A kind of preparation method of hydrogen production catalyst by steam reforming of methane
A methane water vapor reforming technology for hydrogen production, applied in the direction of molecular sieve catalysts, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low metal utilization in carrier channels and accelerate deep oxidation of products , increase catalyst cost and other issues, achieve the effect of improving conversion rate and product selectivity, avoiding further oxidation, and accelerating adsorption and desorption speed
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Embodiment 1
[0030] Weigh 2.97g of nickel nitrate and dissolve it in an appropriate amount of deionized water to obtain solution A; use the equal volume impregnation method to load on 20g of alumina (the pore volume is 0.72ml / g, the specific surface area is 242m 2 / g, strip shape, equivalent diameter 1.5mm) carrier, aged at room temperature for 4h, dried at 80°C for 12h, and calcined at 700°C for 4h to obtain catalyst precursor B, wherein Ni accounted for 3% of the weight of the carrier in terms of elements; catalyst precursor B Activate in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 80%, the reduction conditions are 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the mass concentration of the reduced and activated catalyst precursor B and 300mL is Add 10% sorbitol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3MPa, and react at 220°C for 4 hours; place the re...
Embodiment 2
[0032] Weigh 2.97g of nickel nitrate and dissolve it in an appropriate amount of deionized water to obtain solution A; use equal volume impregnation method to load 20g of silicon oxide (pore volume is 1.06ml / g, specific surface area is 387m 2 / g, spherical, equivalent diameter 0.5mm) carrier, aged at room temperature for 6h, dried at 110°C for 10h, and calcined at 600°C for 4h to obtain catalyst precursor B, in which Ni accounted for 3% of the weight of the carrier in terms of elements; catalyst precursor B was in Activate in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 90%, the reduction conditions are 400 ° C, 0.2 MPa (absolute pressure), and the reduction time is 8 hours; % of sorbitol solution was added to the autoclave, sealed and replaced with hydrogen for 4 times, then adjusted the hydrogen pressure to 2MPa, and reacted at 300°C for 2h; the reacted mixture in the above autoclave was placed for 1h, filtered, and the obtained s...
Embodiment 3
[0034] Weigh 2.97g of nickel nitrate and dissolve it in an appropriate amount of deionized water to obtain solution A; load it on 20g of SBA-15 (the pore volume is 1.23ml / g and the specific surface area is 701m 2 / g, strip shape, equivalent diameter 1.5mm) carrier, aged at room temperature for 8h, dried at 120°C for 6h, and calcined at 600°C for 4h to obtain catalyst precursor B, wherein Ni accounted for 3% of the weight of the carrier in terms of elements; catalyst precursor B Activate in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 10%, the reduction conditions are 500°C, 0.2MPa (absolute pressure), and the reduction time is 6h; the mass concentration of catalyst precursor B after reduction and activation is 300mL Add 10% sorbitol solution into the autoclave, seal it and replace it with hydrogen twice, then adjust the hydrogen pressure to 3MPa, and react at 220°C for 4h; place the reacted mixture in the autoclave for 3h, filter, a...
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