CN203440190U - Multivariant microelectrolysis combined binary catalytic oxidation device - Google Patents
Multivariant microelectrolysis combined binary catalytic oxidation device Download PDFInfo
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- CN203440190U CN203440190U CN201320481997.8U CN201320481997U CN203440190U CN 203440190 U CN203440190 U CN 203440190U CN 201320481997 U CN201320481997 U CN 201320481997U CN 203440190 U CN203440190 U CN 203440190U
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Abstract
The utility model belongs to the technical field of high-concentration refractory wastewater treatment of environmental engineering, and particularly relates to a multivariant microelectrolysis combined binary catalytic oxidation device. The device comprises an adjusting tank, a main device, and a water inlet pipe connecting the adjusting tank with the main device, wherein one end of the water inlet pipe extends to the bottom of the adjusting tank, and the other end is connected with a perforated water distribution pipe arranged in the main device; an acid-alkali feeding device, a lifting pump, a pipe mixer and a pH controller are sequentially arranged on the water inlet pipe in a direction from the adjusting tank to the main device; the perforated water distribution pipe is horizontally arranged at the bottom of the main device; a valve is arranged at the joint of the perforated water distribution pipe and the water inlet pipe. The enhanced electrochemical coupling catalytic oxidation process and device provided by the invention can complete advanced oxidation pretreatment of refractory organic wastewater, and have the advantages of high intensive degree, high adaptability, stability, simpliness and convenience in operation and so on.
Description
Technical field
The utility model belongs to environmental engineering high-concentration hardly-degradable waste water processing technology field, is specifically related to the compound binary catalyst oxidation unit of a kind of polynary micro-electrolysis.
Background technology
The processing of high concentration hard-degraded organic waste water is the at present domestic and international generally acknowledged difficult problem of sewage disposal circle.For this class waste water, at present both at home and abroad research is more the professional waste water such as coking chemical waste water, pharmacy waste water (comprising traditional Chinese medicine wastewater), petrochemical industry/oils waste water, weaving/dyeing waste water, wastewater from chemical industry, paint waste water.So-called " high density ", refers to that the organic concentration (in COD) of this class waste water is higher, general all more than 2000mg/L, have even up to every liter several ten thousand to tens0000 milligrams; So-called " difficult degradation " refers to that the biodegradability of this class waste water is lower, BOD
5/ COD(is hereinafter to be referred as B/C) value is below 0.3, and general B/C value, 0.1 and following, is difficult to biological degradation.So, in industry, generally COD concentration is greater than to 2000mg/L, B/C value is called high concentration hard-degraded organic waste water lower than 0.2 organic waste water unification.
The stack of " high density ", " difficult degradation " two large characteristics, makes this type of waste water in processing, uses separately " routine " methods such as biological process or physico-chemical process to lose possibility.Thereby, the combination of other methods such as research biochemical process and physico-chemical process, try hard to make treatment process, method at home chemical industry there is the promotional value of effective practicality, be the critical problem of current this type of contaminated wastewater of solution.
This class difficult problem of processing in order to solve high-concentration hardly-degradable waste water, colleague has carried out many useful explorations both at home and abroad for many years.In the last few years, domesticly in the processing of the pharmacy waste waters such as antibiotic waste water, have breakthrough; But the processing of the used water difficult to degradate such as coking chemical waste water is still in the middle of research.Sum up achievement in research in recent years, especially the research to used water difficult to degradate such as coking chemical waste waters, up to the present, what (mainly refer to western developed country) abroad and relatively accept is to adopt longer technique, and has suitably merged such as entering the newer thinkings such as (going out) water end (W.E.) dilution, biological process and chemical method combine; At home, in a sense, because construction costs and processing cost are of paramount importance Considerations, so longer technique and higher cost are at least at present or cannot accept and be difficult to put into practice.So to meet the technique of existing state sewage emission standard be the task of top priority in water outlet after seeking that technique is simple, intensive degree is high, cost is lower and making whole system combined treatment.
At present, the treatment process comparatively generally adopting is essentially biological process, but simple biological treatment workshop section is very difficult, this class wastewater treatment is arrived to desirable degree, generally all needs the effective pre-treatment of configuration or advanced treatment as water outlet assurance up to standard comprehensively.
Utility model content
The utility model aims to provide the compound binary catalyst oxidation unit of a kind of polynary micro-electrolysis that a kind of micro-electrolysis, Fenton-like catalyzed oxidation combine with UV-H2O2 advanced oxidation, solve high-concentration hardly-degradable waste water adopt the conventional pretreating effects such as coagulating sedimentation, air supporting poor, can not improve the problems such as biodegradability, water outlet CODcr exceed standard, to realize, reduce toxicity, improve biodegradability and the synchronous object of effectively removing the organism in waste water.
The utility model solves the technical scheme that its technical problem adopts:
The compound binary catalyst oxidation unit of micro-electrolysis, comprises equalizing tank, main device, connects the inlet channel of equalizing tank and main device, and inlet channel one end is stretched into bottom equalizing tank, and the other end perforate water distributor inner with being arranged on main device is connected; On inlet channel, inherent regulation pond to main device direction sets gradually soda acid throwing device, lift pump, line mixer and pH controller; Perforate water distributor is horizontally placed on the bottom of main device, and the junction of perforate water distributor and inlet channel is provided with valve; The outside of main device is provided with external circulation line system; Main device be top with the tube structure of end socket, main device inside is divided into upper and lower two reaction zones, lower floor is strengthening electrochemical reaction district, upper strata is catalytic oxidation district, and the exhalant region that is positioned at catalytic oxidation district top.Soda acid throwing device is set before described lift pump, line mixer and pH controller are set on the inlet channel after lift pump, for realizing acid to adding or effective mixing of alkali, save and adjust civil engineering or facility investment due to pond because of additional pH.The secondary mix and blend of pipelining line mixer after the pre-stirring of impeller one-level of pH value adjustment employing lift pump and pump, the acid adding is effectively mixed, save the facility investment in additional acid adjustment reaction tower or pond, improve the water pump waterpower intensified water-layout effect before the micro-electrolysis in oxidation unit of the present utility model bottom.
As preferably, described inside, two reaction zones is respectively provided with one deck micro-electrolysis stuffing layer, and every layer of micro-electrolysis stuffing layer bottom supported by supporting plate; It is the cylindrical shell of upper and lower opening that the micro-electrolysis stuffing layer top that is positioned at bottom is provided with lower floor's filler Zhu， lower floor filler post that feeds intake that feeds intake, and the feed intake top of post of lower floor's filler is positioned at the top of end socket, for loading the micro-electrolysis stuffing in strengthening electrochemical reaction district; The micro-electrolysis stuffing layer top that is positioned at upper strata is provided with the upper strata filler post that feeds intake, and the filler post that feeds intake in upper strata is also the cylindrical shell of upper and lower opening, and filler the feed intake top of post in upper strata is positioned at the top of end socket, for loading the micro-electrolysis stuffing in catalytic oxidation district.As preferably, the filler post that feeds intake in upper strata distributes ringwise centered by the axis of main device, and the filler post that feeds intake in upper strata has three, and the angle between each is 120 °.
As preferably, the below of main device top, end socket sets out mill weir, the rising pipe top being connected, waste gas and overfoaming collection device interface is installed on end socket with effluent weir, and waste gas and overfoaming collection device interface are connected with waste gas and overfoaming collection device.
As preferably, described external circulation line system comprises: outer circulating tube, hydrogen peroxide throwing device, UV-light (being called for short UV) producer and recycle pump, ultraviolet light generator and recycle pump are connected on outer circulating tube, hydrogen peroxide throwing device is connected to outer circulating tube by pipeline, and the two ends of outer circulating tube respectively strengthening electrochemical reaction district and the catalytic oxidation district inner with main device are communicated with.Ultraviolet light generator is installed on outer circulating tube, by hydrogen peroxide-UV, is formed photochemical catalytic oxidation unit, induction forms its free radical of more hydroxyl, realizes waste water is carried out to deeply processing.
As preferably, the micro-electrolysis stuffing layer top that is positioned at bottom is located in one end of outer circulating tube, and the other end is provided with the micro-electrolysis stuffing layer top that is positioned at top layer, and hydrogen peroxide throwing device, ultraviolet light generator and recycle pump set gradually from top to bottom on outer circulating tube.
As preferably, to strengthen electrochemical reaction district, with the micro-electrolysis stuffing floor below in catalytic oxidation district, the aeration tube being connected with main device extraneous air is set respectively, in the middle of aeration tube adopts, the annular gas distribution structure of air inlet, installs air flowmeter on aeration tube; Aeration tube below strengthening electrochemical reaction district is located between supporting plate and perforate water distributor.The strengthening electrochemical reaction district of bottom and the catalytic oxidation district on top arrange subregion aeration tube and air flowmeter are installed, and subregion is controlled the aeration intensity of each reaction zone.
As preferably, main device cylinder lateral wall is provided with two access openings that distribute up and down, and main device cylinder body bottom is provided with evacuated tube emptying when overhauling.
In the utility model, main device is by the H of bottom strengthening electrochemical reaction district, catalytic oxidation district, middle and upper part and external circulation line system
2o
2-UV photochemical catalytic oxidation forms, and forms trinity oxidizing process, and science has built organic wastewater with difficult degradation thereby coupling, synergistic oxidation technical system.
The beneficial effects of the utility model are: strengthening electrochemistry coupling and catalyzing oxidizing process described in the utility model and device, complete the pre-treatment of organic wastewater with difficult degradation thereby being carried out to advanced oxidation, have that intensive degree is high, a strong adaptability, the feature such as stable, easy and simple to handle.Adopt integrated structure design, have that intensive degree is high, orthofunction, strong adaptability, a feature such as stable, easy and simple to handle.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure: the water shoot of 1-workshop, 2-equalizing tank, 3-soda acid throwing device, 4-lift pump, 5-line mixer, 6-pH controller, 7-perforate water distributor, 8-aeration tube, 9-supporting plate, 10-air flowmeter, 11-micro-electrolysis stuffing layer, 12-effluent weir, 13-end socket, the 14-upper strata filler post that feeds intake, the 15-lower floor filler post that feeds intake, 16-waste gas and overfoaming collection device interface, the main device of 17-, 18-rising pipe, 19-outer circulating tube, 20-hydrogen peroxide throwing device, 21-access opening, 22-ultraviolet light generator, 23-evacuated tube, 24-recycle pump, 25-inlet channel, 26-waste gas and overfoaming collection device, 27-strengthens electrochemical reaction district, 28-catalytic oxidation district, 29-exhalant region.
Embodiment
Below by specific embodiment, and by reference to the accompanying drawings, the technical solution of the utility model is described in further detail.Should be appreciated that enforcement of the present utility model is not limited to the following examples, any pro forma accommodation that the utility model is made and/or change all will be listed the utility model protection domain in.
Embodiment:
The compound binary catalyst oxidation unit of polynary micro-electrolysis as shown in Figure 1, the inlet channel 25 that comprises equalizing tank 2, main device 17, connection equalizing tank and main device, equalizing tank bottom is stretched in inlet channel one end, and the other end perforate water distributor 7 inner with being arranged on main device is connected.On inlet channel, inherent regulation pond to main device 17 directions set gradually soda acid throwing device 3, lift pump 4, line mixer 5, pH controller 6.Perforate water distributor 7 is horizontally placed on the bottom of main device 17, and perforate water distributor 7 is provided with valve with the junction of inlet channel 25.Perforate water distributor adopts the non-character form structure of multilayer.
Main device 17 is for realizing the main device of strengthening electrochemistry coupling and catalyzing oxidation, for the tube structure of top with end socket 13, the airtight connection of cylindrical shell of top end socket and main device, main device 17 cylinder lateral walls are provided with two access openings 21 that distribute up and down, and main device 17 cylinder body bottoms are provided with evacuated tube 23 emptying when overhauling.The below of main device top, end socket sets out mill weir 12, rising pipe 18 tops that are connected with effluent weir, waste gas and overfoaming collection device interface 16 are installed in the side of end socket 13, waste gas and overfoaming collection device interface 16 are connected with waste gas and overfoaming collection device 26.Waste gas and overfoaming collection device can merge the row's of concentrating foam with the evacuated tube 23 of main bottom of device, emptying during maintenance.
Main device 17 inside are divided into upper and lower two reaction zones, and lower floor is catalytic oxidation district 28 for strengthening 27， upper strata, electrochemical reaction district, and the exhalant region 29 that is positioned at top, catalytic oxidation district; Inside, two reaction zones is respectively provided with one deck micro-electrolysis stuffing layer 11, every layer of micro-electrolysis stuffing layer bottom by with water, the supporting plate 9 of crossing gas support.It is the cylindrical shell of upper and lower opening that the micro-electrolysis stuffing layer top that is positioned at bottom is provided with lower floor's filler Zhu15， lower floor filler post that feeds intake that feeds intake, and the feed intake top of post of lower floor's filler is positioned at the top of end socket 13, for loading the micro-electrolysis stuffing in strengthening electrochemical reaction district.The micro-electrolysis stuffing layer top that is positioned at upper strata is provided with the upper strata filler post 14 that feeds intake, and the filler post that feeds intake in upper strata is also the cylindrical shell of upper and lower opening, and filler the feed intake top of post in upper strata is positioned at the top of end socket 13, for loading the micro-electrolysis stuffing in catalytic oxidation district.The filler post 14 that feeds intake in upper strata distributes ringwise centered by the axis of main device 17, and the filler post 14 that feeds intake in upper strata has three, and the angle between each is 120 °.Lower floor's filler post and upper strata filler filler that post consumes for postreaction process that feeds intake that feeds intake.
Strengthening electrochemical reaction district arranges respectively with the micro-electrolysis stuffing floor below in catalytic oxidation district the aeration tube 8 being connected with main device 17 extraneous airs, on aeration tube 8, air flowmeter is installed, in order to control respectively the aeration intensity of each reaction zone.In the middle of aeration tube adopts, the annular gas distribution structure of air inlet, prevents from forming vapour lock short circuit.Aeration tube below strengthening electrochemical reaction district 27 is located between supporting plate 9 and perforate water distributor 7.
The outside of main device 17 is provided with external circulation line system, external circulation line system comprises: outer circulating tube 19, hydrogen peroxide throwing device 20, ultraviolet light generator 22 and recycle pump 24, ultraviolet light generator 22 and recycle pump 24 are connected on outer circulating tube 19, and hydrogen peroxide throwing device 20 is connected to outer circulating tube 19 by pipeline.The two ends of outer circulating tube 19 are communicated with strengthening electrochemical reaction district and the catalytic oxidation district of main device 17 inside respectively.In the present embodiment, the micro-electrolysis stuffing layer top that is positioned at bottom is located in one end of outer circulating tube 19, and the other end is provided with the micro-electrolysis stuffing layer top that is positioned at top layer.Hydrogen peroxide throwing device 20, ultraviolet light generator 22 and recycle pump 24 set gradually from top to bottom on outer circulating tube 19.
Waste water evenly enters by being arranged on the perforate water distributor 7 of main device 17 bottoms, then there is micro-electrolysis reaction with the micro-electrolysis stuffing layer 11 of lower floor, micro-electrolysis stuffing layer 11 through upper strata occurs after micro-electrolysis coupling and catalyzing oxidation again, by middle part, exhalant region, enter outer circulating tube, through hydrogen peroxide throwing device 20, add hydrogen peroxide, then by ultraviolet light generator 22, H occurs
2o
2-UV photocatalysis oxidation reaction; External reflux, to main device 17, is carried out Fenton-like catalytic oxidation with the micro-electrolysis stuffing layer 11 on upper strata again, and water outlet, after effluent weir 12 is collected, drains in follow-up routine and carries out mud-water separation with coagulating sedimentation system to rising pipe 18.The lower floor filler of the filler of lower floor by the setting of the main device crown center post 15 that feeds intake adds, and the filler on upper strata adds by the upper strata filler post 14 that feeds intake.
Pending waste water enters equalizing tank 2 from workshop water shoot 1, on inlet channel, by after line mixer acidity adjustment, by lift pump, pumps into main device 17, from bottom to top successively through the micro-electrolysis of strengthening, catalyzed oxidation, H
2o
2water outlet after the coupling of the advanced oxidations such as-UV photochemical catalytic oxidation, concerted reaction, through in follow-up routine and after coagulating sedimentation, realizes toxicity reduction, improves biochemical, synchronous degradable organic pollutant, and good flow condition is created in follow-up biochemical treatment.Acidity adjustment is by adding acid/alkali in the inlet channel 25 of line mixer 5 and regulate main device water inlet pH value, the required acidity condition of strengthening micro-electrolysis reaction toward being provided with.The secondary mix and blend of pipelining line mixer after the pre-stirring of impeller one-level of pH value adjustment employing lift pump and pump, the acid adding is effectively mixed, save the facility investment in additional acid adjustment reaction tower or pond, improve the water pump waterpower intensified water-layout effect before the micro-electrolysis in oxidation unit bottom.
Described micro-electrolysis reaction is that waste water carries out micro-electrolysis reaction in packing layer lower floor, and pH value is controlled at 2.0～4.0 waste water and carries out micro-electrolysis reaction in the micro-electrolysis stuffing layer of lower floor, constantly produces the Fe of nascent state
2+[H], makes ring-type organic pollutant or complex compound scission of link in waste water generate long-chain or low molecule intermediate product, and part is mineralized into carbonic acid gas and water simultaneously, for subsequent disposal is had laid a good foundation; The pH value of water outlet after micro-electrolysis reaction is generally 4.0～6.0.Described external circulation line system makes waste water at outside external reflux, the H in external reflux of producing of main device
2o
2the laggard catalytic oxidation district that becomes owner of device middle and upper part of-UV photochemical catalytic oxidation advanced oxidation.Described Fenton-like catalytic oxidation utilizes the H in external reflux
2o
2the nascent state Fe that coupling bottom micro-electrolysis reaction produces
2+as catalyzer, the common Fenton reagent that forms, make the intensity of redox reaction reach maximization within a short period of time, by high-intensity catalytic oxidation, generate the extremely strong hydroxyl radical free radical of oxidisability, make organism in water be further degraded to rapidly, fully low molecular compound or easy organic molecule of degrading, the hydrogen peroxide adding and the volume percent of waste water are generally 2 ‰～4 ‰, and the hydrogen peroxide effective concentration adding is in 30% left and right.Fenton oxidizing reaction is 3.0～4.0 to the requirement of water inlet pH value, and micro-electrolysis reaction water outlet pH value is 4.0～6.0, and after hydrogen peroxide hybrid reaction, pH value remains on 3.0～4.0 substantially, just in time meets the requirement of Fenton catalytic oxidation.
Table 1 is for adopting the detection water quality after device described in the utility model is processed continuously to certain difficult degradation organic chemical waste water.In this wastewater oxidation Processing Test: water inlet pH value 9.0 left and right, strengthening electrochemistry and catalyzed oxidation time are 120min; The volume percent of hydrogen peroxide dosage and waste water is 4 ‰.
Table 1 high-concentration hardly-degradable waste water preprocessed data table look-up
Note: in table, data every group of data except pH are sampling determination mean value 5 times.
The feature that high concentrated organic wastewater Pollutant levels are high, toxicity is large, biodegradability is poor, making traditional biological process of take is that the treatment technology of leading is difficult to gather effect.Especially in waste water, effective processing of multiple solvability difficult degradation organic poison is a gordian technique difficult problem for puzzlement enterprise qualified discharge always.More existing traditional chemicals, physico-chemical pretreatment technology are in aspect existing problems such as validity, economy, practicality and ripening degree.The utility model is compared tool with conventional pretreatment method for wastewater and is had the following advantages:
1, the trinity oxidizing process that proposes first to adopt strengthening electrochemistry (micro-electrolysis), Fenton catalyzed oxidation and H2O2-UV photochemical catalytic oxidation combination, science has built organic wastewater with difficult degradation thereby coupling, synergistic oxidation technical system.
2, adopt integrated apparatus design, have that intensive degree is high, orthofunction, energy consumption are low, strong adaptability, the feature such as stable, easy and simple to handle.
3, system effluent quality compared with conventional treatment method can be improved significantly: to Organic Pollutants in Wastewater, CODcr clearance reaches 40-60%; B/C rises to 0.3-0.4 than by 0.10 original left and right, and the biodegradability of waste water is significantly improved, and finally makes waste water reach the requirement of nontoxic, low toxicity, readily biodegradable, guarantee that whole system realizes qualified discharge, and treatment effect is stable.
Above-described embodiment is a kind of preferably scheme of the present utility model, not the utility model is done to any pro forma restriction, also has other variant and remodeling under the prerequisite that does not exceed the technical scheme that claim records.
Claims (8)
1. the compound binary catalyst oxidation unit of polynary micro-electrolysis, it is characterized in that: the inlet channel that comprises equalizing tank, main device, connection equalizing tank and main device, equalizing tank bottom is stretched in inlet channel one end, and the other end perforate water distributor inner with being arranged on main device is connected; On inlet channel, inherent regulation pond to main device direction sets gradually soda acid throwing device, lift pump, line mixer and pH controller; Perforate water distributor is horizontally placed on the bottom of main device, and the junction of perforate water distributor and inlet channel is provided with valve; The outside of main device is provided with external circulation line system; Main device be top with the tube structure of end socket, main device inside is divided into upper and lower two reaction zones, lower floor is strengthening electrochemical reaction district, upper strata is catalytic oxidation district, and the exhalant region that is positioned at catalytic oxidation district top.
2. the compound binary catalyst oxidation unit of polynary micro-electrolysis according to claim 1, is characterized in that: described inside, two reaction zones is respectively provided with one deck micro-electrolysis stuffing layer, and every layer of micro-electrolysis stuffing layer bottom supported by supporting plate; It is the cylindrical shell of upper and lower opening that the micro-electrolysis stuffing layer top that is positioned at bottom is provided with lower floor's filler Zhu， lower floor filler post that feeds intake that feeds intake, and the feed intake top of post of lower floor's filler is positioned at the top of end socket; The micro-electrolysis stuffing layer top that is positioned at upper strata is provided with the upper strata filler post that feeds intake, and the filler post that feeds intake in upper strata is also the cylindrical shell of upper and lower opening, and filler the feed intake top of post in upper strata is positioned at the top of end socket.
3. the compound binary catalyst oxidation unit of polynary micro-electrolysis according to claim 2, is characterized in that: the filler post that feeds intake in upper strata distributes ringwise centered by the axis of main device, and the filler post that feeds intake in upper strata has three, and the angle between each is 120 °.
4. according to the compound binary catalyst oxidation unit of polynary micro-electrolysis described in claim 1 or 2 or 3, it is characterized in that: the below of main device top, end socket sets out mill weir, the rising pipe top being connected with effluent weir, waste gas and overfoaming collection device interface are installed on end socket, waste gas and overfoaming collection device interface are connected with waste gas and overfoaming collection device.
5. the compound binary catalyst oxidation unit of polynary micro-electrolysis according to claim 1, it is characterized in that: described external circulation line system comprises: outer circulating tube, hydrogen peroxide throwing device, ultraviolet light generator and recycle pump, ultraviolet light generator and recycle pump are connected on outer circulating tube, hydrogen peroxide throwing device is connected to outer circulating tube by pipeline, and the two ends of outer circulating tube respectively strengthening electrochemical reaction district and the catalytic oxidation district inner with main device are communicated with.
6. the compound binary catalyst oxidation unit of polynary micro-electrolysis according to claim 5, it is characterized in that: the micro-electrolysis stuffing layer top that is positioned at bottom is located in one end of outer circulating tube, the other end is provided with the micro-electrolysis stuffing layer top that is positioned at top layer, and hydrogen peroxide throwing device, ultraviolet light generator and recycle pump set gradually from top to bottom on outer circulating tube.
7. according to the compound binary catalyst oxidation unit of polynary micro-electrolysis described in claim 1 or 2 or 3, it is characterized in that: strengthening electrochemical reaction district arranges respectively with the micro-electrolysis stuffing floor below in catalytic oxidation district the aeration tube being connected with main device extraneous air, in the middle of aeration tube adopts, the annular gas distribution structure of air inlet, installs air flowmeter on aeration tube; Aeration tube below strengthening electrochemical reaction district is located between supporting plate and perforate water distributor.
8. according to the compound binary catalyst oxidation unit of polynary micro-electrolysis described in claim 1 or 2 or 3, it is characterized in that: main device cylinder lateral wall is provided with two access openings that distribute up and down, main device cylinder body bottom is provided with evacuated tube emptying when overhauling.
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| CN201320481997.8U CN203440190U (en) | 2013-08-07 | 2013-08-07 | Multivariant microelectrolysis combined binary catalytic oxidation device |
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| CN201320481997.8U CN203440190U (en) | 2013-08-07 | 2013-08-07 | Multivariant microelectrolysis combined binary catalytic oxidation device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354295A (en) * | 2018-10-22 | 2019-02-19 | 陈先锐 | Utilize the method for antibiotic in light electrolysis-ozone cooperative degrading cultivation field waste water |
| CN109607702A (en) * | 2019-01-23 | 2019-04-12 | 成都市和谐环保工程技术有限公司 | A kind of device and technique improving Biodegradability of Wastewater |
-
2013
- 2013-08-07 CN CN201320481997.8U patent/CN203440190U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354295A (en) * | 2018-10-22 | 2019-02-19 | 陈先锐 | Utilize the method for antibiotic in light electrolysis-ozone cooperative degrading cultivation field waste water |
| CN109607702A (en) * | 2019-01-23 | 2019-04-12 | 成都市和谐环保工程技术有限公司 | A kind of device and technique improving Biodegradability of Wastewater |
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