TW200522427A - Reinforced polymer electrolyte membrane - Google Patents
Reinforced polymer electrolyte membrane Download PDFInfo
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- H01M8/103—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh]
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Description
200522427 九、發明說明: 【發明所屬之技術領域】 本發明係關於一種製造經補強之聚合物電解質薄膜(例 如’可用於諸如燃料電池之電解電池者)之方法,其包含下 列步驟:使磺酸鹽-或_化磺醯基_官能聚合物與雙脒化合物 混合’且隨後使該雙脒化合物之脒基三聚以形成三嗪鍵 聯。接著可將卣化磧醯基或續酸鹽基轉化為確酸基,此轉 化產生經聚三嗪補強之聚合物電解質。 【先前技術】 _ 據稱國際專利申請公開案第W〇 〇2/5〇142 A1號揭示了基 於具有低Tg的偏二氟乙烯之氟磺化腈可交聯彈性體。 據稱美國專利第5,260,351號揭示在不存在固化劑之狀況 下藉由輕射而固化之全氟彈性體。據稱該參照案係關於全 氟化聚合物(例如彼等由四氟乙烯、全氟烷基全氟乙烯醚製 得的聚合物)之固化及在所得三聚物中提供至少一腈、全氟 苯基、溴或碘之固化位點或交聯單元。 據稱美國專利第5,527,861號揭示含腈之全氟彈性體,其 係由過氧化物、輔劑及使用腈基來引起交聯形成之催化劑 的組合來固4匕。 據稱美國專利第 4,334,082、4,414,159、4,440,917 及 4,454,247號揭示一種用於氣-驗電解電池之離子交換薄 膜’其係由下列各物之共聚物形成··下式之乙稀醚單體, Y2CF0(CF(CF3)CF20)nCF = CF2 (其中 Y係選自由 CF2CN、cf2co2r、CF2C02H、cf2co2m、 96836.doc 200522427 CFKONH2及CFaCONR組成之群);選自四氟乙烯、六氟丙 稀及全氟烷基乙烯醚之全氟化共聚單體;及 CF2=CF(〇CF2CF(CF3))nOCF2CF2S〇2F, 其中η為1或2(4,454,247之請求項1)。據稱該等參照案揭 示一種藉由使腈三聚形成三嗪環來固化含氟彈性體之方 法。(4,454,247第 10卷,第 60-68 頁。) 據稱美國專利第4,242,498號揭示交聯彈性體之聚三σ秦。 據稱美國專利第5,693,748號揭示高分子量聚亞胺基脒及 自其竹生之局分子量聚三唤。 美國專利第6,277,5 12號揭示包含離子鍵共聚聚合物與結 構膜形成聚合物的均勻混合物之聚合物電解質薄膜。視情 況使一或兩者交聯。 【發明内容】 簡言之,本發明提供一種製造聚合物電解質薄膜之方 法,其包含下列步驟·· a)提供包含氟化主鏈及第一側基(包 含選自_化磺醯基及磺酸鹽基之基團)的聚合物與雙脒化 合物之混合物;b)使該混合物形成薄膜;及c)使脒基反應以 形成三嗪基。該方法可包含額外步驟d) ··將選自_化磺醯 基及項酸鹽基之基團轉化為績酸基。該等雙脒化合物一般 為根據下式之化合物: H2N(HN=)C-Rn-C(=NH)NH2 (I), 其中R11為包含1-1 5個碳原子及0-4個氧原子之二價、分枝或 未分枝、部分氟化或全氟化烷基或醚基。第一側基一般係 根據下式:-W-SC^X,其中X為鹵素或-〇-A+,其中A+為任 96836.doc 200522427 =適之有機或無機陽離子,’然而最—般為錄陽離子,且 二=包含⑻個碳原子及G_4個氧原子之分枝或未分枝 二“土或全乳醚基,最-般為-〇-civcf2-cf2-cf2-so2x或 -ΓΐΤΓ-ο_€w °# ^^ ^ ^ ^ ^ ^ ^ 7:1巾’該基質-般為多孔聚四款乙稀網狀物。 ;巾料㈣供根據任何本發W彳法製得的 聚合物電解質薄膜。 之ΐ=Γ’本發明提供包含下列各物的均勻混合物 二物^質薄臈:a)包含氟化主鏈與包含續酸基的第 之第-聚合物;叫作為氟化聚三噪之第二聚合 勿。弟:側基-般係根據下式:_R1_S03H,其中R1為包含 ::原子及〇·4個氧原子之分枝或未分枝全嶋或全 亂醚基,更一如劣 舨為-〇-civcf2-cf2-cf2-so3h 或 把據下2r(CF3)_0-CF2-CIVS03H。該第二聚合物一般包含 根據下式之三價基團:
(II), 其係由二價基團_RU隶 ^ ^ n 連接,其中R為包含卜15個碳原子及 乳原子之分枝或未分枝、部分氟化或全氟化烷基或制 基二更-般地,R"為包含2,破原子之全氣化烧基,且遷 , g此合物可嵌入諸如多孔聚四氟乙烯紹 狀物之多孔支承基質中。 在該申請案中: 96836.doc 200522427 聚合物之”當量,,(EW)意謂將中和一當量鹼之聚合物重 量; 、 聚合物之”水合乘積"(HP)意謂對於存在於薄膜中之每當 量磺酸基而言,由薄膜吸收之水的當量(莫耳)數乘以該聚合 物之當量;及 π高度氟化”意謂含有40重量%或更多、一般5〇重量%或更 多且更一般為60重量%或更多的量之氟。 【實施方式】 本發明提供聚合物電解質薄膜。該薄膜係由下列步驟製 付·首先使包含氟化主鏈及第一側基之聚合物與雙脎化合 物混合,該等側基包括根據式_S〇2X之基團,其中χ為鹵素 或-Ο A,其中A+為任何合適之有機或無機陽離子,·及其次 使脒基三聚以形成包含三嗪基之鍵聯,意即根據下式之三 價基團:
(II)。 該等經補強之聚合物電解質薄膜(PEM)可用於諸如燃料電 池之電解電池。 由根據本發明之交聯聚合物製得的PEM可用以製造用於 燃料電池之薄膜電極組件(MEA)。MEA為質子交換薄膜燃 料電池(例如氫燃料電池)之核心元件。燃料電池係由燃料 (如氫)與氧化劑(如氧)之催化化合來產生可用電之電化學 電池。典型MEA包含聚合物電解質薄膜(PEM)(亦稱作離子 96836.doc 200522427 傳導薄膜(ICM)),其充當固體電解質。PEM之一面與陽極 電極層接觸,且對立面與陰極電極層接觸。每個電極層包 括電化學催化劑,其一般包括鉑金屬。氣體擴散層(GDL) 有助於氣體自陽極及陰極電極材料來回傳送且傳導電流。 GDL亦可稱為流體傳送層(FTL)或擴散體/集電器。陽 極電極層及陰極電極層可以催化劑墨水形式應用於GDL, 並將PEM夾於所得經塗佈之GDL中以形成五層mea。或 者陽極電極層及陰極電極層可以催化劑墨水形式應用於 PEM之對立側面,並將兩個(3:〇1^夾於所得經催化劑塗佈之 薄膜(CCM)中以形成五層MEA。五層MEA之五個層依次 為··陽極GDL,陽極電極層,PEM,陰極電極層及陰極gD]l。 在典型PEM燃料電池中,於陽極處經氫的氧化作用形成質 子,並將其經PEM傳送至陰極以與氧反應,此過程產生在 與電極連接之外電路中流動的電流。該簡在反應氣體之 間形成持久性、無孔、非電傳導性機械障壁,然而其亦易 於通過H+離子。
該磺酸鹽-或南化績醢基-官&聚合物包含主鍵,該_雖 然可分枝或未分枝,但—般未分枝。該主鏈係經i化、一 般經高度氟化且更-般經全1化。該主鏈可包含衍生自四 乱乙稀(TFE)之單元(意即,—般為_CF2_CF2_單元)及衍生自 輔單體之單元’-般包括至少—隸據式cF2=cY奴單 元,其中Y雖-般為恤亦可為CF3,且其枝為包括根據式 S〇2X之鹵化續醯基(X為*素)或續酸鹽基(X為-〇_Α+)之第 -侧基。若-so2x為齒化磺醯基’則χ最一般w。若_s〇2X 96836.doc -10- 200522427 為石黃酸鹽,則可;^ y 、 在4何5適之平衡離子A+,其包括有機 或無機平衡離子,包括金屬 八 括至屬離子(如Ll、Na、K及其類似物)、 々四、欠離子,包括環狀化合物及其類似物。在替 代具體貫施例中,可择+垃 了猎由接枝將弟一側基R添加至主鏈中。 ^側基R-般係經高度仏且更—般係經全I化。r可為 方族或非芳族。及一般為_Rl_s〇2X,其中r]為包含⑻個碳 原子及04個氧原子之分枝或未分枝全氟烷基或全氟醚 _ 般為〇-R - ’其中r2為包含1-15個碳原子及〇_4個 氧原子之刀枝或未分枝全氟燒基或全氟驗基。以】更一般為 -0-R3-,其中R3為包含個碳原子之全氟烷基。r1之實例 包括: 12 、 13 、 14或15 (-CF2CF(CF3)-)n,其中 n/^ 1、2、3、4或 5 (-CF(CF3)CF2-)n,其中 η為 1、2、3、4或 5(-CF2CF(CF3)-)n -CF2-,其中 η為 1、2、3 或 4 (-0-CF2CF2-)n,其中!!為1、2、3、4、5、6或7 (-0-CF2CF2CF2-)n,其中 1!為1、2、3、4或5 (-0-CF2CF2CF2CF2-)n,其中 η為 1、2 或 3 (-0-CF2CF(CF3)-)n,其中 η為 1、2、3、4或 5 (-0-CF2CF(CF2CF3)-)n,其中 η為 1、2 或 3 (-0-CF(CF3)CF2-)n,其中 η為 1、2、3、4或 5 (-0-CF(CF2CF3)CF2-)n,其中 η為 1、2 或 3 (-0-CF2CF(CF3)-)n-0-CF2CF2-,其中 η為 1、2、3 或 4 96836.doc -11 - 200522427 (-O-ChCFCCFWFO-VO-CFaCFK,其中 η為 1、2或 3 OO-CFCCFOCFHn-O-CFsCFr,其中 η為 1、2、3 或 4 G〇-CF(CF2CF3)CF2-)n-〇-CF2CF2-,其中 η為 1、2或 3 -〇-(〇卩2)11-,其中11為1、2、3、4、5、6、7、8、9、1()、 11 、 12 、 13或14 R —般為-0-CF2CF2CF2CF2-S02X 或-〇-CF2_CF(CF3)_ 〇-CF2-CF2-S02X,且最常為 _0_CF2CF2CF2CF2_s〇2x。_s〇2X 基團在聚合作用中最常為-S〇2F,意即X為F。-S02X基團在 薄膜形成中一般為。一般在使用含氟聚 合物作為聚合物電解質之前將_S〇2X轉化為_s〇3H。 k i、弟側基R之含氟*单體可由任何合適之手段合成,該 等手段包括美國專利第6,624,328號所揭示之方法。 雙脉化合物一般為根據下式之化合物: H2N(HN=)C-Rn-C(=NH)NH2 ⑴, 其中R11為包含1-1 5個碳原子及…4個氧原子之二價、分枝或 未刀枝邛分氟化或全氟化烧基或_基。R11 一般係經高度 氟化且更一般係經全氟化。Rll一般未分枝。r11一般包含 2-10個碳原子及〇個氧原子。Rn更一般包含2_6個碳原 子及0 個氧原子。 雙脒化合物可在市面上有售或可由任何合適之方法合 成例如,雙脒化合物可藉由添加氨而衍生自根據下式之 腈化合物: NC-RH-c 别(III), 其中R n係如上所述。 96836.doc 200522427 Q物可由任何合適之方法製得,該等方法包括乳液 “作用、㈣聚合作用、超臨界二氧化碳聚合作用、溶 液或料液聚合作用及其類似方法。在—典型聚合作用 中,於南剪應力(24,_ rpm)下以乳化劑(全氣辛酸鐘, c7Fl5C〇o丽4)使 CF2=CF办CF2CF2CF2CF2_s〇2f(mv4s)在 ,中預乳化。將去離子水饋人配備有葉輪授拌器系統之無 氧聚合銷中’並加熱至筑且接著將該預乳液饋入該聚合 鋼中。進-步在該鋼中饋入氣態四氟乙埽⑽)至6·8巴絕 對反應壓力。於5(TC下及240 rpm授拌器速率下,藉由添加 亞硫酸氫鈉及過氧硫酸氫銨來引發聚合作用。在反應過程 中,使反應溫度保持5(TC。藉由將額外TFE饋入氣相中來使 絶對反應壓力保持6-8巴。在反應過程中可持續將第二部分 MV4S預乳液饋入液相中。在饋入足夠TFE之後,單體饋入 可中斷且持續聚合作用允許減少單體氣相壓力。接著可將 反應為排氣並以氮氣吹洗。 在本發明之一具體實施例中,該聚合物係以_化磺醯基 形式進行處理。在替代具體實施例中,該聚合物係以績酸 鹽形式進行處理。 藉由在鹼中水解可將該聚合物之!|化磺醯基轉化為績酸 鹽形式。在一典型製程中,使該聚合物與將會提供如上所 述之合適平衡離子A+的鹼AOH的水溶液接觸。最一般地, AOH為NH4OH。在一具體實施例中,將浸入之薄膜滴定至 中性。在另一具體實施例中,加入稍過量鹼,例如超過存 在之鹵化磺醯基官能數的卜50%。 96836.doc -13- 200522427 該聚合物可以任何合適之方法與雙脒摻合,該等方法包 括在溶液或懸浮液中混合、捏合、研磨或其類似方法。 該摻合物一般在交聯之前形成薄膜。適於形成薄膜之任 何方法均可使用。該掺合物一般係由懸浮液澆鑄而得。可 使用任何合適之澆鎢方法,該等方法包括棒塗、噴塗、隙 縫塗佈、刷塗及其類似方法。或者,可於諸如擠壓之熔融 製程中由純聚合物形成薄膜。在形成之後,可將薄膜退火。 ”亥薄膜一般具有90微米或更少、更一般6〇微米或更少且最 一般30微米或更少之厚度。較薄之薄膜可為離子通過提供 較少阻力。在燃料電池應用中,該狀況導致冷卻操作及可 用旎S之較多輸出。較薄之薄膜必須由在使用中保持結構 元整性之材料製得。在一典型製程中,薄膜係由下列步驟 濟禱而得:將含有㈣固體之水詩液刮刀塗佈至玻璃板 上,並於8(TC下乾燥10分鐘以形成具有约3〇微米厚度之膜。 米★聚作用之步驟可由任何合適之方法來完成。一般 地,猎由應用-般加熱至⑽^或更高t溫度來實現三聚作 卜了視清況使用合適之引發劑或催化劑,其可允 =在奴低μ度下進行三聚作用。合適之引發劑或催化劑可 氨銨化a物’其包括銨鹽及第四銨化合物的鹽,其 包括诸如l - _ 化人 —虱雜雙核[5乂〇]十一 _7_烯(DBU)鹽之環狀 入- 鼠化幾目文®曰、Lewis酸及其類似物之鹽。使聚 又聯之步驟可全部或部分發生於該薄膜之退火步驟 美:ί可與任何退火步驟獨立進行。在三聚步驟中,使醚 土二聚以形成向人二主甘 3二嗪基之鍵聯,意即根據下式之三價基 96836.doc 200522427 團:
在三聚作用之後,第-側基之切官能可由任何合適之 製程轉化為磺酸形式。鹵化磺醯基可藉由水解而發生轉 化。在-典細呈中,冑該聚合物浸入強鹼之水溶:中且 隨後使其酸化。在-典型具體實施例中,將該聚合物薄膜 浸入水中之15% ΚΟΗποΐα!小時,接著以8〇七之2〇%石肖 酸洗滌兩次,接著用去離子水煮彿兩次。磺酸基可藉由以 任何合適之酸進行酸化而發生轉化。在一典型具體實施例 中,將該薄膜用80°C之20〇/〇硝酸洗滌兩次,接著用去離子水 煮彿兩次。 酸-官能侧基之存在量一般足以引起多於15,〇〇〇、更一般 多於18,000、更一般多於22,000且最一般多於25,〇〇〇之水: 乘積(HP)。較高HP通常與較高之離子傳導率相關。 。 酸-官能側基之存在量一般足以引起少於12〇〇、更一般少 於11 〇〇且更一般少於丨000且更一般少於9〇〇之當量(Ew)。 在另一具體實施例中,可在脒基反應之前將含氟聚合物 與雙脉之摻合物吸收於多孔支承基質中,其形式一般為具 有9〇微米或更少、更一般60微米或更少且最一般3〇微米或 更少之厚度的薄膜。任何適於將含氟聚合物與雙脒之推人 物吸收於支承基質的微孔中之方法均可使用,該等方法包 括超壓、真空、燈芯作用(wicking)、浸入及其類似方法。 96836.doc 15 200522427 該摻$物在脒基反應時變得嵌入該基質中。任何合適之支 基貝均可使p該支承基質—般為非電傳導性。該支承 基貝般包括含氟聚合物,其更一般係經全氟化。典型基 質包括多孔聚四l乙稀(PTFE),例如雙軸伸展之ptfe網狀 物。 應瞭解根據本發明方法製得㈣膜可在化學結構、交聯 構父聯位置、酸-β能基位置及其類似物上不同於彼等 由其它方法製得的薄膜。 本U適用力製造用於諸如燃料電池之電解電池的經補 強聚合物電解質薄膜。 本發明之目的及優勢進-步由下列實例來說明,然而不 應認為該等實例所述之特殊材料及其量以及其它條件及詳 述會過度限制本發明。 實例 除非另外說明,否則所有試劑均獲自或購自Aldrich
Chemical Co.,Milwaukee,Wisc〇nsin或可由已知方法合成。 雙脒 σ 如下所述來製備全氟己二腈雙脒 h2n(hn=)c-c4f8-c(=nh)nh2。 將甲醇(188 g ’ 5.9 mol)饋人g己備有磁性攪拌器之四公升 (L)塑料燒瓶中,並經丨小時添加氟化全氟己二醯基(454 g, 1 ·5 则1)(購自 3M Company,St· Paul,Minnes〇ta)。用苛性鹼 洗滌器來處理氫氣酸副產物。添加水,繼而錢下層含氣 化學產物相,藉此來分離全氟己二酸酯(446 g^ 历〇1)。 96836.doc 200522427 在真空乾燥之後,將全氟己二酸酯(446 g,1.4 mol)饋入盛 有曱醇的配備有機械擾拌器之二公升(L)燒瓶中且使其與 過量氨(54 g,3.2 mol)反應,以生成全氟己二醯胺(385 g, 1.3 mol)。將全氟己二醯胺(385 g,1·3 mol)之二曱基甲醯胺 溶液饋入具有機械攪拌器之三公升(L)燒瓶中,且於-i(TC下 首先與σ比咬(508 g,6·4 mol)反應,繼而與三氟乙酸酐(674 g,3.2 mol)(購自 Aldrich Chemical Co·,Milwaukee, Wisconsin)反應。添加水,繼而蒸館下層含氟化學產物相, 藉此來分離具有64°C沸點之全氟己二腈(235 g,0.9 mol)。 在真空乾燥之後,將全氟己二腈(108 g,0.4 mol)饋入盛有 二乙醚的配備有機械攪拌器之一公升(L)燒瓶中,並於-i〇°G 下與氨(17 g,1 .Omol)反應以生成具有132°C熔點之全氟己 二腈雙脒(112 g,0·9 mol)。由氟及質子NMR來證實該結構。 聚合物 本發明實例所用聚合物電解質係由四氟乙烯(TFE)與 CF2=CF-0-(CF2)4-S02F(MV4S)之乳液共聚作用製得,其係 由美國專利第6,624,328號所揭示之方法來合成。 使用 ULTRA-TURRAX® Model T 25 分散劑 S25KV-25F (IKA-Werke GmbH & Co· KG,Staufen,Germany),於高剪應 力(24,000 rpm)下以APFO乳化劑(全氟辛酸銨, C7F15COONH4)使MV4S在水中預乳化,歷經2分鐘。將去離 子水饋入配備有葉輪攪拌器系統之聚合鍋中。將該鍋加熱 至50°C且接著將預乳液饋入無氧聚合鍋中。於50°C下,進 一步在該鍋中饋入氣態四氟乙烯(TFE)至6巴絕對反應壓 96836.doc 17 200522427 力。於50 C下及240 rpm攪拌器速率下,藉由添加亞硫酸氫 納及過氧硫酸氫銨來引發聚合作用。在反應過程中,使反 應溫度保持5 0 °C。藉由將額外T F E饋入氣相中來使絕對反應 壓力保持6巴。如上所述來製備第二部分MV4S_預乳液。在 反應過程中持續將第二預乳液部分饋入液相中。 在饋入額外TFE以後,關閉單體閥且中斷單體饋入。持續 聚合作用將單體氣相壓力減至約2巴。此時,將反應器排氣 並用氮氣吹洗。 將如此獲得的聚合物分散液與5當量Li〇H(基於氣化石黃醯_ 基/辰度)及足里水混合以製得2〇〇/。聚合物固體混合物。將該 混合物於250。〇加熱,歷經4小時。在該等狀況下,大多數 聚合物(大於95%)變得分散。過滤該分散液以移除UF及未 刀政之聚合物,且接著於Mitsubishi 隱離子交 =樹脂上進行離子交換以生成酸形式之離子鍵共聚物。所 付承合物電解質為具有根據下式之酸性側鍵的全氣化聚合 物〇 (CF2)4-S03H。所得混合物為含有18至19%聚合物固鲁 "夂性刀政液。將该分散液於真空中濃縮至約38%固 體’且接著與正丙醇混合以生成在水/正丙醇溶劑混合物(約 桃水/60%正丙醇)中之所要2Q%㈣分散液。 澆鑄分散液及薄膜 將相對於聚合物巾的續酸基紅丨當量之量的丽4〇H添 加至以上所獲得的聚合物分散液中,以使石黃酸基轉化為石黃 *基團。添加全氟己二腈雙肺h2n(hn=)c-(顧)丽2以使中性聚合物與雙脒達到_別重量比。 96836.doc -18- 200522427 將》亥懸子液到刀塗佈至玻璃盤上,於,c下 鐘,並於增下退火3。分鐘,藉此來細 = 其交聯。所得膜之厚度為⑽㈣。 -並使 分析 圖1與2代表根據以上所製得的薄膜材料之设光譜。該光 譜揭示位於1555⑽]之蜂,其代表三嗓。此結果證明Γ聚 作用可於該聚合物之中性續酸鹽官能存在時發生。 在不脖離本發明料及原則之狀況下,本發明之各種修 正與更改對於熟習此項技術者而言將變得顯而易見,且應 瞭解本發明並未過度限於上文所述之說明性具體實施例。 【圖式簡單說明】 圖1為根據本發明之聚合物電解質薄膜樣品的IR圖譜。 圖2為圖1之IR圖譜的詳圖,其突出了 2〇〇〇_13〇〇波數之範 圍。 96836.doc -19-
Claims (1)
- 200522427 十、申請專利範圍: 1 · 一種製造聚合物電解質薄膜之方法,纟包含以下步驟: a) 提供包含氟化主鏈及第一側基之聚合物與雙脉化合 物的此合物’其中該等第_側基包含選自_化續酿基及 磺酸鹽基之基團; b) 使該混合物形成薄膜;及 C)使該雙肺化合物之該特、基反應以形成三嗔基。 2.如請求項1之方法,其在步驟c)之後,額外包含下列步驟: 句將該等選自由化石黃醮基及續酸鹽基之基團轉化為石黃 酸基。 3·如請求項1或2之方法,其中步驟b)包含將該混合物吸 孔支承基質中。 4. 5· 如請求項1至3中任一 j苜夕士、l ^ ^ w 項之方法,其中該等第一側基係根 據:式、R'-S〇2X,其中XWA+,其中A+為有機或無 機陽離子,且其巾R1為包含M5個碳原子及。_4個氧原子 之分枝或未分枝全氟烷基或全氟醚基。 、 如請求項⑴中任—項之方法,其中該等第一側基係根 據下式.-R -S02X ’其中χ為鹵素,且其中尺丨為包含“I。 個碳原子及0·4個氧原子之分技或未分枝全敦烧基或全氣 其中或等雙腩化合物係 6 ·如請求項1至5中任一項之方法 選自根據下式之化合物: H2N(HN=)C-R11-C(-NH)NH2 ⑴, 子之二價、分 其中R11為包含1-15個碳原?及"個氧原 96836.doc 200522427 f或未分枝、部分氟化或全氟化淀基或趟基。 7. ^如請求項1至6中任一項之方法製得的聚合物電解質 8· 一:合膜’其包含下列各物之均勻混合物: 基;及“物’其包含敗化主鏈及包含續酸基之第-側 b)第二聚合物,其為聚氟化三嗪。 9. 項k聚合物電解f薄膜,其中該等第—側基係根 : 娜11,其令R,為包含個碳原子及〇-4個 乳原子之分枝或未分枝全氟貌基或全氟醚基。 10·如請求項8或9之聚合物電解質薄膜,其中該第二聚合物 包含根據下式之三價基團:(II),, 該等三價基團係由二價基團_Rn·連接,其中r"為包含 1七個碳原子及0·4個氧原子之分枝或未分枝、部分氣化 或全氟化烧基或鍵基。 "•如請求項8至Η)中任-項之聚合物電解質薄膜,其中該均 勻混合物係喪入多孔支承基質中。 96836.doc
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Families Citing this family (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4427291B2 (ja) * | 2003-09-03 | 2010-03-03 | 東亞合成株式会社 | 機能性膜の連続製造方法 |
US7071271B2 (en) * | 2003-10-30 | 2006-07-04 | 3M Innovative Properties Company | Aqueous emulsion polymerization of functionalized fluoromonomers |
US7179847B2 (en) | 2003-11-13 | 2007-02-20 | 3M Innovative Properties Company | Polymer electrolytes crosslinked by e-beam |
US7259208B2 (en) * | 2003-11-13 | 2007-08-21 | 3M Innovative Properties Company | Reinforced polymer electrolyte membrane |
US7265162B2 (en) * | 2003-11-13 | 2007-09-04 | 3M Innovative Properties Company | Bromine, chlorine or iodine functional polymer electrolytes crosslinked by e-beam |
US7074841B2 (en) | 2003-11-13 | 2006-07-11 | Yandrasits Michael A | Polymer electrolyte membranes crosslinked by nitrile trimerization |
US7060756B2 (en) * | 2003-11-24 | 2006-06-13 | 3M Innovative Properties Company | Polymer electrolyte with aromatic sulfone crosslinking |
US7112614B2 (en) * | 2003-12-08 | 2006-09-26 | 3M Innovative Properties Company | Crosslinked polymer |
US7060738B2 (en) * | 2003-12-11 | 2006-06-13 | 3M Innovative Properties Company | Polymer electrolytes crosslinked by ultraviolet radiation |
US7173067B2 (en) * | 2003-12-17 | 2007-02-06 | 3M Innovative Properties Company | Polymer electrolyte membranes crosslinked by direct fluorination |
US7635062B2 (en) * | 2005-03-11 | 2009-12-22 | Bha Group, Inc. | Composite membrane |
WO2008053864A1 (en) * | 2006-10-30 | 2008-05-08 | Nippon Steel Chemical Co., Ltd. | Proton conducting compound and proton conducting polymer |
CN101020758B (zh) * | 2007-02-25 | 2010-05-19 | 山东东岳神舟新材料有限公司 | 一种聚合物离子交换膜及其制备方法 |
EP2554579B1 (en) | 2008-04-24 | 2016-03-30 | 3M Innovative Properties Company | Proton conducting materials |
US20100040926A1 (en) * | 2008-06-23 | 2010-02-18 | Nuvera Fuel Cells, Inc. | Consolidated fuel cell electrode |
US8785023B2 (en) | 2008-07-07 | 2014-07-22 | Enervault Corparation | Cascade redox flow battery systems |
US7820321B2 (en) | 2008-07-07 | 2010-10-26 | Enervault Corporation | Redox flow battery system for distributed energy storage |
CN101320817B (zh) * | 2008-07-11 | 2010-04-14 | 山东东岳神舟新材料有限公司 | 一种纤维增强的多层含氟交联掺杂离子膜及其制备方法 |
CN101670246B (zh) * | 2008-07-22 | 2011-11-23 | 山东东岳神舟新材料有限公司 | 一种微孔膜增强的多层含氟交联掺杂离子膜及其制备方法 |
CN101721922B (zh) * | 2008-07-22 | 2011-12-28 | 山东华夏神舟新材料有限公司 | 一种微孔膜增强的多层含氟交联掺杂离子膜及其制备方法 |
GB0917450D0 (en) * | 2009-10-06 | 2009-11-18 | 3M Innovative Properties Co | Triazine containing fluoropolyether elastomers having very low glass transition temperatures, compositions containing them and methods of making them |
WO2011129967A2 (en) | 2010-04-16 | 2011-10-20 | 3M Innovative Properties Company | Proton conducting materials |
US9893373B2 (en) | 2010-05-25 | 2018-02-13 | 3M Innovative Properties Company | Reinforced electrolyte membrane |
US8927612B2 (en) | 2010-06-18 | 2015-01-06 | Shandong Huaxia Shenzhou New Material Co., Ltd. | Composite having ion exchange function and preparation method and use thereof |
EP2583747B1 (en) | 2010-06-18 | 2016-09-21 | Shandong Huaxia Shenzhou New Material Co., Ltd. | Fluorine containing ionomer composite with ion exchange function, preparation method and use thereof |
US8980484B2 (en) | 2011-03-29 | 2015-03-17 | Enervault Corporation | Monitoring electrolyte concentrations in redox flow battery systems |
US8916281B2 (en) | 2011-03-29 | 2014-12-23 | Enervault Corporation | Rebalancing electrolytes in redox flow battery systems |
GB2550018B (en) * | 2016-03-03 | 2021-11-10 | Xergy Ltd | Anion exchange polymers and anion exchange membranes incorporating same |
KR20230152725A (ko) | 2021-03-29 | 2023-11-03 | 저지앙 하이프루프 뉴 에너지 컴퍼니 리미티드 | 특수 고강화 불소 함유 양성자 또는 이온 교환막의 복합막, 복합막 전극, 특수 고강화 불소 함유 클로르-알칼리 전지막, 특수 이형막 및 이의 제조 방법 |
Family Cites Families (98)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3282875A (en) | 1964-07-22 | 1966-11-01 | Du Pont | Fluorocarbon vinyl ether polymers |
GB1184321A (en) | 1968-05-15 | 1970-03-11 | Du Pont | Electrochemical Cells |
US3635926A (en) | 1969-10-27 | 1972-01-18 | Du Pont | Aqueous process for making improved tetrafluoroethylene / fluoroalkyl perfluorovinyl ether copolymers |
US3784399A (en) | 1971-09-08 | 1974-01-08 | Du Pont | Films of fluorinated polymer containing sulfonyl groups with one surface in the sulfonamide or sulfonamide salt form and a process for preparing such |
US4000356A (en) | 1972-06-19 | 1976-12-28 | Dynamit Nobel Aktiengesellschaft | Process for the preparation of thermoplastically workable fluoro-olefin polymers |
US3853828A (en) | 1973-11-21 | 1974-12-10 | Us Army | Process for crosslinking fluorocarbon polymers |
US4169023A (en) | 1974-02-04 | 1979-09-25 | Tokuyama Soda Kabushiki Kaisha | Electrolytic diaphragms, and method of electrolysis using the same |
US4035565A (en) | 1975-03-27 | 1977-07-12 | E. I. Du Pont De Nemours And Company | Fluoropolymer containing a small amount of bromine-containing olefin units |
US4073752A (en) | 1975-06-02 | 1978-02-14 | The B. F. Goodrich Company | High normality ion exchange membranes containing entrapped electrostatically bulky multicharged ions and method of production |
GB1518387A (en) | 1975-08-29 | 1978-07-19 | Asahi Glass Co Ltd | Fluorinated cation exchange membrane and use thereof in electrolysis of an alkali metal halide |
US4508603A (en) | 1976-08-22 | 1985-04-02 | Asahi Glass Company Ltd. | Fluorinated cation exchange membrane and use thereof in electrolysis of an alkali metal halide |
JPS5329291A (en) | 1976-09-01 | 1978-03-18 | Toyo Soda Mfg Co Ltd | Cation exchange membrane and production of the same |
JPS5397988A (en) | 1977-02-08 | 1978-08-26 | Toyo Soda Mfg Co Ltd | Production of cation exchange membrane |
FR2387260A1 (fr) | 1977-04-12 | 1978-11-10 | Rhone Poulenc Ind | Membranes echangeuses d'ions |
US4230549A (en) | 1977-05-31 | 1980-10-28 | Rai Research Corporation | Separator membranes for electrochemical cells |
JPS53149881A (en) | 1977-06-03 | 1978-12-27 | Asahi Glass Co Ltd | Strengthened cation exchange resin membrane and production thereof |
DE2964541D1 (en) | 1978-09-05 | 1983-02-24 | Ici Plc | Sulphonated polyaryletherketones and process for the manufacture thereof |
US4281092A (en) | 1978-11-30 | 1981-07-28 | E. I. Du Pont De Nemours And Company | Vulcanizable fluorinated copolymers |
US4242498A (en) | 1979-04-09 | 1980-12-30 | Frosch Robert A | Process for the preparation of fluorine containing crosslinked elastomeric polytriazine and product so produced |
US4330654A (en) | 1980-06-11 | 1982-05-18 | The Dow Chemical Company | Novel polymers having acid functionality |
US4470889A (en) | 1980-06-11 | 1984-09-11 | The Dow Chemical Company | Electrolytic cell having an improved ion exchange membrane and process for operating |
DE3023455A1 (de) | 1980-06-24 | 1982-01-14 | Hoechst Ag, 6000 Frankfurt | Verfahren zur fluorierung von polymeren und perfluorierte ionenaustauscher |
US4334082A (en) | 1980-09-26 | 1982-06-08 | E. I. Du Pont De Nemours And Company | Dialkyl perfluoro-ω-fluoroformyl diesters and monomers and polymers therefrom |
US4414159A (en) | 1980-09-26 | 1983-11-08 | E. I. Du Pont De Nemours & Co. | Vinyl ether monomers and polymers therefrom |
ZA818207B (en) | 1980-11-27 | 1982-10-27 | Ici Australia Ltd | Permselective membranes |
US4391844A (en) | 1981-06-26 | 1983-07-05 | Diamond Shamrock Corporation | Method for making linings and coatings from soluble cross-linkable perfluorocarbon copolymers |
US4454247A (en) | 1981-12-14 | 1984-06-12 | E. I. Du Pont De Nemours & Company | Ion exchange membranes |
US4440917A (en) | 1981-12-14 | 1984-04-03 | E. I. Du Pont De Nemours & Company | Vinyl ethers monomers and polymers therefrom |
EP0188486B1 (fr) | 1984-07-13 | 1989-02-01 | Elf Atochem S.A. | Nouveau polymere fluore ionique, son procede de preparation et les membranes d'electrolyse formees a partir de ce polymere |
JPH0641494B2 (ja) | 1984-08-31 | 1994-06-01 | 旭化成工業株式会社 | 架橋可能な含フツ素共重合体 |
US4686024A (en) | 1985-02-01 | 1987-08-11 | The Green Cross Corporation | Novel perfluoro chemicals and polyfluorinated compounds and process for production of the same |
US4743419A (en) | 1985-03-04 | 1988-05-10 | The Dow Chemical Company | On-line film fluorination method |
US4755567A (en) | 1985-11-08 | 1988-07-05 | Exfluor Research Corporation | Perfluorination of ethers in the presence of hydrogen fluoride scavengers |
JP2750594B2 (ja) | 1989-02-01 | 1998-05-13 | 旭化成工業株式会社 | 高分子量ポリイミドイルアミジンとその製造法および用途 |
US5693748A (en) | 1989-02-01 | 1997-12-02 | Asahi Kasei Kogyo Kabushiki Kaisha | High molecular weight polyimidoylamidine and a polytriazine derived therefrom |
US5986012A (en) | 1989-04-24 | 1999-11-16 | E. I. Du Pont De Nemours And Company | Fluorination of radiation crosslinked perfluoroelastomers |
US5260351A (en) | 1989-04-24 | 1993-11-09 | E. I. Du Pont De Nemours And Company | Radiation curing of perfluoroelastomers |
IT1235545B (it) | 1989-07-10 | 1992-09-09 | Ausimont Srl | Fluoroelastomeri dotati di migliore processabilita' e procedimento di preparazione |
US5852148A (en) | 1991-07-10 | 1998-12-22 | Minnesota Mining & Manufacturing Company | Perfluoroalkyl halides and derivatives |
US6048952A (en) | 1991-07-10 | 2000-04-11 | 3M Innovative Properties Company | Perfluoroalkyl halides and derivatives |
US5264508A (en) | 1992-06-25 | 1993-11-23 | The Dow Chemical Company | Polymers of haloperfluoro and perfluoro ethers |
US5330626A (en) | 1993-02-16 | 1994-07-19 | E. I. Du Pont De Nemours And Company | Irradiation of polymeric ion exchange membranes to increase water absorption |
US5608022A (en) | 1993-10-12 | 1997-03-04 | Asahi Kasei Kogyo Kabushiki Kaisha | Perfluorocarbon copolymer containing functional groups and a method for producing it |
US5466930A (en) | 1994-02-23 | 1995-11-14 | Florida State University | Solid scintillators for detecting radioactive ions in solution |
US5447993A (en) | 1994-04-19 | 1995-09-05 | E. I. Du Pont De Nemours And Company | Perfluoroelastomer curing |
JP3298321B2 (ja) | 1994-08-31 | 2002-07-02 | ダイキン工業株式会社 | ビニリデンフルオライド系共重合体水性分散液、ビニリデンフルオライド系シード重合体水性分散液およびそれらの製法 |
US6254978B1 (en) | 1994-11-14 | 2001-07-03 | W. L. Gore & Associates, Inc. | Ultra-thin integral composite membrane |
US5547551A (en) | 1995-03-15 | 1996-08-20 | W. L. Gore & Associates, Inc. | Ultra-thin integral composite membrane |
USRE37701E1 (en) | 1994-11-14 | 2002-05-14 | W. L. Gore & Associates, Inc. | Integral composite membrane |
USRE37307E1 (en) | 1994-11-14 | 2001-08-07 | W. L. Gore & Associates, Inc. | Ultra-thin integral composite membrane |
US5795496A (en) | 1995-11-22 | 1998-08-18 | California Institute Of Technology | Polymer material for electrolytic membranes in fuel cells |
DE19622337C1 (de) | 1996-06-04 | 1998-03-12 | Dlr Deutsche Forschungsanstalt | Vernetzung von modifizierten Engineering Thermoplasten |
US5798417A (en) | 1996-10-15 | 1998-08-25 | E. I. Du Pont De Nemours And Company | (Fluorovinyl ether)-grafted high-surface-area polyolefins and preparation thereof |
US5747546A (en) | 1996-12-31 | 1998-05-05 | The Dow Chemical Company | Ion-exchange polymers having an expanded microstructure |
DE69835366T2 (de) | 1997-03-31 | 2007-07-19 | Daikin Industries, Ltd. | Verfahren zur herstellung von perfluorvinylethersulfonsäure-derivaten |
DE69827239T2 (de) | 1997-07-25 | 2005-12-01 | Acep Inc., Montreal | Aus ionischen Perfluorvinylverbindungen gewonnene Membranen |
US6248469B1 (en) | 1997-08-29 | 2001-06-19 | Foster-Miller, Inc. | Composite solid polymer electrolyte membranes |
JPH11111310A (ja) | 1997-09-30 | 1999-04-23 | Aisin Seiki Co Ltd | 燃料電池用の固体高分子電解質膜およびその製造方法 |
DE19854728B4 (de) | 1997-11-27 | 2006-04-27 | Aisin Seiki K.K., Kariya | Polymerelektrolyt-Brennstoffzelle |
US6462228B1 (en) | 1997-12-22 | 2002-10-08 | 3M Innovative Properties Company | Process for preparation of fluorinated sulfinates |
JPH11204121A (ja) | 1998-01-19 | 1999-07-30 | Aisin Seiki Co Ltd | 固体高分子電解質型燃料電池 |
EP1400539B1 (fr) | 1998-01-30 | 2008-12-03 | Hydro Quebec | Procédé de préparation de polymères sulfonés réticulés |
WO1999045048A1 (en) | 1998-03-03 | 1999-09-10 | E.I. Du Pont De Nemours And Company | Substantially fluorinated ionomers |
JP4150867B2 (ja) | 1998-05-13 | 2008-09-17 | ダイキン工業株式会社 | 燃料電池に使用するのに適した固体高分子電解質用材料 |
US6090895A (en) | 1998-05-22 | 2000-07-18 | 3M Innovative Properties Co., | Crosslinked ion conductive membranes |
CA2330148A1 (en) | 1998-05-29 | 1999-12-09 | E.I. Du Pont De Nemours And Company | Dyeable fluoropolymer fibers and films |
WO2000015679A1 (en) | 1998-09-15 | 2000-03-23 | National Power Plc | Water based grafting |
US6255370B1 (en) | 1999-04-29 | 2001-07-03 | Railroad-Solutions, Llc | Rail spike retention and tie preservation mixture and method |
US6277512B1 (en) | 1999-06-18 | 2001-08-21 | 3M Innovative Properties Company | Polymer electrolyte membranes from mixed dispersions |
JP4539896B2 (ja) | 1999-09-17 | 2010-09-08 | 独立行政法人産業技術総合研究所 | プロトン伝導性膜、その製造方法及びそれを用いた燃料電池 |
US7313429B2 (en) | 2002-01-23 | 2007-12-25 | Stereotaxis, Inc. | Rotating and pivoting magnet for magnetic navigation |
US6423784B1 (en) | 1999-12-15 | 2002-07-23 | 3M Innovative Properties Company | Acid functional fluoropolymer membranes and method of manufacture |
JP4352546B2 (ja) | 1999-12-22 | 2009-10-28 | ユニマテック株式会社 | フルオロエラストマー、その製造方法、架橋性組成物およびその硬化物 |
US6780935B2 (en) | 2000-02-15 | 2004-08-24 | Atofina Chemicals, Inc. | Fluoropolymer resins containing ionic or ionizable groups and products containing the same |
DE10021104A1 (de) | 2000-05-02 | 2001-11-08 | Univ Stuttgart | Organisch-anorganische Membranen |
US6982303B2 (en) | 2000-05-19 | 2006-01-03 | Jochen Kerres | Covalently cross-linked polymers and polymer membranes via sulfinate alkylation |
DE10024576A1 (de) | 2000-05-19 | 2001-11-22 | Univ Stuttgart | Kovalent und ionisch vernetzte Polymere und Polymermembranen |
CA2312194A1 (fr) | 2000-06-13 | 2001-12-13 | Mario Boucher | Elastomeres reticulables fluores bromosulfones a faible tg a base de fluorure de vinylidene et ne contenant ni du tetrafluoroethylene ni de groupement siloxane |
IT1318593B1 (it) | 2000-06-23 | 2003-08-27 | Ausimont Spa | Ionomeri fluorurati. |
IT1318669B1 (it) | 2000-08-08 | 2003-08-27 | Ausimont Spa | Ionomeri fluorurati solfonici. |
EP1359142A4 (en) | 2001-02-01 | 2007-06-13 | Asahi Chemical Ind | PERFLUOROVINYL ETHER MONOMER HAVING A SULFONAMIDE GROUP |
ITMI20010383A1 (it) | 2001-02-26 | 2002-08-26 | Ausimont Spa | Membrane idrofiliche porose |
US6503378B1 (en) | 2001-04-23 | 2003-01-07 | Motorola, Inc. | Polymer electrolyte membrane and method of fabrication |
US7045571B2 (en) | 2001-05-21 | 2006-05-16 | 3M Innovative Properties Company | Emulsion polymerization of fluorinated monomers |
US20040241518A1 (en) | 2001-10-15 | 2004-12-02 | Zhen-Yu Yang | Solid polymer membrane for fuel cell prepared by in situ polymerization |
US6727386B2 (en) | 2001-10-25 | 2004-04-27 | 3M Innovative Properties Company | Aromatic imide and aromatic methylidynetrissulfonyl compounds and method of making |
US7273537B2 (en) | 2002-09-12 | 2007-09-25 | Teck Cominco Metals, Ltd. | Method of production of metal particles through electrolysis |
US6624328B1 (en) | 2002-12-17 | 2003-09-23 | 3M Innovative Properties Company | Preparation of perfluorinated vinyl ethers having a sulfonyl fluoride end-group |
US7348088B2 (en) | 2002-12-19 | 2008-03-25 | 3M Innovative Properties Company | Polymer electrolyte membrane |
US7071271B2 (en) * | 2003-10-30 | 2006-07-04 | 3M Innovative Properties Company | Aqueous emulsion polymerization of functionalized fluoromonomers |
US7259208B2 (en) | 2003-11-13 | 2007-08-21 | 3M Innovative Properties Company | Reinforced polymer electrolyte membrane |
US7074841B2 (en) | 2003-11-13 | 2006-07-11 | Yandrasits Michael A | Polymer electrolyte membranes crosslinked by nitrile trimerization |
US7265162B2 (en) | 2003-11-13 | 2007-09-04 | 3M Innovative Properties Company | Bromine, chlorine or iodine functional polymer electrolytes crosslinked by e-beam |
US7179847B2 (en) | 2003-11-13 | 2007-02-20 | 3M Innovative Properties Company | Polymer electrolytes crosslinked by e-beam |
US7060756B2 (en) * | 2003-11-24 | 2006-06-13 | 3M Innovative Properties Company | Polymer electrolyte with aromatic sulfone crosslinking |
US7112614B2 (en) | 2003-12-08 | 2006-09-26 | 3M Innovative Properties Company | Crosslinked polymer |
US7060738B2 (en) | 2003-12-11 | 2006-06-13 | 3M Innovative Properties Company | Polymer electrolytes crosslinked by ultraviolet radiation |
US7173067B2 (en) | 2003-12-17 | 2007-02-06 | 3M Innovative Properties Company | Polymer electrolyte membranes crosslinked by direct fluorination |
-
2003
- 2003-11-13 US US10/712,360 patent/US7259208B2/en not_active Expired - Fee Related
-
2004
- 2004-10-13 WO PCT/US2004/033799 patent/WO2005052033A1/en active IP Right Grant
- 2004-10-13 EP EP04795020A patent/EP1692211B1/en not_active Not-in-force
- 2004-10-13 AT AT04795020T patent/ATE382068T1/de not_active IP Right Cessation
- 2004-10-13 CN CNB2004800336322A patent/CN100410299C/zh not_active Expired - Fee Related
- 2004-10-13 JP JP2006539504A patent/JP2007513471A/ja active Pending
- 2004-10-13 DE DE602004010932T patent/DE602004010932T2/de not_active Expired - Fee Related
- 2004-10-13 KR KR1020067009327A patent/KR20060117949A/ko not_active Application Discontinuation
- 2004-10-13 CA CA002545169A patent/CA2545169A1/en not_active Abandoned
- 2004-11-01 TW TW093133245A patent/TW200522427A/zh unknown
-
2007
- 2007-07-27 US US11/829,523 patent/US7411022B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP1692211B1 (en) | 2007-12-26 |
EP1692211A1 (en) | 2006-08-23 |
CA2545169A1 (en) | 2005-06-09 |
KR20060117949A (ko) | 2006-11-17 |
JP2007513471A (ja) | 2007-05-24 |
CN100410299C (zh) | 2008-08-13 |
WO2005052033A1 (en) | 2005-06-09 |
ATE382068T1 (de) | 2008-01-15 |
CN1882644A (zh) | 2006-12-20 |
DE602004010932T2 (de) | 2008-12-11 |
DE602004010932D1 (de) | 2008-02-07 |
US20070264561A1 (en) | 2007-11-15 |
US20050107532A1 (en) | 2005-05-19 |
US7411022B2 (en) | 2008-08-12 |
US7259208B2 (en) | 2007-08-21 |
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