A catalyst preparation method for partial oxidation of methane to synthesis gas
A catalyst and synthesis gas technology, applied in the field of supported nickel-based catalyst preparation, can solve the problems of low metal utilization rate of carrier pores, low catalyst contribution, accelerated deep oxidation of products, etc., so as to improve conversion rate and product selectivity, The effect of reducing catalyst cost and avoiding further oxidation
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Embodiment 1
[0027] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, and dried at 110°C for 8 h. The obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 8.7wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.9wt% of catalyst precursor A weight in terms of elements, Ni accounting for 2.8wt% of catalyst precursor A weight in terms of elements, V accounting for 2.1wt% 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
[0029] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, and dried at 110°C for 8 h. The obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 8.7wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.9wt% of catalyst precursor A weight in terms of elements, Ni accounting for 2.8wt% of catalyst precursor A weight in terms of elements, V accounting for 2.1wt% 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
[0031] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, and dried at 110°C for 8 h. The obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 8.7wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.9wt% of catalyst precursor A weight in terms of elements, Ni accounting for 2.8wt% of catalyst precursor A weight in terms of elements, V accounting for 2.1wt% 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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