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Vanadium oxide production industrial wastewater processing method

A technology for industrial wastewater and treatment methods, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc., can solve problems such as high treatment costs, difficult equipment maintenance, and difficult bottom flow slag treatment

Active Publication Date: 2014-09-24
PANZHIHUA IRON & STEEL RES INST OF PANGANG GROUP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, the mainstream production processes of vanadium oxide products are "calcification process" and "sodium process", and there are two corresponding treatment methods for industrial wastewater. The treatment method corresponding to "chemical process" is "evaporative concentration method". Both treatment methods can realize the recycling of wastewater, but both have inevitable shortcomings.
The "milk of lime neutralization method" has low cost, simple process and easy equipment to implement, but it produces a large amount of "neutralization gypsum slag", which is not environmentally friendly
The "evaporative concentration method" has high treatment costs, difficult equipment maintenance, and difficult treatment of the generated underflow slag
Moreover, the above two wastewater treatment methods are single input, without any economic value.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Treat 1 ton of vanadium oxide production industrial wastewater. In the vanadium oxide production industrial wastewater, the content of manganese is 15g / L, the content of ammonium sulfate is 80g / L, the content of vanadium is 0.1g / L, the content of iron is 0.2g / L, phosphorus The content is 0.2g / L, the pH value is 2.5, heat it and keep the wastewater temperature at 85°C, add 1kg FeSO 4 , stirred for 30 minutes, adjusted the pH value of the wastewater to 5 with ammonia water, added 1 kg of calcium oxide, and stirred for 30 minutes. Add 1 kg of activated carbon and 1 kg of manganese dioxide, feed compressed air, and stir for 20 minutes. After iron hydroxide is precipitated, the waste water is filtered to obtain 1 ton of waste water after removal of impurities. The vanadium content in the waste water after removal of impurities is 0.005 g / L, the phosphorus content is 0.005g / L, and the iron content is 0.005g / L. The waste water after impurity removal is passed into the electro...

Embodiment 2

[0031]Treat 1 ton of vanadium oxide production industrial wastewater. In the vanadium oxide production industrial wastewater, the content of manganese is 12g / L, the content of ammonium sulfate is 60g / L, the content of vanadium is 0.2g / L, the content of iron is 0.2g / L, phosphorus The content is 0.1g / L, the pH value is 1.8, heat it and keep the wastewater temperature at 80°C, add 1kg FeSO4, stir for 30 minutes, use ammonia water to adjust the pH value of the wastewater to 5, add 1kg calcium oxide, and stir for 30 minutes. Add 1 kg of activated carbon and 1 kg of manganese dioxide, feed compressed air, and stir for 20 minutes. After iron hydroxide is precipitated, the waste water is filtered to obtain 1 ton of waste water after removal of impurities. The vanadium content in the waste water after removal of impurities is 0.005 g / L, the phosphorus content is 0.005g / L, and the iron content is 0.005g / L. The waste water after impurity removal is passed into the electrolytic cell for e...

Embodiment 3

[0033] Treat 1 ton of vanadium oxide production industrial wastewater. In the vanadium oxide production industrial wastewater, the content of manganese is 10g / L, the content of ammonium sulfate is 40g / L, the content of vanadium is 0.2g / L, the content of iron is 0.2g / L, phosphorus The content is 0.2g / L, the pH value is 2, heat it and keep the wastewater temperature at 75°C, add 1kg FeSO4, stir for 30 minutes, use ammonia water to adjust the pH value of the wastewater to 6, add 1kg calcium oxide, and stir for 30 minutes. Add 1 kg of activated carbon and 1 kg of manganese dioxide, feed compressed air, and stir for 20 minutes. After iron hydroxide is precipitated, the waste water is filtered to obtain 1 ton of waste water after removal of impurities. The vanadium content in the waste water after removal of impurities is 0.005 g / L, the phosphorus content is 0.005g / L, and the iron content is 0.005g / L.

[0034] The waste water after impurity removal is passed into the electrolytic ce...

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Abstract

The invention provides a vanadium oxide production industrial wastewater processing method, vanadium oxide production industrial wastewater contains manganese, vanadium, iron and phosphorus, and the manganese content is 10-15g / L, and the method comprises the following steps: (1) segmented impurity removal and vanadium, iron and phosphorus removal of the vanadium oxide production industrial wastewater to obtain impurity-removed wastewater; and (2) variable electric current electrolysis of the impurity-removed wastewater; wherein the by the impurity removal process, the vanadium content of the impurity-removed wastewater is lower than 0.01g / L, the phosphorus content is lower than 0.01g / L, and the wastewater iron content is less than 0.005g / L. According to the processing method, the processed vanadium oxide production industrial wastewater can be recycled, and has no adverse impact on the quality of products, metal manganese products meeting the national YB / T051-2003DJMnD standard can be recovered, and a certain economic value is produced.

Description

technical field [0001] The invention relates to a method for treating industrial waste water produced by vanadium oxide. Background technique [0002] At present, the mainstream production processes of vanadium oxide products are "calcification process" and "sodium process", and there are two corresponding treatment methods for industrial wastewater. The treatment method corresponding to "chemical process" is "evaporative concentration method". Both treatment methods can achieve wastewater recycling, but both have inevitable shortcomings. The "milk of lime neutralization method" has low cost, simple process, and easy equipment to implement, but it produces a large amount of "neutralization gypsum slag", which is not environmentally friendly. The "evaporative concentration method" has high treatment costs, difficult equipment maintenance, and difficult treatment of the generated underflow slag. And above-mentioned two kinds of waste water treatment methods all are unitary i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/06C25C1/10
Inventor 彭毅孟伟巍陶长元孙朝晖刘作华刘武汉钟国梅叶露卢晓林何文艺申彪吴封
Owner PANZHIHUA IRON & STEEL RES INST OF PANGANG GROUP
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