Method for processing papermaking wastewater by advanced oxidation treatment of activating persulfate or monoperoxy-hydrosulfate with ferrous salt
A technology of monoperoxybisulfate and activated persulfate, which is applied in the fields of oxidized water/sewage treatment, chemical instruments and methods, processing wastewater treatment, etc. Complicated and other problems, to achieve the effect of reducing the color of the effluent, easy to dissolve, and simple operation process
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Embodiment 1
[0029] Under normal temperature conditions, take papermaking wastewater with a CODcr of 100 mg / L and a pH of 7.5 in a wastewater storage tank. like figure 1As shown, use a metering pump to pump into the 60L advanced oxidation device at a flow rate of 30L / h, and at the same time pump a certain concentration of oxidant and ferrous sulfate heptahydrate into the water inlet pipe through a peristaltic pump to control the advanced oxidation device. The hydraulic retention time is about 2 hours. Control the influent concentration of sodium persulfate or monoperoxysodium bisulfate to 1 mmol / L and 1.3 mmol / L, respectively. The addition amount of ferrous salt satisfies the concentration under each reaction condition shown in Table 1 respectively. CODcr detection was carried out on the overflow effluent of the advanced oxidation unit. The above-mentioned advanced oxidation device is a reaction device made of 304 stainless steel that can quickly and effectively mix incoming water.
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Embodiment 2
[0034] Under normal temperature conditions, take papermaking wastewater with a CODcr of 100 mg / L and a pH of 7.5 in a wastewater storage tank. like figure 1 As shown, use a metering pump to pump into the 60L advanced oxidation device at a flow rate of 30L / h, and at the same time pump a certain concentration of oxidant and ferrous sulfate heptahydrate into the water inlet pipe through a peristaltic pump to control the advanced oxidation device. The hydraulic retention time is about 2 hours. Control the influent concentration of sodium persulfate in the influent to 1 mmol / L. The influent concentration of ferrous salt is 1.5 mmol / L. The overflow water from the advanced oxidation device flows into the 90L sedimentation device by itself. Before the water inlet of the sedimentation device, according to the different experimental conditions in Table 2, the sodium hydroxide and calcium hydroxide solutions with appropriate concentrations are pumped in at a certain flow rate through t...
Embodiment 3
[0040] Under normal temperature conditions, take papermaking wastewater with a CODcr of 200 mg / L and a pH of 7.5 in a wastewater storage tank. like figure 1 As shown, the metering pump is pumped into the 60L advanced oxidation device at a flow rate of 30 L / h, and at the same time, a certain concentration of oxidant and ferrous sulfate heptahydrate are pumped into the water inlet pipe through the peristaltic pump to control the advanced oxidation. The hydraulic retention time of the unit is about 2 hours. Control the influent concentration of sodium persulfate in the influent to 2 mmol / L. The influent concentration of ferrous salt was 3 mmol / L. The overflow water from the advanced oxidation device flows into the 90L sedimentation device by itself. Before the water inlet of the sedimentation device, according to the different experimental conditions in Table 3, the peristaltic pump is pumped into the appropriate concentration of sodium hydroxide, calcium hydroxide and polychlo...
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