Gallic acid and clean and efficient production process thereof
A technology of gallic acid and process technology, which is applied in the field of gallic acid production process, can solve the problems of large environmental pollution and high loss of gallic acid, etc., and achieve the effects of improving economic benefits, increasing yield, and high-efficiency production
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Embodiment 1
[0014] 2. Lead the waste liquid generated in the production of gallic acid into the waste liquid adjustment pool, and use the N-503 (N,N-bis-(1-methylheptyl)acetamide) methyl butanone solution with a mass fraction of 40% as The ratio of extraction agent, N-503 methyl butanone solution and waste liquid is 1:8, and three-stage countercurrent extraction of gallic acid in the waste liquid is carried out. After extraction, excess 18% NaOH solution is used for back extraction to generate gallic acid Return to 1 after sodium acid, and regenerate N-503 methyl butanone solution at the same time.
[0015] The waste liquid after the three-stage countercurrent extraction is combined with other domestic wastewater and enters the pH adjustment tank. After adding a small amount of lime milk, it undergoes microbial hydrolysis acidification and EGSB anaerobic reaction. After preliminary precipitation in the primary sedimentation tank, it enters the aerobic tank for biological contact oxidation....
Embodiment 2
[0019] 2. Lead the waste liquid generated in the production of gallic acid into the waste liquid adjustment tank, and use the N-503 (N,N-bis-(1-methylheptyl)acetamide) methyl butanone solution with a mass fraction of 45% as The ratio of extraction agent, N-503 methyl butanone solution and waste liquid is 1:9, and three-stage countercurrent extraction of gallic acid in the waste liquid is carried out. After the extraction, excess 20% NaOH solution is used for back extraction to generate gallic acid Return to 1 after sodium acid, and regenerate N-503 methyl butanone solution at the same time.
[0020] The waste liquid after the three-stage countercurrent extraction is combined with other domestic wastewater and enters the pH adjustment tank. After adding a small amount of lime milk, it undergoes microbial hydrolysis acidification and EGSB anaerobic reaction. After preliminary precipitation in the primary sedimentation tank, it enters the aerobic tank for biological contact oxidat...
Embodiment 3
[0024] 2. Lead the waste liquid generated in the production of gallic acid into the waste liquid adjustment tank, and use the N-503 (N,N-bis-(1-methylheptyl)acetamide) methyl butanone solution with a mass fraction of 50% as The ratio of extractant, N-503 methyl butanone solution and waste liquid is 1:10, and three-stage countercurrent extraction of gallic acid in the waste liquid is carried out. After extraction, excess 17% NaOH solution is used for back extraction to generate gallic acid Return to 1 after sodium acid, and regenerate N-503 methyl butanone solution at the same time.
[0025] The waste liquid after the three-stage countercurrent extraction is combined with other domestic wastewater and enters the pH adjustment tank. After adding a small amount of lime milk, it undergoes microbial hydrolysis acidification and EGSB anaerobic reaction. After preliminary precipitation in the primary sedimentation tank, it enters the aerobic tank for biological contact oxidation. , A...
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