Hydrogenation catalyst, preparation method and application thereof, and hydrogenation reaction method
A hydrogenation catalyst and hydrogenation reaction technology, applied in catalyst activation/preparation, hydrogenation preparation, chemical elements of heterogeneous catalysts, etc., can solve the problems of difficult continuous production and low activity, and achieve high product quality and high catalytic activity. , product quality and stable effect
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preparation example Construction
[0044] According to a second aspect of the present invention, the present invention provides a method for preparing a hydrogenation catalyst, the method comprising the following steps:
[0045] (1) contacting the precipitating agent with a solution containing a nickel compound and a zirconium compound, and separating the solid-phase substance from the mixture obtained by contacting to obtain a precipitate;
[0046] (2) mixing the precipitate with a VIB group metal compound and an aluminum-containing compound, and successively drying, calcining and molding the obtained mixture to obtain a catalyst precursor, wherein the VIB group metal compound is a group VIB metal oxide compounds and / or precursors of Group VIB metal oxides, said aluminum-containing compounds being alumina and / or precursors of alumina;
[0047] (3) contacting the catalyst precursor with a reducing agent under reduction reaction conditions.
[0048] In step (1), the nickel compound and the zirconium compound ar...
preparation example 1
[0103] In this embodiment, the hydrogenation catalyst A is: based on the total amount of the catalyst, the content of nickel element is 30% by weight, the molybdenum oxide (MoO 3 ) content was 5% by weight, the content of zirconia was 20% by weight, and the content of alumina was 45% by weight. Prepared in the following way:
[0104] (1) The aqueous solution containing nickel nitrate and zirconium nitrate and the aqueous solution containing sodium hydroxide and sodium carbonate (the molar ratio of sodium hydroxide: sodium carbonate is 1:2) are co-currently co-currently mixed at 40°C with stirring. Precipitation, controlling the pH value of the end point to be 11, filtering the obtained reaction mixture, and washing the collected solid matter with deionized water 5 times to obtain a nickel-zirconium coprecipitate.
[0105] (2) The nickel-zirconium precipitate is mixed with molybdenum oxide and pseudo-boehmite, slurried, then dried at 120°C for 6 hours, and then calcined at 500...
preparation example 2
[0108] In this preparation example, the hydrogenation catalyst B is: based on the total amount of the catalyst, the content of nickel element is 50% by weight, the content of molybdenum oxide is 0.5% by weight, the content of zirconia is 30% by weight, and the content of alumina is 19.5% by weight . Prepared in the following way:
[0109] (1) Mix an aqueous solution containing nickel chloride and zirconium chloride with an aqueous solution containing potassium hydroxide and sodium carbonate (the molar ratio of potassium hydroxide:sodium carbonate is 1:3) at 60°C with stirring. Flow co-precipitation, controlling the pH value of the end point to be 12, filtering the obtained reaction mixture, washing the collected solid material with deionized water 6 times to obtain nickel-zirconium co-precipitate.
[0110] (2) The nickel zirconium precipitate is mixed with molybdenum oxide and pseudo-boehmite, slurried, then dried at 100°C for 6 hours, then calcined at 400°C for 5 hours, and ...
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