CN214203744U - Electrode frame and diaphragm or bipolar plate integrated assembly - Google Patents
Electrode frame and diaphragm or bipolar plate integrated assembly Download PDFInfo
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- CN214203744U CN214203744U CN202022973281.2U CN202022973281U CN214203744U CN 214203744 U CN214203744 U CN 214203744U CN 202022973281 U CN202022973281 U CN 202022973281U CN 214203744 U CN214203744 U CN 214203744U
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- 239000003792 electrolyte Substances 0.000 claims abstract description 55
- 238000009826 distribution Methods 0.000 claims abstract description 14
- 238000003466 welding Methods 0.000 claims abstract description 12
- 238000007789 sealing Methods 0.000 claims description 4
- 229920001971 elastomer Polymers 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 2
- 239000000853 adhesive Substances 0.000 claims 1
- 230000001070 adhesive effect Effects 0.000 claims 1
- 230000006835 compression Effects 0.000 abstract description 3
- 238000007906 compression Methods 0.000 abstract description 3
- 239000008151 electrolyte solution Substances 0.000 abstract 1
- 239000012528 membrane Substances 0.000 description 11
- 230000002093 peripheral effect Effects 0.000 description 7
- 238000012360 testing method Methods 0.000 description 5
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000004146 energy storage Methods 0.000 description 4
- 229910001416 lithium ion Inorganic materials 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000004891 communication Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 238000010008 shearing Methods 0.000 description 2
- 206010000369 Accident Diseases 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012983 electrochemical energy storage Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229920001973 fluoroelastomer Polymers 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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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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Abstract
本实用新型涉及一种电极框与隔膜或双极板的一体组件。电极框为平板结构，电极框中间区域设置有凹槽，凹槽内设置有双极板或隔膜，并嵌入凹槽中。双极板或隔膜与凹槽上的环形平台之间为焊接或者粘接密封。凹槽内、双极板或隔膜两侧设置有电极。电极框上设置有正极或负极电解液流进出口，电解液进出口与电极之间通过分配流道凹槽相连通。在分配流道上设置有容纳盖片的凹槽，盖片上设置有流道凸台并与分配流道一起组成闭合流道。通过该结构来均匀电解液的分配。在电极框凹槽上设置有可以置于凹槽内的环状盖片，其与凹槽的环形平台位于双极板或隔膜两侧，它们于双极板或隔膜一侧表面的投影相重合。消除了电极压缩对双极板或隔膜厚度方向上的剪切力。
The utility model relates to an integrated assembly of an electrode frame, a diaphragm or a bipolar plate. The electrode frame is a flat plate structure, a groove is arranged in the middle area of the electrode frame, a bipolar plate or a diaphragm is arranged in the groove, and is embedded in the groove. The bipolar plate or diaphragm and the annular platform on the groove are sealed by welding or bonding. Electrodes are arranged in the groove, on both sides of the bipolar plate or the diaphragm. The electrode frame is provided with a positive or negative electrolyte inlet and outlet, and the electrolyte inlet and outlet are communicated with the electrodes through a distribution channel groove. The distribution flow channel is provided with a groove for accommodating a cover sheet, and the cover sheet is provided with a flow channel boss and forms a closed flow channel together with the distribution flow channel. With this structure, the distribution of the electrolyte solution is uniform. An annular cover sheet that can be placed in the groove is arranged on the groove of the electrode frame, and the annular platform of the groove is located on both sides of the bipolar plate or diaphragm, and their projections on one side of the bipolar plate or diaphragm coincide . Shear force in the thickness direction of the bipolar plate or diaphragm due to electrode compression is eliminated.
Description
Technical Field
The utility model relates to a flow battery structure, in particular to an electrode frame and diaphragm or bipolar plate's integrative subassembly among the flow battery.
Background
With the massive construction of renewable energy infrastructure, more and more wind energy and solar energy face the problem of grid-connected power-on. Due to the characteristics of instability and discontinuity of wind energy and solar energy, the grid connection can generate great impact on a power grid, and particularly, the influence caused by new energy grid connection is increasingly severe at present when renewable energy is rapidly developed. In order to solve the problem of renewable energy grid connection, intermediate equipment capable of smoothing renewable energy electric energy output and cutting wind and filling valley is needed to improve the electric energy quality and increase the grid connection time of renewable energy. Energy storage techniques have been developed, and among the numerous energy storage techniques, electrochemical energy storage has made great progress. At present, the lithium ion battery with the largest installed capacity is easy to expand during system design by virtue of the advantages of complete lithium ion battery industry chain and high energy density. But currently, potential safety hazards exist: firstly, hundreds of megawatt energy storage power stations need tens of thousands of lithium ion batteries, the management system of the batteries is complex, and the working state of each battery needs to be considered to avoid short circuit and fire; secondly, such a large number of batteries, the cooling design is especially important, and the fire accident caused by local overheating is strictly avoided. Once a lithium ion battery is on fire, its destructiveness and resulting loss are enormous. Therefore, in recent years, a flow battery which is safer, more reliable and easier to manage is gradually developed, has the outstanding advantages of high cycle efficiency, long cycle life, completely independent design of capacity and power, high cost performance and high safety, and is becoming the first choice of a large-scale energy storage technology.
The flow cell stack is generally assembled in the form of a filter press. Two ends of the electric pile adopt steel or aluminum metal end plates, and the internal current collecting plate, the multiple sections of single cells connected in series and the sealing material are fastened together through metal screws. The monocell comprises a negative bipolar plate, a negative electrode frame, a negative electrode, a diaphragm, a positive electrode frame and a positive bipolar plate. The electrode frame is an important component for organizing the flowing of electrolyte and placing the electrode, and the conversion of electric energy and chemical energy occurs at the same time, so that the key for improving the performance and reliability of the galvanic pile when designing the electrode frame structure with high efficiency and high reliability is realized. The electrode frame is provided with a distribution flow channel and a flow channel cover plate in a flow guide groove which is communicated with the electrode through the anode or cathode electrolyte inlet through hole or the outlet through hole on the electrode frame, so that the purpose of uniformly distributing the electrolyte to flow into and out of the electrode is achieved, and the concentration polarization of the battery is reduced. The runner opening typically contacts the electrode edge directly. Under the condition of welding or bonding process, an annular groove is arranged at the outer edge of a cavity of the electrode frame for placing the electrode, and is used for welding or bonding the diaphragm or the bipolar plate. The electrode frame adopting the welding or bonding structure has the problems in the process of assembling the galvanic pile: the diaphragm or the bipolar plate is welded or bonded in the groove, and the two sides are respectively provided with an electrode. Due to the existence of the groove, the areas of the electrodes on the two sides are different, and the area difference is equal to the area of the annular groove. This causes the electrodes to generate a thickness-direction shear force on the membrane or the plate when compressed, reducing the reliability of the stack.
SUMMERY OF THE UTILITY MODEL
For eliminating above-mentioned electrode frame welding or adhesive bonding structure to the shearing force of membrane or bipolar plate thickness direction, the utility model provides a liquid flow battery electrode frame and diaphragm or bipolar plate's an organic whole subassembly uses this subassembly can improve the reliability of galvanic pile.
The electrode frame and the diaphragm or the bipolar plate are integrated, wherein the electrode frame is of a flat plate structure, a groove A is formed in the surface of one side of the flat plate, a through hole a penetrating through the surface of the other side of the flat plate is formed in the middle of the bottom surface of the groove A, and a space l is reserved between the opening edge of the bottom surface of the groove A and the peripheral edge of the bottom surface of the groove A through the through hole, so that an annular platform area with the width of l is formed. The diaphragm or the bipolar plate is arranged in the groove A, and the peripheral edge of the diaphragm or the bipolar plate is in sealing connection with the annular platform area at the bottom surface of the groove A. Four through holes are arranged at the peripheral edge of the electrode frame and respectively used as an anode electrolyte inlet and outlet and a cathode electrolyte inlet and outlet. And a groove B serving as an electrolyte distribution flow channel is arranged between the anode electrolyte inlet/outlet or the cathode electrolyte inlet/outlet and the groove A, and the groove B is used for communicating the anode electrolyte inlet/outlet or the cathode electrolyte inlet/outlet and the groove A.
The integrated component also comprises an annular cover plate C with the width of l, the annular cover plate C is arranged in the groove A, the annular cover plate C and the annular platform area are respectively arranged oppositely at two sides of the diaphragm or the bipolar plate, and the projections of the annular cover plate C and the annular platform area on one side surface of the diaphragm or the bipolar plate are coincided. And a cover plate D for covering the opening end of the groove B is arranged at the opening end of the groove B, and one end of the cover plate D is connected with the annular cover plate C. The surface of one side of the annular cover plate C close to the cover plate D, which faces the diaphragm or the bipolar plate, is provided with a flow guide groove which penetrates through the inner wall surface and the outer wall surface of the annular cover plate C, and/or the annular cover plate C close to the cover plate D is provided with a flow guide through hole which penetrates through the inner wall surface and the outer wall surface of the annular cover plate A. The groove B is communicated with the flow guide groove and/or the flow guide through hole.
In the above-mentioned integrative subassembly, electrolyte flows in recess B, is equipped with along the water conservancy diversion lug boss of electrolyte flow direction in cover plate D towards recess B's one side surface middle part.
The integrated component adopts welding seal, bonding seal or rubber compression seal between the diaphragm or bipolar plate arranged between the groove A and the annular cover plate C and the annular platform area with the peripheral edge width of l of the groove A.
In the integrated assembly, an electrode is arranged in the through hole a and close to one side of the diaphragm or the bipolar plate.
The electrode frame and the diaphragm or the bipolar plate are integrally assembled and applied to the flow battery.
The utility model has the advantages of as follows: the improved cover plate with the flow channel structure ensures that the shapes of the electrodes arranged on the two sides of the bipolar plate or the ion conduction membrane are completely the same, eliminates the shearing force of electrode compression on the bipolar plate or the ion conduction membrane in the thickness direction, and improves the reliability of the galvanic pile;
drawings
FIG. 1 is a schematic diagram of the assembly of a flow cell electrode frame, a bipolar plate or membrane and a flow channel cover plate in a welded or bonded structure, which are welded or bonded as an integral assembly;
wherein 1, the electrode frame is provided with a distribution flow channel structure; 2. a bipolar plate or membrane; 3. the electrolyte flows into the cover plate on the communicating pipeline between the through hole and the electrode; 4. a cover plate on the communicating pipeline between the electrolyte outflow through hole and the electrode; 11. a cavity for accommodating the electrode in the electrode frame with a distribution flow channel structure; 12. the electrode frame with the distribution flow channel structure is provided with a groove for welding or bonding; 13. the positive electrode (or negative electrode) electrolyte inlet through hole of the electrode frame with the distribution flow channel structure; 14. the positive electrode (or negative electrode) electrolyte outlet through hole of the electrode frame with the distribution flow channel structure; 15. a communicating groove (provided with an electrolyte diversion boss and a diversion groove) between the electrolyte inlet through hole of the anode (or the cathode) and the electrode; 16. and a communicating groove (provided with an electrolyte diversion boss and a diversion groove) between the electrolyte outlet through hole of the positive electrode (or the negative electrode) and the electrode.
Fig. 2 is an integrated assembly provided by the present invention, which includes an electrode frame, a cover plate with a flow guiding protrusion and a flow guiding groove, a bipolar plate or a diaphragm. Schematic diagram of the fit between them;
5, the utility model provides an electrode frame structure; 6. the cover plate is matched with the electrode frame and is provided with a flow guide boss and a flow guide groove; 51. the utility model provides a cavity for accommodating an electrode in an electrode frame structure; 52. the utility model provides a groove A for welding or bonding in an electrode frame structure; 53. the utility model provides a positive (or negative) electrolyte inlet through hole in an electrode frame structure; 54. the utility model provides an anode (or cathode) electrolyte outlet through hole in an electrode frame structure; 55. a communicating groove B1 between the positive (or negative) electrolyte inlet through hole and the electrode; 56. communication groove B2 between the positive (or negative) electrolyte outlet through hole and the electrode;
FIG. 3 is a view showing a cover plate with a flow guiding boss and a flow guiding groove, which is used in cooperation with an electrode frame, in an integrated assembly provided by the present invention;
61, a cavity for accommodating the electrode is arranged in an annular cover plate which is matched with the electrode frame and is provided with a flow guide boss and a flow guide groove; 62. the electrolyte cooperating with 53 flows into the through hole; 63. an electrolyte outflow through hole cooperating with 54; 64. a boss and a groove (embedded in 55 a flow guide channel) with a flow guide function; 65. boss and groove with flow guiding function (Embedded 56 flow guiding channel)
FIG. 4 is a final assembled view of the structure of FIG. 3;
fig. 5 is a graph of multi-cycle coulombic efficiency, voltage efficiency, and energy efficiency for a stack assembled using the structure of fig. 2.
Detailed Description
Example (b):
fig. 1 is a schematic diagram of the conventional flow cell electrode frame, bipolar plate or diaphragm and flow channel cover plate in welded or bonded structure, which are integrated into one assembly. The bipolar plates or separator are embedded in grooves 12 of the electrode frame for welding or bonding. The cover plate 3 on the communicating groove between the electrolyte inlet through hole and the electrode is arranged in the cover plate groove on the communicating groove 15 between the electrolyte inlet through hole and the electrode; the cover plate 4 on the communicating groove between the electrolyte outlet through hole and the electrode is placed in the cover plate groove on the communicating groove 16 between the electrolyte outlet through hole and the electrode. It can be seen that the electrode areas arranged on both sides of the bipolar plate or membrane 2 differ, since the groove 12 for welding or bonding occupies a small area of the outer edge on the bipolar plate or membrane 2. During the assembly of the stack, the electrodes on both sides of the bipolar plate or membrane 2 are compressed and shear forces in the thickness direction of the bipolar plate or membrane are generated at the interface of the groove 12 and the electrode edge, and the bipolar plate or membrane risks to be sheared off after the stack is operated for a long time.
Fig. 2 is an integrated assembly of an electrode frame and a diaphragm or a bipolar plate, which comprises a plate-structured electrode frame 5, a matched annular cover plate 6 with a flow guide boss and a flow guide groove, and a bipolar plate or a diaphragm 2.
The electrode frame 5 is of a flat plate structure, a groove A (52) is formed in the surface of one side of the flat plate, a through hole a (51) penetrating to the surface of the other side of the flat plate is formed in the middle of the bottom surface of the groove A (52), a space l is reserved between the opening edge of the bottom surface of the groove A (52) and the peripheral edge of the bottom surface of the groove A (52) of the through hole a (51), an annular platform area with the width of l is formed, and l belongs to (1-20mm), 8mm is selected in the embodiment.
Placing the diaphragm or bipolar plate 2 in the groove A (52), wherein the peripheral edge of the diaphragm or bipolar plate is required to be in sealing connection with the annular platform area at the bottom surface of the groove A (52);
four through holes are arranged at the edges of the periphery of the electrode frame 5, wherein: 53. the utility model provides a positive (or negative) electrolyte inlet through hole in an electrode frame structure; 54. the utility model provides a positive pole (or negative pole) electrolyte export through-hole among electrode frame structure. The other two through holes are a cathode (or anode) electrolyte inlet through hole and an outlet through hole;
a groove B1(55) serving as an electrolyte distribution flow channel is arranged between the positive electrode (or negative electrode) electrolyte inlet through hole 53 and the groove A (52); a groove B2(56) serving as an electrolyte distribution flow channel is arranged between the anode (or cathode) electrolyte outlet through hole 54 and the groove A (52), and the groove B1(55) and the groove B2(56) communicate the anode (or cathode) electrolyte inlet and outlet with the groove A;
also included in the integral assembly is a ring-shaped flap C of width l (which is a rectangular closure in the ring-shaped flap 6), as shown in figure 3. The annular cover plate C is arranged in the groove A (52), the annular cover plate C and the annular platform area are respectively arranged on two sides of the diaphragm or the bipolar plate oppositely, and the projections of the annular cover plate C and the annular platform area on one side surface of the diaphragm or the bipolar plate are coincided.
A cover D (a branch except a rectangular closed part in the cover 6) for covering the opening ends of the groove B1(55) and the groove B2(56) is arranged at the opening end of a communication groove B1(55) between the anode (or cathode) electrolyte inlet through hole and the electrode and a communication groove B2(56) between the anode (or cathode) electrolyte outlet through hole and the electrode, and one end of the cover D is connected with an annular cover C to jointly form the cover 6. The surface of one side of the annular cover plate C close to the cover plate D, which faces the diaphragm or the bipolar plate, is provided with flow guide grooves 64 and 65 which penetrate through the inner wall surface and the outer wall surface of the annular cover plate C, and the groove B1(55) is communicated with the flow guide groove 64; the groove B2(56) communicates with the guide groove 65.
Electrolyte flows in the grooves B1(55) and B2(56), and a flow guide boss along the flowing direction of the electrolyte is arranged in the middle of one side surface of the cover plate D facing the grooves B1(55) and B2 (56).
The schematic diagram of the matching among the electrode frame 5 with a flat plate structure, the matched annular cover plate 6 with the flow guide bosses and the flow guide grooves and the bipolar plate or the diaphragm 2 is shown in figure 2. The three components are assembled together to form an integral structure as shown in fig. 4. The diaphragm or the bipolar plate 2 is arranged between the groove A (52) and the annular cover plate C, and the diaphragm or the bipolar plate 2 and the annular platform area with the peripheral edge width of l of the groove A (52) are sealed by welding, bonding or rubber pressing. In the through hole a (51), an electrode is provided on the side close to the separator or the bipolar plate.
As can be seen in fig. 4, the electrodes disposed on both sides of the separator or bipolar plate have the same shape, eliminating the influence of shear force and improving the reliability of the stack.
The performance and life test data for the stacks assembled using the two configurations of fig. 1 and 2 are compared, as shown in table 1. The galvanic pile is composed of 25 batteries, 4.35mm carbon felt is used as an electrode, and the self-made weldable diaphragm, the weldable bipolar plate and the fluororubber sealing gasket are assembled. The area of the electrode of the galvanic pile assembled by adopting the structure of the figure 1 is 940cm2 based on the smaller area of the electrodes at two sides of the electrode 2; the electrode area of the electric pile assembled by adopting the structure of FIG. 2 is also 940cm2. The electric pile adopts constant power 4kW to carry out charge-discharge test initial performance.
Table 1 performance data of a cell stack assembled using the two configurations of fig. 1 and 2
As can be seen from table 1, the structural improvement of the electrode frame and the flow channel cover plate does not have a negative effect on the performance of the stack, and the performance stability of the stack is slightly improved. The feasibility of the structure was demonstrated. And simultaneously, testing the performance life of the two galvanic piles, and respectively carrying out charge and discharge tests by adopting 4kW and 5kW variable power, wherein each cycle of charge and discharge is about 1 h. The electric pile adopting the structure of the figure 1 has sudden internal leakage only after about 340 cycles of testing, and the electrolyte is completely transferred into the electrolyte barrel on one side; the performance is still stable when the electric pile adopting the structure of the figure 2 is tested for more than 1400 cycles. The relationship between the efficiency and the charge-discharge cycle is shown in fig. 5. The result proves the utility model provides an electrode frame and supporting runner apron structure can show the reliability that promotes the pile.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022973281.2U CN214203744U (en) | 2020-12-11 | 2020-12-11 | Electrode frame and diaphragm or bipolar plate integrated assembly |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202022973281.2U CN214203744U (en) | 2020-12-11 | 2020-12-11 | Electrode frame and diaphragm or bipolar plate integrated assembly |
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| CN214203744U true CN214203744U (en) | 2021-09-14 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114150337A (en) * | 2021-11-01 | 2022-03-08 | 山东海氢能源科技有限公司 | Electrolytic tank frame with bipolar plates, electrolytic unit and electrolytic equipment |
| CN114622230A (en) * | 2022-03-29 | 2022-06-14 | 嘉庚创新实验室 | Electrochemical reaction apparatus and electrochemical device thereof |
| CN114628720A (en) * | 2020-12-11 | 2022-06-14 | 中国科学院大连化学物理研究所 | An integrated assembly of electrode frame and diaphragm or bipolar plate and its application |
-
2020
- 2020-12-11 CN CN202022973281.2U patent/CN214203744U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114628720A (en) * | 2020-12-11 | 2022-06-14 | 中国科学院大连化学物理研究所 | An integrated assembly of electrode frame and diaphragm or bipolar plate and its application |
| CN114628720B (en) * | 2020-12-11 | 2024-09-20 | 中国科学院大连化学物理研究所 | Integrated assembly of electrode frame and diaphragm or bipolar plate and application thereof |
| CN114150337A (en) * | 2021-11-01 | 2022-03-08 | 山东海氢能源科技有限公司 | Electrolytic tank frame with bipolar plates, electrolytic unit and electrolytic equipment |
| CN114622230A (en) * | 2022-03-29 | 2022-06-14 | 嘉庚创新实验室 | Electrochemical reaction apparatus and electrochemical device thereof |
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