Method for treating high-concentration mixed organic wastewater by using chromium-containing waste liquid
A technology for organic wastewater and waste liquid treatment, applied in separation methods, chemical instruments and methods, neutralized water/sewage treatment, etc., can solve problems such as deterioration of the environment, accumulation of organic toxic substances, carcinogenicity, etc., and achieve the effect of reducing waste of resources
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Embodiment 1
[0018] Example 1: The COD of pharmaceutical wastewater from a pharmaceutical factory is 150,000 mg / L, and the main components are high molecular organic substances. Add 6L of 0.85 mol / L chromium-containing waste liquid, and react for 4 hours at 90°C and an acidity (calculated as sulfuric acid) of 0.6mol / L. The acidic organic gas in the reaction process is absorbed by sodium hydroxide solution, and the reaction is completed. Sodium hydroxide solution is used to neutralize pressure filtration, chromium hydroxide is recycled, and the filtrate and tail gas treatment liquid are subjected to anaerobic and contact oxidation biochemical treatment. The total chromium content in the discharged water is 0.35mg / L, the cod is 89.5mg / L, and the ammonia nitrogen is 10.25 mg / L, and other indicators have reached the national first-class discharge water discharge standard.
Embodiment 2
[0019] Example 2: The COD of wastewater from an aniline manufacturer is 85000 mg / L, the ammonia nitrogen is 278.89 mg / L, and the main component is aniline. Add 5L of 0.85 mol / L chromium-containing waste liquid, and react for 5 hours at 85°C and an acidity (calculated as sulfuric acid) of 0.75 mol / L. The acidic organic gas in the reaction process is absorbed by sodium hydroxide solution, and the reaction is completed. Sodium hydroxide solution is used to neutralize pressure filtration, chromium hydroxide is recycled, and the filtrate and tail gas treatment liquid are subjected to anaerobic and contact oxidation biochemical treatment. The total chromium content in the discharged water is 0.43mg / L, the cod is 92.7mg / L, and the ammonia nitrogen is 13.25 mg / L, and other indicators have reached the national first-class discharge water discharge standards.
Embodiment 3
[0020] Example 3: The COD of the still liquid in a hazardous waste recovery unit is 22350 mg / L, the ammonia nitrogen is 192.75 mg / L, and the composition is complex. Add 4L of 0.54mol / L chromium-containing waste liquid, react for 3 hours at 95°C and acidity (calculated as sulfuric acid) 0.05mol / L, and react for 3 hours. The acidic organic gas in the reaction process is absorbed by sodium hydroxide solution, and the reaction is completed. Sodium hydroxide solution is used to neutralize pressure filtration, chromium hydroxide is recycled, and the filtrate and tail gas treatment liquid are subjected to anaerobic and contact oxidation biochemical treatment. The total chromium content in the discharged water is 0.22mg / L, the cod is 74.5mg / L, and the ammonia nitrogen is 3.24. mg / L, and other indicators have reached the national first-class discharge water discharge standards.
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