CN213905412U

CN213905412U - Solid oxide battery chip with double-electrolyte structure

Info

Publication number: CN213905412U
Application number: CN202022763625.7U
Authority: CN
Inventors: 胡强; 吴剑
Original assignee: Zhejiang Zhen Tai Energy Technology Co ltd
Current assignee: Zhejiang Zhen Tai Energy Technology Co ltd
Priority date: 2020-11-25
Filing date: 2020-11-25
Publication date: 2021-08-06
Anticipated expiration: 2030-11-25

Abstract

The invention provides a solid oxide battery chip with a double-electrolyte structure, and belongs to the technical field of electrochemistry. The air-cooled fuel cell comprises two electrolyte layers, wherein the two electrolyte layers are separated by an inner electrode clamped between the two electrolyte layers, air passages which are regularly arranged are arranged in the inner electrode, at least two side surfaces of the inner electrode are covered with side sealing members, outer surface components are arranged on the outer surface of the electrolyte, the outer surface components comprise a middle layer, an outer electrode, an inner electrode polar plate and an outer electrode polar plate, the inner electrode is connected with the inner electrode polar plate, and the outer electrode is connected with the outer electrode polar plate. The side sealing layer is of a multilayer structure, the inner sublayer can increase the leakage resistance of gas flowing through the inner electrode, the material of the outer sublayer is different from that of the inner sublayer in composition and structure, the side sealing layer can better seal the decompressed leakage gas, and the structural strength can be better maintained.

Description

Solid oxide battery chip with double-electrolyte structure

Technical Field

The invention belongs to the technical field of electrochemistry, relates to a solid oxide battery chip, and particularly relates to a solid oxide battery chip with a double-electrolyte structure.

Background

1. Working principle of Solid Oxide Cell (SOC)

A Solid Oxide Cell (SOC) is a ceramic electrochemical device with Solid Oxide as electrolyte, which is composed of at least one layer of electrolyte and at least two electrodes, a so-called electrode-supported Solid Oxide Cell in which the electrodes provide the overall strength of the Cell, and a so-called electrolyte-supported Solid Oxide Cell in which the electrolyte provides the overall strength of the Cell. The electrolyte material is typically a doped stabilized zirconia, such as yttria doped stabilized zirconia (YSZ), Sc₂O₃Doped stabilized zirconia (ScSZ), scandia yttria doped stabilized zirconia (ScYSZ), scandia ceria doped stabilized zirconia (ScCeSZ), or calcia CaO Stabilized Zirconia (CSZ), etc., with 8 mol% yttria doped stabilized zirconia (8YSZ) being the most widely used. The electrolyte may also be other fluorite-structured oxides such as gadolinium oxide or samarium oxide-doped stabilized cerium oxide, i.e., GDC (gadolinium doped ceria) or SDC (samaria doped ceria), and perovskite-structured oxides such as LaSrGaMgO (LSGM), etc., [ V.V.Kharton, et al, Transport properties of Solid oxide electrolyte ceramics: a brief review, Solid State Ionics,174:135-149(2004) ]. The material composition of the Electrode can be perovskite-structured oxide, such as LaSrMnO (LSM), LaSrCoFeO (LSCF), etc., fluorite-structured oxide, such as SDC, GDC, etc., or composite, such as composite of LSM and YSZ/CGO, etc., or composite of noble metal, such as Pt or composite containing noble metal, such as Pt and YSZ, which are known to those skilled in the art [ E.V.Tsis, et al, Electrode materials and reaction mechanisms in solid oxide fuel cells: a brief review, J.Solid State electrochemistry, 12: 1367-.

When a Solid Oxide Cell (SOC) is operated, the oxygen concentration in the vicinity of at least 2 electrodes differs by a factor of 10 or several orders of magnitude, and hereinafter, a gas having a higher oxygen concentration is referred to as an oxygen-enriched gas, an electrode operating in the oxygen-enriched gas is referred to as an oxygen-enriched electrode, a gas having a lower oxygen concentration is referred to as an oxygen-depleted gas, and the corresponding electrode is referred to as an oxygen-depleted electrode. The oxygen-enriched gas may comprise oxygen, nitrogen, argon, helium, but the most common and most typical oxygen-enriched gas is air, and the corresponding electrode is called an air electrode. The oxygen-depleted gas may contain a variety of gaseous components having fuel-or reducing-properties, such as carbon monoxide, methane, methanol, hydrogen, and the like, and typically an oxygen-depleted atmosphere such as a hydrogen/water mixture, a hydrogen/carbon monoxide/water vapor mixture, a carbon monoxide/carbon dioxide mixture, and a nitrogen oxide (NOx)/nitrogen mixture, and the corresponding electrodes are referred to as fuel electrodes. The oxygen-poor and oxygen-rich electrodes are separated by an electrolyte, which needs to be as dense and gas-tight as possible, and the electrical conductivity should be achieved by ionic rather than electron migration as possible, if there is electron conductivity in the electrolyte, short-circuit current will exist inside the cell, and the overall efficiency of the cell will be significantly reduced. Charge transport of the SOC electrolyte is generally conducted by oxygen ions as carriers, i.e., oxygen ions.

The solid oxide battery (SOC) works in a temperature range of 500 to 1000 ℃, and has two working modes: a Solid Oxide Fuel Cell (SOFC mode) in a power generation mode and a Solid Oxide electrolyte Cell (SOEC mode) in an Electrolysis mode. When the SOC is operated in a power generation mode, namely, an SOFC mode, oxygen molecules in the oxygen-rich electrode undergo a reduction reaction to become oxygen ions (O)^2-) Oxygen ions diffuse from the oxygen-rich electrode side through the electrolyte and migrate to the oxygen-deficient electrode side, which in turn chemically react with fuel gas molecules in the oxygen-deficient electrode if fuel gas molecules are present in the oxygen-deficient electrode. Typically, if the gas component in the oxygen-deficient electrode is hydrogen (H)₂) And carbon monoxide (CO), the chemical reactions that occur in the oxygen-deficient electrode include:

H₂+O^2-→H₂O+2e-

CO+O^2--→CO₂+2e-

the macroscopic representation of the whole process is that oxygen molecules are transferred from the oxygen-enriched gas side to the oxygen-deficient gas side through the electrolyte, and the oxygen concentration difference between the oxygen-enriched gas and the oxygen-deficient gas is reduced. In the power generation mode, the SOC converts the chemical energy of the oxygen-deficient gas into electric energy and outputs the electric energy to the outside. Taking the hydrogen and oxygen electrodes as an example, the electrode reaction and the overall electrochemical reaction in SOFC mode can be expressed as:

anode (oxygen deficient electrode): h₂+O^2-→H₂O+2e-

Cathode (oxygen-rich electrode): 1/2O₂+2e-→O^2-

And (3) total reaction: h₂+1/2O₂→H₂O

If the electrode reaction products cannot be removed in time, the difference in oxygen concentration between the oxygen-rich gas and the oxygen-depleted gas decreases as the reaction proceeds.

Operating a Solid Oxide Cell (SOC) in an electrolysis mode, i.e., SOEC mode, with oxygen-depleted electrode gases, e.g., oxygen (O)₂) Water vapor (H)₂O), carbon dioxide (CO)₂) Nitrogen Oxide (NO)_x) Oxygen molecules or oxygen ions in the molecules are converted into oxygen ions (O) under the action of an external electric field^2-) Diffuses through the electrolyte to the oxygen-rich electrode and undergoes an oxidation reaction within the oxygen-rich electrode to molecular oxygen. The macroscopic expression of the whole process is that oxygen molecules permeate electrolyte from the side of oxygen-poor gas with low oxygen concentration to the side of oxygen-rich gas with high oxygen concentration under the action of an external electric field, and the oxygen concentration difference between the oxygen-rich gas and the oxygen-poor gas is increased. In the electrolysis mode, the SOC absorbs externally input electrical energy and converts it into chemical energy of the oxygen-depleted gas. Taking the hydrogen and oxygen electrodes as an example, the SOEC mode electrode reaction and the overall electrochemical reaction can be expressed as:

anode (oxygen-enriched electrode): o is^2-→1/2O₂+2e-

Cathode (oxygen deficient electrode): h₂O+2e-→H₂+O^2-

And (3) total reaction: h₂O→H₂+1/2O₂

When the SOC is switched between the two modes, the electrical energy and the chemical energy can be converted into each other, which may be accompanied by heat release or absorption. Whether the SOC works in a power generation (SOFC) mode or an electrolysis (SOEC) mode, the SOC can accept external heat energy input or release heat energy to the outside, and therefore mutual conversion among electric energy, heat energy and chemical energy can be achieved by utilizing the SOC technology. When the SOC works in an electrolysis mode (SOEC), the electric energy is converted into chemical energy to be stored, and when the SOC works in a power generation mode (SOFC), the chemical energy of oxygen-poor gas is directly converted into the electric energy, so that the limitation of the Carnot cycle on the power generation efficiency in the heat engine process is avoided, and the efficient chemical energy utilization is realized.

Typical oxygen-depleted gases such as H₂And H₂Mixture of O, in power generation mode (SOFC), the total reaction of SOC is: h₂+1/2O₂→H₂O, in cell mode (SOEC), the overall reaction of SOC is: h₂O→H₂+1/2O₂. A typical oxygen-depleted gas may also be, for example, CO₂，H₂O，CO，H₂The resulting mixture, in generating mode, has a total reaction of SOC: h₂+1/2O₂→H₂O, 2CO+O₂→2CO₂. In electrolytic mode (SOEC), the overall reaction of SOC is H₂O→H₂+1/2O₂，2CO₂→2CO+O₂Containing CO, H₂The electrolysis product of (a), also known as syngas, can be further converted to a series of derived hydrocarbons, such as methanol, ethanol, natural gas, gasoline, diesel, and other mature, widely used fuels or industrial feedstocks, via a mature fischer-tropsch synthesis process. When the gas component containing oxygen is nitrogen oxide NO_xOxysulfide SO_xAnd removing the pollutants by using the electrolytic technology of the SOC at the time of typical environmental pollutants, wherein the chemical process can be expressed as:

NO_x→N₂+O₂(x ═ 1 or 2) or SO_x→S+O₂(x ═ 1 or 2);

2. electrode reaction process of Solid Oxide Cell (SOC)

During the electrode reaction of SOC, at least three phases of substances participate in the reaction, namely oxygen ion (O)^2-) Electron (e)^-) And gaseous substancesSubstances, e.g. molecular oxygen (O)₂) Water (H)₂O), hydrogen (H)₂) Carbon monoxide (CO), and the like. In order to continuously and rapidly perform the electrode reaction process, all substances participating in the reaction need to have a rapid inlet and outlet channel, for example, electrons and oxygen ions needed in the reaction process need to have a smooth transmission channel, that is, the electrode needs to contain a material with high electron conductivity and high oxygen ion conductivity, and also needs to have a certain porosity so as to facilitate the gas reactant at a high temperature to enter the electrode and the gas product of the electrode reaction to be discharged from the electrode. Known oxygen deficient electrode electron conductor materials include metallic nickel (Ni), gold (Au), platinum (Pt), palladium (Pd), rhodium (Rh), etc., and oxygen ion conductors include yttria doped stabilized zirconia (YSZ), scandia yttria doped stabilized zirconia (ScYSZ), scandia ceria doped stabilized zirconia (ScCeSZ) or samarium oxide (Sm)₂O₃) Gadolinium oxide (Gd)₂O₃) Etc. are doped with materials such as stable cerium oxide, e.g., SDC, GDC, etc. Some of the known oxygen ion conductor materials, such as doped stabilized cerium oxide, e.g., SDC, GDC, etc., have certain electron conductivity and are also commonly referred to as mixed conductors. Known oxygen-rich electrode electron conductor materials include LaSrMnO, LaSrCoO, LaSrCoFeO and other oxides which can keep stable properties under a high-temperature oxidizing atmosphere and can change specific compositions within a certain range, and also can be noble metals resistant to high-temperature oxidation, such as silver (Ag), gold (Au), platinum (Pt), palladium (Pd), rhodium (Rh) and the like, and the noble metals resistant to high-temperature oxidation can simultaneously have a catalytic effect to accelerate the electrode reaction. The oxygen ion conductor of the oxygen-rich electrode comprises yttria-doped stabilized zirconia (YSZ), or samarium oxide (Sm)₂O₃) Gadolinium oxide (Gd)₂O₃) The doped stable cerium oxide material, such as SDC, GDC, etc., and the electron conductor material in the oxygen-rich electrode, such as LaSrCoO, LaSrCoFeO, etc., may also have a certain oxygen ion conductivity, and is also referred to in the industry as a mixed conductor. These are well known in the art [ E.V.Tsiaps, et al, Electrode materials and reactions in solid oxide fuel cells: a brief review, J.Solid State electrochemistry, 12: 1367-.

The conventional solid oxide cell is electrode supported, and the arrangement of gas channels in the electrode results in a portion of the electrode structure being hollow, which significantly reduces the structural strength of the cell, with larger gas channel volumes and larger gas channel ratios, and more uneven dimensions, and more strength reduction of the cell. Thus, in typical Solid Oxide Cell (SOC) technology, the size of the gas channels within the electrodes is small, below 1 micron, and in an irregular, dotted distribution [ m.b. mogensen, et al, Reversible solid-oxide cells for Clean and sustainable Energy, Clean Energy,1-27 (2019) ].

The forming method of the gas channel in the electrode is generally to add a certain amount of pore-forming agent, such as graphite or starch, into the precursor powder slurry prepared by the electrode. These pore-forming agents and some solvents, such as alcohol, toluene and isopropanol, etc., are volatilized out of the electrode through high-temperature thermal decomposition during the high-temperature sintering preparation process of the battery, or are oxidized by oxygen in the air to generate gaseous oxides, such as carbon dioxide (CO)₂) Escape the electrode, and leave a gas channel in the electrode, which is well known in the art [ M.Chen, et al, microstuctural definition of Ni/YSZ electrodes in solid oxide electrodes cells under high current, J.Electrochem.Soc., 160: F883-F891 (2013) ].

The tiny gas channels created by this method do not provide a rapid gas transfer path through the electrode, and the entire cell is therefore not provided with sufficient gas supply or timely exhaust gas production, and the conventional remedy is to create external gas channels outside the electrode, in which both oxygen-rich and oxygen-poor gases flow, i.e., oxygen-rich gas channels and oxygen-poor gas channels, which are surrounded by connecting plates, cells, and sealing glass [ m.b. mogensen, et al, Reversible solid-oxide cells for Clean and sustainable, Clean Energy,1-27 (2019) ]. Fig. 1 shows a cross-sectional schematic structure of a cell unit of a typical Solid Oxide Cell (SOC) technology available in the open literature. It can be seen that in these typical configurations, since the diffusion flow rate of gases, particularly oxygen-poor gases, inside the electrode is very low, the gas flow rate leaking from the side edges of the cell is so small that the gaps between the connection plates and the electrode need only be sealed with a high-temperature sealing material, such as glass, without sealing the side edges of the electrode. In the scheme, the air flow main body flows in an air passage which is positioned outside the battery and has a regular shape, the geometric shape and the cross section shape of the air passage can be designed and manufactured as required, a gas raw material serving as a reactant is firstly diffused by an external air passage and enters an electrochemical reaction area of an electrode and electrolyte interface through a relatively compact electrode, and after electrode reaction occurs, a gas product serving as a product is diffused again and enters the external air passage through the relatively compact electrode to be removed and taken away.

In such designs, the gas passages in the electrodes are neither too large nor too large due to structural strength requirements, so that too low a gas flow delivery rate in the electrodes is one of the main factors limiting the electrode reaction rate, and to alleviate this problem, the electrodes in solid oxide cells are typically made very thin, typically 0.05-0.5mm thick, to minimize the diffusion of gas components into and out of the electrode, i.e., from the gas passages to the electrode and electrolyte interface. An electrode that is too thin, while helping to reduce the resistance to gas diffusion into and out of the electrode, can also significantly reduce the structural strength of the cell. The battery designed and manufactured in the mode is easy to break during the assembly and use of the stack, and the whole stack is scrapped due to failure, which is one of the main factors limiting the commercial large-scale use of the high-temperature solid oxide battery technology.

3. Stack assembly design for Solid Oxide Cell (SOC)

The common SOC configuration of the Solid Oxide cell is a chip type, the stack structure of the chip type SOC is realized by connecting SOC elements, sealing rings (sealing), connecting plates (interconnecting) and the like in sequence, and the whole stack is placed in a High temperature environment, which is described in the publication (n.q. minh, System design and application, in-High-temperature Solid Oxide Fuel Cells for the 21^st Century(2^ndEd. ISBN:978-0-12-410453-2), 2015. The sealing ring is generally made of glass or metal (such as gold, silver, etc.), and the material of the connecting plate is usually a high-temperature-resistant alloy. Alloy connecting pieceTab plates also typically require a conductive, oxidation-resistant coating to be sprayed on the surfaces contacting the cells to enhance their oxidation resistance under high temperature conditions and reduce the resistance loss of the stack connections. In most cases, one or more layers of soft metal or ceramic pads are also provided between the electrodes on both sides of the Solid Oxide Cell (SOC) and the alloy connection plate to achieve good electrical contact between the cell (SOC) and the connection plate, typically a mesh made of a high temperature oxidation resistant metal such as gold (Au) or silver (Ag) is used to ensure good electrical contact. In a chip SOC stack, air flows (oxygen-poor and oxygen-rich) flow in an isolated space formed by a connecting plate, a battery (SOC) and a sealing ring, and leakage outside the stack is avoided. Each element of the chip SOC electric pile, including the battery (SOC), the sealing ring and the connecting plate, needs to be manufactured separately and finally combined into a pile. The chip SOC stack is easy to assemble due to the fact that the electrode shape is regular, the current path is short, the power density is relatively large. The chip SOC stack is difficult to be put into practical use because:

1) the seal ring is not highly reliable. The sealing ring needs to simultaneously meet the requirements of airtightness, heat cycle resistance, high-temperature reduction resistance and high-temperature oxidation resistance, has certain mechanical strength and toughness and the like, and also needs to be close to the thermal expansion coefficients of the alloy connecting plate and the SOC battery piece, namely thermal expansion matching, so that the sealing ring is required to be approximately consistent with the dimensional change of the sealing piece under the condition of temperature change. It is difficult to achieve these performance requirements simultaneously with either glass or metal seal rings, for example, glass seal rings are often very weak, they are very susceptible to failure during stack-up and thermal cycling operations in SOC, and even if ceramic and metal seals are barely achieved with glass, the tolerable rate of temperature change must be very low to avoid excessive stress and strain on the seal rings, which results in very long start-up and shut-down times, typically over 10 hours, and sometimes over 20 hours, for a stack employing conventional solid oxide cell technology.

2) Because each group of stack elements needs to be manufactured independently, the technical requirements are high, such as higher requirements on flatness, strength, toughness, oxidation resistance and thermal expansion matching of each element, the stacking cost of the chip SOC group is usually higher, and the practical application is limited.

3) The flexibility of the stack is low. The connection mode of each single battery of the chip SOC stack is in series connection, the sealing ring is a disposable element, once one chip SOC stack is subjected to heat treatment, namely the sealing ring and the sealing element are fused at high temperature, for example, 850 ℃ to realize sealing, each element of the stack group, including each single battery and the connecting plate, can not be replaced, therefore, the failure of any element in the whole stack can cause the failure of the whole stack, the risk of actually using the chip SOC stack is greatly increased, and the use cost is obviously increased.

The prior patent (CN 108336386B) discloses a flat tube structure solid oxide electrochemical device and a preparation method thereof, the patent (CN 108321408B) discloses a flat tube solid oxide electrochemical device containing a plurality of pairs of electrodes and a preparation method thereof, and the patent (CN 108336376B) discloses a flat tube solid oxide battery structure and a preparation method thereof for improving the yield and the single cell power, and provides a scheme for solving the technical problems. When the battery works, the battery using the technology spans a cold and hot temperature interval, the battery performs electrochemical reaction at the hot end, and sealing and external connection are realized at the cold end. The battery adopting the technology is characterized in that: 1) the air flow isolation structure, namely the air passage, required by the battery operation is surrounded by electrolyte, two air passage walls and a layer of partition plate; 2) the constituent materials of the electrolyte, the gas channel wall and the clapboard are the same material or materials with similar compositions; 3) the outer side surfaces of the non-air channel inlet and outlet of the battery are provided with air channel walls, and the air channel walls have certain width to ensure the sealing reliability. In this solution the gas channel seal is realized by the gas channel wall, not by a high temperature sealing material, such as glass, as is commonly used in the art. Although the reserved air flue wall reduces the effective power generation area of the battery, because the components and the properties of the air flue forming materials are close to those of the electrolyte, the common problems in the chip type stack technology that the components are broken and failed in the thermal cycle process of the stack due to the mismatch of the thermal expansion characteristics of the components of the stack or the components of the stack are mutually reacted due to chemical incompatibility and the performance of the stack is weakened and failed due to long-time high-temperature operation are solved or greatly relieved.

A problem with the flat tube cell configuration in practical applications is that it is difficult to compromise the yield and electrical performance of the cell. The air channel surrounding structure in the flat tube version is realized to comprise at least one layer of electrolyte. The electrolyte is a functional component necessary for generating electrochemical reaction when the solid oxide battery works, the thinner the electrolyte is, the smaller the resistance of oxygen ion transmission is, the better the electrical property of the battery is, but the thinner the electrolyte strength is poorer, the electrolyte part forming the air passage is easy to break in the preparation process of the battery or when the battery is operated with large flow of air flow, the yield and the reliability of the flat tube battery are reduced, and the use cost of the technology is increased. Typically, the electrolyte thickness is not less than 0.5mm in order to provide sufficient strength to the gas cell of a flat tube cell, but 0.5mm thickness of electrolyte will result in a cell output density of 100mW/cm²Hereinafter, the output power density of the battery was increased to 300mW/cm²As described above, the thickness of the electrolyte is preferably not more than 0.1mm, but such a thickness makes the electrolyte easily broken at the gas cell, and therefore it is difficult to achieve both yield and electrical properties. In addition, because the side surface of the non-air-passage inlet and outlet of the battery is required to be an air passage wall, when the battery is prepared, the air passage wall at the edge of the battery is required to accurately print or attach corresponding paste or air passage wall membrane sheets at a specified position, so that additional preparation process steps are added, the preparation process requirements of the battery are improved, the cost is increased, and the production efficiency of the battery is also reduced.

The cell disclosed in the above prior patent may also adopt a technical scheme of electrode support, the cell works across a cold and hot temperature interval as well, the cell performs electrochemical reaction at the hot end, sealing and external connection are achieved at the cold end, but the electrolyte surrounding the air passage is replaced by an inner electrode, so that the air passage is completely realized by an electrode material, the strength of the air passage wall and the cell can be realized by properly increasing the thickness of the inner electrode, and meanwhile, the thickness of the electrolyte is kept thin so as to be beneficial to the cell to have higher power. In the scheme, the air channel wall is also arranged on the outer side surface of the non-air channel inlet and outlet of the battery, and the sealing of the high-temperature part is realized by the air channel wall instead of the high-temperature sealing material commonly used in the common technology, such as glass. The width of the air channel wall which must be reserved reduces the power generation area of the battery, and meanwhile, because the side surface of the battery, which is not an air channel inlet and outlet, must be the air channel wall, when the battery is prepared, the air channel wall at the edge of the battery must accurately print or attach corresponding slurry or a membrane at a specified position, so that additional preparation process steps are added, the preparation process requirement of the battery is improved, the cost is increased, and the production efficiency of the battery is also reduced. In addition, this solution is effective for improving the performance and yield of the battery, but has a limited extent because the diffusion rate of gas in the inner electrode having a low porosity is limited, an excessive increase in the thickness of the electrode will result in insufficient gas supply for the electrode reaction, and a thinner inner electrode will result in insufficient strength of the gas channel, thereby failing to achieve high manufacturing yield of the battery.

In the above prior art, the current transmission area of the internal electrode is between the battery working high-temperature area in the middle and the cold-end electrode plate which performs the external connection and sealing functions, the current carrier, i.e. the conductive material, is made of high-temperature-resistant metal such as platinum (Pt) or nickel (Ni), and the current collection resistance of the circuit is large. For example, the conductivity of noble metals such as Pt is low, about 9X 10⁴S/cm, because noble metals are expensive and can only be used in thin layers, the thickness is generally about 50 microns, and the current collection resistance of the Pt coating is about 20mOhm (taking the line width of 1cm and the length of 10cm as an example). Conductivity of nickel is about 1X 10⁵S/cm, but the content of the nickel electrode is generally below 60% due to the requirement of forming in the electrode, and the conductivity of the whole internal electrode is only 200-250S/cm, so that the current collecting resistance of the nickel electrode is about 400mOhm (taking the line width of 1cm, the thickness of 1mm and the length of 10cm as an example), and the line current collecting resistance of the internal electrode is relatively large.

The battery adopting the prior patent needs to span high-temperature and low-temperature regions, namely, the electrode of the battery works in the high-temperature region, and the sealing and external connection of the battery are realized in the low-temperature region, so that the whole battery inevitably transfers heat from the high-temperature region to the low-temperature region during working, heat loss is caused, and the system efficiency is reduced. Due to the complex preparation process of the battery using the technical scheme, only rectangular or square batteries with simpler appearance can be prepared in practice. In the shape design, the channel for transferring heat from the high-temperature area to the low-temperature area is equal in size and cross-sectional area, and the heat loss is large. If a tapered structure is adopted, i.e. the battery gradually reduces in size from a high-temperature working part to a low-temperature sealing part, the passage through which heat is lost from high temperature to low temperature can be gradually narrowed, which is beneficial to reducing the heat loss rate caused by the battery, but in the known technical scheme, the process is complex and difficult to realize.

Disclosure of Invention

The present invention is directed to solving the above-mentioned problems of the prior art, and an object of the present invention is to provide a solid oxide battery chip, which is to solve the technical problem of how to construct a smooth low-resistance gas transmission channel for a rapid electrode reaction, and at the same time, to ensure that the battery has sufficient structural strength.

The purpose of the invention can be realized by the following technical scheme: the solid oxide battery chip with the double-electrolyte structure is characterized by comprising two electrolyte layers, wherein the two electrolyte layers are separated by an inner electrode sandwiched between the two electrolyte layers, air passages which are regularly arranged are arranged inside the inner electrode, at least two side faces of the inner electrode are covered with side sealing components, an outer surface component is arranged on the outer surface of the electrolyte, the outer surface component comprises an intermediate layer, an outer electrode, an inner electrode polar plate and an outer electrode polar plate, the inner electrode is connected with the inner electrode polar plate, and the outer electrode is connected with the outer electrode polar plate.

The oxygen partial pressure difference exists between the inner electrode and the outer electrode, so that the outer electrode can be designed as an oxygen-enriched electrode, the inner electrode can be designed as an oxygen-deficient electrode, the outer electrode can be designed as an oxygen-deficient electrode according to the operation requirement, and the inner electrode can be designed as an oxygen-enriched electrode.

In the solid oxide cell chip with the double-electrolyte-layer structure, the cross-sectional equivalent diameter of a single air channel in the regularly arranged air channels arranged in the inner electrode is 20-200 micrometers.

In the above solid oxide battery chip having a dual electrolyte layer structure, the edge sealing member comprises several sub-layers, wherein at least one of the sub-layers is dense and gas-impermeable, and at least one of the rough gas-permeable sub-layers is disposed between the dense sub-layer and the side surface of the battery chip.

In the solid oxide battery chip with the dual-electrolyte structure, the outer surface component further comprises a plurality of external current collecting lines covering the outer surface of the external electrode, and the conductivity of the external current collecting lines is not lower than that of the external electrode.

In the above solid oxide cell chip having a dual electrolyte structure, the outer surface member further includes a protective layer covering at least one of the outer surface members.

In the solid oxide battery chip with the symmetrical double-electrolyte structure, the inner electrode and the inner electrode polar plate are connected through an inner bus line, and the conductivity of the inner bus line is not lower than that of the inner electrode.

In the solid oxide battery chip having a symmetrical dual electrolyte structure as described above, the internal bus bar is located between the side sealing member and the side of the battery chip.

In the above solid oxide cell chip having a dual electrolyte structure, the main body of the internal bus bar is disposed on the outer surface of the electrolyte and penetrates the electrolyte to be connected to the internal electrode.

In the above solid oxide cell chip having a dual electrolyte structure, the internal current collecting lines penetrate the electrolyte and are individually plugged with a sealing material, preventing gas leakage.

In the solid oxide battery chip with the double-electrolyte structure, the battery chip is in a strip sheet shape, and the shape of the battery chip is gradually narrowed from an outer electrode area in the middle of the battery chip to the end face of the inlet and the outlet of the air passage.

The solid oxide battery chip prepared according to the invention has the following characteristics besides the characteristics of working at the hot end and realizing external connection and sealing at the cold end:

1) the double electrolytes are separated by sandwiched inner electrodes, and the inner electrodes are embedded with regularly arranged micro air passages. The side edges of the non-airflow inlet and outlet end surfaces of the battery cell can also contain outlets of the air passages, so that the process steps for preparing the battery cell can be obviously reduced, the production efficiency of the battery cell is improved, and the production cost of the battery cell is reduced;

2) the internal electrodes may have multiple layers, such as an active internal electrode and a supporting internal electrode, wherein the active internal electrode is more favorable in formulation for performing electrochemical reaction, and the supporting internal electrode is more favorable in composition for improving the overall strength and/or conductivity of the battery chip;

3) because of the embedded regular micro air passages, the number and the positions of the air passages can be adjusted according to the requirements and can be close to the electrolyte, the supply speed of raw material gas or the removal speed of product gas required by electrode reaction is not reduced along with the increase of the thickness of the inner electrode, but is increased along with the increase of the thickness of the inner electrode, and simultaneously, the integral conductance of the inner electrode and the strength of a battery chip are also increased due to the increase of the thickness of the inner electrode;

4) the inner air channels are regularly arranged, and the equivalent diameter of the cross section of each air channel is 20-200 microns, preferably 30-60 microns. Too big air flue cross-section can reduce battery chip intensity, makes the battery chip breakable, shows to reduce battery chip yield, and the air current pressure drop that the during operation of battery chip will be caused to the air flue of undersize is too big. According to the actual test result, the equivalent diameter of the single air passage should be controlled within the range of 30-60 microns. Meanwhile, the number of air passages contained in a single battery cell is more than 6 so as to ensure that the battery cell has certain ventilation capacity and a single battery chip can have enough power;

5) the sides of the cell non-airway walls have special sealing structures, and one sealing structure may contain multiple layers of substructures, which differ in material and microstructure. Different substructures can have different functions, for example, the innermost substructure is mainly used for enhancing contact with the sealing bottom surface and has lower requirement on air tightness, the outermost structure is used for sealing with high requirement on air tightness, more substructures can be embedded in the outermost and innermost substructures according to the requirement on functions, but in any case, at least one of the sublayers of the side sealing component is dense and airtight;

6) the current collecting structure can contain a layer of inner electrode current collecting structure, the conductivity of the current collecting structure is higher, and the current collecting structure is used for reducing the current collecting resistance of the inner electrode. The inner electrode current collecting structure can be positioned in the sealing layer and attached to the side surface of the inner electrode, and can also be positioned at other positions, such as the surface of a battery cell. Preferred internal electrode current collecting structure materials are coatings based on silver (Ag) or nickel (Ni). The material cost of silver and nickel is far lower than that of noble metals such as Pt and the like, the conductivity is high, and the silver and nickel are only used for coating the side face or the side face of the battery chip, so that the structural requirement is avoided, and a large material configuration component adjustment space is provided. The conductivity of the inner electrode current collecting structure may be much greater than that of the commonly used nickel electrode material. For example, the conductivity of a nickel electrode is about 250S/cm, and the current collecting coatings of silver and nickel can respectively realize 6 x 10⁵S/cm and 1X 10⁵Conductivity of S/cm. In the same case, the line resistance of the side current collecting coating with silver (Ag) material is about 17mOhm, and the line resistance of the side current collecting coating with nickel (Ni) material is about 100mOhm (for example, 1mm line width, 0.1mm thickness, 10cm length), both of which are significantly less than the current collecting resistance of the nickel electrode of about 400 mOhm. Obviously, by adopting the structure of the current collecting structure of the inner electrode, the current collecting resistance of the inner electrode of the battery chip can be obviously reduced at lower cost.

7) The cell may adopt a tapered design. Namely, the working surface of the battery chip at the hot end is wider, but the width of the battery chip is gradually reduced along the direction of the gas flow of the inner electrode until the cold end of the battery chip. The tapered design can enable the battery chip to have the working area as large as possible in a high-temperature area, the heat transfer sectional area of the battery core is gradually smaller in a transition area from high temperature to low temperature, and the heat loss caused by the heat conduction of the battery chip is also reduced, so that the power output of the battery core can be effectively improved. According to the experimental result, the output power of the single electric core adopting the reducing design can be about 10% higher than that of the single electric core adopting the rectangular design with the same width. However, the tapered cell chip design may also result in increased internal electrode gas flow resistance, even though the pressure drop of the internal electrode gas as it flows through the cell chip is increased. Practical tests and hydromechanics simulation calculation show that when the included angle between the tapered oblique edge of the battery chip and the straight edge of the hot-end working face is between 5 and 60 degrees, preferably between 10 and 30 degrees, the voltage drop of the inner electrode flowing through the battery chip is small.

According to the functional division, the battery chip according to the present invention should include the following constituent components, wherein the structural component located outside the battery chip, except for the intermediate layer, directly or indirectly attached to the electrolyte is referred to as an outer surface component of the battery chip, and the functions and material compositions of the components are as follows:

1) inner and outer electrode plates: the inner and outer electrodes of the battery chip, which realize the interface part electrically connected with the external device, are preferably made of a material having high conductivity and oxidation resistance, such as a material based on elements of silver (Ag), nickel (Ni), gold (Au), platinum (Pt), rhodium (Ph), palladium (Pd), chromium (Cr), tungsten (W), etc.

2) An inner electrode: the gas flowing through the inner electrode is provided with a place for electrochemical reaction and electrochemical process of the inner electrode, the whole structural strength of the battery chip is provided, and the current transmission channel of the inner electrode is at least partially provided. The inner electrode may contain different sublayer structures to perform three functions of electrochemical reaction, strength support and current transmission, respectively. The different inner electrode sub-layers may be made of materials with similar compositions, preferably, the inner electrode comprises two sub-layers of an active inner electrode and a supporting inner electrode, the composition of the active inner electrode is designed to be more favorable for electrochemical reaction, such as containing 50-60% of 8YSZ and 40-50% of metallic nickel (Ni), and the composition of the supporting inner electrode is designed to be more favorable for electron transmission and strength support of the battery chip, such as 30-50% of 3YSZ and 50-70% of Ni. The internal electrode may further contain a small amount of other additives such as platinum, cerium oxide, aluminum oxide, magnesium oxide, lanthanum oxide, strontium titanate, or a composite based on these additives, based on the basic composition of Ni and YSZ. The content of these additives is usually below 5%, but it can bring better electrochemical activity and better high temperature stability to the inner electrode.

3) Airway: the inner electrode is provided with a raw material supply and a product removal channel required for the electrode process. The air passages extend over the entire inner electrode and to the edge of the battery chip. The equivalent diameter of the single air passage is 20-200 microns, preferably 30-60 microns, so that the air passage can be ensured to be distributed over the inner electrode without remarkably reducing the strength of the inner electrode. The inner electrode with the structured micro air channel arrangement has larger thickness and more air channels, and the air supply quantity of the battery chip is more sufficient and the strength is higher.

4) Electrolyte: and a diaphragm between the inner electrode and the outer electrode provides a channel for ions required by continuous electrode reaction. The smaller the electron conductivity of the electrolyte, the better, and the more airtight the electrolyte. Preferably, the electrolyte is based on doped stabilized zirconia, especially yttria doped stabilized zirconia (YSZ).

5) An internal collector line: and a component which is tightly attached to the inner electrode or is a part of the inner electrode per se and provides a required electron rapid transportation channel for the electrode reaction of the inner electrode. The internal current collecting lines arranged at proper positions by proper materials can effectively increase the overall conductivity of the internal electrodes, so that the battery chip has lower internal resistance, particularly current collecting internal resistance. Preferably, the internal collector has a higher electron conductivity than the internal electrode, and is made of a high temperature oxidation resistant metal material such as silver (Ag), nickel (Ni), gold (Au), platinum (Pt), rhodium (Ph), palladium (Pd), chromium (Cr), tungsten (W), or an alloy thereof, or an oxide such as strontium titanate having a high temperature conductivity under a reducing atmosphere. Preferably, the internal current collecting lines are arranged on the side surfaces of the battery chip, on which the non-gas enters and exits the end surfaces of the battery chip, but can also be arranged on other parts of the battery chip, such as the surface of the battery chip, on which the external electrodes are arranged. The internal collector lines may be either dedicated battery chip components or may be carried by the internal electrodes themselves.

6) An internal bus line: and the electronic transmission channel is communicated with the inner current collecting line and the inner electrode polar plate. Because the inner electrode current is carried, the inner bus line generally has a larger cross-sectional area and higher conductivity so as to ensure that the resistance is smaller when the electron transmission is carried out. Preferably, the internal bus bar has a higher electron conductivity than the internal electrode, and may be composed of a material resistant to high-temperature oxidation, such as silver (Ag), nickel (Ni), gold (Au), platinum (Pt), rhodium (Ph), palladium (Pd), chromium (Cr), tungsten (W), copper (Cu), and the like, and alloys thereof, and composites of these metal materials with an oxide having high-temperature conductivity, such as strontium titanate, doped stabilized cerium oxide, doped stabilized zirconium oxide, and the like, which are known to have high-temperature conductivity.

7) An intermediate layer: the contact between the outer surface parts of the battery chip and the electrolyte is promoted, and the parts of the outer surface parts, which can react with the electrolyte at high temperature, are lightened or avoided. The electrolyte is usually more compact and smooth after being sintered at high temperature of the battery chip, which is not favorable for realizing and maintaining good contact between the outer surface part of the battery chip and the electrolyte. In addition, in the preparation process and the use process of the battery chip, due to the high temperature, such as the highest temperature in the preparation process of the battery chip can reach 1500 ℃, the long-term use of the battery can be maintained in the high temperature range of 500-. These problems can therefore be avoided or alleviated by the introduction of an intermediate layer. The intermediate layer is chemically stable to the electrolyte and the outer surface components of the battery chip at high temperatures, and has a relatively rough surface after preparation, thereby achieving good contact with the outer surface components. The intermediate layer may be prepared not only between the outer electrode and the electrolyte but also between all of the outer surface parts of the battery chip, which may include: external electrodes, internal/external electrode plates, internal/external bus lines, protective layers, sealing structures, and the like. Preferably, the material of the intermediate layer consists of a composite material based on doped ceria (such as SDC or GDC), or doped ceria (SDC or GDC) and doped zirconia (such as YSZ, ScYSZ).

8) External electrode: provides a reaction site for the gas flowing through the outside of the battery chip to generate electrochemical reaction and perform the process of an external electrode. Preferably, the external electrode material is a composite material formed by doped cerium oxide and oxidation-resistant metal such as Ag, Pt, Pd and the like, and also can be an electrode material of the known solid oxide battery technology such as oxides of LaSrMnO, LaSrCoFeO, LaNiFeO and the like or a composite material based on the oxides. In addition, the preparation process of the external electrode may include various known electrode strengthening processes, such as impregnation of active oxides, and the like.

9) An external collector: and a component which is tightly attached to the external electrode or is a part of the external electrode per se and provides an electron rapid transmission channel required by the external electrode for carrying out electrode reaction. Preferably, the external collector is composed of a composite based on a high temperature oxidation resistant metal, such as silver (Ag), nickel (Ni), gold (Au), platinum (Pt), rhodium (Ph), palladium (Pd), chromium (Cr), tungsten (W), etc., and alloys thereof, and an oxide having high temperature conductivity, such as strontium titanate, doped stabilized cerium oxide, doped stabilized zirconium oxide, etc., which are known as oxide materials having high temperature conductivity. Preferably, the outer current collector is arranged at the outer surface of the outer electrode, but may also be located at the inner surface, i.e. between the outer electrode and the electrolyte, or between the outer electrode and the intermediate layer. Preferably, the external current collecting line is in the form of a grid to enhance the current collecting effect.

10) Protective layer: and a structure for directly or indirectly covering and protecting each of the outer surface parts including the external electrode. The outer surface components that the protective layer may cover include: external electrodes, internal/external electrode plates, internal/external bus lines, a protective layer, a side sealing member, a sealing structure and the like. The protective layer can increase the high-temperature stability of each outer surface component of the battery chip including the outer electrode by inhibiting the volatilization loss of the effective components, and can also increase the working stability of the battery chip by enhancing the tolerance of each outer surface component to external gas impurities, such as dust or water vapor, or other gas impurities which are easy to poison and lose efficacy of the outer surface component of the battery chip, such as aromatic hydrocarbon, silane or CO and the like, by a physical filtration or chemical absorption method, thereby effectively prolonging the service life of the battery chip. Preferably, the protective layer may be prepared from an oxide and/or metal material based on alumina, zirconia, ceria, silica, platinum, palladium, rhodium, etc., which can maintain stable properties under high temperature conditions.

11) An outer bus bar: and the electronic transmission channel is communicated with the external collector wire and the external electrode polar plate. Because the outer electrode current is carried, the outer bus wire generally has a larger cross-sectional area and higher conductivity, so as to ensure that the resistance is smaller when the electron is transmitted. Preferably, the outer bus bar is composed of a composite of a metal having higher electron conductivity than the outer electrode material, such as silver (Ag), nickel (Ni), gold (Au), platinum (Pt), rhodium (Ph), palladium (Pd), chromium (Cr), tungsten (W), copper (Cu), etc., and an alloy thereof, and an oxide having high-temperature conductivity, such as strontium titanate, doped stabilized cerium oxide, doped stabilized zirconium oxide, etc., which are known as oxide materials having high-temperature conductivity.

12) Side seal component: the structure for gas-isolated sealing of the non-gas inlet and outlet end faces of the battery chip may comprise a plurality of sublayer mechanisms. Preferably, the battery chip comprises an inner side sealing sub-layer and an outer side sealing sub-layer, wherein the inner side sealing sub-layer covers the side face of the inner electrode of the battery chip and is positioned between the inner electrode and the outer side sealing sub-layer, so that the resistance of airflow of the inner electrode leaking from the side edge of the battery chip is increased, the inner electrode is in good contact with the outer side sealing sub-layer, the inner electrode is chemically stable with the outer side sealing sub-layer, and the inner electrode and the outer side sealing sub-layer are not structurally damaged due to chemical reaction at high temperature. Preferably, the material of the inner side seal layer can be graphite (C) or magnesium silicate talc material, such as (Mg)₆)[Si₈]O₂₀(OH)₄And the like. The side seal outer layer is positioned on the outermost layer of the side seal component of the battery chip and is a compact seal structure for preventing gas flowing through the inner electrode gas channel from leaking to the outside of the battery chip. Preferably, the outer side seal layer may be composed of a graphite or potash-lime glass based material. If the potassium-calcium glass is used, the preferable component proportion range is as follows: k₂O 12-18％CaO 5-12％,SiO₂60-75％。

It should be noted that the above components are divided based on the difference in the functions performed, not their positions or material compositions. In practice, different functional components may be made of materials having similar, or even identical, properties and the same manufacturing process, in which case the different components may have the same, or similar, structural characteristics, which renders them indistinguishable in their microstructural characteristics. For example, the external electrodes, the external collector lines, and the external bus lines, even if they serve different functions, may be fabricated using the same material, e.g., a composite material of 70% Ag and 30% SDC, and the same fabrication process, e.g., screen printing, in the same operation step.

Compared with the prior art, the invention has the following advantages:

1. the regular micro-channels embedded in the inner electrode enable the airflow resistance of gas flowing through the inner electrode to be remarkably reduced, and the regular micro-channels dispersed in the inner electrode help the gas flowing through the inner electrode to be uniformly distributed to all interface areas of electrolyte and electrodes, so that the electrode reaction is more sufficient, and the electrical efficiency of the battery cell is higher;

2. the inner electrode may include multiple sublayers such as an active inner electrode that is more formulated to facilitate the electrochemical reaction and a supporting inner electrode that is more compositionally conducive to improving the overall strength and/or conductivity of the cell.

3. The inner electrode can also be used as a support between two layers of electrolyte, and even if the thickness of the electrolyte is relatively thin, the higher yield can be ensured;

4. the side sealing layer is of a multilayer structure, the inner sublayer can increase the leakage resistance of gas flowing through the inner electrode, the material of the outer sublayer is different from that of the inner sublayer in composition and structure, the side sealing layer can better seal the decompressed leakage gas, and the structural strength can be better maintained.

Drawings

Fig. 1 is a schematic cross-sectional view of a stack unit of a known typical solid oxide cell.

Fig. 2 is a top view structural diagram of the first embodiment of the present invention.

Fig. 3 is a side view of the end of the first embodiment of the present invention.

Fig. 4 is a schematic cross-sectional structure diagram of the first embodiment of the present invention.

Fig. 5 is a top view structural diagram of the second embodiment of the present invention.

Fig. 6 is an exploded view of a second embodiment of the present invention.

Fig. 7 is a top view structural diagram of the third embodiment of the present invention.

Fig. 8 is a top view structural diagram of the fourth embodiment of the present invention.

In the figure, 1, electrolyte; 2. an inner electrode; 201. supporting the inner electrode; 202. an active inner electrode; 3. an outer electrode; 4. a side seal member; 401. a side seal inner layer; 402. side sealing the outer layer; 5. an intermediate layer; 6. an inner electrode pad; 7. an outer electrode plate; 8. an inner bus line; 9. an outer bus line; 10. a sealing structure; 11. an airway; 12. an external collector line; 13. a protective layer; 14. An inner collector line; 15. and (7) connecting the sheets.

Detailed Description

The following are specific embodiments of the present invention and are further described with reference to the drawings, but the present invention is not limited to these embodiments.

The first embodiment is as follows:

as shown in fig. 2 and 3, the present embodiment is a solid oxide battery chip, which adopts a rectangular long strip sheet structure, and includes two layers of electrolytes 1 separated from each other in a thickness direction, an inner electrode 2 is disposed between the two layers of electrolytes 1, and two side surfaces of the inner electrode 2 are respectively covered with a side sealing member 4, an outer surface component is disposed on an outer surface of the electrolyte 1, the outer surface component includes an intermediate layer 5, an outer electrode 3, an inner electrode plate 6, and an outer electrode plate 7, the inner electrode 2 is connected to the inner electrode plate 6, and the outer electrode 3 is connected to the outer electrode plate 7.

Referring to fig. 4, regularly arranged micro gas channels 11 are arranged inside the inner electrode 2, the side seal member 4 comprises two sub-layers of a side seal inner layer 401 and a side seal outer layer 402, the materials of the side seal inner layer 401 and the side seal outer layer 402 are different from the materials of the electrolyte 1 and the inner electrode 2, the side seal outer layer 402 is dense and gas-impermeable, and the side seal inner layer is rough and gas-permeable 401. The inner electrode and the outer electrode are respectively provided with a polar plate so as to facilitate the connection of the battery cell with the outside, the polar plate 7 of the outer electrode is connected with the outer electrode 3 by an outer bus 9, the inner electrode 2 comprises a supporting inner electrode 201 and an active inner electrode 202, the connection of the inner electrode 2 and the polar plate 6 of the inner electrode is connected by an inner bus 8, the outer surface of the outer electrode 3 is provided with an outer current collecting line 12 which is positioned on the outer surface of the outer electrode 3, and the outer current collecting line 12 and the outer electrode 3 are covered with a protective layer 13; the inner electrode polar plate 6, the outer electrode polar plate 7, the outer electrode 3, the outer bus wire 9 and the like are uniformly distributed on the middle layer 5 and are not in direct contact with the electrolyte 1. In the first embodiment, the inner electrode plate 6 and the outer electrode plate 7 are arranged at the same end of the battery cell, and the inner current collecting line 14 is embedded in the side sealing member 4.

The preparation process of the battery chip in the first embodiment is as follows:

1) and (4) preparing a substrate. Substrates are classified into three categories: the preparation process of the support inner electrode substrate, the active inner electrode substrate and the electrolyte substrate comprises the following steps:

(a) and (4) preparing slurry. Ceramic fine powder, such as oxide fine powder of 8YSZ, NiO, GDC and the like, is added with a proper amount of organic auxiliary agents and solvents, such as PVB, triethanolamine, ethanol and the like, and after ball milling and mixing, the ceramic fine powder is uniformly dispersed to prepare stable slurry. In a typical active internal electrode slurry, the content of solid active ingredients is 8 YSZ: NiO: GDC is 5:4:1 (by weight) and has a variation of about 20%, and in a typical supported inner electrode paste, the content of solid active ingredient is 8 YSZ: NiO: al (Al)₂O₃3.5:5.5:1 (by weight), and about 20% of the range. The content of nickel oxide (NiO) in the supporting inner electrode is slightly higher so that the inner electrode has higher conductivity after being reduced. In a typical electrolyte slurry, the solid active ingredient is 8YSZ or ScYSZ.

(b) And (4) preparing a substrate. Preparing the slurry in the step (a) into thin films of an electrolyte and an inner electrode by using a casting machine, wherein the thickness of the typical electrolyte thin film is 5-40 microns, and the thickness of the typical inner electrode thin film is 100-200 microns. The film is dried at 60 ℃ for 2 hours and then cut into sheets of a certain size, such as 270X 220mm, which are called substrates. Accordingly, a substrate prepared from the active internal electrode paste is referred to as an active internal electrode substrate, a substrate prepared from the supporting internal electrode paste is referred to as a supporting internal electrode substrate, and a substrate prepared from the electrolyte paste is referred to as an electrolyte substrate.

(c) And (4) preparing an airway precursor. Preparing an air passage precursor of the battery cell on a substrate supporting the inner electrode. Typical airway precursors are slurries containing fine powders of graphite, starch or other polymeric materials such as PTFE, PVC, etc., preferably in the range of 5-30% solids such as graphite, starch, PTFE, PVC, etc., and the solvent is terpineol. Methods for preparing the precursor paste on the inner electrode substrate include screen printing and high temperature pressing, among others known in the art.

2) The substrate is laminated. Aligning and sequentially overlapping the electrolyte substrate, the active internal electrode substrate, the supporting internal electrode substrate containing the gas channel precursor and the supporting internal electrode substrate without the gas channel according to the sequence shown in figure 4, and then putting the substrates into a vacuum bag for vacuumizing and sealing. Subsequently, the sealed vacuum bag containing the substrate assembly was placed in an isostatic press, and was taken out after applying a pressure of 20MPa in a water bath at 75 ℃ for 5 minutes. By the isostatic pressing process, the individual substrates in the assembly are fused to each other to form a laminated body. The laminate is about 2mm thick and the component layers can no longer be partially or fully separated into individual substrates.

3) And (6) cutting. The laminated body prepared by the steps is placed in a punching machine and is cut into a cell biscuit with a specified design appearance through a punching die. Typically, a laminate can be cut into 3 cell blanks having an outer shape of 65 x 260 mm.

4) And (5) sintering. And placing the cell biscuit in a high-temperature furnace, and selecting a proper heat treatment system to perform high-temperature sintering. After high-temperature sintering, such as sintering at 1400 ℃ for 2 hours, the biscuit size will shrink by 20-30%, and a cell with higher strength is obtained. Meanwhile, in the heat treatment process, because the air flue precursor is gasified and escaped, the regular and uniform embedded micro air flue is left in the battery cell.

5) And firing the intermediate layer. And printing the intermediate layers on the electrolytes on the two sides of the battery core after firing. A typical interlayer material is doped ceria, such as GDC or SDC, and the printing process can be a screen printing process, which is well known in the art. And drying the battery cell printed with the middle layer at 90 ℃ for 1 hour, then placing the battery cell in a high-temperature furnace, then raising the furnace temperature to 1300 ℃, and after 2 hours of calcination, reducing the furnace temperature and controlling the cooling speed not to exceed 5 ℃ per minute. And when the furnace temperature is reduced to room temperature, taking out the battery cell, and firmly firing the middle layers on the two surfaces on the outer surface of the electrolyte of the battery cell.

6) And (4) reducing. And (4) placing the battery cell sintered by the middle layer in a reducing furnace for reduction. The reducing atmosphere is mixed gas of hydrogen and nitrogen, wherein the content of hydrogen is 70-100%, the content of nitrogen is 0-30%, and the reducing condition is 680 ℃ for 6 hours. Through reduction operation, the nickel oxide in the battery core inner electrode is reduced into metallic nickel, so that an additional gas channel is formed in the inner electrode, and meanwhile, because the formed metallic nickel is an electronic conductor, the reduced inner electrode has conductivity, and an electronic transmission channel connected between a battery core high-temperature area for performing electrochemical reaction and an inner electrode pole plate for undertaking connection with the outside can be formed.

7) Preparing an outer surface part. And printing outer surface components of the battery cell on the outer surface of the reduced battery cell, wherein the outer surface components comprise an outer current collecting line, an outer electrode polar plate, an inner electrode polar plate, an outer electrode bus line, an inner electrode bus line, a protective layer and the like, and the components can be completely printed on the intermediate layer or partially or completely printed on the surface of the electrolyte. Because the battery cell is provided with two oppositely arranged electrolytes, the outer surface part on one surface of the battery cell can be sequentially prepared after the outer surface part on the other surface is prepared.

The components of the outer surface components of the battery cell, such as the content of doped stable cerium oxide (SDC or GDC) is 5-20%, the content of silver is 80-95%, and the components of the outer collector lines, the outer electrode polar plates, the inner electrode polar plates, the outer electrode bus lines and the inner electrode bus lines are the same or close to each other, and can be printed in the same step by using the same screen plate. The external electrode comprises the components of 30-55% of doped stable cerium oxide (SDC or GDC) and 45-70% of silver, and the external electrode can be printed before or after the external collector line is printed, but a drying process is carried out between the external collector line and the external collector line, and the drying condition is that the external collector line is dried by hot air at 90 ℃ for 1 hour. The protective layer is composed of alumina, zirconia, silica or various composite materials based on oxides, the preferred component is alumina, and slurry prepared by the oxides is printed or sprayed on other external surface parts after being dried. The various slurries used in the step can use a mixture of ethanol and terpineol as a solvent and graphite with the content of about 0-10% as a pore-forming agent.

8) And preparing an internal collector line. And preparing an internal current collecting line for the battery cell after printing of the components such as the external electrode and the like. Coating the side surface of the battery cell with slurry of an internal collector wire, wherein the basic components are 5-20% of doped stable cerium oxide (SDC or GDC) and 80-95% of silver, and after the internal collector wire is coated, the battery cell needs to be dried by hot air at 90 ℃ for 1 hour until the slurry is cured.

9) And preparing a side seal component. Coating the cell with side sealing inner layer, wherein the side sealing inner layer can be coated on the inner current collecting line coating, and the basic component is graphite or magnesium silicate talc material ((Mg)₆)[Si₈]O₂₀(OH)₄) After the side seal inner layer is dried by hot air at 90 ℃ for 1 hour, the side seal outer layer is continuously coated on the side seal inner layer, the basic material is graphite or potassium-calcium glass, and the component K₂O 12-18％CaO 5-12％,SiO₂60-75％。

10) And (6) heat treatment. And (3) carrying out heat treatment on the battery core subjected to printing and side sealing coating of the outer surface parts, wherein after the heat treatment, each outer surface part forms firm connection with the attachment of the outer surface part, and at least the outermost layer of the side sealing component is densified. The preferable heat treatment system is 850 ℃ for 1 hour, the atmosphere is a reduction protective atmosphere, the hydrogen content is 5-60%, and the balance gas is nitrogen.

11) And (5) strengthening the electrode. The electric core after heat treatment can be used for practical application, and electrode strengthening treatment can be carried out for further improving the electric performance of the electric core and reducing the internal resistance. Typical electrode strengthening treatments are impregnation. For example, SDC (samaria doped ceria) impregnation can be performed by first impregnating Sm (NO)₃)₂，Ce(NO₃)₄According to a certain Sm₂O₃:CeO₂(e.g., Sm in a molar ratio of 20: 80₂O₃:CeO₂) Dissolving in water solution (or dilute nitric acid with pH of about 5), coating the solution on internal and external electrodes, and heating to 500 or 300 deg.C for 20 min to obtain Sm (NO)₃)₂， Ce(NO₃)₄Will decompose to form Sm with a certain proportion₂O₃:CeO₂Doping the stable compound SDC. This process can be repeated 3-5 times to increase the amount of SDC impregnated. SDC is a known oxide with good catalytic activity and mixed ion/electron conductance. After the dipping treatment, the SDC can be dispersed into the electrode with a very fine nanometer scale, such as less than 100 nanometers, and the reaction area of the electrode process, namely TPB (Triple Phase B), is greatly expandedoutary, three-phase interface, i.e., gas-solid electrochemical field), significantly reduces the resistance of the electrode process, reducing the internal resistance of the cell, as is known in the art.

Example two:

referring to fig. 5 and 6, the structure of the second embodiment is substantially the same as that of the first embodiment, except that the intermediate layer 5 may cover the entire outer wall surface of the electrolyte 1 or partially cover the electrolyte 1, the inner electrode plate 6 connected to the inner electrode 2 and the outer electrode plate 7 connected to the outer electrode 3 are respectively disposed at two ends of the battery cell, and the inner bus line 8 is located on the end surface of the battery cell.

Example three:

referring to fig. 7, the structure of the third embodiment is substantially the same as that of the second embodiment, except that the battery chip of the third embodiment adopts a tapered design at both ends, and the included angle α between the tapered oblique edge and the straight edge of the hot-end working face is between 5 and 60 degrees, preferably between 10 and 30 degrees. When the battery chip works, the temperature difference between the temperature at the gas inlet and the gas outlet of the inner electrode 2 and the temperature at the center of the outer electrode is at least more than 200 ℃, and the design can better meet the working state. The external current collecting line 12 of the third embodiment is located on the outer surface of the external electrode 3, and a connecting sheet 15 for external connection is welded on the external electrode polar plate 7, preferably, the connecting sheet 15 is made of a material based on copper, nickel, gold and silver.

Example four:

referring to fig. 8, the structure of the fourth embodiment is substantially the same as that of the third embodiment, except that the inner bus-bar 8 of the fourth embodiment is disposed on the surface of the cell, the high temperature end of the inner bus-bar passes through the opening on the surface of the electrolyte 1 to be connected with the inner electrode 2, the opening surface of the electrolyte 1 is further covered with a sealing structure 10, and the sealing structure 10 permeates the electrolyte 1 and completely covers the opening part of the electrolyte 1, including the junction where the inner bus-bar 8 and the inner electrode 2 are completely covered, so as to ensure that the gas flowing through the inner electrode does not leak out of the cell through the opening.

The specific embodiments described herein are merely illustrative of the spirit of the invention. Various modifications or additions may be made to the described embodiments or alternatives may be employed by those skilled in the art without departing from the spirit or ambit of the invention as defined in the appended claims.

Claims

1. The utility model provides a solid oxide battery chip with two electrolyte structures, its characterized in that, includes two-layer electrolyte layer, it is two-layer the electrolyte layer is separated by the inner electrode of pressing from both sides between, many air flues of regular arrangement are arranged to inner electrode inside, and two at least side covers of inner electrode have the side to seal the component, the surface component has been arranged to the electrolyte, surface component includes intermediate level, outer electrode, inner electrode polar plate and outer electrode polar plate, the inner electrode with the inner electrode polar plate links to each other, the outer electrode with the outer electrode polar plate links to each other.

2. The solid oxide cell chip with a dual electrolyte structure of claim 1, wherein a cross-sectional equivalent diameter dimension of a single air passage of the regularly arranged plurality of air passages arranged in the inner electrode is between 20 and 200 μm.

3. The solid oxide cell chip with a dual electrolyte structure of claim 1, wherein the edge sealing member comprises several sublayers, wherein at least one sublayer is dense and gas impermeable and at least one rough gas permeable sublayer is disposed between the dense and gas impermeable sublayers and the side of the cell chip.

4. The solid oxide cell chip with dual electrolyte structure of claim 1, wherein the outer surface part further comprises a plurality of external current collecting lines covering the outer surface of the external electrode, and the external current collecting lines have an electrical conductivity not lower than that of the external electrode.

5. The solid oxide cell chip with a dual electrolyte structure of claim 1, wherein the outer surface components further comprise a protective layer covering at least one of the outer surface components.

6. The solid oxide cell chip having a dual electrolyte structure as claimed in claim 1, wherein the internal electrode and the internal electrode pad are connected by an internal bus line having an electrical conductivity not lower than that of the internal electrode.

7. The solid oxide cell chip with dual electrolyte structure of claim 6, wherein the internal bus bar is located between a side sealing member and the cell chip side.

8. The solid oxide cell chip having a dual electrolyte structure as claimed in claim 6, wherein the internal bus bar is at least partially disposed on the surface of the electrolyte side where the external electrodes are located, and connected to the internal electrodes through openings in the electrolyte.

9. The solid oxide cell chip having a dual electrolyte structure as claimed in claim 8, wherein a sealing structure is covered at a surface of the electrolyte opening to completely cover and seal a junction of the inner bus line and the inner electrode at the electrolyte opening.

10. The solid oxide cell chip with dual electrolyte structure as claimed in claim 1, wherein the cell chip is in the form of long strip, the shape of the cell chip is gradually narrowed from the outer electrode region at the middle of the cell chip to the inlet and outlet end faces of the air passage, and the included angle between the tapered oblique side and the straight edge of the outer electrode region at the middle of the cell chip is 5-60 °.