Electrocatalytic dechlorination method for parachloronitrobenzene

A technology for electrolysis of chloronitrobenzene and p-chloronitrobenzene is applied in the field of electrochemistry for removing p-chloronitrobenzene in water, which can solve the difficulty of electrochemical dechlorination, high toxicity and stability, and cannot produce dechlorination. and other problems, to achieve good dechlorination effect, reduce energy consumption, and remove the dechlorination effect at one time

Inactive Publication Date: 2016-06-29
NANJING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the existence of chlorine and nitro group, the electrophilic attack of aerobic biological oxidase on benzene ring is blocked, so the treatment efficiency of p-chloronitrobenzene is very low; the process of anaerobic microbial reduction dechlorination is slow, and the dechlorination effect is low. Difference
Improper treatment of pollutants after adsorption enrichment and separation will lead to secondary pollution
Advanced oxidation technologies such as Fenton oxidation, photocatalytic oxidation, and ultrasonic cavitation have developed rapidly, but there are still defects such as low processing efficiency and high cost, and there is still a big gap from popularization and use.
The treatment of p-chloronitrobenzene by the metal reduction method is affected by many factors such as pH, metal particle size and specific surface area, mixing speed, etc., and there are defects such as easy passivation of the metal, low mass transfer efficiency, and formation of highly toxic end products.
[0004] Due to the existence of the para-nitro group, the chlorine on the benzene ring requires a large activation energy, and the structure is stable and difficult to remove
The existing reduction technology for the reduction product of p-chloronitrobenzene is mostly p-chloroaniline, which still has high toxicity and stability, which is not conducive to the subsequent biochemical or oxidation treatment
It was reported before that in the study of electrochemical reduction of o-chloronitrobenzene, the use of a titanium plate as the cathode cannot produce dechlorination, the reduction product is o-chloroaniline and the reaction takes a long time and the reaction efficiency is low, while p-chloronitrobenzene The structure is more stable, and electrochemical dechlorination is more difficult
However, in some studies on the reduction of p-chloronitrobenzene by electrobiological methods, the reduced product is mainly p-chloroaniline, and the dechlorination effect cannot be achieved.

Method used

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  • Electrocatalytic dechlorination method for parachloronitrobenzene

Examples

Experimental program
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Effect test

Embodiment 1

[0023] The nickel foam was ultrasonically cleaned with acetone and methanol followed by acid washing and water washing; the palladium chloride loading solution was an aqueous solution prepared with a 1:3 molar ratio of palladium chloride and sodium chloride; the loading amount of palladium was 2mg / cm 2 . figure 1 It is a surface morphology map of different multiples of the palladium foam nickel electrode, which has a uniform distribution and a large specific surface area.

[0024] The anode uses ruthenium iridium titanium electrode, the cathode uses the palladium foam nickel electrode with the above load, the electrolyte uses 50mmol / l sodium sulfate and 25g / l p-chloronitrobenzene mixed solution, and the electrolyte is placed in an electrocatalytic reactor. Constant current reaction, the current density is 10mA / cm 2 The removal efficiency of p-chloronitrobenzene and the yield of aniline in 30 minutes are shown in Table 1.

Embodiment 2

[0026] The loading of palladium was changed to 0.5, and other implementation conditions were the same as in Example 1. The removal efficiency of p-chloronitrobenzene and the yield of aniline within 30 minutes are shown in Table 1.

Embodiment 3

[0028] The loading of palladium was changed to 1, and other implementation conditions were the same as in Example 1. The removal efficiency of p-chloronitrobenzene and the yield of aniline within 30 minutes are shown in Table 1.

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Abstract

The invention discloses a method for electrocatalytic dechlorination of p-chloronitrobenzene, which comprises the following steps: adopting an impregnation method to load noble metal palladium on a foamed nickel material with a three-dimensional structure as the cathode of an electrocatalytic reactor; The waste water of base benzene is passed into the electrocatalytic reactor, and the whole reactor is filled, and the electrochemical treatment starts under constant current, and the reduction reaction of p-chloronitrobenzene occurs in the cathode chamber, and it is first reduced to p-Chloroaniline, and then undergoes dechlorination to form aniline due to the superior performance of the palladium-containing nickel foam electrode. The present invention replaces metal reduction with electrocatalytic reduction, which avoids the problems of easy passivation of metals and low mass transfer efficiency, and overcomes the difficult problem that traditional electrodes are difficult to dechlorinate p-chloronitrobenzene. Take off effectively.

Description

Technical field [0001] The invention relates to a method for removing highly toxic organic matter, in particular to an electrochemical method for removing p-chloronitrobenzene in water. Background technique [0002] P-Chloronitrobenzene exists in industrial wastewater (generally with a concentration of 0.05-200mg / L), and it is difficult to degrade in nature. It has been detected in some major water bodies in my country. P-chloronitrobenzene can cause methemoglobinemia in humans and animals, and has weak carcinogenic and mutagenic effects. As a high-risk, difficult-to-degrade, persistent environmental organic pollutant, my country has strict standards for its discharge. In my country's GB8978-1996 "Integrated Wastewater Discharge Standard", the first-level emission standard of p-chloronitrobenzene is 0.5mg / L, the secondary standard is 1.0mg / L, and the tertiary standard is 5.0mg / L. Therefore, due to the toxicity and stability of chloronitrobenzene, its residue and accumulation in...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/461C02F101/38C02F101/36
CPCC02F1/46104C02F1/46109C02F2001/46133C02F2101/36C02F2101/38
Inventor 李爱民吴一凡宋海欧王柏俊王长明李文涛双陈冬
Owner NANJING UNIV
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