CN1600700A - Technique of electrolytic oxidation for treating waste water of containing phenol - Google Patents
Technique of electrolytic oxidation for treating waste water of containing phenol Download PDFInfo
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- CN1600700A CN1600700A CN 03151224 CN03151224A CN1600700A CN 1600700 A CN1600700 A CN 1600700A CN 03151224 CN03151224 CN 03151224 CN 03151224 A CN03151224 A CN 03151224A CN 1600700 A CN1600700 A CN 1600700A
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Abstract
The invention relates to stirringless, internal circulating and double coordinating electrolyzing oxide treatment technology for organic waste water which is difficult to be degradated, particularly for the waste water containing phenol. Internal circulating plate frame electrolytic tank is used, Ti group PbO2 electrode is used as positive pole, stainless steel is negative pole, waste water containing phenol is used as electrolyte to discharge and generate strong oxide group-hydroxyl free radical on positive pole, negative pole get electron to form H2O2, negative and positive poles are coordinated action to realize deep oxide decomposing to phenol pollutant, and then to achieve the goal of treating waste water containing phenol.
Description
Technical Field
The invention belongs to a stirring-free, internal circulation and double-synergistic electrolytic oxidation treatment process of refractory organic wastewater in environmental electrochemistry, in particular to an electrolytic oxidation treatment process of phenol-containing wastewater, which is suitable for the treatment occasion of phenol-containing wastewater.
Background
With the rapid development of industrialization, especially chemical industry, the variety of artificially synthesized organic matters is increasing day by day, and although the substance world of human society is greatly enriched, the environmental pollution, which is a byproduct, is becoming more serious, especially organic waste water (such as phenol) generated in petrochemical industry and organic synthesis, which often has the characteristics of 'three causes' (carcinogenesis, teratogenesis and causing outburst), and poses serious threat to the health and survival of human beings. Statistically, 80% of the diseases worldwide are associated with water pollution.
The phenol compound is used as an important organic chemical basic raw material and is widely applied to various aspects of national economy. Because of strong toxicity and irritation, the water environment is seriously damaged by random discharge without treatment. The united states environmental protection agency published in 1997 statute, stipulates 129 important pollutants to be controlled, phenol compounds are one of them, and phenol content is one of the important indexes for evaluating water quality pollution degree. The content of I, II water volatile phenol (mainly phenol) is less than 0.002mg/L, and the content of III water is less than 0.005 mg/L; the content of volatile phenol in all pollution discharge units is less than 0.5mg/L according to the first-level standard regulation in GB8978-1996 Integrated wastewater discharge Standard. As the phenol compounds belong to polar ionizable organic matters, the adsorption and biological enrichment effects of the phenol compounds on sediments are usually less, the water body is difficult to recover to an uncontaminated degree through comprehensive effects of physics, chemistry, biology and the like, and the potential influence on the human environment is great.
The prior treatment applied to the phenol-containing wastewater mainly comprises a coagulation method, an adsorption method, a salting-out method, an extraction method, a chemical oxidation method, a biological oxidation method and the like. Wherein the salting-out method, extraction method and ion exchange technology are suitable forWhen the concentration of phenol is more than 100mg/L, the recovered phenol is taken as the main point, the concentration of effluent is often more than 10mg/L, and the problems of recovery of added chemical reagents and the like are involved; the principle of chemical oxidation treatment is to oxidize phenol into benzenediol, butenedioic acid and CO under the action of an oxidant and a catalyst, such as wet oxidation, photocatalytic oxidation, ozone oxidation, hydrogen peroxide reaction and the like2And the like; the biological oxidation is suitable for the occasion that the phenol concentration is less than 100mg/L, the phenol removal rate can reach 90% for the wastewater with the phenol concentration of 10-15 mg/L, when the phenol concentration is more than 20mg/L, the phenol removal efficiency is reduced, and the wastewater can reach the standard and be discharged after being diluted. In combination with the above analysis, these methods have the major disadvantages of large equipment volume, complicated operation, large sludge amount, complicated post-treatment, etc., which require addition of chemicals. The similar technology adopts a graphite anode, so that the concentration of phenol can be reduced from 15-100 mg/L to 4.8-5.6 mg/L, and the waste COD per kgThe power consumption of water treatment is 70.5 kWh; adopts a Pt electrode, consumes 50kWh of electricity per kgCOD wastewater treatment, adopts SnO2And the electrode consumes 30kWh of electricity per kg of COD wastewater treatment. The oxidation process of the phenol organic matters on the electrode material is accompanied by oxygen evolution reaction and hydrogen evolution reaction, so that the oxidation potential and the current efficiency are reduced, the energy consumption for treating the COD of unit wastewater is high, and the implementation effect is influenced.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide the electrolytic oxidation treatment process of the phenol-containing wastewater, which basically does not need to add chemicals, does not need a stirring system, has the synergistic action of a cathode and an anode, is simple to operate and can effectively remove phenol substances.
An electrolytic oxidation treatment process of phenol-containing wastewater, which is characterized in that Ti-based PbO is adopted2The electrode is an anode, the stainless steel is a cathode, the waste water containing phenol is electrolyte, and strong oxidation groups-hydroxyl free radicals-OH are generated by discharging at the anode through electrolyzing water in the electrolyte, and electrons are obtained at the cathode to form H2O2The deep oxidative decomposition of phenol pollutants is realized by the synergistic action of the anode and the cathode, so that the aim of electrolytic oxidation treatment of the phenol-containing wastewater is fulfilled; wherein the anodeAnd cathodes are alternately arranged, the number of the cathode plates is more than that of the anode plates by 1, the distance between the adjacent electrode plates is 20mm, the power supply for electrolysis adopts a steady-current direct-current power supply, and the current density is 30mA/cm2The electrolyte in the electrolytic cell is internally circulated without stirring,
the anode reaction is as follows:
the cathode reaction is as follows:
the phenol oxidative decomposition reaction comprises the following steps:
the principle of the treatment process is as follows:
OH groups and H formed during electrolysis2O2All have strong oxidizing property, especially the OH group oxidizing electrode has a potential of up to 2.80V, in ratio to O3(2.07V) is 35% higher, second to fluorine in oxidation capacity; in addition, the group has high electronegativity (electrophilicity), has an electron affinity of 569.3kJ, and easily attacks a high electron cloud density point. H2O2The oxidation electrode potential was 1.76V. Thus, OH groups and H2O2Can play a double synergistic effect, realize the deep oxidative decomposition of pollutants and further achieve the purpose of treatment.
The invention provides Ti-based PbO with an active layer2A catalytic electrode. The electrode can work under high current density which can reach 30-50 mA/cm2Even at 200mA/cm2The plating loss increases slightly when the current density is operated. Electrode at 60 ℃ 1mol/LH2SO4In the solution, the anode oxygen release life can reach 45 h. Addition of SnO2+Sb2O3+MnO2Active intermediate layer for improving conventional Ti/PbO2And (4) electrode performance. EDS, 2SEM and XRD analysis results of the electrode show that the electrode has a surface layer of 452 mu m84.55 percent of Pb and PbO2Relative percentage of97.6%, i.e. the surface of the electrode is mainly lead oxide and a small amount of MnO is added2(ii) a The active layer has small crystal grains, is compact and has no cracks, can effectively prevent oxygen from diffusing to the substrate, and reduces TiO2Forming an insulating layer; the active layer is mushroom-shaped, has larger roughness and large specific surface area, and meets the requirements of a porous electrode; sb2O3、MnO2、PbO2The three coexist, which plays the role of preventing the coating from falling off. Thus, from the appearance characteristics, Ti/SnO2+Sb2O3+MnO2/PbO2The electrode has good catalytic performance, the coating is not easy to fall off, and the service life is long.
Compared with theprior art, the non-stirring, internal circulation and double-synergistic electrolytic oxidation treatment process for the phenol-containing wastewater, disclosed by the invention, basically does not need to add chemicals, has the advantages of small equipment volume, easiness in operation, small sludge amount, simplicity in post-treatment and the like, overcomes the problem of high energy consumption caused by a large number of side reactions such as oxygen evolution and hydrogen evolution in the similar technology, and has very important market development prospect.
Detailed Description
Example 1:
the implementation scheme and the working principle of the invention are as follows: stirring-free, internal circulation and double-synergic electrolytic oxidation treatment process of waste water containing phenol of 12.1mg/L and 24.7mg/L, adopting a polypropylene plate-frame type electrolytic tank and Ti-based PbO2The catalytic electrode is an anode, the stainless steel is a cathode, the waste water containing phenol is electrolyte, strong oxidation groups-hydroxyl free radicals-OH are generated by discharging at the anode through electrolyzing water in the electrolyte, and electrons are obtained at the cathode to generate H2O2The positive and negative electrodes act synergistically to realize deep oxidative decomposition of phenol pollutants, so that the aim of electrolytic oxidation treatment of the phenol-containing wastewater is fulfilled; wherein the number of the anode plates is 1, the number of the cathode plates is 2, the anodes and the cathodes are alternately arranged, the distance between the adjacent electrode plates is 20mm, and the effective electrode plate areas of the anodes and the cathodes are 1200cm2The power supply for electrolysis adopts a steady-current direct-current power supply, and the current density is 30mA/cm2The hydraulic retention time in the electrolytic cell is 120min, the wastewater treatment results are shown in Table 1,
the anode reaction is as follows:
the cathode reaction is as follows:
the phenol oxidative decomposition reaction comprises the following steps:
the results in Table 1 show that the process for treating waste water by electrolytic oxidation can effectively treat the waste water containing phenol, the removal rate of volatile phenol is 92.5 percent, and the removal rate of COD isCr、BOD5The removal rates are respectively 89.6% and 76.76%, the B/C ratio is increased from the original 0.14 to 0.31, and the biochemical property of the wastewater is greatly improved. The power consumption per kgCOD is 10.40 kWh.
TABLE 1 results of wastewater treatment
The monitoring method comprises the following steps: CODCr、BOD5Phenol, pH and the like are prepared by corresponding methods specified in Water and wastewater monitoring and analyzing method which is compiled by the State environmental protection administration.
Example 2:
the implementation scheme and the working principle of the invention are as follows: the other conditions are the same, the number of the anode plates is 2, the number of the cathode plates is 3, the anodes and the cathodes are alternately arranged, the distance between the adjacent electrode plates is 20mm, and the effective electrode plate areas of the anodes and the cathodes are 2400cm2The power supply for electrolysis adopts a steady-current direct-current power supply, and the current density is 30mA/cm2The hydraulic retention time in the electrolytic cell is 60min, the wastewater treatment results are shown in Table 2,
the anode reaction is as follows:
the cathode reaction is as follows:
the phenol oxidative decomposition reaction comprises the following steps:
the results in Table 2 show that the process for treating waste water by electrolytic oxidation can effectively treat the waste water containing phenol, the removal rate of volatile phenol is 92.0 percent, and the removal rate of COD isCr、BOD5The removal rates are 91.06 percent and 78.06 percent respectively, the B/C ratio is increased from the original 0.14 to 0.34, and the biochemical property of the waste water is greatly improved. The power consumption per kgCOD is 5.20 kWh.
TABLE 2 results of wastewater treatment
The monitoring method comprises the following steps: CODCr、BOD5Phenol, pH and the like are prepared by corresponding methods specified in Water and wastewater monitoring and analyzing method which is compiled by the State environmental protection administration.
Example 3:
the implementation scheme and the working principle of the invention are as follows: a process for treating the waste water containing phenol (12.1 mg/L) without stirring, internal circulation and dual-synergistic electrolytic oxidation features use of polypropylene plate-frame electrolyzer and Ti-base PbO2The catalytic electrode is an anode, the stainless steel is a cathode, the waste water containing phenol is electrolyte, strong oxidation groups-hydroxyl free radicals-OH are generated by discharging at the anode through electrolyzing water in the electrolyte, and electrons are obtained at the cathode to generate H2O2The positive and negative electrodes act synergistically to realize deep oxidative decomposition of phenol pollutants, so that the aim of electrolytic oxidation treatment of the phenol-containing wastewater is fulfilled; wherein the number of the anode plates is 1 and 2 respectively, the number of the cathode plates is 2 and 3 respectively, the anodes and the cathodes are alternately arranged, the distance between the adjacent electrode plates is 20mm, and the effective electrode plate areas of the anodes and the cathodes are 1200cm respectively2、2400cm2The power supply for electrolysis adopts a steady-current direct-current power supply, and the current density is 30mA/cm2The hydraulic retention time in the electrolytic cell is 60min, the wastewater treatment results are shown in Table 3,
the anode reaction is as follows:
the cathode reaction is as follows:
the phenol oxidative decomposition reaction comprises the following steps:
the results in Table 3 show that under the same current density and electrolysis time conditions, the removal rate of the volatile phenol in 2 anode electrolysis processes is 1.6 times that of 1 polar plate, and the removal rate of the volatile phenol in COD is 1.6 times that of the volatile phenol in 2 anode electrolysis processesCr、BOD5The removal rate is 1.3 times and 1.6 times of that of 1 polar plate respectively.
TABLE 3 results of wastewater treatment
The monitoring method comprises the following steps: CODCr、BOD5Phenol, pH and the like are prepared by corresponding methods specified in Water and wastewater monitoring and analyzing method which is compiled by the State environmental protection administration.
Example 4:
the implementation scheme and the working principle of the invention are as follows: the process for the treatment of wastewater containing 24.7mg/L phenol without stirring, internal circulation and double-synergistic electrolytic oxidation is the same as that of example 3, and the results of the wastewater treatment are shown in Table 4,
the anode reaction is as follows:
the cathode reaction is as follows:
the phenol oxidative decomposition reaction comprises the following steps:
TABLE 4 results of wastewater treatment
The monitoring method comprises the following steps: CODCr、BOD5Phenol, pH and the like are prepared by corresponding methods specified in Water and wastewater monitoring and analyzing method which is compiled by the State environmental protection administration.
The results in Table 4 show that under the same current density and electrolysis time conditions, the removal rate of volatile phenol by 2 anode electrolysis processes is 1.3 times that of 1 polar plate, and COD is reducedCr、BOD5The removal rate is 1.3 times and 1.4 times of that of 1 polar plate respectively.
In conclusion, the effective area of the polar plate is 2400cm2In the plate-frame type polypropylene electrolytic tank with the distance between the adjacent polar plates of 20mm, Ti-based PbO is used2The electrode is an anode, the stainless steel is a cathode, and the current density is 30mA/cm2Hydraulic retention time 60minThe steady flow direct current electrolysis process of the invention has no stirring, internal circulation and double-synergistic electrolytic oxidation treatment process of the phenol-containing wastewater, the volatile phenol content reaches 92 percent, and the COD is treatedCr、BOD5The removal rate reaches 91 percent and is over 75 percent respectively, the B/C ratio is greatly increased, the biochemical property of the wastewater is improved, and the effluent reaches the third-level standard of GB8978-1996 Integrated wastewater discharge Standard.
Compared with the prior art, the process for treating the phenol-containing wastewater by the double-synergistic electrolytic oxidation without stirring and internal circulation basically does not need to add chemicals, has the advantages of small equipment volume, easy operation, small sludge amount, simple post-treatment and the like, overcomes the problem of high energy consumption caused by a large amount of side reactions such as oxygen evolution and hydrogen evolution in the similar technology, and has very important market development prospect.
Claims (1)
1. An electrolytic oxidation treatment process of phenol-containing wastewater, which is characterized in that Ti-based PbO is adopted2The electrode is an anode, the stainless steel is a cathode, the waste water containing phenol is electrolyte, and the electrode is placed on the anode through electrolysisGenerating strong oxidizing radical-hydroxyl radical-OH by electricity, and obtaining electrons from cathode to form H2O2The deep oxidative decomposition of phenol pollutants is realized by the synergistic action of the anode and the cathode, so that the aim of electrolytic oxidation treatment of the phenol-containing wastewater is fulfilled; wherein, the anodes and the cathodes are arranged alternately, the number of the cathode plates is 1 more than that of the anode plates, the distance between the adjacent electrode plates is 20mm, the power supply for electrolysis adopts a voltage-stabilizing direct-current power supply, the current density is 30mA/cm2The electrolyte in the electrolytic cell is internally circulated without stirring,
the anode reaction is as follows:
the cathode reaction is as follows:
the phenol oxidative decomposition reaction comprises the following steps:
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Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100336735C (en) * | 2004-03-12 | 2007-09-12 | 云南大学 | Method and apparatus for treating high concentrated organic wastewater by hydrothermal electrical catalytic oxidation |
| CN100352770C (en) * | 2006-01-23 | 2007-12-05 | 南京大学 | Integrated process for treating waste water of p-aminophenol production and resource recovery method |
| CN100408485C (en) * | 2006-09-27 | 2008-08-06 | 蓝星化工新材料股份有限公司无锡树脂厂 | Method of circulation utilizing phenol containing waste water in novolac epoxy preparing process |
| CN100436336C (en) * | 2005-12-12 | 2008-11-26 | 中国科学院过程工程研究所 | Enzyme electric coupling catalyzation for treating waste water containing phenol, aromatic amine and azo-dye |
| CN101508477B (en) * | 2009-03-19 | 2010-10-20 | 扬州大学 | Electrochemical oxidation processing method for wastewater containing anthraquinone dye |
| CN101016632B (en) * | 2006-12-22 | 2010-11-24 | 扬州大学 | Process of preparing metal oxide electrode by polymeric precursor thermal decomposition method |
| CN102092878A (en) * | 2010-12-08 | 2011-06-15 | 湖州森蓝环境工程有限公司 | Treatment method of heavy metal organic industrial waste water |
| CN102211829A (en) * | 2010-04-01 | 2011-10-12 | 上海晶园环保科技有限公司 | Advanced oxidation device and method for treating high-concentration organic substance wastewater |
| CN102219338A (en) * | 2011-04-15 | 2011-10-19 | 北京师范大学 | Method for removing organic contaminants in water through electrochemical oxidation and biological enzyme catalyzing |
| CN102276025A (en) * | 2011-07-04 | 2011-12-14 | 武汉大学 | Electro-Fenton apparatus for processing organic wastewater |
| CN101898116B (en) * | 2009-05-25 | 2012-06-13 | 奇迪电器集团有限公司 | Filter medium and preparation method thereof, filter element, water purifier and water dispenser |
| CN102502946A (en) * | 2011-12-26 | 2012-06-20 | 天津大学 | Method for treating chemical wastewater by utilizing three-dimensional electrode-biological membrane process |
| CN101844006B (en) * | 2009-03-27 | 2012-09-05 | 奇迪电器集团有限公司 | Filter medium and preparation method thereof, filter element, water purification device and water dispenser |
| CN102701337A (en) * | 2012-05-29 | 2012-10-03 | 中国科学院过程工程研究所 | Method and reactor for removing organic matters by enzyme electrode coupled electroflocculation |
| CN104495989A (en) * | 2014-12-24 | 2015-04-08 | 武汉大学 | Electrochemical oxidation device for advanced treatment of wastewater produced by amidoximation |
| CN105858823A (en) * | 2016-05-12 | 2016-08-17 | 安徽国能亿盛环保科技有限公司 | Phenol-containing wastewater treatment process |
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2003
- 2003-09-24 CN CN 03151224 patent/CN1247467C/en not_active Expired - Fee Related
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| CN100336735C (en) * | 2004-03-12 | 2007-09-12 | 云南大学 | Method and apparatus for treating high concentrated organic wastewater by hydrothermal electrical catalytic oxidation |
| CN100436336C (en) * | 2005-12-12 | 2008-11-26 | 中国科学院过程工程研究所 | Enzyme electric coupling catalyzation for treating waste water containing phenol, aromatic amine and azo-dye |
| CN100352770C (en) * | 2006-01-23 | 2007-12-05 | 南京大学 | Integrated process for treating waste water of p-aminophenol production and resource recovery method |
| CN100408485C (en) * | 2006-09-27 | 2008-08-06 | 蓝星化工新材料股份有限公司无锡树脂厂 | Method of circulation utilizing phenol containing waste water in novolac epoxy preparing process |
| CN101016632B (en) * | 2006-12-22 | 2010-11-24 | 扬州大学 | Process of preparing metal oxide electrode by polymeric precursor thermal decomposition method |
| CN101508477B (en) * | 2009-03-19 | 2010-10-20 | 扬州大学 | Electrochemical oxidation processing method for wastewater containing anthraquinone dye |
| CN101844006B (en) * | 2009-03-27 | 2012-09-05 | 奇迪电器集团有限公司 | Filter medium and preparation method thereof, filter element, water purification device and water dispenser |
| CN101898116B (en) * | 2009-05-25 | 2012-06-13 | 奇迪电器集团有限公司 | Filter medium and preparation method thereof, filter element, water purifier and water dispenser |
| CN102211829A (en) * | 2010-04-01 | 2011-10-12 | 上海晶园环保科技有限公司 | Advanced oxidation device and method for treating high-concentration organic substance wastewater |
| CN102092878A (en) * | 2010-12-08 | 2011-06-15 | 湖州森蓝环境工程有限公司 | Treatment method of heavy metal organic industrial waste water |
| CN102092878B (en) * | 2010-12-08 | 2013-04-24 | 湖州森蓝环境工程有限公司 | Treatment method of heavy metal organic industrial waste water |
| CN102219338A (en) * | 2011-04-15 | 2011-10-19 | 北京师范大学 | Method for removing organic contaminants in water through electrochemical oxidation and biological enzyme catalyzing |
| CN102276025A (en) * | 2011-07-04 | 2011-12-14 | 武汉大学 | Electro-Fenton apparatus for processing organic wastewater |
| CN102502946A (en) * | 2011-12-26 | 2012-06-20 | 天津大学 | Method for treating chemical wastewater by utilizing three-dimensional electrode-biological membrane process |
| CN102701337A (en) * | 2012-05-29 | 2012-10-03 | 中国科学院过程工程研究所 | Method and reactor for removing organic matters by enzyme electrode coupled electroflocculation |
| CN104495989A (en) * | 2014-12-24 | 2015-04-08 | 武汉大学 | Electrochemical oxidation device for advanced treatment of wastewater produced by amidoximation |
| CN105858823A (en) * | 2016-05-12 | 2016-08-17 | 安徽国能亿盛环保科技有限公司 | Phenol-containing wastewater treatment process |
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