Disposal process for fully standardized discharge of highly nondegradable organic wastewater

A treatment process and organic matter technology, which is applied in the field of high-refractory organic waste water to meet the discharge standards. It can solve the problems of low treatment load, environmental hazards, long treatment time, etc., and achieve high B/C ratio without secondary pollution. , to achieve the effect of fully meeting the emission standards

Inactive Publication Date: 2019-10-11
杭州深瑞环境有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The traditional activated sludge method and anaerobic process can effectively decompose organic matter in the treatment of refractory organic wastewater, but in actual engineering, it is found that anaerobic process is difficult to treat some organic matter, and it occupies a large area, takes a long time to process, and has low processing load. , and the effluent COD is difficult to reach the standard
Among the physical and chemical methods, the coagulation sedimentation method has a good effect in removing refractory organic pollutants and wastewater chroma, but this method mainly transfers pollutants in water to flocs and sludge, and has not achieved complete degradation, and will still cause great harm to the environment
Advanced oxidation methods include Fenton method, photocatalytic oxidation method, wet oxidation method, ozone oxidation method, etc., which have the advantages of high chemical reaction efficiency, good pollutant degradation effect, and small footprint. The disadvantage is that the treatment cost is high, and some The process is easy to cause secondary pollution, such as the Fenton process produces a large amount of sludge
Among them, the reason for the high treatment cost of the wet oxidation method is that the concentration of organic matter is low, and the heat generated by oxidation is not enough to maintain the heat required by the process, requiring a large amount of external heat supply
Membrane separation technology can efficiently separate pollutants in water, such as particulate matter, macromolecular organic matter and salt in water, and is currently the most commonly used technical means for sewage treatment at home and abroad. However, membrane separation method only concentrates pollutants and cannot achieve the digestion of pollutants.
The patent with the application number CN201610309671.5 proposes "a difficult organic wastewater treatment process technology", which adopts anaerobic and aerobic biochemical treatment and then uses MBR membrane to filter, but this process cannot completely digest pollutants, and most organic matter is still concentrated inside the MBR membrane

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  • Disposal process for fully standardized discharge of highly nondegradable organic wastewater
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Experimental program
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Effect test

Embodiment 1

[0025] A treatment process for the high-refractory organic waste water to meet the standard discharge. The high-refractory organic waste water is first passed into the biochemical pool 21 for anaerobic treatment, and then flows to the raw water tank 1, driven by the booster pump 2, and then passes through the quartz sand filter 3 in turn. After being filtered by a precision filter 4 with a precision of 1 μm, it is passed into one of the adsorption tanks 5, and the adsorption tank 5 is filled with a macroporous adsorption resin. After the wastewater is absorbed by the macroporous adsorption resin, the waste water that meets the standard is discharged. The adsorption time is For 20 minutes, the adsorption temperature of the macroporous resin is 15°C, and the adsorption pressure is normal pressure. After a period of adsorption, there will be many adsorbates on the macroporous resin, which are basically refractory organic substances. At this time, the pipeline Switch to another ads...

Embodiment 2

[0027]A treatment process for the high-refractory organic waste water to meet the standard discharge. The high-refractory organic waste water is first passed into the biochemical pool 21 for anaerobic treatment, and then flows to the raw water tank 1, driven by the booster pump 2, and then passes through the quartz sand filter 3 in turn. After being filtered by a precision filter 4 with a precision of 5 μm, it is passed into one of the adsorption tanks 5. The adsorption tank 5 is filled with macroporous adsorption resin. After the waste water is adsorbed by the macroporous adsorption resin, the waste water that meets the standard is discharged. The adsorption time is 240min, the adsorption temperature of the macroporous resin is 50°C, and the adsorption pressure is normal pressure. After a period of adsorption, there will be many adsorbates on the macroporous resin, which are basically refractory organic substances. At this time, the pipeline Switch to another adsorption tank, ...

Embodiment 3

[0029] A treatment process for the high-refractory organic waste water to meet the standard discharge. The high-refractory organic waste water is first passed into the biochemical pool 21 for anaerobic treatment, and then flows to the raw water tank 1, driven by the booster pump 2, and then passes through the quartz sand filter 3 in turn. After being filtered by a precision filter 4 with a precision of 3 μm, it is passed into one of the adsorption tanks 5, and the adsorption tank 5 is filled with a macroporous adsorption resin. After the waste water is adsorbed by the macroporous adsorption resin, the waste water that meets the standard is discharged. The adsorption time is 150min, the adsorption temperature of the macroporous resin is 35°C, and the adsorption pressure is normal pressure. After a period of adsorption, there will be many adsorbates on the macroporous resin, which are basically refractory organic substances. At this time, the pipeline Switch to another adsorption...

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Abstract

The invention relates to a wastewater disposal process, in particular to a disposal process for fully standardized discharge of highly nondegradable organic wastewater. The disposal process comprisesthe following steps that the highly nondegradable organic wastewater is subjected to high-efficiency biochemical treatment and then subjected to adsorption with macroporous resin, and standard tail water is discharged after the adsorption; the macroporous resin is eluted with a desorption agent, an obtained eluent is subjected to a wet oxidation reaction for wet oxidation degradation, most of nondegradable organic matter is completely degraded, a small part of the nondegradable organic matter is decomposed into organic matter wastewater which can be subjected to biochemical treatment easily, the high-efficiency biochemical treatment and the macroporous resin adsorption are carried out again, and the steps above are repeated circularly until fully standardized discharge of all the organic wastewater is realized. The disposal process can effectively realize the complete degradation of the highly nondegradable organic matter.

Description

technical field [0001] The invention relates to a waste water treatment process, in particular to a treatment process for discharging highly refractory organic waste water up to the standard. Background technique [0002] The treatment of highly difficult organic waste water is a difficult problem in the domestic and foreign sewage treatment industry. "Refractory" means that the biodegradability of this type of waste water is low, and BOD 5 The / COD value is generally less than 0.3 or even lower, and it is difficult to biodegrade. The COD of the biochemical effluent is still 1000mg / L~30000mg / L, and the organic matter causing this situation is polycyclic aromatic hydrocarbons, heterocyclic and long-chain alkanes or both Nitrogen, oxygen, sulfur heterocyclic compounds, oil, ammonia nitrogen and other toxic and harmful substances. Typical industries such as petrochemical, coal chemical, printing and dyeing, pharmaceutical, chemical, light industry, and pesticide often produce ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F101/30
CPCC02F1/00C02F1/001C02F1/285C02F1/725C02F1/74C02F3/28C02F9/00C02F2101/30C02F2301/08C02F2303/10C02F2303/16
Inventor 伍立波万金玲
Owner 杭州深瑞环境有限公司
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