CN201882958U - High-efficient electrocoagulation reactor capable of adjusting pitches among electrodes - Google Patents
High-efficient electrocoagulation reactor capable of adjusting pitches among electrodes Download PDFInfo
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- CN201882958U CN201882958U CN2010206195655U CN201020619565U CN201882958U CN 201882958 U CN201882958 U CN 201882958U CN 2010206195655 U CN2010206195655 U CN 2010206195655U CN 201020619565 U CN201020619565 U CN 201020619565U CN 201882958 U CN201882958 U CN 201882958U
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- reaction tank
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Abstract
The utility model discloses a high-efficient electrocoagulation reactor capable of adjusting pitches among electrodes, which comprises a reaction tank, cathode and anode electrodes, a stirring device and a power source. A water outlet is arranged on the upper portion of the reaction tank, a water inlet and a dirt discharge opening are disposed on the lower portion of the reaction tank, a partition board for fixing the electrodes is disposed above the reaction tank and provided with slotted holes arranged at equal intervals, the intervals among the slotted holes are 10mm, and pitches among the cathode and the anode electrodes can be adjusted by means of changing positions of the cathode and anode electrodes inserting into the slotted holes. The high-efficient electrocoagulation reactor can improve effects of treatment to sewages in different characteristics by means of changing the positions of the electrodes inserted into the slotted holes on the premise without raising voltage or increasing the amount of the reaction tank. In addition, the high-efficient electrocoagulation reactor overcomes shortages of high energy consumption, complex operation and the like of an existing electrocoagulation reactor, during treatment, multiple pollutants such as COD (chloride), SS (suspensions) and the like in sewage are cleared at one step under combined actions of various electrochemical reaction such as electrocoagulation, active oxidation, active reduction and the like, and clearing rage is higher than 90%.
Description
Technical field
The utility model relates to the sewage treatment equipment field, relates in particular to a kind of efficient electric flocculation reactor of adjustable electrode spacing.
Background technology
Electricity flocculation is exactly under External Electrical Field, and a large amount of positively charged ions of soluble anode (sacrificial anode) generation are flocculated to waste water, thereby with the water purification technology of pollutant removal, it has electrochemical oxidation, flocculation and air supporting three's characteristics concurrently.
Electric flocculation technique is because simple and compact device, and removable pollutent is extensive, need not to add advantage such as a large amount of chemical agents 10 years in the past, and this technology has been used for the processing of various trade effluents by American-European countries.D.Ryan etc. are at " separating and purification techniques " (Ryan, D.Separation andPurification Technology, 2007,58 (3): introduced 347-352) and answered the electricity consumption flocculence to handle sugar-refining industry waste water, its chroma removal rate is greater than 90%, and the COD clearance is greater than 60%; (Moral, G.Separation and Purification Technology, 2007,54 (1): 124-129) adopt electricity flocculation/H such as G.Ron-Morales
2O
2The coupling method has been carried out experimental study to grocery trade waste water, the result show this method to the clearance of colourity near 60%, to turbidity, COD and BOD
5Clearance all above 90%; Z.Zaroual etc. are in " hazardous material periodical " (Zaroual, Z.Journal ofhazardous materials, 2006,131 (3): 73-78; ) in introduced and utilize sequencing batch reactor to handle textile waste with electric flocculence, the clearance of colourity is reached 100%, the COD clearance reaches more than 80%, its effluent quality has reached local emission standard; A.Dimoglo etc. are at " cleaning technique and Environmental policy " (Dimoglo, A.Clean Techn.Environ, 2004,6 (2): introduced with electric flocculation technique 288-295) and handled petrochemical wastewater, clearance to turbidity is about 88%, the clearance of oleaginousness is about 80%, and the clearance of COD is about 80%, and wherein the clearance of hydro carbons and phenolic compound is respectively 80% and 50%; Old snow is bright at " water technology " (1997,23 (3): analyzed the power consumption of electric flocculation plant and the relation between the various influence factor 165-168) theoretically, the theoretical calculation formula that has proposed the processing energy consumption has illustrated power consumption and current density, the treating water specific conductivity, the relation between polar plate spacing and the electric current leakage rate.
Take a broad view of domestic and international present Research, the electric flocculation technique equipment configuration is simple, does not need to use to add chemical agent, and it is a kind of rising waste water treatment process that non-secondary pollution, electricity consumption flocculence are handled waste water.Yet, research at present is mainly based on the research pollutant removal, and analysis various factors such as concentration of electrolyte, Pollutant levels, current density, electrode materials, pH values etc. are to the influence of pollutant removal, and for operating process how to simplify the electricity flocculation, cut down the consumption of energy, prevent that effectively aspects such as battery lead plate passivation also lack further investigation, especially lack theory to electric flocculation reactor moulding design, for a certain specific water quality, adopt the reactor of which kind of structure, processing parameter, how to optimize etc., still by rule of thumb or test come to determine, can not infer fully theoretically.
The utility model content
The purpose of this utility model is in order to solve above-mentioned deficiency, to propose the electric flocculation reactor that a kind of energy consumption is low, simple to operate, can effectively handle multiple sewage.
For realizing above-mentioned utility model purpose, the utility model adopts following technical scheme:
A kind of efficient electric flocculation reactor of adjustable economize on electricity interpole gap, comprise reactive tank, the top of reactive tank is provided with water outlet, the bottom is provided with water-in and scale removing mouth, frame has dividing plate directly over the described reactive tank, and dividing plate is provided with the hole slot of equidistant 10mm, and negative electrode is a Graphite Electrodes, anode is the ferroelectric utmost point, and anodic-cathodic is realized fixing by the mode of inserting hole slot and linked to each other with external power source.Described whipping appts is stirring arm or magnetic stirring apparatus.The useful area of anode and negative electrode and reactive tank volumetric ratio are 1: 11～13.
After adopting technique scheme, sewage enters the flocculating chamber from the water-in of reactive tank bottom, produces flco after the electrolytic pole board electrolysis, stirs post precipitation waste water and is discharged by water outlet.Because negative electrode adopts Graphite Electrodes, anode adopts the ferroelectric utmost point, and therefore, negative electrode does not consume in electric flocculation reaction process, and anode then generates Fe (OH) in reaction
3And Fe (OH)
2Flco.Consider sewage mobile from bottom to top in reactive tank, this water conservancy condition is relatively stable, helps growing up of flco.Simultaneously, the stirring by whipping appts can make reaction more abundant in electric flocculation process.Generally speaking, will effectively improve the treatment effect of electricity flocculation after the employing the technical program.
As a kind of innovation, equidistant (10mm) hole slot that described dividing plate is provided with makes operator not promoting external voltage, not increase under the prerequisite of reactive tank number, inserts the position improvement of hole slot to the different characteristics sewage treatment effect by changing electrode.In addition, make operator's regular dismounting electrolytic pole board, remove the dirt on the electrode, prolong electrode life, prevent electrode passivation, guarantee electric flocculation treatment effect but described electrode inserts the fixed form of hole slot.
In addition, reactor also can increase according to the practical situation of sewage or reduce the reactive tank number, and conditioned reaction system size realizes the effective processing to multiple sewage such as paper pulp wastewater, mining industry waste water, food wastewater, dyeing waste water, oilfield sewages.
The utility model has overcome electric flocculation reactor energy consumption height, inferior positions such as complicated operation, in treating processes, multiple pollutents such as the COD in the sewage, SS are under the acting in conjunction of multiple electrochemical reactions such as electricity flocculation, active oxidation, active reduction, by disposable removing, clearance rate is more than 90%.
Description of drawings
Fig. 1 is the structural representation of the utility model electricity flocculation reactor.
Fig. 2 is the plan structure synoptic diagram of reactive tank in the utility model electricity flocculation reactor.
Fig. 3 is the structural representation when whipping appts adopts another kind of embodiment in the utility model electricity flocculation reactor.
Each description of reference numerals among the figure
The 1-reactive tank 5-anode 8-12-of flocculating chamber magnetic stirring apparatus
2-water-in 6-negative electrode 9-hole slot
3-water outlet 7a-stirring rake 10-dividing plate
4-scale removing mouth 7b-magneton 11-power supply
Embodiment
Explain the utility model in detail with the form of embodiment below, but the utility model is not limited to following examples.
A kind of efficient electric flocculation reactor of adjustable economize on electricity interpole gap, comprise reactive tank 1, the top of reactive tank 1 is provided with water outlet 3, the bottom is provided with water-in 2 and scale removing mouth 4, frame has dividing plate 10 directly over the reactive tank 1, dividing plate 10 is provided with the equidistantly hole slot 9 of (10mm), and anodic-cathodic is realized fixing by the mode of inserting hole slot and linked to each other with power supply 11.Whipping appts can be stirring arm 7a or magnetic stirring apparatus 12.
Example one: electric flocculation treatment tropeolin-D waste water effect research
Utilize the utility model device to handle tropeolin-D waste water, experimental installation as shown in Figure 3, the processing volume of reactive tank 1 is 500ml, anode 5 is the ferroelectric utmost point, negative electrode 6 is a Graphite Electrodes, and the anodic-cathodic useful area is 10cm * 4cm, and the electrode useful area is 1: 12.5 with reactive tank processing volume ratio.Experiment comes the control electrode distance by the distance of regulating electrode insertion hole slot, and electrode distance is 2.5cm in the experiment.Electric current is controlled by constant voltage supply, and output voltage range is 0～50V.Reactive tank 1 places on the magnetic stirring apparatus 12 and stirs (reaction system is less so adopt magnetic stirrer), be provided with the magneton 7b that cooperates practicality with magnetic stirring apparatus 12 in the flocculating chamber 8 of reactive tank 1, make reaction evenly, the temperature regulating device that temperature of reaction is carried by whipping appts is controlled at 25 ℃.
Experimental result is found: be 3.0 in methyl orange solution pH value, the concentration 0.5gL of bath voltage 20V, wastewater volume 500ml, ionogen KCL
-1Condition under, adopt electric flocculence to handle 500mgL
-1Tropeolin-D simulated wastewater 10min, its chroma removal rate can reach 97%; After handling 60min, initial COD
CrConcentration is 858mgL
-1The tropeolin-D simulated wastewater, COD
CrClearance can reach 92%.
Example two: spread of electrodes is to the impact effect research of various wastewater chroma removal rate
Utilize the utility model device treating refuse percolate, oil field waste and tropeolin-D waste water, experimental installation as shown in Figure 3.The pH value of regulating three kinds of waste water is 3.0, bath voltage is the concentration 0.5gL of 20V, ionogen KCL
-1, chroma removal rate and spread of electrodes relation see Table 1 behind the processing 30min.
Table 1 spread of electrodes is to the influence of different chroma in waste water clearances
Tropeolin-D waste water, oil field waste and percolate chroma removal rate maximum are respectively as shown in Table 1: 97.6%, 97.8%, 98.7%, the optimum electrode spacing is respectively: 25mm, 20mm, 15mm, therefore test shows that this device can be at booster tension not, do not increase under the prerequisite of reactive tank number, insert the position improvement of hole slot to the different characteristics sewage treatment effect by changing electrode.
Claims (5)
1. the efficient electric flocculation reactor of an adjustable economize on electricity interpole gap, comprise reactive tank (1), anode (5), negative electrode (6), whipping appts, flocculating chamber (8) and power supply (11), it is characterized in that: described reactive tank (1) bottom is provided with water-in (2) and scale removing mouth (4), and the top of reactive tank (1) is provided with water outlet (3); Reactive tank (1) top is provided with the dividing plate (10) that fixed electorde is used, and dividing plate (10) is provided with equally spaced hole slot (9).
2. the efficient electric flocculation reactor of adjustable economize on electricity interpole gap according to claim 1 is characterized in that: the spacing that dividing plate (10) is gone up adjacent hole slot (9) is 10mm.
3. the efficient electric flocculation reactor of adjustable economize on electricity interpole gap according to claim 1 is characterized in that: described anode (5) is the ferroelectric utmost point, and described negative electrode (6) is a Graphite Electrodes.
4. the efficient electric flocculation reactor of adjustable economize on electricity interpole gap according to claim 1 is characterized in that: the useful area and the reactive tank volumetric ratio of described anode (5) and negative electrode (6) are 1: 11～13.
5. the efficient electric flocculation reactor of adjustable economize on electricity interpole gap according to claim 1 is characterized in that: described whipping appts is magnetic stirring apparatus (12) or stirring rake (7a).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206195655U CN201882958U (en) | 2010-11-22 | 2010-11-22 | High-efficient electrocoagulation reactor capable of adjusting pitches among electrodes |
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| CN2010206195655U CN201882958U (en) | 2010-11-22 | 2010-11-22 | High-efficient electrocoagulation reactor capable of adjusting pitches among electrodes |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101973607A (en) * | 2010-11-22 | 2011-02-16 | 浙江富春江环保热电股份有限公司 | Efficient electrocoagulation reactor capable of adjusting electrode distance |
| CN102336472A (en) * | 2011-09-08 | 2012-02-01 | 大连理工大学 | Electrically enhanced ANAMMOX biologic nitrogen removal method |
| CN102701337A (en) * | 2012-05-29 | 2012-10-03 | 中国科学院过程工程研究所 | Method and reactor for removing organic matters by enzyme electrode coupled electroflocculation |
| WO2013013342A1 (en) * | 2011-07-28 | 2013-01-31 | General Electric Company | Apparatus for one step removal of contaminants from aqueous system and method thereof |
-
2010
- 2010-11-22 CN CN2010206195655U patent/CN201882958U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101973607A (en) * | 2010-11-22 | 2011-02-16 | 浙江富春江环保热电股份有限公司 | Efficient electrocoagulation reactor capable of adjusting electrode distance |
| WO2013013342A1 (en) * | 2011-07-28 | 2013-01-31 | General Electric Company | Apparatus for one step removal of contaminants from aqueous system and method thereof |
| CN102336472A (en) * | 2011-09-08 | 2012-02-01 | 大连理工大学 | Electrically enhanced ANAMMOX biologic nitrogen removal method |
| CN102336472B (en) * | 2011-09-08 | 2013-07-31 | 大连理工大学 | Electrically enhanced ANAMMOX device |
| CN102701337A (en) * | 2012-05-29 | 2012-10-03 | 中国科学院过程工程研究所 | Method and reactor for removing organic matters by enzyme electrode coupled electroflocculation |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110629 Termination date: 20181122 |
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| CF01 | Termination of patent right due to non-payment of annual fee |