TW487599B - A fuel cell for conversion of a fuel and an oxidant into a reaction product and a catalyst for use in said fuel cell - Google Patents
A fuel cell for conversion of a fuel and an oxidant into a reaction product and a catalyst for use in said fuel cell Download PDFInfo
- Publication number
- TW487599B TW487599B TW088120953A TW88120953A TW487599B TW 487599 B TW487599 B TW 487599B TW 088120953 A TW088120953 A TW 088120953A TW 88120953 A TW88120953 A TW 88120953A TW 487599 B TW487599 B TW 487599B
- Authority
- TW
- Taiwan
- Prior art keywords
- catalyst
- oxide
- fuel cell
- item
- patent application
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 63
- 239000000446 fuel Substances 0.000 title claims abstract description 58
- 239000007800 oxidant agent Substances 0.000 title claims abstract description 8
- 230000001590 oxidative effect Effects 0.000 title claims abstract description 8
- 239000007795 chemical reaction product Substances 0.000 title claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 title abstract description 9
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 74
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 38
- 229910052737 gold Inorganic materials 0.000 claims abstract description 29
- 239000010931 gold Substances 0.000 claims abstract description 29
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 239000003792 electrolyte Substances 0.000 claims abstract description 6
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 17
- 238000007254 oxidation reaction Methods 0.000 claims description 11
- 229910000449 hafnium oxide Inorganic materials 0.000 claims description 10
- WIHZLLGSGQNAGK-UHFFFAOYSA-N hafnium(4+);oxygen(2-) Chemical compound [O-2].[O-2].[Hf+4] WIHZLLGSGQNAGK-UHFFFAOYSA-N 0.000 claims description 10
- 230000003647 oxidation Effects 0.000 claims description 10
- 230000003197 catalytic effect Effects 0.000 claims description 9
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 8
- 229910000314 transition metal oxide Inorganic materials 0.000 claims description 7
- 229910000428 cobalt oxide Inorganic materials 0.000 claims description 5
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 claims description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- 230000002079 cooperative effect Effects 0.000 claims description 4
- 229910000476 molybdenum oxide Inorganic materials 0.000 claims description 4
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 claims description 4
- 229910052723 transition metal Inorganic materials 0.000 claims description 4
- 150000003624 transition metals Chemical class 0.000 claims description 4
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims 3
- PCTMTFRHKVHKIS-BMFZQQSSSA-N (1s,3r,4e,6e,8e,10e,12e,14e,16e,18s,19r,20r,21s,25r,27r,30r,31r,33s,35r,37s,38r)-3-[(2r,3s,4s,5s,6r)-4-amino-3,5-dihydroxy-6-methyloxan-2-yl]oxy-19,25,27,30,31,33,35,37-octahydroxy-18,20,21-trimethyl-23-oxo-22,39-dioxabicyclo[33.3.1]nonatriaconta-4,6,8,10 Chemical compound C1C=C2C[C@@H](OS(O)(=O)=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2.O[C@H]1[C@@H](N)[C@H](O)[C@@H](C)O[C@H]1O[C@H]1/C=C/C=C/C=C/C=C/C=C/C=C/C=C/[C@H](C)[C@@H](O)[C@@H](C)[C@H](C)OC(=O)C[C@H](O)C[C@H](O)CC[C@@H](O)[C@H](O)C[C@H](O)C[C@](O)(C[C@H](O)[C@H]2C(O)=O)O[C@H]2C1 PCTMTFRHKVHKIS-BMFZQQSSSA-N 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 229910000420 cerium oxide Inorganic materials 0.000 abstract 1
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 abstract 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 abstract 1
- 229910001928 zirconium oxide Inorganic materials 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000011541 reaction mixture Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 238000005215 recombination Methods 0.000 description 2
- 230000006798 recombination Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9075—Catalytic material supported on carriers, e.g. powder carriers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/52—Gold
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8913—Cobalt and noble metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8933—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/894—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inert Electrodes (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
487599 A7 B7 五、發明説明(/ ) 本發明之 本發明乃關於燃料電池。 (請先閱讀背面之注意事項再填寫本頁) 燃料電池係用以將化學能連續轉化成直流電之裝置。 該電池係由二個藉離子傳導性電解質所分開之導電電極以 及用於燃料、氧化劑與反應產物之連續移進與移出電池之 供應裝置所構成。該燃料可以是氣態或液態;電解質可以 是液態或固態;且氧化劑爲氣態。該電極爲固體,但亦可 以是多孔性且含有催化劑。燃料電池與電池不同,因爲電 力係從必須飼入其中之化學燃料所製造。 經濟部智慧財產局員工消費合作社印製 燃料電池的技術已落後熱燃燒引擎的發展,但在小規 模之發電領域中仍是一競爭者。對此點有許多原因。例如 ’燃料電池天生上係零排放之動力來源且有廣範圍之可能 燃料(potential fuel)與可能之氧化劑(potential oxidant)。再 者,當燃料電池驅動之車輛靜止時,無燃料被使用。但限 制燃料電池發展之問題亦存在。例如,適當之燃料必須可 以在具競爭力之價格下得到。再者,適當且價格實在的催 化劑仍然不可得。已嘗試將賤金屬(base metal)作爲催化劑 ,但通常會發生催化劑的退化。亦曾使用舶族金屬,但在 低負載下足夠高之活性仍未達到。 本發明之槪述 根據本發明之第一方面,其係提供一含有二個電極之 燃料電池,該電極被用於將燃料與氧化劑轉化成反應產物 之電解質所分開,該燃料電池的特色爲該電極包括一催化 劑,其含有具有黃金以有效催化之形式捕捉於其上之氧化 3 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) 487599 Α7 Β7 五、發明說明() 物載體,且燃料爲甲醇或甲烷。 根據本發明之第二方面,其係提供一催化劑,其含有 具有黃金以有效催化之形式捕捉於其上之氧化物載體,以 使用於含有二個電極之燃料電池上,該電極被用以轉化選 自甲醇或甲烷之燃料與氧化劑成爲反應產物之電解質所分 根據本發明之第三方面,其係提供一種氧化燃料電池 中作爲燃料之甲醇或甲烷之方法,其特色爲氧化作用係在 含有氧化物載體之催化劑的存在下發生,該氧化物載體具 有黃金以有效催化之形式捕捉於其上。 圖式簡單說明 圖1A與1B係在各種溫度下之甲烷氧化圖,圖1B係 說明重複測試之結果; 圖2A與2B係在各種溫度下之甲烷氧化圖,圖2B係 說明催化劑K5(3)之重複測試之結果;且 圖3對甲醇重組,本發明之催化劑之活性與白金催化 劑之活性之比較圖。 具體實施例之描述 使用於燃料電池中之以黃金爲基礎之較佳催化劑之實 例係揭示於美國專利第5,759,949號、ΕΡ 0789621與W0 97/45192、其係收錄於此以作爲參考之用。 以黃金爲基礎之催化劑之一較佳形式係含有氧化物載 體、較佳係氧化鈽與氧化鍩之混合物、較佳係氧化鈷之過 渡金屬氧化物,黃金係複合至其上且可選擇性地亦含有氧 4 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁) 裝
ί I ί n I (ϋ I I I n If if I 經濟部智慧財產局員工消費合作社印製 487599 A7 B7 五、發明説明u ) 化欽或氧化鉬。 氧化物載體存在於催化劑中之量較佳係佔催化劑重量 之至少50%、且通常係佔催化劑重量之至少60%。氧化鈽 通吊係佔氧化锆與氧化鈽混合物之重量之至少5 〇%。氧化 姉對氧化锆之較佳重量比係在5 : 1至2 : 1、典型上係約3 :1之範圍。 催化劑係以有效催化之形式含有黃金,此形式將根據 催化劑之性質而改變。 黃金之濃度通常係低的,即佔催化劑重量之2%或更 低。 如前述所提,催化劑較佳係亦含有形式爲氧化物之過 渡金屬,其例如爲氧化鐵、或較佳係氧化鈷。 在實施本發明時,已發現特別有效且可使用之燃料是 甲烷與甲醇。 以黃金爲基礎之催化劑可同時應用於發生在燃料電池 中之電化學與化學氧化反應。 可使用以黃金爲基礎之催化劑之燃料電池之實例係包 括作爲燃料之甲烷之完全與部份氧化。在甲烷之氧化中, 測試描述於WO 97/45192中以黃金爲基礎之催化劑之型號 之能力。所使用之組成係揭示於表1中。 5 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) 音T» 經濟部智慧財產局員工消費合作社印製 487599 A7 ______ _B7 五、發明説明(> ) 表1 :用 於甲烷宗全氬化測試之催化劑之組 成 規貝IJ K1 K2 K5⑵ K5(3) 活性成份 1.0% Au 1.0% Co 1.0% Au 1.0% Co 1.0% Au 1.0% Co 1.0% Au 1.0% Co 載體 Ce〇2 38% 49% 44% 42% Ce〇2/Zr〇2 47.5% 40% 38% 40% Ti〇2 9.5% 10% 15% 15% 用於平衡之其他 氧化物 5.0% 1.0% 3.0% 3.0% (請先閲讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 該測試係以0.25%之甲烷(見圖1)與2.5%之甲烷(見圖 2)以及平衡之空氣進行。氣體混合物之每小時空間速率係 12000小時」。 樣品Κ1與Κ2係在0.25%之甲院、平衡之空氣中測S式 至500°C,且樣品Κ5(2)與Κ5(3)係在60(TC下測試。在每 一個測試後,將樣品在空氣中冷卻至室溫且再重新測試。 已發現K5(3)在600°C之溫度下可得到最高之甲烷轉化 率且係穩定的。 樣品10、:^2、:^5(2)與反5(3)亦在2.5%之甲烷、平衡 之空氣中測試至600°C。 將K5(3)在空氣中從600°C冷卻至室溫且在反應混合物 中再重新測試至600°C以評估在甲烷測試氣體之最高濃度 下之催化劑穩定性。 已發現催化劑在甲烷之最高濃度下表現良好且顯示良 6 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐1 ' ' --- 487599 A7 _________ 五、發明説明u-) 好之持久性。 (請先閲讀背面之注意事項再填寫本頁) 以黃金爲基礎之催化劑亦可以使用於直接甲醇燃料電 池中。甲醇被考慮可作爲燃料之選擇係因爲其與現存之分 配網路之相容性。所進行之測試之結果顯示以黃金爲基礎 之催化劑在低溫下對甲醇氧化係非常地活化。此係有意義 的’因爲甲醇燃料電池商業化之主要限制爲缺乏在低於 100°C之溫度下用於甲醇氧化之催化劑。 揭示於W0 97/45192中之各種以黃金爲基礎之催化劑 之類型係測試其對催化甲醇氧化之穩定性。催化劑K2與 K5(2)係用於測試甲醇氧化。 樣品Κ2係在含有6.5%甲醇、平衡空氣之反應混合物 中評估,而樣品Κ5(2)係含有6.5%與11%之甲醇、平衡空 氣之混合物中測試。 實驗1與2係藉泵送所需之液態甲醇至蒸發器中以進 行。在實驗3中,係使用一擴散器(bubbler)以如所提供之 方法般將甲醇飼入,以得到在操作條件下更一致且均勻之 反應混合物。每一個樣品測試下之操作條件係列於結果中 。反應物與產物分析係藉使用氣相色層分析儀以得到。 經濟部智慧財產局員工消費合作社印製 結果 對實驗1與2,液態甲醇係以適當之泵量飼入蒸發器 中,在開始反應之前,先將樣品冷卻至50°C。 甯驗1 樣品.K2 反應物組成:6.5%CH3OH、平衡空氣 7 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 487599 A7 B7 五、發明説明( 空間速率:20000小時’ 流速:200毫升/分鐘 樣品重量:〇·6克 溫度(°c) CH3〇H轉化率% 殘留之 50 18.8 0 100 65.6 〇 I-----ΜΨ丨— (請先閲讀背面之注意事項再填寫本頁) 實驗2 樣品·· K5(2)反應物組成:6.5%CH3OH、平衡空氣 空間速率:62600小時“ 訂 流速:313毫升/分鐘 樣品重量:0.3克 圭1 :佳迴Iff商童#:>槎品醇氣化之活性 溫度(°c) CH3〇H轉化率% 殘留之產物 50 99.7 0___ 100 99.8 0 經濟部智慧財產局員工消費合作社印製 對實驗3,樣品在開始反應之前係先冷卻至室溫’甲 醇係在室溫下藉噴入之空氣經由液態甲醇擴散器以飼入。 謇驗3 樣品:K5(2)反應物組成:11%CH30H、平衡空氣 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 487599 A7 B7 五、發明説明(7) 空間速率:57600小時^ 流速:96毫升/分鐘 樣品重量:0.1克 表1 :爲溫度函數之樣品K5(2)對甲醇氧化之活性 溫度(°c) CH3〇H轉化率% 殘留之產物co(%) 44 99.4 0 50 100 0 100 100 0 本發明之黃金催化劑用於甲醇重組之活性係與白金催 化劑者相比,且係如圖3所顯示爲較佳。 (請先閲讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐)
Claims (1)
- 487599六、申請專利範圍 ABCD t 正 一 (請先閱讀背面之注意事項再填寫本頁) 1. 一種燃料電池,其含有二個電極,該電極被用於將 燃料與氧化劑轉化成反應產物之電解質所分開,其特徵在 於該電極包括一催化劑,其含有具有黃金以有效催化之形 式捕捉於其上之氧化物載體,且其特徵在於該燃料爲甲醇 或甲烷。 2. 根據申請專利範圍第1項之燃料電池,其中該催化 劑係含有爲氧化锆與氧化鈽混合物之氧化物載體,其具有 黃金以有效催化之形式捕捉於其上,氧化物載體存在於催 化劑中之量係佔催化劑重量之至少50%。 3·根據申請專利範圍第2項之燃料電池,其中該氧化 物載體存在於催化劑中之量係佔催化劑重量之至少60%。 4·根據申請專利範圍第2項之燃料電池,其中該氧化 鈽對氧化锆之重量比係在5 : 1至2 : 1。 5·根據申請專利範圍第1項之燃料電池,其中該催化 劑亦含有形式爲氧化物之過渡金屬。 6·根據申請專利範圍第5項之燃料電池,其中該過渡 金屬氧化物係選自氧化鈷與氧化鐵。, 經濟部智慧財產局員工消費合作社印製 7·根據申請專利範圍第6項之燃料電池,其中該黃金 係與過渡金屬氧化物錯合。 8·根據申請專利範圍第1項之燃料電池,其中該催化 劑係包括氧化鈦或氧化鉬。 9·一種催化劑,其含有具有黃金以有效催化之形式捕 捉於其上之氧化物載體,其係使用於含有二個電極之燃料 電池上’該電極被用以轉化選自甲醇或甲烷之燃料與氧化 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 經濟部智慧財產局員工消費合作社印制衣 487599 餡 C8 D8 六、申請專利範圍 劑成爲反應產物之電解質所分開,其中該催化劑係含有爲 氧化锆與氧化鈽混合物之氧化物載體,其具有黃金被以有 效催化之形式捕捉於其上,氧化物載體存在於催化劑中之 量係佔催化劑重量之至少50%。 1〇·根據申請專利範圍第9項之催化劑,其中該氧化物 載體存在於催化劑中之量係佔催化劑重量之至少60%。 11·根據申請專利範圍第9項之催化劑,其中該氧化鈽 對氧化锆之重量比係在5 : 1至2 ·· 1。 12·根據申請專利範圍第9項之催化劑,其中該催化劑 亦含有形式爲氧化物之過渡金屬。 13·根據申請專利範圍第12項之催化劑,其中該過渡 金屬氧化物係選自氧化鈷與氧化鐵。 H·根據申請專利範圍第13項之催化劑,其中該黃金 係與過渡金屬氧化物錯合。 I5·根據申請專利範圍第9項之催化劑,其中催化劑係 包括氧化鈦或氧化鉬。 16·根據申請專利範圍第1項之燃料電池,其中燃料電 池中作爲燃料之甲醇或甲烷之氧化作用係在含有具有黃金 以有效催化之形式捕捉於其上之氧化物載體之催化劑的存 在下發生。 17.根據申請專利範圍第1或16項之燃料電池,其中 該催化劑係含有爲氧化锆與氧化鈽混合物之氧化物載體, 其具有黃金以有效催化之形式捕捉於其上,氧化物載體存 在於催化劑中之量係佔催化劑重量之至少50%。 2 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公H (請先閱讀背面之注意事項再填寫本頁)經濟部智慧財產局員工消費合作社印製 487599 A8 B8 C8 D8 六、申請專利範圍 18.根據申請專利範圍第17項之燃料電池,其中該氧 化物載體存在於催化劑中之量係佔催化劑重量之至少60% 〇 I9·根據申請專利範圍第17項之燃料電池,其中該氧 化鈽對氧化锆之重量比係在5 : 1至2 : 1。 20.根據申請專利範圍第16項之燃料電池,其中該催 化劑亦含有形式爲氧化物之過渡金屬。 21·根據申請專利範圍第20項之燃料電池,其中該過 渡金屬氧化物係選自氧化鈷與氧化鐵。 22. 根據申請專利範圍第21項之燃料電池,其中該黃 金係與過渡金屬氧化物錯合。 23. 根據申請專利範圍第16項之燃料電池,其中該催 化劑係包括氧化鈦或氧化鉬。 3 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ZA985243 | 1998-09-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| TW487599B true TW487599B (en) | 2002-05-21 |
Family
ID=25587081
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW088120953A TW487599B (en) | 1998-09-07 | 1999-12-01 | A fuel cell for conversion of a fuel and an oxidant into a reaction product and a catalyst for use in said fuel cell |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US20020012828A1 (zh) |
| AU (1) | AU5382799A (zh) |
| CA (1) | CA2343519A1 (zh) |
| DE (1) | DE19983527T1 (zh) |
| GB (1) | GB2357628A (zh) |
| TW (1) | TW487599B (zh) |
| WO (1) | WO2000013791A1 (zh) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6589680B1 (en) | 1999-03-03 | 2003-07-08 | The Trustees Of The University Of Pennsylvania | Method for solid oxide fuel cell anode preparation |
| US8007954B2 (en) | 2000-11-09 | 2011-08-30 | The Trustees Of The University Of Pennsylvania | Use of sulfur-containing fuels for direct oxidation fuel cells |
| US20040172084A1 (en) * | 2003-02-03 | 2004-09-02 | Knudson Mark B. | Method and apparatus for treatment of gastro-esophageal reflux disease (GERD) |
| TWI301824B (en) * | 2005-05-24 | 2008-10-11 | Nat Univ Tsing Hua | Process for producing hydrogen with high yield under low temperature |
| US7704919B2 (en) * | 2005-08-01 | 2010-04-27 | Brookhaven Science Associates, Llc | Electrocatalysts having gold monolayers on platinum nanoparticle cores, and uses thereof |
| WO2014181289A2 (en) * | 2013-05-08 | 2014-11-13 | Saudi Basic Industries Corporation | Gold containing catalysts for propane dehydrogenation |
| US10367208B2 (en) | 2015-05-06 | 2019-07-30 | Robert E. Buxbaum | High efficiency fuel reforming and water use in a high temperature fuel-cell system and process for the such thereof |
| CN114643055B (zh) * | 2022-04-08 | 2023-07-07 | 浙江大学 | 一种用于催化氮氧化物直接分解的负载了纳米金的纳米氧化铈及其制备方法 |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63252908A (ja) * | 1987-04-08 | 1988-10-20 | Agency Of Ind Science & Technol | 金超微粒子固定化酸化物、その製造法、酸化触媒、還元触媒、可燃性ガスセンサ素子、及び電極用触媒 |
| GB8816114D0 (en) * | 1988-07-06 | 1988-08-10 | Johnson Matthey Plc | Reforming catalyst |
| GB9226434D0 (en) * | 1992-12-18 | 1993-02-10 | Johnson Matthey Plc | Catalyst |
| IL108635A (en) * | 1993-02-18 | 1997-09-30 | Grigorova Bojidara | Catalyst for use in an oxidation reaction |
| IL112414A (en) * | 1994-01-25 | 1998-08-16 | Anglo American Res Lab Pty Ltd | Method of preparing a catalyst by impregnating a porous support with a solution |
| ES2132728T3 (es) * | 1994-11-02 | 1999-08-16 | Anglo American Res Lab Pty Ltd | Catalizador con soporte de oxido de zirconio/oxido de cerio. |
| JP3570046B2 (ja) * | 1995-11-02 | 2004-09-29 | 株式会社豊田中央研究所 | 低温型燃料電池 |
| BG62687B1 (bg) * | 1997-05-15 | 2000-05-31 | "Ламан-Консулт"Оод | Златен катализатор за окисление на въглероден оксид и въглеводороди, редуциране на азотни оксиди иразлагане на озон |
| BG62723B1 (bg) * | 1997-09-29 | 2000-06-30 | "Ламан-Консулт"Оод | Златен катализатор и приложението му при горивниелементи |
-
1999
- 1999-09-02 GB GB0107089A patent/GB2357628A/en not_active Withdrawn
- 1999-09-02 CA CA002343519A patent/CA2343519A1/en not_active Abandoned
- 1999-09-02 WO PCT/IB1999/001495 patent/WO2000013791A1/en not_active Ceased
- 1999-09-02 DE DE19983527T patent/DE19983527T1/de not_active Withdrawn
- 1999-09-02 AU AU53827/99A patent/AU5382799A/en not_active Abandoned
- 1999-09-03 US US09/389,320 patent/US20020012828A1/en not_active Abandoned
- 1999-12-01 TW TW088120953A patent/TW487599B/zh active
Also Published As
| Publication number | Publication date |
|---|---|
| US20020012828A1 (en) | 2002-01-31 |
| WO2000013791A1 (en) | 2000-03-16 |
| CA2343519A1 (en) | 2000-03-16 |
| GB2357628A (en) | 2001-06-27 |
| DE19983527T1 (de) | 2001-08-02 |
| GB0107089D0 (en) | 2001-05-09 |
| AU5382799A (en) | 2000-03-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Lindström et al. | Hydrogen generation by steam reforming of methanol over copper-based catalysts for fuel cell applications | |
| An et al. | Carbon-neutral sustainable energy technology: Direct ethanol fuel cells | |
| Li et al. | The CO poisoning effect in PEMFCs operational at temperatures up to 200 C | |
| Hu et al. | CO tolerance of nano-architectured Pt–Mo anode electrocatalysts for PEM fuel cells | |
| CN100438160C (zh) | 用于燃料电池的Pt/Ru合金催化剂 | |
| JP5792220B2 (ja) | ガス拡散基材および電極 | |
| US20230366109A1 (en) | Solid acid electrochemical cells for the production of hydrogen | |
| JPH11250922A (ja) | 100℃を超える温度で動作するポリマー膜電気化学的電池 | |
| CN101168130A (zh) | 用于氧化一氧化碳的催化剂及其制备方法 | |
| TW487599B (en) | A fuel cell for conversion of a fuel and an oxidant into a reaction product and a catalyst for use in said fuel cell | |
| US6692856B2 (en) | High throughput screening device for combinatorial chemistry | |
| CN102895984B (zh) | 电催化触媒及包含该电催化触媒的燃料电池 | |
| WO2003056649A1 (en) | Fuel cell | |
| JP2001522122A (ja) | 燃料電池用金触媒 | |
| US20110036012A1 (en) | Method for prereforming ethanol | |
| Rahman et al. | On-board H2 generation by a catalytic hollow fibre microreactor for portable device applications | |
| Tsiplakides et al. | Electrochemical promoted catalysis: towards practical utilization | |
| KR100520439B1 (ko) | 직접 포름산 연료전지용 백금계 합금 촉매 | |
| Yoon et al. | Effects of low hydrocarbons on the solid oxide fuel cell anode | |
| Basu | Fuel cell systems | |
| Tu et al. | Paper‐structured catalyst with a dispersion of ceria‐based oxide support for improving the performance of an SOFC fed with simulated biogas | |
| US20050119119A1 (en) | Water gas shift catalyst on a lanthanum-doped anatase titanium dioxide support for fuel cells application | |
| EP1923939A2 (en) | Fuel oxidizing catalyst, method for preparing the same, and reformer and fuel cell system including the same | |
| Karanfil et al. | The electrochemical mechanism and transport phenomenon of liquid fuel cells | |
| Dahl et al. | The use of tin oxide in fuel cells |