Preparation method of catalyst for oxidative hydrogenation of propane
A technology for oxidative dehydrogenation and catalysts, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., to achieve improved utilization, tight pore structure, and improved resource utilization Effect
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Embodiment 1
[0032] (1) Preparation of the catalyst, the steps are as follows:
[0033] The waste hydrodesulfurization HDS catalyst (MoCo / Al 2 o 3 ), after extraction to remove the oil on the surface of the catalyst, after drying and roasting, the treated waste HDS catalyst (containing Mo: 12.7 wt%, Co: 2.2 wt%, V: 2.4 wt%, Ni: 1.7 wt%, Al 2 o 3 : 71.6 wt%), grind the catalyst to 200 mesh (referring to passing through a 200 mesh sieve), weigh 100 g of the powder, add 250 mL of 98 wt% concentrated sulfuric acid, stir at 50 °C to dissolve the solid, and collect the filtrate by filtration , to the filtrate was added 2.1 g NH 4 VO 3 , after stirring and dissolving, add 12.5 g of citric acid, add 135 g of pseudo-boehmite after all dissolved, stir at 70 °C until the solution is evaporated to dryness, dry the obtained solid at 100 °C for 8 h, and roast at 600 °C for 4 h , the final catalyst MoCoV / Al can be obtained after tablet molding 2 o 3 . Based on the weight of the catalyst, MoO 3 T...
Embodiment 2
[0037] In Example 1, the concentrated sulfuric acid was changed to 300 mL of a mixed solution of 98 wt% concentrated sulfuric acid and 65 wt% nitric acid, the volume ratio was 2:1, the citric acid was changed to 7.5 g, and the pseudoboehmite was changed to 370 g , the rest are the same as in Example 1, and the catalyst obtained is MoCoV / Al 2 o 3 . Based on the weight of the catalyst, MoO 3 The content of CoO is 5.6%, the content of CoO is 0.8%, V 2 o 5 The content of Al is 1.6%, Al 2 o 3 The content is 92%. The physical and chemical properties of the catalysts are listed in Table 1.
[0038] The evaluation of the catalyst is the same as in Example 1, and the results of the oxidative dehydrogenation of propane to propylene with the catalyst are shown in Table 2.
Embodiment 3
[0040] In Example 1, the catalyst is changed to the waste hydrodesulfurization HDS MoCoNi / Al of the fixed-bed residual oil hydrogenation industrial unit 2 o 3 Catalyst (containing Mo: 15.6 wt%, Co: 1.6 wt%, V: 1.7 wt%, Ni: 2.3 wt%, Al 2 o 3 : 68.5 wt%), concentrated sulfuric acid was changed to 350 mL of a mixed solution of 98 wt% concentrated sulfuric acid and 65 wt% concentrated nitric acid, the volume ratio was 1:1, NH 4 VO 3 Change it to 5.5 g, add 3.8 g of cobalt nitrate, change citric acid to 15.4 g, change pseudo-boehmite to 290 g, and the rest are the same as in Example 1, and the obtained catalyst is MoCoV / Al 2 o 3 . Based on the weight of the catalyst, MoO 3 The content of CoO is 7.7%, the content of CoO is 0.7%, V 2 o 5 The content of Al is 1.6%, Al 2 o 3 The content is 90%. The physical and chemical properties of the catalysts are listed in Table 1.
[0041] The evaluation of the catalyst is the same as in Example 1, and the results of the oxidative deh...
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