Method for preparing ethylene glycol and 1,2-propylene glycol by carrying out selective hydrogenolysis on high-carbon polyalcohol
A technology of polyols and ethylene glycol, applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve unfavorable large-scale industrial applications, poor catalyst stability, no conversion rate or yield, etc. problems, achieve good cycle stability, high anti-sintering stability, and low cost
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Embodiment 1
[0027] Weigh 7.1 g copper nitrate trihydrate, 3.08 g nickel nitrate hexahydrate, 3.14 g SiO 2 Xerogel powder and 24.00 g of urea were added to the autoclave, 200 mL of distilled water was added, the autoclave was sealed, the temperature was raised to 100 °C with stirring, and the precipitation reaction was carried out for 2 h. After cooling down to room temperature, it was suction-filtered, washed three times with distilled water and absolute ethanol, dried at 120 °C for 12 h, roasted in a muffle furnace at 400 °C for 3 h, pressed into tablets, ground and sieved (80-100 mesh), A catalyst precursor with mass percentages of 37.3% copper oxide, 12.7% nickel oxide and 50% silicon oxide was obtained. The sieved catalyst precursor was reductively activated in a hydrogen atmosphere at 300 °C for 4 h to obtain the catalyst A provided by the present invention.
Embodiment 2
[0029] Operation is the same as in Example 1, just replace 3.14 g SiO with 3.14 g SBA-15 molecular sieve powder 2 Dry gel powder, the catalyst composition is the same as above, and the catalyst B provided by the present invention can be obtained after reduction and activation.
Embodiment 3
[0031] Weigh 18.96 g of copper nitrate trihydrate, 3.04 g of nickel nitrate hexahydrate, and 3.90 g of 20 wt% acidic silica sol into a round-bottomed flask, add 185 mL of distilled water and stir to dissolve, and dissolve with 10 wt% Na 2 CO 3 The solution was precipitated as a precipitating agent, and the precipitation was completed until pH ~ 10, and the temperature was raised to 80 °C for aging for 4 h, filtered and washed with distilled water until neutral, dried at 120 °C for 12 h, roasted in a muffle furnace at 500 °C for 3 h, and ground Sieve (80-100 mesh) to obtain a catalyst precursor with mass percentages of 80.0% copper oxide, 10.0% nickel oxide and 10.0% silicon oxide. Catalyst C provided by the present invention was obtained by reductively activating the sieved catalyst precursor at 550 °C in a hydrogen atmosphere for 3 h.
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