Method for preparing hydrofining catalyst by waste catalyst
A technology for hydrotreating and spent catalysts, applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as excessive interaction, metal environmental pollution, waste of resources, etc., and achieve easy implementation. The effect of operation, improving pore structure and improving activity
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Embodiment 1
[0029] First, the waste W-Ni / Al 2 o 3 Hydrofining catalyst (containing 27.86w% WO 3 , 2.39w% NiO, 6.61w% C, 6.01w% S, 0.06w% Fe, the rest is Al 2 o 3 ) to 250 mesh; then, mixed with 2.0w% WO 3 Grind, then add 20w% binder to form; Then, the catalyst is regenerated (activated) under the following conditions: the catalyst is loaded into the regeneration device, and the device is replaced with the inert gas nitrogen, and then the oxygen content is gradually reduced. Increase to 2.5v% temperature rise, constant temperature for 2h at 120°C, constant temperature for 2h at 200°C, constant temperature for 1.5h at 290°C, and constant temperature for 3h at 490°C. The number of the obtained activated catalyst is A.
Embodiment 2
[0031] Waste W-Ni / Al used in embodiment 1 2 o 3The hydrorefining catalyst powder is soaked in a cobalt nitrate solution with a total CoO content of 2.0w%, dried at 120°C and then molded by adding 20w% binder. The catalyst was then activated under the same conditions as in Example 1. The obtained catalyst was numbered B.
Embodiment 3
[0033] Waste W-Ni / Al used in embodiment 1 2 o 3 Hydrofining catalyst powder, mixed with 1.0w% MoO 3 , 0.8w% WO 3 Grinding with 0.2w% CoO, and adding 20w% binder to shape. The catalyst was then regenerated under the same conditions as in Example 1. The number of the obtained catalyst is C.
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