An integrated method for catalyst carbon deposition removal and catalyst activity evaluation
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] The residual oil hydrogenation catalyst (Ni-Mo / γ-Al 2 o 3 , carbon deposit amount is 18.74%) and 80 grams of purity is 98.5% tetrahydronaphthalene mixed, reacted 60 minutes at 420 ℃, the hydrogen that produces adopts gas chromatography external standard method to quantify, and the composition of liquid after reaction is analyzed by liquid chromatography. The carbon deposition removal rate of the catalyst is 59.6%, the hydrogen production is 0.22 moles, and the activity of the catalyst recovers from 34.7% to 92.6%.
Embodiment 2
[0015] The residual oil hydrogenation catalyst (Ni-Mo / γ-Al 2 o 3 , the amount of carbon deposition is 18.74%) mixed with 40 grams of tetrahydronaphthalene with a purity of 98.5% and 110 grams of 9,10-dihydrophenanthrene with a purity of 95%, and reacted for 15 minutes at 420 ° C, and the hydrogen produced by gas chromatography The external standard method was used for quantification, and the composition of the reacted liquid was analyzed by liquid chromatography. The carbon deposition removal rate of the catalyst is 66.0%, the hydrogen production is 0.12 moles, and the activity of the catalyst recovers from 34.7% to 89.8%.
Embodiment 3
[0017] The residual oil hydrogenation catalyst (Ni-Mo / γ-Al 2 o 3 , carbon deposit amount is 18.74%) and 240 grams of purity is 98.5% tetrahydronaphthalene mixed, reacted 30 minutes at 420 ℃, the hydrogen that produces adopts gas chromatography external standard method to quantify, and the composition of liquid after the reaction is analyzed by liquid chromatography. The carbon deposition removal rate of the catalyst is 61.8%, the hydrogen production is 0.38 moles, and the activity of the catalyst recovers from 34.7% to 94.2%.
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