Preparation and use method of a coking benzene hydrodesulfurization catalyst
A technology for hydrodesulfurization and coking of benzene, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc. The effect of catalytic hydrogenation effect
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Embodiment 1
[0041] This embodiment provides a method for preparing a coked benzene hydrodesulfurization catalyst, comprising the following steps:
[0042] S1. Weigh two portions of 30g aluminum oxide powder and 20g titanium dioxide powder, and mix them respectively to prepare a mixed powder carrier of aluminum oxide and titanium dioxide;
[0043] S2. Use the impregnation method to load active metal components on the mixed powder carrier: one part of the mixed powder carrier is immersed in a solution containing tungsten and a solution containing nickel successively twice, wherein the loading amount of tungsten is represented by oxidation The amount of nickel is 0.5g; the loading of nickel is 0.05g in terms of oxides, citric acid is added to the solution containing tungsten, and the amount of citric acid added is 0.25g to obtain an active catalyst carrier Z1;
[0044] Another part of the mixed powder carrier was immersed twice in a solution containing cobalt and in a solution containing mol...
Embodiment 2
[0059] This embodiment provides a method for preparing a coked benzene hydrodesulfurization catalyst, comprising the following steps:
[0060] S1. Weigh two portions of 42g aluminum oxide powder and 18g titanium dioxide powder, and mix them respectively to prepare a mixed powder carrier of aluminum oxide and titanium dioxide;
[0061] S2. Use the impregnation method to load active metal components on the mixed powder carrier: one part of the mixed powder carrier is immersed twice in a solution containing molybdenum and a solution containing nickel, wherein the loading amount of molybdenum is represented by oxidation The amount of nickel is 2.4g; the loading of nickel is 0.6g in terms of oxide, and citric acid is added in the solution containing molybdenum, and the amount of citric acid added is 2.4g to obtain an active catalyst carrier Z1;
[0062] Another part of the mixed powder carrier was immersed twice in the solution containing cobalt, in the solution containing molybden...
Embodiment 3
[0077] This embodiment provides a method for preparing a coked benzene hydrodesulfurization catalyst, comprising the following steps:
[0078] S1. Weigh two portions of 52g aluminum oxide powder and 13g titanium dioxide powder, and mix them respectively to prepare a mixed powder carrier of aluminum oxide and titanium dioxide;
[0079] S2. Use the impregnation method to load active metal components on the mixed powder carrier: one part of the mixed powder carrier is immersed in a solution containing tungsten and a solution containing nickel successively twice, wherein the loading amount of tungsten is represented by oxidation The amount of nickel is 1.95g; the loading of nickel is 1.95g in terms of oxide, and citric acid is added in the solution containing molybdenum, and the amount of citric acid added is 3.9g to obtain an active catalyst carrier Z1;
[0080] Another part of the mixed powder carrier was immersed twice successively in the solution containing cobalt, in the solu...
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