A kind of hydrogenation saturation method of aromatics
A technology for hydrogenation of aromatics and aromatics, applied in the field of hydrogenation and saturation of aromatics, can solve problems such as irregular pore size distribution, and achieve the effects of easy separation and recovery, mild reaction conditions, and long service life
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Embodiment 1
[0022] Catalyst preparation:
[0023] a. Weigh 2.0g of P123 and dissolve it in 40ml of absolute ethanol, add dropwise 3ml of concentrated nitric acid with a mass concentration of 65%, add 4.08g of aluminum isopropoxide under vigorous stirring, and continue stirring for 5 Hour. Then, the resulting solution was evaporated to dryness of ethanol at 60°C and aged for 48 hours to obtain a pale yellow solid. The pale yellow solid was raised from room temperature to 400° C. at a heating rate of 1° C. / min in a muffle furnace, and calcined for 4 hours to obtain supported alumina.
[0024] b. Prepare the Ru precursor solution at 1% by mass, and load Ru on the above-mentioned alumina carrier by the equal volume impregnation method. With a heating rate of 5°C / min and a hydrogen flow rate of 60ml / g, the Ru / Al 2 o 3 Reduction, the reduced state metal catalyst A is obtained. The catalyst has an ordered mesoporous structure, and its pore shape is hexagonal, HR-TEM sees figure 1 .
Embodiment 2
[0028] Except for using the Rh precursor in step b, it was prepared by the same method as described in Example 1 to obtain a reduced metal catalyst B.
Embodiment 3
[0030] Except for using the Pd precursor in step b, it was prepared by the same method as described in Example 1 to obtain a reduced metal catalyst C.
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