CN204375849U - A kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field - Google Patents
A kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field Download PDFInfo
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- CN204375849U CN204375849U CN201420864208.3U CN201420864208U CN204375849U CN 204375849 U CN204375849 U CN 204375849U CN 201420864208 U CN201420864208 U CN 201420864208U CN 204375849 U CN204375849 U CN 204375849U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Abstract
The utility model discloses a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field.This fuel cell comprises reaction system, externally-applied magnetic field and data acquisition and monitoring system.Reaction system comprises anode reaction system and cathode reaction system, and wherein anode reaction system comprises anode microbe, anode electrode, anode chamber, enters sample tap and electrolyte.Cathode reaction system comprises cathode microbial, cathode electrode, cathode chamber, sample feeding pipe, return duct, air-blowing pump, brown surge flask, wireway, aeration head, constant flow pump and electrolyte.Externally-applied magnetic field comprises two blocks of the same magnet.Data acquisition and monitoring system comprises conductive filament, wire, external resistance, data acquisition system.The utility model can remove carbon and phosphorus in waste water simultaneously, and nitrogen in waste water is oxidized to nitrate nitrogen, realizes high efficiency synchronous dephosphorization, de-carbon, nitrated and electrogenesis.Externally-applied magnetic field effectively improves electrogenesis and the sewage disposal performance of microbiological fuel cell.
Description
Technical field
The utility model belongs to biological fuel cell field, particularly relates to a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field.
Background technology
Along with the mankind increase day by day to environmental resource exploitation activity, industrial and agricultural production develops rapidly on a large scale, phenomenon that industrialization brings " urbanization ", makes the sewage in a large number containing pollutant hardly degraded organic substance, nitrogen, phosphorus etc. enter lake, reservoir and river.There is large-area body eutrophication phenomenon in the reservoir in urban lakes and contiguous cities and towns.The eutrophication initial stage, Measures of Algae in Water Body and other planktonic organisms breed rapidly, water body production capacity improve; In the eutrophication later stage, the decline of Dissolved Oxygen in Water content, algae, planktonic organism, plant, aquatile and fish decline even disappear.Eutrophication has become the great environmental problem in world wide in water environment protection.
Microbiological fuel cell (Microbial Fuel Cell, MFC) a kind ofly utilizes microbe that the chemical energy in organic substance is directly changed into the device of electric energy.Utilize microbiological fuel cell, not only can organic substance in pollution degradation water body and remove the pollutants such as nitrogen, phosphorus and heavy metal, but also the electron recovery that can will produce in decomposing organic matter process, be converted into electric current, thus obtain electric energy.Under the dual-pressure of energy shortage and environmental pollution, microbiological fuel cell receives the attention of national governments and major company because synchronously processing waste water and electrogenesis, be considered to 21 century cleaning, efficiently generation technology.
Microbiological fuel cell operation principle: anaerobe, anodic oxidation is organic while, produces electronics and proton.Electron transmission, on anode, arrives negative electrode by external circuit, and the proton that proton is transmitted by proton exchange membrane arrival negative electrode and external circuit generates water with oxygen reaction under catalyst action, thus completes the loop of electronics and proton.Along with the organic continuous oxidation of anode and cathode reaction continue carry out, obtain lasting electric current under closed-loop path.
Utility model content
The purpose of this utility model overcomes the deficiencies in the prior art, provides a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field.
A kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field, comprise reaction system, externally-applied magnetic field and data acquisition and monitoring system, described reaction system comprises anode reaction system and cathode reaction system, and wherein anode reaction system comprises anode microbe, anode electrode, anode chamber, enters sample tap and electrolyte; Cathode reaction system comprises cathode microbial, cathode electrode, cathode chamber, sample feeding pipe, return duct, air-blowing pump, brown surge flask, wireway, aeration head, constant flow pump and electrolyte; In cathode reaction system, electrolyte is successively through return duct, brown surge flask, sample feeding pipe, under the effect of constant flow pump, form Inner eycle; Air-blowing pump is connected with aeration head in brown surge flask by wireway; Anode chamber is identical with size with cathode chamber structure, and both are separated by proton exchange membrane, and anode electrode and cathode electrode are close to proton exchange membrane both sides respectively; Externally-applied magnetic field comprises two blocks of magnet, and two blocks of magnet are close to outside anode chamber and cathode chamber respectively, parallel with cathode electrode direction with proton exchange membrane, anode electrode; Data acquisition and monitoring system comprises conductive filament, wire, external resistance, data acquisition system; Anode electrode and cathode electrode are all connected with conductive filament, and conductive filament is connected to form closed-loop path by wire and external resistance again; External resistance two ends are also connected with data acquisition system by wire.
Further, return duct is connected with the delivery port at cathode chamber top, and sample feeding pipe passes the water inlet at cathode chamber top and stretches into cathode chamber inner bottom part.
Further, two blocks of magnet in externally-applied magnetic field are size, structure, permanent magnet that magnetic field intensity is identical, and with anode chamber and cathode chamber near magnet coplanar flat smooth; Two blocks of magnet are that opposite pole is relative or like pole is relative.
Further, except sample introduction and sampling process, the sample tap that enters at top, anode chamber is closed condition always, to guarantee that anode chamber is anaerobic environment; Air-blowing pump is open mode always, makes cathode reaction system always in good oxygen condition; In brown surge flask, aeration rate size is regulated by air-blowing pump discharge control button.
Further, the magnetic field intensity of two pieces of magnet surfaces is 0 ~ 200 mT.
Further, described electrolyte is Nitrogen-and Phosphorus-containing organic wastewater, and initial pH is 7.0 ~ 7.5.
Further, in anode chamber, dissolved oxygen is 0.02 ~ 0.05 mg/L, brown surge flask electrolyte inside dissolved oxygen is 0.5 ~ 5.0 mg/L, different cathode chamber dissolved oxygen microbiological fuel cell output voltage, dephosphorization, de-carbon and nitrogen nitrification effect are all different, even likely denitrogenate under low DO condition simultaneously.
Further, after this microbiological fuel cell output voltage is less than 50 mV, brown surge flask electrolyte inside is discharged to outside reaction system, electrolyte in anode chamber is back in brown surge flask, after fill it up with fresh untreated Nitrogen-and Phosphorus-containing organic wastewater in the anode compartment, circular flow like this.
Further, the height of anode chamber and cathode chamber is more than or equal to the width of horizontal direction.
Further, anode electrode is identical with cathode electrode area, is carbon cloth, carbon paper, carbon felt, graphite felt or graphite cake, both can identical also can be different, the volume ratio of electrode area and reative cell is 1 cm
2: 0.1 ~ 10 cm
3
Further, described anode microbe and cathode microbial are microbe mixts in the active sludge microorganism of sewage treatment plant's process sanitary sewage and the microbiological fuel cell of stable operation half a year.
Further, electrolyte is full of in anode chamber and cathode chamber, during primary starting, the anaerobic and aerobic mud supernatant of microbe, sewage treatment plant's secondary sedimentation tank in stable operation microbiological fuel cell half a year of inoculation bacterium liquid to be volume ratio be 1:3:3, inoculation bacteria liquid long-pending with chamber volume than being 1:3.When output voltage is less than 50 mV, electrolyte in brown surge flask is discharged to outside reaction system, anode chamber's electrolyte inside is all back in brown surge flask, adds fresh untreated Nitrogen-and Phosphorus-containing organic wastewater (artificial distribution or actual waste water) in anode room.
Further, described anode chamber is a strictly anaerobic environment, and anolyte dissolved oxygen is 0.02 ~ 0.05 mg/L.The air-blowing pump that brown surge flask connects is in open mode always, and controls aeration rate size with air-blowing pump discharge control button, thus the dissolved oxygen of control cathode liquid, in cathode chamber, dissolved oxygen controls within the scope of 0.5 ~ 5.0 mg/L.
Further, described data acquisition system is Keithley 2007 type data acquisition unit.
Compared with the prior art, the utility model tool has the following advantages and beneficial effect:
(1) the reactor start-up time obviously shortens, and electrogenesis amount increases;
(2) externally-applied magnetic field effectively reduces the internal resistance of microbiological fuel cell, improves the performance of microbiological fuel cell;
(3) this reaction system can efficient dephosphorization and de-carbon, and nitrogen in electrolyte can high efficiency nitrification;
(4) this reaction system can under negative electrode low DO condition simultaneous denitrification, dephosphorization, de-carbon electrogenesis;
(5) externally-applied magnetic field not only effectively improves microbiological fuel cell electrogenesis and water treatmenting performance, also reduces the operation energy consumption of microbiological fuel cell;
(6) brown surge flask effectively improves microbiological fuel cell operation stability, the diffusion of less cathode dissolution oxygen anode room.
Accompanying drawing explanation
Fig. 1 is a kind of efficient dephosphorization nitrification microbial fuel cell structural representation being provided with externally-applied magnetic field.
Fig. 2 is that in embodiment, externally-applied magnetic field is 50 mT, and cathode dissolution oxygen is about 3.5mg/L electrogenesis Data Comparison figure when starting with blank group.
Fig. 3 a, Fig. 3 b are that in embodiment, externally-applied magnetic field is 50 mT respectively, and cathode dissolution oxygen is about 3.5mg/L and the polarization curve of blank group and power density curve.
Embodiment
Below by specific embodiment, being described in detail implementation of the present utility model, if having process or the technique of special detailed description below, is all that those skilled in the art can refer to existing techniques in realizing.
A kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field in this example, as shown in Figure 1, by anode chamber 3), anode electrode 5), anode microbe 4), enter sample tap 6), proton exchange membrane 1), the double-chamber microbiological fuel cell that forms of cathode chamber 16, cathode electrode 17, cathode microbial 15, sample feeding pipe 13, return duct 11, air-blowing pump 14, brown surge flask 19, aeration head 20, constant flow pump 12 and magnet 2, its anode electrode 5 is carbon papers, and cathode electrode 17 scribbles 0.5 mg/cm
2the carbon cloth of platinum carbon, and Catalytic Layer is towards proton exchange membrane 1.
External 1000 Ohmic resistances of battery, intermittent duty at ambient temperature, when cell voltage is lower than 50 mV, brown surge flask 19 electrolyte inside is discharged to outside reaction system, anode chamber 3 electrolyte is back to brown surge flask 19, adds fresh untreated Nitrogen-and Phosphorus-containing organic wastewater in anode room 3.
Manual simulation's waste water is filled a prescription: NaHCO
35.96 g/L, NaC
2h
3o
21.00 g/L, KH
2pO
40.54 g/L, NH
4cl 0.21 g/L, metal and trace element, vitamin.
The utility model starts as follows:
Nitrogen-and Phosphorus-containing manual simulation organic wastewater 80 ml is added in clean beaker, add the inoculation bacterium liquid 40 ml anaerobic and aerobic mud supernatant of microbe, sewage treatment plant's secondary sedimentation tank (in stable operation microbiological fuel cell half a year of inoculation bacterium liquid to be volume ratio be 1:3:3) again, mixing, anode chamber 3 mixed liquor of simulated wastewater and inoculation bacterium liquid is full of about 28 ml, and residual mixed liquor about 92 ml is all added in brown surge flask 19.Sample tap 6 is entered at top, anode chamber 3 seal, open constant flow pump 12 and air-blowing pump 14.After two days, electrolyte in brown surge flask 19 is discharged to outside reaction system, opens top, anode chamber 3 and enter sample tap 6, anode chamber 3 electrolyte inside is all back in brown surge flask 19.Circular flow like this.Reaction system is added to the discharge reaction system whole time period as a reaction time using Nitrogen-and Phosphorus-containing organic wastewater.Time more than three cycles of operation of microbiological fuel cell output voltage stabilization, start-up course completes.
Utility model works process is as follows:
Simulated wastewater joins anode chamber 3, after running 72 h, cell output voltage is less than 50 mV, discharge electrolyte in brown surge flask 19, electrolyte whole in anode chamber 3 is back to brown surge flask 19, add fresh untreated simulated wastewater in anode chamber 3, after 72 h, repeat last round of operation.
Fig. 2 is that in embodiment, externally-applied magnetic field is 50 mT, and cathode dissolution oxygen is about 3.5mg/L electrogenesis data when starting with blank group.Under this condition, additional 50 mT microbiological fuel cells have started required time about 10 days, and maximum output voltage is 553 ± 2 mV.The startup of blank group completes required time about 16 days, and maximum output voltage is 523 ± 2 mV.
Fig. 3 a, Fig. 3 b are in embodiment, and externally-applied magnetic field is 50 mT, the relation of cell power density and cell voltage and current density when electrolyte dissolved oxygen is about 3.5 mg/L in brown surge flask 19.Additional 50 mT microbiological fuel cells are 1936 mA/m in current density
2time reach peak power output 548 mW/ m
2, the internal resistance of cell is about 207 ohm.Under this condition, the clearance of phosphorus is greater than 96%, COD clearance and is greater than 90%, and the mineralized nitrogen of about 70% has become nitrate nitrogen.Blank group is 1791 mA/m in current density
2time reach peak power output 526 mW/ m
2, the internal resistance of cell is about 232 ohm.Under this condition, the clearance of phosphorus is less than 93%, COD clearance about 80%, and the mineralized nitrogen of about 70% has become nitrite nitrogen.
As can be seen from the above experimental data, externally-applied magnetic field can significantly improve microbiological fuel cell electrogenesis and water treatmenting performance.
Finally, it is also to be noted that what enumerate above is only some specific embodiment of the present utility model.Obviously, the utility model is not limited to above examples of implementation, can also have many distortion.All distortion that those of ordinary skill in the art can directly derive from content disclosed in the utility model or associate, all should think protection range of the present utility model.
Claims (7)
1. one kind is provided with the efficient dephosphorization nitrification microbial fuel cell of externally-applied magnetic field, comprise reaction system, externally-applied magnetic field and data acquisition and monitoring system, it is characterized in that: described reaction system comprises anode reaction system and cathode reaction system, wherein anode reaction system comprise anode microbe (4), anode electrode (5), anode chamber (3), enter sample tap (6) and electrolyte; Cathode reaction system comprises cathode microbial (15), cathode electrode (17), cathode chamber (16), sample feeding pipe (13), return duct (11), air-blowing pump (14), brown surge flask (19), wireway (18), aeration head (20), constant flow pump (12) and electrolyte; In cathode reaction system, electrolyte is successively through return duct (11), brown surge flask (19), sample feeding pipe (13), under the effect of constant flow pump (12), form Inner eycle; Air-blowing pump (14) is connected with aeration head (20) in brown surge flask (19) by wireway (18); Anode chamber (3) is identical with size with cathode chamber (16) structure, and both are separated by proton exchange membrane (1), and anode electrode (5) and cathode electrode (17) are close to proton exchange membrane (1) both sides respectively; Externally-applied magnetic field comprises two pieces of magnet (2), and two pieces of magnet (2) are close to anode chamber (3) and cathode chamber (16) outside respectively, parallel with cathode electrode (17) direction with proton exchange membrane (1), anode electrode (5); Data acquisition and monitoring system comprises conductive filament (7), wire (9), external resistance (8), data acquisition system (10); Anode electrode (5) and cathode electrode (17) are all connected with conductive filament (7), and conductive filament (7) is connected to form closed-loop path by wire (9) and external resistance (8) again; External resistance (8) two ends are also connected with data acquisition system (10) by wire (9).
2. a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field according to claim 1, it is characterized in that return duct (11) is connected with the delivery port at cathode chamber (16) top, sample feeding pipe (13) through cathode chamber (16) top water inlet and stretch into cathode chamber (16) inner bottom part.
3. a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field according to claim 1, the two pieces of magnet (2) that it is characterized in that in externally-applied magnetic field are size, structure, permanent magnet that magnetic field intensity is identical, and with anode chamber (3) and cathode chamber (16) near magnet (2) coplanar flat smooth; Two pieces of magnet (2) are for opposite pole is relative or like pole is relative.
4. a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field according to claim 1, it is characterized in that except sample introduction and sampling process, the sample tap (6) that enters at anode chamber (3) top is closed condition always, to guarantee that anode chamber (3) is anaerobic environment; Air-blowing pump (14) is open mode always, makes cathode reaction system always in good oxygen condition; In brown surge flask (19), aeration rate size is regulated by air-blowing pump (14) flow control button.
5. a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field according to claim 1, is characterized in that the magnetic field intensity on two pieces of magnet (2) surfaces is 0 ~ 200 mT.
6. a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field according to claim 1, is characterized in that the height of anode chamber (3) and cathode chamber (16) is more than or equal to the width of horizontal direction.
7. a kind of efficient dephosphorization nitrification microbial fuel cell being provided with externally-applied magnetic field according to claim 1, it is characterized in that anode electrode (5) is identical with cathode electrode (17) area, be carbon cloth, carbon paper, carbon felt, graphite felt or graphite cake, both may be the same or different, and the volume ratio of electrode area and reative cell is 1 cm
2: 0.1 ~ 10 cm
3.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104577171A (en) * | 2014-12-31 | 2015-04-29 | 华南理工大学 | Efficient dephosphorization and nitrification microbial fuel cell with external magnetic field |
| CN105253991A (en) * | 2015-10-20 | 2016-01-20 | 浙江工商大学 | Electromagnetic field coupling desalting device with pollution reduction function and method |
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2014
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104577171A (en) * | 2014-12-31 | 2015-04-29 | 华南理工大学 | Efficient dephosphorization and nitrification microbial fuel cell with external magnetic field |
| CN105253991A (en) * | 2015-10-20 | 2016-01-20 | 浙江工商大学 | Electromagnetic field coupling desalting device with pollution reduction function and method |
| CN105253991B (en) * | 2015-10-20 | 2017-07-21 | 浙江工商大学 | A kind of electromagnetic field couples desalter and method for having the dirty function of drop concurrently |
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| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150603 Termination date: 20171231 |
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| CF01 | Termination of patent right due to non-payment of annual fee |