Catalyst for producing H2 by methane directly conversion based on Fe3O4 and preparation method thereof
A catalyst and direct technology, applied in the field of composite Fe3O4 type methane direct conversion to H2 catalyst and its preparation, can solve the problems of low temperature and loss of function, and achieve the effects of improving activation, prolonging service life and reducing temperature
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Embodiment 1
[0024] Example 1: The catalyst contains 5.63 mol% Co, 8.19 mol% Cr. Weigh 12.1200gFe(NO 3 ) 3 9H 2 O, 0.4917gCo(NO 3 ) 2 ·6H 2 O, 0.9832gCr(NO 3 ) 3 9H 2 O, add 22.8mL distilled water to prepare a mixed solution of about 1.5mol / L; add 8.195g urea to the mixed solution, stir evenly, heat up to 90°C, and react at a constant temperature for 3h; filter and wash with distilled water until neutral; use ethanol Replace the water in it until no water is detected in the eluate; put the filter cake in an oven and dry it at a constant temperature of 150°C for 10 hours; take it out and put it in a muffle furnace and roast it at 500°C for 10 hours; crush the roasted product into 20-40 mesh powder to obtain the catalyst MH-1.
Embodiment 2
[0025] Example 2: The catalyst contains 8.35 mol% Cu, 12.61 mol% V. Weigh 12.1200gFe(NO 3 ) 3 9H 2 O, 0.5001gCu(CH 3 COO) 2 ·H 2 O, 0.4425gNH 4 VO 3, add 24.2mL distilled water to prepare a mixed solution of about 1.5mol / L; add 6.532g urea to the mixed solution, stir evenly, raise the temperature to 85°C, and react at constant temperature for 4h; filter and wash with distilled water until neutral; replace with ethanol From the water content to the eluate, no water can be detected; put the filter cake in an oven and dry it at a constant temperature of 150°C for 8 hours; take it out and put it in a muffle furnace and roast it at 550°C for 10 hours; crush the roasted product into 20-40 mesh powder to obtain the catalyst MH -2.
Embodiment 3
[0026] Embodiment 3: Adopt similar method among the embodiment 1, prepare a series of catalysts, catalyst, component, component ratio, precipitation agent, precipitation agent ratio, drying temperature, drying time, calcination temperature and calcination time are shown in Table 1.
[0027] Table 1
[0028] catalyst
PUM
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