Preparation method of TiO2/Al2O3 composite carrier
A technology of composite carrier and powder, applied in catalyst carrier, chemical instrument and method, chemical/physical process, etc., can solve problems such as limitation of TiO2 doping amount, and achieve the effect of concentrated pore size distribution
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Embodiment 1
[0012] Take 1 mol of aluminum nitrate and stir it to make it fully dissolved in twice distilled water, add 0.5 mol of dodecylamine in the solution as a template agent, adjust the pH value of the solution with ammonia water, stir well, and heat treat to obtain γ-Al 2 o 3 powder.
[0013] First dissolve butyl titanate in absolute ethanol, stir and add glacial acetic acid as an inhibitor to make it react with butyl titanate to form a chelate, so that butyl titanate is evenly hydrolyzed and the agglomeration of hydrolyzed products is reduced , to obtain a fine and uniform colloidal solution. Add dodecylamine as a template to the absolute ethanol solution of butyl titanate, and add a small amount of aluminum isopropoxide to increase the stability of the sample skeleton structure, and then add deionized water to the sol to make the colloidal particles Form an open skeleton structure. At the same time, slowly add the prepared γ-Al in different proportions 2 o 3 Powders and sols ...
Embodiment 2
[0015] Will (NH 4 ) 6 MO 7 o 24 4H 2 O and (NH 4 ) 2 HPO 4 The mixed solution was added to the TiO 2 , Al 2 o 3 , the TiO prepared in Example 1 2 / Al 2 o 3 Among the three carriers, impregnated, evaporated, dried, and calcined, the MoPO X Catalyst precursors that are active components. Then, in H 2 In the stream, the temperature was programmed to 600 °C for 4 h, and then cooled to room temperature, in 0.5% O 2 N 2 Passivation in flow for 2 h yielded MoP catalysts supported on three different supports for subsequent reactions. Ni is added as an auxiliary agent by impregnation. MoO 3 and NiO 2 The loadings are 18% and 5%, respectively. The evaluation of catalytic performance was carried out on a continuous hydrogenation microreactor with a catalyst loading of 10 mL, and the feed oil was catalytically cracked light gasoline. The reaction conditions are: reaction temperature 100-180°C, reaction pressure 2 MPa, volumetric space velocity 3 h -1 , The volume rat...
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