High-salinity wastewater advanced oxidation method,industrial waste salt resourceful treatment method, and equipment

A technology for advanced oxidation and high-salt wastewater, which is applied in the fields of oxidized water/sewage treatment, water/sewage treatment, chemical instruments and methods, etc., and can solve the problems of inability to practically solve organic pollutants, high treatment costs, and insufficient incineration, etc. Achieve the effect of improving advanced oxidation efficiency and high reaction efficiency

Active Publication Date: 2020-05-19
NANJING UNIV YANCHENG ENVIRONMENTAL PROTECTION TECH & ENG RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] Industrial waste salt refers to the by-product crystalline salts produced in industrial production. The annual output of waste salt in my country has exceeded 10 million tons. Chemical products, especially waste salt produced in the process of pesticide production contain a large amount of organic matter. If not handled properly, it will directly Leading to the pollution of surface water, groundwater and soil, the waste salt is traditionally landfilled after the harmless treatment by pyrolysis, resulting in a huge waste of resources; however, by degrading the high-salt wastewater and then reusing it In the process of treatment, it is often difficult to degrade the organic matter due to the high salt concentration in the wastewater.
[0003] The prior art of Chinese Patent Application Publication No. CN107185948A discloses a waste salt treatment technology using waste salt thermal desorption unit + evaporation crystallization unit as the main body. Waste salt is heated to 500-650°C under anaerobic conditions for dehydration (100-150°C), organic matter evaporation (150-380°C), cracking (380-600°C) and other reactions. Evaporation cannot actually solve the problem of organic pollutants, and there may also be a problem of air pollution. It is also difficult to completely degrade the organic matter by heating and cracking. The method in the prior art is difficult to effectively remove the organic matter in the waste salt.
The prior art of Chinese Patent Application Publication No. CN107321755A discloses a utilization process including waste salt feeding system, waste salt melting system, tail gas treatment system, molten salt cooling granulation system to treat waste water containing sodium chloride, although for waste salt The treatment effect is better, but it uses the high-temperature flue gas generated by natural gas combustion to burn and incinerate the organic matter in the waste salt during the rising process in the furnace. One is that the incineration of organic matter will cause exhaust gas pollution, and the other is that the treatment cost is high. The temperature is as high as 1200°C, making it difficult to apply it in the actual industry on a large scale
The prior art of Chinese Patent Application Publication No. CN108929708A discloses a combined process of anaerobic pyrolysis carbonization + carbonization particle removal + two-stage membrane acid-base production to treat wastewater containing sodium chloride. The steps for removing organic matter are: in the cracking stage, use The small molecular organics in the waste salt are gasified, and the aromatic ring organics are cracked into hydrogen, carbon monoxide and small molecular organics. The gas products obtained in the cracking stage are collected and sent to the RTO incinerator; the carbonization stage makes the remaining small part of the waste salt unable to be completely The cracked condensed ring substances are carbonized into activated carbon and retained in the residue. Although it has a certain treatment effect on waste salt, the operating cost is high. The waste salt after incineration is agglomerated, and some organic matter remains in the waste salt due to insufficient incineration. In practical application, due to the high chloride ion content of waste salt, when this kind of waste salt is processed in the incineration device, the equipment will be corroded, and the final equipment will be scrapped from time to time. Therefore, simple incineration It is difficult for the waste salt treated by the method to meet the requirements of resource utilization
However, in this prior art, the oxidation efficiency in the treatment step of the advanced oxidation unit still needs to be further improved

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  • High-salinity wastewater advanced oxidation method,industrial waste salt resourceful treatment method, and equipment
  • High-salinity wastewater advanced oxidation method,industrial waste salt resourceful treatment method, and equipment
  • High-salinity wastewater advanced oxidation method,industrial waste salt resourceful treatment method, and equipment

Examples

Experimental program
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Effect test

Embodiment 1

[0060] Such as figure 1 As shown, the waste salt of a certain chemical enterprise first uses a rotary heating furnace for high-temperature pyrolysis, and the waste salt after pyrolysis is dissolved in water to make high-salt wastewater, in which the mass fraction of control salt (sodium chloride) is 23%wt, After testing, compared with the waste water with the same mass fraction of the initial waste salt before pyrolysis, the TOC decreased from the initial 800.8mg / L to 33.1mg / L, and the TN decreased from the initial 40.3mg / L to 8.2mg / L , and then pass the wastewater through the pretreatment unit to remove impurities.

[0061] First, add hydrochloric acid to the reaction kettle to adjust the pH of the solution to 5.5. After the pH-adjusted wastewater is passed through a bag filter to remove particulate impurities, and after a small laboratory test, it is measured that the above-mentioned high-salt wastewater after pyrolysis is normal at 25°C. The first-order kinetic constant k ...

Embodiment 2

[0077] Waste salt from a chemical company first uses a multi-layer disc cracking furnace for high-temperature pyrolysis, and the pyrolyzed waste salt is dissolved in water to produce high-salt wastewater, in which the concentration of salt (sodium chloride) is controlled at 23% wt. Detect the TOC of waste salt and reduce to 29.9mg / L, TN by initial 35mg / L and reduce to 15mg / L (the TOC concentration of initial waste salt and the TN concentration are that waste salt is formulated as salt (chlorination) by initial 680mg / L Sodium) mass fraction is the corresponding concentration when 23%wt), then the high-salt wastewater is removed by the pretreatment unit.

[0078] First, through the pretreatment unit, the pH of the solution is adjusted to 5.5 by adding hydrochloric acid to the reactor. After the pH-adjusted wastewater is passed through a bag filter to remove particulate impurities, the above-mentioned pyrolyzed water is measured through a small laboratory test. The first-order ki...

Embodiment 3

[0103]Waste salt from a chemical company first uses a rotary heating furnace for high-temperature pyrolysis, and the pyrolyzed waste salt is dissolved in water to produce high-salt wastewater. The mass fraction of the control salt (sodium chloride) is 23%wt. After testing, the waste The TOC of salt reduces to 17.9mg / L by initial 450mg / L, TN reduces to 15mg / L by initial 40mg / L (TOC concentration and TN concentration of initial waste salt are that waste salt is formulated as salt (sodium chloride) The corresponding concentration when the mass fraction is 23%wt), is removed by the pretreatment unit.

[0104] First, add hydrochloric acid to the reaction kettle to adjust the pH of the solution to 5.5. After the pH-adjusted wastewater is passed through a bag filter to remove particulate impurities, and after a small laboratory test, it is measured that the above-mentioned high-salt wastewater after pyrolysis is normal at 25°C. The first-order kinetic constant k corresponding to the ...

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Abstract

The invention discloses a high-salinity wastewater advanced oxidation method, an industrial waste salt resourceful treatment method, and equipment, and belongs to the field of environmental protection. The high-salinity wastewater advanced oxidation methodcomprises the step of degrading organic matters inhigh-salinity wastewater in a manner of simultaneously carrying out advanced oxidation by combining ultraviolet irradiation, hydrogen peroxide and a persulfate. According to determination thatprimary kinetic constant k is in different intervals and the removal rate of TOC is in different stages at 25 DEG C and normal pressure, different advanced oxidation conditions are respectively set, so that the reaction efficiency is improved to the maximum extent on the basis of ensuring that the energy consumption is reduced. Furthermore, the high-salinity wastewater advanced oxidation method is used as a treatment method for recycling industrial waste salt. After treatment by an advanced oxidation unit disclosed in the invention, the treated waste salt is used for an ionic membrane caustic soda production process, so that economic benefits are created for enterprises, and resource utilization of the waste salt is realized.

Description

technical field [0001] The invention belongs to the field of environmental protection, and more specifically relates to an advanced oxidation method of high-salt wastewater, a method and equipment for recycling industrial waste salt. Background technique [0002] Industrial waste salt refers to the by-product crystalline salts produced in industrial production. The annual output of waste salt in my country has exceeded 10 million tons. Chemical products, especially waste salt produced in the process of pesticide production contain a large amount of organic matter. If not handled properly, it will directly Leading to the pollution of surface water, groundwater and soil, the waste salt is traditionally landfilled after the harmless treatment by pyrolysis, resulting in a huge waste of resources; however, by degrading the high-salt wastewater and then reusing it In the process of treatment, it is often difficult to degrade the organic matter due to the high salt concentration in t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/72C02F1/32C01D3/14C01D3/04C02F101/30
CPCC01D3/04C01D3/14C02F1/32C02F1/722C02F2101/30C02F2305/026
Inventor 王炼陈利芳高静静戴建军李爱民周腾腾朱强
Owner NANJING UNIV YANCHENG ENVIRONMENTAL PROTECTION TECH & ENG RES INST
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