A kind of cfan catalyst and its preparation and application in hydrogen production from methane
A catalyst, methane technology, applied in the direction of heterogeneous catalyst chemical elements, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., to achieve easy recovery and utilization, inhibit sintering and agglomeration, and improve methane The effect of conversion rate
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Embodiment 1
[0064] 1) Mix ferric nitrate, calcium nitrate, nickel nitrate, aluminum nitrate and citric acid (the molar ratio of Ca-Fe-Al-Ni elements in the material is 4:4:1:1), the molar addition of citric acid is all 1.3 times the total moles of metal atoms;
[0065] 2) Add deionized water and configure it into a solution to meet the concentration of the nickel nitrate solution in the mixed solution of 0.10mol / L;
[0066] 3) Stir the prepared solution at 40°C for 30 minutes;
[0067] 4) Put the solution obtained in step 3) in a drying box, foam and dry for 5 hours in the temperature range of 180°C, and crush and grind the obtained solid sample;
[0068] 5) Put the sample after grinding in the step 4) into a muffle furnace, and calcinate at 850°C for 4 hours in an air atmosphere. The temperature rise rate is guaranteed to be 2.5°C / min. The calcined solid powder is ground to The particle size is less than 0.3mm, and the CFAN catalyst is finally obtained, and the catalyst is ground to a particle ...
Embodiment 2
[0121] Compared with Example 1, the only difference is that the catalytic reaction temperature of methane is 600-850°C. Determine the rate of methane hydrogen production, product hydrogen purity and methane conversion rate, the results are shown in Figure 8 ~ Figure 10 .
[0122] After determining the best catalyst, we optimized the reaction temperature range, using hydrogen yield, hydrogen concentration and methane conversion as indicators, and the results are as follows Figure 8 , Picture 10 Shown. The results of hydrogen production rate and hydrogen concentration in the temperature range of 600-850 ℃, it can be found that when the temperature is lower than 700 ℃, both the hydrogen production rate and the hydrogen concentration, the performance is greatly reduced. When the temperature is higher than 800℃, it can be found that the catalyst performance is good at the initial stage of the reaction, and too high temperature will cause rapid agglomeration and sintering of the ca...
Embodiment 3
[0124] Compared with Example 1, newly prepared CFAN→half an hour catalytic methane cracking CFAN→one hour catalytic methane cracking CFAN, the carrier is slightly reduced, and the coefficient y is from 1.52→1.40→1.28, which proves the minimal reduction of the carrier. The coefficient y gradually decreases from large, and the methane cracking activity of this process does not change significantly, such as Picture 11 , Picture 12 As shown, the oxygen carrier still maintains high catalytic activity for methane cracking, that is, high hydrogen yield and concentration.
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