Method for preparing 1, 6-hexanediol by hydrogenating 1, 6-dimethyl adipate
A technology for the preparation of dimethyl adipate and hydrogen, which is applied in chemical instruments and methods, preparation of hydroxyl compounds, and preparation of organic compounds, etc., can solve the problems of complicated preparation process and poor selectivity of noble metal catalysts, and achieve high catalyst activity, The effect of simplification of separation or purification process and mild reaction conditions
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Embodiment 1
[0029] 20 parts of RuCl 3 2H 2 O, 20 parts SnCl 4 , 5 parts CoCl 2 ·6H 2 O and 1000 parts of γ-Al 2 o 3 Mix, add appropriate amount of ethanol to impregnate for 12h, dry in vacuum and calcined to get Ru-Sn-Co / Al 2 o 3 Catalyst precursor. 20 parts of Ru-Sn-Co / Al 2 o 3 Transfer to an autoclave, then add 100 parts of water as a solvent, replace it with high-purity hydrogen for 3 times, fill it with hydrogen at a pressure of 5.0Mpa, and reduce it for 2 hours at a temperature of 180°C. After cooling, add 100 parts of 1,6-adipic acid Dimethyl ester and 200 parts of methanol were replaced by hydrogen 3 times, filled with hydrogen at a pressure of 5.0Mpa, reacted at a temperature of 220°C for 10 hours, cooled to take out the reaction solution, centrifuged, and analyzed by gas chromatography. The results showed that 1,6-hexanedi The conversion rate of dimethyl ester was 99.5%, and the selectivity of 1,6-hexanediol was 99.5%.
Embodiment 2
[0031] 20 parts of RuCl 3 2H 2 O, 20 parts SnCl 2 , 30 parts CoCl 2 ·6H 2 O and 1000 parts of γ-Al 2 o 3 Mix, add appropriate amount of ethanol to impregnate for 12h, dry in vacuum and calcined to get Ru-Sn-Co / Al 2 o 3 Catalyst precursor. 30 parts of Ru-Sn-Co / Al 2 o 3 Transfer to an autoclave, then add 100 parts of water as a solvent, replace it with high-purity hydrogen for 3 times, fill it with hydrogen at a pressure of 5.0Mpa, and reduce it at a temperature of 180°C for 2 hours. After cooling, add 200 parts of 1,6-adipic acid Dimethyl ester and 200 parts of water were replaced by hydrogen 3 times, filled with hydrogen at a pressure of 3.0MPa, reacted at a temperature of 220°C for 12 hours, cooled to take out the reaction solution, centrifuged, and analyzed by gas chromatography. The results showed that 1,6-hexanedi The conversion rate of dimethyl ester was 99.0%, and the selectivity of 1,6-hexanediol was 98.5%.
Embodiment 3
[0033] 10 parts of RuCl 2 (PPh 3 ) 3 , 15 parts SnO, 5 parts CoCl 2 ·6H 2 O and 1000 parts SiO 2 Mix, add an appropriate amount of 1,4-dioxane to impregnate for 12 hours, stir overnight at room temperature, spin dry, vacuum dry, and calcinate to obtain Ru-Sn-Co / SiO 2 Catalyst precursor. 10 parts of Ru-Sn-Co / SiO 2 Transfer to an autoclave, then add 100 parts of water as a solvent, replace it with high-purity hydrogen for 3 times, fill it with hydrogen at a pressure of 5.0Mpa, and reduce it for 5 hours at a temperature of 100°C. After cooling, add 100 parts of 1,6-adipic acid Dimethyl ester and 100 parts to get 1,4-dioxane, replaced hydrogen 3 times, filled with hydrogen pressure 5.0MPa, reacted at a temperature of 150°C for 10h, cooled and took out the reaction solution, analyzed by gas chromatography, the results showed that 1 , the conversion rate of dimethyl 6-adipate was 79%, and the selectivity of 1,6-hexanediol was 34%.
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