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Glyphosate-producing wastewater treatment integration technology

A technology for glyphosate wastewater and production wastewater, applied in natural water treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve problems such as limited oxidation degree, waste of resources, incompleteness, etc., and achieve Blends quickly and evenly

Inactive Publication Date: 2015-05-13
四川省生态环境科学研究院 +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the glyphosate in it cannot be recycled, it will pollute the environment and cause a certain waste of resources
[0003] In May 2013, the state initiated an environmental inspection of the glyphosate industry. The main contents of the inspection include: total pollutant emission reduction tasks, waste water discharge up to standard, waste gas recovery and treatment, waste water treatment facilities, mother liquor recovery device, solid waste treatment, process Pollution control, etc., and the water quality of such wastewater is complex (COD cr =5000~17000 mg / L, NH 3 -N<500mg / L, TP<20~100mg / L, formaldehyde=3000~5000mg / L, chloride ion<10000mg / L, pH=2.0~4.0), the degradation is difficult, and the traditional process is difficult to fully degrade, resulting in difficult drainage Discharge up to the standard, causing serious pollution to the environment, has become the bottleneck of enterprise development
However, due to the high concentration of organic matter, a large amount of oxidant is theoretically required, and it is unrealistic to completely oxidize all organic matter into inorganic matter, and the processing cost is too high for manufacturers to afford.
[0007] ② Hydrogen peroxide / O 3 The oxidation method mainly uses hydrogen peroxide and O 3 The combination of strong oxidizing properties oxidizes organic matter such as organic phosphorus and organic nitrogen in the mother liquor into inorganic matter in a certain pH environment. The oxidation degree of this oxidation method is limited, and the decomposition rate of organic matter in wastewater is only about 40%. Oxidation is not complete, unable to achieve the purpose of effective treatment or auxiliary treatment
[0010] ⑤ Resin adsorption method is to realize the recovery of useful substances such as glyphosate in wastewater through the selective adsorption of adsorption resins such as large pores, which is conducive to saving resources and reducing the difficulty of subsequent treatment. However, glyphosate wastewater has many impurities and is harmful to resins. Adsorption has great limitations and incompleteness. At present, the method is still in the small test stage, and the recovery rate is only about 45%.
However, SBR relies heavily on modern automation control technology, which requires a high degree of automation, operation, management, and maintenance, and requires high quality operation and management personnel. If manual operation is used, there will be cumbersome operations due to the water inlet and outlet
[0018] The combination of various physicochemical and biochemical processes mentioned above has its own characteristics, but each individual physicochemical method and biochemical method has its own defects and deficiencies, resulting in unstable pretreatment and impact on subsequent biochemical processes. Incomplete treatment of macromolecular and refractory organic substances is powerless, resulting in the problem that glyphosate wastewater cannot meet the discharge standards after treatment

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Implementation example 1: get glyphosate waste water (COD cr =12020mg / L, pH=2-3, TP=96mg / L, formaldehyde=5362mg / L) 1L, directly into the micro-electrolysis filler, aeration reaction for 2h, after adjusting the pH to 3-4, adding 2mL of hydrogen peroxide reagent, exposure Gas reaction for 2 hours, adjust the pH to about 9 with milk of lime, and effluent COD after flocculation and precipitation cr 49.17% reduction, formaldehyde reduction 82.56%. After the effluent enters the anaerobic reaction tank and stays for 48 hours, it enters the specific contact oxidation tank and aeration tank for treatment. After the effluent is tested, the COD cr It is 89.6mg / L.

Embodiment 2

[0041] Implementation example 2: A glyphosate production enterprise in Sichuan discharges wastewater (COD cr =10000-13000mg / L, pH=2-3, TP3 / d, the design flow rate is about 5m 3 / h. The waste water is lifted to the micro-electrolysis tower through the regulating tank, and the residence time is about 2 hours. The effluent is added with acid to adjust the pH to 3-4, and hydrogen peroxide is added, and enters the Fenton reactor for reaction. The residence time is about 2 hours. Aluminum), PAM (polyacrylamide), adjusted to pH = 8-9, enters the sedimentation tank, after sedimentation, it is lifted to the UASB reactor by the pump, and the residence time is 48h. After that, it enters the fourth-stage contact oxidation tank for treatment, and then enters the aeration tank. Add PAC (polyaluminum chloride) phosphorus removal agent. The average dosing amount per ton of wastewater in the whole process is about 16kg of liquid PAC (polyaluminum chloride), 10kg of lime, 2kg of PAM (polyacr...

Embodiment 3

[0042] Implementation example 3: A chemical company in Sichuan discharges glyphosate production wastewater (COD cr =5000-16281mg / L, pH=2-4, TP3 / d, take 1L of water sample, directly enter the micro-electrolysis filler, aerate for 2 hours, then adjust the pH to 3-4, add 2mL hydrogen peroxide reagent, aerate for 2 hours, adjust the pH to about 9 with lime milk, flocculate and settle COD cr 47.45% reduction, formaldehyde reduction 84.67%, chloride ion reduction 36.43%. After the effluent enters the anaerobic reaction tank and stays for 48 hours, it enters a specific aerobic reactor (four-stage contact oxidation tank and one-stage aeration tank) for reaction, and the effluent is tested, and the COD cr It is 75.32mg / L.

[0043] Since the control conditions involved in the present invention are relatively high, especially for the aerobic biochemical system, the technical quality of the users is high, and automatic programming assistance is required.

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PUM

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Abstract

The invention discloses a gyphosate-producing wastewater treatment integration technology. The technology comprises steps as follows: micro-electrolysis treatment is performed under the aeration condition, toxic and degradation-resistant organic matters in wastewater are oxidized by a Fenton regent comprising hydrogen peroxide and ferrous ions which are by-products produced by ferric carbon filler, after lime is added to effluent and pH is regulated to 8-9, a flocculating agent is added for precipitation, suspended matters and iron-phosphorus precipitates are removed, effluent after precipitation is sent to an upflow anaerobic reactor, and degradation-resistant and toxic organic matters in wastewater are further degraded, removed and transformed, the effluent enters a multi-stage contact oxidation pond and a primary aeration sedimentation tank for biochemical treatment, the treated wastewater is emitted up to standard, and the organic matter removal rate in a pretreatment combination physicochemical technology can be up to 50%. The technology is stable in operation and good in treatment effect, the treatment cost is reduced, and the treated effluent can meet the integrated wastewater discharge standard (GB-8978-1996).

Description

technical field [0001] The invention relates to an industrial waste water treatment process, in particular to a process method for glyphosate pesticide production waste water treatment including physical, chemical and biological treatment. Background technique [0002] Glyphosate (PMG) is the largest pesticide export species in my country and is a broad-spectrum herbicide. One of the mainstream domestic production processes is the iminodiacetic acid (IDA) route, and its production wastewater contains iminodiacetic acid salts , chloroacetic acid, ammonium triacetate, glycine and other difficult-to-biodegradable organic substances, and contain a large amount of methanol, formaldehyde, glyphosate, dimethyl phosphite and salts, etc., and the annual production of glyphosate mother liquor wastewater in the country is about 2 million Ton. Glyphosate production wastewater belongs to toxic and harmful industrial production wastewater. The wastewater has the characteristics of large di...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F103/36
Inventor 陈亚平田庆华袁志福姜延雄罗思强周文波王维
Owner 四川省生态环境科学研究院
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