Anthraquinone hydrogenation heterogeneous channel monolithic catalyst and preparation method thereof
An integral catalyst, catalyst technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve the problem of difficult to achieve higher conversion depth, insufficient conversion depth, Problems such as decreased activity and selectivity
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Embodiment 1
[0027] a) Fully mix 5000 grams of aluminum hydroxide dry rubber powder (dry basis 73.6w%), 100 grams of methyl cellulose, 4300 grams of water and 500 grams of 30w% nitric acid solution to form a plastic paste, put the paste Put it into a die with a hole density of 300 / square inch, a height of 10 cm, and an area ratio of opening I and opening II of 1:5, extrude into a multi-channel overall structure, dry at 150°C for 12 hours, and bake at 650°C for 4 hours. Hour, obtain catalyst carrier;
[0028] b) Take a honeycomb-shaped γ-alumina block with a pore size of 300, an area ratio of opening I and opening II of 1:5, and a height of 10 cm, and immerse it in an aqueous solution of 0.5Mol / L palladium chloride at room temperature. Immerse for 5 minutes, blow out the remaining solution in the channel after taking it out, dry at 120°C for 6 hours, bake at 450°C for 2 hours, repeat twice to obtain the catalyst in the oxidation state;
[0029] c) put the oxidized catalyst obtained in step...
Embodiment 2
[0032] The catalyst preparation method is the same as in Example 1, except that the metal type, content, mesh number of the carrier, the area ratio of the upper and lower openings of the carrier channel, and the reduction conditions are different. The reducing agent used is hydrogen, and the reduction conditions are: hydrogen The pressure was 2MPa, the temperature was 300°C, and the catalysts obtained were numbered E-2 for 4 hours. See Table 1 for the specific conditions and reaction results.
Embodiment 3~7
[0034] The catalyst preparation method is the same as that in Example 1, except that the metal species used, the content, the mesh number of the support, the area ratio of the support pore opening I and the opening II, the shape of the support opening, and the reduction conditions are different. The obtained catalyst The numbers are E-3~E-7 respectively, and the specific conditions and reaction results are shown in Table 1.
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