Process for preparing ethandiol by catalytic hydration of epoxyethane
A technology for catalytic hydration of ethylene oxide and ethylene oxide, which is applied in the fields of hydrolysis preparation, organic chemistry, bulk chemical production, etc., can solve the problem of ethylene glycol catalyst polluting the environment, high ratio of ethylene glycol reaction water, catalyst High reaction water ratio and other issues
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Embodiment 1
[0043] Weigh 12 grams of commercially available niobium oxalate and dissolve it in 40 milliliters of water to make a niobium oxalate solution; weigh 1.8 grams of Zn(NO 3 ) 2 ·6H 2 O was dissolved in 5 ml of 10% dilute nitric acid aqueous solution to make a zinc nitrate solution. Weigh 100 grams of α-alumina, add it to the kneader, then add the niobium oxalate and zinc nitrate solutions prepared above, fully knead with α-alumina to form a mass material, extrude into strips, and place in the air at 150°C. After drying for 2 hours, the catalyst A was obtained by calcining in air at 600°C for 4 hours. The catalyst composition is shown in Table 1.
Embodiment 2
[0045] Weigh 90 grams of α-alumina, 10 grams of titanium dioxide and 12 grams of commercially available niobic acid, respectively, add them to the kneader and mix them well to obtain a mixed material, and weigh 8.1 grams of Cd (NO 3 ) 2 ·6H 2 O was dissolved in 40 ml of 10% dilute nitric acid aqueous solution to prepare a cadmium nitrate solution, which was added to the aforementioned mixture, kneaded and extruded, dried under vacuum at 120°C for 2 hours, and baked at 500°C in an ammonia atmosphere for 4 hours , to obtain catalyst B. The catalyst composition is shown in Table 1.
Embodiment 3
[0047] Catalyst C was prepared by the method of Example 2, except that in the preparation process, the amount of niobium amine complex was 7.6 grams, titanium dioxide was 100 grams, Cd (NO 3 ) 2 ·6H 2 O2.7 g was dissolved in 40 ml of water, dried in air at 100°C for 3 hours, and calcined in air at 200°C for 4 hours. The catalyst composition is shown in Table 1.
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