Process for preparing hydrogenating refining catalyst by waste hydrogenating refining catalyst
A hydrogenation catalyst and hydrogenation refining technology, applied in the direction of catalyst activation/preparation, catalyst regeneration/reactivation, chemical instruments and methods, etc., can solve the problems of metal environmental pollution, excessive interaction, waste of resources, etc., and achieve improvement Pore structure, easy operation, and the effect of improving activity
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Embodiment 1
[0032] Take a waste W-Ni / Al with a particle size of about 250 mesh 2 o 3 Hydrodesulfurization catalyst powder (containing 27.86wt% WO 3 , 2.39wt% NiO, 6.61wt% C, 6.01wt% S, 0.06wt% Fe, the remainder being Al 2 o 3 ) 20.0g, adding 0.9g WO with a particle size of 250 mesh 3 and 1.6g titania-alumina (the specific surface area is 241m 2 / g, the pore volume is 0.60cm 3 / g, the average pore diameter is 9.0nm, containing 5.32wt% of titanium dioxide) and mixed, adding 4.5g of adhesive to shape. Then regenerate the catalyst under the following conditions: put the catalyst into the regeneration device, first replace the device with nitrogen, then adjust the oxygen content to 2.50v%, then start to heat up, keep the temperature at 120°C for 2 hours, and at 200°C 2h, constant temperature at 290°C for 1.5h, constant temperature at 490°C for 3h. The number of the obtained regenerated catalyst is A.
Embodiment 2
[0034] Get the waste W-Ni / Al used in embodiment 1 2 o 3 Hydrodesulfurization catalyst powder 20.0g, soak with 40ml, 2.25wt% cobalt nitrate solution, add 1.8g alumina monohydrate after drying at 120 ℃ (after roasting, the specific surface area can be 282m 2 / g, the pore volume is 0.63cm 3 / g, γ-alumina with an average pore size of 9.0nm) and ground to 250 mesh, adding 4.5g of binder to shape. The catalyst was then regenerated under the same conditions as in Example 1. The obtained catalyst was numbered B.
Embodiment 3
[0036] Get the waste W-Ni / Al used in embodiment 1 2 o 3 Hydrodesulfurization catalyst powder 20.0g, mixed with 0.4gMoO 3 , 0.4gWO 3 And 0.1gCoO and 0.8g silica / alumina (specific surface area is 272m 2 / g, the pore volume is 0.62cm 3 / g, the average pore diameter is 9.1nm, containing silicon dioxide 1.25wt%) and 0.8g diboron trioxide-alumina (specific surface area is 234m 2 / g, the pore volume is 0.63cm 3 / g, with an average pore diameter of 10.8nm, containing 5.05wt% boron trioxide) and mixing, adding 4.5g of adhesive to form. 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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