A method for combined treatment of nitrogen-containing organic wastewater and pickling waste liquid
A technology for organic wastewater and pickling waste liquid, applied in chemical instruments and methods, multi-stage water/sewage treatment, oxidized water/sewage treatment, etc., to achieve the effects of recycling, improving removal efficiency, and promoting conversion efficiency
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Embodiment 1
[0030] Such as figure 1 As shown, the corresponding labels of the components in the present invention are as follows: 1 lye pool, 2 pickling waste pool, 3 nitrogen-containing organic waste water pool, 4 homogeneous pool, 5 high-pressure pump, 6 temperature control system, 7 preheating device, 8 first heat exchanger, 9 supercritical water oxidation reactor, 10 second heat exchanger, 11 high temperature and pressure control system, 12 buffer vessel, 13 desalination system, 14 air separation system, 15 brine drying system, 16 Gas-liquid separation device, 17 gas-water heat exchange system, 18 heavy metal recovery device, 19 hot water reuse device.
[0031] The supercritical water oxidation reaction device in the present invention comprises: a heating and temperature control system 6, a preheater 7, a first heat exchanger 8, a supercritical water oxidation reactor 9, a second heat exchanger 10, and a high-temperature pressure control system 11 , buffer container 12, desalination ...
Embodiment 2
[0041] The operation of each component is the same as in Example 1. The reaction conditions in the supercritical water oxidation reactor are: temperature 400°C, pressure 23MPa, reaction time 90 seconds, oxygen partial pressure 3MPa, and supercritical water oxidation technology is used to treat chlorpyrifos production wastewater.
[0042] Influent TOC 4500mg / L, ammonia nitrogen 220mg / L, adding stainless steel pickling and rinsing wastewater, NO 3 - The concentration is 5880mg / L, the total chromium is 156mg / L, the total nickel is 2.6mg / L, the ratio of the dosage of stainless steel pickling and rinsing wastewater to the dosage of chlorpyrifos production wastewater is 0.9, and the pH of the mixed wastewater is adjusted to 6.2. Water oxidation system, TOC removal rate reaches 98.3%, ammonia nitrogen removal rate reaches 90.5%.
Embodiment 3
[0044] The temperature is 400°C, the pressure is 23MPa, the reaction time is 90 seconds, and the partial pressure of oxygen is 3MPa. Supercritical water oxidation technology is used to treat chlorpyrifos production wastewater. Influent TOC 4500mg / L, ammonia nitrogen 220mg / L, adding stainless steel pickling and rinsing wastewater, NO 3 - The concentration is 5880mg / L, the total chromium is 156mg / L, the total nickel is 2.6mg / L, the ratio of the dosage of stainless steel pickling and rinsing wastewater to the dosage of chlorpyrifos production wastewater is 2.4, mix evenly, adjust the pH to 6.2, and pass through supercritical water Oxidation system, TOC removal rate reaches 99.9%, ammonia nitrogen removal rate reaches 99.8%.
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