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Treatment method of non-ferrous metal smelting wastewater

A technology of non-ferrous metals and treatment methods, applied in the field of simultaneous removal of various pollutants, can solve the problems of electro-flocculation electrode corrosion, high treatment cost, complex components, etc. simple craftsmanship

Pending Publication Date: 2022-07-29
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] However, the treatment of non-ferrous metal smelting wastewater by electrochemical technology usually faces the following problems: (1) Non-ferrous smelting wastewater contains a variety of pollutants with complex components, among which heavy metals and organic matter are often in complex forms, which makes it relatively difficult to treat by electrochemical technology alone Larger and relatively low treatment efficiency, it is difficult to simultaneously remove multiple pollutants up to the standard; (2) Electrocoagulation electrodes are severely corroded, resulting in high treatment costs during actual operation

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  • Treatment method of non-ferrous metal smelting wastewater

Examples

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Embodiment 1

[0052] Take tungsten smelting wastewater from a tungsten smelting plant in Jiangxi. The pH value of the wastewater is 3.4, the NaCl content is 15g / L, the COD is 336mg / L, the ammonia nitrogen is 73mg / L, the fluoride is 85mg / L, and the total phosphorus is 13mg / L. , The total arsenic is 4.4mg / L, and the concentration of related pollutants exceeds the requirements of the national standard "Comprehensive Wastewater Discharge Standard 8978-1996" (COD<100mg / L, ammonia nitrogen <15mg / L, fluoride <10mg / L, Total phosphorus <0.5mg / L, total arsenic <0.5mg / L).

[0053] Preprocessing:

[0054] First, 1 g / L of lime was added to the waste water for pretreatment, and the pH of the waste water was adjusted to 9.5, followed by sedimentation and solid-liquid separation. After pretreatment, the NaCl content of wastewater was 15g / L, COD was 288mg / L, ammonia nitrogen was 70mg / L, fluoride was 28mg / L, total phosphorus was 3.8mg / L, and total arsenic was 2.5mg / L. The pretreated wastewater is then sent...

Embodiment 2

[0062] Take tungsten smelting wastewater from a tungsten smelting plant in Jiangxi. The pH value of the wastewater is 3.4, the NaCl content is 15g / L, the COD is 336mg / L, the ammonia nitrogen is 73mg / L, the fluoride is 85mg / L, and the total phosphorus is 13mg / L. , The total arsenic is 4.4mg / L, and the concentration of related pollutants exceeds the requirements of the national standard "Comprehensive Wastewater Discharge Standard 8978-1996" (COD<100mg / L, ammonia nitrogen <15mg / L, fluoride <10mg / L, Total phosphorus <0.5mg / L, total arsenic <0.5mg / L).

[0063] First, 1 g / L of lime was added to the wastewater for pretreatment, and the pH of the wastewater was adjusted to 9.5, followed by sedimentation and solid-liquid separation. After pretreatment, the NaCl content of wastewater was 15g / L, COD was 288mg / L, ammonia nitrogen was 70mg / L, fluoride was 28mg / L, total phosphorus was 3.8mg / L, and total arsenic was 2.5mg / L. The pretreated wastewater is then sent to an electrochemical syst...

Embodiment 3

[0066] Take tungsten smelting wastewater from a tungsten smelting plant in Jiangxi. The pH value of the wastewater is 2.5, the NaCl content is 12g / L, the COD is 196mg / L, the ammonia nitrogen is 45mg / L, the fluoride is 156mg / L, and the total phosphorus is 21mg / L. , The total arsenic is 6.7mg / L, and the concentration of relevant pollutants exceeds the requirements of the national standard "Comprehensive Wastewater Discharge Standard 8978-1996" (COD<100mg / L, ammonia nitrogen <15mg / L, fluoride <10mg / L, Total phosphorus <0.5mg / L, total arsenic <0.5mg / L).

[0067] First, 1.5 g / L of tungsten smelting slag was added to the wastewater for pretreatment, and the pH of the wastewater was adjusted to 10.0, followed by sedimentation and solid-liquid separation. After pretreatment, the NaCl content of wastewater was 12g / L, COD was 180mg / L, ammonia nitrogen was 45mg / L, fluoride was 23mg / L, total phosphorus was 2.4mg / L, and total arsenic was 1.7mg / L. The pretreated wastewater is then sent to ...

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Abstract

The invention belongs to the field of wastewater treatment, and particularly relates to a treatment method of non-ferrous metal smelting wastewater, which comprises the following steps: regulating the non-ferrous metal smelting wastewater to pre-treat at the pH value of 9-11, and separating to obtain pre-treated wastewater; the pretreated wastewater is subjected to electrochemical oxidation treatment, and a metal M salt solution is continuously conveyed to the position between the polar plates and close to the anode end in the treatment process; the metal M salt solution is an aqueous solution in which at least one of ions of Fe and Al is dissolved, and the conveying flow velocity of the metal M salt solution is 2-200mg / (L.min). According to the method, synchronous and efficient treatment of various pollutants in the non-ferrous metal smelting wastewater can be synergistically realized, synergistic interaction can be realized, and in addition, the material and equipment cost can be effectively reduced.

Description

technical field [0001] The invention belongs to the technical field of industrial wastewater treatment, and in particular relates to a method for synchronously removing various pollutants such as organic matter and heavy metals in non-ferrous metal smelting wastewater. Background technique [0002] In the smelting process of non-ferrous metals, a large amount of waste water containing various pollutants and difficult to treat will be produced. For example, the mainstream process used in tungsten smelting in my country is the "alkali decomposition-ion exchange process". Every ton of APT (ammonium paratungstate) produced by this process will produce 120 to 160 tons of difficult-to-treat wastewater. The wastewater contains salt (NaCl) and contains high Concentration of COD (chemical oxygen demand), ammonia nitrogen, fluoride, phosphorus, arsenic and other pollutants; another example, when the pyrotechnic lead is used, a large amount of flue gas washing wastewater will be produce...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/06C02F103/16
CPCC02F9/00C02F2103/16C02F1/66C02F1/4672C02F1/56C02F1/5263
Inventor 孙伟孟祥松胡岳华蒋晓云丁伟王松林韩海生王艳秀张晨阳曾平邹元焘
Owner CENT SOUTH UNIV