CN107275651A - A kind of TiO2The preparation method of microbiological fuel cell hydrogen manufacturing - Google Patents
A kind of TiO2The preparation method of microbiological fuel cell hydrogen manufacturing Download PDFInfo
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- CN107275651A CN107275651A CN201710421229.6A CN201710421229A CN107275651A CN 107275651 A CN107275651 A CN 107275651A CN 201710421229 A CN201710421229 A CN 201710421229A CN 107275651 A CN107275651 A CN 107275651A
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- fuel cell
- microbiological fuel
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/16—Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8825—Methods for deposition of the catalytic active composition
- H01M4/8828—Coating with slurry or ink
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9075—Catalytic material supported on carriers, e.g. powder carriers
- H01M4/9083—Catalytic material supported on carriers, e.g. powder carriers on carbon or graphite
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0656—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by electrochemical means
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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
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- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Materials Engineering (AREA)
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- Microbiology (AREA)
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- Inert Electrodes (AREA)
Abstract
The invention discloses a kind of TiO2The preparation method of microbiological fuel cell hydrogen manufacturing, fuel battery cathode material uses titania nanotube, the decomposition water under light conditions, produces hydrogen;Comprise the following steps:The deionized water of measured amounts, absolute ethyl alcohol adds P25, NaOH solid wherein;Ultrasound is simultaneously stirred, bottom does not have attachment, it is poured into the liner of reactor and adds stirring magneton, oil bath, sample takes out and is first washed with deionized, and then with HCl centrifuge washings repeatedly, then is washed with deionized water to neutrality, dried in vacuum drying chamber, finally calcining can prepare titania nanotube in tube furnace.Titania nanotube is applied on microorganism fuel cell cathode, microbiological fuel cell produces hydrogen through running after a while in the case of sunshine irradiation.The present invention improves titania nanotube photocatalytic hydrogen production by water decomposition ability using photoelectric-synergetic effect, while can generate electricity, handles organic pollution, simple system, hydrogen generation efficiency is high.
Description
Technical field
The invention belongs to microbiological fuel cell field, specifically related to a kind of TiO2The making of microbiological fuel cell hydrogen manufacturing
Method.
Background technology
Microbiological fuel cell be it is a kind of the chemical energy stored in debirs can be converted into electric energy it is renewable,
Clean energy technology, is had broad prospects in waste water resource using aspect.Electrode material is used as electrochemical reaction and electronics
The important place of transmission, is the important component of energy storage conversion devices, and the performance to electrochemical energy is played to pass weight
The effect wanted.Therefore cathode material has very important meaning to the performance for lifting microbiological fuel cell.The calorific value of hydrogen
Height, combustion velocity is fast, water is produced after releasing energy and renewable, is acknowledged as a kind of cleaning green energy resource.At present, produce
The method of hydrogen has many kinds, chemical hydrogen manufacturing, water electrolysis hydrogen production, biological hydrogen production etc..Wherein chemical hydrogen manufacturing is mostly by natural gas
The reformation of the compounds such as oil is made, and is current hydrogen manufacturing mode most widely used in the world.Water electrolysis hydrogen production is a kind of complete
The hydrogen manufacturing mode of cleaning, but its energy consumption is larger, is subject to certain restrictions at the scene in terms of hydrogen manufacturing.Biological hydrogen production is with organic waste
Thing is raw material, and hydrogen is produced by microbial fermentation, but fermentation and hydrogen production can not make organic matter exhaustive oxidation, and production hydrogen rate is relatively low.
The microbiological fuel cell production hydrogen studied at present is mostly catalyst using platinum, but platinum price is costly, limitation
Its application in practice, while main method is applied voltage.Cathode microbial fuel by catalyst of titanium dioxide
Battery can have higher power output, cheap and easy to get, and the dielectric constant of titanium dioxide is higher, therefore with excellent electrical property
Energy.Titanium dioxide has the performance of semiconductor, at the same can ultraviolet irradiation under decomposition water, produce hydrogen.
The content of the invention
The present invention relates to a kind of TiO2The preparation method of microbiological fuel cell hydrogen manufacturing, anode of microbial fuel cell is decomposed
Organic matter, electronics and proton are provided for negative electrode, and negative electrode uses titania nanotube material also primary electron and photochemical catalyzing
Hydrogen manufacturing, the hydrogen produced is collected by vacuum collection airbag.It is simple in construction, fewer than traditional microbiological fuel cell hydrogen manufacturing extraneous electricity
The input of pressure, supplied for electronic and proton are stopped than traditional photocatalysis water hydrogen manufacturing, improve decomposition efficiency.
The present invention adopts the following technical scheme that, a kind of TiO2The preparation method of microbiological fuel cell hydrogen manufacturing, its feature exists
It is as follows in method and step:
(1) 30ml deionized water is measured, absolute ethyl alcohol 30ml adds 2g P25 (titanium dioxide granules wherein)、10
Mol/L NaOH solution 30ml;2 h of ultrasound, stir 12 h, are well mixed it, bottom does not have attachment, is poured into
The liner of reactor(100ml) and it is put into drying box 180 DEG C of reaction 24h;
(2) sample takes out and is first washed with deionized, then multiple with 0.01 mol/L HCl centrifuge washings, then spends
Ion is washed to neutrality, dries 10 h under the conditions of 40 DEG C in vacuum drying chamber(Note aqueous in material before drying
Amount, first can carry out suction filtration to solid), last 350 DEG C of (nitrogen protection) calcining, 4 h in tube furnace.(5 DEG C of programming rate/
min);
(3)Sample 20mg plus 30uL adhesive plus 120 μ L deionizations are taken, ultrasonic 30min is applied on 1*2cm carbon cloth;Ventilation
Drying 24h can be assembled on microorganism fuel cell cathode;
(4)Double-chamber microbiological fuel cell, centre takes PEM to separate, and tinfoil parcel anode prevents ultraviolet from irradiating;
Negative electrode is sealed, and uses incandescent lamp(Or ultraviolet)Irradiation, gas is collected using vacuum bag.
In step (4) of the present invention, microbiological fuel cell, which is used, uses PEM between double-chamber structure, dual chamber
Separate, anode is sodium acetate using the sludge in domestication sewage treatment plant, anode nutriment, and cathode solution is buffer solution.
In step (4) of the present invention, it is characterised in that Cathode buffer liquid concentration is 0.1M.
It is an advantage of the invention that:The microbiological fuel cell hydrogen manufacturing new method of the present invention, is acted on, negative electrode using photoelectric-synergetic
Titania nanotube photocatalytic hydrogen production by water decomposition ability is improved, anode can be produced electricity, and anode can be with synchronization process organic contamination
Thing.
Brief description of the drawings
Fig. 1 produces hydrogen schematic diagram for the microbiological fuel cell of the present invention.
Fig. 2 is titania nanotube XRD diffraction patterns of the invention.
In figure, 1- carbon brush, 2- instrument connections, 3- liquid-changing holes, 4- anodes, 5- test systems, 6- external resistances, 7- clips, 8-
PEM, 9- magnetons, 10- carbon cloths, 11- negative electrodes, 12- flexible pipes, 13- vacuum bags.
Embodiment
Below in conjunction with the accompanying drawings and the invention will be further described by embodiment, but it should be noted that embodiment not
Constitute the restriction to the claimed scope of the invention.
In Fig. 1, microbiological fuel cell of the invention production hydrogen schematic diagram, mainly by 1- carbon brush, 2- instrument connections, 3- changes liquid
Hole, 4- anodes, 5- test systems, 6- external resistances, 7- clips, 8- PEMs, 9- magnetons, 10- coating graphene-titanium dioxides
Titanium carbon cloth, 11- negative electrodes, 12- flexible pipes, 13- vacuum bags composition.It is characterized in that passing through 8- protons between 4- anodes and 11- negative electrodes
Exchange membrane, which separates to combine using 7- clips, 2- instrument connections and 3- liquid-changing holes on composition main part, 4- anodes, 4- sun
Be inside pole inside 1- carbon brush position, 4- anodes inside 1- carbon brush and 11- negative electrodes 10- coating graphene-titanium dioxide carbon cloths by
6- external resistances are connected, and 5- test systems are connect in the connection of 6- external resistances, and 9- magnetons respectively have one in 4- anodes and 11- negative electrodes, and 11- is cloudy
It is 10- coating graphene-titanium dioxide carbon cloths inside pole, 11- negative electrodes and 13- vacuum bags, metal contact is connected by 12- flexible pipes
Gap at AB glue seal.
Case study on implementation
A kind of TiO2The preparation method of microbiological fuel cell hydrogen manufacturing, it is characterised in that method and step is as follows:
(1) deionized water of measured amounts, adds 0.1g P25 (titanium dioxide granules wherein), 4 g NaOH consolidate
Body, the concentration for finally ensureing NaOH solution is 10mol/L.2 h of ultrasound, stir 12 h, are well mixed it, bottom is not attached
Thing, the liner of reactor is poured into(25ml) and stirring magneton is put into, is transferred in oil bath that (magneton is still in a kettle.
Still in stirring during reaction) 120 DEG C of reaction 24h.
(2) sample takes out and is first washed with deionized, then multiple with 0.01 mol/L HCl centrifuge washings, then uses
Deionized water is washed till neutrality, dries 10 h under the conditions of 40 DEG C in vacuum drying chamber(Note aqueous in material before drying
Amount, first can carry out suction filtration to solid), last 400 DEG C of (nitrogen protection) calcining, 2 h in tube furnace.(5 DEG C of programming rate/
min)。
(3) sample 20mg plus 30 μ L adhesives plus 120 μ L deionizations are taken, ultrasonic mixing 30min is applied to 1*2cm carbon
On cloth.Aeration-drying 24h can be assembled on microorganism fuel cell cathode.
(4) double-chamber microbiological fuel cell, centre takes PEM to separate, and tinfoil parcel anode prevents ultraviolet from shining
Penetrate.Negative electrode is sealed, and uses incandescent lamp(Or ultraviolet)Irradiation, gas is collected using vacuum bag.Anode is using domestication sewage disposal
Sludge in factory, anode nutriment is sodium acetate, and cathode solution buffer concentration is 0.1M/L.
Claims (7)
1. a kind of TiO2The preparation method of microbiological fuel cell hydrogen manufacturing, it is characterised in that method and step is as follows:
(1) 10 mol/L NaOH solution 30ml, absolute ethyl alcohol 30ml are measured, 2g P25 is added wherein;2 h of ultrasound,
12 h are stirred, are well mixed it, bottom does not have attachment, is poured into the liner of reactor and is put into 180 in drying box
DEG C reaction 24h;
(2) sample takes out and is first washed with deionized, then multiple with 0.01 mol/L HCl centrifuge washings, then spends
Ion is washed to neutrality, dries 10 h under the conditions of 40 DEG C in vacuum drying chamber, finally 350 DEG C of 4 h of calcining in tube furnace;
(3)Sample 20mg plus 30uL adhesive plus 120 μ L deionizations are taken, ultrasonic 30min is applied on 1*2cm carbon cloth;Ventilation
Drying 24h can be assembled on microorganism fuel cell cathode;
(4)Microbiological fuel cell is double-chamber structure, and centre takes PEM to separate, and tinfoil parcel anode prevents ultraviolet
Irradiation;Negative electrode is sealed, and is irradiated using incandescent lamp, and gas is collected using vacuum bag.
2. according to the method described in claim 1, it is characterised in that:Described step (1) naoh concentration is 10mol/
L30ml, absolute ethyl alcohol is 30ml, and P25 is ultrasonic mixing 2h before 2g, hydro-thermal reaction, stirs 12h.
3. according to the method described in claim 1, it is characterised in that:Described step (1) hydrothermal temperature is 180 DEG C, when
Between be 24h.
4. according to the method described in claim 1, it is characterised in that:Described step (2) sample is washed with deionized water to neutrality,
10 h are dried under the conditions of 40 DEG C in vacuum drying chamber, (nitrogen protection) 350 DEG C of calcining 4h (programming rates 5 in tube furnace
℃/min)。
5. according to the method described in claim 1, it is characterised in that:Described step (3) sample 20mg adds 30 μ L Nafion molten
Liquid, 120 μ L deionizations, ultrasonic mixing 30min.
6. according to the method described in claim 1, it is characterised in that:Described step (4) microbiological fuel cell uses dual chamber
Separated between structure, dual chamber using PEM, anode is using the sludge in domestication sewage treatment plant, anode nutriment
Sodium acetate, cathode solution is buffer solution.
7. according to the method described in claim 1, it is characterised in that:Described step (4) Cathode buffer liquid concentration is 0.1M/
L。
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112458487A (en) * | 2020-09-03 | 2021-03-09 | 南昌航空大学 | Medium-alkali asymmetric microbial electrolytic cell and application thereof in hydrogen production |
Citations (4)
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CN104311142A (en) * | 2014-09-30 | 2015-01-28 | 东南大学 | Vertically grown TiO2 nanosheet and preparation method thereof |
CN105308782A (en) * | 2013-06-20 | 2016-02-03 | 加利福尼亚大学董事会 | Self-biased and sustainable microbial electrohydrogenesis device |
-
2017
- 2017-06-07 CN CN201710421229.6A patent/CN107275651A/en active Pending
Patent Citations (4)
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US20080213632A1 (en) * | 2007-02-10 | 2008-09-04 | Noguera Daniel R | Light-powered microbial fuel cells |
CN102381727A (en) * | 2011-04-02 | 2012-03-21 | 中国海洋大学 | Process for preparing titanium dioxide mesoporous nano-belt material by solvothermal method |
CN105308782A (en) * | 2013-06-20 | 2016-02-03 | 加利福尼亚大学董事会 | Self-biased and sustainable microbial electrohydrogenesis device |
CN104311142A (en) * | 2014-09-30 | 2015-01-28 | 东南大学 | Vertically grown TiO2 nanosheet and preparation method thereof |
Non-Patent Citations (2)
Title |
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QING-YUN CHEN等: "Hydrogen production on TiO2 nanorod arrays cathode coupling with bio-anode with additional electricity generation", 《JOURNAL OF POWER SOURCES》 * |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112458487A (en) * | 2020-09-03 | 2021-03-09 | 南昌航空大学 | Medium-alkali asymmetric microbial electrolytic cell and application thereof in hydrogen production |
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