CN104733748B - Medium-high-temperature fuel cell integrated operation system - Google Patents

Medium-high-temperature fuel cell integrated operation system Download PDF

Info

Publication number
CN104733748B
CN104733748B CN201310723448.1A CN201310723448A CN104733748B CN 104733748 B CN104733748 B CN 104733748B CN 201310723448 A CN201310723448 A CN 201310723448A CN 104733748 B CN104733748 B CN 104733748B
Authority
CN
China
Prior art keywords
fuel cell
hydrogen
air
coolant
cooling fluid
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
Application number
CN201310723448.1A
Other languages
Chinese (zh)
Other versions
CN104733748A (en
Inventor
胡里清
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.)
Shanghai Shenli Technology Co Ltd
Original Assignee
Shanghai Shen Li High Tech Co Ltd
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 Shanghai Shen Li High Tech Co Ltd filed Critical Shanghai Shen Li High Tech Co Ltd
Priority to CN201310723448.1A priority Critical patent/CN104733748B/en
Publication of CN104733748A publication Critical patent/CN104733748A/en
Application granted granted Critical
Publication of CN104733748B publication Critical patent/CN104733748B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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

Abstract

The invention relates to a medium-high-temperature fuel cell integrated operation system. The medium-high-temperature fuel cell integrated operation system comprises a fuel cell pile, a hydrogen supply and circulating system, an air supply and circulating system, a cooling fluid circulating system, a heat exchanger and a cooling fluid circulating loop, wherein the hydrogen supply and circulating system, the air supply and circulating system and the cooling fluid circulating system are connected to the fuel cell pile; the heat exchanger is used for preheating hydrogen and air, the cooling fluid circulating loop is used for controlling the flow of the cooling fluid, the hydrogen flowing out of a pressure stabilizing valve enters the fuel cell pile by virtue of an injection pump after being subjected to heat exchanged with the heat exchanger, the air flowing out of a fan enters the fuel cell pile after being subjected to heat exchanged with the heat exchanger, and hot air discharged from an air outlet of the fuel cell pile is returned to the heat exchanger; the cooling fluid circulating loop comprises two electromagnetic control valves which are respectively connected to a cooling fluid circulating pump and a cooling fluid heat radiator and connected to a cooling fluid storage box by virtue of a circulating pipe, and all or partial cooling fluid does not enter the fuel cell pile by controlling one or two electromagnetic control valves. Compared with the prior art, the medium-high-temperature fuel cell integrated operation system has the advantages that a medium-high-temperature fuel cell is stable to operate and high in efficiency.

Description

A kind of high temperature fuel cell integrated operation system
Technical field
The present invention relates to a kind of technical field of new energies, more particularly, to a kind of high temperature fuel cell integrated operation system System.
Background technology
Proton Exchange Membrane Fuel Cells technology is the topmost key technology of 21 century human use's Hydrogen Energy.Many countries The attention and support energetically of height are all given to Proton Exchange Membrane Fuel Cells technology industrialization, and achieves many essence The progress of property.It is contemplated that, comprehensive industrialization of the technology will produce significant impact to future world energy supply and general layout. In modern society's life and economic construction, supply of electric power and the importance for ensureing are more and more important, while to improving power generation With service efficiency and it is eco-friendly require degree improve constantly.The close user of distributed power generation, reduces electric power remote conveying Send, increasingly paid attention to by various countries according to the advantage that need for electricity is adjusted flexibly.
According to the running temperature of PEM, Proton Exchange Membrane Fuel Cells (PEMFC) can be divided into low temperature and high temperature Two types.The running temperature of low-temperature protonic exchange film fuel battery is generally not more than 90 DEG C, with starting fast, power density High, lightweight, small volume advantage, it is very high to the hydrogen purity requirement as fuel, the renewable energy such as suitable and solar energy Source is connected, and unstable renewable energy conversion is stable electric energy by the high-purity hydrogen produced using electrolysis water;High temperature The running temperature of Proton Exchange Membrane Fuel Cells is at 100 DEG C to 200 DEG C, although compare low-temperature protonic exchange film fuel battery (work Make 90 DEG C of temperature <) toggle speed slightly slow (needing preheating), power density it is slightly lower, but high temperature pem fuel is electric There is very strong CO tolerance catalysts ability in pond (operating temperature 100-200 DEG C), be especially suitable for by natural gas, piped gas, methyl alcohol, third The obtained hydrogen of the various ways such as alkane, even rubbish landfill gas and biological energy source reformation, greatly reduces fuel cell power generation The use threshold of technology, and the high temperature due to high-temperature fuel cell operation with more than 100 DEG C, pile generates water and all vaporizes, Fuel cell pack inner flow passage water blockoff is not resulted in, the reliability of fuel cell is greatly improved, and service life compares low temp fuel Battery is higher by more than 10 times.Additionally, the high temperature that the operation of high temperature Proton Exchange Membrane Fuel Cells is produced is easier to be recycled, It is integrated into cogeneration system (CHP) and further improves its capacity usage ratio.High temperature Proton Exchange Membrane Fuel Cells has fortune The advantages of row stability height, simple system, life-span length, its application is very wide, from small-sized resident's home terminal cogeneration, To building, the distributed power generation of cell, large-scale center power station.
High temperature proton exchange film fuel cell technology is as Solid-State proton exchange membrane used in fuel cell as electrolyte One kind, the key property of its electrolyte, the basic structure of membrane electrode (membrane electrode assembly MEA) and The working method of fuel cell is similar with low-temperature protonic exchange film fuel battery (90 DEG C of operating temperature <):Electrolyte is equally matter Conductor, the insulator of electronics of son, and have low-down gas permeability;Membrane electrode MEA is equally its core component, membrane electrode With elementary cell-fuel-cell single-cell that the bipolar plates of its both sides constitute fuel cell;The basic structure of membrane electrode is also Middle PEM, film both sides are respectively attached gas diffusion layers outside negative electrode and anode electrocatalyst, anode and cathode elctro-catalyst;Work Make process, through the gas diffusion layers for having hole to catalyst layer, the hydrogen side of fuel cell is anode to hydrogen, and catalyst makes hydrogen Gas is separated into proton and electronics, and proton reaches negative electrode (i.e. oxygen side) by electrolyte, and electronics flows through an external circuit and arrives Up to negative electrode, in negative electrode proton, electronics and oxygen reaction water is generated.
One typical battery stack is generally included:(1) the water conservancy diversion import of fuel and oxidant gas and flow-guiding channel, by fuel (such as hydrogen, methyl alcohol or by methyl alcohol, natural gas, gasoline Jing after reforming the hydrogen-rich gas that obtains) and oxidant (mainly oxygen or Air) it is uniformly distributed in the guiding gutter of each anode, cathode plane;(2) import and export of cooling fluid (such as water) are led to water conservancy diversion Road, cooling fluid is evenly distributed in each battery pack inner cooling channel, by hydrogen, oxygen electrochemistry exothermic reaction in fuel cell The heat absorption of generation and taking out of after battery pack is radiated;(3) fuel and the outlet of oxidant gas and corresponding flow-guiding channel, Fuel gas, when discharging, can carry out liquid, the water of steam state generated in fuel cell with oxidant gas.Generally, will be all Fuel, oxidant, the import and export of cooling fluid are all opened on an end plate of fuel cell unit or on two end plates.
High temperature fuel cell, running temperature is 100-200 DEG C, and cold air or hydrogen enters pile, to power generation performance Fluctuation can be produced, generating efficiency is affected, and high temperature fuel cell is to need external power supply to produce heat to make pile temperature in startup Degree reaches more than 100 DEG C, can startup optimization.
The content of the invention
The purpose of the present invention is exactly the defect in order to overcome above-mentioned prior art to exist and provides a kind of convenient startup and transport The stable high temperature fuel cell integrated operation system of row.
The purpose of the present invention can be achieved through the following technical solutions:A kind of high temperature fuel cell integrated operation system System, including fuel cell pack, and it is connected to the supply of the hydrogen on fuel cell pack and the circulatory system, air supply and cyclic system The supply of system and cooling fluid circulation system, wherein hydrogen includes hydrogen gas tank, pressure-reducing valve, pressure maintaining valve, jet pump, vapour with the circulatory system Separator, described hydrogen gas tank passes sequentially through the hydrogen inlet that pressure-reducing valve, pressure maintaining valve, jet pump are connected to fuel cell pack, The hydrogen outlet connection steam-water separator of fuel cell pack, the gas vent connection jet pump of steam-water separator;Described air Supply includes filter, blower fan with the circulatory system, and the entrance connection filter of blower fan, the air of outlet connection fuel cell pack enters Mouthful;Described cooling fluid circulation system includes coolant recirculation pump, coolant storage tank, cooling water radiator, described cooling Liquid storage tank is sequentially connected the coolant inlet of coolant recirculation pump, cooling water radiator, fuel cell pack, fuel cell pack it is cold But liquid outlet connects coolant storage tank, it is characterised in that also include the heat exchanger preheated to hydrogen and air, and control The coolant closed circuit of coolant rate, the hydrogen flowed out from pressure maintaining valve is entered after heat exchanger heat exchange by jet pump Fuel cell pack, the air flowed out from blower fan enters fuel cell pack, the air outlet slit of fuel cell pack Jing after heat exchanger heat exchange The hot-air of discharge returns heat exchanger;Described coolant closed circuit includes two solenoid electric valves and a circulation line, The circulation line connection coolant recirculation pump and coolant storage tank, a magnetic valve a in two described solenoid electric valves sets Put on the main pipeline of cooling fluid incoming fuel battery pile, another magnetic valve b is arranged on circulation pipe, by control wherein One or two solenoid electric valves make all or part of not even incoming fuel battery pile of cooling liquid.
Heating tube, one or more hydrogen flow-path tube, one or more air stream deferent are provided with described heat exchanger, are changed Hot device bottom is provided with air intake, and top is provided with air outlet and exhaust-valve;Described hydrogen flow-path tube two ends connect respectively Connecting fan and fuel cell pack are distinguished in pressure maintaining valve and jet pump, described air stream deferent two ends, and described heating tube is external Power supply, preheats to hydrogen and air, while reclaiming the heat of the air flowed out from fuel cell pack.
Described heating tube includes being provided with 1~20, and the power of every heating tube is 0.1~500w.
Described heating tube is quartz glass tube or aluminum fin-stock cage walls or copper clad pipe.
Temperature probe T 1 is provided with the air outlet slit of described fuel cell pack, cooling fluid exit is provided with temperature spy Survey device T2.
Described two solenoid electric valves connection controller, controller connection temperature probe T 1 and temperature probe T 2, When the temperature of the detection of temperature probe T 1 is less than 100 DEG C, a small amount of air and hydrogen or electric without air or hydrogen incoming fuel Chi Dui, closes magnetic valve a, opens magnetic valve b, and coolant all returns coolant storage tank;When the temperature of temperature probe T 1 it is big In 100 DEG C, when the temperature of temperature probe T 2 is close 100 DEG C, magnetic valve a and magnetic valve b opens and controls coolant portion simultaneously Divide and coolant storage tank is returned by circulation line, be partially into fuel cell pack, the coolant control of incoming fuel battery pile exists The 1~20% of coolant total flow;When the temperature of temperature probe T 2 is more than 120 DEG C, hydrogen, air normally enter fuel electricity Chi Dui, magnetic valve a standard-sized sheets, magnetic valve b is closed, and coolant fully enters fuel cell pack, and by cooling water radiator control The temperature of incoming fuel battery pile.
Two described solenoid electric valves can also be replaced by a triple valve.
Compared with prior art, the present invention has advantages below:Heat exchanger is set before fuel cell pack, is on the one hand passed through Hydrogen and air preheat to suitable with fuel cell stack operation temperature, to heat fuel cell pack predetermined startup are reached by heat exchanger Temperature (100 DEG C of >), on the other hand reclaims the temperature of the high-temperature gas discharged from fuel cell pack air outlet slit, realizes heat Recycle, in case cold air incoming fuel battery pile causes fuel cell stack operation unstable.Simultaneously the present invention is provided with cold But the loop control loop of liquid so as to which, at the fuel cell stack operation initial stage, a small amount of cooling fluid enters pile, when fuel electricity Fuel cell pack by coolant inlet standard-sized sheet, is being fully entered when Chi Dui normally runs, energy waste is being reduced.
Description of the drawings
Fig. 1 is the schematic diagram of the present invention.
Specific embodiment
Below in conjunction with the accompanying drawings the present invention is described in detail with specific embodiment.
Embodiment 1
As shown in figure 1, a kind of 10kw high temperatures fuel cell integrated operation system, including fuel cell pack 5, its size is about 105mm × 400mm × 700mm, and the hydrogen supply being connected on fuel cell pack with the circulatory system, air supply and follow Loop systems and cooling fluid circulation system, wherein hydrogen supply with the circulatory system including hydrogen gas tank 1, pressure-reducing valve 2, pressure maintaining valve 3, draw Penetrate pump 4, steam-water separator 6, described hydrogen gas tank 1 pass sequentially through pressure-reducing valve 2, pressure maintaining valve 3 (by pressure stability 0.1~ 1bar), jet pump 4 is connected to the hydrogen inlet of fuel cell pack 5, the hydrogen outlet connection steam-water separator of fuel cell pack 5 6, the gas vent connection jet pump 4 of steam-water separator 6, steam-water separator 6 is also connected with exhaust-valve 7, and it is single that hydrogen container 1 is also connected with band To the hydrogen charging port 9 of valve 8;Described air supply includes filter 10, blower fan 11 with the circulatory system, and the entrance of blower fan 11 connected Filter 10, the air intlet of outlet connection fuel cell pack 5;Described cooling fluid circulation system includes coolant recirculation pump 13rd, coolant storage tank 12, cooling water radiator 14, described coolant storage tank 12 is sequentially connected coolant recirculation pump 13, cooling The coolant inlet of liquid radiator 14, fuel cell pack 5, the cooling liquid outlet connection coolant storage tank 12 of fuel cell pack 5;
Described system also includes the heat exchanger 15 preheated to hydrogen and air, and controls the cold of coolant rate But liquid closed circuit, is provided with 152, two conjunctions of hydrogen flow-path tube that heating tube 151, two unites two into one in described heat exchanger 15 Two is one air stream deferent 153, and exchanger base is provided with air intake, and top is provided with air outlet and exhaust-valve 154;Institute The hydrogen flow-path tube two ends stated connect respectively pressure maintaining valve 3 and jet pump 4, described air stream deferent two ends difference connecting fan 11 With fuel cell pack 5, the described external power supply of heating tube 151, from pressure maintaining valve 3 flow out hydrogen through heat exchanger heat exchange after, lead to The incoming fuel battery pile 5 of jet pump 4 is crossed, the air flowed out from blower fan 11 enters fuel cell pack 5, combustion Jing after the heat exchange of heat exchanger 15 The hot-air that the air outlet slit of material battery pile 5 is discharged returns heat exchanger;Described heating tube includes being provided with 3, every heating tube Power be 200w, hydrogen and air are preheated, at the same reclaim from fuel cell pack flow out air heat.Described Heating tube is quartz glass tube or aluminum fin-stock cage walls or copper clad pipe.
Described coolant closed circuit includes two magnetic valves:Magnetic valve a18, magnetic valve b19, magnetic valve a18 difference Connection coolant recirculation pump 13 and cooling water radiator 14, magnetic valve b19 is arranged on circulation pipe, and circulation pipe two ends connect respectively Coolant recirculation pump 13 and coolant storage tank 12, and it is provided with magnetic valve 20 in the bottom of coolant storage tank 12.
Temperature probe T is provided with the air outlet slit of described fuel cell pack 5116, cooling fluid exit is provided with temperature Degree detector T217。
Magnetic valve a18, magnetic valve b19 connect controller, controller connection temperature probe T116 and hygrosensor T217, work as temperature probe T1When the temperature of 16 detections are less than 100 DEG C, a small amount of air and hydrogen incoming fuel battery pile, magnetic valve A18 is closed, magnetic valve b19 full opens, and coolant all returns coolant storage tank;Work as temperature probe T116 temperature is more than 100 DEG C, temperature probe T2When 17 temperature is close 100 DEG C, magnetic valve a18 is opened part, magnetic valve b19 is opened, and is controlled cold But the part of liquid returns coolant storage tank by circulation pipe, is partially into fuel cell pack, the coolant of incoming fuel battery pile Control is the 10% of coolant total flow;Work as temperature probe T2When 17 temperature is more than 120 DEG C, magnetic valve a18 standard-sized sheets, electromagnetism Valve b19 is closed, while hydrogen, air standard-sized sheet, and controls the temperature of incoming fuel battery pile by heat exchanger, now fuel cell Power can export 0~10kw with free and stable.
Embodiment 2
By a 30kw high temperature fuel cell pack, the battery pile has that 3 10kw modular concurrents are integrated to be formed, integrated operation System such as embodiment 1, described magnetic valve a18, magnetic valve b19 is replaced by a triple valve, and remaining is with embodiment 1.
Heating tube can be arranged as required to 1~20, and the power of every heating tube may be selected 0.1~500w.

Claims (7)

1. a kind of high temperature fuel cell integrated operation system, including fuel cell pack, and be connected on fuel cell pack Hydrogen is supplied and the circulatory system, air supply and the circulatory system and cooling fluid circulation system, wherein hydrogen supply and cyclic system System includes hydrogen gas tank, pressure-reducing valve, pressure maintaining valve, jet pump, steam-water separator, and described hydrogen gas tank passes sequentially through pressure-reducing valve, voltage stabilizing Valve, jet pump are connected to the hydrogen inlet of fuel cell pack, the hydrogen outlet connection steam-water separator of fuel cell pack, carbonated drink point Gas vent from device connects jet pump;Described air supply includes filter, blower fan with the circulatory system, and the entrance of blower fan connects Take over filter, the air intlet of outlet connection fuel cell pack;Described cooling fluid circulation system include coolant recirculation pump, Coolant storage tank, cooling water radiator, described coolant storage tank is sequentially connected coolant recirculation pump, cooling water radiator, combustion The coolant inlet of material battery pile, the cooling liquid outlet connection coolant storage tank of fuel cell pack, it is characterised in that it is right also to include The heat exchanger that hydrogen and air are preheated, and the coolant closed circuit of control coolant rate, flow out from pressure maintaining valve After heat exchanger heat exchange, by jet pump incoming fuel battery pile, the air flowed out from blower fan is Jing after heat exchanger heat exchange for hydrogen Incoming fuel battery pile, the hot-air that the air outlet slit of fuel cell pack is discharged returns heat exchanger;Described coolant is looped back Road includes two solenoid electric valves and a circulation line, and the circulation line connects coolant recirculation pump and coolant storage tank, institute A solenoid electric valve a in two solenoid electric valves stated is arranged on the main pipeline of cooling fluid incoming fuel battery pile, Another solenoid electric valve b is arranged on circulation pipe, makes cooling liquid complete by controlling one of them or two solenoid electric valves Portion or part not even incoming fuel battery pile.
2. a kind of high temperature fuel cell integrated operation system according to claim 1, it is characterised in that described heat exchange Heating tube, one or more hydrogen flow-path tube, one or more air stream deferent are provided with device, exchanger base is provided with air and enters Mouthful, top is provided with air outlet and exhaust-valve;Described hydrogen flow-path tube two ends connect respectively pressure maintaining valve and jet pump, described Air stream deferent two ends difference connecting fan and fuel cell pack, described heating tube external power supply, hydrogen and air are entered Row preheating, while reclaiming the heat of the air flowed out from fuel cell pack.
3. a kind of high temperature fuel cell integrated operation system according to claim 2, it is characterised in that described heating Pipe is provided with 1~20, and the power of every heating tube is 0.1~500w.
4. a kind of high temperature fuel cell integrated operation system according to claim 2, it is characterised in that described heating Manage as quartz glass tube or aluminum fin-stock cage walls or copper clad pipe.
5. a kind of high temperature fuel cell integrated operation system according to claim 1, it is characterised in that described fuel Temperature probe T 1 is provided with the air outlet slit of battery pile, cooling fluid exit is provided with temperature probe T 2.
6. a kind of high temperature fuel cell integrated operation system according to claim 5, it is characterised in that described two Solenoid electric valve connects controller, controller connection temperature probe T 1 and temperature probe T 2, when temperature probe T 1 is detected Temperature when being less than 100 DEG C, a small amount of air and hydrogen or without air or hydrogen incoming fuel battery pile close solenoid electric valve A, opens solenoid electric valve b, and coolant all returns coolant storage tank;When the temperature of temperature probe T 1 is more than 100 DEG C, temperature When the temperature of detector T2 is close 100 DEG C, solenoid electric valve a and solenoid electric valve b is opened and is controlled cooling liquid part and leads to simultaneously Cross circulation line and return coolant storage tank, be partially into fuel cell pack, the coolant control of incoming fuel battery pile is in cooling The 1~20% of liquid total flow;When the temperature of temperature probe T 2 is more than 120 DEG C, hydrogen, air normally enter fuel cell Heap, solenoid electric valve a standard-sized sheets, solenoid electric valve b is closed, and coolant fully enters fuel cell pack, and is radiated by coolant Device controls the temperature of incoming fuel battery pile.
7. a kind of high temperature fuel cell integrated operation system according to claim 1 or 6, it is characterised in that described Two solenoid electric valves can also be replaced by a triple valve.
CN201310723448.1A 2013-12-24 2013-12-24 Medium-high-temperature fuel cell integrated operation system Active CN104733748B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310723448.1A CN104733748B (en) 2013-12-24 2013-12-24 Medium-high-temperature fuel cell integrated operation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310723448.1A CN104733748B (en) 2013-12-24 2013-12-24 Medium-high-temperature fuel cell integrated operation system

Publications (2)

Publication Number Publication Date
CN104733748A CN104733748A (en) 2015-06-24
CN104733748B true CN104733748B (en) 2017-05-10

Family

ID=53457410

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310723448.1A Active CN104733748B (en) 2013-12-24 2013-12-24 Medium-high-temperature fuel cell integrated operation system

Country Status (1)

Country Link
CN (1) CN104733748B (en)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106558713B (en) * 2015-09-18 2019-12-10 北京亿华通科技股份有限公司 Low-temperature starting system and operation method for fuel cell
CN106532097B (en) * 2016-12-09 2023-08-29 新源动力股份有限公司 Connecting piece for fuel cell system
CN106532083B (en) * 2016-12-15 2023-07-28 新源动力股份有限公司 Fuel cell connection module with water-containing thermal management structure design
CN106677260A (en) * 2017-01-24 2017-05-17 武汉地质资源环境工业技术研究院有限公司 Proton exchange membrane fuel cell air water intake device
CN106592696A (en) * 2017-01-24 2017-04-26 武汉地质资源环境工业技术研究院有限公司 Fuel cell based air water-taking device
CN106759662A (en) * 2017-02-28 2017-05-31 武汉地质资源环境工业技术研究院有限公司 One proton exchanging film fuel battery apparatus for recovering
CN109873183B (en) * 2017-12-04 2021-06-18 中国科学院大连化学物理研究所 Direct liquid fuel cell power generation device
CN107978822B (en) * 2017-12-20 2023-09-22 新源动力股份有限公司 Fuel cell system structure with hydrogen circulation and heat exchange functions
CN108417856B (en) * 2018-03-02 2020-12-22 上海氢尚新能源科技有限公司 Fuel cell flow guide bipolar plate with timely and convenient drainage and fuel cell system
JP7098560B2 (en) * 2019-03-15 2022-07-11 本田技研工業株式会社 Fuel cell system and fuel cell stack temperature control method
CN109786790B (en) * 2019-03-27 2024-02-23 佛山市清极能源科技有限公司 Fuel cell system capable of being started and stopped at low temperature and control method thereof
CN112397741B (en) * 2019-08-19 2022-05-03 未势能源科技有限公司 Fuel cell system and method of operation
CN110676482B (en) * 2019-09-09 2022-02-08 全球能源互联网研究院有限公司 Fuel cell cogeneration system
CN110649280A (en) * 2019-09-26 2020-01-03 上海电气集团股份有限公司 Fuel cell cogeneration system and device
CN112582731B (en) * 2019-09-30 2022-09-09 比亚迪股份有限公司 Battery module
CN112670530A (en) * 2019-10-16 2021-04-16 上海德威明兴新能源科技有限公司 Hydrogen heating device
CN110970638B (en) * 2019-12-11 2024-04-16 浙江氢谷新能源汽车有限公司 Fuel cell heat balance gas-gas three-phase heat exchange system
CN111092244A (en) * 2019-12-11 2020-05-01 浙江氢谷新能源汽车有限公司 Fuel cell heat balance 'gas-liquid' three-phase heat exchange system
CN112993316B (en) * 2019-12-16 2022-06-10 中车时代电动汽车股份有限公司 Raw material supply system for fuel cell
CN111452674B (en) * 2020-04-20 2023-10-24 中极氢能汽车(长治)有限公司 Full-power hydrogen fuel cell car auxiliary group energy system cooling system
CN112467169B (en) * 2020-11-11 2021-11-05 国科微城市智能科技(南京)有限责任公司 Use method for starting hydrogen fuel cell by waste heat energy storage
CN112599814A (en) * 2020-11-25 2021-04-02 清华大学 Fuel cell system and fuel cell vehicle
CN113346103B (en) * 2021-05-28 2022-08-16 黄冈格罗夫氢能汽车有限公司 Fuel cell heat dissipation system for high-power station and control method
CN113745567B (en) * 2021-08-26 2023-01-31 武汉氢能与燃料电池产业技术研究院有限公司 Fuel cell power supply system based on phase change energy storage

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1339181A (en) * 1998-11-02 2002-03-06 兹特克公司 Fuel cell stacks for ultra-high efficiency power systems
CN102163731B (en) * 2010-02-19 2014-06-04 通用汽车环球科技运作有限责任公司 Compressor system with a freewheeling expander
CN203674322U (en) * 2013-12-24 2014-06-25 上海神力科技有限公司 Integrated operation system for middle and high-temperature fuel cell

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1339181A (en) * 1998-11-02 2002-03-06 兹特克公司 Fuel cell stacks for ultra-high efficiency power systems
CN102163731B (en) * 2010-02-19 2014-06-04 通用汽车环球科技运作有限责任公司 Compressor system with a freewheeling expander
CN203674322U (en) * 2013-12-24 2014-06-25 上海神力科技有限公司 Integrated operation system for middle and high-temperature fuel cell

Also Published As

Publication number Publication date
CN104733748A (en) 2015-06-24

Similar Documents

Publication Publication Date Title
CN104733748B (en) Medium-high-temperature fuel cell integrated operation system
CN203674322U (en) Integrated operation system for middle and high-temperature fuel cell
CN104577168B (en) Methanol water hydrogen production power generation system and hydrogen production power generation method
CN100367533C (en) Cooling system for a fuel cell stack
CN104733746B (en) A kind of low temperature and high temperature fuel cell combined operation system
CN113278993B (en) High-safety fuel cell electrolytic cell system and working method thereof
US8227119B2 (en) Fuel cell system
CN104577163B (en) A kind of hydrogen gas generating system and its electricity-generating method
CN102437357B (en) Water balance system of fuel cell
WO2010123146A1 (en) Method of controlling a fuel cell system
US20120135322A1 (en) Fuel cell system
CN206961949U (en) Humidification device and fuel cell system
CN113278992B (en) Water vapor turbocharged fuel cell electrolytic cell system and working method thereof
CN201238067Y (en) Electric pile activation system of fuel cell
CN101764238A (en) Method for safely and efficiently cycling fuel cell hydrogen or oxygen
CN102751523B (en) Integration battery, the integrated battery pile comprising it and integrated battery system
CN101853957B (en) Fuel cell system
KR101095665B1 (en) Fuel cull power generation system
US8685577B2 (en) Fuel cell system and method of controlling the fuel cell system
CN109713337B (en) Direct methanol fuel cell and lithium ion battery hybrid output device and output method
CN101447573A (en) Device for recycling fuel cell generating water
CN114628732B (en) Solar-assisted fuel cell waste heat recovery integrated system and method
CN203690408U (en) Joint operation system for low-temperature and medium-high temperature fuel cells
CN215209640U (en) Proton exchange membrane electrolytic hydrogen production device based on photovoltaic cell
CN204289611U (en) A kind of methanol-water preparing hydrogen, generating power system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant