CN110492157A - Tubular methanol fuel cell - Google Patents

Tubular methanol fuel cell Download PDF

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Publication number
CN110492157A
CN110492157A CN201910689161.9A CN201910689161A CN110492157A CN 110492157 A CN110492157 A CN 110492157A CN 201910689161 A CN201910689161 A CN 201910689161A CN 110492157 A CN110492157 A CN 110492157A
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CN
China
Prior art keywords
screw thread
tubular
porous
fuel cell
methanol
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201910689161.9A
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Chinese (zh)
Inventor
朱应利
高磊
李建宇
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Tianjin University of Science and Technology
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Tianjin University of Science and Technology
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Priority to CN201910689161.9A priority Critical patent/CN110492157A/en
Publication of CN110492157A publication Critical patent/CN110492157A/en
Pending legal-status Critical Current

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04119Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
    • H01M8/04156Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying with product water removal
    • H01M8/04164Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying with product water removal by condensers, gas-liquid separators or filters
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1004Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1009Fuel cells with solid electrolytes with one of the reactants being liquid, solid or liquid-charged
    • H01M8/1011Direct alcohol fuel cells [DAFC], e.g. direct methanol fuel cells [DMFC]
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

The present invention relates to field of fuel cell technology, more particularly to a kind of tubular methanol fuel cell, including the anodic porous internal screw thread cylinder methanol chamber encapsulated from inside to outside, tubular type membrane electrode, porous metal mesh and porous afflux pressure rings, the ring Zhou Jun of the porous afflux pressure rings has equipped with pressure rings aperture, the side of porous afflux pressure rings is opening-like, it is fixed in the position that there are two link blocks, several connecting holes are equipped on link block, bolt passes through the connecting hole, the both ends of bolt are fixed by nut, the pressure of porous afflux pressure rings is adjusted by adjusting nut tightness adjusting, methanol cavity thin-wall aperture is uniformly provided on the side wall of the anodic porous internal screw thread cylinder methanol chamber, the top seal of the anodic porous internal screw thread cylinder methanol chamber is equipped with gas-liquid separation device.Present invention environmental protection is easy sealing, series-parallel combination multiplicity, volumetric specific power density height.

Description

Tubular methanol fuel cell
Technical field
The present invention relates to field of fuel cell technology more particularly to a kind of tubular methanol fuel cells.
Background technique
Direct methanol fuel cell is that the oxygen in a kind of methanol aqueous solution and cathode air by anode passes through electrochemistry Reaction converts chemical energy to the power generator of electric energy, without the reformation hydrogen production by methanol, gasoline and natural gas for hair Electricity itself does not have the combustion reaction process of fuel, therefore is not limited by Carnot cycle, and energy transformation ratio can reach 60%.Low emission, high-energy density, the quickly and easily battery that charges have attracted the concern of more and more people, direct methanol combustion A battery seemingly suitable selection is expected, because it is not only environmentally protective but also capacity usage ratio is high.Direct methanol fuel electricity Pond membrane electrode is mostly, so composition pile can only be together in series using bipolar plates, to form plate and frame knot using plate design Structure, form are relatively simple, volume ratio is cumbersome, and volumetric specific power density is not high, and bipolar plates involve great expense, technical requirements compared with Height is unfavorable for the commercialization process of methanol fuel cell.
Currently, the Tubular Direct Methanol Fuel Cell provided in Chinese patent CN109411792A relies on cathode collector certainly The shortcomings that body fastening force encapsulation battery, the patent is: encapsulation pressure in this way is uncontrollable, and encapsulates pressure to methanol fuel electricity Pond performance is affected, and loosening must occur in the battery structure after working long hours in above-mentioned patent, each component cannot be pasted closely It closes, influences battery performance.In addition, the circular direct methanol fuel battery provided in Chinese patent CN100590923C, the patent Encapsulation pressure it is also unadjustable, in addition battery use check valve carry out physical management, structure is complicated, and cost is higher.
Summary of the invention
It is an object of the invention to overcome the shortcomings of above-mentioned technology, and provide a kind of tubular methanol fuel cell.
To achieve the above object, using following technical scheme: a kind of tubular methanol fuel cell, feature exist the present invention In: including anodic porous internal screw thread cylinder methanol chamber, tubular type membrane electrode, porous metal mesh and the porous collection encapsulated from inside to outside Pressure rings are flowed, the ring Zhou Jun of the porous afflux pressure rings has equipped with pressure rings aperture, and the side of porous afflux pressure rings is in open Mouth shape, fixed in the position there are two link blocks, several connecting holes are equipped on link block, and bolt passes through the connecting hole, The both ends of bolt are fixed by nut, and the pressure of porous afflux pressure rings, the anodic porous are adjusted by adjusting nut tightness adjusting Methanol cavity thin-wall aperture is uniformly provided on the side wall of internal screw thread cylinder methanol chamber, the anodic porous internal screw thread cylinder methanol chamber Top seal is equipped with gas-liquid separation device.
Preferably, the gas-liquid separation device includes that external screw thread screws head, gas-liquid separation membrane and the hollow ventilation of external screw thread Head, the external screw thread screw head and are threadedly coupled with the anodic porous internal screw thread cylinder methanol chamber, and the external screw thread screws in head Portion has cavity, and cavity bottom has connecting hole, and the gas-liquid separation membrane is placed on the top of the connecting hole, the external screw thread The cavity that hollow ventilation head and the external screw thread screw head is threadedly engaged and compresses the gas-liquid separation membrane, and the external screw thread is hollow The inside of ventilation head is equipped with exhaust passage, and one end of exhaust passage is located at the bottom of the hollow ventilation head of external screw thread, and the other end extends To the outside of the hollow ventilation head of external screw thread.The intracavitary electrochemical reaction of battery fuel generates carbon dioxide gas and is effectively discharged, and object Material is blocked in fuel cavity.
Preferably, the tubular type membrane electrode includes the anode gas diffusion layer, anode catalyst layer, proton exchange of tubular structure Film, cathode catalysis layer, tubular structure cathode gas diffusion layer, tubular anode gas diffusion layers are in most inner side, followed by anode Catalytic Layer, proton exchange membrane, cathode catalysis layer, tubular type cathode gas diffusion layer are fitted closely in outermost, five layers of interlayer structure Constitute tubular type membrane electrode.
Preferably, the other end of the exhaust passage is located at the top side of external screw thread air exchange head.
Preferably, it is identical with the external screw thread to screw the connection bore dia of a bottom for the diameter of the exhaust passage.
Preferably, the material of the anodic porous internal screw thread cylinder methanol chamber is graphite or stainless steel and other metal materials.
Preferably, the cathode gas diffusion layer of the anode gas diffusion layer of the tubular structure and tubular structure be carbon cloth, Foam metal, can be with curved conductive gas permeable material or the Ni-based three-dimensional grapheme of foam.
Preferably, layer of transparent is equipped between the edge of the tubular type membrane electrode and anodic porous internal screw thread cylinder methanol chamber Polyester film double-faced waterproofing glue.
The beneficial effects of the present invention are: compared with the existing technology, cell membrane-electrode inner surface has a strata ester film two-sided Marine glue, cell outer end have porous afflux pressure rings, by adjusting bolt and nut control encapsulation pressure, electricity of " acting from inside in coordination with forces attacking from outside " in this way Each component fitting in pond is even closer, and contact internal resistance is smaller;Gas-liquid separation device is simplified, the complexity such as check valve, pump portion has been abandoned Part, only with one layer of gas-liquid separation membrane, external screw thread screws the hollow ventilation head of head, external screw thread from spiralization, and structure is simpler.
Detailed description of the invention
Fig. 1 is surface structure schematic diagram after tubular methanol fuel cell of the present invention encapsulation;
Fig. 2 is that tubular methanol fuel cell of the present invention encapsulates rear axle sectional view;
Fig. 3 is the enlarged drawing in Fig. 2 at A;
Fig. 4 is that tubular methanol fuel cell of the present invention encapsulates after-explosion schematic diagram;
Fig. 5 is the voltage and current-curve and power-current curve of tubular methanol fuel cell of the present invention;
Fig. 6 is the Nyquist curve of tubular methanol fuel cell of the present invention;
In figure: the hollow ventilation head of 1- external screw thread, 2- external screw thread screw head, 3- anodic porous internal screw thread cylinder methanol chamber, 4- Gas-liquid separation membrane, 5- methanol cavity thin-wall aperture, 6- anode gas diffusion layer, 7- anode catalyst layer, 8- proton exchange membrane, 9- cathode Catalytic Layer, 10- cathode gas diffusion layer, 11- porous metal mesh, the porous afflux pressure rings of 12-, 13- nut, 14- screw.
Specific embodiment
With reference to the accompanying drawing and the preferred embodiment specific embodiment that the present invention will be described in detail.Fig. 1-4 shows a kind of pipe Formula methanol fuel cell, including anodic porous internal screw thread cylinder methanol chamber 3, tubular type membrane electrode (the tubular type knot encapsulated from inside to outside The cathode gas expansion of the anode gas diffusion layer 6, anode catalyst layer 7, proton exchange membrane 8, cathode catalysis layer 9, tubular structure of structure Dissipate layer 10), porous metal mesh 11, porous afflux pressure rings 12, screw 14, nut 13.Anodic porous internal screw thread cylinder methanol chamber 3 Whole height is 60mm, internal diameter 17mm, outer diameter 18mm, and wall thickness 0.5mm, methanol chamber height is 40mm, and methanol cavity thin-wall is small Bore dia is 2mm (experiment aperture 1-2 millimeters of battery performance of discovery is optimal), the anode gas diffusion layer 6 and cathode of tubular structure Gas diffusion layers 10 are with a thickness of 0.5mm.The anode gas diffusion layer of the tubular structure and the cathode gas diffusion of tubular structure Layer be carbon cloth, foam metal, can be with curved conductive gas permeable material, the material of gas diffusion layers is that foam is Ni-based in this implementation column Three-dimensional grapheme.It is poly- equipped with layer of transparent between the anode side edges and anodic porous internal screw thread cylinder methanol chamber of tubular type membrane electrode Ester film double-faced waterproofing glue.The two is fitted closely, prevents material from revealing.
The ring Zhou Jun of the porous afflux pressure rings has equipped with pressure rings aperture, is conducive to the discharge of methanol fuel cell product And breathing.The side of porous afflux pressure rings is opening-like, and fixed in the position there are two link blocks, is equipped on link block Several connecting holes, bolt pass through the connecting hole, and the both ends of bolt are fixed by nut, by tightening the porous collection of nut adjustment Flow the pressure of pressure rings.Porous afflux pressurizes itself with certain pretightning force, if encapsulation pressure requirements, Ke Yitong is not achieved in it It crosses and tightens nut increase pressure, in addition can also pass through screw on nut flexible modulation in cell operations and encapsulate pressure.
It includes the hollow ventilation head 1 of external screw thread being arranged from top to bottom, gas-liquid that gas-liquid separation device is placed in the battery Seperation film 4, external screw thread screw first 2, and external screw thread, which screws first 2 and is threadedly engaged with anodic porous internal screw thread cylinder methanol chamber 3, to be screwed, institute It states external screw thread to screw with cavity inside head, cavity bottom has connecting hole, and the gas-liquid separation membrane is placed on the connecting hole Top, the cavity that the hollow ventilation head 1 of the external screw thread and the external screw thread screw first 2 is threadedly engaged and compresses the gas-liquid point From film, the inside of the hollow ventilation head of external screw thread is equipped with exhaust passage, and one end of exhaust passage is located at the hollow ventilation of external screw thread The bottom of head, the other end extend to the outside of the hollow ventilation head of external screw thread.The intracavitary electrochemical reaction of methanol generates after encapsulation two Carbonoxide bubble passes sequentially through connecting hole, gas-liquid separation membrane, exhaust passage discharge, and then to stay in methanol intracavitary for methanol solution.
Fig. 5 shows power-electricity that the obtained square box closed symbols curve in this example is tubular methanol fuel cell Flow curve, circular hollow mark curve is the voltage-current curve of tubular methanol fuel cell, by curve it can be seen that battery Maximum power output be 72mW, cell height 6cm, outer diameter 1.8cm, the volume of battery is 15.26cm3, then tubular type first The volumetric specific power density of alcohol fuel battery is 4.72mW/cm3, because external environment is 26 DEG C of room temperature when battery testing, humidity It is 40%, if improving temperature and humidity, the power of tubular methanol fuel cell can be higher, and performance also can be more preferable.Top it is rectangular Frame closed symbols curve is the power-current curve for having the tubular methanol fuel cell of 11 structure of porous metal mesh, the side of lower part Shape frame closed symbols curve is the power-current curve of the tubular methanol fuel cell of no 11 structure of porous metal mesh, can be seen The battery maximum power output for having 11 structure of porous metal mesh out is 72mW, and the battery highest without 11 structure of porous metal mesh is defeated Power is only 53mW out.The circle marker curve on top is the electricity for having the tubular methanol fuel cell of 11 structure of porous metal mesh Piezo-electric flow curve, the circle marker curve of lower part for the tubular methanol fuel cell of no 11 structure of porous metal mesh electric piezo-electric Flow curve, it can be seen that the battery most High Output Current for having 11 structure of porous metal mesh is 540mA, and without 11 knot of porous metal mesh The battery of structure most High Output Current is only 380mA.
Fig. 6 shows the Nyquist curve graph of tubular methanol fuel cell in this example, and left side circular curve is to have porous gold Belong to the Nyquist curve graph of the tubular methanol fuel cell of 11 structure of net, right side circular curve is to have 11 structure of porous metal mesh Tubular methanol fuel cell Nyquist curve graph, it can be seen that have the tubular methanol fuel electricity of 11 structure of porous metal mesh Pond internal resistance is 0.13 Ω, and the tubular methanol internal resistance of fuel cell of no 11 structure of porous metal mesh is 0.19 Ω, so there is porous gold The tubular methanol internal resistance of fuel cell for belonging to 11 structure of net is lower, and output electric current is higher, and peak power is bigger, and performance is more excellent.
The hollow ventilation head 1 of battery external screw thread and the porous afflux pressure rings 12 (or 11 connecting wire of porous metal mesh) of battery When connecing load, the work of tubular methanol fuel cell electric discharge, after injecting methanol to anodic porous internal screw thread cylinder methanol chamber 3, methanol The table of the anode ring-type nickel foam base graphene gas diffusion layers (anode diffusion layer) 6 of tubular structure is uniformly scattered by aperture Then face passes through the porous structure of the anode ring-type nickel foam base graphene gas diffusion layers (anode diffusion layer) 6 of tubular structure It is evenly distributed in 7 surface of anode catalyst layer, methanol aqueous solution occurs electrochemical reaction in anode catalyst layer and generates carbon dioxide Minute bubbles, hydrogen ion and electronics, while the oxygen in air is small by porous 12 aperture of afflux pressure rings and porous metal mesh 11 Hole and cathode tubulose nickel foam base graphene gas diffusion layers (cathode diffusion layer) 10 uniformly reach cathode catalysis layer 9, and Anode-side imports the electronics of cathode by external circuit and electrochemical reaction generation occurs across the hydrogen ion of proton exchange membrane 8 Water.The carbon dioxide minute bubbles that tubular methanol anode of fuel cell side generates are assembled in anodic porous internal screw thread cylinder methanol chamber 3 And through after gas-liquid separation membrane 4, the hollow structure discharge battery of first 2 and the hollow ventilation head 1 of external screw thread, electricity are screwed by external screw thread The water that pool cathode side generates then passes through cathode tubulose nickel foam base graphene gas diffusion layers (cathode diffusion layer) 10 and porous collection Flow 12 aperture of pressure rings and the discharge of 11 aperture of porous metal mesh.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered It is considered as protection scope of the present invention.

Claims (8)

1. a kind of tubular methanol fuel cell, it is characterised in that: including the anodic porous internal screw thread cylinder first encapsulated from inside to outside The ring Zhou Jun of alcohol chamber, tubular type membrane electrode, porous metal mesh and porous afflux pressure rings, the porous afflux pressure rings is equipped with The side of pressure rings aperture, porous afflux pressure rings is opening-like, and fixed in the position there are two link blocks, sets on link block There are several connecting holes, bolt passes through the connecting hole, and the both ends of bolt are fixed by nut, by adjusting nut tightness adjusting adjusting It is small to be uniformly provided with methanol cavity thin-wall on the side wall of the anodic porous internal screw thread cylinder methanol chamber for the pressure of porous afflux pressure rings The top seal in hole, the anodic porous internal screw thread cylinder methanol chamber is equipped with gas-liquid separation device.
2. tubular methanol fuel cell according to claim 1, it is characterised in that: the gas-liquid separation device includes outer spiral shell Line screws head, gas-liquid separation membrane and the hollow ventilation head of external screw thread, the external screw thread and screws head and the anodic porous internal screw thread Cylinder methanol chamber is threadedly coupled, and the external screw thread is screwed with cavity inside head, and cavity bottom has connecting hole, the gas-liquid point From the top that film is placed on the connecting hole, the cavity screw thread that the hollow ventilation head of external screw thread screws head with the external screw thread is matched Merge and compress the gas-liquid separation membrane, the inside of the hollow ventilation head of external screw thread is equipped with exhaust passage, one end of exhaust passage Positioned at the bottom of the hollow ventilation head of external screw thread, the other end extends to the outside of the hollow ventilation head of external screw thread.
3. tubular methanol fuel cell according to claim 1 or 2, it is characterised in that: the tubular type membrane electrode includes pipe The cathode gas expansion of the anode gas diffusion layer, anode catalyst layer, proton exchange membrane, cathode catalysis layer, tubular structure of formula structure Layer is dissipated, tubular anode gas diffusion layers are in most inner side, followed by anode catalyst layer, proton exchange membrane, cathode catalysis layer, tubular type are negative For pole gas diffusion layers in outermost, five layers of interlayer structure, which fit closely, constitutes tubular type membrane electrode.
4. tubular methanol fuel cell according to claim 3, it is characterised in that: the other end of the exhaust passage is located at The top side of external screw thread air exchange head.
5. tubular methanol fuel cell according to claim 4, it is characterised in that: the diameter of the exhaust passage with it is described The connection bore dia that external screw thread screws a bottom is identical.
6. tubular methanol fuel cell according to claim 5, it is characterised in that: the anodic porous internal screw thread cylinder first The material of alcohol chamber is graphite or stainless steel and other metal materials.
7. tubular methanol fuel cell according to claim 6, it is characterised in that: the anodic gas of the tubular structure expands Dissipate layer and tubular structure cathode gas diffusion layer be carbon cloth, foam metal, can be with curved conductive gas permeable material or foam Ni-based three-dimensional grapheme.
8. tubular methanol fuel cell according to claim 7, it is characterised in that: the edge and sun of the tubular type membrane electrode Layer of transparent polyester film double-faced waterproofing glue is equipped between extremely porous internal screw thread cylinder methanol chamber.
CN201910689161.9A 2019-07-29 2019-07-29 Tubular methanol fuel cell Pending CN110492157A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111999391A (en) * 2020-06-24 2020-11-27 天津科技大学 Acoustic emission monitoring device and fatigue damage analysis method for material structure by using same
CN113488674A (en) * 2021-07-07 2021-10-08 哈尔滨工业大学(深圳) Cylindrical self-breathing fuel cell and assembly method thereof

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US20070178367A1 (en) * 2006-02-01 2007-08-02 Matsushita Electric Industrial Co., Ltd. Direct oxidation fuel cell and method for operating direct oxidation fuel cell system
US20090169941A1 (en) * 2007-10-25 2009-07-02 Relion, Inc. Direct liquid fuel cell
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CN103165923A (en) * 2013-02-06 2013-06-19 中国科学院上海硅酸盐研究所 Electric collecting device of positive electrode supporting tube type battery, manufacture method thereof and battery stack
CN107195929A (en) * 2017-06-28 2017-09-22 天津科技大学 Button-shaped DMFC
CN107572636A (en) * 2017-09-20 2018-01-12 云南腾雅环境科技有限公司 A kind of equipment for minimizing energy-efficient overflow-type electric flocculation technique
CN210467993U (en) * 2019-07-29 2020-05-05 天津科技大学 Tubular methanol fuel cell

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070178367A1 (en) * 2006-02-01 2007-08-02 Matsushita Electric Industrial Co., Ltd. Direct oxidation fuel cell and method for operating direct oxidation fuel cell system
US20090169941A1 (en) * 2007-10-25 2009-07-02 Relion, Inc. Direct liquid fuel cell
CN201962369U (en) * 2011-01-21 2011-09-07 中冶焊接科技有限公司 Tube type electrolytic tank set
CN103094595A (en) * 2013-01-22 2013-05-08 中国科学院上海硅酸盐研究所 Anode support tube type solid oxide fuel cell and assembling method thereof
CN103165923A (en) * 2013-02-06 2013-06-19 中国科学院上海硅酸盐研究所 Electric collecting device of positive electrode supporting tube type battery, manufacture method thereof and battery stack
CN107195929A (en) * 2017-06-28 2017-09-22 天津科技大学 Button-shaped DMFC
CN107572636A (en) * 2017-09-20 2018-01-12 云南腾雅环境科技有限公司 A kind of equipment for minimizing energy-efficient overflow-type electric flocculation technique
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111999391A (en) * 2020-06-24 2020-11-27 天津科技大学 Acoustic emission monitoring device and fatigue damage analysis method for material structure by using same
CN113488674A (en) * 2021-07-07 2021-10-08 哈尔滨工业大学(深圳) Cylindrical self-breathing fuel cell and assembly method thereof
CN113488674B (en) * 2021-07-07 2022-06-17 哈尔滨工业大学(深圳) Assembling method of cylindrical self-breathing fuel cell

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