 9.31g of cobalt nitrate, 2.23g of ferric nitrate and 4.00g of oxalic acid in an agate mortar and mix well; add 2mL of ethylene glycol to it, grind for 30min, transfer it into a beaker, and put it into the beaker after ultrasonic treatment for 1h overnight in a drying oven at 110° C.; then put it into a muffle furnace and bake at 250° C. for 3 hours to obtain a catalyst. figure 2 For the Fe prepared in Example 1 a co b o x Transmission electron microscope (TEM) photo of the @MC catalyst.
[0029] The catalytic performance of the catalysts for CO oxidation was tested in a fixed bed reactor system. 200mg of 40-60 mesh catalyst was loaded into the reactor, and the catalyst was pretreated in nitrogen at 200°C for 30min before testing; 2 , the rest is N 2 (Equilibrium gas) reaction gas, the space velocity is 15000mL / (g·h), the reaction temperature is controlled and the conversion rate of CO is measured after the reaction reaches stability. The moisture content is...
Embodiment 2
[0032] Using the catalyst prepared in Example 1, reduce the calcination temperature of the catalyst to 230° C., and the other preparation conditions of the catalyst and the evaluation method of the catalyst are the same as in Example 1.
[0033] Activity evaluation results show that using the prepared Fe 3 co 16 o x @MC Catalyst, under humid conditions (0.6vol.%H 2 O) The complete conversion temperature of CO is 60°C; and in humid conditions (0.6vol.%H 2 (0) and temperature of reaction is that the stability of catalyst is tested under 70 ℃, test result is as follows Figure 4 As shown, the activity of the catalyst did not change after 350 hours of operation. In order to evaluate the catalytic stability at different CO conversion rates, under humid conditions (0.6vol.%H 2 (0) and the stability of the test catalyst under different reaction temperatures, the test results are as follows Figure 5 as shown, Figure 5 Middle: a: catalyst activity measured at 40°C; b: catalyst...
Embodiment 3
[0035] Using the catalyst prepared in Example 1, increase the catalyst calcination temperature to 350° C., and the other preparation conditions of the catalyst and the evaluation method of the catalyst are the same as in Example 1.
[0036] Activity evaluation results show that using the prepared Fe 3 co 16 o x @MC catalyst, under normal conditions (3-10ppm H 2 O) The complete conversion temperature of CO is -96°C under humid conditions (0.6vol.%H 2 O) The complete conversion temperature of CO is 70 °C.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


