Catalyst for preparing monohydric alcohol and dihydric alcohol by hydrogenation of dimethyl substituted 1,3-dioxane, and application
A technology of dioxane and dimethyl, applied in metal/metal oxide/metal hydroxide catalysts, molecular sieve catalysts, reduction preparation of oxygen-containing functional groups, etc., can solve problems such as side reactions
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Embodiment 1
[0011] Example 1 : select the composition as Ni / active SiO 2 / Al 2 o 3 catalyst, the mass ratio of each component is 20 / 20 / 60, 8ml of the catalyst is placed in a quartz reduction tube, under normal pressure, the hydrogen flow rate is 40ml / min, the temperature is raised to 400°C at a heating rate of 2°C / min, and at 400°C Reduction for 6 hours; keep the hydrogen flow at 40ml / min and cool down to normal temperature, and under the protection of hydrogen, transfer the catalyst to the reaction substrate 4,4-dimethyl-1,3-dioxane through degassing In methanol 50% solution, the reaction substrate is 24ml, at hydrogen pressure 4mPa, temperature 140 ℃, reaction time 12 hours, its conversion rate of substrate is 95%, the selectivity of isoamyl alcohol is 92%.
Embodiment 2
[0012] Example 2 : select the composition as Ni / active SiO 2 / Al 2 o 3 catalyst, the mass ratio of each component is 20 / 20 / 60, 8ml of the catalyst is placed in a quartz reduction tube, under normal pressure, the hydrogen flow rate is 40ml / min, the temperature is raised to 400°C at a heating rate of 2°C / min, and at 400°C Reduction for 6 hours; keep the hydrogen flow at 40ml / min and cool down to normal temperature, and under the protection of hydrogen, transfer the catalyst to the deaerated reaction substrate as 4,5-dimethyl-1,3-dioxane In methanol 50% solution, the reaction substrate is 24ml, at hydrogen pressure 4mPa, temperature 140 ℃, reaction time 12 hours, its substrate conversion rate is 85%, the selectivity of isoprene glycol is 85%.
Embodiment 3
[0013] Example 3: The selected composition is Ni / Hβ molecular sieve / Al 2 o 3 catalyst, the mass ratio of each component is 20 / 20 / 60, 8ml of the catalyst is placed in a quartz reduction tube, under normal pressure, the hydrogen flow rate is 40ml / min, the temperature is raised to 400°C at a heating rate of 2°C / min, and at 400°C Reduction for 6 hours; keep the hydrogen flow at 40ml / min and cool down to normal temperature, and under the protection of hydrogen, transfer the catalyst to the reaction substrate 4,4-dimethyl-1,3-dioxane through degassing In methanol 50% solution, the reaction substrate is 24ml, under hydrogen pressure 4mPa, temperature 110 ℃, reaction time 12 hours, its substrate conversion rate is about 100%, the selectivity of isoamyl alcohol is 89%.
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