CN106784961B - A kind of air distributor for anode support type tubular type SOFC battery pile - Google Patents

A kind of air distributor for anode support type tubular type SOFC battery pile Download PDF

Info

Publication number
CN106784961B
CN106784961B CN201611085745.8A CN201611085745A CN106784961B CN 106784961 B CN106784961 B CN 106784961B CN 201611085745 A CN201611085745 A CN 201611085745A CN 106784961 B CN106784961 B CN 106784961B
Authority
CN
China
Prior art keywords
air
anode support
sofc battery
support type
distributor box
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
CN201611085745.8A
Other languages
Chinese (zh)
Other versions
CN106784961A (en
Inventor
陈代芬
徐雨
周拓
章心怡
马杰
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.)
Jiangsu University of Science and Technology
Original Assignee
Jiangsu University of Science and Technology
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 Jiangsu University of Science and Technology filed Critical Jiangsu University of Science and Technology
Priority to CN201611085745.8A priority Critical patent/CN106784961B/en
Publication of CN106784961A publication Critical patent/CN106784961A/en
Application granted granted Critical
Publication of CN106784961B publication Critical patent/CN106784961B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/2484Details of groupings of fuel cells characterised by external manifolds
    • H01M8/2485Arrangements for sealing external manifolds; Arrangements for mounting external manifolds around a stack
    • 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
    • H01M8/04201Reactant storage and supply, e.g. means for feeding, pipes
    • 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 invention discloses a kind of air distributors for anode support type tubular type SOFC battery pile, including sprue distributor box, preformed hole is closely passed through and is arranged in array for anode support type SOFC battery pipe unit on two opposite faces before and after the sprue distributor box, inside sprue distributor box, closed air flow channel is formed around SOFC battery pipe unit, the bottom side of sprue distributor box is equipped with uniform air intake, a side similar in sprue distributor box and air intake is from the bottom to top gradually to the inclined-plane of contract, offgas outlet is uniformly distributed on another side on the other side, the air flow direction of air intake and the flow direction of offgas outlet are mutually perpendicular to.The present invention is based on the SOFC pile internal flow regularities of distribution, the main region for influencing flow distribution is improved, heap level and the uniform air distribution quality of battery unit level are realized, many disadvantages for overcoming tubular type SOFC pile of the tradition based on cathode support type are conducive to.

Description

A kind of air distributor for anode support type tubular type SOFC battery pile
Technical field
The present invention relates to a kind of solid oxide fuel cell, and in particular to a kind of air distributor of SOFC battery pile.
Background technique
Fuel cell is a kind of generating equipment that reactant chemical energy is converted into electric energy.As a kind of efficient, clear Clean and stable performance energy technology, great advantage is to avoid combustion process directly for fuel compared with traditional power generation type Chemical energy be converted into output electric energy, energy conversion efficiency is not limited by " Carnot cycle ".
Solid oxide fuel cell (SOFC) is most one of the type of some commercial potential in all multiple fuel cells, master Wanting advantage includes: the fuel service efficiency with up to 50~60%, and product is mainly the waste heat of water and high-quality, to waste heat Secondary use gross efficiency may be up to 80% or more;Output power, runs smoothly and noiseless;Fuel source is flexible, not only fits For hydrogen, carbon monoxide, it is also applied for a variety of renewable carbon hydrogen fuels such as natural gas, coal gas and biogas;Low greenhouse Gas discharge;The problems such as leakage, corrosion is not present in all solid state component, and is easy to modularization assembling;Without using high price catalyst Material, advantage of lower cost.
SOFC battery pile mainly includes plate and two kinds of Basic Designs of cast and corresponding a variety of evolutions at present Design.Wherein tubular type SOFC pile design has stable structure firm, do not need the outstanding advantages such as complicated elevated-temperature seal and by Extensive concern.The tube type design of Siemens Westinghouse Power Corp., the U.S. is current most representative more mature design, cast SOFC battery unit is a structure open at one end closed at one end, thin by three layers of cathode-electrolyte-anode respectively from inside to outside The ceramic tube of film composition, is a kind of typical cathode support type structural design scheme.Air flows on the inside of ceramic tube, fuel gas Body supply is distributed on the outside of piping unit, this is primarily due to: on the one hand, in a fuel cell, air is not only reactant (oxygen Gas) main source and pile heat transfer main carriers, it largely influences electrochemical reaction, the temperature of SOFC Degree, stress, physical property distribution influence pile overall work performance and service life, therefore the design of air distributor is tubular type SOFC electricity Heap matter of utmost importance to be solved;And on the other hand, since reactant (oxygen) aerial volume fraction only has 21%, simultaneously The air utilization ratio of SOFC pile also only has 30% or so (fuel is generally up to 80% or more), therefore the molecular mass in pile Biggish air often has very high flow compared to the lesser fuel of molecular mass.It is experimentally confirmed that using empty on the outside of pipeline The mode of gas distribution has larger difficulty, and unreasonable design often leads to air as reactant and thermotransport carrier in battery (heap level) and battery unit pipe surface distribute (battery unit level) extremely non-uniform phenomenon between unit, this will substantially Degree reduces battery performance and service life.Therefore, the air generally on the inside of ceramic tube is distributed for the air of tubular type SOFC pile at present Be allocated by battery unit inside pipeline, thus between guaranteeing ceramic tube cells unit and battery unit cathode-side surface compared with Good air distributing uniformity.And such ceramic tube inside air method of salary distribution is corresponding, inevitable requirement SOFC unit is using yin Pole is in the cathode support type design of insides of pipes.
However be pointed out that using cathode support type tubular type SOFC design between solving tubular SOFC unit and While element cell superficial air evenly distributed this matter of utmost importance of degree, but also cathode support type tube designs are brought into simultaneously A series of unfavorable factors, this largely reduces tubular type Performance data: i) thickness of supporting element cathode is excessive causes Concentration difference loss in the heavier oxygen molecule diffusion process of molecular weight is excessive;Ii) since in the case where aoxidizing atmosphere, cathode is generally used The lower ceramic material of the conductivity such as LSM is as electronic conduction medium, the very long electric current collection path of insides of pipes in addition, because This tubular type cathode support means very high ohmic loss;Iii) fuel (especially wet hydrogen fuel) is on the outside of tubular cells unit When distribution, flow path resistance is too small, and to easily lead to fuel utilization rate too low;Iv) air flow resistance high in pipeline will lead to The output of required additional pump power is lost, while aggravating the pressure difference of air side and hydrogen gas side, increases the risk of air leakage;v) Since air has very high flow value compared to fuel, high-speed air fluid will aggravate cavitation in pipeline, simultaneously Air is the main carriers of heat again, and the peeling of electric current collection coating between interior connector is managed in aggravation by this.
Obvious, tubular type SOFC pile such as uses the design of anode support type ceramics pipe unit (to distribute in air hose, cartridge Outside distribution) it can effectively solve the problems, such as that above-mentioned some column are secondary, however as without reasonable pipeline outside air distribution design Mating, between severe battery unit and the air distribution results of battery surface will lead to even more serious operation of fuel cells effect Fruit.
Summary of the invention
Goal of the invention: in view of the above-mentioned deficiencies in the prior art, it is an object of the present invention to provide a kind of for anode support type pipe The air distributor of formula SOFC battery pile, thus the pottery overcome needed for solving in anode support type tubular type SOFC pile application process The outer air distribution problems of porcelain tube, significantly improve air (pile level) and battery list between battery unit in tubular type pile Air in first two levels of axial surface (battery unit level) distributes quality.
Technical solution: the present invention provides a kind of air distributor for anode support type tubular type SOFC battery pile, packets Include sprue distributor box, before and after the sprue distributor box on two opposite faces preformed hole for anode support type SOFC battery Pipe unit is closely passed through and is arranged in array, and is formed inside sprue distributor box, around SOFC battery pipe unit closed The bottom side of air flow channel, the sprue distributor box is equipped with uniform air intake, sprue distributor box and air intake A similar side is to be uniformly distributed on another side on the other side from the bottom to top gradually to the inclined-plane of contract Offgas outlet, the air flow direction of air intake and the flow direction of offgas outlet are mutually perpendicular to.
Further, the anode support type SOFC battery pipe unit includes anode support from the inside to the outside, electrolyte layer And cathode layer, cell tube unit pipe inside is fuel channel, and air is distributed in pipe exterior space.
Further, the orientation of the air intake is consistent with the axial direction of SOFC battery pipe unit, improves air In the distribution quality of each cell tube unit axial direction.
Further, air via air intake supervisor branch to after several main pipeline manifolds be correspondingly connected to along longitudinal direction it is each The caliber of air intake, the air intake supervisor is gradually reduced as air flows to, will the corresponding air of piece supervisor of script Flow is divided into multiple manifolds, and the flow velocity of each manifold is effectively reduced, so that the air distributing uniformity between main pipeline manifold is constrained, Be conducive to improve SOFC unit between (heap level) air distributing uniformity.
Further, offgas outlet converges into exhaust collection master after being connected respectively each exhaust collection manifold transversely The caliber of pipe, the exhaust collection supervisor is gradually increased along air discharge direction, and offgas outlet carries out tail gas using multiple manifolds It collects, can also reduce the air velocity in exhaust manifold, the air so as to improve air in battery pipe unit outer surface distributes matter Exhaust collection magnitude relation between amount, and constraint exhaust collection manifold.
The in/out mouth main pipeline of sprue distributor box passes through series of manifolds and carries out air distribution and collection, is being promoted Axial direction air is evenly distributed while spend, and reduces air velocity, increases the air uniformity in battery groundwork region.This Outside, the characteristic that there is air intake supervisor tube section gradually to contract, so that the air input be conducive in series of manifolds is uniform;It is similar , exhaust collection supervisor has flaring sectional area characteristic, can improve tail gas evenly distributing in series of manifolds.
Further, the offgas outlet divides the side that two longitudinal column are evenly distributed in the sprue distributor box, Air can be improved in each battery unit surface and the air distributing uniformity of axial direction.
Further, the offgas outlet is finally connected to the gas heating zone for being accommodated in the inner main pipeline manifold.
Further, the main pipeline manifold extends simultaneously detour in gas heating zone, more efficient can inhale from tail gas Take heat inlet gas.
Further, the top surface of the sprue distributor box more other cell tubes at a distance from top layer SOFC battery pipe unit Cell spacing reduces 1/3, and top of the excessive air by distributor is avoided by way of increasing the path flow resistance It is flowed out along around battery cell arrangement area.
Further, the side of the sprue distributor box where the offgas outlet with closest to SOFC battery pipe unit away from 1/3 is reduced from more other cell tube cell spacings, it is therefore an objective to be increased the resistance of the runner in the vertical direction, be forced more skies Air-flow avoids air from directly detouring by top layer space to the region around battery-arrangements area through battery-arrangements area, increases Distribution quality of the air between battery unit.
The utility model has the advantages that the present invention is based on the SOFC pile internal flow regularity of distribution, to the main region for influencing flow distribution Improved: bottom of box side is uniformly arranged in the air intake of sprue distributor box, so as to improve air each The distribution quality of a SOFC unit ceramic tube axial direction;Cabinet is the inclined-plane tapered close to the side of air intake, to reduce master Static air pressure near runner distributor box top area is strong, improves air distributing uniformity of the air between battery unit pipe;It is empty The flow direction of gas entrance and exit is mutually perpendicular to, while improving air between tubular type SOFC battery unit and SOFC ceramic tube list The air of first surface axial direction distributes quality;
The above air distribution under the premise of, realize air between anode support type SOFC ceramics pipe unit (heap level), And the more uniform air of battery unit ceramic tube cathode outer surface (battery unit level) distributes quality, is conducive to overcome tradition Many disadvantages of tubular type SOFC pile based on cathode support type, the advantage of anode support type tubular type SOFC structure of the present invention is such as Under:
Concentration difference loses advantage: the anode support structure of battery pipe unit is distributed in insides of pipes, and outside is relatively thin cathode, It is lost to significantly reduce oxygen in the concentration difference of cathode;
Ohmic loss advantage: since anode is mainly using metallic particles as conducting medium under reducing atmosphere, electronic conductance Rate is substantially better than cathode, and tubular cells unit inside electrode has the shortcomings that long electric current collection path in addition, therefore anode is made It is on the inside of tubular cells for supporting layer, cathode configures more flexible electric current collection part on the outside, ohm can be greatly lowered Loss;
Fuel (especially wet hydrogen fuel) passes through battery unit pipe transmitted inwards, it is ensured that the flow velocity and flow resistance of fuel And then increase substantially the fuel availability of tubular type SOFC pile;
The low air of utilization rate has lower flow resistance and pressure, on the one hand by external broad runner distribution It can reduce and be pumped into mechanical energy consumption, while it is poor to reduce the actual pressure of fuel-side and air side inside and outside pipe, to reduce oxygen Risk is peeled off in the cavitation erosion of current collection layer between risk of leakage and cathode and chain junctor, improves battery life;
Anode is in SOFC unit inside pipeline, is conducive to protect and avoids the reoxidized of anode material.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of air distributor box of the present invention;
Fig. 2 is the front view of air distributor box;
Fig. 3 is the partial schematic diagram of sprue distributor box;
Fig. 4 is the partial schematic diagram of air intake supervisor and main pipeline manifold;
Fig. 5 is the partial schematic diagram that exhaust collection manifold corresponding with entrance and exhaust collection are responsible for;
Fig. 6 is the partial schematic diagram of inlet gas heating region.
Specific embodiment
Technical solution of the present invention is described in detail below, but protection scope of the present invention is not limited to the implementation Example.
Embodiment: a kind of air distributor for anode support type tubular type SOFC battery pile, as shown in Figure 1, 2, mainly Component is a hollow sprue distributor box 3, as shown in figure 3, the setting length of sprue distributor box 3, height, thick direction are respectively X, Y, Z-direction.Several holes are reserved on former and later two faces of sprue distributor box 3 for anode support type SOFC battery pipe unit 1 It corresponds to across and is fitted close, so that SOFC battery pipe unit 1 is arranged in array on the surface of sprue distributor box 3, simultaneously 3 inner space of sprue distributor box is capable of forming the channel for air circulation around SOFC battery pipe unit 1.Specifically, Each anode support type SOFC battery pipe unit 1 includes anode support, electrolyte layer and cathode layer from the inside to the outside, SOFC electricity It is fuel flow channel in pond pipe unit 1, and pipe peripheral air flow passage area.
The bottom left of sprue distributor box 3 is equipped with 4 air intakes arranged along Z-direction, and 4 air intakes are all located at 1 region of SOFC battery pipe unit is with a left side.As shown in figure 4, being equipped with the sky extended along Z-direction in the lower section of air intake Gas entrance is responsible for 2-1, and the direction of sprue distributor box 3 is entered along air stream, and the caliber of air intake supervisor 2-1 is gradually reduced, Therefore pipeline section is tapered.The equidistant master for being connected with 4 reciprocation extensions in X direction on the length direction of air intake supervisor 2-1 Conduit manifold 2-2, therefore, the air of inflow air intake supervisor 2-1 flows into after can uniformly branching to 4 main pipeline manifold 2-2 Air intake flow velocity is reduced to original 1/4 by sprue distributor box 3.Specifically, main pipeline manifold 2-2 is from air intake master Pipe 2-1 starts to extend a distance into X direction first, then near reversed detour to air intake supervisor 2-1, it is unified vertically to On each air intake of sprue distributor box 3 is connected to along Y-direction, rather than be directly passed through from horizontal X direction, this is to increase Air distribution quality is advantageous between unit pipes, therefore after air can be via 4 main pipeline manifold 2-2 reductions of speed, from side-lower to uniform Low speed inputs in sprue distributor box 3.
Left sides similar in sprue distributor box 3 and air intake are gradually to be tilted to the right from the bottom to top to contract Inclined-plane, inclined degree are that the distance on lower left corner SOFC battery pipe unit 1 to 3 left side X-direction of distributor box is upper left corner SOFC Battery pipe unit 1 is conducive to increase the air velocity close to top area to 2 times of distance between 3 left side of distributor box, thus Reduce the static pressure in the region, finally make air along Y-direction evenly distribute after flow into battery-arrangements area.Sprue distributor box 3 Inner space can be divided into distribution area head 3-1, battery cell arrangement area 3-3 and distribution area tail portion 3-5 from left to right, SOFC battery pipe unit 1 is distribution area head 3-1, SOFC cell tube array with left region to the left side of sprue distributor box 3 It is distribution area tail portion 3-5 that the region at place, which is battery cell arrangement area 3-3, SOFC cell tube with right region to right side, and from The space of battery cell arrangement area 3-3 or more to 3 top surface of sprue distributor box is 3-4 at the top of distribution area.Air enters sprue After distributor box 3, since distribution area head 3-1 has the diminishing feature in space from the bottom to top, therefore air can be carried out along Y-direction Pressure regulation obtains the more uniform pressure distribution of Y-direction, and then air distributes input battery unit row with more uniform Y-Z plane Arrange area 3-3.Under normal circumstances, on the one hand, since low air utilization ratio leads to high air mass flow, on the other hand, battery list Identical permutation area 3-3 flow resistance with higher, most of air can be selected from battery cell arrangement area 3-3 or more, top Runner bypass battery cell arrangement area 3-3, so as to cause between excessively poor battery unit air distribute quality.Therefore, this reality The height that example distributes 3-4 at the top of area by narrowing, that is, the spacing of top layer SOFC battery pipe unit 1 and distributor top cover are applied, 1/3 is reduced compared to the spacing between SOFC battery pipe unit 1, increases the resistance that air passes through the fluid path, is forced more Air flows through battery cell arrangements area 3-3, and excessive air is avoided to pass through distributor box 3 by way of increasing the path flow resistance Upper edge around battery cell arrangement area 3-3 outflow, so that more air be forced to flow into battery cell arrangement area 3-3.Distribution There is area tail portion 3-5 the resistance obviously to narrow to increase feature, between most right vertical setting of types SOFC battery pipe unit 1 and distributor right side Away from reducing 1/3 compared to the spacing between SOFC battery pipe unit 1, by increasing tail portion collecting region 3-5 and battery cell arrangement The flow resistance ratio of area 3-3 forces more air to flow through battery cell arrangement area 3-3, increases air between battery unit Distribute quality.
8 offgas outlets are uniformly equipped on the right side of sprue distributor box 3, offgas outlet is divided into two column, and each column 4 Equidistant arranges along Y-direction, and the offgas outlet of top is not higher than height where top layer SOFC battery pipe unit 1.Such as Fig. 5 institute Show, each offgas outlet is correspondingly connected with an exhaust collection manifold 4-1, and the exhaust collection manifold 4-1 of same column converges into a tail The caliber of gas collecting main 4-2, exhaust collection supervisor 4-2 are gradually increased along tail gas discharge direction, therefore exhaust collection supervisor 4-2 Section from top to bottom gradually expands, and supervisor's sectional area, which is gradually increased, causes flow velocity in pipe to decline, according to Bernoulli Jacob's conservation of mechanical energy Pressure increases in equation pipe, to realize uniform air trapping amount between exhaust collection manifold 4-1.Due to main pipeline manifold 2- 23 one sections of connection distributor boxes and exhaust collection manifold 4-1 are in orthogonal orientation, and air enters distributor box 3 and outflow point Direction with case 3 is mutually perpendicular to, and promotes air to export diffusion upwards, to dextrad from entrance, the air of inflow can quickly enter electricity Between battery cell arrangements area 3-3 each unit, while entrance and exit is evenly distributed on the axial direction of battery pipe unit, therefore Air on each battery unit axial direction is uniformly abundant.
Then, as shown in fig. 6, two-way is imported directly by the exhaust collection supervisor 4-2 high hot exhaust gas collected positioned at mainstream The inlet gas heating region 5-1 of 3 lower section of road distributor box, the region are made of heat exchanger housing 5-2, inlet gas heating zone 4 main pipeline manifold 2-2 are accommodated in the inner by domain, and manifold is extended in the area fully absorbs tail gas heat quantity for heated inlet Air.
Finally, it designs, realizes under the premise of distribution outside air between battery unit and battery unit through the invention Superficial air evenly distributes, to use exploitation high performance anode support type tubular type SOFC pile to lay a good foundation.

Claims (10)

1. a kind of air distributor for anode support type tubular type SOFC battery pile, it is characterised in that: distributed including sprue Case, preformed hole is closely worn for anode support type SOFC battery pipe unit on two opposite faces before and after the sprue distributor box It crosses and is arranged in array, form air flow channel, the mainstream inside sprue distributor box and around SOFC battery pipe unit The bottom side of road distributor box is equipped with uniform air intake, and sprue distributor box is served as reasons with a side similar in air intake Under it is supreme gradually to the inclined-plane of contract, be uniformly distributed with offgas outlet, air intake on another side on the other side Air flow direction and the flow direction of offgas outlet be mutually perpendicular to.
2. the air distributor according to claim 1 for anode support type tubular type SOFC battery pile, it is characterised in that: The anode support type SOFC battery pipe unit includes anode support, electrolyte layer and cathode layer from the inside to the outside.
3. the air distributor according to claim 1 for anode support type tubular type SOFC battery pile, it is characterised in that: The orientation of the air intake is consistent with the axial direction of SOFC battery pipe unit.
4. the air distributor according to claim 1 or 3 for anode support type tubular type SOFC battery pile, feature exist It is correspondingly connected to each air intake, institute along longitudinal direction after: air branches to several main pipeline manifolds via air intake supervisor The caliber of air intake supervisor is stated as air flow direction is gradually reduced.
5. the air distributor according to claim 1 for anode support type tubular type SOFC battery pile, it is characterised in that: Offgas outlet converges into exhaust collection supervisor, the exhaust collection after being connected respectively each exhaust collection manifold transversely The caliber of supervisor is gradually increased along tail gas discharge direction.
6. being directed to the air distributor of anode support type tubular type SOFC battery pile according to claim 1 or 5, feature exists In: the offgas outlet divides the side that two longitudinal column are evenly distributed in the sprue distributor box.
7. the air distributor according to claim 4 for anode support type tubular type SOFC battery pile, it is characterised in that: The offgas outlet is finally connected to the gas heating zone for being accommodated in the inner main pipeline manifold.
8. the air distributor according to claim 7 for anode support type tubular type SOFC battery pile, it is characterised in that: The main pipeline manifold extends in gas heating zone and detour.
9. the air distributor according to claim 1 for anode support type tubular type SOFC battery pile, it is characterised in that: The top surface of the sprue distributor box more other cell tube cell spacings at a distance from top layer SOFC battery pipe unit reduce 1/3。
10. the air distributor according to claim 1 for anode support type tubular type SOFC battery pile, feature exist In: the side of the sprue distributor box where the offgas outlet with closest to more other batteries at a distance from SOFC battery pipe unit Pipe unit spacing reduces 1/3.
CN201611085745.8A 2016-12-01 2016-12-01 A kind of air distributor for anode support type tubular type SOFC battery pile Active CN106784961B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611085745.8A CN106784961B (en) 2016-12-01 2016-12-01 A kind of air distributor for anode support type tubular type SOFC battery pile

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611085745.8A CN106784961B (en) 2016-12-01 2016-12-01 A kind of air distributor for anode support type tubular type SOFC battery pile

Publications (2)

Publication Number Publication Date
CN106784961A CN106784961A (en) 2017-05-31
CN106784961B true CN106784961B (en) 2019-03-29

Family

ID=58913899

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611085745.8A Active CN106784961B (en) 2016-12-01 2016-12-01 A kind of air distributor for anode support type tubular type SOFC battery pile

Country Status (1)

Country Link
CN (1) CN106784961B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106784958B (en) * 2017-01-09 2019-04-16 江苏科技大学 A kind of fuel cell pack with-cocurrent-convection current complex optimum feature of reporting to the leadship after accomplishing a task
CN111769315B (en) * 2020-06-30 2024-07-09 国鸿氢能科技(嘉兴)股份有限公司 Fuel cell fluid manifold structure
CN114566690A (en) * 2022-02-10 2022-05-31 浙江氢邦科技有限公司 Structure for fuel gas inlet and outlet of flat tube type cell stack and manufacturing method thereof
CN116885234B (en) * 2023-07-27 2024-05-28 广东佛燃科技有限公司 Air flow distribution base suitable for multiple SOFC (solid oxide Fuel cell) pile modules
CN117174982B (en) * 2023-11-02 2024-01-23 四川荣创新能动力系统有限公司 Air in-out stack distribution structure of fuel cell and in-out stack assembly thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102170009A (en) * 2011-03-29 2011-08-31 中国华能集团清洁能源技术研究院有限公司 Solid oxide direct carbon fuel cell stack of tablet bubbling bed
EP2538481A2 (en) * 2011-06-23 2012-12-26 Honeywell International Inc. Power generator having fuel cell and membrane conduits
CN103165923A (en) * 2013-02-06 2013-06-19 中国科学院上海硅酸盐研究所 Electric collecting device of positive electrode supporting tube type battery, manufacture method thereof and battery stack
CN105810980A (en) * 2016-03-25 2016-07-27 山西大学 Assembly method for battery pile of tubular solid oxide fuel cell

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102170009A (en) * 2011-03-29 2011-08-31 中国华能集团清洁能源技术研究院有限公司 Solid oxide direct carbon fuel cell stack of tablet bubbling bed
EP2538481A2 (en) * 2011-06-23 2012-12-26 Honeywell International Inc. Power generator having fuel cell and membrane conduits
CN103165923A (en) * 2013-02-06 2013-06-19 中国科学院上海硅酸盐研究所 Electric collecting device of positive electrode supporting tube type battery, manufacture method thereof and battery stack
CN105810980A (en) * 2016-03-25 2016-07-27 山西大学 Assembly method for battery pile of tubular solid oxide fuel cell

Also Published As

Publication number Publication date
CN106784961A (en) 2017-05-31

Similar Documents

Publication Publication Date Title
CN106784961B (en) A kind of air distributor for anode support type tubular type SOFC battery pile
CN103579658B (en) A kind of liquid stream battery stack
CN106816610B (en) Proton exchange membrane fuel cell bipolar plate based on labyrinth baffle plate structure flow field
CN104916860B (en) A kind of pile group tandem arrangement based on outer air flow chamber SOFC
CN104218252B (en) Flat solid oxide fuel cell pile device
CN104821407B (en) Vein shape fuel cell flow field structure, fuel battery double plates and fuel cell
CN106997956A (en) Fluid-flow assembly and the fuel cell pile containing the fluid-flow assembly
CN102637885A (en) Cooling system and fuel cell stack
CN109004246A (en) A kind of liquid phase refrigerating module based on high power density fuel cell
CN104900942A (en) Integrated aluminum-air fuel cell system, and liquid flow and airflow control method
CN108417856A (en) It is a kind of to drain timely and conveniently fuel battery flow guiding bipolar plates and fuel cell system
CN106025309A (en) Fuel cell with spatial structural MEA (membrane electrode assembly)
CN208608303U (en) A kind of battery pole plates
CN202817106U (en) Novel flow field plate structure of proton exchange membrane fuel cell
CN107579262B (en) A kind of flat-plate-type solid-oxide fuel battery connecting component and its application
CN206711974U (en) A kind of novel flat intermediate temperature solid oxide fuel cell pile
CN220724363U (en) Buffer type flow field structure of proton exchange membrane electrolytic tank
CN104900886B (en) A kind of metal double polar plates with convection type coolant flow field
CN106784958B (en) A kind of fuel cell pack with-cocurrent-convection current complex optimum feature of reporting to the leadship after accomplishing a task
CN107482238A (en) A kind of PEM cell flow field plates with helical structure runner
CN206931655U (en) A kind of bipolar plates for increasing exchange membrane effective area
CN211743309U (en) Bipolar plate for testing power generation performance of membrane electrode of hydrogen fuel cell
CN202888318U (en) Flow cell pile with external distribution pipe
CN108550875B (en) Proton exchange membrane fuel cell flow channel
CN207504106U (en) A kind of fuel battery double plates

Legal Events

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