TW567332B - Fuel single cell performance testing device and method of the same - Google Patents
Fuel single cell performance testing device and method of the same Download PDFInfo
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567332 五、發明說明(1) 詳細說明: 一、發明領域: 本發明係為一種燃料電池之性能測試技術,特別是有 關於一種燃料電池單電池之電流-電壓特性測試裝置及方 法0 二、背景說明: 查燃料電池(F u e 1 C e 1 1)係一種藉著電化學反應,直 接利用含氫燃料和空氣產生電力的裝置。由於燃料^也1 有低污染、咼效率、高能量密度等優點,故成為二 國研發和推廣的對象。在各種燃料電池中,質^交來各 料電地(PEMFC)的操作溫度較低、起動迅速、體積&與重^_燃 的能量密度較高,因而最具產業價值。 貝一里 圖一中顯示了一典型燃料電池組之組成構件分 側視不意圖。該燃料電池組丨係由複數個膜電極组τ之 2(Membrane Electrode Assembles,MEA)組構而— 個膜電極組體2中包括有一第一觸媒層、一古J :- 體擴散層3與雙極板4:置\八電極組體2結 1〇 〇 則且置組合即成為-燃料電池單電池 版雙極板材料大多採用碳 合碳板、或者是金屬或:;二、彳考渗配高分子的: ίο所組構而成之組體頂::2 =個燃料電池單電: 極導流板5、阶極導β _而再、,·。5氣體擴散層3、陽 流板5中設置構成燃料電池,組。在該陽極 有虱乳通道51與氫氣引入管道52,可連 1 妾 567332 五、發明說明(2) 至儲氫裝置,以引入氫氣至該燃料電池丨中。雙極板4 面形成有複數個氣體通道41,而在雙極板4之底面形右項 複數個氫氣通道4 2。在每—個氣體通道4 1之間形 導電接觸區域410,每一個氫氣通道42之間亦形成凸巳之 導電接觸區域420,以與氣體擴散層相接觸。 =電池在反應時係依賴以+質子交換削 電化學反應’其性能與濕度、溫度、嶋;離 工=k s、背壓…等條件皆息息相關。再者, = Ϊ I ί : ί各:=J ;最佳條件(例如電極表面活性、電 電電池在組成後,需進行活化處理。欲使μ'料 :,而欲測試該燃料電池之各項特性(:如件二取= 性),亦必需將這些參數設定在可控 μ電反特 燃料電池之特性設定適合的測試及取樣方、下心並依據 精確之信號擷取及測試結果。惟 技’,:此取得最 池單電池之電流_電壓特性仍 引技術中’對於燃料電 本發明概述: 為精確之夏測方法。 緣此,本發明之主要目的係 之性能測試裝[用卩測試—辦料電池單電池 條件下之電氣特性。 電池早電池於設定操作 本發明之另一目的係提供一 -電壓特性量測方法,其係n則蛾^電池單電池之電流 設定之操作溫度、濕度、背壓條件、’、/、、“池單電池工作於 、卞、及放電 567332 五、發明說明(3) 空氣源及氫氣源通入該燃料電池單電池,以在不同之設定 電壓下^以彳自號取樣之方式置測該燃料電池早電池之電流 變化狀況。 本發明之另一目的係提供一種以平衡點擷取之信號取 樣步驟來進行燃料電池單電池之特性量測,以使燃料電池 單電池在進行電流-電壓之性能測試時,可以有效解決信 號擷取時之信號暫態至平衡態時之不穩狀況,而可得到最 精確之信號擷取及測試結果。 本發明之其它目的及其功效,將藉由以下之實施例及 附呈圖式作進一步之說明: 較佳實施例說明: 在進行本發明之測試作業時,首先需將製備之燃料電 池單電池與測試裝置予以連接。圖二顯示了本發明測試裝 置與燃料電池單電池在進行測試時之連接示意圖。其主要 是在該燃料電池單電池1 0之空氣入口經由空氣管線P1送入 適當流量之空氣源。該空氣源可為一般空氣或是氧氣源。 該空氣源可由一空氣流量偵測與控制計7 1予以控制及 作流量之偵測。該空氣流量偵測與控制計7 1可由一控制裝 置8之控制線所送出之控制信號S1予以控制,而其所偵測 出之空氣流量信號S2則可傳送至控制裝置8中,作為信號 之計算及作為控制之依據。再者,在該空氣管線P1中亦可 配置有一加溫與加濕控制計7 2。 而在該燃料電池單電池1 0之氫氣入口則經由氫氣管線 P2送入適當流量之氫氣源,該氫氣源可為氫氣或是含氫氣567332 V. Description of the invention (1) Detailed description: 1. Field of the invention: The present invention is a technology for testing the performance of a fuel cell, and in particular, it relates to a device and method for testing the current-voltage characteristics of a fuel cell. Description: The fuel cell (Fue 1 C e 1 1) is a kind of device that directly uses hydrogen-containing fuel and air to generate electricity through electrochemical reactions. Because fuel also has the advantages of low pollution, low efficiency, and high energy density, it has become the object of research and development and promotion in the two countries. Among various fuel cells, the operating temperature of PEMFC is relatively low, the start-up speed is fast, and the energy density of volume and recombustion is high, so it has the most industrial value. Bayeri Figure 1 shows the components of a typical fuel cell stack in a side view. The fuel cell stack is composed of a plurality of membrane electrode groups τ-2 (Membrane Electrode Assembles, MEA)-each membrane electrode assembly 2 includes a first catalyst layer, an ancient J:-bulk diffusion layer 3 And bipolar plate 4: set \ eight electrode group body 2 junction 100 sets and set to become-the fuel cell single-cell version of the bipolar plate materials mostly use carbon-carbon plate, or metal or: Infiltrated with polymer: ίο the group body composed of: 2: 2 = single fuel cell: pole deflector 5, step pole β _ and then, .... 5 The gas diffusion layer 3 and the anode plate 5 are arranged to constitute a fuel cell and a stack. The anode has lice milk channel 51 and hydrogen introduction pipe 52, which can be connected to 妾 567332. V. Description of the invention (2) to the hydrogen storage device to introduce hydrogen into the fuel cell. A plurality of gas channels 41 are formed on the surface of the bipolar plate 4, and a plurality of hydrogen channels 42 are formed on the bottom surface of the bipolar plate 4 to the right. A conductive contact area 410 is formed between each of the gas channels 41, and a convex conductive contact area 420 is also formed between each of the hydrogen channels 42 to contact the gas diffusion layer. = Batteries rely on + proton exchange to cut electrochemical reactions. Its performance is closely related to humidity, temperature, 嶋; ionization = k s, back pressure, etc. Furthermore, = Ϊ I ί: ί each: = J; The best conditions (such as electrode surface activity, electric cells need to be activated after the composition. To make μ ′ :, and to test each item of the fuel cell Characteristics (: If two pieces are selected = properties), these parameters must also be set in the characteristics of the controllable μ-electric special fuel cell. Set the appropriate test and sampling method, and focus on accurate signal acquisition and test results. ',: The current-voltage characteristics of this battery cell are still cited in the technology.' For fuel power, the present invention is summarized: It is an accurate summer test method. Therefore, the main purpose of the present invention is a performance test device [use 卩 test —Electrical characteristics under the conditions of battery cells. Battery early setting operation Another object of the present invention is to provide a method for measuring voltage characteristics, which is the operating temperature of the current setting of the battery cell Humidity, back pressure conditions, ', / ,, "Pool cells work at, 卞, and discharge 567332 V. Description of the invention (3) Air source and hydrogen source are connected to the fuel cell unit, under different set voltages ^ The self-number sampling method is used to measure the current change of the fuel cell early battery. Another object of the present invention is to provide a fuel cell single cell characteristic measurement by using a signal sampling step obtained from the equilibrium point to make fuel When performing the current-voltage performance test of a battery cell, it can effectively solve the unstable condition of the signal transient state to the equilibrium state during signal acquisition, and can obtain the most accurate signal acquisition and test results. The purpose and its effects will be further explained by the following examples and attached drawings: Description of preferred embodiments: When carrying out the test operation of the present invention, the prepared fuel cell single cells and test devices must be Connection. Figure 2 shows the connection between the test device of the present invention and the fuel cell unit during the test. It is mainly that the air inlet of the fuel cell unit 10 is fed into the air source with an appropriate flow rate through the air line P1. The air source can be general air or oxygen source. The air source can be controlled and flowed by an air flow detection and control meter 71. The air flow detection and control meter 71 can be controlled by a control signal S1 sent from a control line of a control device 8, and the detected air flow signal S2 can be transmitted to the control device 8. As a signal calculation and as a basis for control. In addition, a heating and humidification control meter 7 2 can also be configured in the air line P1. The hydrogen inlet of the fuel cell unit 10 is passed through the hydrogen line P2 sends a hydrogen source with appropriate flow rate. The hydrogen source can be hydrogen or containing hydrogen.
567332 五、發明說明(4) 體。該氫氣源可由一氫氣流量伯 作流量之㈣。該氫氣流量制計73予以控制及 8之控制線所送出之控制信^幻1^控/計73可由控制裝置 夕巧名、古旦γ〜日丨女1他S3予以控制,而其所偵測出 之虱^里乜.4則亦可傳送至控制裝置8中,作567332 V. Description of the invention (4) style. The hydrogen source may be a flow rate dependent on a hydrogen flow rate. The hydrogen flow meter 73 is controlled and the control letter sent by the control line 8 is magic 1 ^ the control / meter 73 can be controlled by the control device Xi Qiaoming, Gu Dan γ ~ Day 丨 female 1 and S 3, and its detection The detected lice ^ 乜 .4 can also be transmitted to the control device 8 as
之計算及作為控制之依據。再去 JU ^ ^ ^ ^ , 丹者’在該氫氣管線P2中亦可 配置有一加溫與加濕控制計7 4。 該燃料電池單電池1 〇之陽托n ^ r ^ β ^極及陰極經由信號線S5、S6 連接至-電子負載75 ’故該燃料電池單電池1〇之電流訊號 :經由信號祕、S6M量測。而該燃料電池單電池1〇之 電壓訊號則可經由信號線S7、38予以量測。該電 亦經由信號線S9、S10連接至該控制敦置8,可由控制裝置 8抆制a玄電子負載75之動作與接收該電子負載75之各項信 號。 … 燃料電池單電池1 0配置有一加熱裝置76,用以使該燃 料電池單電池ίο加熱至一適當之操作溫度,該加熱裝置76 =動作可經由信號線S1 1受控制裝置8之控制。該燃料電池 單,池1 0亦配置有一溫度檢測元件77,用以檢測該燃料電 池單電池1 0之貫際操作溫度’該檢測出之溫度信號可經由 信號線S12傳送至控制裝置8中。燃料電池單電池1〇與空氣 流量偵測與控制計71、氫氣流量偵測與控制計7 3、電子負 載7 5、加熱裝置7 6、溫度檢測元件7 7與控制裝置8在經過 如圖一所示之管線及信號線之連接之後,即可以化學計量 比1 · 5 (& ) · 3 · 〇 ( A 1 r)之預定氫氣及空氣流量,分別經由 鼠氣管線P 2及空氣管線P 1通入該燃料電池單電池1 Q中,無The calculation and basis of control. Then go to JU ^ ^ ^ ^, Dan who ’can also be equipped with a heating and humidification control meter 74 in the hydrogen pipeline P2. The fuel cell single-cell anode ^ r ^ β ^ pole and cathode are connected to the electronic load 75 via signal lines S5, S6. Therefore, the current signal of the fuel cell single-cell 10: via the signal secret, S6M Measurement. The voltage signal of the fuel cell unit 10 can be measured through the signal lines S7, 38. The electricity is also connected to the control setting 8 via signal lines S9 and S10, and the control device 8 can control the operation of the axuan electronic load 75 and receive various signals of the electronic load 75. … The fuel cell unit 10 is provided with a heating device 76 for heating the fuel cell unit to a proper operating temperature. The heating device 76 = the action can be controlled by the control device 8 via the signal line S1 1. The fuel cell unit 10 is also provided with a temperature detecting element 77 for detecting the interim operating temperature of the fuel cell unit 10 '. The detected temperature signal can be transmitted to the control device 8 through a signal line S12. Fuel cell unit 10 and air flow detection and control meter 71, hydrogen flow detection and control meter 7 3. Electronic load 7 5. Heating device 7 6. Temperature detection element 7 7 and control device 8 After the connection of the pipeline and the signal line shown, a predetermined hydrogen and air flow of stoichiometric ratio 1 · 5 (&) · 3 · 〇 (A 1 r) can be passed through the rat gas line P 2 and the air line P, respectively. 1 into the fuel cell unit 1 Q, no
第7頁 567332Page 7 567332
背歷C1 a t m) 即 TH= Tc + 10 當濕潤性。 』遐溫度UH、ΓΑ)需衷# ,TA= Tc+5VC_(Tc) 保持燃料電池單電池 此階段Tc設定50。c,放電模式為定 、 ^ 2V,待電壓升至0.8〜1.0V時,電壓嗖定0 ,1刀始設疋 τ 电1 "又疋0 · 5 V,時間q〜8小 視u密度上升趨勢而定期間並觀察電流變化情C1 a t m) is TH = Tc + 10 when wetting. 』TEMP temperature UH, ΓΑ) Necessity #, TA = Tc + 5VC_ (Tc) Keep the fuel cell unit Tc is set to 50 at this stage. c, the discharge mode is constant, ^ 2V, when the voltage rises to 0.8 ~ 1.0V, the voltage is set to 0, 1 knife set 疋 τ electricity 1 " again 疋 0 · 5 V, time q ~ 8 small u density Up-trend period and observe current changes
”,再將Tc升至80。c,氣體條件同前所 度到達%,電壓設定〇. 2V,時間〇. 5小時;产接#待胍 (3atm,表壓30psi),並觀察電流變化情形,予背壓 經過上述之前期步驟、且待穩定後^進 池單電池之測試。在進行測試時,其測試 況可能有所不同,例如: 悚件依小N之相 '/气車用I - V測試條件為: 溫度·· Tc = 80。c,TH = 90。C,TA = 85。C 流量:1· 5(H2) : 3· O(Air) 背壓:pH = pA = 30psig 增濕:水瓶氣泡法(外部濕潤)", And then increase Tc to 80. c, the gas conditions reached the same as before, the voltage was set to 0.2V, time 0.5 hours; production of # 待 guan (3atm, gauge pressure 30psi), and observe the current changes After the pre-pressure has passed the previous steps and is stable after entering the battery cell test, the test conditions may be different during the test, for example: The phase of the thriller is based on the small N '/ I for gas vehicles -V test conditions are: Temperature · Tc = 80.c, TH = 90.C, TA = 85. C Flow: 1.5 (H2): 3. O (Air) Back pressure: pH = pA = 30psig increase Wet: water bottle bubble method (external wet)
放電··以定電壓方式 機車用I-V測試條件為: 溫度:Tc = 5〇。C,Th = 25。c,Ta = 5〇。c J量·· 15(¾) : 3.0(Air) 背壓:PH = 5psig,Pa無背壓 增濕:H2dry,Air外部濕潤Discharge ·· Constant voltage I-V test conditions for locomotive are: Temperature: Tc = 50. C, Th = 25. c, Ta = 50. c J ··· 15 (¾): 3.0 (Air) Back pressure: PH = 5psig, Pa without back pressure Humidification: H2dry, Air external humidification
第8頁 567332 五、發明說明(6) 放電+以定電壓方式 〇 4〇vV^. ^ M # ^ "D ^〇CV^0· 8〇V ^ < 間設定為3。:,時間較短(1°秒),°,〜〇.40V區域,時 式進ί傳以Γ也電流-電壓性能時’皆以人工操作方 八 U此耗費相當多的人力時間, 本身性能受制於溫度與水含量變化。若是ηηΐ [:域^長,性能將因膜水含量減;:::電=流 壓高電流區域停留太長,性能丄水含 =實驗:;;:而非常不穩[故為能減少人力耗費及 曰刀Μ ^的%疋性、再現性,本發明 具備了控制、嘈敌雪工迄普r 吓休用之測试方法, 栌&π 電子負載之電壓、電流值、控制反康氣 體流速’可做電流_電壓性”反:: 再現性,屯承的括、,。认,Α 以j重硬數次貫驗觀察其 測試(Life Test)、並可在控了做長广期之,命 單點實驗值等功能。本發明之之4:幕上即時項取 狀兄可信號操取時之信號暫態至平 j、个私狀況,而可得 果。 J敢精確之信號擷取及測試結 顯示本發明平衝點自動和 1=4勒减取方法之流程圖。在勃 圖三 行平衝點 始設定, 設定值、 接著 之拍員取時,首先在步驟1 n 士 T 70你少鄉1 〇 1中作各項設定值之初 例如包括測試時之每_加 4 、 個彳s號擷取週期的取樣數 標準差設定值、時間值等。 ,在步驟1 0 2中作電流、電壓等信號之擷取,並Page 8 567332 V. Description of the invention (6) Discharge + constant voltage 〇 4〇vV ^. ^ M # ^ " D ^ 〇CV ^ 0 · 80V ^ < :, The time is short (1 ° second), °, ~ .40V area, the time type is transmitted with Γ and the current-voltage performance is' all manual operation of the square U. This consumes a lot of human time, its own performance Subject to changes in temperature and water content. If it is ηηΐ [: domain ^ long, performance will decrease due to membrane water content; ::: electricity = current pressure stays in high current region too long, performance 丄 water content = experiment: ;; and very unstable [so it can reduce manpower Consumption and% reproducibility of the knife M ^, the present invention has a test method for control, noisy snowman so far, and the voltage and current value of the electronic load and control Gas flow rate 'can be done as current_voltage' reverse :: reproducibility, enclosing, and admitting, A, observing its test (Life Test) with a number of hard tests several times, and can be controlled in Changguang In the end, functions such as single-point experimental values, etc. The fourth of the present invention: the real-time item on the screen can be used to signal the transient state of the signal when the signal is manipulated, and the result can be obtained. J dare to be precise The signal acquisition and test results show the flow chart of the method of automatic flushing and subtraction of 1 = 4 in the present invention. Set the three rows of flushing points on the Botu first, set the value, and then take the shot, first in step 1 n Taxi T 70 At the beginning of each set value in 〇1, for example, including every test, plus 4, 彳 s number acquisition cycle The sampling number of the standard deviation set value, time value, etc., in step 102 for the acquisition of current, voltage and other signals, and
567332 五、發明說明(7) 在步驟1 0 3中判斷取樣數是否已達預設之取樣數設定值(例 如1 0點)。如果仍未達到預定次數之信號取樣數,則回到 前一步驟1 0 2,繼續進行下一個取樣動作。步驟1 〇 3中當判 斷該信號之取樣數已達到預設之取樣數設定值時,則控制 裝置8中之中央處理單元81即進行資料之運算步驟,以計 算所擷取信號之標準差(步驟1 0 4)。 在步驟1 05中,判斷取樣流程是否超出預設之時間 值,如果尚未超出設定時間,則進行取樣值標準差與其設 定值之比較步驟。當比對出該標準差小於或等於設定值時 (步驟1 0 6 ),即進行平衡點之擷取(步驟1 〇 7 )。如果該取樣 值標準差大於預定倍數(例如1 〇倍)之設定值時(步驟 1 0 8 ),則回到步驟1 0 1,重新各項設定值之初始設定。而 當該取樣值標準差並未大於1 〇倍之設定值時,則回到步驟 1 〇 2,繼續進行信號之榻取。 在前述步驟1 0 5中,當判斷取樣之時間已超出預設之 時間值時,則進行時間值及設定值之累增處理步驟,其係 首先將時間值之時間加1 0秒(步驟1 〇 9 ),而設定值則是等 於原設定值加上原設定值乘〇 · 5倍(步驟11 〇 )。接著於步驟 1 11中判斷設定值是否超出6倍的原設定值,若否,則回到 步驟1 0 5,再判斷是否超出設定值之步驟;若是,則在步 领11 2中將設定值設定為等於6倍的原設定值,並回到步驟 1〇5 中。 經過上述之平衡點操取方法後,可在燃料電池單電池 的性能測試時,可以有效解決信號擷取時之信號暫態至平567332 V. Description of the invention (7) In step 103, it is judged whether the sampling number has reached the preset sampling number setting value (for example, 10 points). If the number of signal samples has not been reached yet, return to the previous step 102 and continue to the next sampling operation. When it is judged that the sampling number of the signal has reached the preset sampling number setting value in step 〇3, the central processing unit 81 in the control device 8 performs the data calculation step to calculate the standard deviation of the captured signal ( Step 1 0 4). In step 105, it is judged whether the sampling process exceeds a preset time value, and if the set time has not been exceeded, a step of comparing the standard deviation of the sampling value with its set value is performed. When the standard deviation is less than or equal to the set value (step 106), the equilibrium point is captured (step 107). If the standard deviation of the sampling value is larger than the set value of a predetermined multiple (for example, 10 times) (step 108), return to step 101 and reset the initial setting of each set value. When the standard deviation of the sampling value is not greater than the set value of 10 times, the process returns to step 102 and continues to take signals. In the foregoing step 105, when it is judged that the sampling time has exceeded the preset time value, the step of accumulating the time value and the set value is performed, which first adds the time of the time value to 10 seconds (step 1 〇9), and the set value is equal to the original set value plus the original set value multiplied by 0.5 times (step 11 〇). Then in step 1 11 determine whether the set value exceeds 6 times the original set value. If not, go back to step 105 and judge whether it exceeds the set value. If yes, set the value in step 11 2 Set it to 6 times the original set value and return to step 105. After the above-mentioned balance point manipulation method, the performance of the fuel cell single cell can effectively solve the signal transient to flat state during signal acquisition.
第10頁 567332 五、發明說明(8) 衡態時之不穩狀況,而可得到最精確之信號擷取及測試結 果。 此外,依據前述取得電流-電壓特性資料,由於〇2 (氧 氣)還原反應為速率決定步驟(Rate Determining Step), 為求得一些反應動力參數(如交換電流密度、阻抗等),電 流-電壓曲線可藉由以下的方程式來分析: E = E〇 -bl〇g( I) - ir 其中E。-Er+ blogl。’ ΕΓ為Ο〗运原反應之可逆電位 (Reversible Potential),b 為其Tafel slope,I。為其交 換電流密度(Exchange Current Density),R為電池阻 抗’它包括電荷轉移阻抗,Charge TransferPage 10 567332 V. Description of the invention (8) The unstable state during equilibrium, and the most accurate signal acquisition and test results can be obtained. In addition, according to the aforementioned current-voltage characteristic data, since the 〇2 (oxygen) reduction reaction is a rate determining step (Rate Determining Step), in order to obtain some reaction kinetic parameters (such as exchange current density, impedance, etc.), the current-voltage curve It can be analyzed by the following equation: E = E〇-bl〇g (I)-ir where E. -Er + blogl. ′ Γ is the Reversible Potential of the transport reaction, b is its Tafel slope, I. For its Exchange Current Density, R is the battery impedance ’It includes charge transfer impedance, Charge Transfer
Resistance,112氧化反應)、歐姆阻抗(r〇,〇hmicResistance (112 oxidation reaction), ohmic resistance (r〇, 〇hmic
Resistance,主要來自電解質)、質傳阻抗(Ι^,Mass Transport Resistance,〇2還原反應);此處將不考慮4氧 化過電位(0verpotential)及%還原反應質傳限制(Mass T r a n s ρ 〇 r t L i m i t a t i ο η) 〇Resistance, mainly from the electrolyte), mass transport resistance (Ι ^, Mass Transport Resistance, 〇2 reduction reaction); 4 oxidation overpotential (0verpotential) and% reduction reaction mass transfer limit (Mass Trans ρ 〇rt L imitati ο η) 〇
藉由上述之本發明實施例說明可知,本 :用價值,且本發明在申請專利,,並未以;類= 專利或產品公開在先,故本發明業已符合於專利之要件。 明,之實施例說明,僅為本發明之較佳實施例說 二項技術者當可依據本發明之上述實施例說明 之改良及變ϊ。然而這些依據本發明實施例 界定之專利範圍内。 月之發明精神及所From the above description of the embodiment of the present invention, it can be known that: this invention is of value, and the invention is in the process of applying for a patent, but not before; category = patent or product disclosure first, so the invention has already met the requirements of the patent. It should be noted that the description of the embodiments is merely a description of the preferred embodiments of the present invention. Two technicians should be able to make improvements and changes according to the above embodiments of the present invention. However, these patents are defined in accordance with the embodiments of the present invention. The spirit and invention of the month
567332 圖式簡單說明 (一) 圖式簡要說明: 圖一係顯示一燃料電池組之組成構件分解時之側視示 意圖; 圖二顯示了本發明測試裝置與燃料電池單電池在進行 測試時之連接示意圖; 圖三顯示本發明平衝點自動榻取方法之流程圖。 (二) 圖號說明:567332 Brief description of the drawings (1) Brief description of the drawings: Figure 1 is a schematic side view of a fuel cell stack when the components are disassembled; Figure 2 shows the connection between the test device of the present invention and a fuel cell unit during a test Schematic diagram; Figure 3 shows a flow chart of the automatic punching method for flat punching points according to the present invention. (2) Explanation of drawing number:
1 燃 料 電 池 組 10 燃 料 電 池 單 電 池 2 膜 電 極 組 體 201 第 一 觸 媒 層 202 高 分 子 質 子 交 換膜 203 第 二 觸 媒 層 3 氣 體 擴 散層 4 雙 極 板 41 氣 體 通 道 410 導 電 接 觸 區 域 411 水 平 壁 面 412 側 壁 面 413 側壁 面 42 氫 氣 通 道 420 導 電 接 觸 區 域 5 陽 極 導 流 板 51 氫 氣 通 道 第12頁 567332 圖式簡單說明 52 氫 氣 引 入 管 道 6 陰 極 導 流 板 71 空 氣 流 量 偵 測 與 控 制 計 72 加 溫 與 加 濕 控 制 計 73 氫 氣 流 量 偵 測 與 控 制 計 74 加 溫 與 加 濕 控 制 計 75 電 子 負 載 76 加 熱 裝 置 77 溫 度 檢 測 元 件 8 控 制 裝 置 P1 空 氣 管 線 P2 氫 氣 管 線 S1 控 制 信 號 S2 空 氣 流 量 信 號 S3 控 制 信 號 S4 氫 氣 流 量 信 號 S5、 S6 信 號 線 S7、 S8 信 號 線 S9、 S10 信 號 線 S11 、S12 信 號 線1 Fuel cell stack 10 Fuel cell unit 2 Membrane electrode assembly 201 First catalyst layer 202 Polymer proton exchange membrane 203 Second catalyst layer 3 Gas diffusion layer 4 Bipolar plate 41 Gas channel 410 Conductive contact area 411 Horizontal wall surface 412 Side wall surface 413 Side wall surface 42 Hydrogen channel 420 Conductive contact area 5 Anode deflector 51 Hydrogen channel Page 12 567332 Brief description of the diagram 52 Hydrogen introduction pipe 6 Cathode deflector 71 Air flow detection and control meter 72 Heating and Humidification control meter 73 Hydrogen flow detection and control meter 74 Heating and humidification control meter 75 Electronic load 76 Heating device 77 Temperature detection element 8 Control device P1 Air line P2 Hydrogen line S1 Control signal S2 Air flow signal S3 Control signal S4 Hydrogen flow signal S5, S6 signal S7, S8 signal line S9, S10 signal lines S11, S12 signal line
第13頁Page 13
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CN100390559C (en) * | 2004-11-11 | 2008-05-28 | 英业达股份有限公司 | Apparatus for testing electronic instrument |
US9419843B2 (en) | 2006-07-06 | 2016-08-16 | Broadcom Corporation | Custom ASIC combining VoIP and security IP |
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CN100390559C (en) * | 2004-11-11 | 2008-05-28 | 英业达股份有限公司 | Apparatus for testing electronic instrument |
US9419843B2 (en) | 2006-07-06 | 2016-08-16 | Broadcom Corporation | Custom ASIC combining VoIP and security IP |
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