1. Technical Field
The technical field relates to a ceramic cell structure, particularly to a ceramic cell structure added with an electron barrier layer. The electron barrier layer can overcome the disadvantages when using the electrolyte layer individually, as well as improve the cell performance,
2. Related Art
Solid oxide fuel cell (SOFC) is a fuel cell with features of high efficiency, simple structure, and easy operation, in the beginning, the SOFC is mainly used as an auxiliary power system in large buildings. Recently, with the improving of the SOFC technique, the SOFC can be used as independent and distributed power station. Compared to the centralized type power station, the distributed power generating system can not only avoid the energy loss during transferring electricity, but also prevent wide area power outage when the traditional centralized type power station is malfunction or the power transfer is cut off. Therefore, the distributed power generating system is a very ideal power generating means, which is now actually applied to large power plants, distributed power source, or electric cars, etc.
Under the high temperature operation of SOFC, the response of the electrode is quick. Therefore, no nobly metal is needed as a catalyst for the electrode, so the material cost can be reduced. However, on the other side, the over high operation temperature of the SOFC (larger than 800° C.) is easy to cause reaction of the electrode material and the electrolyte surface to increase the total resistance of the cell, as well as cause electrode peeling due to the huge difference of the thermal expansion coefficient of the electrode and electrolyte, which significantly reduces the life expectancy of the cell. Those problems mentioned above limit the development of the'SOFC, so reducing the operation temperature to medium low (500° C.-700° C.) is necessary. The conventional YSZ based Ni-YSZ anode needs relatively high operation temperature (700° C.-1000° C.) to obtain enough energy, to drive the oxygen ion to flow in the oxygen cavity. However, the high temperature may cause many problems (such as the high cost and short life of the equipment which uses high temperature type SOFC). In order to solve those problems, many researches have been done to replace the YSZ with a mixed SDC as anode material.
According to the research, the material of rare earth element doped ceria is a good oxygen ion conductor, which has high conductivity arid ion transport number at 500° C. Especially, the samarium oxide added with cerium oxide (SDC SmXCe1-XO2-6)) is the best electrolyte material, and the conductive oxygen ion at 800° C. is three times than the YSZ. Ordinary electrolyte material should be sintered until reaching 95% theoretical density in, order to be used in the cell. However, the oxide added with cerium is still hard to become dense condition under high temperature sintering (larger than 1500° C.), and the diffusion of the cerium oxide becomes significant above 1450° C.
Thus, it is known that SDC has the advantages of high ionic conductivity at medium low temperature, low sintering temperature, and good matching for the cathode material and anode material. However, drawbacks of the SDC still exist, such as the easy reduction from Ce4+ to Ce3+ under reducing atmosphere. And since the electron conductivity of the electrolyte will increase, the open circuit voltage will drop accordingly.
Besides SDC, another new electrolyte, LSGM (LaxSr1-XGayMg1-yO3-δ) uses ABO3 perovskite structure to replace the traditional fluorite structure, and can show more superior oxygen ion conductivity at 700′C than can that of YSZ (Y2O3)X(ZrO2)1-X), so as to be more suitable for being used in SOFC. Since the LSGM shows good conductivity under low temperature, the LSGM can also be used as a good electrolyte. Besides, the LSGM also has the advantages of high open circuit voltage, stable chemical property under reducing atmosphere, being able to be used above 600°C. However, the LSGM also has the drawbacks of high sintering temperature, the ingredient being easy to change during, sintering, easy to react with anode or cathode material due to high activity,
If solely using SDC or LSGM as the electrolyte between the anode and cathode, the disadvantages mentioned above will be shown. Therefore, disadvantages can be found when using single type electrolyte material as the electrolyte layer between the upper electrode layer (normally anode) and lower electrode layer (normally cathode). For, example, as shown in US patent US2008/0261099 and US2009/0136821, the US2008/0261099 provides a solid oxide electrolyte layer between two electrode layers, and the electrolyte layer includes YSZ and ScSZ (such as Scandia ceria stabilized zirconia 10Sc1CeSZ). However, the US2008/0261099 has the problem of low ion conductivity ratio. Since the total conductivity is electron conductivity plus ion conductivity, electron conduction can thus exist under the low ion conductivity ratio. Moreover, the electron conduction will result in energy loss and cause the dropping of the open circuit voltage and generating high heat.
As to US 2009/0136821, the differences between this patent and the aforementioned patent lie in that the layers in the SOFC is not limited to three. As shown in
The main purpose of the additional layer 4 and the another layer 6 as disclosed in the US 2009/0136821 is to act like a chemical barrier layer or buffer layer to prevent the anode or the cathode reacting with the electrolyte layer cause the anode or cathode might react with the electrolyte layer under high heat processing. Even though US 2009/0136821 discloses the idea of interlayer, US 2009/0136821 still encounters the same problem as found in US 2008/0261099. Since the ion conductivity ratio of the electrolyte layer cannot reach 100%, US 2009/0136821 can cause energy loss due to the electron conducting. Therefore, even though multilayer structure is used, the open circuit voltage still drops and high heat is still generated due to conducting electricity via the electron if not considering the energy loss caused by the electron conducting,
Therefore, in order to overcome the aforementioned drawbacks, if at least one electron barrier layer which cuts the electron, conduction can be disposed between the upper electrode layer and the electrolyte layer, the lower electrode layer and the electrolyte layer, or any two of the electrolyte layers, the energy loss due to the electron conduction can be prevented, and the present invention should be the best solution for solving the conventional problems.
The preferred embodiment of the present invention is related to a ceramic cell structure which is added with an electron barrier layer. Conducting electricity via the electron can be prevented by adding the electron barrier layer, thereby improving the cell performance.
The preferred embodiment of the present invention provides a ceramic cell structure, which includes an upper electrode layer and a lower electrode layer, and at least one electrolyte layer and at least one electron barrier, layer are disposed between the upper electrode layer and the lower electrode layer.
More specifically, the electrolyte layer is an oxide with Bi2O3 group, an oxide with CeCO2 group, an oxide with ZrO2 group, an oxide with ThO2 group, an oxide with HfO2 group, or an oxide with LaGaO3 group.
More specifically, LaGaO3 in the oxide with LaGaO3 group is doped with element Sr, Mg, or Co.
More specifically, LaGaO3 in the oxide with LaGaO3 group is doped with element Sr or Mg.
More specifically, CeO2 in the oxide with CeO2 group is doped with element Sm, Gd, or La.
More specifically, ZrO2 in the oxide with ZrO2 group is stabilized with element Y or Sc.
More specifically, an ionic conductivity ratio of the electron harrier layer is greater than 95%.
More specifically, the electron barrier layer is an oxide with Bi2O3 group, an oxide with ZrO2 group, an oxide with ThO2 group, an oxide with HfO2 group, or an oxide with LaGaO3 group.
More specifically, LaGaO3 in the oxide with LaGaO3 group is doped with element Sr, Mg, or. Co.
More specific LaGaO3 in the oxide with LaGaO3 group is doped with element Sr or Mg.
More specifically, ZrO2 in the oxide with ZrO2 group is stabilized with element Y or Sc.
More specifically, a thickness of the electrolyte layer is between 0.1 μm and 50 μm.
More specifically, a thickness of the electron barrier layer is between 0.1 μm and 50 μm.
More specifically, the electrolyte layer is disposed between the upper electrode layer and the lower electrode layer; the electron barrier layer is disposed between the upper electrode layer and the electrolyte layer.
More specifically, the electrolyte layer is disposed between the upper electrode layer and the lower electrode layer; the electron barrier layer is disposed between the electrolyte layer and the lower electrode layer.
Another preferred embodiment of the present invention provides a ceramic cell structure, which includes an upper electrode layer and a lower electrode layer, and an electron barrier layer disposed between the upper electrode layer and the lower electrode layer; a first electrolyte layer disposed between the upper electrode layer and the electron barrier layer; and a second electrolyte layer disposed between the electron barrier layer and the lower electrode layer.
More specifically, the first electrolyte layer or/and the second electrolyte layer is an oxide with B i2O3 group, an oxide with CeO2 group, an oxide with ZrO2 group, an oxide with ThO2 group, an oxide with HfO2 group, or an oxide with LaGaO3 group.
More specifically, LaGaO2 in the oxide with LaGaO3 group is doped with element Sr, Mg, or Co.
More specifically, LaGaO3 in the oxide with LaGaO3group is doped with element Sr or Mg.
More specifically, CeO2 in the oxide with CeO2 group is doped with clement Sm, Gd, or La.
More specifically, ZrO2 in the oxide with ZrO2 group is stabilized with element Y or Sc.
More specifically, an ionic conductivity ratio of the electron barrier layer is greater than 95%.
More specifically, the electron barrier layer is an oxide with Bi2O3 group, an oxide with ZrO2 group, an oxide with ThO2 group, an oxide with HfO2 group, or an oxide with LaGaO3 group.
More specifically, LaGaO3 in the oxide with LaGaO3 group is doped with element Sr, Mg, or Co.
More specifically, LaGaO3 in the oxide with LaGaO3 group is doped with element Sr or Mg.
More specifically, ZrO2 in the oxide with ZrO2 group is stabilized with element Y or Sc.
More specifically, a thickness of the first electrolyte layer is between 0.1 μm and 50 μm.
More specifically, a thickness of the second electrolyte layer is between 0.1 μm and 50 μm.
More specifically, a thickness of the electron barrier layer is between 0.1 μm and 50 μm.
These and other features and advantages of the various embodiments disclosed herein will be better understood with respect to the following description and drawings, in which like numbers refer to like parts throughout, and in which:
Referring to
The upper electrode layer as disclosed in the present embodiment is cathode (also can be anode), and the lower electrode layer 2 is anode also can be cathode). The first electrolyte layer 3 and the second electrolyte layer 5 are formed by the following electrolyte material: an, oxide with Bi2O3 group, an oxide with CeO2group, an oxide with ZrO2 group, an oxide with ThO2 group, an oxide with HfO2 group, or an oxide with LaGaO3 group. Wherein, the LaGaO3 in the oxide with LaGaO3 group can be doped with element Sr, Mg, or Co; the CeO2 in the oxide with CeO2 group can also be doped with element Sm, Gd, or La, and the ZrO2 in the oxide with ZrO2 group can be stabilized with element Y or Sc.
It will be the best if the material of the electrode layer has 100% ionic conductivity ratio, however, most of the electrode layer has lower than 98% ionic conductivity ratio. The whole conductivity is electron conductivity plus ionic conductivity (στ=σi=σe), and the perfect condition of the electrolyte layer is having 100% ionic conductivity. However, in the actual condition, the ionic conductivity ratio of the electrolyte layer
is usually smaller than 98% (the electron conductivity is not 0%). Since conducting electricity by the electron can cause energy loss, the preferred embodiment of the present invention adds at least one electron barrier layer in addition to the electrolyte layer, so that when the electron conducts electricity, the electron barrier layer can block the electricity conduction of the electron. Under the best condition in the preferred embodiment of the present invention, the ionic conductivity ratio of the electron barrier layer
should be equal or greater than 95% (such as 95%, 95.5%, 96%, 96.5%, 97%, 97.5%, 98%, 98.5%, 99%, 100%), but the present invention can also be applied with any electrolyte material having 0-100% ionic conductivity ratio.
The electron barrier layer 4 is formed by the following, electrolyte material: an oxide with Bi2O3 group, an oxide with CeO2, group, an oxide with ZrO2 group, an oxide with ThO2 group, an oxide with HfO2 group, or an oxide with LaGaO3 group. Wherein, the LaGaO3 in the oxide with LaGaO3 group can be doped with element Sr, Mg, or Co; the CeO2 in the oxide with CeO2 group can also be doped with element Sm, Gd, or La, and the ZrO2in the oxide with ZrO2 group can be stabilized with clement Y or Sc.
Step 201: Scraping-tape formed slurry is under two-stage ball milling process. The ball milling material is zirconia ball The solvent is a mixture of toluene and alcohol having weight ratio 6:4. A dispersant is added to keep the granules in the slurry dispersed. An adhesive and a plasticizer are further added to provide linking and supporting intensity to the thin scraping tape when the scraping tape is formed.
Step 202: The anode is a mixture of the NiO and SDC, and the weight ratio of the NiO and SDC is 6:4, Carbon black is added as pore-forming agent. The scraping-tape forming method is used to prepare the anode, the electrolyte layer, and the electron barrier layer, and those are co-sintered under 1250 to1500° C.
Step 203: The cathode is printed on the sintered electrolyte by the screen printing technique, and the sintering temperature is between 1000° C. to 1200° C.
It is noted that, the aforementioned ceramic cell structure manufacturing process is merely one of the preferred embodiments, and is not limited thereto, such as blade molding method, sputtering method, coating method, screen printing method, and beading method. The manufacturing process of the present invention should overcome sintering matching, thermal expansion matching, chemical matching, and sintering shrinkage matching. The anode sintering temperature in the present invention is between 1250° C. to 1500° C., and the cathode sintering temperature is between 1000° C. to 1200° C. Besides, the thickness of the first electrolyte layer 3, the second electrolyte layer 5, and the electron barrier layer 4 is between 0.1 μm to 50 μm (0.1, 0.5. 2.5, 5, 7.5, 10, 12.5, 15, 17.5, 20, 22.5, 75, 27.5, 30, 37.5, 15, 37.5, 40, 42.5, 45, 47.5, 50). The thickness of different layers can be different, and the effect can be slightly different as well. The thickness can determine the characteristic of the layers. Theoretically, when the thickness is large to a specific extent (depends on the material), the power will decrease, but the stability and mechanical property of the electrolyte membrane will be better.
After the first manufacturing process (the first and the second electrolyte layers use SDC, and the electron barrier layer uses LSGM), electrical measurement is applied, and the results are shown as
(1) In the six sets of experimental groups (550, 600, 650, 700, 750, 800° C.) of the first preferred embodiment of the present invention (as shown in
(2) It can be seen from
(3) Besides, for the power density, when comparing
(4) Based on the above, the advantages and disadvantages of the conventional pure SDC and the pure LSGM lie in that:
(5) According to the advantages and disadvantages of the aforementioned conventional pure SDC and the pure LSGM, and the testing results of
Besides the first preferred embodiment, a single electrolyte layer and a single electron barrier layer can also be used to achieve the same purpose. As shown in
The present invention combines the SDC and LSGM to compare with the single SDC or LSGM, it is obvious that the combination of the SDC and the LSGM can overcome the drawback and keep the advantage of solely using the SDC or LSGM. Therefore, the present invention selects different electrolyte material of the electrolyte layer and the electron barrier layer with different characteristic (if more than one electrolyte layer or electron barrier layer exist, same material might be used as well). Solely using the electrolyte layer might cause open circuit voltage dropping and high heat due to the electro conduction of the electron. However, after adding the electron barrier layer, the electro conduction of the electron can be avoided. Therefore, when selecting the electrolyte material for the electrolyte layer and the electron barrier layer, it is not considered in the present invention if the material used in the electron barrier layer cannot overcome the drawback of the material used in the electrolyte layer, and vice versa.
Furthermore, at least one electrolyte layer and one electron barrier layer can be used between the upper electrode layer 1 and the lower electrode layer 2. However, one electrolyte layer and multiple electron harrier layers, multiple electrolyte layers and one electron harrier layer, or multiple electrolyte layers and multiple electron harrier layers, can also be used between the upper electrode layer 1 and the lower electrode layer 2. The arrangement of the electrolyte layer and the electron barrier layer can be at least one of the following arrangements, or a combination thereof:
(1) One side of the electrolyte layer contacts the upper electrode layer 1, and the other side thereof contacts the electron barrier layer;
(2) One side of the electrolyte layer contacts the lower electrode layer 2, and the other side thereof contacts the electron barrier layer;
(3) One side of the electron barrier layer contacts the upper electrode layer 1, and the other side thereof contacts the electrolyte layer;
(4) One side of the electron barrier layer contacts the lower electrode layer 2, and the other side thereof contacts the electrolyte layer;
(5) When there are at least one electron barrier layer and at least one electrolyte layer disposed between the upper electrode layer 1 and the lower electrode layer 2, an electrolyte layer will be provided between at least two electron barrier layers, or an electron barrier layer is provided between;at least two electrolyte layers,
The aforementioned embodiment is shown as a flat plate structure, but can also be designed as tube structure, as shown in
After measuring the tube shape structure as shown in fourth embodiment, a schematic diagram showing the data and relationship of the measured voltage/the power density and the current density is obtained. The experimental results of the fourth embodiment (
(1) According to
(2) It can be known by comparing the
(3) Besides, as to the power density, it can be known from the comparison of
Based on those described above, the purpose of the present invention can still be achieved when the present invention is formed in a tube structure. Even though the ceramic cell is shown in flat plate structure, the cell can also be designed as tube structure according to the fourth embodiment. The cell can be designed as different shape or structure according to different application, but the stacking structure layer inside the cell should be the same as described in the present invention, and thus not repeat hereinafter,
Besides, no matter how many layers, flat plate or tube structure the present invention has, it should be considered that if there will be a second phase formed between different layers when the electrolyte layer and electron barrier layer of the present invention are under sintering process. The thermal expansion coefficient of each layer should match to one another, so that cracking or separation of those layers will not happen after the cell is manufactured. Each layer should match in chemical properties, not only good binding ability, but also high oxygen ion transferring ability, so that the cell still keeps the high electro conductivity feature. Besides, the electron barrier layer 4 can be added into the cell only if the electron barrier layer 4 does not influence the working of the upper electrode and the lower electrode.
The advantages of the ceramic cell structure of present invention as compared to the conventional technique are as follows:
(1) The present invention can be added with electron barrier layer which is able to overcome the drawback of solely using the electrolyte layer, and improve the cell performance alter being processed.
(2) The ordinary electrolyte layer cannot 100% conduct the electricity via the ion, so the electron will conduct the electricity which results in energy loss. Therefore, the present invention uses electron barrier layer having high ionic conductivity ratio to combine with the electrolyte layer, thereby stopping conducting electricity via the electron.
(3) The drawback of solely using the electrolyte layer is causing the problem of conducting electricity via electron, which results in dropping of open circuit voltage and causes high temperature. However, after being added with the electron barrier layer in the present invention, the electricity conducting of the electron can be prevented, and the open circuit voltage, as well as the power density above 700° C. can be increased.
Although the present invention has been described with reference to the foregoing preferred embodiments, it will be understood that the invention is not limited to the details thereof. Various equivalent variations and modifications can still occur to those skilled in this art in view of the teachings of the present invention. Thus, all such variations and equivalent modifications are also embraced within the scope of the invention as defined in the appended claims.
Number | Date | Country | Kind |
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104140398 | Dec 2015 | TW | national |