CFAN catalyst, preparation method thereof, and application of CFAN catalyst in production of hydrogen from methane
A catalyst, methane technology, used in heterogeneous catalyst chemical elements, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., to improve stability and catalytic activity, inhibit sintering and agglomeration, The effect of suppressing sintering and agglomeration
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Embodiment 1
[0065] 1) Mix iron nitrate, calcium nitrate, nickel nitrate, aluminum nitrate and citric acid (in the material, the molar ratio of Ca-Fe-Al-Ni element is 4:4:1:1), and the molar addition amount of citric acid is all 1.3 times the total molar weight of metal atoms;
[0066] 2) Add deionized water to configure a solution, satisfying that the concentration of nickel nitrate solution in the mixed solution is 0.10mol / L;
[0067] 3) Stir the prepared solution at 40°C for 30 minutes;
[0068] 4) Put the solution obtained in step 3) in a drying oven, foam and dry for 5 hours at a temperature range of 180° C., and crush and grind the obtained solid sample;
[0069] 5) Put the ground sample in step 4) into a muffle furnace, and calcinate it at 850° C. for 4 hours in an air atmosphere. The heating rate is guaranteed to be 2.5° C. / min, and the calcined solid powder is ground to The particle size is less than 0.3 mm, and the CFAN catalyst is finally obtained, and the catalyst is ground t...
Embodiment 2
[0123] Compared with Example 1, the only difference is that the methane catalytic reaction temperature is 600-850°C. Determination of methane hydrogen production rate, product hydrogen purity and methane conversion rate, the results are shown in Figure 8 ~ Figure 10 .
[0124] After determining the best catalyst, we optimized the reaction temperature range, using hydrogen production rate, hydrogen concentration and methane conversion as indicators, the results are as follows Figure 8 , Figure 10 shown. From the graph of hydrogen yield and hydrogen concentration results in the temperature range of 600-850°C, it can be found that when the temperature is lower than 700°C, both the hydrogen yield and the hydrogen concentration will drop significantly in performance. When the temperature is higher than 800°C, it can be found that the catalyst has good performance at the initial stage of the reaction, but too high a temperature will cause rapid agglomeration and sintering of t...
Embodiment 3
[0126] Compared with Example 1, the newly prepared CFAN→half-hour catalytic methane cracking CFAN→one-hour catalytic methane cracking CFAN, a slight reduction of the carrier occurs, and the coefficient y is from 1.52→1.40→1.28, which proves the trace reduction of the carrier. The coefficient y gradually decreases from large to small, but the methane cracking activity of the process does not change significantly, such as Figure 11 , Figure 12 As shown, the oxygen carrier still maintains high catalytic activity for methane cracking, that is, high hydrogen production rate and concentration.
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