CN111430754A - Solid hydrogen storage waste heat recovery device for hydrogen fuel cell - Google Patents
Solid hydrogen storage waste heat recovery device for hydrogen fuel cell Download PDFInfo
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- CN111430754A CN111430754A CN202010349960.4A CN202010349960A CN111430754A CN 111430754 A CN111430754 A CN 111430754A CN 202010349960 A CN202010349960 A CN 202010349960A CN 111430754 A CN111430754 A CN 111430754A
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- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 142
- 239000001257 hydrogen Substances 0.000 title claims abstract description 142
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 139
- 238000003860 storage Methods 0.000 title claims abstract description 98
- 239000000446 fuel Substances 0.000 title claims abstract description 69
- 239000007787 solid Substances 0.000 title claims abstract description 54
- 239000002918 waste heat Substances 0.000 title claims abstract description 41
- 238000011084 recovery Methods 0.000 title claims abstract description 30
- 239000007789 gas Substances 0.000 claims abstract description 67
- 238000009826 distribution Methods 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 5
- 238000004804 winding Methods 0.000 claims description 23
- 239000000498 cooling water Substances 0.000 claims description 8
- 238000007789 sealing Methods 0.000 claims description 5
- 229910000838 Al alloy Inorganic materials 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 238000001125 extrusion Methods 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 230000008676 import Effects 0.000 claims 3
- 230000036647 reaction Effects 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 description 11
- 229910045601 alloy Inorganic materials 0.000 description 9
- 239000000956 alloy Substances 0.000 description 9
- 238000001816 cooling Methods 0.000 description 7
- 239000000110 cooling liquid Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C11/00—Use of gas-solvents or gas-sorbents in vessels
- F17C11/005—Use of gas-solvents or gas-sorbents in vessels for hydrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
-
- 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
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04029—Heat exchange using liquids
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0104—Shape cylindrical
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0302—Heat exchange with the fluid by heating
- F17C2227/0327—Heat exchange with the fluid by heating with recovery of heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0337—Heat exchange with the fluid by cooling
- F17C2227/0341—Heat exchange with the fluid by cooling using another fluid
- F17C2227/0348—Water cooling
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0369—Localisation of heat exchange in or on a vessel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0388—Localisation of heat exchange separate
- F17C2227/039—Localisation of heat exchange separate on the pipes
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- 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
- Y02E60/32—Hydrogen storage
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- 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
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- Manufacturing & Machinery (AREA)
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- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fuel Cell (AREA)
Abstract
The invention relates to a solid hydrogen storage waste heat recovery device of a hydrogen fuel cell, which comprises a solid hydrogen storage cylinder and a shell, wherein the solid hydrogen storage cylinder is arranged in the shell, the upper end of the shell is connected with a seal head, a gas distribution plate is arranged between the shell and the seal head, through holes are uniformly arranged on the gas distribution plate along the circumferential direction, a finned tube is arranged between the shell and the solid hydrogen storage cylinder, one side of the seal head is provided with a gas inlet, the gas inlet is connected with a cathode tail gas inlet connecting tube, the other side of the bottom of the shell is provided with a gas outlet, the gas outlet is connected with a cathode tail gas outlet connecting tube, the cathode tail gas inlet connecting tube is used for introducing cathode tail gas after reaction of the hydrogen fuel cell, the cathode tail gas; compared with the prior art, the invention solves the problems of complex solid-state hydrogen storage waste heat recovery structure, low waste heat recovery efficiency and unstable released hydrogen of the existing fuel cell system.
Description
[ technical field ]
The invention belongs to the field of hydrogen energy utilization, and particularly relates to a solid-state hydrogen storage waste heat recovery device for a hydrogen fuel cell.
[ background art ]
The hydrogen fuel cell system directly generates electric energy through the catalytic reaction between hydrogen and oxygen, and has the characteristics of high efficiency and environmental protection. The hydrogen fuel cell system mainly includes: the fuel cell system comprises a galvanic pile unit, an air fuel unit, a hydrogen fuel unit, a thermal management unit, a control unit and a hydrogen storage unit. The fuel cell generates a large amount of waste heat in the hydrogen energy conversion process and needs to be discharged in time. Liquid-cooled fuel cells and air-cooled cells can be classified according to the difference of refrigerants. The hydrogen storage modes of the hydrogen fuel cell include high-pressure hydrogen storage, liquid hydrogen storage and solid hydrogen storage. The solid-state hydrogen storage utilizes special alloy to release heat to absorb and store hydrogen, the hydrogen storage pressure can be as low as 1-5MPa, and the solid-state hydrogen storage has the characteristics of low hydrogenation pressure, high hydrogen storage density, high safety and wide application prospect. The hydrogen fuel required by the operation of the solid hydrogen storage fuel cell is realized by heating the solid hydrogen storage alloy to release gaseous hydrogen.
In order to improve the energy utilization efficiency and the volumetric energy density of a solid hydrogen storage fuel cell system, a technology for releasing hydrogen from waste heat of a solid hydrogen storage absorption system has been reported in related documents. For example, document 1 (fuel cell module with heat exchange and power exchange [ P ]. china: CN2563756) discloses a fuel cell system for a notebook computer, which uses the heat discharged from a host to heat a hydrogen storage unit. Document 2 (Liu Shi Xiang, Wang Cheng and Mao Zong, China: CN101118969, 2008-02-06) and document 3 (Lu Wei Zhong, research on novel air-cooled self-humidifying proton exchange membrane fuel cell technology [ D ]. Harbin engineering university) disclose a coupled hydrogen storage unit, which is characterized in that the hydrogen storage units are arranged between adjacent fuel cells at intervals in a flat plate structure, the surface of a fuel cell polar plate is contacted with the outer wall of the hydrogen storage unit, waste heat generated by the fuel cells is absorbed through a heat transfer medium, and a fan, a water pump and a refrigerant are not used. Document 4 (patent EP0917225a1) discloses an air-cooled fuel cell system, which is characterized in that air for cooling a stack to absorb heat and raise temperature is used to heat a solid hydrogen storage alloy, and hydrogen is released to supply to a hydrogen fuel cell fuel.
However, the following disadvantages exist: the hydrogen storage unit disclosed in document 1 absorbs heat from the host computer and discharges waste heat, and does not use the fuel cell system to discharge waste heat. The fuel cell coupled with the hydrogen storage unit disclosed in documents 2 and 3 has the common characteristic that the hydrogen storage unit comprises a plurality of flat-plate hydrogen storage containers which are arranged between adjacent fuel polar plates at intervals, so that the device has a complex structure and low sealing reliability, the resistance of the fuel cell is increased, and the power generation performance of the fuel cell is reduced. The solid-state hydrogen storage fuel cell waste heat recovery device disclosed in document 4 is only suitable for an air-cooled fuel cell stack, the heating medium for heating the hydrogen storage unit is air for absorbing heat and raising temperature after cooling the cell stack, and the temperature of heat dissipation air is easily affected by the ambient temperature, so that the stable operation of the hydrogen storage unit and the cell stack is not facilitated.
[ summary of the invention ]
The invention aims to solve the defects and provide a solid hydrogen storage waste heat recovery device for a hydrogen fuel cell, which solves the problems of complex solid hydrogen storage waste heat recovery structure, low waste heat recovery efficiency and unstable released hydrogen of the conventional fuel cell system.
The solid hydrogen storage waste heat recovery device comprises a solid hydrogen storage cylinder 1 and a shell 3, wherein the shell 3 is a cylinder with an open upper end, the solid hydrogen storage cylinder 1 is arranged in the shell 3, the upper end of the shell 3 is connected with a seal head 2 and is connected with the solid hydrogen storage cylinder 1 through the seal head 2 in a sealing manner, a gas distribution plate 6 is arranged between the shell 3 and the seal head 2, the gas distribution plate 6 is annular plate-shaped, through holes 8 are uniformly arranged on the gas distribution plate 6 along the circumferential direction, a finned tube 7 is arranged between the shell 3 and the solid hydrogen storage cylinder 1, the finned tube 7 is arranged below the gas distribution plate 6 and is reserved with a gap with the gas distribution plate 6, an air inlet is arranged on one side of the seal head 2 and is connected with a cathode tail gas inlet 4, and an air outlet is arranged on the other side of the bottom of the, the gas outlet is connected with a cathode tail gas outlet connecting pipe 5, the cathode tail gas inlet connecting pipe 4 is used for introducing the cathode tail gas after the reaction of the hydrogen fuel cell, the cathode tail gas flows into the end socket 2 from the cathode tail gas inlet connecting pipe 4, then flows into the finned tube 7 after being uniformly distributed through the gas distribution plate 6, and flows out from the cathode tail gas outlet connecting pipe 5 after the waste heat is released by the finned tube 7.
Further, the finned tube 7 comprises a tube body 9 and fins 10, the fins 10 are distributed on the outer wall of the tube body 9 along the axial direction and are uniformly distributed along the circumferential direction, and the tube body 9 and the fins 10 are of an integrated structure.
Further, the fin 10 extends from one end of the tube 9 to the other end of the tube 9, and is vertically disposed on the outer wall of the tube 9.
Further, the fins 10 of the finned tube 7 are assembled with the inner surface of the shell 3 in an interference fit mode, and the inner surface of the finned tube 7 is in contact with the outer surface of the solid hydrogen storage cylinder 1.
Further, the finned tube 7 is formed by one-time extrusion of aluminum alloy.
Further, the top end of the seal head 2 is connected with the shell 3 in a sealing mode, a first flange is welded at the bottom end of the seal head 2, and the first flange is connected with a second flange at the top end of the shell 3.
The invention also provides a solid hydrogen storage waste heat recovery device for the hydrogen fuel cell, which comprises a solid hydrogen storage cylinder II 11 and a heat exchange tube 13, wherein the heat exchange tube 13 is a spiral winding tube, the heat exchange tube 13 is spirally wound on the outer wall of the solid hydrogen storage cylinder II 11 and is tightly attached to the outer wall of the solid hydrogen storage cylinder II 11, one end of the heat exchange tube 13 is a spiral winding tube inlet 12, the other end of the heat exchange tube 13 is a spiral winding tube outlet 14, the spiral winding tube inlet 12 is used for introducing circulating cooling water for the hydrogen fuel cell, the circulating cooling water sequentially heats the heat exchange tube 13 and the solid hydrogen storage cylinder II 11 in a heat conduction mode after flowing in from the spiral winding tube inlet 12, and flows out from the spiral winding tube outlet 14 after releasing the waste heat.
Further, the heat exchange tube 13 is made of a stainless steel tube or a copper tube.
Compared with the prior art, the invention has the following advantages:
(1) the larger the temperature difference between the heating medium and the hydrogen storage alloy is, the more the hydrogen storage alloy is beneficial to absorbing heat, and the waste heat recovery efficiency of the hydrogen fuel cell is improved; the heating medium adopted by the waste heat recovery of the invention is the cathode tail gas of the hydrogen fuel cell, the temperature of the heating medium is close to the operation temperature of the electric pile and is about 60-80 ℃, while the heating medium adopted by the document 4 is the heat dissipation air of the electric pile, and the temperature is generally not more than 50 ℃;
(2) the heat exchange air chamber of the hydrogen storage unit has high structure compactness, the fins arranged on the finned tubes greatly increase the heat transfer area, the heat exchange with small temperature difference of 5 ℃ can be realized, and the waste heat of the fuel cell can be recovered as much as possible;
(3) the solid-state hydrogen storage waste heat recovery device for the fuel cell is realized by concentrating the outer side of the hydrogen storage cylinder, and compared with a flat-plate type fuel cell hydrogen storage unit, the solid-state hydrogen storage waste heat recovery device for the fuel cell reduces the resistance of a galvanic pile, simplifies the structure of the galvanic pile, and is easy to process, manufacture and install;
(4) the temperature of the electric pile is generally controlled to be 60-80 ℃ when the electric pile normally operates, and the flow change fluctuation of cathode gas is small; the invention adopts the battery cathode tail gas as the heating medium for the air-cooled fuel battery, thereby ensuring the stability of the hydrogen quantity absorbed and released by the hydrogen storage alloy; for the liquid cooling fuel cell, because the flow rate and the temperature change of the cooling liquid are small, the circulating cooling liquid flowing out of the cell is adopted as the heating medium, and the stability of the amount of hydrogen released by the hydrogen storage alloy is also ensured;
(5) the invention solves the problems of complex solid hydrogen storage waste heat recovery structure, low waste heat recovery efficiency, unstable hydrogen release and the like of the existing fuel cell system, and is worthy of popularization and application.
[ description of the drawings ]
FIG. 1 is a schematic structural diagram of a solid-state hydrogen storage waste heat recovery device of an air-cooled fuel cell of the present invention;
FIG. 2 is a cross-sectional view of FIG. 1;
FIG. 3 is a schematic structural view of the finned tube of FIG. 1;
FIG. 4 is a schematic diagram of the gas distribution plate of FIG. 1;
FIG. 5 is a schematic structural diagram of a solid-state hydrogen storage waste heat recovery device of a water-cooling fuel cell according to the present invention;
in the figure: 1. the device comprises a solid hydrogen storage cylinder 2, a seal head 3, a shell 4, a cathode tail gas inlet connecting pipe 5, a cathode tail gas outlet connecting pipe 6, a distribution plate 7, a finned pipe 8, a through hole 9, a pipe body 10, fins 11, a solid hydrogen storage cylinder II 12, a spiral winding pipe inlet 13, a heat exchange pipe 14 and a spiral winding pipe outlet.
[ detailed description of the invention ]
The invention is further described below with reference to the accompanying drawings:
the air cooling fuel cell adopts hydrogen fuel cell cathode tail gas as heating medium to heat the solid hydrogen storage cylinder, the operation temperature of the fuel electric pile is controlled between 60 ℃ and 80 ℃, and the temperature of the cathode tail gas is correspondingly controlled between 60 ℃ and 80 ℃. As shown in attached figures 1 and 2, the solid hydrogen storage waste heat recovery device of the air-cooled fuel cell comprises a solid hydrogen storage cylinder 1, a seal head 2, a shell 3, a cathode tail gas inlet connecting pipe 4, a cathode tail gas outlet connecting pipe 5, a gas distribution plate 6 and a finned tube 7, wherein the shell 3 is a cylinder with an open upper end, the solid hydrogen storage cylinder 1 is arranged in the shell 3, the upper end of the shell 3 is connected with the seal head 2 and is hermetically connected with the solid hydrogen storage cylinder 1 through the seal head 2, the gas distribution plate 6 is arranged between the shell 3 and the seal head 2, the gas distribution plate 6 is in an annular plate shape, through holes 8 are uniformly arranged on the gas distribution plate 6 along the circumferential direction, the finned tube 7 is arranged between the shell 3 and the solid hydrogen storage cylinder 1, the finned tube 7 is arranged below the gas distribution plate 6 and is reserved with a gap between the finned tube, the other side of the bottom of the shell 3 is provided with an air outlet which is connected with a cathode tail gas outlet connecting pipe 5, a cathode tail gas inlet connecting pipe 4 is used for introducing cathode tail gas after reaction of the hydrogen fuel cell, the cathode tail gas flows into the seal head 2 from the cathode tail gas inlet connecting pipe 4 and then flows into the finned tube 7 after flowing through the gas distribution plate 6 and being uniformly distributed, temperature difference exists between the cathode tail gas and the fin of the finned tube 7, heat sequentially heats the metal finned tube 7, the solid hydrogen storage cylinder 1 and hydrogen storage alloy in the solid hydrogen storage cylinder 1 through a heat conduction mode so as to release hydrogen, and the cathode tail gas flows out from the cathode.
The top end of the seal head 2 is hermetically connected with the shell 3, and the bottom end of the seal head 2 is welded with a first flange and is connected with a second flange at the top end of the shell 3 through the first flange. The finned tube 7 comprises a tube body 9 and fins 10, the fins 10 are axially distributed on the outer wall of the tube body 9 and are uniformly distributed along the circumferential direction, and the tube body 9 and the fins 10 are of an integrated structure; the fins 10 extend from one end of the tube 9 to the other end of the tube 9, and are vertically arranged on the outer wall of the tube 9. The fins 10 of the finned tube 7 are assembled with the inner surface of the shell 3 in an interference fit manner so as to ensure that the inner surface of the shell 3 is effectively and fully contacted with fin tips of the fins of the finned tube 7, thereby preventing gas from flowing through gaps between the fins 10 and the inner surface of the shell 3 and taking away heat; the inner surface of the finned tube 7 is fully contacted with the outer surface of the solid hydrogen storage cylinder 1 so as to ensure that the finned tube 7 effectively heats the solid hydrogen storage cylinder 1; the finned tube 7 is made of aluminum alloy, and the finned tube 7 is formed by one-time extrusion of aluminum alloy; a gap is reserved between the bottom end of the finned tube 7 and the bottom end of the solid hydrogen storage cylinder 1, the cathode tail gas outlet connecting tube 5 is arranged at the gap, and a gap is reserved between the bottom end of the solid hydrogen storage cylinder 1 and the bottom end of the shell 3 so as to ensure that the cathode tail gas can uniformly flow out of the cathode tail gas outlet connecting tube 5 after the residual heat is released.
In the invention, the liquid cooling fuel cell mostly adopts circulating cooling water as a heating medium to heat the solid hydrogen storage cylinder II 11, as shown in the attached figure 5, the liquid-cooled fuel cell solid hydrogen storage waste heat recovery device comprises a solid hydrogen storage cylinder II 11 and a heat exchange tube 13, the heat exchange tube 13 is a spiral winding tube, the heat exchange tube 13 is made of stainless steel tube, copper tube and the like, the heat exchange tube 13 is spirally wound on the outer wall of the solid hydrogen storage cylinder II 11, and clinging to the outer wall of the solid hydrogen storage cylinder II 11, one end of the heat exchange tube 13 is a spiral winding tube inlet 12, the other end of the heat exchange tube 13 is a spiral winding tube outlet 14, the spiral winding tube inlet 12 is used for introducing circulating cooling water of the hydrogen fuel cell, after the circulating cooling water flows in from the spiral winding tube inlet 12, the heat exchange tube 13 and the solid hydrogen storage cylinder II 11 are sequentially heated in a heat conduction mode until the waste heat is released and then flows out from the spiral winding tube outlet 14. Namely, the circulating cooling liquid after cooling the fuel cell flows into the spiral winding pipe inlet 12 of the heat exchange pipe 13, and the circulating cooling water sequentially heats the heat exchange pipe 13 and the solid hydrogen storage cylinder II 11 in a heat conduction mode until the heat is absorbed by the hydrogen storage alloy, releases hydrogen, flows out from the spiral winding pipe outlet 14 of the heat exchange pipe 13 and is used as the circulating cooling liquid to continuously cool the fuel cell.
The present invention is not limited to the above embodiments, and any other changes, modifications, substitutions, combinations, and simplifications which do not depart from the spirit and principle of the present invention should be construed as equivalents and are included in the scope of the present invention.
Claims (8)
1. The utility model provides a solid-state hydrogen storage waste heat recovery device of hydrogen fuel cell which characterized in that: including solid-state hydrogen storage cylinder (1) and casing (3), casing (3) are the open cylinder in upper end, casing (3) are arranged in to solid-state hydrogen storage cylinder (1), casing (3) upper end is connected with head (2) to through sealing connection between head (2) and solid-state hydrogen storage cylinder (1), be provided with gas distribution plate (6) between casing (3) and head (2), gas distribution plate (6) are the annular plate form, through-hole (8) have evenly been arranged along circumference on gas distribution plate (6), be provided with finned tube (7) between casing (3) and solid-state hydrogen storage cylinder (1), finned tube (7) set up in gas distribution plate (6) below, and with gas distribution plate (6) between reserve the space, the air inlet has been seted up to head (2) one side, cathode tail gas import takeover (4) is connected to the air inlet, the gas outlet has been seted up to casing (3) bottom opposite side, cathode tail gas outlet takeover (5) is connected to the gas outlet, cathode tail gas import takeover (4) are used for letting in hydrogen fuel cell reaction back cathode tail gas, cathode tail gas flows into finned tube (7) after gas distribution board (6) evenly distributed after flowing into head (2) from cathode tail gas import takeover (4) to flow out from cathode tail gas outlet takeover (5) after finned tube (7) release waste heat.
2. The solid state hydrogen storage waste heat recovery device of a hydrogen fuel cell according to claim 1, characterized in that: the finned tube (7) comprises a tube body (9) and fins (10), the fins (10) are axially distributed on the outer wall of the tube body (9) and are uniformly arranged along the circumferential direction, and the tube body (9) and the fins (10) are of an integrated structure.
3. The solid state hydrogen storage waste heat recovery device of a hydrogen fuel cell according to claim 2, characterized in that: fin (10) extend to the body (9) other end from body (9) one end, and are vertical form setting on body (9) outer wall.
4. The solid state hydrogen storage waste heat recovery device of a hydrogen fuel cell according to claim 1, 2 or 3, characterized in that: the fin (10) of the finned tube (7) is assembled with the inner surface of the shell (3) in an interference fit mode, and the inner surface of the finned tube (7) is in contact with the outer surface of the solid hydrogen storage cylinder (1).
5. The solid state hydrogen storage waste heat recovery device of a hydrogen fuel cell according to claim 1, 2 or 3, characterized in that: the finned tube (7) is formed by one-time extrusion of aluminum alloy.
6. The solid state hydrogen storage waste heat recovery device of a hydrogen fuel cell according to claim 1, 2 or 3, characterized in that: the top end of the seal head (2) is connected with the shell (3) in a sealing mode, a first flange is welded at the bottom end of the seal head (2), and the first flange is connected with a second flange at the top end of the shell (3).
7. The utility model provides a solid-state hydrogen storage waste heat recovery device of hydrogen fuel cell which characterized in that: including solid-state hydrogen storage cylinder two (11) and heat exchange tube (13), heat exchange tube (13) are spiral winding pipe, heat exchange tube (13) adopt spiral winding in solid-state hydrogen storage cylinder two (11) outer wall, and hug closely with solid-state hydrogen storage cylinder two (11) outer wall, heat exchange tube (13) one end is spiral winding pipe entry (12), heat exchange tube (13) other end is spiral winding pipe export (14), spiral winding pipe entry (12) are used for letting in hydrogen fuel cell recirculated cooling water, recirculated cooling water flows in the back from spiral winding pipe entry (12), heats heat exchange tube (13), solid-state hydrogen storage cylinder two (11) in proper order through the heat conduction mode, flows from spiral winding pipe export (14) after releasing the waste heat.
8. The solid state hydrogen storage waste heat recovery device of a hydrogen fuel cell according to claim 7, characterized in that: the heat exchange tube (13) is made of a stainless steel tube or a copper tube.
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CN114484275A (en) * | 2022-01-26 | 2022-05-13 | 海南天宇科技集团有限公司 | Hydrogen storage bottle integration frame with high-efficient heat transfer function |
CN114614043A (en) * | 2022-03-21 | 2022-06-10 | 天津新氢动力科技有限公司 | Slow-release capsule type metal solid hydrogen storage fuel cell system |
CN114883589A (en) * | 2022-05-24 | 2022-08-09 | 江苏科技大学 | Waste heat recycling device for hydrogen fuel cell power ship |
CN114976118A (en) * | 2022-07-29 | 2022-08-30 | 河南新飞电器集团有限公司 | Power device of hydrogen fuel cell new energy special vehicle |
US11913733B2 (en) | 2020-06-12 | 2024-02-27 | Asia Pacific Fuel Cell Technologies, Ltd. | Heat transferring device and heat transferring component thereof |
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