CN108539229A - A kind of fuel cell pile hydrogen circulation device and method - Google Patents

A kind of fuel cell pile hydrogen circulation device and method Download PDF

Info

Publication number
CN108539229A
CN108539229A CN201810613558.5A CN201810613558A CN108539229A CN 108539229 A CN108539229 A CN 108539229A CN 201810613558 A CN201810613558 A CN 201810613558A CN 108539229 A CN108539229 A CN 108539229A
Authority
CN
China
Prior art keywords
hydrogen
pile
hydrogen gas
flow channel
humidified
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.)
Withdrawn
Application number
CN201810613558.5A
Other languages
Chinese (zh)
Inventor
周江东
陈融
张宝春
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NANTONG BING ENERGY Inc
Original Assignee
NANTONG BING ENERGY Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by NANTONG BING ENERGY Inc filed Critical NANTONG BING ENERGY Inc
Priority to CN201810613558.5A priority Critical patent/CN108539229A/en
Publication of CN108539229A publication Critical patent/CN108539229A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • 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
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • 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

Landscapes

  • 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, specifically disclose a kind of fuel cell pile hydrogen circulation device and method, pile is equipped with anode flow channel entrance and anode flow channel exports, input terminal and the anode flow channel of water collector of being humidified is exported and is connected to by hydrogen circulation line, the output end of water collector of being humidified is connected to the input terminal of hydrogen gas circulating pump by hydrogen circulation line, and the output end of hydrogen gas circulating pump is connected to anode flow channel entrance by hydrogen circulation line.The present invention can adjust humidity according to pile operating condition, it will not allow water slug runner that pile will not be allowed to enter dry mouth in high power in changed power, lesion electrode, power is caused to decline, hydrogen gas circulating system can heat air inlet when cold-starting, accelerate cold start speed, solving fuel cell water and being unevenly distributed can make pile part gradually be dried, and even make pile Problem of Failure.

Description

A kind of fuel cell pile hydrogen circulation device and method
Technical field
Fuel cell field of the present invention, specifically a kind of fuel cell pile hydrogen circulation device and method.
Background technology
Proton exchange membrane hydrogen fuel cell (PEMFC) is fuel cell one kind, when hydrogen fuel cell and external circuit are formed back Lu Shi, for anode-side hydrogen under catalyst (pt) effect, hydrogen is converted to Hydrogen Proton, and is combined to form proton hydrate with water, cloudy The oxygen (oxygen in air) of pole side forms oxonium ion under catalyst (pt) effect, under the effect of anode and cathode potential difference, hydration Hydrogen Proton orientation migrates to cathode from anode, is combined with the oxonium ion that cathode is formed and generates water, meanwhile, part water is in osmotic pressure Effect is lower to enter anode flow channel, and external circuit forms electric current.To which the chemical energy that reaction gas contains is converted directly into electric energy.
The basic unit of fuel cell pile is monocell, and multiple cells in series form pile, and monocell is by film electricity Pole, diffusion layer, deflector are constituted, and hydrogen side is anode, and oxygen side is cathode.Membrane electrode is made of proton exchange membrane and painting electrode.It is single The effective voltage of battery is very low, open-circuit voltage 1.229V, rated operational voltage range 0.55-0.75V.Usually monocell is set It is calculated as the larger laminate structure of area, area is supplied to more greatly the electric current of external circuit also bigger;Many cells in series to Sufficiently high voltage is obtained, the partition board between the anode of monocell and the cathode of another monocell is referred to as bipolar plates.It is bipolar Have the cushion rubber to seal between plate and membrane electrode, it is this by multilayer single battery group at laminate structure be pile.
As fuel cell enters practical stage, for fuel battery stability, the service life, low cost research increasingly Deeply.Wherein, service life and stability are the important indicators of estimating fuel battery maturity, and hydrogen is empty or hydrogen-oxygen fuel cell also not example Outside, there are many factor for influencing stable fuel cell operation, and the water management of membrane electrode is one of key factor.
The purpose of water management is to maintain the distributing homogeneity of water under pile different capacity, and hydrogen inlet water is more to make pile Ponding is exported, pile water blockoff is even made to fail.The water of hydrogen inlet is few, can make to damage membrane electrode into dry mouth, make pile It is unable to steady operation.In a fuel cell, water is that cathode generates, and part water can enter anode flow channel under the action of osmotic pressure, Discharge pile is recycled with hydrogen.General hydrogen gas circulating system filters out most of liquid water, only sends seldom vapor back to Hydrogen inlet, and as variation of ambient temperature recycle hydrogen is apparent non-adjustable to the humidification variation of hydrogen inlet.
For the deficiency of existing fuel cell, it is necessary to develop a kind of low consumable, highly reliable Fuel Cell Humidity control Mode processed makes the device and method of the continual and steady efficient operation of fuel cell.
Invention content
The object of the present invention is to provide a kind of fuel cell pile hydrogen circulation device and methods, are raising when system designs Pile generating efficiency can reduce the flow-rate ratio of reaction gas as possible, and many important environmental requirement fuel availabilitys having are more than 99%, it reduces air (oxygen) for hydrogen air (or oxygen) fuel cell and humidifies degree, improve hydrogen fuel hydrogen utilization ratio, carry The stability of high battery and service life etc. are designed exploitation.
To solve above-mentioned hydrogen cycle, water blockoff and the uneven technical problem of pile water distribution, the present invention provides a kind of combustions Expect battery stack hydrogen circulation device, including pile, hydrogen gas valve, hydrogen circulation line, hydrogen gas circulating pump, temperature sensing Device, can be humidified water collector and drain valve;The pile is equipped with anode flow channel entrance and anode flow channel exports, and described be humidified is catchmented The input terminal of device is exported with the anode flow channel and is connected to by hydrogen circulation line, the output end of the water collector that is humidified and institute The input terminal for stating hydrogen gas circulating pump is connected to by hydrogen circulation line, the output end of the hydrogen gas circulating pump and the anode flow channel Entrance is connected to by hydrogen circulation line, and the temperature sensor is located at the hydrogen gas circulating pump output end and the anode flow channel On hydrogen circulation line between entrance, the drain valve is connected to by drainage pipeline with the water collector that is humidified, the hydrogen Gas intake valve is connected to the cycle of the hydrogen between the temperature sensor and the hydrogen gas circulating pump output end by air inlet pipeline On pipeline.
Further, heating tape is equipped in the hydrogen circulation line.
Further, the hydrogen gas valve and drain valve are solenoid valve.
Further, described be humidified in water collector is equipped with heater.
The present invention also provides a kind of fuel cell pile hydrogen gas circulating methods, include the following steps:Open hydrogen gas Valve opens simultaneously drain valve, empties the air in pile, starts pile, after pile starts, hydrogen can humidification cycle system start Hydrogen circulation line is heated in work, primer liner heating tape, and opening hydrogen gas valve makes hydrogen pass through temperature sensor Enter pile anode flow channel from the anode flow channel entrance of pile after detection, the liquid water in pile anode flow channel is said with anode stream Mouthful wet hydrogen of the discharge with certain humidity is exported from anode flow channel to be discharged, and the wet hydrogen and liquid water of discharge are into the collection that can be humidified Hydrophone, then by can be humidified water collector by wet hydrogen and aqueous water from, the liquid water after separation can be humidified in water collector, point Hydrogen circulation line of the wet hydrogen by heating from after enters hydrogen gas circulating pump, then is exported by hydrogen gas circulating pump, wet hydrogen It is discharged into the mixing of the hydrogen in hydrogen circulation line with hydrogen gas valve, mixed hydrogen is after temperature sensor detects from electricity The anode flow channel entrance of heap enters pile anode flow channel;
When temperature sensor detects that the hydrogen in hydrogen circulation line is less than 30 DEG C into the temperature before heap or pile exports Power increases, and when hydrogen gas humidity reduces, starts the liquid water heating that the collection water heater pair that can be humidified can be humidified in water collector Become vapor, hydrogen circulation line of the vapor mixing wet hydrogen by heating enters hydrogen gas circulating pump, then is followed by hydrogen Ring pump output, wet hydrogen and hydrogen gas valve are discharged into the mixing of the hydrogen in hydrogen circulation line, and mixed hydrogen is through excess temperature Enter pile anode flow channel from the anode flow channel entrance of pile after sensor detection;
When temperature sensor detects that the hydrogen in hydrogen circulation line is higher than 50 DEG C into the temperature before heap or pile exports Power reduces, and when hydrogen gas humidity increases, closing, which can be humidified, collects water heater, opens drain valve, can be humidified in water collector Hydrogen gas circulating system is discharged by discharge pipe line in excessive water and impurity gas, and the wet hydrogen of the water collector that can be humidified separation is by heating Hydrogen circulation line enter hydrogen gas circulating pump, then exported by hydrogen gas circulating pump, wet hydrogen and hydrogen gas valve are discharged into hydrogen Hydrogen mixing in circulation line, mixed hydrogen enter after temperature sensor detects from the anode flow channel entrance of pile Pile anode flow channel.
The beneficial effects of the invention are as follows:The adjustable humidification cycle device and method of fuel cell pile hydrogen of the present invention, passes through Pile operating condition adjusts humidity, will not allow water slug runner that will not allow pile entrance in high power in low-power in this way Dry, lesion electrode causes power to decline, liquid water can be effectively prevented in conventional operation and enters pile, so as to cause Liquid water embolism, influence to generate electricity, hydrogen gas circulating system can heat air inlet when cold-starting, accelerate cold start-up speed Degree.
Description of the drawings
It, below will be to required in embodiment or description of the prior art in order to illustrate more clearly of technical scheme of the present invention The attached drawing used is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the invention, right For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings Its attached drawing.
Fig. 1 is the structural schematic diagram of fuel cell pile hydrogen circulation device of the present invention.
In figure:1, pile;2, hydrogen gas valve;3, hydrogen circulation line;4, hydrogen gas circulating pump;5, temperature sensor;6、 Can be humidified water collector;7, drain valve;8, anode flow channel entrance;9, anode flow channel exports;10, air inlet pipeline;11, discharge pipe line.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on Embodiment in the present invention, those of ordinary skill in the art obtained under the premise of not making creative work it is all its His embodiment, shall fall within the protection scope of the present invention.
In the specific embodiment of the invention, as shown in Figure 1, a kind of fuel cell pile hydrogen circulation device is specifically disclosed, Including pile 1, hydrogen gas valve 2, hydrogen circulation line 3, hydrogen gas circulating pump 4, temperature sensor 5, can be humidified water collector 6 and row Water valve 7;Be equipped with anode flow channel entrance 8 and anode flow channel outlet 9 in the pile 1, the input terminal of the water collector 6 that is humidified with The anode flow channel outlet 9 is connected to by hydrogen circulation line 3, and the output end of the water collector 6 that is humidified is followed with the hydrogen The input terminal of ring pump 4 is connected to by hydrogen circulation line 3, the output end of the hydrogen gas circulating pump 4 and the anode flow channel entrance 8 It is connected to by hydrogen circulation line 3, the temperature sensor 5 is located at 4 output end of the hydrogen gas circulating pump and the anode flow channel On hydrogen circulation line 3 between entrance 8, the drain valve 7 is connected to by drainage pipeline 11 with the water collector 6 that is humidified, The hydrogen gas valve 2 is connected to by air inlet pipeline 10 between 4 output end of the temperature sensor 5 and the hydrogen gas circulating pump Hydrogen circulation line 3 on, heating tape is equipped in hydrogen circulation line 3, hydrogen gas valve 2 and drain valve 7 are solenoid valve, can be increased Heater is equipped in wet water collector 6.
The present invention also provides a kind of fuel cell pile hydrogen gas circulating methods, include the following steps:Open hydrogen gas Valve 2 opens simultaneously drain valve 7, empties the air in pile 1, starts pile 1, after pile 1 starts, hydrogen can humidification cycle system It starts to work, hydrogen circulation line 3 is heated in primer liner heating tape, and opening hydrogen gas valve 2 makes hydrogen through excess temperature Sensor 5 from the anode flow channel entrance 8 of pile 1 enters pile anode flow channel after detecting, the liquid water in pile anode flow channel with 9 wet hydrogen of the discharge with certain humidity of anode flow channel outlet is discharged from anode flow channel outlet 9, the wet hydrogen and liquid water of discharge Into the water collector 6 that can be humidified, then by the water collector 6 that can be humidified by wet hydrogen and aqueous water from, liquid water after separation can It is humidified in water collector 6, hydrogen circulation line 3 of the wet hydrogen after separation by heating enters hydrogen gas circulating pump 4, then passes through hydrogen Circulating pump 4 exports, and wet hydrogen and hydrogen gas valve 2 are discharged into the mixing of the hydrogen in hydrogen circulation line 3, and mixed hydrogen passes through Enter 1 anode flow channel of pile from the anode flow channel entrance 8 of pile 1 after the detection of temperature sensor 5;
When temperature sensor 5 detects that the hydrogen in hydrogen circulation line 3 is less than 30 DEG C into the temperature before heap or pile 1 is defeated Go out power increase, when hydrogen gas humidity reduces, starts the liquid water that collection water heater pair can be humidified in water collector 6 that can be humidified and add At vapor, hydrogen circulation pipe 3 tunnel of the vapor mixing wet hydrogen by heating enters hydrogen gas circulating pump 4, then passes through hydrogen for thermal change Gas circulating pump 4 exports, and wet hydrogen and hydrogen gas valve 2 are discharged into the mixing of the hydrogen in hydrogen circulation line 3, mixed hydrogen warp Enter 1 anode flow channel of pile from the anode flow channel entrance 8 of pile 1 after the detection of excess temperature sensor 5;
When temperature sensor 5 detects that the hydrogen in hydrogen circulation line 3 is higher than 50 DEG C into the temperature before heap or pile 1 is defeated Go out power reduction, when hydrogen gas humidity increases, closing, which can be humidified, collects water heater, opens drain valve 7, can be humidified water collector Hydrogen gas circulating system, the wet hydrogen warp of the water collector 6 that can be humidified separation is discharged by discharge pipe line 11 in excessive water and impurity gas in 6 The hydrogen circulation line 3 for crossing heating enters hydrogen gas circulating pump 4, then is exported by hydrogen gas circulating pump 4, wet hydrogen and hydrogen gas valve 2 are discharged into the hydrogen mixing in hydrogen circulation line 3, and mixed hydrogen is after the detection of temperature sensor 5 from the anode of pile 1 Flow channel entry point 8 enters 1 anode flow channel of pile.
The cycle humidity of hydrogen realizes that the hydrogen temperature of cycle is heated by adjusting by adjusting the hydrogen temperature of cycle The power of band realizes, when the temperature in hydrogen gas circulating system increases less than 30 DEG C of pipelines or pile output power, hydrogen gas When humidity reduces, heating tape power reduces, humidity of the raising hydrogen into heap;When the temperature in hydrogen gas circulating system higher than 50 DEG C or Pile output power reduces, and when hydrogen gas humidity increases, pipeline heating band power increases, and reduction hydrogen, can into the humidity of heap To reach the adjustable humidity cycle of hydrogen, hydrogen is humidified, maintains the balance of water in pile, plays stable pile work Purpose, hydrogen gas circulating system can heat air inlet when cold-starting, accelerate cold start speed.
With the variation of pile output power, to adjust the rate of recovery and hydrogen gas circulating pump flow of recycle hydrogen, the hydrogen of consumption Tolerance is directly proportional with pile output power, and the bigger hydrogen into pile of pile output power is more, and the yield of hydrogen is just It is bigger, it is determined according to pile output power, it is general to recycle the 25%-40% that flow is hydrogen gas consumption, many important rings having Border requires fuel availability to be more than 99%, is that system designs using fuel cell pile hydrogen circulating technology in this case Optimal selection.
Hydrogen humidity in hydrogen gas circulating system is adjusted by adjusting the hydrogen temperature in circulation line, hydrogen cycle Hydrogen temperature in pipeline is realized by adjusting the power of pipeline heating tape, can be reached hydrogen automatic adjustable humidity and be returned It receives, the hydrogen in hydrogen circulation line is humidified, maintain the balance of water in pile, play the purpose of stable pile work.
Although the section Example of the present invention was illustrated and described, will be apparent that the present invention is not limited to this, this The technical staff in field is appreciated that:These embodiments can be carried out without departing from the principle and spirit of the present invention A variety of change, modification, replacement and modification, the scope of the present invention are limited by claim and its equivalent.

Claims (5)

1. a kind of fuel cell pile hydrogen circulation device, which is characterized in that including pile (1), hydrogen gas valve (2), hydrogen Circulation line (3), hydrogen gas circulating pump (4), temperature sensor (5), can be humidified water collector (6) and drain valve (7);The pile (1) anode flow channel entrance (8) and anode flow channel outlet (9), input terminal and the sun of the water collector that is humidified (6) are equipped in Pole runner exit (9) is connected to by hydrogen circulation line (3), and the output end of the water collector that is humidified (6) is followed with the hydrogen The input terminal that ring pumps (4) is connected to by hydrogen circulation line (3), output end and the anode stream of the hydrogen gas circulating pump (4) Road entrance (8) is connected to by hydrogen circulation line (3), and the temperature sensor (5) is located at the hydrogen gas circulating pump (4) output end On hydrogen circulation line (3) between the anode flow channel entrance (8), the drain valve (7) by drainage pipeline (11) with The water collector that is humidified (6) connection, the hydrogen gas valve (2) are connected to the temperature sensor by air inlet pipeline (10) (5) on the hydrogen circulation line (3) between the hydrogen gas circulating pump (4) output end.
2. a kind of fuel cell pile hydrogen circulation device according to claim 1, it is characterised in that:The hydrogen cycle Heating tape is equipped in pipeline (3).
3. a kind of fuel cell pile hydrogen circulation device according to claim 1, it is characterised in that:The hydrogen gas Valve (2) and drain valve (7) are solenoid valve.
4. a kind of fuel cell pile hydrogen circulation device according to claim 1, it is characterised in that:The collection that is humidified Heater is equipped in hydrophone (6).
5. a kind of fuel cell pile hydrogen gas circulating method, which is characterized in that described in any one of claim 1-4 A kind of fuel cell pile hydrogen circulation device, includes the following steps:
It opens hydrogen gas valve and opens simultaneously drain valve, empty the air in pile, start pile, close drain valve, pile opens After dynamic, hydrogen can humidification cycle system starts, primer liner heating tape heats hydrogen circulation line, opens hydrogen Intake valve makes hydrogen enter pile anode flow channel, pile anode from the anode flow channel entrance of pile after temperature sensor detects Liquid water in runner, which is exported with wet hydrogen from anode flow channel, to be discharged, and the wet hydrogen and liquid water of discharge catchment into that can be humidified Device, then by the water collector that can be humidified by wet hydrogen and aqueous water from the liquid water after separation can be humidified in water collector, separation The hydrogen circulation line of rear wet hydrogen by heating enters hydrogen gas circulating pump, then is exported by hydrogen gas circulating pump, wet hydrogen and Hydrogen gas valve is discharged into the mixing of the hydrogen in hydrogen circulation line, and mixed hydrogen is after temperature sensor detects from pile Anode flow channel entrance enter pile anode flow channel;
When temperature sensor detects that the hydrogen in hydrogen circulation line is less than 30 DEG C or pile output power into the temperature before heap Increase, when hydrogen gas humidity reduces, starts the liquid water heating that the collection water heater pair that can be humidified can be humidified in water collector and become Vapor, hydrogen circulation line of the vapor mixing wet hydrogen by heating enters hydrogen gas circulating pump, then passes through hydrogen gas circulating pump Output, wet hydrogen and hydrogen gas valve are discharged into the mixing of the hydrogen in hydrogen circulation line, and mixed hydrogen passes through temperature sensing Enter pile anode flow channel from the anode flow channel entrance of pile after device detection;
When temperature sensor detects that the hydrogen in hydrogen circulation line is higher than 50 DEG C or pile output power into the temperature before heap It reduces, when hydrogen gas humidity increases, closing, which can be humidified, collects water heater, opens drain valve, can be humidified in water collector excessive Water and impurity gas pass through discharge pipe line be discharged hydrogen gas circulating system, the water collector that can be humidified separation wet hydrogen by heating hydrogen Gas circulation line enters hydrogen gas circulating pump, then is exported by hydrogen gas circulating pump, and wet hydrogen and hydrogen gas valve are discharged into hydrogen cycle Hydrogen mixing in pipeline, mixed hydrogen enter pile after temperature sensor detects from the anode flow channel entrance of pile Anode flow channel.
CN201810613558.5A 2018-06-14 2018-06-14 A kind of fuel cell pile hydrogen circulation device and method Withdrawn CN108539229A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810613558.5A CN108539229A (en) 2018-06-14 2018-06-14 A kind of fuel cell pile hydrogen circulation device and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810613558.5A CN108539229A (en) 2018-06-14 2018-06-14 A kind of fuel cell pile hydrogen circulation device and method

Publications (1)

Publication Number Publication Date
CN108539229A true CN108539229A (en) 2018-09-14

Family

ID=63470946

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810613558.5A Withdrawn CN108539229A (en) 2018-06-14 2018-06-14 A kind of fuel cell pile hydrogen circulation device and method

Country Status (1)

Country Link
CN (1) CN108539229A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110429300A (en) * 2019-08-07 2019-11-08 上海捷氢科技有限公司 Starting method, starter and the fuel cell system of hydrogen gas circulating pump
CN110808388A (en) * 2019-11-13 2020-02-18 武汉理工大学 Self-humidifying fuel cell stack lossless starting system and method
WO2020173168A1 (en) * 2019-02-28 2020-09-03 中山大洋电机股份有限公司 Hydrogen circulation device for fuel cell and fuel cell to which same is applied
CN111834653A (en) * 2020-06-05 2020-10-27 湖北德普电气股份有限公司 Hydrogen circulating device and method for fuel cell stack
CN115020759A (en) * 2021-03-05 2022-09-06 郑州宇通客车股份有限公司 Fuel cell anode water management control system and method
CN116130707A (en) * 2022-12-28 2023-05-16 上海氢晨新能源科技有限公司 Control method and device of fuel cell system and fuel cell system
WO2024060797A1 (en) * 2022-09-23 2024-03-28 中国第一汽车股份有限公司 Fuel cell, and cell stack humidity control apparatus and method therefor

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020173168A1 (en) * 2019-02-28 2020-09-03 中山大洋电机股份有限公司 Hydrogen circulation device for fuel cell and fuel cell to which same is applied
CN110429300A (en) * 2019-08-07 2019-11-08 上海捷氢科技有限公司 Starting method, starter and the fuel cell system of hydrogen gas circulating pump
CN110808388A (en) * 2019-11-13 2020-02-18 武汉理工大学 Self-humidifying fuel cell stack lossless starting system and method
CN110808388B (en) * 2019-11-13 2022-08-16 武汉理工大学 Self-humidifying fuel cell stack lossless starting system and method
CN111834653A (en) * 2020-06-05 2020-10-27 湖北德普电气股份有限公司 Hydrogen circulating device and method for fuel cell stack
CN115020759A (en) * 2021-03-05 2022-09-06 郑州宇通客车股份有限公司 Fuel cell anode water management control system and method
CN115020759B (en) * 2021-03-05 2023-10-03 宇通客车股份有限公司 Anode water management control system and method for fuel cell
WO2024060797A1 (en) * 2022-09-23 2024-03-28 中国第一汽车股份有限公司 Fuel cell, and cell stack humidity control apparatus and method therefor
CN116130707A (en) * 2022-12-28 2023-05-16 上海氢晨新能源科技有限公司 Control method and device of fuel cell system and fuel cell system
CN116130707B (en) * 2022-12-28 2024-01-12 上海氢晨新能源科技有限公司 Control method of fuel cell system apparatus and fuel cell system

Similar Documents

Publication Publication Date Title
CN108539229A (en) A kind of fuel cell pile hydrogen circulation device and method
CN110010932B (en) Vehicle-mounted fuel cell water management system and method
CN104409750B (en) A kind of fuel cell tail gas blood circulation
CN101023547B (en) Control of the polymer humidifying membrane of a fuel cell
US10522855B2 (en) Method for creating an oxygen depleted gas in a fuel cell system
CN105742673B (en) The method of the operating of fuel cell system and control fuel cell
CN109216734B (en) Auxiliary system for facilitating humidification and low-temperature start of fuel cell
CN105186016A (en) Electrically controlled hydrogen-spraying pressure regulating device of fuel cell system
CN108832157B (en) Hydrogen recovery device for proton exchange membrane fuel cell
CN209357839U (en) A kind of bubble type humidifier and fuel cell pile system using fuel cell pile waste heat auxiliary humidification
CN112216853A (en) Fuel cell system and humidity control method thereof
CN208489292U (en) A kind of fuel cell pile hydrogen circulation device
KR20090091388A (en) Evaporative cooling type fuel cell system and stack cooling method for the same
CA2389197C (en) Fuel cell and method of operating same
CN208797107U (en) Facilitate the auxiliary system of fuel cell humidifying and cold-starting
JP2011029158A (en) Fuel cell system
CN114068997A (en) High-efficiency energy-saving fuel cell stack test system
CN115020755B (en) Fuel cell system and humidifying method thereof
CN106129436A (en) A kind of compact type intelligent humidification system for fuel cell and air-humidification method thereof
CN209691856U (en) A kind of on-vehicle fuel water management system
JP5287184B2 (en) Fuel cell system
KR101134475B1 (en) Method for controlling fuel cell in low temperature
JP2002246059A (en) Fuel cell system
CN212725389U (en) Humidification system for fuel cell
CN207977405U (en) One proton exchanging film fuel battery air humidifying device

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
WW01 Invention patent application withdrawn after publication

Application publication date: 20180914

WW01 Invention patent application withdrawn after publication