Method for synthesizing 2,6-dihydroxytoluene by using waste acid
A technology of dihydroxytoluene and methylaniline, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of a large amount of waste acid and alkali, high production cost, low production capacity, etc., and reduce emissions , Improve product yield, reduce the effect of three wastes treatment cost
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Embodiment 1
[0047] (1) Preparation of 3-chloro-2-methylaniline sulfate solution: prepare 7kg of sulfuric acid solution with a content of 60%, add 3kg of 3-chloro-2-methylaniline, stir at 30°C for 1 hour until the system is clear; prepare sodium nitrite Aqueous solution: Weigh 1.5kg of sodium nitrite and add it to 3.5kg of water, stir for 0.5h until the system is clarified, feed the two materials at a ratio of 2:1, control the reaction residence time to 10s, and the reaction temperature to 15°C, and the reaction is discharged Then add it directly to 16kg of 40% sulfuric acid aqueous solution (the first batch of reaction is prepared by new concentrated sulfuric acid, and the latter is the sulfuric acid solution extracted by intermediate synthesis, which is used repeatedly for 8 times), keep warm at 55°C for 1.5h, and take a sample to detect the end of the reaction. Add 9 kg of chloroform for extraction, separate the organic phase, which is a chloroform solution of 3-chloro-2 methylphenol, di...
Embodiment 2
[0050] (1) Preparation of 3-chloro-2-methylaniline sulfate solution: prepare 21kg of sulfuric acid solution with a content of 60%, add 9kg of 3-chloro-2-methylaniline, stir at 35°C for 1 hour until the system is clear; prepare sodium nitrite Aqueous solution: Weigh 4.5kg of sodium nitrite and add it to 10.5kg of water, stir for 0.5h until the system is clear, feed the two materials at a ratio of 2:1, control the reaction residence time of 13s, the reaction temperature is 20°C, and the reaction is discharged Then add it directly to 48kg of 40% sulfuric acid aqueous solution (the first batch of reaction is prepared by new concentrated sulfuric acid, and the latter is the sulfuric acid solution extracted by intermediate synthesis, which is used repeatedly for 6 times), keep warm at 50°C for 1.5h, and take a sample to detect the end of the reaction. Add 21kg of toluene for extraction, separate the organic phase, which is a toluene solution of 3-chloro-2-methylphenol, directly enter...
Embodiment 3
[0053] Comparative Experiment
[0054]
[0055] in conclusion
[0056] 1. The production process of the present invention produces 30-40 tons of acidic waste water less than the conventional process for producing one ton of product.
[0057] 2. The post-treatment scheme described in the present invention is not suitable for activated carbon, and the production of one ton of products reduces ~0.5 tons of waste activated carbon slag compared with conventional processes.
[0058] 3. Compared with the conventional process, the process scheme of the present invention can improve the yield by more than 20%.
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