CN104112866B - The burning of a kind of fuel cell system is reformed and is premixed integrated apparatus - Google Patents
The burning of a kind of fuel cell system is reformed and is premixed integrated apparatus Download PDFInfo
- Publication number
- CN104112866B CN104112866B CN201310138809.6A CN201310138809A CN104112866B CN 104112866 B CN104112866 B CN 104112866B CN 201310138809 A CN201310138809 A CN 201310138809A CN 104112866 B CN104112866 B CN 104112866B
- Authority
- CN
- China
- Prior art keywords
- chamber
- reformation
- gas
- premix
- tubulation
- 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
Classifications
-
- 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
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04268—Heating of fuel cells during the start-up of the fuel cells
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0618—Reforming processes, e.g. autothermal, partial oxidation or steam reforming
-
- 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
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)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Abstract
The invention discloses a kind of fuel cell system burning reformation premix integrated apparatus.Specifically, described device is connected with burner, reformation chamber and vaporization premix chamber from bottom to up, and the outer wall of the flue gas expansion chamber of burner simultaneously constitutes reformation chamber and the outer wall of vaporization premix chamber.The high-quality heat of combustor of the present invention is primarily used for reforming reaction heat supply, and remaining heat is then further used in preheating methane and vaporizes water, it is achieved that the cascade utilization of energy, it is achieved that system effectiveness maximizes.
Description
Technical field
The present invention relates to a kind of burning reformation premix integrated apparatus, a kind of burning for fuel cell system
Reform and premix integrated apparatus.
Background technology
Fuel cell efficiently, environmentally friendly by the chemical energy etc. being stored in fuel can leniently be converted into electric energy,
Hydrogen is the optimum fuel of fuel cell, if only with hydrogen as fuel, and can fuel cell system industry, rule
Modelling develops, and how the fuel such as natural gas is converted into hydrogen and seems most important.
Steam reformation hydrogen production technology (CH industrially4+H2O→CO+3H2) the most ripe, but this extensive hydrogen manufacturing
Technology can not meet the requirement of fuel cell system compact, miniaturization.
Owing to fuel cell system hydrogen demand is few, so the design ginseng of the large-scale process for making hydrogen of maturation cannot be reduced merely
Number, therefore, this area in the urgent need to develop be applicable to fuel cell system and steam reformation integrated small device.
Summary of the invention
The invention provides a kind of collecting burning, reform, vaporize, preheat and mixed function is in one for fuel cell system
The reformer of body.
A first aspect of the present invention, it is provided that a kind of fuel cell system is reformed with burning and premixed integrated apparatus, described
Device be connected with from bottom to up burner, reformation chamber and vaporization premix chamber.
In another preference, described burner also includes flue gas expansion chamber, and described flue gas expansion chamber is located at burning
Device top, upwardly extends and surrounds described reformation chamber and vaporization premix chamber.
In another preference, the shell of described flue gas expansion chamber forms described reformation chamber and the closing of vaporization premix chamber
Shell.
In another preference, the exhanst gas outlet of described flue gas expansion chamber is positioned at top or the top of flue gas expansion chamber.
In another preference, described flue gas expansion chamber (or its shell) is stainless steel or alloy material.
In another preference, the size of described flue gas expansion chamber is 90-320, it is preferred that 100-305mm, more preferably
Ground, 133-245mm.
In another preference, described burner also includes fuel inlet, air intlet and Fuel-air hybrid chamber,
And fuel inlet, air intlet and Fuel-air hybrid chamber are interconnected with described flue gas expansion chamber.
In another preference, described burner also includes spark plug, flame plate and/or exhanst gas outlet.
In another preference, described burner also includes flame-proof switch, gas flowmeter.
In another preference, the pipe diameter of described fuel inlet is 5-20mm, is more preferably 10-15mm.
In another preference, the pipe diameter of described air intlet is 5-40mm, is more preferably 10-30mm.
In another preference, described Fuel-air hybrid chamber includes the most mixed chamber and the most mixed chamber, and described fuel enters
The combustor end of mouth stretches in the most mixed chamber.
In another preference, the shape in described first mixed chamber and the most mixed chamber includes cone or cylinder.
In another preference, the combustor end tube wall of described fuel inlet is provided with cellular opening.
In another preference, the arrangement mode of described cellular opening is the most evenly distributed.
In another preference, between described first mixed chamber and the most mixed chamber, it is provided with dismountable attachment means.
In another preference, described dismountable attachment means includes Flange joint.
In another preference, described vaporization premix chamber include material inlet, reducing premix coil pipe, mixing surge tank with
And mixed gas outlet, wherein, described material inlet, reducing premix coil pipe, mixing surge tank and mixed gas outlet are sequentially
Communicate mutually.
In another preference, described vaporization premix chamber include material inlet, reducing premix coil pipe, mixing surge tank with
And mixed gas outlet, wherein, described material inlet, reducing premix coil pipe, mixing surge tank and mixed gas outlet are sequentially
Interconnect.
In another preference, described reducing premix coil pipe coiling is located at outside mixing surge tank.
In another preference, described mixing surge tank is provided with Heat Conduction Material.
In another preference, described Heat Conduction Material include honeycomb metal, net metal, porous media material or
A combination thereof.
In another preference, described material inlet includes water inlet and methane import.
In another preference, the diameter of described reducing premix coil pipe is increased thick by inlet-outlet direction；And/or
Described reducing premix coil pipe at least includes two kinds of diameters.
In another preference, described reducing premix coil pipe includes slim pipe diameter coil pipe and extra heavy pipe footpath coil pipe.
In another preference, it is peripheral that described slim pipe diameter coil pipe is paperwrapped in extra heavy pipe footpath coil pipe.
In another preference, described reformation chamber includes that mixed gas outlet, reformation tubulation and reformate are given vent to anger
Mouthful, and described mixed gas outlet, reformation tubulation and reformate gas outlet be sequentially interconnected.
In another preference, between described mixed gas outlet and reformation tubulation, it is provided with gas distribution dish, wherein, described
The mixed gas that gas distribution dish flows out in being collected from mixing surge tank, and described mixed gas is entered reformation row
Pipe；And/or
Gas current collecting plates, wherein, described gas current collecting plates it is provided with between described reformation tubulation and reformate gas outlet
For collecting the reformed gas in reformation tubulation, and described reformed gas is entered reformate gas outlet.
In another preference, described reformation tubulation is evenly arranged around the centrage of shunting disk and current collecting plates.
In another preference, described reformation tubulation quantity is n, the wherein positive integer of n=2-16；And/or
In another preference, the tube wall of described reformation tubulation is provided with external thread structure.
In another preference, described gas distribution dish or gas current collecting plates respectively set n through hole, n be 2-16 just
Integer, and gas distribution dish is connected by described reformation tubulation with the through hole of gas current collecting plates.
In another preference, described reformation chamber is additionally provided with temperature controller.
Second aspect present invention, it is provided that a kind of fuel cell system, described fuel cell system includes such as the present invention the
Burning described in Yi Fangmian is reformed premix integrated apparatus and fuel cell, air compressor machine, water knockout drum and water tank, dosing pump, each
Class valve control and attemperating unit.
In should be understood that within the scope of the present invention, above-mentioned each technical characteristic of the present invention and having in below (eg embodiment)
Can be combined with each other between each technical characteristic that body describes, thus constitute new or preferred technical scheme.As space is limited, exist
This tires out the most one by one states.
Accompanying drawing explanation
Fig. 1 is the structural representation of the burning reformation vaporization preheating integrated apparatus for fuel cell system；
Fig. 2 is the internal structure schematic diagram of burning reformation vaporization preheating integrated apparatus；
Fig. 3 is the reformer tubes structural pipe wall schematic diagram of external thread structure.
Wherein, 1-burner, 2-reformer, 3-vaporization preheats at the beginning of mixing arrangement, 4-fuel inlet, 5-air intlet, 6-
Mixed chamber, 7-flange, the most mixed chamber of 8-, 9-flame plate, 10-spark plug, 11-bolt, 12-reformate gas outlet, 13-gas afflux
Dish, 14-flue gas expansion chamber, 15-external thread structure reformation tubulation, 16-gas distribution dish, 17-is filled with perforated metal material and mixes
Closing surge tank, 18-slim pipe diameter coil pipe, 19-extra heavy pipe footpath coil pipe, 20-combustion product gases exports, 21-water inlet, 22-Imported gas,
23-mixed gas outlet, 24,25-thermocouple, the anti-riot switch interface of 26-.
Detailed description of the invention
The present inventor through extensively in-depth study, first by the burner in fuel cell system, reformation chamber and
Vaporization premix chamber connects combination from bottom to up, makes reformation and vaporization premix chamber be positioned at inside the flue gas expansion chamber of burner, from
And taking full advantage of the heat in burner, the flue gas reformer that i.e. burning fuel produces reaches to react temperature required, weight
The flue gas after-heat that whole reaction has utilized is required for feed-water flashing and natural gas preheating, makes water in vaporization preheating mixing arrangement
Vaporization resupplies reformer after becoming steam, natural gas pre-heating temperature elevation and mixing with steam.Apparatus of the present invention make waste heat
Ladder utilizes, and is conducive to improving level of integrated system and system whole efficiency.
Burner
In the present invention, burner is for the anode exhaust gas of fuel cell or other fuel gas of burning.Anode exhaust gas or
After fuel gas, its heat is used in reforming reaction and the premix of reforming reaction raw material for ladder.Generally, described
Fuel gas includes natural gas.
The burner of the present invention includes flue gas fuel inlet, air intlet and Fuel-air hybrid chamber, described fuel
Import, air intlet are connected with Fuel-air hybrid chamber, and the described pipeline used by fuel inlet stretches into Fuel-air and mixes
Close intracavity.
Wherein, described Fuel-air hybrid chamber also can farther include the most mixed chamber and the most mixed chamber.In order to make fuel with empty
Gas can be sufficiently mixed, and the combustor end of described fuel inlet is positioned at the most mixed intracavity, and its tube wall is provided with cellular opening, and institute
The arrangement mode of the cellular opening stated is the most evenly distributed.When being passed through air and fuel, cavernous opening energy
Make fuel mix with air with certain pressure, thus sufficiently burn.
The pipe diameter that can be used for fuel inlet of the present invention or air intlet is not particularly limited, and can reform according to burning
The amount that the size of premix integrated apparatus and described fuel and air need carries out different designs.Generally, described combustion
The pipe diameter of material import is 5-20mm, preferably 10-15mm；The pipe diameter of described air intlet is 5-40mm, excellent
Choosing for 10-30mm.
In the present invention, described burner is provided with a flue gas expansion chamber, and described flue gas expansion chamber is located at burner top,
Upwardly extend and surround described reformation chamber and vaporization premix chamber.The top of flue gas expansion chamber is additionally provided with one for discharging residue cigarette
The exhanst gas outlet of gas.
The material that can be used for flue gas expansion chamber of the present invention (or its shell) is not particularly limited, and can be any tolerance high temperature
Material.Generally, described flue gas expansion chamber (or its shell) is rustless steel or alloy material.
The diameter of flue gas expansion chamber of the present invention is not particularly limited, as long as reformer and vaporization preheating can be covered or surround
Chamber, or be designed according to the size of burning reformation premix integrated apparatus or manufacture.Generally, described flue gas expansion chamber
Size (external diameter) is 90-320, it is preferred that 100-305mm, more preferably, 133-245mm.
In another preference, after described fuel and air enter the preliminary mixing of the most mixed chamber entrance, enter back into the most mixed chamber
Mix homogeneously, is burnt at flame plate by electricity sparking spark plug and produces flue gas, and flue gas injection goes out to enter flue gas expansion chamber, works as institute
The shell stating flue gas expansion chamber forms described reformation chamber and the closure of vaporization premix chamber, then flue gas is on burner
Diffusion reduction of speed in the reformation chamber of side and the vaporization preheating cavity surrounding package cavity on top, thus heating is positioned at burner top
Reformation chamber and vaporization premix chamber.
Additionally, the burner of the present invention also includes spark plug, flame plate, exhanst gas outlet, flame-proof switch and/or gas flow
Meter.Burner charging, just mixed between cavity segment with combustion flame dish, the most mixed cavity segment separate, and use Flange joint, install clever
Work, dismounting and change are conveniently.Occur to prevent burner from becoming the dangerous situations such as high-pressure bottle, be provided with flame-proof switch, it is ensured that
Safe and reliable operation.Control fuel flow rate 1-35l/min by effusion meter simultaneously and control combustion power, regulation natural gas and sky
Gas ratio 10-20 controls combustion flame position and height.
Vaporization premix chamber
In the present invention, vaporization premix chamber includes material inlet, reducing premix coil pipe, mixing surge tank and mixed gas
Outlet, described material inlet, reducing premix coil pipe, mixing surge tank and mixed gas outlet sequentially interconnect.
Wherein, described material inlet includes water inlet and methane import；Described reducing premix coil pipe coiling is located at mixed
Closing outside surge tank, reducing premix coil pipe at least includes two kinds of diameters, and its diameter is increased thick by inlet-outlet direction.Generally, described
Reducing premix coil pipe include slim pipe diameter coil pipe and extra heavy pipe footpath coil pipe.
The flow of the reducing premix coil pipe caliber and fuel that can be used for the present invention is not particularly limited, and can reform according to burning
The size of premix integrated apparatus is designed or manufactures.Generally, slim pipe diameter coil pipe is paperwrapped in the periphery of extra heavy pipe footpath coil pipe, and carefully
A diameter of 2-10mm of caliber coil pipe, more preferably, for 4-6mm, discharge is 1-160g/min；A diameter of 6-of extra heavy pipe footpath coil pipe
20mm, more preferably, for 8-16mm, after methane and aqueous water enter slim pipe diameter coil pipe by material inlet, carries via burner
The heat of confession, aqueous water is gradually through being vaporized into water vapour, and enters the coil pipe in more extra heavy pipe footpath after volumetric expansion.Certainly,
The diameter of reducing premix coil pipe can also be gradual change type or multi-stag, may be incorporated for the heating of aqueous water.
In the present invention, mixing surge tank is connected to the far-end of reducing premix coil pipe, can fill Heat Conduction Material with slow inside it
Rush mixed gas and make it heat further.Can be used for the present invention and mix the Heat Conduction Material of surge tank and size does not all have special limit
System, wherein, Heat Conduction Material can be that any heat conduction is quick and can form the material of air-flow buffer effect, such as, metal or other
Heat-conducting medium, it is preferred that described metal or heat-conducting medium material are cellular, netted or cellular；The size of mixing surge tank
Can be designed or manufacture according to the size of burning reformation premix integrated apparatus, such as 50-102mm.
Can be used for the present invention to vaporize the unstrpped gas of premix chamber and include methane or natural gas.Methane or natural gas can lead directly to slow
Rush tank, or jointly lead to reducing coil pipe with water inlet.In another preference, unstrpped gas can be directly entered mixing surge tank,
And after being sufficiently mixed with steam, enter reformer and carry out reforming reaction.
Total in the present invention, the ratio of unstrpped gas and steam can be through source of the gas or effusion meter according to the water of reforming reactants
The different needs of carbon ratio (water vapour is between 1 to 5 from the mol ratio of natural gas) are adjusted.In another preference, this combustion
The hydrogen that burning reformation vaporization pre-mixing apparatus may be used for being prepared by gas renormalizing in fuel cell system is for fuel cell power generation.
Reformation chamber
In the present invention, described reformation chamber includes mixed gas outlet, reformation tubulation and reformate gas outlet, and
Described mixed gas outlet, reformation tubulation and reformate gas outlet are sequentially interconnected.
Wherein, gas distribution dish, wherein, described gas distribution dish it are provided with between described mixed gas outlet and reformation tubulation
The mixed gas flowed out in being collected from mixing surge tank, and described mixed gas is entered reformation tubulation；And/or
Being provided with gas current collecting plates between described reformation tubulation and reformate gas outlet, described gas current collecting plates is used for receiving
Reformed gas in collection reformation tubulation, and described reformed gas is entered reformate gas outlet.
In the present invention, described gas distribution dish or gas current collecting plates respectively setting n through hole, n is the positive integer of 2-16,
And gas distribution dish is connected by described reformation tubulation with the through hole of gas current collecting plates.And the quantity of tubulation of reforming can be according to dividing
Flow table or the via design of current collecting plates；In a preference, described through hole is uniformly distributed on gas distribution dish or current collecting plates,
And described reformation tubulation is evenly arranged around the centrage of shunting disk and current collecting plates.Wherein, described reformation tubulation quantity is n
Individual, the wherein positive integer of n=2-16.Reformer tubes number can 2-26 root, in a preference, described reformation tubulation number is 6-16 root
In order to be able to make the heat exchange of the reformed gas within reformation tubulation and reforming reaction more abundant, preferably in described reformation
The tube wall of tubulation is provided with external thread structure, thus strengthens the heat exchange area of reformed gas.
The size of the reformation tubulation that can be used for the present invention is not particularly limited, and can include various being suitable for apparatus of the present invention
Size, generally, its size is 10-50mm*250mm-700mm, and more preferably, described reformation tubulation is 18-28*330-
465mm。
In the present invention, premix chamber is led on top, reformation chamber, therebetween with the mixed gas inlet warp of steam and natural gas
Shunting disk connects, and burner is led in bottom, connects with current collecting plates therebetween.Mixed gas in gas distribution dish is entered by through hole
Each reformation tubulation carries out reforming reaction, and the reformate gas reacting generation in each reformation tubulation is collected by current collecting plates, and led to
Cross gas outlet to discharge.
In addition described reformation chamber is additionally provided with temperature controller, can feed back reformer tubes interior reaction temperature by temperature controller, control
The burning inlet fuel of burner.Gaseous mixture after reforming reaction is conveyed in the anode of fuel cell pack and carries out reaction and make
With.
Fuel cell system
Fuel cell system of the present invention includes that the present invention burns to reform and premixes integrated apparatus and fuel cell, pneumatics
Machine, water knockout drum and water tank, dosing pump, all kinds of valve control and attemperating unit.
Application
The present invention reformation premix integrated apparatus that burns can be used on a small scale hydrogen manufacturing it can also be used to outside fuel cell system
Reform, thus there is not hydrogen storage and transportation problem, as long as connecting natural to the reformation premix integrated apparatus of fuel cell system
Gas, just can continuously export electric energy.This system can be as a kind of safe and environment-friendly, of good reliability and compact conformation, reasonable cloth
Portable or the distributed fuel cell TRT put.Fuel cell distributed co-generation unit can network in regionality
In can be that the webserver, telecommunication apparatus, residential quarters, hospital, bank etc. provide stabilized power source, cheap heat is provided simultaneously
Source.Its market scale, compared with big and user's ability to bear is moderate, has good market application foreground and commercial value.
Beneficial effects of the present invention
The invention provides the reforming reaction device of a kind of fuel cell burning capacity cascade utilization.This device passes through will
The flue gas expansion chamber of burner is located at reformation chamber and the periphery of vaporization premix chamber, and the heat energy making combustor produce sequentially passes through reformation
Chamber, He Shui-methane premix chamber carry out repeatedly step heat exchange, by burning, vaporize, preheat, mix, the multifunctional unit such as reformation in
Integrally, and simple in construction, it is possible to meet the requirement of miniaturization, eliminate steam generator, improve the integrated level of device.Combustor
High-quality heat be primarily used for as peripheral reforming reaction heat supply, remaining heat is then further used in preheating methane also
Vaporization water, it is achieved that the cascade utilization of energy, it is achieved that system effectiveness maximizes.
The all documents mentioned in the present invention are incorporated as reference the most in this application, just as each document by individually
It is incorporated as with reference to like that.In addition, it is to be understood that after the above-mentioned teachings having read the present invention, those skilled in the art can
To make various changes or modifications the present invention, these equivalent form of values fall within the model that the application appended claims is limited equally
Enclose.
Claims (9)
1. a fuel cell system is reformed with burning and is premixed integrated apparatus, it is characterised in that described device is from bottom to top
Be connected with burner, reformation chamber and vaporization premix chamber；Wherein
Described reformation chamber includes mixed gas outlet, reformation tubulation and reformate gas outlet, and described mixed gas
Outlet, reformation tubulation and reformate gas outlet are sequentially interconnected；And
Being provided with gas distribution dish between described mixed gas outlet and reformation tubulation, described gas distribution dish is used for being collected from mixing
The mixed gas flowed out in surge tank, and described mixed gas is entered reformation tubulation；And/or
Being provided with gas current collecting plates between described reformation tubulation and reformate gas outlet, wherein, described gas current collecting plates is used for
Collect the reformed gas in reformation tubulation, and described reformed gas is entered reformate gas outlet.
2. device as claimed in claim 1, it is characterised in that described burner also includes flue gas expansion chamber, and described cigarette
Gas expansion chamber is located at burner top, upwardly extends and surround described reformation chamber and vaporization premix chamber.
3. device as claimed in claim 2, it is characterised in that described burner also include fuel inlet, air intlet and
Fuel-air hybrid chamber, and fuel inlet, air intlet and Fuel-air hybrid chamber interconnect mutually with described flue gas expansion chamber
Logical.
4. device as claimed in claim 3, it is characterised in that described Fuel-air hybrid chamber includes that the most mixed chamber is with the most mixed
Chamber, and the combustor end of described fuel inlet stretches into just in mixed chamber.
5. the device as described in claim 1-4 is arbitrary, it is characterised in that described vaporization premix chamber includes material inlet, change
Footpath premix coil pipe, mixing surge tank and mixed gas outlet, wherein, described material inlet, reducing premix coil pipe, mixing buffering
Tank and mixed gas outlet communicate the most mutually.
6. device as claimed in claim 5, it is characterised in that the diameter of described reducing premix coil pipe is by inlet-outlet side
Thick to increasing；And/or
Described reducing premix coil pipe at least includes two kinds of diameters.
7. device as claimed in claim 1, it is characterised in that described reformation tubulation is around shunting disk and the center of current collecting plates
Line is evenly arranged.
8. device as claimed in claim 1, it is characterised in that respectively set n on described gas distribution dish or gas current collecting plates
Through hole, n is the positive integer of 2-16, and gas distribution dish is connected by described reformation tubulation with the through hole of gas current collecting plates.
9. a fuel cell system, it is characterised in that described fuel cell system includes the weight that burns as claimed in claim 1
Whole premix integrated apparatus and fuel cell, air compressor machine, water knockout drum and water tank, dosing pump, all kinds of valve control and attemperating unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310138809.6A CN104112866B (en) | 2013-04-19 | 2013-04-19 | The burning of a kind of fuel cell system is reformed and is premixed integrated apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310138809.6A CN104112866B (en) | 2013-04-19 | 2013-04-19 | The burning of a kind of fuel cell system is reformed and is premixed integrated apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104112866A CN104112866A (en) | 2014-10-22 |
| CN104112866B true CN104112866B (en) | 2016-12-28 |
Family
ID=51709576
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310138809.6A Active CN104112866B (en) | 2013-04-19 | 2013-04-19 | The burning of a kind of fuel cell system is reformed and is premixed integrated apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104112866B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107910570A (en) * | 2017-12-14 | 2018-04-13 | 上海新源动力有限公司 | A kind of hydrogen air body dual disposal structure of fuel cell system |
| CN112151831B (en) * | 2019-06-27 | 2022-11-22 | 国家能源投资集团有限责任公司 | Reformer and fuel cell power generation system thereof |
| CN112072146A (en) * | 2020-10-14 | 2020-12-11 | 浙江浙能技术研究院有限公司 | Heat exchange, combustion and reformer assembly and method for high-temperature fuel cell power generation system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1568286A (en) * | 2002-06-03 | 2005-01-19 | 日产自动车株式会社 | Combustor, fuel reforming device, fuel cell system and method for starting up the fuel reforming system |
| CN102826507A (en) * | 2012-08-24 | 2012-12-19 | 华南理工大学 | Method and device of hydrogen production by natural gas and steam reforming for micro fuel cells |
| CN202737041U (en) * | 2012-08-24 | 2013-02-13 | 华南理工大学 | Natural gas steam reforming hydrogen production device for micro fuel cells |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7235217B2 (en) * | 2003-04-04 | 2007-06-26 | Texaco Inc. | Method and apparatus for rapid heating of fuel reforming reactants |
-
2013
- 2013-04-19 CN CN201310138809.6A patent/CN104112866B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1568286A (en) * | 2002-06-03 | 2005-01-19 | 日产自动车株式会社 | Combustor, fuel reforming device, fuel cell system and method for starting up the fuel reforming system |
| CN102826507A (en) * | 2012-08-24 | 2012-12-19 | 华南理工大学 | Method and device of hydrogen production by natural gas and steam reforming for micro fuel cells |
| CN202737041U (en) * | 2012-08-24 | 2013-02-13 | 华南理工大学 | Natural gas steam reforming hydrogen production device for micro fuel cells |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104112866A (en) | 2014-10-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104112867B (en) | The reforming reaction device of a kind of SOFC system burning capacity cascade utilization and electricity generation system | |
| CN106784924A (en) | A kind of hot zone structure of solid oxide fuel cell power generating system | |
| CN104112866B (en) | The burning of a kind of fuel cell system is reformed and is premixed integrated apparatus | |
| CN110902651B (en) | Self-heating annular methanol reforming hydrogen production reactor | |
| CN109748241A (en) | A kind of high efficiency reformers of methane self-heating recapitalization | |
| CN110425511A (en) | Ultralow nitrogen gas-steam boiler | |
| CN102826507B (en) | Method and device of hydrogen production by natural gas and steam reforming for micro fuel cells | |
| CN108110279B (en) | Movable methanol recombination fuel cell system | |
| CN202737041U (en) | Natural gas steam reforming hydrogen production device for micro fuel cells | |
| CN206148541U (en) | Ammonia fuel cell | |
| CN103107348B (en) | A kind of SOFC system coupled mode reforming reactor and electricity generation system | |
| CN112072146A (en) | Heat exchange, combustion and reformer assembly and method for high-temperature fuel cell power generation system | |
| CN210528462U (en) | High-performance reforming reactor | |
| CN208980324U (en) | A kind of quick start self-heating type preparing hydrogen by reforming methanol microreactor | |
| CN113834064B (en) | Ammonia gas burner | |
| CN107702132A (en) | Hydrogen-oxygen mixing auxiliary combustion equipment | |
| CN206514303U (en) | A kind of burner of hydrogen making by natural gas reformation reburner | |
| CN210921481U (en) | New forms of energy combustion system | |
| CN102798155B (en) | Living beings stove | |
| CN206412418U (en) | A kind of water hydrogen generator | |
| CN214360254U (en) | Natural gas reformer | |
| CN219510764U (en) | Baffling heat exchange steam generator | |
| CN205279063U (en) | Novel automatic burning furnace that fires of coal gasification is stored up in environmental protection | |
| CN203099815U (en) | Direct-injection-type biomass combustor | |
| CN204665354U (en) | A kind of fuel gas nozzle |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |