Low-salt recycling technology for mechanical cutting emulsified liquid waste
A technology of mechanical cutting and waste liquid, applied in chemical instruments and methods, special compound water treatment, oxidized water/sewage treatment, etc., can solve the problems of low electrochemical separation efficiency, affecting the recycling route, and low wastewater recycling rate. , to achieve the effect of reducing the dosage, reducing the treatment cost and saving the cost of water
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[0047] Example 1
[0048] The emulsified waste liquid comes from the lubricating fluid and cleaning fluid produced by an engine factory in Shanghai. Use 0.4% NaOH solution to adjust the pH to 5, the waste water starts to evaporate into water vapor at a negative pressure (80kPa) and the temperature is 70°C, and the water vapor condenses into a distilled clear liquid, which is collected and discharged into the multi-stage combined advanced oxidation reactor 03; Manganese dioxide (as an ozone catalyst) is added to the reactor, the dosage is 100 mg / L, the dosage of ozone is 1 mg / L, the concentration of introduced ozone is 60 mg / L, and the hydraulic retention time is 30 min; H 2 O 2 The dosage is 0.4%, H 2 O 2 :Fe 2+ = 2:1, the Venturi dosing position is located at 2 / 3 of the reactor elevation; adjust the pH to about 8 with NaOH solution, and enter the vertical flow sedimentation tank 06 for precipitation and separation. See Table 1 for the effluent quality of each process. T...
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[0052] Example 2
[0053] The same procedure was carried out as described in Example 1. The COD of the wastewater is 30000mg / L, the pH is 7, the TOC is 5000mg / L, and the hardness is 300mg / L (in terms of CaCO 3 count). The pH was adjusted to 6 with NaOH solution, and the wastewater began to evaporate at a negative pressure (40kPa) and a temperature of 90°C; the ozone catalyst MnO in the reactor 2 The dosage is 400mg / L, the dosage of ozone is 5mg / L, the concentration of the injected ozone is 120mg / L, and the hydraulic retention time is 90min; H 2 O 2 The dosage is 0.6%, H 2 O 2 :Fe 2+ = 4:1, the Venturi injection position is located 1 / 3 from the bottom of the reactor. The distillation concentration ratio of the final emulsified waste liquid is 19, the recovery rate of clean water is 95%, and the effluent after precipitation has low salt, low concentration and low hardness, which meets the requirements of self-reuse. The effluent from the vertical flow sedimentation tank ...
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[0056] Example 3
[0057] The same operation was performed as described in Example 1, but the treated water was different, and the control conditions and parameters were different. The pH was adjusted to 5.5 with NaOH solution, and the wastewater started to evaporate into water vapor at 60kPa and the temperature was 80℃; the ozone catalyst MnO 2 The dosage is 250mg / L, the dosage of ozone is 3mg / L, the concentration of the injected ozone is 90mg / L, and the hydraulic retention time is 60min; H 2 O 2 The dosage is 0.5%, H 2 O 2 :Fe 2+ =3:1, the dosing position is located at 1 / 2 of the bottom of the multi-stage combined advanced oxidation reactor 03. See Table 3 for the effluent quality of each process. The recovery rate of distilled water from the final emulsified waste liquid reaches 92%, and the effluent after precipitation meets the requirement of self-reuse.
[0058] Table 3 Analysis table of water quality of each process
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