Method for preparing 1, 3-butanediol through catalytic hydrogenation
A technology for catalytic hydrogenation and butanediol, applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve the problems of reduced reaction selectivity, low hydrogenation activity of Raney nickel, low production efficiency, etc.
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Embodiment 1
[0018] 29.72 g of Ni(NO 3 ) 2 ·6H 2 O, 25.64 g of Na 2 SiO3 9H 2 O was dissolved in 200 ml of distilled water to obtain solution A, and 23.57 g of anhydrous Na 2 CO 3 Dissolve in 200 ml of distilled water to obtain solution B. Under stirring conditions, solution A and solution B were added dropwise to 400 ml of distilled water at the same time to form a green precipitate, and the filter cake obtained by washing and dehydrating the precipitate was dispersed in 200 ml of n-butanol, and the solvent was evaporated at 353 K, and Continue drying at 393 K to obtain a supported metal nickel catalyst precursor. The obtained catalyst precursor is pressed into tablets, sieved, and 60-80 mesh catalyst precursor particles are collected by sieving.
Embodiment 2
[0020] Take 4 g of the pre-reduced metal nickel catalyst particles prepared in Example 2, pack them into a fixed-bed reaction tube, and reduce them in 40 ml / min flowing hydrogen at a temperature of 723 K for 2 h, and then drop the temperature to 333 K. The hydrogen pressure was raised to 3 MPa, and the DMF solution with a mass percentage of 50% of 3-hydroxybutyraldehyde was injected into the reactor with a metering pump, and a trickle bed catalytic hydrogenation reaction was carried out, and the flow rate of the reaction solution was 3 ml / h , the ratio of the amount of hydrogen to 3-hydroxybutyraldehyde is 20:1. The solution after the reaction was collected, and its composition was analyzed by chromatography. It was calculated that the conversion rate of 3-hydroxybutyraldehyde was 86%, and the selectivity of 1,3-butanediol was 88%.
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