Method for preparing methyl-2-buten-1-ol from 3-methylcrotonaldehyde by selective hydrogenation
A technology of prenyl aldehyde and prenol, applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve the problem of high reaction temperature and pressure, high price and low space velocity of prenol And other problems, to achieve the effect of good activity stability, long operation time, and reduce production cost
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Embodiment 1
[0027] Mix and stir a certain amount of aluminum nitrate, zinc tetrachloride and deionized water evenly to obtain an impregnation solution containing Al-Zn; add a certain amount of α-CeO2 carrier to the above impregnation solution, let it stand for aging at room temperature for 24 hours, and then pass through Drying at 80°C for 4h, calcining at 700°C for 4h, to obtain Catalyst I;
[0028] The catalyst precursor is reduced, the reduction temperature is 400°C, the reduction time is 10h, the hydrogen content in the hydrogen-containing atmosphere is 15% by volume, and the volume space velocity of the hydrogen-containing atmosphere is 2000h -1 , to obtain catalyst I. By adjusting the amount of active component and carrier, the composition of catalyst I is: Al content 11.5% by weight, Zn content 9.3% by weight, α-CeO2 content 79.2% by weight.
Embodiment 2
[0030] Mix and stir a certain amount of aluminum nitrate, zinc tetrachloride and deionized water evenly to obtain an impregnating solution containing Al-Zn; add a certain amount of gamma-CeO2 carrier to the above impregnating solution, let it stand for aging at room temperature for 24 hours, and then pass through Drying at 80°C for 4h, and calcining at 700°C for 4h to prepare the catalyst precursor;
[0031] The catalyst precursor is reduced, the reduction temperature is 400°C, the reduction time is 10h, the hydrogen content in the hydrogen-containing atmosphere is 15% by volume, and the volume space velocity of the hydrogen-containing atmosphere is 2000h -1 , to obtain Catalyst II. By adjusting the amount of active components and supports, the composition of the catalyst II is: the content of Al is 13.2% by weight, the content of Zn is 8.8% by weight, and the content of γ-CeO2 is 78% by weight.
Embodiment 3
[0033] Mix and stir a certain amount of aluminum nitrate, zinc tetrachloride and deionized water evenly to obtain an impregnating solution containing Al-Zn; add a certain amount of gamma-CeO2 carrier to the above impregnating solution, let it stand for aging at room temperature for 24 hours, and then pass through Drying at 80°C for 4h, and calcining at 700°C for 4h to prepare the catalyst precursor;
[0034] The catalyst precursor is reduced, the reduction temperature is 400°C, the reduction time is 10h, the hydrogen content in the hydrogen-containing atmosphere is 15% by volume, and the volume space velocity of the hydrogen-containing atmosphere is 2000h -1 , to obtain catalyst III. By adjusting the amount of active components and supports, the composition of the catalyst III is as follows: the content of Al is 8.6% by weight, the content of Zn is 12.1% by weight, and the content of γ-CeO2 is 79.3% by weight.
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