Preparation method and application of catalyst composition for Fischer-Tropsch synthesis
A catalyst and composition technology, applied in the preparation of liquid hydrocarbon mixtures, chemical instruments and methods, catalysts for physical/chemical processes, etc., can solve the problems of low catalyst activity, reduced gasoline yield, poor stability, etc., and achieve good selectivity. , The effect of high activity and high CO conversion rate
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Embodiment 1
[0063] Preparation of composite carrier 10g: add deionized water to reaction kettle a, stir and add TiO 2 , then add acid to control the pH value of the mixed solution, stir and mix evenly to prepare slurry A; add deionized water to reaction kettle b, stir and add TiO2, stir and mix evenly to prepare slurry B; mix slurry A, B is mixed evenly and left to stand to obtain slurry C; add silica sol to slurry C, stir and mix evenly to obtain slurry D; add ZrCl4 to slurry D, control the temperature and continue to stir and mix evenly to obtain slurry Material E; the slurry E is spray-dried and shaped to obtain a particle powder, and the particle powder is roasted to obtain a composite carrier of the catalyst;
[0064] Weigh 9.00g of copper sulfate and disperse it into 10.71g of silica sol (SiO 2 content of 20.6%), then dried at 130°C in air for 3 hours, and then calcined at 200°C in air. An aqueous solution in which 0.7% of ruthenium chloride was dissolved was immersed in 5 g of th...
Embodiment 2
[0070] Active component precursor becomes 0.3g ruthenium chloride and 0.4g cobalt nitrate solution, other conditions are identical with embodiment 1, use catalyst a2, implement under reaction temperature 270 ℃, in addition, use and embodiment 1 same method to react. Table 1 shows the reaction results and the composition analysis results of the products obtained at this time.
Embodiment 3
[0072] The active component precursor becomes ruthenium chloride, cobalt nitrate and ferric chloride solution, using catalyst a3, the Ru:Co:Fe mass ratio of the active metal in catalyst a3 is 1:1-4:1-3, at the reaction temperature The reaction was carried out in the same manner as in Example 1 except that it was implemented at 280°C. Table 1 shows the reaction results and the composition analysis results of the products obtained at this time.
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