CN1850644A - Three-dimensional electrode reactor for treating hard-degradeable organic waste water - Google Patents
Three-dimensional electrode reactor for treating hard-degradeable organic waste water Download PDFInfo
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- CN1850644A CN1850644A CN 200610081233 CN200610081233A CN1850644A CN 1850644 A CN1850644 A CN 1850644A CN 200610081233 CN200610081233 CN 200610081233 CN 200610081233 A CN200610081233 A CN 200610081233A CN 1850644 A CN1850644 A CN 1850644A
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Abstract
The invention relates to a waste water processing device, connected of at least two unit reaction chambers, where adjacent unit reaction chambers share a case wall, the shared case wall of each unit reaction chamber and a case wall parallel and opposite to it are made with a row of flow guide holes each, where a row is far from particle electrode flow guide bucket and the other row is close to the bucket; feed electrodes are arranged in the unit reaction chamber, and insulated support rod passes through the feed electrode and is fixed on the case wall, and the particle bucket is arranged at the bottom, and an aeration device is arranged below the bucket, and particle electrodes are distributed in the unit reaction chamber; at least two feed rods are used to supply power to the feed rods, and it is provided with water inlet and outlet.
Description
Technical field:
The present invention relates to a kind of wastewater treatment equipment, particularly a kind of apparatus for electrochemical treatment of organic wastewater with difficult degradation thereby.
Background technology:
The processing of organic wastewater with difficult degradation thereby is that of field of waste water treatment studies focus and difficult point, investigators also proposed many treatment processs at organic wastewater with difficult degradation thereby, wherein electrochemical process is handled waste water and generally be need not a lot of pharmaceutical chemicalss, aftertreatment is simple, floor space is little, convenient management, sludge quantity are seldom.It is a kind of green technology that can satisfy technico-economical comparison advanced person, 3 basic demands such as nontoxic and free from environmental pollution simultaneously.Yet relevant research is confined to the two-dimensional flat plate electrode more, because two-dimensional electrode face body causes mass-transfer efficiency low than for a short time, causes treatment effect lower, so fail to be widely used in practice.Phase late 1960s has proposed three-diemsnional electrode three-dimension-electrode) notion.3 D electrode reactor is a kind of novel electrochemical reactor, is granule electrode particle-electrode again) or bed electrode bed-electrode).It is granular or other fragmental working electrode material of filling and make filling working electrode material surface charging between the conventional two-dimensional electrolytic tank electrode, becomes a new utmost point the 3rd utmost point), in working electrode material surface energy generation electrochemical reaction.By contrast, three-diemsnional electrode increases because of its face body ratio, and interionic distance is from little, and mass transfer effect is good, and the current efficiency height has treatment effect preferably.But the reactor design scheme that can use is not in practice also arranged at present.
Summary of the invention:
The objective of the invention is for provide a kind of can be at the 3 D electrode reactor of practical application in industry.
In order to achieve the above object, the present invention adopts following technical scheme: reactor adopts the fluidized-bed form, totally according to idea of modular.Whole reactor is connected and composed by at least two unit process chambers, the shared shell wall of adjacent cells reaction chamber, offer 1 row's pod apertures on two parallel relative shell walls of each unit process chamber respectively, pod apertures on one of them shell wall is away from granule electrode water conservancy diversion bucket, and the pod apertures on the another one shell wall is near granule electrode water conservancy diversion bucket; The reaction chamber shell wall connects and composes the housing of reactor, and unit process is indoor the feed electrode that is arranged in parallel, and passes the feed electrode with insulating support rod and is fixed; Bottom, unit process chamber is provided with granule electrode water conservancy diversion bucket, and at the arranged beneath aerating apparatus of granule electrode water conservancy diversion bucket, granule electrode is filled branch in the middle of the whole unit reaction chamber under the effect of current air-flow; In the reaction chamber outside, respectively to the feed electrode power supply, one is connected with all anode feed electrodes by at least two feeder pillars; Feed electrode and aerator in each reaction chamber can be installed separately and change.
The feed electrode adopts stainless steel plate, and the cathode-anode plate parallel interval arranges that water (flow) direction was vertical when its direction was moved with reactor, and polar plate spacing is 6～10mm, and two groups of pole plates carry out feed by feeder pillar respectively.It is electrode materials that granule electrode adopts columnar activated carbon, and particle diameter is 1.5～4mm, is fluidization owing to the aeration effect in reactor.In order to prevent that the part from the dead angle occurring and causing build-up of particles, particle water conservancy diversion bucket is set at reactor bottom.
During the reactor operation, offer constant voltage of feed electrode by external direct current power supply by feeder pillar, granule electrode is in electric field action lower surface generation repolarization, produce the OH group with strong oxidizing property under electrochemical action, the hardly degraded organic substance in OH group and waste water reaction rapidly makes it obtain degraded.
Description of drawings:
Fig. 13 D electrode reactor top plan view
The positive cross-sectional schematic in Fig. 2 unit process chamber
Side, Fig. 3 unit process chamber cross-sectional schematic
Embodiment:
Come embodiment is specifically described below in conjunction with accompanying drawing, as shown in Figure 1, whole reactor is a rectangle, and being linked to each other by 16 unit process chambers forms, and each unit process chamber useful volume is 0.625m
3, the quantity of unit process chamber is calculated according to the residence time according to the water yield of handling in the whole reactor.Retention time of sewage is 45～90min.As shown in Figure 2, offer pod apertures 7 on the shared shell wall of adjacent cells reaction chamber, waste water seethes mobile up and down along pod apertures in the middle of the unit process chamber.In each element cell, thoroughly do away with edge support bars 6 with 4 and pass feed electrode 4 pole plate is fixed, adopt insulating washer to intercept between feed electrode 4 pole plates, be shelved on the supporter that is welded in advance on the reactor wall.Granule electrode 9 is being the fluidization campaign under air-flow and the flow action between reactor and feed electrode 4, part granule electrode 9 since the gravity settling effect along the domatic sinking of particle water conservancy diversion bucket, again blown afloat by air-flow when the centre is compiled, aerating apparatus 8 links to each other with external source of the gas by pipeline.Two feeder pillars 5 connect respectively by lead powers to feed electrode 4, and one is connecting all anode feed electrodes, and other one connects all cathode feed electrodes.
Adopt the 3 D electrode reactor of foregoing invention to handle antibiotic pharmaceutical wastewater, get the pending waste water of a series of COD concentration, CODcr is respectively 3000mg/L, 2000mg/L, 1000mg/L, pH=7.The residence time of choosing waste water during processing is 60min, at polar plate spacing=8mm, and polar plate voltage=18V, the COD degradation rate that changes waste water under the treatment condition of pH=8 can reach 67.2%, 65.4%, 68.3% respectively;
And the two-dimensional flat plate electrode is under the optimization experiment condition, and its treatment effect is respectively 23.4%, 18.5%, 15.7%.Comparatively speaking, use the obvious processing effect of 3 D electrode reactor, degradation rate is more stable; The B/C value of waste water reaches 0.36 after the processing by about 0.15 before handling, and has obtained improving largely in the biodegradability through waste water after the reactor for treatment.
Claims (7)
1. 3 D electrode reactor of handling organic wastewater with difficult degradation thereby, it is characterized in that, at least connect to form by two unit process chambers, the shared shell wall of adjacent cells reaction chamber, offer 1 row's pod apertures (7) on the shared shell wall of each unit process chamber and the relative shell wall in parallel respectively, pod apertures on one of them shell wall (7) is away from granule electrode water conservancy diversion bucket (10), and the pod apertures on the another one shell wall (7) is near granule electrode water conservancy diversion bucket (10); The reaction chamber shell wall connects and composes the housing (1) of reactor, the indoor feed electrode (4) that is equipped with of unit process, insulating support rod (6) passes feed electrode (4) and is fixed on the shell wall, bottom, unit process chamber is provided with granule electrode water conservancy diversion bucket (10), at the arranged beneath aerating apparatus (8) of granule electrode water conservancy diversion bucket (10), granule electrode (9) is filled branch in the middle of the unit process chamber; In the unit process outdoor, respectively to feed electrode (4) power supply, one is connected with all anode feed electrodes by at least two feeder pillars (5), and other one is connected with the cathode feed electrode, is provided with water-in (2) and water outlet (3) at reactor.
2. reactor according to claim 1 is characterized in that feed electrode (4) is made up of the stainless steel plate that is arranged in parallel.
3. reactor according to claim 2 is characterized in that the spacing between the stainless steel plate is 6～10mm.
4. reactor according to claim 1 is characterized in that the granule electrode (9) that adopts is the columnar activated carbon particle.
5. reactor according to claim 4 is characterized in that the columnar activated carbon particle grain size is 1.5～4mm.
6. reactor according to claim 1 is characterized in that the filling ratio of granule electrode (9) in reactor is 50%～70%.
7. reactor according to claim 1 is characterized in that being provided with in the bottom of each unit process chamber particle water conservancy diversion bucket (10), and forming the domatic and bottom surface angle of four of bucket is 120 °～150 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNB2006100812334A CN100384752C (en) | 2006-05-26 | 2006-05-26 | Three-dimensional electrode reactor for treating hard-degradeable organic waste water |
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| CNB2006100812334A CN100384752C (en) | 2006-05-26 | 2006-05-26 | Three-dimensional electrode reactor for treating hard-degradeable organic waste water |
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| CN1850644A true CN1850644A (en) | 2006-10-25 |
| CN100384752C CN100384752C (en) | 2008-04-30 |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101224401B (en) * | 2007-10-19 | 2010-07-07 | 东华大学 | Fixed bed inhomogeneous three dimensional electrode photo electrocatalysis reactor |
| CN101811794A (en) * | 2010-05-11 | 2010-08-25 | 中国环境科学研究院 | Method for pretreating industrial wastewater of ABS (Acrylonitrile Butadiene Styrene) resin |
| CN101857309A (en) * | 2010-06-12 | 2010-10-13 | 浙江工商大学 | Electrochemical biological combined denitrification reactor |
| CN102020342A (en) * | 2011-01-14 | 2011-04-20 | 南京大学 | Compound three-dimensional electrode reactor and application thereof in treatment of nitrogenous organic wastewater |
| CN102491459A (en) * | 2011-12-02 | 2012-06-13 | 北京化工大学 | Nonmetal doped titanium-based film electrode as well as preparation method and application thereof |
| CN102502924A (en) * | 2011-10-27 | 2012-06-20 | 浙江理工大学 | Method for deeply treating alpha-naphthylamine wastewater |
| CN103304008A (en) * | 2013-07-10 | 2013-09-18 | 武汉大学 | Method for treating organic wastewater by using ferroferric oxide particle electrode in cooperation with electrochemical oxidization |
| CN106517487A (en) * | 2017-01-17 | 2017-03-22 | 中冶赛迪工程技术股份有限公司 | Modular multi-tube Fenton fluidized bed reactor |
| CN106986426A (en) * | 2017-05-09 | 2017-07-28 | 中国矿业大学 | A kind of bed electrode reactor design method for wastewater treatment |
| CN112811676A (en) * | 2020-12-30 | 2021-05-18 | 黑晶科技(嘉兴)有限公司 | Method for degrading antibiotic-containing wastewater by using geopolymer particle three-dimensional electrode |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1151084C (en) * | 2002-01-16 | 2004-05-26 | 中山大学 | Three-dimension electrode reactor and use for treating organic waste water |
| CN1203005C (en) * | 2003-07-11 | 2005-05-25 | 天津大学 | 3-D electrode-membrane reactor with potential measurement and control funtion |
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2006
- 2006-05-26 CN CNB2006100812334A patent/CN100384752C/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101224401B (en) * | 2007-10-19 | 2010-07-07 | 东华大学 | Fixed bed inhomogeneous three dimensional electrode photo electrocatalysis reactor |
| CN101811794A (en) * | 2010-05-11 | 2010-08-25 | 中国环境科学研究院 | Method for pretreating industrial wastewater of ABS (Acrylonitrile Butadiene Styrene) resin |
| CN101811794B (en) * | 2010-05-11 | 2011-07-20 | 中国环境科学研究院 | Method for pretreating industrial wastewater of ABS (Acrylonitrile Butadiene Styrene) resin |
| CN101857309A (en) * | 2010-06-12 | 2010-10-13 | 浙江工商大学 | Electrochemical biological combined denitrification reactor |
| CN102020342A (en) * | 2011-01-14 | 2011-04-20 | 南京大学 | Compound three-dimensional electrode reactor and application thereof in treatment of nitrogenous organic wastewater |
| CN102502924A (en) * | 2011-10-27 | 2012-06-20 | 浙江理工大学 | Method for deeply treating alpha-naphthylamine wastewater |
| CN102491459A (en) * | 2011-12-02 | 2012-06-13 | 北京化工大学 | Nonmetal doped titanium-based film electrode as well as preparation method and application thereof |
| CN102491459B (en) * | 2011-12-02 | 2013-06-19 | 北京化工大学 | Nonmetal doped titanium-based film electrode as well as preparation method and application thereof |
| CN103304008A (en) * | 2013-07-10 | 2013-09-18 | 武汉大学 | Method for treating organic wastewater by using ferroferric oxide particle electrode in cooperation with electrochemical oxidization |
| CN106517487A (en) * | 2017-01-17 | 2017-03-22 | 中冶赛迪工程技术股份有限公司 | Modular multi-tube Fenton fluidized bed reactor |
| CN106986426A (en) * | 2017-05-09 | 2017-07-28 | 中国矿业大学 | A kind of bed electrode reactor design method for wastewater treatment |
| CN106986426B (en) * | 2017-05-09 | 2020-05-05 | 中国矿业大学 | Design method of bed electrode reactor for wastewater treatment |
| CN112811676A (en) * | 2020-12-30 | 2021-05-18 | 黑晶科技(嘉兴)有限公司 | Method for degrading antibiotic-containing wastewater by using geopolymer particle three-dimensional electrode |
| CN112811676B (en) * | 2020-12-30 | 2023-08-15 | 黑晶科技(嘉兴)有限公司 | Method for degrading antibiotic-containing wastewater by using geopolymer particle three-dimensional electrode |
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| CN100384752C (en) | 2008-04-30 |
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