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Method for performing Fenton treatment on 6-nitro-1-diazo-2-naphthol-4-sulfonic acid wastewater and coproducing sodium sulfate

A technology of acid oxygen body and sodium sulfate, which is applied in filtration treatment, multi-stage water treatment, water/sewage treatment, etc., can solve the problems of incomplete oxidation, low removal rate of organic matter, and low utilization rate, so as to improve efficiency and The effect of equipment utilization, improvement of wastewater treatment efficiency, and ease of recycling

Active Publication Date: 2016-05-11
ZHEJIANG RUNTU INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] At present, there are two main methods for treating this type of wastewater: (1) complex extraction method, complex extraction treatment has high efficiency and high selectivity. The efficiency is reduced, and the stripping solution is difficult to handle at the same time
(2) Traditional Fenton treatment method, the traditional Fenton oxidation technology mainly uses lime to neutralize excess acid, produces calcium sulfate and other precipitates, and adsorbs and removes organic matter. Although it can achieve a decolorization rate>90%, the organic matter removal rate is relatively low. Low (COD removal rate is about 60%-70%), and H 2 o 2 The low utilization rate leads to high treatment costs. Due to incomplete oxidation, the final effluent is brownish-yellow to brown. It is difficult to discharge the wastewater up to the standard, and it is even more difficult to meet the reuse requirements. It also produces a large amount of solid waste, which increases the production cost of the enterprise and has an impact on the environment.

Method used

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  • Method for performing Fenton treatment on 6-nitro-1-diazo-2-naphthol-4-sulfonic acid wastewater and coproducing sodium sulfate
  • Method for performing Fenton treatment on 6-nitro-1-diazo-2-naphthol-4-sulfonic acid wastewater and coproducing sodium sulfate
  • Method for performing Fenton treatment on 6-nitro-1-diazo-2-naphthol-4-sulfonic acid wastewater and coproducing sodium sulfate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Put 200ml of 6-nitro-1,2,4-acid oxygen body reduction transposition wastewater into a beaker, adjust the pH to 2.5 with sodium carbonate, add 0.3g of activated carbon and 1mmol of FeSO at 35°C 4 , and then slowly add 3ml mass percent concentration of 28% H 2 o 2 , keep the temperature constant, let the reaction stand for 2h, adjust the pH to 10 with 25% aqueous sodium hydroxide solution in mass percentage, slowly add 10% Al in mass fraction under stirring 2 (SO 4 ) 3 solution, adjust the pH to 6.2, and then let it stand for 0.5h. Filter the turbid liquid after standing and settling. Repeat the process of oxidation, sedimentation and filtration for 3 times, the filtrate meets the treatment requirements, and after evaporation, concentration and drying, industrial grade sodium sulfate is obtained, with a content of more than 98%.

Embodiment 2

[0033] Put 200ml of 6-nitro-1,2,4-acid oxygen body acid precipitation wastewater into a beaker, adjust the pH to 2.0 with sodium carbonate, add 0.4g of activated carbon and 2mmol of FeSO at 45°C 4 , and then slowly add 4ml mass percent concentration of 28% H 2 o 2 , keep the temperature constant, let it stand for 1.5h, adjust the pH to 9.5 with 35% aqueous sodium hydroxide solution, slowly add 30% Al with mass fraction under stirring 2 (SO 4 ) 3 solution, adjust the pH to 6.5, and then let it stand for 1h. Filter the turbid liquid after standing and settling. The process of oxidation, sedimentation and filtration is repeated twice, and the filtrate meets the treatment requirements. After evaporation, concentration and drying, industrial grade sodium sulfate is obtained, with a content of more than 98%.

Embodiment 3

[0035] Put 100ml of 6-nitro-1,2,4-acid oxygen body reduction translocation and acid precipitation wastewater into a beaker, adjust the pH to 2.8 with 30% sodium hydroxide, add 0.1g of activated carbon at 25°C, 0.5 mmol FeSO 4 , and then slowly add 2ml mass percent concentration of 28% H 2 o 2 , keep the temperature constant, let the reaction stand for 1.5h, adjust the pH to 9.3 with 30% aqueous sodium hydroxide solution, slowly add Al with a mass fraction of 20% under stirring 2 (SO 4 ) 3solution, adjust the pH to 6.5, and then let it stand for 0.5h. Filter the turbid liquid after standing and settling. Repeat the process of oxidation, sedimentation and filtration for 4 times, and the filtrate meets the processing requirements. After evaporation, concentration and drying, industrial grade sodium sulfate is obtained, with a content of more than 98%.

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Abstract

The invention discloses a method for performing Fenton treatment on 6-nitro-1-diazo-2-naphthol-4-sulfonic acid wastewater and coproducing sodium sulfate, which comprises the following steps: (1) adding alkali into 6-nitro-1-diazo-2-naphthol-4-sulfonic acid wastewater, and regulating the pH value to 2.0-3.0; (2) under stirring conditions, adding activated carbon, FeSO4 and H2O2 into the wastewater subjected to pH value regulation to perform oxidation reaction; (3) adding alkali into the oxidated wastewater to regulate the pH value to 9-10; (4) adding an Al2(SO4)3 solution into the wastewater treated by the step (3) until the pH value of the reaction system reaches 6-7, sufficiently standing and settling to obtain a turbid solution, and filtering the turbid solution to obtain a filtrate; (5) if the filtrate obtained in the step (4) satisfies the treatment requirements, concentrating by evaporation and drying to obtain the industrial-grade sodium sulfate; and if the filtrate obtained in the step (4) does not satisfy the treatment requirements, repeating the steps (2)-(4) until the filtrate satisfies the treatment requirements. The treatment method has the advantages of simple technique and no environment pollution, and can coproduce sodium sulfate in the treatment process, thereby maximally utilizing the resources.

Description

technical field [0001] The invention belongs to the technical field of industrial waste water treatment and reuse for environmental protection, and specifically relates to the comprehensive treatment of waste water produced in the production process of 6-nitro-1,2,4-acid oxygen body, and the co-production of sodium sulfate at the same time, which belongs to the category of clean production . Background technique [0002] 6-nitro-1,2,4-acid oxygen body, CAS number is 5366-84-7, the structure is shown in formula (I), the Chinese alias is 6-nitro-1-diazo-2-naphthol -4-sulfonic acid is an important dye intermediate, mainly used in the manufacture of acid dyes and metal complex dyes. [0003] [0004] The production method of 6-nitro-1,2,4-acid oxygen body is to use ethyl naphthol as the main raw material, and it is prepared through nitrosation, sulfonation, reductive transposition, diazotization, acid precipitation, nitration and other processes. There are three main source...

Claims

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Application Information

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IPC IPC(8): C02F9/10C01D5/00C01D5/16
CPCC01D5/00C01D5/16C02F1/001C02F1/04C02F1/048C02F1/283C02F1/52C02F1/5236C02F1/66C02F1/722C02F9/00C02F2103/36C02F2301/08C02F2305/026
Inventor 陈伟东李茂赵益明夏骏钢章文刚
Owner ZHEJIANG RUNTU INST
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