A kind of method of organosilicon waste water treatment
A wastewater treatment and organosilicon technology, which is applied in water/sewage treatment, water/sewage multi-stage treatment, oxidized water/sewage treatment, etc. problem, to achieve the effect of COD reduction, easy operation and stable operation
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Embodiment 1
[0019] Example 1: organic silicon wastewater raw water COD 1200mg / L, pH 1.1; add lime to adjust the pH value of the wastewater to 8.5, and carry out precipitation to remove some organic matter; add NaOH alkali to the clear liquid after precipitation to adjust the pH to 11.8, and heat to 60°C, carry out the polymerization of organosilicon monomers, the polymerization time is 12hr, and then filter; the filtered waste water continues to be at 60°C, add acid to control pH3.0, and add 1.0kg of ferrous sulfate and 20kg of 27.5 per ton of waste water % hydrogen peroxide and other chemical oxidation treatment for 5 hours, the COD of the treated wastewater was reduced to 165mg / L.
Embodiment 2
[0020] Example 2: organic silicon wastewater raw water COD 1800mg / L, pH0.5; add lime to adjust the pH value of the wastewater to 7.0, and carry out precipitation to remove part of the organic matter; add NaOH and KOH to the supernatant after precipitation to adjust the pH to 11.5, and heat At 80°C, carry out the polymerization of organosilicon monomers, the polymerization time is 5hr, and then filter; the filtered waste water continues to be at 80°C, add acid to control pH4.0, and add 1.0kg of ferrous sulfate and 25kg of per ton of waste water 27.5% hydrogen peroxide, etc. were subjected to chemical oxidation treatment for 6 hours, and the COD of the treated wastewater was reduced to 204mg / L.
Embodiment 3
[0021] Example 3: organic silicon wastewater raw water COD 1600mg / L, pH 0.9; add lime to adjust the pH value of the wastewater to 7.5, and carry out precipitation to remove some organic matter; add NaOH and KOH to the supernatant after precipitation to adjust the pH to 12.0, and heat At 70°C, carry out the polymerization of organosilicon monomers, the polymerization time is 5hr, and then filter; the filtered waste water continues to be at 70°C, add acid to control pH3.5, and add 1.0kg ferrous sulfate and 25kg per ton of waste water 27.5% hydrogen peroxide, etc. were subjected to chemical oxidation treatment for 5 hours, and the COD of the treated wastewater was reduced to 210mg / L.
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