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Adsorption oxidation method for treating high-concentration acrylonitrile wastewater

A high-concentration technology for acrylonitrile wastewater, applied in chemical instruments and methods, multi-stage water/sewage treatment, adsorption water/sewage treatment, etc., can solve problems such as secondary pollution, limited application, and air pollution, and achieve reduced treatment cost, improve processing efficiency, and extend the effect of the working cycle

Inactive Publication Date: 2011-09-21
TSINGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At the end of the 20th century, foreign countries used electrolysis to treat this wastewater and had industrial applications, but due to its high cost, the application was very limited.
At present, the main methods of my country's treatment of this wastewater are: (1) incineration. Many high-concentration acrylonitrile wastewaters in my country are treated with this method. The advantage is that the treatment is thorough, but the energy consumption of wastewater treatment is high. It is around 230-250 yuan, and in the actual operation process, due to the harmful gas generated by combustion, it will cause secondary pollution and air pollution, and its own equipment is also prone to scaling
(2) Evaporation and rectification method, the principle is to use the different boiling points of the substances in the waste water, acrylonitrile is 77.3°C, acetonitrile is 81.6°C, water is 100°C, and the heavy component is higher than 120°C. Heating and controlling the temperature in the still , to obtain components with different boiling points from different parts of the top of the fractionation tower to achieve the purpose of separation, but its disadvantages are high energy consumption, incomplete treatment, and high treatment cost
(3) Fenton (Fenton) reagent method, hydrogen peroxide and catalyst Fe 2+ The oxidation system formed is called Fenton's reagent, in Fe 2+ Under the action of catalysis, hydrogen peroxide can generate active hydroxyl radicals, thereby triggering free radical chain reactions, accelerating the oxidation of organic matter and reducing substances, thereby effectively reducing COD in acrylonitrile wastewater, and the removal rate can reach about 80%. As acrylonitrile Wastewater pretreatment is a relatively effective method, but hydrogen peroxide is easy to decompose ineffectively during the operation of this treatment method, resulting in a decrease in treatment efficiency and an increase in treatment cost, and it is difficult to achieve efficient treatment of acrylonitrile wastewater by Fenton reagent

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] The acrylonitrile wastewater used is the wastewater produced by the production of acrylonitrile as the treatment object. The wastewater contains a large amount of harmful substances such as acrylonitrile oligomers, acrylonitrile, hydrides, and acetonitrile. Among them, the CODcr is 19869.2mg / L, and the ammonia nitrogen content is 316.2mg / L, the chromaticity is 4120 degrees, and the turbidity is 228.0NTU.

[0016] An adsorption oxidation method for treating high-concentration acrylonitrile wastewater, comprising the following steps:

[0017] 1) First, add an aqueous flocculant solution with a mass ratio of 7.2:100 to the acrylonitrile wastewater, stir for 35 minutes at a rotational speed of 100 rpm, and let stand for 3 hours until the flocs settle to the bottom of the container for later use. The aqueous flocculant solution is the mass The concentration is the combination of anionic polyacrylamide and 2% polyaluminum chloride aqueous solution at a concentration of 0.1%, ...

Embodiment 2

[0024] The acrylonitrile wastewater used is the wastewater produced by the production of acrylonitrile as the treatment object. The wastewater contains a large amount of harmful substances such as acrylonitrile oligomers, acrylonitrile, hydrides, and acetonitrile. Among them, the CODcr is 22009.2mg / L, and the ammonia nitrogen content is 328.0mg / L, the chromaticity is 3240 degrees, and the turbidity is 218.0NTU.

[0025] An adsorption oxidation method for treating high-concentration acrylonitrile wastewater, comprising the following steps:

[0026] 1) First, add an aqueous flocculant solution with a mass ratio of 15:100 relative to the wastewater to the acrylonitrile wastewater, stir for 5 minutes at a speed of 200 rpm, and let stand for 24 hours until the flocs settle to the bottom of the container for later use. The aqueous flocculant solution is the mass The concentration is a combination of 0.01% nonionic polyacrylamide and 1% polyaluminum chloride aqueous solution, and the...

Embodiment 3

[0033] The acrylonitrile wastewater used is the wastewater produced by the production of acrylonitrile as the treatment object, and the wastewater contains a large amount of harmful substances such as acrylonitrile oligomers, acrylonitrile, hydrides, and acetonitrile. Among them, CODcr is 17726.0mg / L, ammonia nitrogen content is 332.9mg / L, color is 7840 degrees, and turbidity is 335.6NTU.

[0034] An adsorption oxidation method for treating high-concentration acrylonitrile wastewater, comprising the following steps:

[0035] 1) First add an aqueous flocculant solution with a mass ratio of 10.1:100 to the acrylonitrile wastewater, stir for 2 hours at a speed of 20 rpm, and let stand for 1 hour until the flocs settle to the bottom of the container for later use. The aqueous flocculant solution is the mass The concentration is a combination of 0.01% cationic polyacrylamide and 5% polyaluminum chloride aqueous solution, and the mass ratio of cationic polyacrylamide and polyaluminum ...

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Abstract

The invention relates to an adsorption oxidation method for treating high-concentration acrylonitrile wastewater, which comprises the following steps of: adding aqueous solution of a flocculating agent into the acrylonitrile wastewater, stirring, and standing until flocs are settled at the bottom of a container for later use; making the wastewater pass through a microfiltration membrane or an ultrafiltration membrane to remove suspended particles, the flocs and acrylonitrile oligomer from the wastewater, regulating the pH value of the wastewater, adding activated carbon and a Fenton reagent, and stirring for adsorption oxidation; filtering the wastewater by using activated carbon filter cloth, adding the activated carbon and hydrogen peroxide into the wastewater, and stirring for secondary adsorption oxidation; and filtering the wastewater by using the activated carbon filter cloth, and neutralizing filtrate by using sodium hydroxide until the filtrate is neutral. The method improves treatment efficiency, is not limited by the chemical oxygen demand (COD) of the wastewater, avoids secondary pollution, is low in energy consumption, easy and convenient to operate and small in occupied area, and has the characteristics that the method is high-efficiency, economic and environment-friendly.

Description

technical field [0001] The invention relates to a method for treating acrylonitrile wastewater, in particular to an adsorption oxidation method for treating high-concentration acrylonitrile wastewater. Background technique [0002] Acrylonitrile (AN) is mainly used in the production of acrylic fiber, nitrile rubber, adiponitrile, acrylamide, ABS resin, etc. Other uses such as caprolactam, polyol polymer, acrylonitrile in synthetic fiber, synthetic rubber, plastics and other fields It also has broad application prospects. In the production process of acrylonitrile, every 1 ton of acrylonitrile produced is accompanied by about 1 ton of waste water, and the quenching, absorption, and recovery systems need a large amount of water as quenching water, absorption water and solvent water. There are 10 sets of acrylonitrile plants in my country, with an annual output of more than 1 million tons of acrylonitrile. Under such circumstances, the treatment of high-concentration, highly t...

Claims

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Application Information

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IPC IPC(8): C02F9/04C02F1/28C02F1/72
Inventor 李继定展侠郑冬菊
Owner TSINGHUA UNIV
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