Catalyst carbon deposit removal and catalyst activity evaluation integrated method
An evaluation method and technology for catalysts, applied in catalyst regeneration/reactivation, chemical instruments and methods, catalysts for physical/chemical processes, etc. Structure and properties have no effect
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Embodiment 1
[0013] 10 grams of residual oil hydrogenation catalyst after industrial operation (Ni-Mo / γ-Al 2 O 3 , the amount of carbon deposition is 18.74%) and 80 grams of tetrahydronaphthalene with a purity of 98.5% were mixed, reacted at 420 ° C for 60 minutes, the generated hydrogen was quantified by gas chromatography external standard method, and the composition of the liquid after the reaction was analyzed by liquid chromatography. The coke removal rate of the catalyst was 59.6%, the hydrogen production was 0.22 moles, and the activity of the catalyst recovered from 34.7% to 92.6%.
Embodiment 2
[0015] 10 grams of residual oil hydrogenation catalyst after industrial operation (Ni-Mo / γ-Al 2 O 3 , the carbon deposition amount is 18.74%) mixed with 40 grams of tetralin with a purity of 98.5% and 110 grams of 9,10-dihydrophenanthrene with a purity of 95%, and reacted at 420 ° C for 15 minutes. The external standard method was used for quantification, and the composition of the reaction liquid was analyzed by liquid chromatography. The coke removal rate of the catalyst was 66.0%, the hydrogen production was 0.12 moles, and the activity of the catalyst recovered from 34.7% to 89.8%.
Embodiment 3
[0017] 10 grams of residual oil hydrogenation catalyst after industrial operation (Ni-Mo / γ-Al 2 O 3 , the amount of carbon deposition is 18.74%) and 240 grams of tetrahydronaphthalene with a purity of 98.5% were mixed, reacted at 420 ° C for 30 minutes, the hydrogen produced was quantified by gas chromatography external standard method, and the composition of the liquid after the reaction was analyzed by liquid chromatography. The coke removal rate of the catalyst was 61.8%, the hydrogen production was 0.38 moles, and the activity of the catalyst recovered from 34.7% to 94.2%.
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