A kind of highly stable benzene hydrogenation cyclohexene catalyst and its preparation method and application
A high stability, catalyst technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve the difficulty of precious metal recovery, catalyst salt difficulty, benzene conversion rate lower problem
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Embodiment 1
[0026] Embodiment 1 (if there is no special note below, the percentages are all percentages by weight)
[0027] The preparation steps of a kind of catalyst of the present invention are as follows:
[0028](1) Take 1 mole of ethyl orthosilicate and 20 moles of tetrabutyl titanate, mix them slowly and drop them into 100 liters of nitric acid solution with a pH value of 2 at 35°C, stir rapidly, and carry out hydrolysis. After completion, continue to stir for 20 minutes, let stand for aging for 4 hours, separate out the solid, dry at 110°C for 8 hours, and bake at 580°C for 3 hours to obtain a molar ratio of silicon dioxide to titanium dioxide of 1:20 and a specific surface area of 506m 3 / g, the pore volume is 0.71cm 3 / g of silica and titania composite oxide.
[0029] (2) Take 400 grams of boric acid aqueous solution containing 15 grams of boron oxide, and 475 grams of the composite oxide obtained in step (1), fully mix them at room temperature, let stand for 12 hours, dry a...
Embodiment 2
[0032] The preparation method of a catalyst of the present invention is the same as that in Example 1, except that in the silicon dioxide and titanium dioxide composite oxide prepared in step (1), the molar ratio of silicon dioxide and titanium dioxide is 1:5, and the specific surface area is 537m 3 / g, the pore volume is 0.68cm 3 / g; (2) The amount of boric acid used in the step is different; (3) The zinc-containing compound used in the step is zinc nitrate, and the content is different. A catalyst of the present invention was obtained, coded as E-2, its composition is shown in Table 1, and the reaction results of benzene partial hydrogenation to cyclohexene are shown in Table 2.
Embodiment 3
[0034] The preparation method of a catalyst of the present invention is the same as that in Example 1, except that in the silicon dioxide and titanium dioxide composite oxide prepared in step (1), the molar ratio of silicon dioxide and titanium dioxide is 1:10, and the specific surface area is 637m 3 / g, the pore volume is 0.60cm3 / g; (3) The active metal component used in the step is palladium, and the content is different. A catalyst of the present invention was obtained, coded as E-3, its composition is shown in Table 1, and the reaction results of cyclohexene produced by partial hydrogenation of benzene are shown in Table 2.
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