Catalyzer for industrial production of 1,6-hexamethylene glycol and method of preparing the same
A technology of catalyst and hexanediol, which is applied in the preparation of hydroxyl compounds, chemical instruments and methods, and the preparation of organic compounds, can solve the problems of increased catalyst costs, high equipment requirements, and complicated catalyst processes, and achieve obvious social benefits and Economic benefits, uniform precipitation, good dispersion and thermal stability
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Embodiment 1
[0022]Mix 172.96 kg of copper nitrate and 289.06 kg of zinc nitrate, dissolve it in 486 liters of deionized water to form a mixed salt solution; dissolve 36.22 kg of aluminum hydroxide in 855 liters of deionized water to prepare a suspension; Sodium and 318 kg of sodium carbonate are dissolved in 405 liters of deionized water to form a mixed alkali solution, and the heating temperature is controlled between 50 and 90 ° C, and the mixed salt solution and aluminum hydroxide solution are neutralized with the alkali solution under stirring, and the control The pH value is 7~8, the addition time is controlled for 4 hours, and the precipitate is produced at the same time. The precipitate is filtered, washed, dried at 100°C for 15 hours, granulated, roasted at 200±5°C for 2 hours, and roasted at 500±5°C After 1 hour, add the mixing agent and mix evenly, and finally press into tablets to obtain catalyst I. The contents of copper oxide, zinc oxide and aluminum oxide in catalyst I are 36...
Embodiment 2
[0024] Mix 86.48 kg of copper nitrate and 144.53 kg of zinc nitrate, and dissolve it with 243 liters of deionized water to form a mixed salt solution; dissolve 18.11 kg of aluminum hydroxide in 428 liters of deionized water to prepare a suspension; Sodium and 398 kg of sodium carbonate are dissolved in 315 liters of deionized water to form a mixed alkali solution, and the heating temperature is controlled at 50-90°C, and the mixed salt solution and aluminum hydroxide solution are neutralized with the alkali solution under stirring to control the pH value 7-8, control the addition time for 4 hours, and produce precipitate at the same time, filter and wash the precipitate, dry at 100°C for 15 hours, then granulate, roast at 200±5°C for 2 hours, and roast at 500±5°C for 1 hour hour, then add the mixing agent and mix evenly, and finally press into tablets to obtain the catalyst II. The contents of copper oxide, zinc oxide and aluminum oxide in the catalyst II are 36%, 59% and 15% r...
Embodiment 3
[0026] Mix 136.13 kg of copper nitrate and 82.69 kg of zinc nitrate, dissolve it in 375 liters of deionized water to form a mixed salt solution; dissolve 17.56 kg of aluminum hydroxide in 855 liters of deionized water to prepare a suspension; Sodium and 318 kg of sodium carbonate are dissolved in 405 liters of deionized water to form a mixed alkali solution, and the heating temperature is controlled between 50 and 90 ° C, and the mixed salt solution and aluminum hydroxide solution are neutralized with the alkali solution under stirring, and the control The pH value is 7-8, the addition time is controlled for 4 hours, and the precipitate is produced at the same time. The precipitate is filtered, washed, dried at 100°C for 15 hours, granulated, roasted at 200±5°C for 2 hours, and roasted at 500±5°C After 1 hour, the mixture was added and mixed evenly, and finally pressed into tablets to obtain Catalyst III. The contents of copper oxide, zinc oxide and aluminum oxide in Catalyst I...
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