CN106006857A - Method for degrading organic dye wastewater through graphene electrode and photoelectric Feton cooperatively - Google Patents

Method for degrading organic dye wastewater through graphene electrode and photoelectric Feton cooperatively Download PDF

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Publication number
CN106006857A
CN106006857A CN201610547239.XA CN201610547239A CN106006857A CN 106006857 A CN106006857 A CN 106006857A CN 201610547239 A CN201610547239 A CN 201610547239A CN 106006857 A CN106006857 A CN 106006857A
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China
Prior art keywords
electrode
organic dye
waste water
dye waste
degrading organic
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CN201610547239.XA
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Chinese (zh)
Inventor
程庆利
刘栓
陶彬
张卫华
刘全祯
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China Petroleum and Chemical Corp
Sinopec Qingdao Safety Engineering Institute
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China Petroleum and Chemical Corp
Sinopec Qingdao Safety Engineering Institute
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Priority to CN201610547239.XA priority Critical patent/CN106006857A/en
Publication of CN106006857A publication Critical patent/CN106006857A/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/722Oxidation by peroxides
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/308Dyes; Colorants; Fluorescent agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/02Specific form of oxidant
    • C02F2305/026Fenton's reagent
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/10Photocatalysts
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Abstract

The invention discloses a method for degrading organic dye wastewater through graphene electrode and photoelectric Feton cooperatively. The method includes the steps that firstly, graphene and valence-variable metallic oxide are mixed, emulgator, absolute ethyl alcohol and teflon are added to the mixture in sequence, and the mixture is dispersed evenly through an ultrasound function till paste in a cohesion form is mixed and formed; then, the obtained paste is ground into a film, the film is attached to a nickel net and pressed into an electrode under certain pressure, and residues on the surface of the electrode are removed; the soaked electrode is placed in an infrared box to be dried, and a graphite composite electrode is obtained; the graphite composite electrode serves as the cathode, sheet iron serves as an anode, an illumination device is switched on, and organic dye wastewater is degraded by illuminating an electrolytic cell with sunlight. The sunlight is added to an electric Fenton reaction to form an electric Fenton system, and the method is applied to a dye wastewater treatment practice and improves dye wastewater degradation capacity.

Description

Graphene electrodes and the method for photoelectricity Feton Synergistic degradation organic dye waste water
Technical field
The present invention relates to Organic Dyestuff Wastewater Treatment technical field, be specifically related to a kind of Graphene electrodes and the collaborative fall of photoelectricity Feton The method solving organic dye waste water.
Background technology
Fenton high-level oxidation technology can be used to process waste water from dyestuff and various toxic organic pollutant.In Fenton reaction The hydroxyl radical free radical activity generated is big, and oxidizing potential is high, can directly by oxidation operation mineralising, generation water, carbon dioxide and Inorganic ions, Fenton system, mainly in the case of energising, produces H in cathode chamber electro-catalysis2O2, in the solution with appraise at the current rate Metal ion is (such as Fe3+/Fe2+Deng) reaction generation strong oxidizer hydroxyl radical free radical (OH), OH activity is high, and oxidability is strong, Can effectively degrade even mineralising toxic organic pollutants.
But, simple relies on Fenton oxidation technology poor to the degradation effect of waste water from dyestuff.
Summary of the invention
In order to solve the technical problem of dye wastewater degradation weak effect present in above-mentioned prior art, the present invention proposes a kind of stone Ink alkene electrode and the method for photoelectricity Feton Synergistic degradation organic dye waste water, add to sunlight in Fenton reaction and formed Photoelectro-Fenton process system, is applied in dye wastewater treatment practice, the method increases the degradation capability to waste water from dyestuff.
Its technical solution includes:
A kind of method of degrading organic dye waste water, comprises the following steps successively:
The first step, preparation electrolysis unit, the electrolyte including electrolysis bath, being positioned at electrolysis bath and two electrodes, wherein, with ferrum Sheet is as anode, using graphite combination electrode as negative electrode, arranges magnetic stirring apparatus in described electrolysis bath;
Second step, illumination apparatus is set on described electrolysis unit side, opens electrolysis bath described in illumination apparatus sunlight, Adding organic dye waste water in described electrolysis bath, open magnetic stirring apparatus, controlling voltage is 3~4V, organic dye waste water PH is 3~5, at room temperature degrades organic dye waste water.
As a preferred version of the present invention, the preparation method of above-mentioned graphite combination electrode includes:
First, graphite and variable valency metal oxide are mixed, are added thereto to emulsifying agent, dehydrated alcohol and politef successively, Ultrasonication makes it be uniformly dispersed, until being mixed to form the mastic of cohesion shape;
Secondly, gained mastic is rolled into the film that thickness is 2~3mm, and is attached on nickel screen, press under pressure Make electrode, this electrode is soaked removing surface residue in organic solvent;
Finally, the electrode after soaking is placed in infrared case, arranges temperature 80 DEG C insulation 2h, obtains graphite combination electrode.
Preferably, electrolysis bath described in radiation of visible light is selected, it is seen that light is external lighting type.
Preferably, variable valency metal oxide is MnO2, nanometer Fe3O4Or nanometer Cu2O。
Preferably, under the pressure of 10~30MPa, it is pressed into electrode.
Preferably, above-mentioned organic solvent is acetone soln.
Preferably, above-mentioned dehydrated alcohol is 1~2:1 with the volume ratio of politef.
Compared with prior art, the present invention forms photoelectro-Fenton process during visible ray or sunlight add to Fenton reaction In system, it is applied in dye wastewater treatment, can be with sensitizing dyestuff under visible light exposure, dye molecule can be broken down into little Molecule and inorganic ions;Good with electric conductivity, the graphite that hydrogen-evolution overpotential is higher is that substrate cathode prepares material, is not sacrificing H2O2 On the basis of productivity, variable valency metal oxide is combined with graphite, prepares graphite combination electrode, by homemade graphite is combined Electrode is as negative electrode, and it produces H2O2Electro-catalysis efficiency high, in Fenton system, the H that negative electrode is newly-generated2O2Can be direct With metal-oxide generation heterogeneous Fenton, extend the sewage disposal pH scope of Fenton system, simple to operate, bar Part is easily-controllable.
Fenton high-level oxidation technology is combined by the present invention with photocatalysis, and the two can have engine dyeing with concerted catalysis degraded Material waste water, it is seen that light can have obvious concerted catalysis effect with sensitizing dyestuff, photoelectro-Fenton process system is effectively improved dyestuff and gives up The mineralization degree of water.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings the present invention is described in further details:
Fig. 1 is installation drawing of the present invention;
Fig. 2 is in dark reaction, visible light photocatalysis, Fenton system and photoelectro-Fenton process system in the embodiment of the present invention 1 To 7g/L rhdamine B wastewater degradation kinetic curve figure;
Fig. 3 is the embodiment of the present invention 3 under different tableting pressure (respectively 10MPa, 20MPa, 25MPa, 30MPa) to dye That expects wastewater degradation speed affects figure;
In Fig. 1,1, illumination apparatus, 2, electrolysis bath, 3, anode-iron plate, 4, negative electrode-graphite combination electrode, 5, unidirectional current Source, 6, magnetic stirring apparatus.
Detailed description of the invention
The present invention proposes a kind of Graphene electrodes and the method for photoelectricity Feton Synergistic degradation organic dye waste water, in order to make this Bright advantage, technical scheme are clearer, clear and definite, elaborate the present invention below in conjunction with specific embodiment.
As it is shown in figure 1, device of the present invention, including illumination apparatus 1, electrolysis unit 2 and magnetic stirring apparatus 6, wherein, Illumination apparatus 1 is positioned at electrolysis unit side, and it provides light source to irradiate electrolysis unit 2, and light source can be with simulated solar irradiation, it is also possible to For visible ray, electrolysis unit include electrolysis bath 2, the anode-iron plate 3 being positioned at electrolysis bath 2 and negative electrode-graphite combination electrode 4, And it is positioned at the DC source 5 above electrolysis bath, given up to being passed through organic dyestuff therein in advance by magnetic stirring apparatus 6 at electrolysis bath 2 Water is sufficiently stirred for.
Below in conjunction with said apparatus and embodiment, the present invention will be further described.
Embodiment 1:
The present invention, the method for degrading organic dye waste water, specifically include following steps:
First prepare graphite combination electrode, weigh 10g graphite, add 2 " OP " emulsifying agents, 3mL dehydrated alcohol and 1.0g Politef, ultrasonic making is uniformly dispersed, until mixture forms cohesion shape mastic, mastic is rolled into the film of about 2mm, It is attached on stainless (steel) wire, under 30MPa pressure, suppresses to obtain electrode, in acetone soln, soak 2h remove electrode surface residual Ethanol and " OP " emulsifying agent;In infrared case, 80 DEG C of insulation 2h, i.e. make graphite electrode, its final size: floor space × height =1.0cm2×5mm;
Secondly, using the graphite combination electrode for preparing as negative electrode, iron plate, as anode, throws rhdamine B in electrolysis bath Waste water, the dosage of rhdamine B waste water is 7g/L, and Fenton system applied voltage is 3V, by sulphuric acid regulation dye The pH of material waste water is 3.5, it is seen that light is external lighting type, and employing light source is simulated solar irradiation, and waste water processes and carries out under stirring at room temperature;
Finally, dark reaction, visible light photocatalysis, Fenton system (be not added with light, be energized, stirring) and photoelectricity are carried out respectively Fenton system (visible light exposure, energising, stirring) experiment, degradation kinetics curve is shown in Fig. 2.
In degradation results: 120min, the clearance to peacock green is respectively 0.3%, and 3.5%, 78.5% and 99.7%, photoelectro-Fenton process System is greatly improved the removal efficiency to rhdamine B waste water.
Embodiment 2:
The present invention, the method for degrading organic dye waste water, specifically include following steps:
Prepare graphene combination electrode, weigh 8g Graphene, add 1 " OP " emulsifying agent, 2mL dehydrated alcohol and 1.0g poly- Tetrafluoroethene, ultrasonic making is uniformly dispersed, until mixture forms cohesion shape mastic, mastic is rolled into the film of about 2mm, attached On stainless (steel) wire, under 20MPa pressure, suppress to obtain electrode, in acetone soln, soak 2h remove the second of electrode surface residual Alcohol and " OP " emulsifying agent;In infrared case, 80 DEG C of insulation 2h, i.e. make graphite electrode, its final size: floor space × height=1.0 cm2×5mm;
Being negative electrode by the Graphene electrodes prepared, iron plate is anode, and the dosage of rhdamine B waste water is 5g/L, electricity Fenton system applied voltage is 4V;Sulfur acid for adjusting pH is 3.5, sunlight irradiation, and waste water processes and carries out under stirring at room temperature.
In degradation results: 80min, the clearance to rhodamine B is respectively 97.5%.
Embodiment 3:
The present invention, the method for degrading organic dye waste water, specifically include following steps:
Weigh 8.5g Graphene, add 1 " OP " emulsifying agent, 2.5mL dehydrated alcohol and 1.0g politef, super Sound makes to be uniformly dispersed, until mixture forms cohesion shape mastic, mastic is rolled into the film of about 2mm, is attached to stainless (steel) wire On, suppress to obtain Graphene electrodes at various pressures, in acetone soln soak 2h remove electrode surface residual ethanol and " OP " emulsifying agent, in infrared case, 80 DEG C of insulation 2h, i.e. make graphite electrode, its final size: floor space × height=1.0cm2×5 mm;
Being negative electrode by the high pure graphite electrode prepared, iron plate is anode, and the dosage of methyl orange dye waste water is 4g/L, electricity Fenton system applied voltage is 4V;Sulfur acid for adjusting pH is 3.0, sunlight irradiation, and waste water processes and carries out under stirring at room temperature. In 120min, the clearance to Methyl Orange in Wastewater is 98.6%.Respectively under 10MPa, 20MPa, 25MPa, 30MPa tableting pressure To dye wastewater degradation, the figure that affects of degradation rate is shown in Fig. 3.
It should be noted that any equivalent way that those skilled in the art are made under the teaching of this specification, or substantially become Type mode all should be within the scope of the present invention.

Claims (7)

1. the method for a degrading organic dye waste water, it is characterised in that comprise the following steps successively:
The first step, preparation electrolysis unit, the electrolyte including electrolysis bath, being positioned at electrolysis bath and two electrodes, wherein, with ferrum Sheet is as anode, using graphite combination electrode as negative electrode, arranges magnetic stirring apparatus in described electrolysis bath;
Second step, illumination apparatus is set on described electrolysis unit side, opens electrolysis bath described in illumination apparatus sunlight, Adding organic dye waste water in described electrolysis bath, open magnetic stirring apparatus, controlling voltage is 3~4V, organic dye waste water PH is 3~5, at room temperature degrades organic dye waste water.
The method of degrading organic dye waste water the most according to claim 1, it is characterised in that the preparation of described graphite combination electrode Method includes:
First, graphite and variable valency metal oxide are mixed, are added thereto to emulsifying agent, dehydrated alcohol and politef successively, Ultrasonication makes it be uniformly dispersed, until being mixed to form the mastic of cohesion shape;
Secondly, gained mastic is rolled into the film that thickness is 2~3mm, and is attached on nickel screen, press under pressure Make electrode, this electrode is soaked removing surface residue in organic solvent;
Finally, the electrode after soaking is placed in infrared case, arranges temperature 80 DEG C insulation 2h, obtains graphite combination electrode.
The method of degrading organic dye waste water the most according to claim 1, it is characterised in that: select and be electrolysed described in radiation of visible light Groove, described visible ray is external lighting type.
The method of degrading organic dye waste water the most according to claim 2, it is characterised in that: described variable valency metal oxide is MnO2, nanometer Fe3O4Or nanometer Cu2O。
The method of degrading organic dye waste water the most according to claim 2, it is characterised in that: press under the pressure of 10~30MPa Make electrode.
The method of degrading organic dye waste water the most according to claim 2, it is characterised in that: described organic solvent is acetone soln.
The method of degrading organic dye waste water the most according to claim 2, it is characterised in that: described dehydrated alcohol and polytetrafluoroethyl-ne The volume ratio of alkene is 1~2:1.
CN201610547239.XA 2016-07-12 2016-07-12 Method for degrading organic dye wastewater through graphene electrode and photoelectric Feton cooperatively Pending CN106006857A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107352703A (en) * 2017-05-19 2017-11-17 江苏大地益源环境修复有限公司 A kind of nearly method and apparatus in situ for removing heavy metal ion in underground water
CN108190997A (en) * 2017-12-08 2018-06-22 浙江工业大学 A kind of intensive control method of photoelectricity Fenton pretreatment tea polyphenols pharmacy waste water
CN108249545A (en) * 2018-03-09 2018-07-06 南京大学 A kind of photoelectricity-Fenton azo dye wastewaters treatment reactor and application method
CN109399765A (en) * 2017-08-16 2019-03-01 南京理工大学 Utilize the method for amorphous alloy electrochemical degradation azo dyes

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104525201A (en) * 2015-01-05 2015-04-22 华东理工大学 Non-homogeneous-phase Fenton catalyst with magnetism and preparing method and application thereof
CN105253950A (en) * 2015-11-13 2016-01-20 中国科学院宁波材料技术与工程研究所 Method and equipment for degrading organic waste water through UV-light concerted electro-Fenton system
CN105417638A (en) * 2015-11-13 2016-03-23 中国科学院宁波材料技术与工程研究所 Heterogeneous electric Fenton system and preparation and application thereof
CN105731624A (en) * 2014-12-11 2016-07-06 中国石油天然气股份有限公司 Method for treating reverse osmosis concentrated water through heterogeneous Fenton-like reaction catalytic oxidization

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105731624A (en) * 2014-12-11 2016-07-06 中国石油天然气股份有限公司 Method for treating reverse osmosis concentrated water through heterogeneous Fenton-like reaction catalytic oxidization
CN104525201A (en) * 2015-01-05 2015-04-22 华东理工大学 Non-homogeneous-phase Fenton catalyst with magnetism and preparing method and application thereof
CN105253950A (en) * 2015-11-13 2016-01-20 中国科学院宁波材料技术与工程研究所 Method and equipment for degrading organic waste water through UV-light concerted electro-Fenton system
CN105417638A (en) * 2015-11-13 2016-03-23 中国科学院宁波材料技术与工程研究所 Heterogeneous electric Fenton system and preparation and application thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
JURATE VIRKUTYTE等: "《光和废水除微污染技术》", 30 June 2013 *
周曼: "非铁基芬顿(Fenton)体系高级氧化技术的发展和现状", 《化学工程与装备》 *
陈国华: "《环境污染治理方法原理与工艺》", 30 September 2003 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107352703A (en) * 2017-05-19 2017-11-17 江苏大地益源环境修复有限公司 A kind of nearly method and apparatus in situ for removing heavy metal ion in underground water
CN107352703B (en) * 2017-05-19 2020-10-02 江苏大地益源环境修复有限公司 Method and equipment for removing heavy metal ions in underground water in near-situ manner
CN109399765A (en) * 2017-08-16 2019-03-01 南京理工大学 Utilize the method for amorphous alloy electrochemical degradation azo dyes
CN108190997A (en) * 2017-12-08 2018-06-22 浙江工业大学 A kind of intensive control method of photoelectricity Fenton pretreatment tea polyphenols pharmacy waste water
CN108249545A (en) * 2018-03-09 2018-07-06 南京大学 A kind of photoelectricity-Fenton azo dye wastewaters treatment reactor and application method
CN108249545B (en) * 2018-03-09 2023-12-26 南京大学 photoelectric-Fenton azo dye wastewater treatment reactor and use method thereof

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Application publication date: 20161012