Technology for producing hydroquinone by hydrolysis of p-aminophenol through continuous method
A technology of p-aminophenol and hydroquinone, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of high energy consumption, large amount of waste water, low production capacity, etc., and achieve reduction of side reactions, Effects of reduced waste water and high yield
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Embodiment 1
[0030] Replace the air in the batching system and hydrolysis reaction device with nitrogen. Add water, 30% hydrochloric acid and p-aminophenol hydrochloride into the batching tank (2), the molar ratio of p-aminophenol hydrochloride:hydrochloric acid:water is 1:3:100. Through the metering pump (3), the hydrolyzed raw material passes through the pipeline mixer (4) at a flow rate of 13Kg / min, passes through the heat exchanger-2 (5), and then heats up to 230°C through the heat exchanger-1 (6). The material feed port at the top of the reactor (7) enters the tower reactor (7). The tower reactor (7) has a volume of 1.5m3 and a diameter-to-height ratio of 10. The reaction temperature is 230°C. At the same time, the circulation pump (8) is used to continuously extract the hydrolyzed liquid at the bottom of the tower and circulate it so that the reaction material stays in the tower for 300 minutes, and the hydrolyzed reaction liquid overflows from the upper part of the tower reactor (7)...
Embodiment 2
[0032]According to the method described in Example 1, the difference is that the controlled hydrolysis reaction time is 200 minutes. During the hydrolysis reaction, the conversion rate of p-aminophenol hydrochloride is 50%. The water phase of the extraction tower (1) is transported from the bottom of the extraction tower to the batching tank (2), and p-aminophenol hydrochloride is added continuously. The additional amount is The transformation amount of p-aminophenol hydrochloride in the reaction scheme. The organic phase of the extraction tower was desolvated and distilled to obtain hydroquinone with a purity of 99.5%, yield: 95%.
Embodiment 3
[0034] According to the method described in Example 1, the difference is that the controlled hydrolysis reaction time is 150 minutes. During the hydrolysis reaction, the conversion rate of p-aminophenol hydrochloride is 40%. The water phase of the extraction tower (1) is transported from the bottom of the extraction tower to the batching tank (2), and p-aminophenol hydrochloride is added continuously. The additional amount is The transformation amount of p-aminophenol hydrochloride in the reaction scheme. The organic phase of the extraction tower was desolvated and distilled to obtain hydroquinone with a purity of 99.5%, yield: 98%.
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