Treatment method of lead-containing wastewater

A treatment method and technology for wastewater, which can be used in water/sewage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., and can solve problems such as poor selectivity, oxidation failure, and small treatment capacity.

Inactive Publication Date: 2012-05-30
CHANGZHOU YAHUAN ENVIRONMENTAL PROTECTION TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The chemical precipitation method has simple equipment, convenient operation, and good treatment effect. At present, it is widely used in the treatment of high-concentration and large-flow lead-containing wastewater, but the cost is high, the treatment capacity is small, the selectivity is poor, the sludge volume is large, and the sludge is not easy to process. Disposal, easy to cause secondary pollution
The ion exchange method has the advantages of small footprint, convenient management, high lead ion removal rate, and proper treatment can make the regeneration liquid be recycled as a resource, which will not cause secondary pollution to the environment, but the one-time investment is large and the operating cost is high. Susceptible to pollution or oxidation failure, frequent regeneration, and certain difficulties in regeneration
The electrolysis process is mature, has a high removal rate, no secondary pollution, and the precipitated heavy metals can be recycled. It has strong adaptability to the change of wastewater quality an...

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0030] Add LMS-2 with a volume ratio of 4% and P507 with a volume ratio of 5% to kerosene with a volume ratio of 91%, and stir at a speed of 150r / min for 10min to obtain a membrane phase; Volume, the concentration is that the citric acid solution of 1mg / L is slowly added in the film phase, stirs 20min with the speed of 500r / min, makes the water-in-oil type emulsion; / L of wastewater, the dosage of the emulsion is 10mg / L, the pH of the wastewater is 5.5, and it is stirred at a speed of 1000r / min for 30min. The ion concentration dropped to 0.01mg / L, and the lead removal rate reached 99.96%.

example 2

[0032] Span 80 with a volume ratio of 4% and TBP with a volume ratio of 5% were respectively added to n-heptane with a volume ratio of 91%, and stirred at a speed of 100r / min for 10min to obtain a membrane phase; Equal volume, the citric acid solution that concentration is 1mg / L slowly joins in the membrane phase, stirs 20min with the speed of 600r / min, makes the water-in-oil type emulsion; In the 200mg / L wastewater, the dosage of the emulsion is 10mg / L, the pH of the wastewater is 5.5, stirred at a speed of 1000r / min for 40min, and allowed to stand for stratification. The lead ion concentration dropped to 0.02mg / L, and the lead removal rate reached 99.99%.

example 3

[0034] Add span 80 with a volume ratio of 4% and dithizone with a volume ratio of 6% to kerosene with a volume ratio of 90%, and stir at a speed of 130r / min for 10min to obtain a membrane phase; Equal volume, the sulfuric acid solution that concentration is 1mg / L slowly joins in the membrane phase, stirs 20min with the speed of 650r / min, makes the water-in-oil type emulsion; / L of waste water, the dosage of emulsion is 18mg / L, the pH of waste water is 5.0, stirred at a speed of 1200r / min for 40min, standing for stratification, the emulsion obtained after stratification is demulsified by high-voltage electric field, and the discharged waste water is lead The ion concentration dropped to 0.08mg / L, and the lead removal rate reached 99.98%.

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PUM

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Abstract

The invention discloses a treatment method of lead-containing wastewater. The treatment method sequentially comprises the steps of: (1) respectively adding a membrane surfactant at a volume ratio of 3%-5% and a flowing carrier at the volume ratio of 4%-10% to a membrane solvent at the volume ratio of 85%-93% and stirring at a low speed for 10-15 min to prepare a membrane phase; (2) slowly adding an internal water phase medicament having the same volume as the membrane phase to the membrane phase and stirring at a high speed for 10-30 min to prepare a water-in-oil type emulsion; and (3) adding the prepared emulsion to the wastewater at a lead concentration of 10-1000 mg/L until the pH of an external water phase is 3.0-5.5, standing for laying after stirring at a high speed for 30-60 min, breaking the emulsion obtained after the layering through a high-voltage electric field, and separating out an oil phase and an internal water phase, wherein the discharged water can reach the national discharge standard. The treatment method of the lead-containing wastewater disclosed by the invention is fast, efficient, energy-saving and free from phase change, purifies water quality, gathers and recycles heavy metal ions and has simple equipment, convenient operation, a lead removal rate of more than 99.9% and unprecedented application foreground in the field of heavy metal wastewater treatment.

Description

technical field [0001] The invention relates to a treatment method for lead-containing waste water, which relates to the removal of lead in waste water in industries such as storage battery production, ore dressing, petroleum processing, lead smelting, and recycling of waste lead-acid storage batteries, and belongs to the field of waste water treatment in environmental protection. Background technique [0002] Lead is a widely distributed element in nature and one of the elements commonly used in industry. It mostly exists in the form of sulfide in nature, and only a small amount is in the state of metal, and often coexists with zinc, copper and other elements. Lead and its compounds are non-degradable environmental pollutants, which can flow into the environment in large quantities through waste water, waste gas, and waste residues, and directly or indirectly enter the human body through the food chain, soil, water, and air, causing damage to the hematopoietic system, causin...

Claims

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Application Information

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IPC IPC(8): C02F1/62
Inventor 雷春生雷思宇金利军
Owner CHANGZHOU YAHUAN ENVIRONMENTAL PROTECTION TECH
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