Recycling treatment method for low-concentration amide type wastewater
A treatment method and technology of amide compounds, applied in water/sewage treatment, chemical instruments and methods, degassed water/sewage treatment, etc., can solve the problems of large impact on biochemical systems, large amounts of calcium salt precipitation, and low reuse value , to achieve the effect of reducing treatment cost, simple operation and reducing pollution
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Embodiment 1
[0025] Take 300L of low-concentration DMF (DMF mass fraction 1.87%) production wastewater, the COD of the wastewater is 8600mg / L, and the TN is 4868mg / L. Adjust the pH of the wastewater with sodium hydroxide. The molar ratio of NaOH to DMF is 1.2:1. At this time, the pH of the solution is 12.9. Then, it is alkaline hydrolyzed at 60°C for 2 hours. The DMF content in the wastewater is 0.0008%.
[0026] Cool the wastewater after alkaline hydrolysis and transfer it to the stripping tower to separate dimethylamine, and control the gas-liquid ratio to 3000:1. The gas from the stripping tower is separated by a cyclone separator and then enters the absorption spray tower for secondary spraying Absorption, the primary spray uses condensed water, the secondary spray uses waste hydrochloric acid, and the concentration of waste hydrochloric acid is 10wt%. After the secondary spray absorption, the TVOCs at the air outlet are 0. The TN content of the waste water after stripping was detecte...
Embodiment 2
[0029] Take 300kg of DMAC (DMAC mass fraction 1.98%) production wastewater, the COD of the wastewater is 8762mg / L, and the TN is 4983mg / L. Adjust the pH of the wastewater with sodium hydroxide. The molar ratio of NaOH to DMAC is 1.3:1. At this time, the pH of the solution is 13.4. Then, it is alkaline hydrolyzed at 40°C for 2 hours. The content of DMAC in the wastewater is 0.0007%.
[0030] The waste water after alkali hydrolysis is lowered to room temperature, and then transferred to the stripping tower to separate dimethylamine, and the gas-liquid ratio is controlled to be 3500:1. The gas from the stripping tower is separated by a cyclone separator and then enters the absorption spray tower for secondary purification. Spray absorption, the primary spray uses condensed water, the secondary spray uses waste hydrochloric acid, and the concentration of waste hydrochloric acid is 15wt%. After the secondary spray absorption, the TVOCs at the air outlet are 0. The TN content of th...
Embodiment 3
[0033]Take 250kg of low-concentration DMF production wastewater. The DMF content in the wastewater is 1.89%, the COD is 8762mg / L, and the TN is 4983mg / L. Adjust the pH of the wastewater with sodium hydroxide. The molar ratio of NaOH to DMF is 1.25:1. At this time, the pH of the solution is 13.2. Then, it is alkaline hydrolyzed at 50°C for 2 hours. The DMF content in the wastewater is 0.0006%.
[0034] The waste water after alkaline hydrolysis is lowered to room temperature, and then transferred to the stripping tower to separate dimethylamine, and the gas-liquid ratio is controlled to be 4000:1. The gas from the stripping tower is separated by a cyclone separator and then enters the absorption spray tower for secondary purification. Spray absorption, the primary spray uses condensed water, the secondary spray uses waste hydrochloric acid, and the concentration of waste hydrochloric acid is 5wt%. After the secondary spray absorption, the TVOCs at the air outlet are 0. The TN c...
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