Method for synthesizing ethanol
A technology supported by ethanol and alumina, applied in chemical instruments and methods, preparation of organic compounds, preparation of hydroxyl compounds, etc., can solve the problems of low ethanol selectivity and yield, cumbersome catalyst separation and recovery process, expensive catalysts, etc. Achieve high selectivity and yield
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Embodiment 1
[0018] (1) Preparation of alumina supported palladium catalyst: Weigh 5g α-Al 2 O 3 , Weighing 0.063g Pd(NO 3 ) 2 ·2H 2 O is prepared as an immersion liquid, the solvent is deionized water, and the specific surface area is 15m 2 / g carrier α-Al 2 O 3 Soak in the dipping solution for 10 hours, evaporate the water at 80°C to obtain a solid, then dry the solid at 120°C for 12 hours and calcinate at 400°C for 2 hours to obtain an alumina supported palladium catalyst (Pd / α-Al 2 O 3 ).
[0019] (2) Preparation of dimethyl oxalate: The inner diameter of the stainless steel fixed-bed reactor is 8mm, the amount of the alumina supported palladium catalyst is 2ml, and the catalyst is reduced with 50ml / min CO at 350°C for 2h before use. The raw material gas carbon monoxide and methyl nitrite (wherein, methyl nitrite is prepared according to the document US 4353843) passes through the reactor from top to bottom (the volume ratio of carbon monoxide and methyl nitrite is 1.4:1), the volume of the...
Embodiment 2
[0023] According to Example 1, the alumina supported palladium catalyst, dimethyl oxalate and silica supported copper catalyst were prepared;
[0024] In the ethanol preparation step, the reaction temperature is 280°C, the molar ratio of hydrogen to dimethyl oxalate is 350, and the residence time is 5.7s (under standard conditions). Other conditions are the same as in Example 1. The conversion rate of dimethyl oxalate is 100%. The selectivity of ethanol is 83%, the selectivity of n-propanol is 12%, and the selectivity of isopropanol is 1%.
Embodiment 3
[0026] According to Example 1, the alumina supported palladium catalyst, dimethyl oxalate and silica supported copper catalyst were prepared;
[0027] In the ethanol preparation step, the reaction temperature is 290℃, the residence time is 3s (under standard conditions), other conditions are the same as in Example 2, the conversion rate of dimethyl oxalate is 100%, the selectivity of ethanol is 75%, and the selection of n-propanol The performance is 7% and the selectivity of isopropanol is 5%.
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