Preparation method of catalyst for methane steam reforming to produce hydrogen
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 8h, and the obtained catalyst was calcined at 450°C for 4h 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 in terms of elements Accounting for 1.8wt% of catalyst precursor A weight, Ni accounts for 2.9wt% of catalyst precursor A weight in terms of elements, V accounts for 1.7wt% of catalyst precursor A weight in terms of elements; 20g of catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrog...
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 8h, and the obtained catalyst was calcined at 450°C for 4h 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 in terms of elements Accounting for 1.8wt% of catalyst precursor A weight, Ni accounts for 2.9wt% of catalyst precursor A weight in terms of elements, V accounts for 1.7wt% of catalyst precursor A weight in terms of elements; 20g of catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrog...
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 8h, and the obtained catalyst was calcined at 450°C for 4h 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 in terms of elements Accounting for 1.8wt% of catalyst precursor A weight, Ni accounts for 2.9wt% of catalyst precursor A weight in terms of elements, V accounts for 1.7wt% of catalyst precursor A weight in terms of elements; 20g of catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrog...
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