Hydroquinone preparation method
A technology of hydroquinone and p-chlorophenol, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of low recovery rate of manganese resources, serious environmental pollution, and high equipment costs, and achieve recycling The effect of good application effect, low equipment investment and high production cost
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[0025] Example 1
[0026] Put 106.6g of p-chlorophenol, 581.0g of 40% potassium hydroxide, KOH / ZrO into a 1L autoclave 2 Catalyst 10.7g, heated after nitrogen replacement, controlled the reaction temperature at 215°C, reacted for 12 hours, the alkali hydrolyzate was filtered to recover the catalyst, the filtrate was acidified with 35% concentrated hydrochloric acid 430g to pH=2~3. The conversion rate of p-chlorophenol is 98.5% and the selectivity of hydroquinone is 87.1%.
Example Embodiment
[0029] Example 2
[0030] Put 21.3g of p-chlorophenol, 493.9g of 10% potassium hydroxide, NaOH / ZrO into a 1L autoclave 2 The catalyst was 3.0g, after nitrogen replacement, the temperature was raised, the reaction temperature was controlled to 210°C, and the reaction was carried out for 12 hours. The alkali hydrolyzate was filtered to recover the catalyst, and the filtrate was acidified with 35% concentrated hydrochloric acid 93.0g to pH=2~3. The conversion rate of p-chlorophenol was 78.2%, and the selectivity of hydroquinone was 89.4%.
Example Embodiment
[0031] Example 3
[0032] Put 79.9g of p-chlorophenol, 522.9g of 25% potassium hydroxide and Na in a 1L autoclave 2 CO 3 / ZrO 2 The catalyst was 9.7g, after nitrogen replacement, the temperature was raised, the reaction temperature was controlled at 220°C, and the reaction was conducted for 8 hours. The alkali hydrolyzate was filtered to recover the catalyst, and the filtrate was acidified to pH=2~3 with 245.3g of 35% concentrated hydrochloric acid. The conversion rate of p-chlorophenol was 82.4%, and the selectivity of hydroquinone was 90.1%.
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