TWI441384B - A novel process for fabrication of a sputter deposited fully dense electrolyte layer embedded in a high performance membrane electrolyte assembly (mea) (unit cell) of solid oxide fuel cell - Google Patents
A novel process for fabrication of a sputter deposited fully dense electrolyte layer embedded in a high performance membrane electrolyte assembly (mea) (unit cell) of solid oxide fuel cell Download PDFInfo
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Description
本發明係有關於一種用於固態氧化物燃料電池電解質層之製造技術,特別是有關於一種薄膜製作程序,即磁控濺鍍法(Magnetron Sputter),並結合燃料電池膜電極組(Membrane Electrode Assembly,MEA)製作程序,如刮刀成型(Tape casting)、薄帶層合(Lamination)、真空熱壓合(Vacuum Hot Pressing)、網板印刷(Screen printing)、旋轉鍍膜(Spin coating)或電漿噴塗(Plasma spray coating)等,與燒結技術最佳化之創新製備全緻密電解質之技術,以研製出固態氧化物燃料電池之氣密電解質層。The present invention relates to a manufacturing technique for an electrolyte layer of a solid oxide fuel cell, and more particularly to a film forming process, namely, Magnetron Sputter, combined with a fuel cell membrane electrode assembly (Membrane Electrode Assembly) , MEA) production procedures, such as Tape casting, Lamination, Vacuum Hot Pressing, Screen printing, Spin coating, or Plasma spraying (Plasma spray coating), etc., and the optimization of sintering technology to produce a fully dense electrolyte technology to develop a gas-tight electrolyte layer of a solid oxide fuel cell.
隨著油價高漲與環保意識抬頭,再生能源技術已成為本世紀最重要的發展技術之一。固態氧化物燃料電池為具備高效率、低污染和多元化能源之發電系統,且材料組成簡單、結構模組化與可持續穩定發電之特色,是最具有發展潛力的發電系統。As oil prices rise and environmental awareness rises, renewable energy technology has become one of the most important development technologies of this century. Solid oxide fuel cells are power generation systems with high efficiency, low pollution and diversified energy, and are characterized by simple material composition, modular structure and sustainable and stable power generation. They are the most promising power generation systems.
電解質支撐基板之電池(Electrolyte Supported Cell:簡稱ESC)操作溫度在800~1000℃間。其電解質層基板厚度在150~300μm左右。屬於第一世代之SOFC-MEA。以陽極支撐基板單元電池(Anode Supported Cell:簡稱ASC)操作溫度在650~800℃間,其電解質層厚度在10μm左右,屬於第二世代之SOFC-MEA。(NiO+8YSZ)是ASC/ESC之陽極材料。陰極材料主要為LSM(鑭鍶錳氧化物)及 LSCF(鑭鍶鈷鐵氧化物),其厚度介於30~60μm間。新電解質材料及陰極材料正在世界各研究室創新研發,期待開發新材料俾使SOFC-MEA操作溫度下降到500~700℃,屆時SOFC之電池堆(Stack)組裝零組件如連接板(Inter-connector)等,可使用金屬材料而接換陶瓷材料,不僅容易製造,其機械/穩定/耐久度增加,更可降低整體成本(Cost down)。本項技術發展,在大學及國家研究室方面,著重材料研發,期望發明進步材料,以降低阻抗,增加離導/電導度,增進SOFC之發電功率。The battery of the electrolyte supporting substrate (Electrolyte Supported Cell: ESC) operates at a temperature between 800 and 1000 °C. The thickness of the electrolyte layer substrate is about 150 to 300 μm. It belongs to SOFC-MEA of the first generation. The anode support substrate unit (Anode Supported Cell: ASC) has an operating temperature of 650-800 ° C and an electrolyte layer thickness of about 10 μm, belonging to the second generation SOFC-MEA. (NiO+8YSZ) is the anode material of ASC/ESC. The cathode material is mainly LSM (镧锶 manganese oxide) and LSCF (samarium cobalt oxide) with a thickness between 30 and 60 μm. New electrolyte materials and cathode materials are being researched and developed in various research labs around the world. It is expected to develop new materials and reduce the operating temperature of SOFC-MEA to 500~700 °C. At that time, the stack components of SOFC stacks such as connecting plates (Inter-connector) ), the metal material can be used to replace the ceramic material, which is not only easy to manufacture, but also increases in mechanical/stability/endurance, and lowers the overall cost. This technology development, in the field of universities and national research, focuses on material research and development, and hopes to invent advanced materials to reduce impedance, increase the conductance/conductivity, and increase the power generation of SOFC.
本發明之主要目的係為研製出固態氧化物燃料電池具備全緻密電解質層之製造程序。The main object of the present invention is to develop a manufacturing process for a solid oxide fuel cell having a fully dense electrolyte layer.
根據本發明上述之目的,提出一種以磁控濺鍍程序為主,並結合燃料電池膜電極組(Membrane Electrode Assembly,MEA)製作程序,如刮刀成型(Tape casting)、薄帶層合(Lamination)、真空熱壓合(Vacuum Hot Pressing)、網板印刷(Screen printing)、旋轉鍍膜(Spin coating)或電漿噴塗(Plasma spray coating)等,配合燒結條件之設計與控制,可成功製備全緻密電解質之製程。本發明所指之磁控濺鍍程序包含(1)濺鍍氧化物靶材之射頻磁控濺鍍法與(2)濺鍍金屬合金靶材之反應性磁控濺鍍法,包含直流與射頻。以陽極支撐基板單元電池(Anode Supported Cell:簡稱ASC)為例,本發明程序係將電解質薄膜以磁控濺鍍技術製備於 陰極層塗佈在半電池之電解質面上,因而可研製出具有全緻密電解質層之陽極支撐型固態氧化物燃料電池。以下說明本發明較佳實施例。According to the above object of the present invention, a magnetron sputtering process is mainly combined with a Membrane Electrode Assembly (MEA) manufacturing process, such as tape casting and lamination. , vacuum thermocompression (Vacuum Hot Pressing), screen printing, spin coating or plasma spray coating, combined with the design and control of sintering conditions, can successfully prepare fully dense electrolyte Process. The magnetron sputtering process referred to in the present invention comprises (1) a radio frequency magnetron sputtering method for sputtering an oxide target and (2) a reactive magnetron sputtering method for a sputtering metal alloy target, including a direct current and a radio frequency. . Taking an anode supported substrate unit (ASC) as an example, the program of the present invention prepares an electrolyte film by magnetron sputtering. The cathode layer is coated on the electrolyte surface of the half-cell, so that an anode-supported solid oxide fuel cell having a fully dense electrolyte layer can be developed. Preferred embodiments of the invention are described below.
本發明係一項製作具「全緻密(Fully dense)/零氣體滲透率(Zero gas leakage rate)或氣密(Air tight)之電解質(如8YSZ/GDC/YDC/LSGM等)層」之平板型固態氧化物燃料電池膜電極組合元件(SOFC-MEA)(即單元電池(Unit cell))之程序。此程序之實施方法說明如下:The present invention is a flat type for producing a layer having a "Fully dense"/Zero gas leakage rate or an air tight (e.g., 8YSZ/GDC/YDC/LSGM, etc.) layer. Procedure for solid oxide fuel cell membrane electrode assembly (SOFC-MEA) (ie, unit cell). The implementation method of this program is as follows:
步驟1:在平板型SOFC-MEA之電極基板(Electrode Substrate),以磁控濺鍍法(Magnetron Sputter)之薄膜製作程序,將電解質薄膜(5~15μm)建構於電極基板上,而形成SOFC之半電池(Half cell),並在1200℃~1600℃間(以1400℃首選)進行數小時(3小時以上)之燒結,得到首階段之半電池,此階段電解質可為YSZ,GDC,YDC,SDC,LSGM。再以電子顯微鏡(SEM)作半電池之微結構(Micro-structure)分析,確認電解質層已達到無開口性孔洞(Open-pore free)之微結構狀態與完全緻密(Fully dense)之程度。Step 1: On the electrode substrate (Electrode Substrate) of the flat type SOFC-MEA, an electrolyte film (5-15 μm) is constructed on the electrode substrate by a magnetron sputtering method (Magnetron Sputter), and the SOFC is formed. Half cell (Half cell), and sintering at 1200 ° C ~ 1600 ° C (first choice of 1400 ° C) for several hours (more than 3 hours), to get the first half of the battery, the electrolyte can be YSZ, GDC, YDC, SDC, LSGM. Electron microscopy (SEM) was used as a micro-structure analysis of the half-cell to confirm that the electrolyte layer had reached the open state and the degree of full density of the open-pore free.
步驟2:在半電池之電解質層上,以網板印刷程序,建置具多孔性(Porous)之陰極層(通常材料為LSM或LSCF等),再執行1200℃上下之煅燒3小時左右,即可完成SOFC-MEA之製作。如此作出SOFC-MEA,具高操作性能,耐久性與穩定性。可由單元電池之電性測試(Performance test of SOFC-MEA)驗證。上述過程,為製備具完全緻密(Fully dense)/氣密(Air-tight)之電解 質層之SOFC-MEA之程序。上述步驟1及步驟2之簡易流程圖如圖一所示。Step 2: On the electrolyte layer of the half-cell, a porous (Porous) cathode layer (usually LSM or LSCF, etc.) is built by a screen printing process, and then calcined at 1200 ° C for about 3 hours, that is, The production of SOFC-MEA can be completed. The SOFC-MEA is thus made with high operational performance, durability and stability. It can be verified by the performance test of SOFC-MEA. The above process for preparing a fully dense/air-tight electrolysis The program of the SOFC-MEA of the quality layer. A simple flow chart of steps 1 and 2 above is shown in FIG.
以下詳細說明本發明之實施範例:The following describes an embodiment of the present invention in detail:
步驟1:製作具全緻密/氣密電解質(8YSZ/GDC/LSGM)層之固態氧化物燃料電池組合元件(SOFC-MEA)單元電池(Unit Cell)之程序。此MEA之陽極基板是以50wt% NiO+50wt% 8YSZ與特定量之造孔劑(Pore former)石墨(Graphite)組成基本材料,經刮刀成型程序、薄帶層合與真空壓合程序等製作而成,具強機械強度,厚度約1000μm,大小為5×5cm2 ~12×12cm2 。Step 1: Procedure for making a solid oxide fuel cell composite component (SOFC-MEA) unit cell (Unit Cell) with a fully dense/airtight electrolyte (8YSZ/GDC/LSGM) layer. The anode substrate of the MEA is composed of 50 wt% NiO+50 wt% 8YSZ and a specific amount of Pore former graphite (Graphite), and is formed by a blade forming process, a thin strip lamination and a vacuum pressing procedure. It has strong mechanical strength, a thickness of about 1000 μm, and a size of 5×5 cm 2 to 12×12 cm 2 .
步驟2:電解質薄膜製作方式,以射頻磁控濺鍍法(靶材材料為8YSZ氧化物靶材)及直流磁控濺鍍法(靶材材料為Zrx Y1-x 合金靶材,80<x<100wt.%)將電解質材料沉積於電極基板上,厚度為5~10μm,而形成SOFC之半電池(Half cell),並在1200℃~1600℃間(以1400℃首選)進行數小時(3小時以上)之燒結,得到首階段之半電池,並以SEM作半電池之微結構(Microstructure)分析,確認電解質層已達到無開口性孔洞(Open-pore free)之微結構狀態,如圖二所示,其電解質層之厚度約5/10μm,已形成一完全緻密之結構。可達到氣密效能,滿足SOFC-MEA電解質層之必要要求。只剩下之極少數孔洞,為封閉性孔洞(Close pore),不影響電解質層之氣密性與氣體之滲透率。Step 2: Electrolyte film production method, RF magnetron sputtering (target material is 8YSZ oxide target) and DC magnetron sputtering (target material is Zr x Y 1-x alloy target, 80<x<100wt.%) The electrolyte material is deposited on the electrode substrate to a thickness of 5 to 10 μm to form a half cell of the SOFC, and is carried out for several hours between 1200 ° C and 1600 ° C (preferred at 1400 ° C) ( After sintering for more than 3 hours, the first stage half-battery was obtained, and the microstructure analysis of the half-cell was performed by SEM, and it was confirmed that the electrolyte layer had reached the micro-structure state of the open-pore free, as shown in the figure. As shown in the second, the thickness of the electrolyte layer is about 5/10 μm, and a completely dense structure has been formed. Airtight performance can be achieved to meet the necessary requirements of the SOFC-MEA electrolyte layer. Only a few holes remain, which are closed pores, which do not affect the airtightness of the electrolyte layer and the permeability of the gas.
步驟3:為達完整確認電解質氣密效能,可測量步驟2所得之半電池之氣體滲透率,當氣體滲透率在1×10-6 l/cm2 /sec以下時,可以認為此電解質層為完全緻密目標。Step 3: In order to completely confirm the electrolyte gas tightness performance, the gas permeability of the half-cell obtained in the step 2 can be measured. When the gas permeability is below 1×10 -6 l/cm 2 /sec, the electrolyte layer can be considered as Fully dense target.
步驟4:經步驟3確認之完全緻密半電池結構,以網板印刷程序,建構具多孔性之陰極層LSM材料。再執行1100℃/3hrs之燒結程序,即可製成高操作性能之SOFC-MEA(Unit cell)。其單元全電池之橫截面微觀結構,以SEM分析結果如圖三所示。將製得之SOFC-MEA作電性性能測試,發電測試溫度為700/750/800℃,測試氣氛為100% H2 /O2 ,流量為200/300/400cc/min。整體測試時間可長達120小時以上而沒有效能減弱之情形,其測試過程如圖四所示。單元電池的開路電壓(Open circuit voltage,OCV)穩定接近理論值,最高達1.06V,800℃時之發電功率密度最大可達515mW/cm2 (如圖五所示),顯示利用濺鍍法製備所得之電解質層致密且穩定,所得之單元電池有優異發電性能。由以上結果證明本製作程序之優異性,創新性與技術之關鍵性,確已符合發明專利申請要件。爰依法提出專利申請。Step 4: The fully dense half-cell structure confirmed in step 3 is constructed by a screen printing process to construct a porous cathode layer LSM material. By performing a sintering process at 1100 ° C / 3 hrs, a high operating performance SOFC-MEA (Unit cell) can be produced. The cross-sectional microstructure of the unit full cell is shown in Figure 3 as the SEM analysis. The prepared SOFC-MEA was tested for electrical performance. The power generation test temperature was 700/750/800 ° C, the test atmosphere was 100% H 2 /O 2 , and the flow rate was 200/300/400 cc/min. The overall test time can be as long as 120 hours or more without the performance weakening. The test process is shown in Figure 4. The open circuit voltage (OCV) of the unit cell is close to the theoretical value, up to 1.06V, and the power density at 800°C is up to 515mW/cm 2 (as shown in Figure 5). It is prepared by sputtering. The obtained electrolyte layer is dense and stable, and the obtained unit cell has excellent power generation performance. The above results prove that the excellence of the production process, the innovation and the key to the technology, have indeed met the requirements of the invention patent application.提出 Submit a patent application in accordance with the law.
惟以上所敘過程,僅為本發明之實例而已,當不能以此限定本發明實施之範圍,故依本發明申請專利範圍及發明說明書內容所作之簡單之等效變化與修飾,皆應仍屬本發明專利涵蓋之範圍領域。However, the above-described processes are merely examples of the present invention, and the scope of the present invention and the simple equivalent changes and modifications of the contents of the invention should be The scope of coverage of the patents of the present invention.
第一圖係為本發明程序之簡要實施示意圖。The first figure is a schematic diagram of a brief implementation of the procedure of the present invention.
第二圖係經薄膜技術搭配燒結條件之固態氧化物燃料電池橫截面結構之SEM微結構分析圖:(a)氧化物靶材製備電解質之半電池結構圖,(b)氧化物靶材製備電解質之電解質層表面形貌,(c)合金靶材反應性濺鍍製備電解質之半電池結構圖,(d)合金靶材反應性濺鍍製備電解質之電解質層表面形貌。The second figure is a SEM microstructural analysis of the cross-sectional structure of a solid oxide fuel cell with thin film technology and sintering conditions: (a) half-cell structure diagram of the oxide target preparation electrolyte, and (b) oxide target preparation electrolyte The surface morphology of the electrolyte layer, (c) the half-cell structure diagram of the electrolyte target reactive sputtering to prepare the electrolyte, and (d) the surface morphology of the electrolyte layer prepared by reactive sputtering of the alloy target.
第三圖係氧化物靶材製備電解質之固態氧化物燃料電池全電池結構圖。The third figure is a full cell structure diagram of a solid oxide fuel cell in which an oxide target is prepared for an electrolyte.
第四圖係氧化物靶材製備電解質之固態氧化物燃料電池電性性能測試過程圖。The fourth figure is a diagram showing the electrical performance test procedure of the solid oxide fuel cell for preparing an electrolyte from an oxide target.
第五圖係固態氧化物燃料電池之電性性能測試結果JVP圖(電流密度/電壓/發電功率密度):(a)單元電池在不同溫度下測試結果(700/750/800℃),(b)單元電池在不同H2 /O2 流量下測試結果(100% H2 /O2 flow rates:200/300/400cc/min)。The fifth picture shows the electrical performance test results of solid oxide fuel cells. JVP diagram (current density / voltage / power generation density): (a) test results of unit cells at different temperatures (700/750/800 ° C), (b The cell batteries were tested at different H 2 /O 2 flow rates (100% H 2 /O 2 flow rates: 200/300/400 cc/min).
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