A kind of catalyst preparation method for hydrogen production by steam reforming of methane
A methane steam reforming technology for hydrogen production, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc. Deep oxidation of products, increase in catalyst cost and other issues, to 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
[0025] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, dried at 110°C for 8 h, and the obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 9.3wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.8wt% of catalyst precursor A weight in terms of elements, Ni accounting for 2.9wt% of catalyst precursor A weight in terms of elements, V accounting for 1.7wt% of catalyst precursor A weight in terms of elements; Activation in a mixed atmosphere, 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 reduced and activated catalyst precursor A is mixed with 300mL of 10% mass concentration of Sorbet Add the alcohol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3...
Embodiment 2
[0027] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, dried at 110°C for 8 h, and the obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 9.3wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.8wt% of catalyst precursor A weight in terms of elements, Ni accounting for 2.9wt% of catalyst precursor A weight in terms of elements, V accounting for 1.7wt% of catalyst precursor A weight in terms of elements; Activation in a mixed atmosphere, 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 reduced and activated catalyst precursor A is mixed with 300mL of 10% mass concentration of Sorbet Add the alcohol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3...
Embodiment 3
[0029] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, dried at 110°C for 8 h, and the obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 9.3wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.8wt% of catalyst precursor A weight in terms of elements, Ni accounting for 2.9wt% of catalyst precursor A weight in terms of elements, V accounting for 1.7wt% of catalyst precursor A weight in terms of elements; Activation in a mixed atmosphere, 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 reduced and activated catalyst precursor A is mixed with 300mL of 10% mass concentration of Sorbet Add the alcohol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3...
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