CN110492139B - Gas mixing device for hydrogen fuel cell - Google Patents
Gas mixing device for hydrogen fuel cell Download PDFInfo
- Publication number
- CN110492139B CN110492139B CN201910713990.6A CN201910713990A CN110492139B CN 110492139 B CN110492139 B CN 110492139B CN 201910713990 A CN201910713990 A CN 201910713990A CN 110492139 B CN110492139 B CN 110492139B
- Authority
- CN
- China
- Prior art keywords
- end cover
- gas
- fuel cell
- liquid
- hydrogen fuel
- Prior art date
- 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.)
- Active
Links
- 239000007789 gas Substances 0.000 title claims abstract description 71
- 238000002156 mixing Methods 0.000 title claims abstract description 56
- 239000000446 fuel Substances 0.000 title claims abstract description 33
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 239000001257 hydrogen Substances 0.000 title claims abstract description 18
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 47
- 239000001301 oxygen Substances 0.000 claims abstract description 28
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 28
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000012544 monitoring process Methods 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 229910000619 316 stainless steel Inorganic materials 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 6
- 238000001914 filtration Methods 0.000 abstract description 5
- 238000013461 design Methods 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000009434 installation Methods 0.000 abstract description 2
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000010248 power generation Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04097—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04119—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
- H01M8/04126—Humidifying
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04119—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
- H01M8/04156—Arrangements 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
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Energy (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
The utility model discloses a gas mixing device for a hydrogen fuel cell, which comprises a cylindrical mixing tank formed by an upper end cover, a tank body and a lower end cover, wherein a filter for filtering mixed gas is arranged at the inner side of the upper end cover, a pressure sensor, an oxygen concentration sensor and an overpressure exhaust valve are sequentially arranged at the outer side of the upper end cover, an air inlet channel and an oxygen inlet channel are arranged on one side wall of the tank body along the tangential direction, a fuel cell stack tail gas inlet channel is arranged on the other side wall along the tangential direction, a liquid collector is arranged on the lower end cover, and a liquid level switch and an electromagnetic valve are arranged on the liquid collector. The utility model adopts a multifunctional integrated design and gas rotation mixing technology, effectively realizes the pressure and concentration monitoring, gas humidification, gas-liquid separation and gas filtration of mixed gas, and has the advantages of simple structure, low technical difficulty, convenient installation and transportation, low manufacturing and maintenance cost, suitability for large-scale production and the like.
Description
Technical Field
The utility model belongs to the technical field of fuel cells, and particularly relates to a gas mixing device for a hydrogen fuel cell.
Background
The hydrogen fuel cell is a power generation device for directly converting chemical energy existing in fuel and oxidant into electric energy through electrochemical reaction, and has the advantages of high energy conversion efficiency, high energy density, low vibration noise, zero emission and the like. Therefore, the hydrogen fuel cell is regarded as an ideal power device with cleanness and high efficiency in the 21 st century, is an important way for solving two problems of resource shortage and pollution deterioration, and has wide development and application prospect in the fields of new energy automobiles and green ships.
As a core component of a fuel cell power plant, a fuel cell stack has been demanded as an index of high power generation efficiency. At present, the main technical approach adopted by expert scholars at home and abroad is to improve a fuel cell stack body, such as bipolar plate structure optimization, membrane electrode material optimization and the like, but the requirements on professional quality, process equipment precision and material advancement of designers are higher, and the technical difficulty is higher. Based on the above, the utility model proposes to adopt a gas mixing and air supplying technology, namely, the concentration of oxygen in cathode gas supplied to the fuel cell stack is increased by mixing oxygen and air, so that the power generation efficiency of the fuel cell stack is improved.
The Chinese patent with publication number of CN109316987A, named as "gas mixing method and gas mixing system", discloses a gas mixing method and a gas mixing system, wherein a gas mixing device comprises a mixing tank and a vacuum pump, and a pressure controller is arranged on the mixing tank to realize gas receiving, mixing and pressure real-time monitoring. The Chinese patent with publication number of CN202921183U and name of automatic mixing equipment for oxygen and argon discloses automatic mixing equipment for gases, wherein a gas mixing device is a gas mixer, and an oxygen analyzer is arranged on a gas outlet pipeline of the automatic mixing equipment for monitoring the concentration of oxygen.
The gas mixing device can monitor the pressure and the concentration of the mixed gas and meet the use requirements of general users, but for the fuel cell stack with strict performance requirements of the mixed gas, the use requirements cannot be met: the fuel cell stack requires not only pressure and concentration monitoring of the cathode gas, but also strict requirements on cathode gas humidity, moisture and quality.
Disclosure of Invention
Based on the above, the utility model designs a gas mixing device for a hydrogen fuel cell, which can realize the monitoring of the pressure and concentration of air/oxygen mixed gas, the gas humidification, the gas-liquid separation and the gas filtration, and effectively improve the power generation efficiency of a fuel cell stack.
The technical scheme adopted for solving the technical problems is as follows: the utility model provides a gaseous blending device for hydrogen fuel cell, includes by upper end cover, jar body and lower extreme cover through the cylindrical blending jar that the bolt connects gradually formation, the upper end cover inboard be provided with and be used for mixing gas filterable filter, upper end cover outside has set gradually pressure sensor, oxygen concentration sensor and superpressure exhaust valve, jar body one side lateral wall be provided with air inlet duct and oxygen inlet duct along tangential direction, one side lateral wall be provided with fuel cell stack tail gas intake duct along tangential direction, the lower extreme cover on be provided with the liquid trap, the liquid trap on be provided with liquid level switch and solenoid valve.
The material of the mixing tank of the gas mixing device for the hydrogen fuel cell is 316 stainless steel.
The filter material of the gas mixing device for the hydrogen fuel cell is 316 stainless steel, the pore diameter of the filter layer is 2um, and the filter layer is connected with the mixing upper end cover through bolts.
The pressure sensor and the oxygen concentration sensor of the gas mixing device for the hydrogen fuel cell are connected with the upper end cover through threads and are arranged in the drift diameter of the filter for monitoring the pressure and the concentration of mixed gas; the overpressure emptying valve is a mechanical valve and is connected with the upper end cover through threads and used for automatically emptying the mixed gas under overpressure.
The liquid collector of the gas mixing device for the hydrogen fuel cell is made of 316 stainless steel and is connected with the lower end cover through bolts.
The liquid level switch and the electromagnetic valve of the gas mixing device for the hydrogen fuel cell are connected with the liquid collector through threads, the liquid level switch is conducted when the liquid water deposited by the liquid collector is excessive, and the electromagnetic valve is opened to discharge the liquid water.
The utility model has the beneficial effects that:
1, the utility model adopts a multifunctional integrated design, and effectively integrates the functions of mixed gas pressure and concentration monitoring, gas humidification, gas filtration and gas-liquid separation into a movable mixed tank;
2, the utility model adopts a gas rotation mixing technology to lead air, oxygen and tail gas of the fuel cell stack to enter the gas along the tangential direction of the mixing body, thereby realizing humidification, gas-liquid separation and uniform mixing of the gas in the tank;
the system has the advantages of simple structure, low technical difficulty, convenient installation and transportation, low manufacturing and maintenance cost and suitability for large-scale production.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
fig. 2 is a schematic diagram of the principles of the present utility model.
The reference numerals are as follows: 3-1-mixing tank, 1-1-upper end cover, 1-2-tank body, 1-2-1-air inlet, 1-2-2-oxygen inlet, 1-2-3-tail gas inlet, 1-3-lower end cover, 3-2-filter, 3-pressure sensor, 3-4-oxygen concentration sensor, 3-5-overpressure emptying valve, 3-6-liquid collector, 3-7-liquid level switch and 3-8-electromagnetic valve.
Detailed Description
The present utility model will be described in detail below with reference to the accompanying drawings and examples, which follow.
As shown in FIG. 1, the utility model discloses a gas mixing device for a hydrogen fuel cell, which comprises a mixing tank 3-1, a filter 3-2, a pressure sensor 3-3, an oxygen concentration sensor 3-4, an overpressure evacuation valve 3-5, a liquid collector 3-6, a liquid level switch 3-7 and an electromagnetic valve 3-8. The material of the mixing tank 3-1 is 316 stainless steel, and the mixing tank comprises an upper end cover 1-1, a tank body 1-2 and a lower end cover 1-3 which are sequentially connected through bolts, and is used for gas humidification, gas-liquid separation and uniform mixing. The side wall of one side of the tank body 1-2 is provided with an air inlet channel 1-2-1 and an oxygen inlet channel 1-2-2 along the tangential direction, the side wall of one side is provided with a fuel cell stack tail gas inlet channel 1-2-3 along the tangential direction, the filter 3-2 is made of 316 stainless steel, the micropore diameter of the filter layer is 2um, and the filter layer is connected with the upper end cover 1-1 through bolts and used for filtering mixed gas. The pressure sensor 3-3 and the oxygen concentration sensor 3-4 are connected with the upper end cover 1-1 of the mixing and filling device through threads, are arranged in the path of the filter 3-2 and are used for monitoring the pressure and concentration of the mixed gas. The overpressure evacuation valve 3-5 is a mechanical valve and is connected with the upper end cover 1-1 of the mixing tank through threads for automatically evacuating the mixed gas under overpressure. The liquid collector 3-6 is made of 316 stainless steel and is connected with the lower end cover 1-3 of the mixing tank through bolts. The liquid level switch 3-7 and the electromagnetic valve 3-8 are connected with the liquid collector 3-6 through threads, and the liquid level switch 3-7 feeds back collected signals to the electromagnetic valve 8 to drain liquid water in the liquid collector 3-6.
As shown in fig. 2, the technical principle of the present utility model will be described with reference to the structure of the present utility model as follows:
under the working condition, tail gas, air and oxygen of electrochemical reaction of a cathode of a galvanic pile enter from an air inlet channel in the tangential direction of the mixing tank 3-1, and form a cyclone under the guidance of the inner wall of the tank body 1-2, so that on one hand, the tail gas, the air and the oxygen are uniformly mixed, on the other hand, liquid water in the mixed gas generates centrifugal motion, falls on the inner wall of the tank body 1-2, flows to the bottom of the mixing tank 3-1 under the action of gravity, and gas-water separation is realized.
After the liquid water deposited on the liquid collector 3-6 at the bottom of the mixing tank 3-1 is evaporated and vaporized, the mixed gas is humidified, when the liquid water deposited on the liquid collector 3-6 is excessive, the liquid level switch 3-7 is turned on, the electromagnetic valve 3-8 is opened, and the liquid water is discharged out of the liquid collector 3-6.
The oxygen concentration sensor 3-4 arranged on the upper end cover 1-1 of the mixing and filling is used for monitoring the concentration of the mixed gas, and can feed back a collection signal to the electric valve group on the air and oxygen supply pipeline, when the oxygen concentration is high, the air inflow of the air is increased, the air inflow of the oxygen is reduced, and when the oxygen concentration is low, the air inflow is opposite.
The pressure sensor 3-3 arranged on the upper end cover 1-1 of the mixing tank is used for monitoring the pressure of the mixed gas, the overpressure evacuation valve 3-5 is used for automatically evacuating the mixed gas under overpressure, the filter 3-2 filters out impurities in the mixed gas on one hand, and the liquid water in the mixed gas is subjected to secondary water diversion on the other hand.
Finally, the high-quality mixed gas with certain pressure, humidity, moisture and oxygen concentration is supplied to the cathode of the fuel cell stack.
The above embodiments are merely illustrative of the principles of the present utility model and its effectiveness, and some practical embodiments, and variations and modifications may be made by those skilled in the art without departing from the inventive concept, which are all within the scope of the present utility model.
Claims (4)
1. A gas mixing device for a hydrogen fuel cell, characterized by: including by upper end cover (1-1), jar body (1-2) and lower end cover (1-3) through the cylindrical blending jar (3-1) that the bolt formed of connecting gradually, upper end cover (1-1) inboard be provided with be used for mixing gaseous filterable filter (3-2), upper end cover (1-1) outside has set gradually pressure sensor (3-3), oxygen concentration sensor (3-4) and superpressure evacuation valve (3-5), jar body (1-2) one side wall be provided with air inlet duct (1-2-1) and oxygen inlet duct (1-2-2) along tangential direction, one side wall be provided with tail gas inlet duct (1-2-3) along tangential direction, lower end cover (1-3) on be provided with liquid collector (3-6), liquid collector (3-6) on be provided with liquid level switch (3-7) and solenoid valve (3-8), blending jar (3-1) material be 316 stainless steel, filter (3-2) material be 316 micropore diameter, be that the micropore diameter is 316 is steel, mix end cover (1-1) through being connected with bolt.
2. The gas mixing device for the hydrogen fuel cell according to claim 1, wherein the pressure sensor (3-3) and the oxygen concentration sensor (3-4) are connected with the upper end cover (1-1) through threads and are arranged in the path of the filter (3-2) for monitoring the pressure and concentration of the mixed gas; the overpressure evacuation valve (3-5) is a mechanical valve and is connected with the upper end cover (1-1) through threads for automatically evacuating the mixed gas under overpressure.
3. The gas mixing device for the hydrogen fuel cell according to claim 1, wherein the liquid collector (3-6) is made of 316 stainless steel and is connected with the lower end cover (1-3) through bolts.
4. A gas mixing device for a hydrogen fuel cell according to claim 1, wherein the liquid level switch (3-7) and the electromagnetic valve (3-8) are connected with the liquid collector (3-6) by screw threads, the liquid level switch (3-7) is turned on when the liquid water deposited in the liquid collector (3-6) is excessive, and the electromagnetic valve (3-8) is opened to discharge the liquid water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910713990.6A CN110492139B (en) | 2019-08-02 | 2019-08-02 | Gas mixing device for hydrogen fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910713990.6A CN110492139B (en) | 2019-08-02 | 2019-08-02 | Gas mixing device for hydrogen fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110492139A CN110492139A (en) | 2019-11-22 |
| CN110492139B true CN110492139B (en) | 2024-03-12 |
Family
ID=68549275
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910713990.6A Active CN110492139B (en) | 2019-08-02 | 2019-08-02 | Gas mixing device for hydrogen fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110492139B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113719460B (en) * | 2021-08-28 | 2023-12-26 | 深圳市深信创联智能科技有限责任公司 | Special direct-driven high-speed centrifugal air compression device for low-energy-consumption hydrogen fuel cell |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2536892Y (en) * | 2002-02-10 | 2003-02-19 | 华东船舶工业学院 | Gas mixing feeder |
| JP2005310557A (en) * | 2004-04-21 | 2005-11-04 | Matsushita Electric Works Ltd | Mixer and fuel cell using it |
| CN101146598A (en) * | 2003-11-07 | 2008-03-19 | 丰田自动车株式会社 | Gas processing device |
| KR20110007843A (en) * | 2009-07-17 | 2011-01-25 | (주)퓨얼셀 파워 | Fuel cull power generation system |
| CN102035008A (en) * | 2010-11-16 | 2011-04-27 | 上海恒劲动力科技有限公司 | Fuel battery system using vessel-contained oxygen gas as oxidizer and control system thereof |
| CN203196578U (en) * | 2013-04-01 | 2013-09-18 | 广州市上腾电子科技有限公司 | Mixed gas preparation device |
| CN203955061U (en) * | 2014-07-11 | 2014-11-26 | 天津市鹏翔科技有限公司 | A kind of efficient mixture buffer system |
| CN204746001U (en) * | 2015-06-24 | 2015-11-11 | 杭州翔盛气体设备有限公司 | Deareator |
| CN106642127A (en) * | 2016-11-24 | 2017-05-10 | 兴化市紫邦燃器具科技有限公司 | Mandatory all-over three-dimensional gas mixing chamber |
| CN210349982U (en) * | 2019-08-02 | 2020-04-17 | 武汉船用电力推进装置研究所（中国船舶重工集团公司第七一二研究所） | Gas blending device for hydrogen fuel cell |
-
2019
- 2019-08-02 CN CN201910713990.6A patent/CN110492139B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2536892Y (en) * | 2002-02-10 | 2003-02-19 | 华东船舶工业学院 | Gas mixing feeder |
| CN101146598A (en) * | 2003-11-07 | 2008-03-19 | 丰田自动车株式会社 | Gas processing device |
| JP2005310557A (en) * | 2004-04-21 | 2005-11-04 | Matsushita Electric Works Ltd | Mixer and fuel cell using it |
| KR20110007843A (en) * | 2009-07-17 | 2011-01-25 | (주)퓨얼셀 파워 | Fuel cull power generation system |
| CN102035008A (en) * | 2010-11-16 | 2011-04-27 | 上海恒劲动力科技有限公司 | Fuel battery system using vessel-contained oxygen gas as oxidizer and control system thereof |
| CN203196578U (en) * | 2013-04-01 | 2013-09-18 | 广州市上腾电子科技有限公司 | Mixed gas preparation device |
| CN203955061U (en) * | 2014-07-11 | 2014-11-26 | 天津市鹏翔科技有限公司 | A kind of efficient mixture buffer system |
| CN204746001U (en) * | 2015-06-24 | 2015-11-11 | 杭州翔盛气体设备有限公司 | Deareator |
| CN106642127A (en) * | 2016-11-24 | 2017-05-10 | 兴化市紫邦燃器具科技有限公司 | Mandatory all-over three-dimensional gas mixing chamber |
| CN210349982U (en) * | 2019-08-02 | 2020-04-17 | 武汉船用电力推进装置研究所（中国船舶重工集团公司第七一二研究所） | Gas blending device for hydrogen fuel cell |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110492139A (en) | 2019-11-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110600763A (en) | Fuel cell stack gas supply system | |
| CN211062794U (en) | Fuel cell hydrogen supply and return ejector device and fuel cell system | |
| CN106898801A (en) | A kind of gas-liquid separator for direct liquid feed fuel cell system | |
| CN106374127B (en) | A kind of drop water aeration declines biological fuel cell | |
| CN107546401A (en) | A kind of bidirectional reversible fuel cell system | |
| CN110492139B (en) | Gas mixing device for hydrogen fuel cell | |
| CN109701757A (en) | A kind of gas-liquid separating method and separator for direct liquid feed fuel cell | |
| CN211530097U (en) | Gas-water separation device for anode tail gas of vertical fuel cell | |
| CN210349982U (en) | Gas blending device for hydrogen fuel cell | |
| CN110228845B (en) | Alternating-current and plug-flow type bioelectrochemical system | |
| CN114032569B (en) | High-efficiency electrolytic structure device | |
| CN209276647U (en) | It is a kind of to utilize decomposing water with solar energy device for producing hydrogen | |
| CN104716366A (en) | Gas-liquid separator for miniature fuel cell systems | |
| CN209001026U (en) | A kind of ripple flow-field plate | |
| CN115404503B (en) | Microchannel membraneless electrolytic hydrogen production device and preparation method thereof | |
| CN111584913A (en) | Vertical current reciprocal type microbial fuel cell | |
| CN217848008U (en) | Humidifying device for fuel cell | |
| CN209298250U (en) | A kind of graphite bipolar plate of fuel battery | |
| CN211530095U (en) | Centrifugal gas-water separator for anode tail gas of fuel cell | |
| CN212700920U (en) | Swirl generator for water-gas separator | |
| CN202797153U (en) | Tail gas treatment device of methanol fuel cell test system | |
| CN101644651B (en) | Device for automatically detecting and supplementing concentration of methanol solution in direct methanol fuel cells | |
| CN110943242B (en) | Porous medium water separator for fuel cell | |
| CN216778211U (en) | Steam-water separation device | |
| CN107842062A (en) | Suitable for the photovoltaic dielectric film integrated air water generator of high temperature low moisture environments |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |