CN202265445U - Multiphase repolarization electro-catalysis industrial effluent treatment system for removing biological toxicity efficiently - Google Patents
Multiphase repolarization electro-catalysis industrial effluent treatment system for removing biological toxicity efficiently Download PDFInfo
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Abstract
The utility model discloses a multiphase repolarization electro-catalysis industrial effluent treatment system for removing biological toxicity efficiently. The multiphase repolarization electro-catalysis industrial effluent treatment system comprises a reactor shell, wherein the reactor shell is divided into a water inlet area, an electrolytic reaction area, a water outlet area and a precipitation area; the water inlet area consists of a water inlet spray nozzle and a water distribution partition plate which is perpendicular to the water inlet spray nozzle; a channel is reserved between the bottom edge of the water distribution partition plate and the reactor shell; the electrolytic reaction area consists of an anode and cathodes which are arranged in the reactor shell, and the bottom of the electrolytic reaction area is provided with an aeration system; the anode is a meshed anode, the cathodes are columnar cathodes, a plurality of grid spaces are formed in the meshed anode, and one columnar cathode is arranged in each grid; the water outlet area comprises a water outlet weir plate, an upper water outlet pipe and a lower water outlet pipe; and a channel is reserved between the water outlet weir plate and the top of the reactor shell. According to the multiphase repolarization electro-catalysis industrial effluent treatment system, processes of electro-catalysis oxidation, chemical oxidation, flocculation, air floating, precipitation and the like are combined to form a multielement reaction process, so the multiphase repolarization electro-catalysis industrial effluent treatment system is high in treatment efficiency, low in unit energy consumption, long in service life of electrodes and easy and convenient to operate and maintain.
Description
Technical field
The utility model relates to a kind of treatment technology of waste water, relates in particular to a kind of industrial wastewater treatment system.
Background technology
Development along with The modern industry; Increasing industrial pollution and discharge of wastewater have caused huge burden to aquatic ecosystem; Especially " two-supremes one difficulty " (high pollution substrate concentration, high bio-toxicity, difficult for biological degradation) organic waste water of industries generations such as agricultural chemicals, medicine, chemical industry, dyestuff, process hides is the difficult problem in the environmental pollution improvement always.This type of waste water often pollutant kind is various, and difficulty of governance is big; The waste water ph variation range is bigger, and corrodibility is stronger; The waste water saltiness is high, and bio-toxicity is big, even has teratogenesis, carcinogenic, mutagenic harm.Enter the poisoning that receiving water body not only can cause aquatic animals and plants, the deterioration of aquatic environment, but also can pass through water body, atmosphere and hydrobiological transmission indirect hazard human beings'health.
Bio-toxicity is meant direct or potentially contaminated and the toxicity hazard that certain chemical substance or mixture cause environment, and these chemical substances get into environment can produce certain ecological toxicological effect to biotic population and the coenosis of forming the ecosystem.For example, cause biological acute poisoning dead, cause organism endocrine regulation, reproduction and immunity function imbalance, neurobehavioral and growth disorder etc., even cause various human and plant-animal disease.Its detected result generally uses luminescent bacteria relative inhibition (%) to represent.For Waste Water Treatment; Because that cause bio-toxicity is occurring in nature non-existent artificial-synthetic compound originally mostly; Effectively degrade their mikrobe of these new synthetic compounds owing to do not have; Possibly in enterprise's drainage procedure, accumulate in a large number and get into the subsequent wastewater treatment link, thereby cause the running of biochemical system to lack of proper care even collapse, influence the total system operation stability.Therefore, advanced, efficient, the economic improvement technology of waste water exploitation to this type of high bio-toxicity has important practical significance.
At present, the conventional treatment method of trade effluent is to carry out pre-treatment with physico-chemical process earlier, precipitates, filters out the part pollution substance in the waste water, and then carry out further processing up to standard through biological process.But for the poisonous waste water of high density, conventional method for pretreating can't effectively be removed bio-toxicity, even can be because the secondary pollutant of introducing in the preprocessing process can more influence the effect that follow-up biological process is handled on the contrary.Along with the development of high-level oxidation technology (AOPs), electrochemical oxidation process obtains concern more and more widely.Compare with other AOPs methods, electrochemical process has following advantage:
(1) generally need not the redox processes that outer adding medicine promptly can be realized poisonous pollutant component in the waste water, can effectively avoid secondary pollution problem;
(2) can change reaction conditions at any time through changing impressed current voltage, controllability is more intense;
(3) electrochemical reaction is generally carried out at normal temperatures and pressures, and energy utilization efficiency is high, and reaction conditions is gentle;
(4) structure of reactor is all simple relatively with operation, and the control through reaction conditions can be reduced to working cost in the reasonable range;
(5) when containing heavy metal ion and halide ion in the waste water, can improve redox efficient through indirect reaction, and reclaim useful component;
(6) occupation area of equipment is little, and simple installation has effects such as air supporting, flocculation, deposition, sterilization simultaneously concurrently.
Therefore, the catalytic oxidation method has bigger technical superiority and wide application prospect in the poisonous Industrial Wastewater Treatment of high density field.
Traditional electrocatalysis equipment structure is comparatively simple; Equipment body generally is to be made up of the cathode-anode plate that is staggeredly placed that is parallel to water (flow) direction; General water (flow) direction from up to down; Or through traverse baffle and simple water distribution system fully the contacting of sewage and battery lead plate in the realization response process of trying one's best, thereby reach the purpose of removal pollutent.Shortcomings such as it is little that the traditional electrode of this structure exists specific surface area, and processing efficiency is low, power consumption is high, electrode materials consumption is big are so fail in industry, to obtain to widely apply.
Three-dimensional electrolysis is improved traditional electric catalyticing system, between anode and cathode, has filled the composite particles electrode, thereby has increased greatly and water contacted specific surface area and mass-transfer efficiency.But the short-circuit current and the by-pass current that cause because of skewness between the electrode are the greatest problem that influences the three-diemsnional electrode processing efficiency.Present solution generally is that in electrolyzer, to keep the volume ratio of conductive particle and dielectric particle be 1: 3 or 1: 4; Dielectric medium has occupied most of volume of electrolyzer; Reduced the effective working space of electrolyzer, and the leakage current that dielectric medium causes does not obtain utilizing.Therefore the fundamentally unit's of solution spatiotemporal efficiency and the not good enough present situation of processing efficiency.
The utility model content
To above-mentioned prior art; The utility model provides a kind of heterogeneous multipole electrocatalysis industrial wastewater treatment system of efficient removal bio-toxicity; The utility model can overcome the shortcoming of existing poisonous indegradable industrial effluent treatment technology, particularly the weak point of existing catalytic oxidation method and apparatus.Through improving method of design such as hydraulics, augmenting response area, raising catalytic performance, introducing coupling reaction; Processes such as catalytic oxidation, chemical oxidation, flocculation, air supporting, deposition are combined; Form the multicomponent reaction process, and high as a kind of processing efficiency of technology basic design, unit consumption of energy is low, electrode life is long, the multipole electrocatalysis industrial wastewater treatment system of simple and convenient operation and maintenance.
In order to solve the problems of the technologies described above; The utility model is efficiently removed the technical scheme that the heterogeneous multipole electrocatalysis industrial wastewater treatment system of bio-toxicity is achieved: comprise reactor shell, be divided into inhalant region, electrolytic reaction district, exhalant region and settling region in the said reactor shell; Said inhalant region is formed by the water inlet nozzle with the water distribution dividing plate of the perpendicular layout of water inlet nozzle, leaves passage between the base of said water distribution dividing plate and the said reactor shell; Said electrolytic reaction district forms by being arranged on intravital anode of reactor enclosure and negative electrode, and the intravital bottom of said reactor enclosure is provided with aerating system; Said anode is a meshed anode, and said negative electrode is a cylindrical cathode, and said meshed anode has formed a plurality of mesh spaces, in each grid, is equipped with a cylindrical cathode; Said exhalant region comprises water outlet weir plate, upper water-out pipe and lower discharging tube, is provided with ball valve on said upper water-out pipe and the lower discharging tube respectively and holds back filtration unit; Said water outlet weir plate is arranged in the said reactor shell, its highly be from the mouth of pipe of said upper water-out pipe upwards and and the top of said reactor shell between leave passage; Said settling region is made up of slag chute, scraper plate, slag-drip opening valve and scum pipe.
The utility model is efficiently removed in the heterogeneous multipole electrocatalysis industrial wastewater treatment system of bio-toxicity, and said reactor shell is made by non-metallic material or made through rotproofing and the metallic substance that has an insulation layer.Said electrolytic reaction is provided with granule electrode in the district.Said granule electrode is made up of conductive particle and dielectric particle; Wherein, Said conductive particle is selected from one or more in activated carbon granule, graphite granule, conductivity ceramics grain and the resin particle, and said dielectric particle is selected from one or more in glass, resin, high molecular polymer, grit and the ceramic non-conductive material particle.Said anode surface and/or granule electrode surfaces coated are covered with the catalytic specie layer.
Compared with prior art, the beneficial effect of the utility model is:
1, the utility model has replaced traditional parallel plate electrode type electrolyzer with the novel electrolytic system of netted modular construction; Such structure can promote the unrestricted flow of current; Increase the electrode effective ratio area greatly; Improve current efficiency, cut down the consumption of energy and processing cost, also can reduce the device fabrication cost simultaneously.
2, through on upper and lower rising pipe, valve being set, make the utility model Waste Water Treatment both can be set at continuous operation mode, also can be set at the sequence batch (operating mode.Through adjusting, can change reaction time, simultaneously to adapt to different quality condition and water outlet requirement to the water inlet flow velocity.
3, behind the waste water process water distribution dividing plate; Get into the electrolytic reaction district evenly distributedly from the bottom of inhalant region, and formed the electrode design of blocking, both can avoid the current short circuit by cylindrical cathode in each grid in the meshed anode and meshed anode all around; Improve mass transfer effect; Can guarantee simultaneously the waste water anodic-cathodic of repeatedly flowing through, oxidation and reduction reaction are present in the reaction process simultaneously, thereby guarantee the thorough removal of toxicant and other pollutents.
4, the distribution design through electrode unit, and cooperate the use of its bottom aerating system, can eliminate the reaction dead angle; Improve hydraulics; Prevent the generation of concentration polarization, further improve the generation speed and the generation of indirect oxidation material, thereby improve the electrolytic catalysis processing efficiency; Meanwhile,, can remove the suspension dirt settling of electrode surface, reduce electrode fouling, prolong electrode life, reduce the electrode cleaning interval through the gas-liquid souring.
5, the utility model Waste Water Treatment extendability is strong, can realize the expansion of operating mode through technology coupled mode.For example: change the intensity and the density of aerating system, and add flocculation agent, can realize the air supporting or the flocculation sediment effect of degraded product; For another example:, realize the effect of multipole bed electrolysis through adding granule electrode; Also have:, realize the composite catalytic oxidation effect through adding water miscible catalyzer.
6, the utility model Waste Water Treatment is applied widely, not only is applicable to the detoxification pre-treatment of bio-toxicity waste water, also is applicable to the pre-treatment of the trade effluent that biochemical property is relatively poor.For example: for the trade effluent of COD＞1000mg/L, the utility model Waste Water Treatment can be used as pretreatment process, except removing portion C OD and bio-toxicity, can effectively improve biodegradability, is beneficial to get into follow-up biochemical system handles; The utility model Waste Water Treatment is particularly suited for for finally removing of difficult degradation meta-bolites after the degree of depth processing up to standard, particularly biochemical process of the low concentration waste water of COD＜500mg/L effective especially; For the light polluted-water of COD＜100mg/L, through reaching the miscellaneous water standard, the purpose of water reuse in the realization after the processing of the utility model Waste Water Treatment.
Description of drawings
Fig. 1 is the utility model industrial wastewater treatment system two dimensional structure simplified schematic diagram;
Fig. 2 is the utility model industrial wastewater treatment system vertical section structure simplified schematic diagram;
Among the figure:
1---reactor shell 2---water distribution dividing plate 3---water inlet pipe
4---inlet pipe 5---meshed anode 6---cylindrical cathodes
7---water outlet weir plate 81---upper water-out pipe 82---lower discharging tubes
91---flowing water Valve 92---following flowing water Valve 10---bracing frames
11---slag bucket 12---slag-drip opening valve 13---scum pipes
Embodiment
Below in conjunction with embodiment the utility model is done to describe in further detail.
As depicted in figs. 1 and 2; The heterogeneous multipole electrocatalysis industrial wastewater treatment system of a kind of efficient removal bio-toxicity of the utility model; Comprise reactor shell; Be divided into inhalant region, electrolytic reaction district, exhalant region and settling region in the said reactor shell, the two dot chain line among Fig. 1 and Fig. 2 shows the approximate location in above-mentioned 4 zones.Wherein: said inhalant region is formed by water inlet nozzle 3 with the water distribution dividing plate 2 of water inlet nozzle 3 perpendicular layouts, leaves passage between the base of said water distribution dividing plate 2 and the said reactor shell 1.Said electrolytic reaction district is by being arranged on intravital anode 5 of reactor enclosure and negative electrode 6, and the intravital bottom of said reactor enclosure is provided with aerating system; Said anode is a meshed anode 5, and said negative electrode is a cylindrical cathode 6, and said meshed anode 5 has formed a plurality of mesh spaces, in each grid, is equipped with a cylindrical cathode 6.Said exhalant region comprises water outlet weir plate 7, upper water-out pipe 81 and lower discharging tube 82, and said upper water-out pipe 81 is provided with ball valve respectively and holds back filtration unit with lower discharging tube 82; Said water outlet weir plate 7 is arranged in the said reactor shell 1, its highly be from the mouth of pipe of said upper water-out pipe 81 upwards and and the top of said reactor shell 1 between leave passage.Said settling region is made up of slag chute 11, scraper plate, slag-drip opening valve 12 and scum pipe 13.
Reactor shell 1 in the utility model Waste Water Treatment can be made by non-metallic material (like PVC, PMMA etc.) or metallic substance (like carbon steel, stainless steel etc.); If adopt metallic substance to make, should carry out the protection against corrosion and the insulation work in early stage.
In the utility model Waste Water Treatment; Anode design is become wire mesh electrode, and this electrode materials can be that plain carbon stool, stainless steel, DSA (titanium-based metal oxide coatings), carbon (activated carbon or crystal carbon) and other are fit to make cancellated precious metal material electrode.The percentage of open area of this mesh electrode＞70%, the about 0.5～1cm of single hole crack area size of grid
2This netted design on the one hand can be in keeping reaction process reduces the usage quantity of precious metal under the prerequisite of current density, reduces cost; Can keep good hydraulic performance on the other hand, under the effect of the aerating system that is positioned at its bottom, promote the unrestricted flow of water body, stop the appearance at electrode reaction dead angle.
In the utility model Waste Water Treatment, Cathode Design is become column, said cylindrical cathode 6 can guarantee and the contact area of meshed anode 5 plates on the one hand, effectively improves current density; Then can reduce the making and the maintenance cost of equipment on the other hand, keep the stability of equipment work simultaneously.Cylindrical cathode 6 can be graphite, carbon steel or other inactive, conductive material.Each cylindrical cathode 6 constitutes a little electrolysis cells with its meshed anode 5 all around; Waste water can unrestricted flow between each electrolysis cells, thus, both can avoid the current short circuit; Improve mass transfer effect; Can guarantee simultaneously the waste water anodic-cathodic of repeatedly flowing through, oxidation and reduction reaction are present in the reaction process simultaneously, thereby guarantee the thorough removal of tool toxicant and other pollutents.
The power supply of the utility model Waste Water Treatment can be according to the different quality condition, adapted D.C. regulated power supply, Voltage pulsating direct-current supply or high-voltage pulse power source.Voltage of supply should adopt the following safety voltage of 36V, the about 1～10A/dm of current density
2Be connected with the electrodes use parallel way, guarantee the unanimity of current field condition between each little electrolysis cells.
To different waste water; Can be chosen in and whether dose granule electrode in the electrolytic reaction district; To constitute the multipole electrolysis reactor, granule electrode is to be mixed by conductive particle and dielectric particle to constitute, thus the current efficiency of making full use of; Both blending ratios are adjusted according to the wastewater source difference to some extent, and the volume ratio of conductive particle and dielectric particle can be 1: 3 or 1: 4.Wherein, Conductive particle is selected from one or more in activated carbon granule, graphite granule, conductivity ceramics grain and the resin particle, and the dielectric particle electrode is selected from one or more in the non-conductive material particles such as glass, resin, high molecular polymer, grit and pottery.Simultaneously to some special water, also should select for use a part of load that the particle of catalytic specie coating is arranged, reach the purpose of catalyzed degradation specific pollutant.The particle diameter of above-mentioned particle is generally 3～5mm.Above-mentioned particulate surface can be coated with the catalytic specie layer.
Water outlet in the utility model Waste Water Treatment take be equipment be equipped with rising pipe up and down, and with the keying of valve pilot piping.Wherein upper water-out pipe 81 is designed by continuous operation mode, and the water outlet weir plate 7 in the design of upper water-out mouth place can guarantee that continuous effluent is even, holds back surface scum as far as possible; Lower discharging tube 82 is designed by the sequence batch (operating mode, after water inlet and accomplishing electrolytic reaction, opens valve 92 water outlets on the lower discharging tube 82, then, closes the processing that this valve carries out next batch waste water.Sediment blocking pipe in the water is established at the water outlet place of lower discharging tube 82 and to be held back grid or line strainer.
The aerating system of the utility model Waste Water Treatment is arranged on bottom, electrolytic reaction district, is provided with to be used for driving the waste water up-flow to promote the perforation gas distribution pipe or the aeration head of electrolytic reaction district internal recycle fluidised form.The perforation gas distribution pipe is vertical with the gas distribution main with many groups by the gas distribution main of a level, and the level that is parallel to each other perforation arm constitutes.Whole aerating system is fixed on the bottom of equipment with bracing frame 10, and this bracing frame 10 also plays the effect of support electrode.
Be provided with dregs scraper (scraper plate) in the settling region, all collect the sediment that is deposited in reactor bottom in the slag bucket 11, drain via the slag notch of scum pipe 13 ends again through the tangential movement of scraper plate.Native system is taked regularly to scrape slag (opening and closing the slag-drip opening valve) and is walked clearly, brings unnecessary energy consumption waste to prevent sediment secondary dissolving in water.
Usually, the residence time of waste water in equipment body is 0.5～3h, and this depends primarily on influent quality and processing requirements.Can also add water miscible catalyzer to some special waters, selecting for use of this catalyzer comprises H
2O
2, metallic salt (iron, magnesium, aluminium etc.) or the water-soluble ion (like halogenide, nitro salt etc.) of indirect oxidation function is arranged.
Through following examples the utility model is done further to specify, but do not meant that any restriction the utility model.
Application example 1:
After certain chemical development district first phase is built, the about 1200t/d of comprehensive discharge trade effluent, based process technology is " acidication+catalytic oxidation+MBR+ active carbon filtration "; Second phase builds and finishes; The comprehensive discharge trade effluent is increased to 2000t/d; Original technology can not reach the water outlet requirement, and especially the second phase is gone into garden enterprise has man insecticide factory of number and Western medicine midbody factory, and the wastewater biological toxicity that gives off is higher; Biodegradability is poor, has had a strong impact on the operation stability of biochemical process.
Composite wastewater factory water inlet monitoring index is as shown in table 1:
Certain chemical industrial park composite wastewater factory operation of table 1 detects data (mg/L)
| Project | COD Cr | BOD 5 | NH 4 +-N | TP | SS | Luminescent bacteria presses down light rate (%) relatively |
| First phase water inlet MV | 496 | 244 | 62 | 9 | 176 | 22 |
| Second phase water inlet MV | 742 | 268 | 64 | 16 | 226 | 46 |
Pre-treatment is carried out in water inlet after adopting heterogeneous multipole electrocatalysis technology for treating industrial waste water to simple filtration, and current density is controlled at 5.0mA/cm
2, the residence time is 1 hour, the periodic running pattern.After pre-treatment, COD is cut to below the 500mg/L, and B/C rises to more than 0.5, and simultaneously, luminescent bacteria presses down the light rate relatively and is reduced to below 11%, the biodegradability that is significantly improved and the effect that reduces bio-toxicity.Final outflow water COD content is 30～40mg/L, is lower than the requirement of one-level B in " urban wastewater treatment firm pollutant emission standard (GB 18918-2002) ", the about 4～5KWH/ ton of power consumption water.
Application example 2:
Certain semisynthetic antibiotics pharmaceutical factory waste water is mainly produced the beta-lactam series product, comprises semisynthetic penicillin and semi-synthetic cynnematin etc.Former water is faint yellow, the about 6400mg/L of COD, and pH4.06, luminescent bacteria presses down the light rate relatively up to 94%.Former water need not regulated and promptly directly get into the heterogeneous multipole electrocatalysis of the utility model industrial wastewater treatment system, adopts intermittent operation mode, and the residence time is 90 minutes, and current density is controlled at 10.0mA/cm
2
Behind the electrocatalysis pretreatment technology, water outlet is by the faint yellow water white transparency that becomes, and COD concentration is reduced to 1700mg/L, and clearance reaches 73.4%; Luminescent bacteria presses down the light rate relatively and reduces to 23%, and clearance reaches 75.5%.Water outlet can directly get into biochemical system, carries out further conventional processing up to standard.
Application implementation example 3:
Certain comprehensive garden sewage work, the comprehensive draining of taking in peripheral enterprise and Residential areas carries out processing up to standard.Water inlet COD concentration is 600～1000mg/L, and pH 6.5～7.5, and based process technology is " air supporting+A
2Little flocculation sediment+the sand filtration of O+ ", the about 90mg/L of water outlet COD can reach secondary requirement in " urban wastewater treatment firm pollutant emission standard (GB 18918-2002) ".
But if require this sewage effluents to reach the regulation of one-level B in " urban wastewater treatment firm pollutant emission standard (GB 18918-2002) ", i.e. water outlet COD＜60mg/L is difficult to reach requirement with the technology of prior art, need improve original technical process.Be about to the bioprocess technology water outlet and enter into the heterogeneous multipole electrocatalysis of the utility model industrial wastewater treatment system, the successive reaction pattern, about 30min of the residence time, current density is controlled at 10.0mA/cm
2The about 100mg/L of water inlet COD, water outlet COD reduces to 40～50mg/L, behind little flocculation and filtration process, can reach the water outlet requirement fully again.
Although top combination figure is described the utility model; But the utility model is not limited to above-mentioned embodiment, and above-mentioned embodiment only is schematically, rather than restrictive; Those of ordinary skill in the art is under the enlightenment of the utility model; Under the situation that does not break away from the utility model aim, can also make a lot of distortion, these all belong within the protection of the utility model.
Claims (5)
1. an efficient heterogeneous multipole electrocatalysis industrial wastewater treatment system of removing bio-toxicity comprises reactor shell, is divided into inhalant region, electrolytic reaction district, exhalant region and settling region in the said reactor shell;
Said inhalant region is formed by water inlet nozzle (3) with the water distribution dividing plate (2) of the perpendicular layout of water inlet nozzle (3), leaves passage between the base of said water distribution dividing plate (2) and the said reactor shell (1);
Said electrolytic reaction district is by being arranged on the intravital anode of reactor enclosure (5) and negative electrode (6) is formed, and the intravital bottom of said reactor enclosure is provided with aerating system; Said anode is meshed anode (5), and said negative electrode is cylindrical cathode (6), and said meshed anode (5) has formed a plurality of mesh spaces, in each grid, is equipped with a cylindrical cathode (6);
Said exhalant region comprises water outlet weir plate (7), upper water-out pipe (81) and lower discharging tube (82), is provided with ball valve on said upper water-out pipe (81) and the lower discharging tube (82) respectively and holds back filtration unit; Said water outlet weir plate (7) is arranged in the said reactor shell (1), its highly be from the mouth of pipe of said upper water-out pipe (81) upwards and and the top of said reactor shell (1) between leave passage;
Said settling region is made up of slag chute (11), scraper plate, slag-drip opening valve (12) and scum pipe (13).
2. the heterogeneous multipole electrocatalysis industrial wastewater treatment system of efficient removal bio-toxicity according to claim 1 is characterized in that: said reactor shell (1) is made by non-metallic material or is made through rotproofing and the metallic substance that has an insulation layer.
3. the heterogeneous multipole electrocatalysis industrial wastewater treatment system of efficient removal bio-toxicity according to claim 1, it is characterized in that: said anode surface is coated with the catalytic specie layer.
4. the heterogeneous multipole electrocatalysis industrial wastewater treatment system of efficient removal bio-toxicity according to claim 1, it is characterized in that: said electrolytic reaction is provided with granule electrode in the district.
5. the heterogeneous multipole electrocatalysis industrial wastewater treatment system of efficient removal bio-toxicity according to claim 4, it is characterized in that: the surfaces coated of said granule electrode is covered with the catalytic specie layer.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102381744A (en) * | 2011-09-28 | 2012-03-21 | 天津市环境保护科学研究院 | Polyphase multipole electrocatalytic industrial wastewater processing system for high efficiency biological toxicity removal |
| CN104445530A (en) * | 2014-12-11 | 2015-03-25 | 广东电网有限责任公司电力科学研究院 | Electrochemical treatment device of desulphurization waste water |
| CN105170253A (en) * | 2014-06-05 | 2015-12-23 | 住友重机械环境工程株式会社 | Biaxial differential crushing system |
| CN107188276A (en) * | 2017-06-22 | 2017-09-22 | 广东益诺欧环保股份有限公司 | A kind of composite electrochemical catalytic oxidizing equipment |
| CN111112324A (en) * | 2019-12-20 | 2020-05-08 | 清华大学 | Organic pollutant treatment device and equipment in soil and underground water |
-
2011
- 2011-09-28 CN CN 201120372932 patent/CN202265445U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102381744A (en) * | 2011-09-28 | 2012-03-21 | 天津市环境保护科学研究院 | Polyphase multipole electrocatalytic industrial wastewater processing system for high efficiency biological toxicity removal |
| CN102381744B (en) * | 2011-09-28 | 2013-11-27 | 天津市环境保护科学研究院 | Polyphase multipole electrocatalytic industrial wastewater processing system for high efficiency biological toxicity removal |
| CN105170253A (en) * | 2014-06-05 | 2015-12-23 | 住友重机械环境工程株式会社 | Biaxial differential crushing system |
| CN104445530A (en) * | 2014-12-11 | 2015-03-25 | 广东电网有限责任公司电力科学研究院 | Electrochemical treatment device of desulphurization waste water |
| CN107188276A (en) * | 2017-06-22 | 2017-09-22 | 广东益诺欧环保股份有限公司 | A kind of composite electrochemical catalytic oxidizing equipment |
| CN111112324A (en) * | 2019-12-20 | 2020-05-08 | 清华大学 | Organic pollutant treatment device and equipment in soil and underground water |
| CN111112324B (en) * | 2019-12-20 | 2021-09-03 | 清华大学 | Organic pollutant treatment device and equipment in soil and underground water |
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