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Method for waste water treatment by Fenton reaction

A technology for treating wastewater and reaction, which is applied in the field of Fenton reaction to treat sewage, can solve the problems of shortening Fenton reaction time, reducing the amount of Fenton reagent, and high processing costs, and achieve the effects of reducing macromolecular colloid oxidation, prolonging oxidation time, and reducing volume

Active Publication Date: 2011-07-27
徐州美利圆环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method not only does not overcome the aforementioned disadvantages of large amount of Fenton reaction reagents and high processing costs, but also results in higher processing costs due to the addition of a titanium metal catalyst.
[0012] The above-mentioned various improvements to the Fenton reaction do not involve reducing the amount of Fenton reagent and shortening the Fenton reaction time. There is still room for improvement.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Example 1: Take 1000mL of secondary sedimentation water from a pulp mill, sewage property: COD Cr It is 535mg / l, BOD120mg / l, SS is 87mg / l, and chroma is 467. Adjust the pH to around 6.

[0025] Dissolve 520mg of aluminum chloride, 760mg of polyferric sulfate, 360mg of ferrous sulfate and 180mg of 30% concentration hydrogen peroxide, add appropriate amount of water to dissolve, mix well, add the above to the sewage, stir and react for 20 minutes, then add 2mg of PAM coagulant, The reaction was stirred for another 5 minutes and allowed to stand for 15 minutes to separate the supernatant. Determination of COD in effluent Cr , BOD, SS, chroma. The results are shown in Table 1

Embodiment 2

[0029] Example 2: Take 1000mL of secondary sedimentation water from a certain printing and dyeing factory, its sewage property: COD Cr 430mg / l, BOD140mg / l, SS 96mg / l, chroma 937, pH adjusted to about 6.

[0030] Add 860 mg of polyaluminum sulfate, 860 mg of ferric chloride, 400 mg of ferrous sulfate and 360 mg of 30% hydrogen peroxide, add appropriate amount of water to dissolve, mix well, add the above to the above sewage, stir and react for 20 minutes, then add 2 mg of PAM coagulant, The reaction was stirred for another 5 minutes and allowed to stand for 15 minutes to separate the supernatant. Determination of COD in effluent Cr , BOD, SS, chroma. The results are shown in Table 2

Embodiment 3

[0031] Embodiment 3: Take 1000mL of wastewater from a certain pharmaceutical factory, the nature of sewage: COD Cr It is 375mg / l, BOD187mg / l, SS is 54mg / l, chroma is 593, and pH is adjusted to about 6.

[0032] Add 600mg of aluminum sulfate, 500mg of polyferric chloride, 250mg of ferrous chloride and 150mg of 30% hydrogen peroxide, add appropriate amount of water to dissolve, mix well, add the above to the above sewage, stir and react for 20 minutes, then add 2mg of PAM coagulant , stirred for another 5 minutes, and stood still for 15 minutes to separate the supernatant. Determination of COD in effluent Cr , BOD, SS, chroma. The results are shown in Table 3

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PUM

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Abstract

The invention relates to the improvement on Fenton waste water treatment method, which is characterized in that: firstly, an aluminum salt and / or iron salt flocculating agent and a Fenton reagent are fully mixed in a mass ratio of 2.5-4.5:1; and secondary, the mixed medicinal agent is added into waste water to be treated at a concentration of 800 to 3,000ppm to fully react. The method has the advantages that: the characteristic that the Fenton reaction reagent has an excellent oxidizing effect on soluble organic substances and the characteristic that the aluminum salt or / and iron salt flocculating agent has a good flocculating and separation effect on insoluble organic colloids and suspended particles are used; the utilization rate of H2O2 is high; 10 to 30 percent of the dosage of the flocculating agent can be saved; 50 to 80 percent of the dosage of the Fenton oxidizer is saved; the waste water treatment efficiency is improved; the dosage of the flocculating agent is reduced withoutlowering the treatment effect, so the produced sludge is reduced, a high synergy of the aluminum salt and / or iron salt flocculating agent and the Fenton reagent is achieved and advantages that cannotbe achieved by the signal use of the aluminum salt and / or iron salt flocculating agent or the Fenton reagent are achieved; and a new approach for treating waste water by oxidization with Fenton is provided.

Description

technical field [0001] The invention is an improvement to a sewage Fenton (Fenton) treatment method, in particular to a Fenton reaction treatment sewage treatment method with less dosage of chemicals and wide adaptability to acidity. Background technique [0002] The Fenton reaction has a very strong oxidizing ability and can oxidize many kinds of organic matter, so it is used for the treatment of refractory organic wastewater. Usually Fenton reaction, is to directly Fenton reaction reagent (ferrous salt and strong oxidizing agent such as H 2 o 2 or HClO) into the treated water, Fenton oxidation is the ferrous ion reacting with the oxidizing agent in the water to produce strongly oxidized hydroxyl radicals, which oxidize and carbonize the refractory organic matter in the wastewater into degradable small molecules to achieve the degradation effect. Fenton's reagent is directly added, and the ferrous salt that plays a catalytic role in the Fenton's reagent is dissolved in wa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/72C02F1/52
Inventor 苗勇潘文秀王家雷范公明杜郭君
Owner 徐州美利圆环保科技有限公司
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