CN219286456U - Connector of high-temperature solid oxide electrolytic cell pile - Google Patents
Connector of high-temperature solid oxide electrolytic cell pile Download PDFInfo
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- CN219286456U CN219286456U CN202223596683.0U CN202223596683U CN219286456U CN 219286456 U CN219286456 U CN 219286456U CN 202223596683 U CN202223596683 U CN 202223596683U CN 219286456 U CN219286456 U CN 219286456U
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Abstract
The utility model discloses a connector of a high-temperature solid oxide electrolytic cell pile, which comprises a connector body, wherein a plurality of air channels are formed in the upper surface of the connector body at equal intervals, a plurality of hydrogen channels are formed in the lower surface of the connector body at equal intervals, the air channels and the hydrogen channels are arranged in a crossing manner, and a gas inlet and a gas outlet penetrating through the connector body are formed in the connector body. The utility model realizes that the air flow channel and the hydrogen flow channel are arranged alternately on the upper surface and the lower surface of the connector body through the cooperation of the structures, the air flow channel is arranged along the width of the connector body, the hydrogen flow channel is arranged along the length direction of the connector body, the air flow channel is open at the side (to the side surface of the connector), the hydrogen flow channel is open to the gas inlet and outlet, the whole structure of the connector is simple in design, easy to produce and manufacture, the effective area of the battery can be utilized to the greatest extent, and the utilization rate of gas is improved.
Description
Technical Field
The utility model relates to the technical field of solid oxide electrolytic cell stacks, in particular to a connector of a high-temperature solid oxide electrolytic cell stack.
Background
High temperature solid oxide cells (solid oxide electrolysis cell, SOEC) are considered to be one of the most efficient energy conversion and storage devices.
The flat plate type high temperature solid oxide electrolytic cell stack is generally formed by stacking a plurality of electrolytic cell units in series, and in order to separate hydrogen and oxygen generated between two adjacent electrolytic cells, a separator is required to be placed between two cells, and simultaneously, the cathode of one cell and the anode of the other cell are connected, and the separator is called a connector. The connector serves as one of the key components in the high temperature solid oxide cell stack, which functions to transport electrons between adjacent single cell units and to divide the cathode side and anode side gases. The gas flow distribution device can distribute gas flow in and out, provide a channel for gas to flow on two sides, output gas on the cathode side and gas on the anode side, participate in electrochemical reaction, remove products of the electrochemical reaction and ensure that the electrochemical reaction is continuously carried out.
The gas inlet and outlet on the existing connector are generally designed by uniformly distributing a plurality of small holes, and the design of the small holes increases the processing procedure, improves the processing cost of the connector, and the gas flow channel is not directly communicated with the gas inlet and outlet, so that the gas inlet and outlet efficiency is low, and the gas utilization rate and the electrochemical reaction rate are reduced. And the design causes the design of other parts in the pile such as sealing elements and the like to be complex, thereby improving the production cost of the whole pile. In order to solve the above problems, we propose a connector for a high temperature solid oxide cell stack.
Disclosure of Invention
The utility model aims to provide a connector of a high-temperature solid oxide electrolytic cell pile, which is provided with an air flow channel and a hydrogen flow channel which are arranged on the upper surface and the lower surface of a connector body in a crossing way, wherein the air flow channel is open at the side (opened to the end part of the connector body), the hydrogen flow channel is opened to a gas inlet and a gas outlet, the effective area of a cell is utilized to the greatest extent, the gas utilization rate is improved, and the problems in the background technology are solved.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a connector of high temperature solid oxide electrolytic cell pile, includes the connector body, a plurality of air current way has been seted up to the equidistant upper surface of connector body, a plurality of hydrogen runner has been seted up to the equidistant lower surface of connector body, and air current way and hydrogen runner alternately set up, gas inlet and the gas outlet of running through the connector body have been seted up on the connector body, the hydrogen runner is located between gas inlet and the gas outlet.
Preferably, the air flow channels are distributed on the connector body along the width direction of the connector body.
Preferably, the length of the air flow channel is equal to the width of the connector body.
Preferably, the air flow passage and the hydrogen flow passage do not penetrate the connector body up and down.
Preferably, the air flow channel and the hydrogen flow channel are not communicated up and down.
Preferably, the hydrogen flow channels are distributed on the connector body along the length direction of the connector body.
Preferably, the number of the gas inlets and the number of the gas outlets are two.
Preferably, the gas inlet and the gas outlet are symmetrically distributed on the connector body.
Preferably, two ends of the hydrogen flow channel are respectively communicated with the gas inlet and the gas outlet.
Preferably, the air flow channel and the hydrogen flow channel have the same width.
Compared with the prior art, the utility model has the beneficial effects that: the air flow channel and the hydrogen flow channel are arranged on the upper surface and the lower surface of the connector body in a crossing way, the air flow channel is arranged along the width of the connector body, the hydrogen flow channel is arranged along the length direction of the connector body, the air flow channel is open at the side (to the side surface of the connector body), the hydrogen flow channel is open to the gas inlet and outlet, the whole connector is simple in design, easy to produce and manufacture, the effective area of the battery is utilized to the greatest extent, and the gas utilization rate is improved.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
fig. 2 is a schematic view of the bottom view structure of the present utility model.
In the figure: 1. a connector body; 2. an air flow passage; 3. a hydrogen flow passage; 4. a gas inlet; 5. and a gas outlet.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1 to 2, the present utility model provides a technical solution: the utility model provides a connector of high temperature solid oxide electrolytic cell pile, includes connector body 1, and a plurality of air current way 2 has been seted up to equidistant on the upper surface of connector body 1, and a plurality of hydrogen runner 3 has been seted up to equidistant on the lower surface of connector body 1, and air current way 2 is seted up around on connector body 1, and hydrogen runner 3 is seted up on the connector body about, has seted up gas inlet 4 and gas outlet 5 that run through connector body 1 on the connector body 1, and hydrogen runner 3 is located between gas inlet 4 and gas outlet 5.
Further, the air flow channels 2 are distributed on the connector body 1 along the width direction of the connector body 1, and the air flow channels 2 are opened on the connector body 1 front and back.
Further, the length of the air flow passage 2 is equal to the width of the connector body 1, and the air flow passage side is open (opened to the side of the connector body 1, i.e., the length of the air flow passage 2 is equal to the width of the connector body 1).
Furthermore, the air flow channel 2 and the hydrogen flow channel 3 do not penetrate through the connector body 1 from top to bottom, and the air flow channel 2 and the hydrogen flow channel 3 are distributed on the upper side and the lower side of the connector body 1 and do not interfere with each other.
Furthermore, the air flow channel 2 and the hydrogen flow channel 3 are not communicated up and down, so that the respective inlet and outlet of air and hydrogen are not influenced, the inlet and outlet gas is purer, and other gases are not mixed.
Further, the hydrogen flow channels 3 are distributed on the connector body 1 along the length direction of the connector body 1, the air flow channels 2 are formed along the width of the connector body 1, and the hydrogen flow channels 3 are formed along the length direction of the connector body 1, so that the air flow channels 2 and the hydrogen flow channels 3 are arranged on the upper surface and the lower surface of the connector body 1 in a crossing manner.
Further, the number of the gas inlets 4 and the number of the gas outlets 5 are two, and the number of the gas inlets 4 and the number of the gas outlets 5 are two, so that the gas inlet amount is increased.
Further, the gas inlets 4 and the gas outlets 5 are symmetrically distributed on the connector body 1, so that the gas can enter and exit more uniformly.
Further, the two ends of the hydrogen flow channel 3 are respectively communicated with the gas inlet 4 and the gas outlet 5, the air flow channel 2 and the hydrogen flow channel 3 are arranged on the upper surface and the lower surface of the connector body 1 in a crossing way, the air flow channel 2 is arranged along the width of the connector body 1, the hydrogen flow channel 3 is arranged along the length direction of the connector body 1, the side of the air flow channel 2 is open (to the side surface of the connector body 1), the hydrogen flow channel 3 is opened to the gas inlet and outlet, the effective area of the battery is utilized to the greatest extent, and the gas utilization rate is improved.
Further, the air flow path 2 and the hydrogen flow path 3 have the same width.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (10)
1. The utility model provides a connector of high temperature solid oxide electrolysis cell pile, includes connector body (1), its characterized in that: the novel hydrogen gas connector is characterized in that a plurality of air channels (2) are formed in the upper surface of the connector body (1) at equal intervals, a plurality of hydrogen channels (3) are formed in the lower surface of the connector body (1) at equal intervals, a gas inlet (4) and a gas outlet (5) penetrating through the connector body (1) are formed in the connector body (1), and the hydrogen channels (3) are located between the gas inlet (4) and the gas outlet (5).
2. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the air flow channels (2) are distributed on the connector body (1) along the width direction of the connector body (1).
3. The connector of a high temperature solid oxide cell stack of claim 2, wherein: the length of the air flow channel (2) is equal to the width of the connector body (1).
4. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the air flow channel (2) and the hydrogen flow channel (3) do not vertically penetrate through the connector body (1).
5. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the air flow channel (2) and the hydrogen flow channel (3) are not communicated up and down.
6. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the hydrogen flow channels (3) are distributed on the connector body (1) along the length direction of the connector body (1).
7. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the number of the gas inlets (4) and the number of the gas outlets (5) are two.
8. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the gas inlet (4) and the gas outlet (5) are symmetrically distributed on the connector body (1).
9. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the two ends of the hydrogen flow channel (3) are respectively communicated with the gas inlet (4) and the gas outlet (5).
10. The connector for a high temperature solid oxide cell stack of claim 1, wherein: the widths of the air flow channel (2) and the hydrogen flow channel (3) are the same.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202223596683.0U CN219286456U (en) | 2022-12-30 | 2022-12-30 | Connector of high-temperature solid oxide electrolytic cell pile |
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CN202223596683.0U CN219286456U (en) | 2022-12-30 | 2022-12-30 | Connector of high-temperature solid oxide electrolytic cell pile |
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CN219286456U true CN219286456U (en) | 2023-06-30 |
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CN202223596683.0U Active CN219286456U (en) | 2022-12-30 | 2022-12-30 | Connector of high-temperature solid oxide electrolytic cell pile |
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