Method used for preparing iron-based hydrogenation catalyst from iron-containing waste residue raw material
A hydrogenation catalyst and catalyst technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve environmental pollution and other problems, and achieve environmental pollution and improve The effect of factory economic benefits and easy implementation of technology
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Embodiment 1
[0042] Iron-containing waste slag is selected from steel slag, and its composition is TFe content 16.03%, MgO content 1.35%, MnO content 0.95%, TiO 2 Content 3.98%. The steel slag is crushed with a ball mill, and the crushed sample is sieved, and 200 g of a sample with a particle size greater than 150 mesh is taken, added to 0.8 L of 1.0 mol / L dilute sulfuric acid, stirred for 2 hours, and the obtained slurry is filtered to obtain the treated sub iron salt solution.
[0043] Preparation of sodium metaaluminate solution concentration is 15gAl 2 o 3 / L, the caustic ratio is 3.5, a total of 2L, the concentration of the prepared aluminum sulfate solution is 30gAl 2 o 3 / L, a total of 0.5L.
[0044] Gradually add the prepared ferrous sulfate solution into the sodium metaaluminate solution, stir and mix to obtain a suspension of ferrous hydroxide; feed oxygen-containing gas (oxygen content 70v%), and control the temperature of the suspension to 30°C , the oxygen-containing gas...
Embodiment 2
[0049] Other conditions are the same as in Example 1, except that oxygen-containing gas (80v%) is passed into during the preparation of alkaline suspension I, the time of passing through is 3h, citric acid is changed into malic acid, the treatment temperature is 60°C, and the treatment time is 5h. The gel forming temperature is 25° C., the gel forming pH value is 7.5, and the catalyst S-2 with a particle size of 0.4-0.6 mm is prepared.
Embodiment 3
[0051] Other conditions are the same as in Example 1, except that the caustic ratio of sodium metaaluminate solution is 5.0, adding 195m 2 / g, the pore volume is 0.93mL / g, the average pore diameter is 120g of macroporous alumina of 19nm, the addition of citric acid is 12g and the addition of tartaric acid is 12g, the Al in the acidic suspension II 2 o 3 Amount / Al in Alkaline Suspension I 2 o 3 The ratio is 3.8:1, and catalyst S-3 with a particle size of 0.4-0.6 mm is prepared.
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