Technique for pretreating aniline-containing wastewater by adopting resin adsorption method

A resin adsorption and pretreatment technology, applied in the direction of adsorption water/sewage treatment, filtration treatment, special treatment goals, etc., can solve the problems of high energy consumption, troublesome operation and management, and complex structure of pollutants in the incineration method, and achieve desorption regeneration Easy, wide application range, good adsorption effect

Inactive Publication Date: 2017-08-15
NANTONG BOTAO CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] (1) The structure of pollutants is complex and the concentration is high
[0005] This type of wastewater generally has a complex pollutant structure and high solubility in water, so the concentration and COD of this type of wastewater in water are several thousand to tens of thousands mg/L
[0006] (2) High salt content
[0008] (3) Wastewater is highly acidic (alkali)
[0009] (4) deep color
The BOD/COD value of aniline substances in water is low, generally inhibits the growth of microorganisms, and has poor biodegradability. It is difficult to achieve the desired effect with conventional biochemical methods.
[0013] (6) High biological toxicity
For example, in the extraction treatment method, the extraction agent is easily lost and causes secondary pollution, and at the same time, the energy consumption is high, and the operation is relativel

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0037] Example 1

[0038] In the present embodiment, the resin adsorption method for pretreatment of aniline-containing wastewater process includes the following steps:

[0039] (1) The wastewater with pH value of 8.5, COD content of 32000mg / L, and aniline content of 2900mg / L is sent to the front-stage original wastewater tank through the primary filter, and the wastewater in the original wastewater tank is then transferred to a 1m 3 The flow rate of / h is sent to the precision filter to filter out mechanical impurities;

[0040] (2) After the mechanical impurities are filtered out, the waste water is continuously fed into the first resin adsorption tower and the second resin adsorption tower through the circulating pump, and the flow rate is controlled to 1m 3 / h; The aniline-containing wastewater entering the resin adsorption tower is continuously adsorbed by the NKA-2 resin column in the adsorption tower through two stages to adsorb the aniline in the wastewater;

[0041] (3) After ...

Example Embodiment

[0044] Example 2

[0045] In the present embodiment, the resin adsorption method for pretreatment of aniline-containing wastewater process includes the following steps:

[0046] (1) The wastewater with pH value of 8.5, COD content of 32000mg / L, and aniline content of 3100mg / L is sent to the original wastewater tank of the previous stage through the first-stage filter, and the wastewater in the original wastewater tank is passed through the transfer pump to 3m 3 The flow rate of / h is sent to the precision filter to filter out mechanical impurities;

[0047] (2) After the mechanical impurities are filtered out, the wastewater is continuously fed into the first resin adsorption tower and the second resin adsorption tower through the circulating pump, and the flow rate is controlled to 3m 3 / h; The aniline-containing wastewater entering the resin adsorption tower is continuously adsorbed by the NKA-2 resin column in the adsorption tower through two stages to adsorb the aniline in the was...

Example Embodiment

[0051] Example 3

[0052] In the present embodiment, the resin adsorption method for pretreatment of aniline-containing wastewater process includes the following steps:

[0053] (1) The wastewater with pH value of 8.5, COD content of 32000mg / L, and aniline content of 3000mg / L is sent to the fore-stage original wastewater tank through the primary filter, and the wastewater in the original wastewater tank is then transferred to a 2m 3 The flow rate of / h is sent to the precision filter to filter out mechanical impurities;

[0054] (2) After the mechanical impurities are filtered out, the wastewater is continuously fed into the first resin adsorption tower and the second resin adsorption tower through the circulating pump, and the flow rate is controlled to 2m 3 / h; The aniline-containing wastewater entering the resin adsorption tower is continuously adsorbed by the NKA-2 resin column in the adsorption tower through two stages to adsorb the aniline in the wastewater;

[0055] (3) After th...

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PUM

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Abstract

The invention relates to a technique for pretreating aniline-containing wastewater by adopting a resin adsorption method. The technique comprises the following steps: (1) feeding the aniline-containing wastewater into a pre-stage raw wastewater tank through a first-level filter, conveying the wastewater in the raw wastewater tank into a fine filter, and filtering out the mechanical impurities; (2) after filtering out the mechanical impurities, continuously feeding wastewater into a first resin absorbing tower and a second resin absorbing tower in turn through a circulating pump, performing two-stage continuous absorption on the aniline-containing wastewater entering the resin absorbing towers through the resin columns in the absorbing towers, and absorbing the aniline in the wastewater to the upper surface; and (3) after absorbing the resin, feeding the pretreated wastewater into a wastewater treating pond through a wastewater pump, activating the treated resin columns and recycling. The invention has the advantages that the resin adsorption method is adopted for absorbing the aniline in the aniline wastewater, and the treating method can effectively treat the wastewater and can realize the waste resource recycling.

Description

technical field [0001] The invention relates to a waste water treatment process, in particular to a resin adsorption method for pretreatment of waste water containing benzene [0002] Amine Wastewater Process. Background technique [0003] At present, BTA is mainly synthesized by one-step pressurized reaction of o-phenylenediamine and sodium nitrite, and TTA is mainly synthesized by one-step pressurized reaction of methyl-o-phenylenediamine and sodium nitrite. However, in the production process, organic pollutants with complex structure, deep color, difficult biodegradation, high biotoxicity and poor biodegradability will be generated, so that the content of anilines in wastewater sometimes reaches as high as 8000-10000mg / L. Aniline wastewater usually has the following characteristics: [0004] (1) The structure of pollutants is complex and the concentration is high [0005] This type of wastewater generally has a complex pollutant structure and high solubility in water, ...

Claims

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Application Information

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IPC IPC(8): C02F1/28C02F1/00C02F101/38
CPCC02F1/285C02F1/001C02F2101/38C02F2301/08C02F2303/16
Inventor 黄海涛王宏李桂萍
Owner NANTONG BOTAO CHEM
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