Sullage oxidized coagulated decolorizing process technique

A technology of oxidative coagulation and treatment process, which is applied in water/sewage multi-stage treatment, oxidized water/sewage treatment, water/sludge/sewage treatment, etc. It can solve the problem of poor treatment efficiency, high treatment cost and increased dosage and other problems, to achieve the effect of improving removal efficiency, reasonable treatment costs, and reducing operating costs

Active Publication Date: 2008-03-12
山东环发科技开发有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to its unreasonable process, there are some defects that cannot be ignored in practical applications.
First, due to only adding PAC PAM in the reaction tank, the oxidation ability is insufficient, and the decolorization effect is poor; second, because only PAC PAM is added in the reaction tank, the oxidation ability is insufficient, and the sewage COD removal effect is not ideal; third, due to Only add PAC PAM in the reaction tank, the oxidation capacity is insufficient, in order to improve the treatment efficiency, the amount of dosing is greatly increased, resulting in too high unit treatment cost
Fourth, due to the unreasonable selection of oxidant, the unit treatment operation cost is too high and the treatment efficiency is too poor

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0010] A sewage oxidative coagulation decolorization treatment process. The sewage first enters the oxidation decolorization section, and an oxidant is added to the sewage, and then enters the coagulation reactor after 1-180 minutes of oxidation; the coagulant PAC is first added to the coagulation reactor After a full coagulation reaction for 1-60 minutes, the flocculant PAM is added. After a full reaction for 0-20 minutes, the wastewater enters the solid-liquid clarification separator, and passes through the solid-liquid clarification separator. Liquid discharge.

[0011] The oxidant is sodium hypochlorite, and its dosage is 50-20000 PPM.

[0012] The added amounts of the coagulant PAC and the flocculant PAM are 0-2000PPM for the coagulant PAC, and 0-20PPM for the flocculant PAM.

Embodiment 2

[0014] A sewage oxidative coagulation decolorization treatment process, the process is the same as the first embodiment, the difference is:

[0015] The oxidant is calcium hypochlorite, and its dosage is 50-20000 PPM.

Embodiment 3

[0017] An oxidative decolorization coagulation reaction treatment process. The process is the same as that of the first embodiment, but the difference lies in:

[0018] The oxidant is hydrogen peroxide, and the added amount is 50-10000 PPM.

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PUM

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Abstract

The present invention relates to a sewage oxidation coagulation decolorizing treatment technics. The sewage firstly enters an oxidation decoloring section. Added in An oxidant, the sewage enters a mixed coagulation reactor after the oxidation reaction lasting for 1 to 180 minutes; a coagulant PAC is added in the mixed coagulation reactor and after the fully mixed coagulation reacting, a flocculating agent PAM is added in; after fully reacting, the sewage enters a solid-liquor separator and the clear solution after separating solid from liquor is discharged through the solid-liquor separator. The oxidant is an oxidant of sodium hypochlorite, or calcium hypochlorite or peroxide or any combination of the three; the quantities added to are respectively that the sodium hypochlorite and the calcium hypochlorite are respectively 50 to 20000 PPM, and the peroxide is 0 to 10000 PPM. The quantities of the added coagulant PAC and the flocculating agent PAM are respectively that the PAC is 0 to 2000PPM and the PAM is 0 to 20 PPM. The present invention has the advantages of good treatment effect, innocuity of reaction products, no need of secondary treatment and good operation performance. The present invention has a quicker reaction speed under a normal temperature and is convenient to match and join with the front and back treatment technics.

Description

Technical field [0001] The invention relates to a sewage treatment process, in particular to a sewage oxidation coagulation decolorization treatment process. Background technique [0002] The currently used sewage decolorization coagulation treatment system generally adopts the addition of PAC and PAM in the coagulation reaction tank, and the reaction enters the sedimentation tank to separate the mud and water. However, due to its unreasonable technology, there are some defects that cannot be ignored in practical applications. First, because only PAC PAM is added to the reaction tank, the oxidation capacity is insufficient, and the decolorization effect is poor; second, because only PAC PAM is added to the reaction tank, the oxidation capacity is insufficient, and the COD removal effect of sewage is not ideal; third, because Only adding PAC PAM to the reaction tank has insufficient oxidizing capacity. In order to improve the treatment efficiency, the dosage is greatly increased a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04C02F1/72C02F1/52
Inventor 彭吉成
Owner 山东环发科技开发有限公司
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