A kind of solid base catalyst and preparation method thereof
A technology of solid base catalyst and catalyst quality, which is applied in the direction of catalyst carrier, molecular sieve catalyst, chemical instruments and methods, etc., which can solve the problem that the mechanical strength of the catalyst cannot meet the requirements of the catalyst, the low resistance to metal and non-hydrocarbon impurities, and the poor stability of the catalyst at high temperature low yield of dry gas and coke, excellent high-temperature hydrothermal stability, and high conversion rate of heavy oil
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Embodiment 1
[0067] (1) The selection of the silica carrier is the same as that of the comparative example.
[0068] (2) Pore thickening treatment: the silica carrier is first modified by silicon in the gel synthesis stage, and the silica carrier gel is first replaced with ethanol to replace the water in the gel, and then the ethanol solution containing ethyl orthosilicate Replacement, and finally replace the ethanol solution with water, and dry at 120°C to obtain a silicon-modified silica carrier. The mass proportion of the modified component in the silica carrier is 1.5wt%.
[0069] (3) Transition metal doping: Doping the transition metal with manganese, using 0.1mol / L manganese nitrate dilute solution to treat silicon-modified silica carrier, dissolving with dilute sulfuric acid to adjust pH=3, washing and drying to obtain manganese-modified A permanent silica carrier, manganese forms a bond with silicon in the carrier, and the mass ratio of manganese to the silica carrier is 0.25wt%. ...
Embodiment 2
[0074] (1) The silicon-aluminum composite oxide carrier is selected, and the BET specific surface area is measured to be 583m 2 / g, average pore diameter 4.9nm, pore volume 0.68cm 3 / g, mesopore volume 0.65 cm 3 / g, the proportion of mesoporous pore volume (more than 2nm pore volume) is 95.59%.
[0075] (2) Pore thickening treatment: the silicon-aluminum composite oxide carrier is first modified with titanium in the gel synthesis stage, and the silicon-aluminum composite oxide carrier gel is first replaced with ethanol to replace the water in the gel, and then with titanium tetrachloride The ethanol solution was replaced, and finally the ethanol solution was replaced with water, and finally dried at 120°C to obtain a titanium-modified silicon-aluminum composite oxide carrier. The mass ratio of the modified component titanium dioxide to the silicon-aluminum composite oxide carrier was 1.5wt %.
[0076] (3) Transition metal doping: Doping the transition metal with manganese, ...
Embodiment 3
[0081] (1) The silicon-aluminum composite oxide carrier is selected, and the BET specific surface area is measured to be 556m 2 / g, average pore diameter 5.6nm, pore volume 0.72cm 3 / g, mesopore volume 0.71 cm 3 / g, the proportion of mesoporous pore volume (more than 2nm pore volume) is 98.61%.
[0082] (2) The channel thickening treatment is the same as in Example 2.
[0083] (3) Transition metal doping is the same as in Example 2.
[0084] (4) The surface modification treatment is the same as in Example 2.
[0085] (5) The preparation of the microsphere catalyst by the integrated method of spray drying is the same as in Example 2.
[0086] (6) Catalyst evaluation and product analysis are the same as in Comparative Example 1.
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