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Treatment device and method for wastewater containing ammonia nitrogen and phosphorus

A treatment device and treatment method technology, applied in water/sewage treatment, oxidized water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of waste residue, high treatment cost, easy scaling and blockage, etc., to achieve Reduced processing costs, simple device structure, and environmentally friendly effects

Inactive Publication Date: 2019-04-19
CENT SOUTH UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although the operating cost of the biological method is low, microorganisms need to be cultivated and domesticated, and the biological treatment occupies a large area and has strict temperature requirements; while the chemical precipitation method and stripping method have high costs and are difficult to meet the standards; the membrane interception method has high requirements for water quality and is easy to accumulate. Scale blockage increases treatment costs; although the electrolytic catalytic oxidation method occupies a small area, the ammonia nitrogen treatment reaction speed, the ammonia nitrogen or total phosphorus index after wastewater treatment can be stably below 0.5mg / L, but the process is difficult to control and the treatment cost High, the cathode material is not corrosion-resistant, and the ammonia nitrogen or total phosphorus indicators are difficult to meet the standards at the same time.
[0004] CN108751325A discloses an ammonia nitrogen wastewater treatment system and ammonia nitrogen wastewater treatment method, CN108793518A discloses an ammonia nitrogen wastewater treatment method and device, CN108249645A discloses an ammonia nitrogen wastewater treatment system, and CN104230061A discloses a ammonia nitrogen wastewater catalytic oxidation treatment method, both It is a device or method that uses electrolysis to treat ammonia nitrogen wastewater. They have common technical defects: the cathode material is not corrosion-resistant, the cost is high, and the electrolytic cell is not completely sealed, causing the generated waste gas to spread outward and pollute the environment.
CN107857426A discloses a comprehensive treatment method for phosphorus-containing wastewater, which is to use potassium permanganate to oxidize organic phosphorus substances in wastewater into inorganic phosphorus, and filter to remove impurities, but the biggest technical defect is high cost
However, the disadvantage is that the process is long, waste residue will be generated, and the waste water needs to be heated to 75°C, which consumes a lot of energy.
However, the disadvantage of the above-mentioned method is that it needs to consume metal iron, aluminum or magnesium, the cost is high, and it can only treat wastewater containing orthophosphate. If the wastewater contains phosphorous acid or hypophosphite, this method cannot handle it, and it cannot Removal of ammonia nitrogen; as for the electrolysis of heavy metal ions, there will also be problems, because the electrolytic method of removing heavy metal wastewater cannot meet the discharge standards, and must be further treated with alkali and chemical precipitation to filter before the discharge can meet the standards

Method used

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  • Treatment device and method for wastewater containing ammonia nitrogen and phosphorus

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Embodiment 1~4

[0065] Such as figure 1 As shown, the device includes a waste water pool 1, a pH value adjustment unit 2, a head tank 3, an electrolyte batching device 4 and an electrolytic catalytic oxidation unit 5; the waste water pool 1 is connected to the pH value adjustment unit 2 through a water pump 1-1 The pH adjustment unit 2 is connected to the head tank 3; the head tank 3 is connected to the electrolyte batching device 4 and the water inlet 5-1 at the bottom of one end of the electrolytic catalytic oxidation unit 5; the electrolyte batching device 4 is connected to The water inlet 5-1 at the lower part of one end of the electrolytic catalytic oxidation unit 5 is connected; the water outlet 5-2 of the electrolytic catalytic oxidation unit 5 is arranged on the upper part of the other end of the electrolytic catalytic oxidation unit 5; the electrolytic catalytic oxidation unit 5 is a sealing device The exhaust port 5-3 at the top of the electrolytic catalytic oxidation unit 5 is conn...

Embodiment 1

[0068] Pump the ammonia nitrogen and phosphorus-containing waste water 1 in the waste water pool 1 into the pH value adjustment unit 2, adjust the pH value of the waste water to 10.1 with calcium hydroxide, and import the alkaline waste water into the high level tank 3 for storage. The tank 3 flows into the electrolyte dosing device 4, adding sodium chloride to prepare an electrolyte solution with a chloride ion concentration of 100g / L, and the remaining part of the alkaline wastewater in the electrolyte solution and the high level tank 3 is 0.03:1 in volume ratio (electrolytic catalytic oxidation The chloride ion concentration of the mixed liquid in the unit is 2.9g / L), and the mixed water inflow is 5m 3 / h, through the water inlet 5-1 at the bottom of one end of the electrolytic catalytic oxidation unit 5, mix and flow into the electrolytic catalytic oxidation unit 5, and the current density at the anode is 35mA / cm 2 , the voltage is 5V, the electrolytic catalytic oxidation ...

Embodiment 2

[0071] Pump the ammonia nitrogen-containing waste water 1 in the waste water pool 1 into the pH adjustment unit 2, adjust the pH value of the waste water to 11.5 with calcium hydroxide, and import the alkaline waste water into the head tank 3 for storage, and then, a part of the alkaline waste water is discharged from the head tank 3 Flow into the electrolyte dosing device 4, add sodium chloride to be mixed with the electrolyte solution with a chloride ion concentration of 130g / L, and the remaining part of the alkaline wastewater in the electrolyte solution and the head tank 3 is mixed at a volume ratio of 0.04:1 (in the electrolytic catalytic oxidation unit) The chloride ion concentration of the liquid is 5.0g / L), and the mixed water intake is 3m 3 / h, through the water inlet 5-1 at the bottom of one end of the electrolytic catalytic oxidation unit 5, mix and flow into the electrolytic catalytic oxidation unit 5, and the current density at the anode is 25mA / cm 2 , the voltage ...

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Abstract

The invention discloses a treatment device and method for wastewater containing ammonia nitrogen and phosphorus. The device comprises a wastewater tank, a pH regulation unit, a high-position tank, anelectrolyte preparation device and an electrolytic catalytic oxidation unit; the wastewater tank is connected with the pH regulation unit through a water pump; the pH regulation unit is connected withthe high-position tank; the high-position tank is connected with the electrolyte preparation device and a water inlet in the lower portion of one end of the electrolytic catalytic oxidation unit; theelectrolyte preparation device is connected with the water inlet in the lower portion of one end of the electrolytic catalytic oxidation unit; a water outlet of the electrolytic catalytic oxidation unit is formed in the upper portion of the other end of the electrolytic catalytic oxidation unit. The invention also discloses a treatment method for wastewater containing ammonia nitrogen and phosphorus. The device is simple in structure, resistant to corrosion and convenient to operate; in the method, the emission concentration of ammonia nitrogen is smaller than or equal to 3 mg / L, the emissionconcentration of phosphorus is smaller than or equal to 0.25 mg / L, and the integrated wastewater discharge standard of the Ministry of Environmental Protection is met; the process is simple, the costis low, and no waste gas is emitted.

Description

technical field [0001] The invention relates to a wastewater treatment device and method, in particular to a wastewater treatment device and method containing ammonia nitrogen and phosphorus. Background technique [0002] The smelting or processing of zinc, manganese, tungsten and other metals will produce a large amount of wastewater containing ammonia nitrogen and phosphorus. If it is directly discharged, it will cause eutrophication in a large area of ​​the water body, leading to the deterioration of the water environment and directly threatening human health. In particular, the ammonia nitrogen and phosphorus wastewater discharged by some industries has complex components, strong toxicity, and strong carcinogenicity, thereby further deepening the pollution of water bodies. At the same time, it also brings great difficulties to the water supply project, such as the deterioration of water quality, the formation of biofouling to block pipes and equipment, and the impact of ...

Claims

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Application Information

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IPC IPC(8): C02F1/461C02F1/72B01D53/18C02F101/16C02F101/10
CPCB01D53/18C02F1/4672C02F2101/10C02F2101/16
Inventor 楚广银瑰夏邵峰楚盛
Owner CENT SOUTH UNIV
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