Treating method and treating apparatus of waste water containing organic material
A treatment method and treatment device technology, applied in water/sewage treatment, water treatment parameter control, neutralization water/sewage treatment, etc., to reduce load and prevent reactivity reduction
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Embodiment 1
[0097] The wastewater with a TOC concentration of 5 mg / L and a calcium ion concentration of 10 mg / L, which is mainly composed of surfactants, is used as raw water and treated with the device shown in Figure 1. First, add EDTA series antiscaling agent (sodium salt of ethylenediaminetetraacetic acid) to raw water, its amount is 5 times weight of the calcium ion concentration of raw water, then, add NaOH to make pH reach 10.5, use RO membrane separation device (Japanese The low-pressure aromatic polyamide type RO membrane "ES-10" manufactured by Todenko) was subjected to RO membrane separation treatment under the conditions of a flow rate of 80 L / h and a recovery rate of 75%.
[0098] After adding hydrogen peroxide in an amount 1.2 times the TOC to RO concentrated water obtained by the RO membrane separation treatment, ozone was added in an amount 10 times the TOC. Then, under the condition of water flow SV10 / h, to the activated carbon tower, and then under the condition of water...
Embodiment 2
[0101] Except that hydrogen peroxide is not added to the RO concentrated water, all the others are treated in the same manner as in Example 1, and the pH, TOC concentration and TOC removal rate of the ozone treated water (the effluent water of the ozone reaction tower), and the effluent water of the activated carbon tower are studied. The pH, TOC concentration and TOC removal rate, and the pH, TOC concentration, and TOC removal rate of the treated water (the effluent water of the ion exchange tower), the results are shown in Table 1.
Embodiment 3
[0103] Except increasing the addition amount of alkali so that the pH of ozone treated water reaches 10, all the other are processed identically with embodiment 1, study the pH, TOC concentration and TOC removal rate of ozone treated water (the effluent water of ozone reaction tower), and The pH, TOC concentration, and TOC removal rate of the effluent water from the activated carbon tower, and the pH, TOC concentration, and TOC removal rate of the treated water (the effluent water from the ion exchange tower), are shown in Table 1.
[0104] RO
[0105] As can be seen from Table 1, according to the present invention, TOC in RO concentrated water can be removed to a high degree.
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