Oil refining alkali dreg waste liquid processing method
A technology for refining alkali residue and alkali residue waste liquid, which is applied in chemical instruments and methods, water/sewage multi-stage treatment, neutralized water/sewage treatment, etc. High content, adverse effects of sewage treatment equipment, etc., to achieve good environmental and economic benefits, reduce COD, avoid random discharge and special treatment effects
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Embodiment 1
[0043] A company's catalytic gasoline alkali residue and liquid hydrocarbon alkali residue mixed alkali residue waste liquid, of which COD is 3.21×10 5 mg / L, Na 2 S (measured in S) is 1.18×10 4 mg / L, mercaptan sulfur (calculated as S) is 1.71×10 4 mg / L, the total sulfide (calculated as S) is 3.12×10 4 mg / L, volatile phenol is 8.07×10 4 mg / L. Using the present invention figure 1 The method shown is processed, first using N 2 and SO 2 Acidification treatment of alkali slag waste liquid with mixed gas to control N 2 and SO 2 The molar ratio of SO is 1:50~10:1, in order to make SO 2 Fully utilized, SO in the mixed gas 2 The concentration gradually decreases with the progress of the acidification reaction, which can be calculated according to the outlet SO of the acidification reactor 2 The concentration is adjusted and controlled, acidified until the pH of the alkali slag waste liquid drops to 2.0.
[0044] During the acidification process, before the pH drops to 10, t...
Embodiment 2
[0050] A company's catalytic gasoline alkali residue and liquid hydrocarbon alkali residue mixed alkali residue waste liquid, of which COD is 2.83×10 5 mg / L, Na 2 S (measured in S) is 1.33×10 4 mg / L, mercaptan sulfur (calculated as S) is 2.03×10 4 mg / L, the total sulfide (calculated as S) is 3.69×10 4 mg / L, volatile phenol is 5.26×10 4 mg / L. Using the present invention figure 1 The method shown is processed, first using N 2 and SO 2 Acidification treatment of alkali slag waste liquid with mixed gas to control N 2 and SO 2 The molar ratio of SO is 1:50~10:1, in order to make SO 2 Fully utilized, SO in the mixed gas 2 The concentration gradually decreases with the progress of the acidification reaction, which can be calculated according to the outlet SO of the acidification reactor 2 The concentration is adjusted and controlled until the pH of the alkali slag waste liquid drops to 4.0.
[0051]During the acidification process, before the pH drops to 9.5, the acidifie...
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