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TW200924846A - Siloxane membrane main ingredients - Google Patents

Siloxane membrane main ingredients Download PDF

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Publication number
TW200924846A
TW200924846A TW096147015A TW96147015A TW200924846A TW 200924846 A TW200924846 A TW 200924846A TW 096147015 A TW096147015 A TW 096147015A TW 96147015 A TW96147015 A TW 96147015A TW 200924846 A TW200924846 A TW 200924846A
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Taiwan
Prior art keywords
film
siloxane
sample
modified
membrane
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TW096147015A
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Chinese (zh)
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TWI370752B (en
Inventor
Xin-Guo Hong
zu-de Ren
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Univ Yuan Ze
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

This invention siloxane membrane main ingredients including modified solid containing double bonds of oligo-siloxane, proton conductive monomer and crosslinking agent, and modified absorbent compounds. This invention silicone membrane feature is that the double bond of oligo-siloxane is reaction products from hydroxypropyl-terminated dimethyl siloxane and glycidyl methacrylate. The weight of glycidyl methacrylate is below 30 percent as compared with the weight of hydroxypropyl-terminated dimethyl siloxane. Hydroxypropyl-terminated dimethyl siloxane, molecular weight range of 500 g/mol and 50000 g/mol, can be used in fuel cells and water gel membrane optical products.

Description

200924846 九、發明說明: 【發明所屬之技術領域】 本發明係關於一種矽氧烷膜材,尤指用於燃料電池質子交換 膜的矽氧烷膜材。 【先前技術】 〇 在各種燃料電池中’質子交換膜燃料電池(Proton Exchange200924846 IX. Description of the Invention: [Technical Field] The present invention relates to a decane film, especially a siloxane film for a proton exchange membrane of a fuel cell. [Prior Art] 质 Proton Exchange Membrane Fuel Cell in Various Fuel Cells (Proton Exchange)

Membrane Fuel Cell ;PEMFC)因其材料取得、溫度控制(低於1〇(rc ) 均較其他類型燃料電池簡化,成本可大幅降低,為各國能源開發 技術的重點科技。 質子交換膜(Proton Exchange Membrane, PEM)為燃料電池 產生電化學反應場所。PEM之兩侧產生氧化及還原反應,膜中之 氫離子(H+)在陽極端由膜中的水傳遞至陰極端參與還原反應,生 〇成水與電。質子交換膜為網狀結構,藉由其内部相通的孔隙,使 得離子在其間移動,而構成通路。 離子於離子交換膜的傳導模式可分為兩大類:一為Macro- homogeneous Model,使用Stefan-Maxwell方程式來研究離子傳 導模式’另-為P〇re-model。在膜中氫離子的傳遞是以彻+、h祝 的形態進行。而傳輸一個氫離子詩3〜6個水分子來搭配進行, 其巾氫離子因受到陽極水分子之back_dif —與心加— osmosis的影響,促使.氫離子由電解質膜傳輸_極觸媒層與氧氣 200924846 進行還原反應而產生水;因此若膜中水分子蒸發過多,將使薄膜 導電度變差不穩定。對質子交換膜燃料電池而言,薄膜的電阻對 其電池性能的好壞有歧性的影響;而薄膜的含水量愈高電阻就 愈小’電解質膜愈薄氫離子傳送愈容易,但太薄氣氣和氧氣會造 成Cross-over現象,使電池性能下降。 早期使用之交換膜以苯驗續酸與福馬林經縮合反應成膜,但 是它會污染PEMFC所生成的水並使性能大幅下降,使電池壽命減 ❹短。質子交鋪在陽減應所產生之氯離子會經由高分子電解質 膜傳送至陽極’並與氧賴縣水。錢離子在電膜中傳送 是以聊的型態進行,傳導一個氫離子約f 4~6個水分子,故質 子於高分子膜中運動與膜之含水量相關。而水與甲醇之性質相似 (如相似之偶極距),故在質子傳導時曱醇會與水分子—起經由電 滲透(electro-osmotic)及擴散(diffusi〇n)運動由陽極移動至陰 極’故質子交換膜的保濕能力非常重要。DMpc所用之適合質子傳 ©導膜應具優良氫質子傳導度,但為一電絕緣體。大部分商品化之 膜材包含碳氟高分子域加上側鏈接枝sulf〇nic㈣官能基做 為質子傳導用。 理想質子交換膜必須合有下列性質: (1) 質子導電度高 (2) 電子導電度低 ⑶低燃料滲透率(防止氫氣、曱醇和氧氣CrQSS0ver) 200924846 (4) 尺寸安定性(dimensi〇nai对油出你)佳 (5) 機械強度佳 (6) 薄膜含水量低,必須具有良好的離子導電性 (7) 薄膜於完全乾燥下,其阻抗必須高 (8) 化學穩定佳 目前國内外對於燃料電池質子交換膜的研究著重於提高其導 電度、甲醇的Crossover及尺寸安定性。 © 應用於PEMFC之質子交換膜約可分成: (1)氟素系質子交換膜:如Naf ion membrane、Aeiplex membrane ' XUS membrane # ° 在質子父換膜燃料系統中,質子交換膜的要求是必須要具有 良好的質子導電度、機械強度以及耐久度,杜邦早在196〇年便已 開發出來的Nafion可以符合上述要求。随〇n膜是一帶電荷的氣 碳聚合物,以聚四氟乙稀為原料的陽離子交換臈。其主鍵為疏水 ❹性的說碳化合物,不具有電荷’支鏈則是帶電荷的親水性s〇「陰 離子基’與sor接合的質子可以在聚電解質中自由移動,形成傳 導質子功能。其優點有:高度化學穩定性、高機械度、不導電子、 不透氣性及質子傳導電阻小。 然而’ Nafion膜也有價格過高,以及無法防止甲醇的透過而 造成Cr酿删:之現象產生之缺點。這是因為,全氣系質子交換 膜有極高曱醇滲透率,高曱縣透率的顧是來自於極大的離子 200924846 基團所形成的大通道,而此大通道形成的原因和其高分子結構有 關’且隨著曱醇濃度越高’Crossover會越嚴重,此為造成DMFC性 能衰減的主因。 (2)碳氫類高分子材及其複合材:包括sulfonated poly(phenylene oxide) * sulfonated poly (phenylene sulfide) , sulfonated polysuIfone ’sulfonated polycarbonate > sulfonated polystyrene * sulfonated ❺ polyimide ’ sulfonated polyquinoxaline , sulfonated (phosphonated) polyphosphazene » sulfonated polyetherefeskefone (S-PEEK),sulfonated polybenzimidazole (PBI) , sulfonated polyethersuIfone (SPSU) , sulfonated poly (aryl ether su If one)/Base»Poly (aryl ene ether sulfone) * poly (4-phenoxybe-nzoyl- 1,4-phenylene, poly-X2000 (PPBP) 等及其他各種高分子或無機複合材。Membrane Fuel Cell (PEMFC) is a key technology for energy development technologies in various countries due to its material acquisition and temperature control (less than 1 〇 (rc) is simplified compared to other types of fuel cells. Proton Exchange Membrane , PEM) produces an electrochemical reaction site for the fuel cell. The two sides of the PEM generate oxidation and reduction reactions, and the hydrogen ions (H+) in the membrane are transferred from the water in the membrane to the cathode end at the anode end to participate in the reduction reaction, and the water is produced into water. The proton exchange membrane is a network structure, and the ions communicate with each other through the pores communicating therewith to form a pathway. The conduction modes of ions in the ion exchange membrane can be divided into two categories: one is a Macro-homogeneous model. The Stefan-Maxwell equation was used to study the ion conduction mode 'another' is P〇re-model. The transfer of hydrogen ions in the membrane is carried out in the form of a +, h wish. The transmission of a hydrogen ion poem 3 to 6 water molecules In order to match, the hydrogen ion of the towel is affected by the back_dif of the anode water molecule and the osmosis of the anode. The hydrogen ion is transported by the electrolyte membrane_electrocatalyst layer and oxygen 200924846 The reduction reaction produces water; therefore, if the water molecules in the membrane evaporate too much, the conductivity of the film will become unstable and unstable. For the proton exchange membrane fuel cell, the resistance of the film is disproportionate to the performance of the battery. The effect is; the higher the water content of the film, the smaller the resistance. The thinner the electrolyte membrane is, the easier it is to transfer hydrogen ions, but the too thin gas and oxygen will cause the Cross-over phenomenon, which will degrade the performance of the battery. The exchange membrane used in the early stage is benzene. The test acid and the formalin are condensed to form a film, but it will pollute the water produced by the PEMFC and greatly reduce the performance, so that the battery life will be shortened. The protons will be filtered by the cations. The electrolyte membrane is transported to the anode 'and with the oxygen water. The money ion is transported in the electric film. The hydrogen ion is about 4 to 6 water molecules, so the protons move in the polymer membrane. The water content of the membrane is related. The nature of water and methanol is similar (such as the similar dipole moment), so in proton conduction, sterols will interact with water molecules via electro-osmotic and diffusion (diffusi〇n). The movement moves from the anode to the cathode. Therefore, the moisturizing ability of the proton exchange membrane is very important. The suitable proton transfer membrane used by DMpc should have excellent hydrogen proton conductivity, but it is an electrical insulator. Most commercial membranes contain fluorocarbon. The polymer domain plus the side-linking branch sulf〇nic(iv) functional group is used for proton conduction. The ideal proton exchange membrane must have the following properties: (1) high proton conductivity (2) low electron conductivity (3) low fuel permeability (preventing hydrogen gas) , sterol and oxygen CrQSS0ver) 200924846 (4) Dimensional stability (dimensi〇nai to oil out) Good (5) Good mechanical strength (6) Low moisture content of the film, must have good ionic conductivity (7) The film is completely Under dry conditions, the impedance must be high (8) Chemical stability. At present, research on fuel cell proton exchange membranes at home and abroad focuses on improving its conductivity, crossover and dimensional stability of methanol. © Proton exchange membranes for PEMFC can be divided into: (1) Fluoride proton exchange membranes: such as Naf ion membrane, Aeiplex membrane 'XUS membrane # ° In the proton parent membrane fuel system, the requirement of proton exchange membrane is required To have good proton conductivity, mechanical strength and durability, Dufan, which was developed in 196 years, can meet the above requirements. The 〇n film is a charged carbon polymer, and the cation exchange ruthenium is made of polytetrafluoroethylene. The primary bond is a hydrophobic carbon-based carbon compound, and does not have a charge. The branch is a charged hydrophilic s. The "anion-based" and sor-bonded protons can move freely in the polyelectrolyte to form a conductive proton function. There are: high chemical stability, high mechanical strength, non-conducting, non-breathing and low proton conduction resistance. However, 'Nafion membrane is also too expensive, and can not prevent the transmission of methanol and cause the failure of Cr: This is because the total gas proton exchange membrane has a very high sterol permeability, and the high permeability of the Gaochun County is derived from the large channel formed by the extremely large ion 200924846 group, and the reason for the formation of this large channel and its The polymer structure is related to 'and the higher the concentration of sterol', the more serious the Crossover will be. This is the main cause of the DMFC performance degradation. (2) Hydrocarbon polymer materials and their composite materials: including sulfonated poly(phenylene oxide) * Sulfonated poly (phenylene sulfide) , sulfonated polysuIfone 'sulfonated polycarbonate > sulfonated polystyrene * sulfonated ❺ polyimide ' sulfonated polyqu Inoxaline, sulfonated (phosphonated) polyphosphazene » sulfonated polyetherefeskefone (S-PEEK), sulfonated polybenzimidazole (PBI), sulfonated polyethersuIfone (SPSU), sulfonated poly (aryl ether su If one)/Base»Poly (aryl ene ether sulfone) * poly ( 4-phenoxybe-nzoyl- 1,4-phenylene, poly-X2000 (PPBP) and other various polymer or inorganic composite materials.

❹ (3)非sulfonated高分子膜材:如無機酸doped PBI及PBI 類衍生高分子材。 (4)無機系質子交換膜,如 sulfonated polyphosphazene。 現有DMFC高分子電解質薄膜有: 如 Gore-select from Gore,Nafion from Du Pont ’ Flemion 200924846 from Asahi Glass,Aciplex from Asahi Chemical Co.等之 sulfonated perfluorinated 高分子膜。 SPEEK :商品名 Victrex,ICI ; Fuma-Tech Germany ; Axiva, Germany❹ (3) Non-sulfonated polymer membranes: such as inorganic acid doped PBI and PBI-derived polymer materials. (4) Inorganic proton exchange membranes such as sulfonated polyphosphazene. The existing DMFC polymer electrolyte membranes are: sulfonated perfluorinated polymer membranes such as Gore-select from Gore, Nafion from Du Pont ’ Flemion 200924846 from Asahi Glass, Aciplex from Asahi Chemical Co., and the like. SPEEK : trade name Victrex, ICI ; Fuma-Tech Germany ; Axiva, Germany

Hydrated SPSU:商品名 Udel-Modifiedby Nolte et al.,Kerres et al. BI 類膜材:Celtec V ❹ Modified膜材Hydrated SPSU: trade name Udel-Modifiedby Nolte et al., Kerres et al. BI film: Celtec V ❹ Modified film

Nafion EwllOO : Du Pont Nafion/silica composite * CNR-TAE Institute Transformation & Storage of Energy » Italy BMI doped Nafion : Du Pont S-poly(arylether sulfone) : CNR-TAE Institute Transformation & Storage of Energy , Italy © S-poly(4-phenoxybenzoy 1-1.4-phenylene) :Maxdem Inc,Nafion EwllOO : Du Pont Nafion/silica composite * CNR-TAE Institute Transformation & Storage of Energy » Italy BMI doped Nafion : Du Pont S-poly (arylether sulfone) : CNR-TAE Institute Transformation & Storage of Energy , Italy © S -poly(4-phenoxybenzoy 1-1.4-phenylene) :Maxdem Inc,

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Imidazole doped PEEK · Max Plank Institute FKF » Germany S-PEEK/PBI Blend : University of Stuttgart , Germany S-PSU/PBI Blend · Germany 以專利文獻來看: PBI-H3P〇4: US 5716727、5525436、6099988 200924846Imidazole doped PEEK · Max Plank Institute FKF » Germany S-PEEK/PBI Blend : University of Stuttgart , Germany S-PSU/PBI Blend · Germany Patent documents: PBI-H3P〇4: US 5716727, 5525436, 6099988 200924846

Polysulfone » polyaryl ether/inorganic : US 7008971 S-PEEK : US 6984713 SPES : US 6869986 , EP 0574791A1 S-PSU/PBI : DE 19817374A1 S-Polyaryletherketone : EP 574791A1 然而,上述膜材存在有些許缺點,例如成膜方式因溶劑溶解 © 度受限;另如酸Doping之膜材如PBI/磷酸亦易因水之產生而流失 磷酸降低電池性能;如耐熱穩定性不足,合成成型方式複雜,價 格仍高等缺點。 為了解決上述問題,本發明所發展出的新型改質之石夕氧炫構 造質子交換膜材’可彌補現有膜材(如Nafi〇n)的價昂、成型受限、 甲醇高透過性、高溫質子傳導度降等缺點。 _ 【發明内容】 ❹ 本發明之主要目的在提供一種矽氧烷膜材,其主要固成份包 括改質含雙鍵之梦氧燒寡聚物、質子導電單體、交聯劑、及改質 吸水性化合物,而改質含雙鍵之石夕氧烷寡聚物為羥丙基封端二甲 基矽氧烷(hydroxypropy卜terminated dimethyl siloxane)與甲 基丙稀酸環氧丙脂(glycidyl methacrylate)之反應產物。在製作 膜材時,僅需用UV照射在pet膜上的已攪拌的反應產物,即可使 之硬化成膜,而不須複雜之合成步驟來製作成膜。 11 200924846 本發明之次要目触提供-録氧賊材,著調整其他 反應單體種類、含量、及反應條件,以製作出不職度、延展性 (flexibility)、及成型條件需要之各種麵,_低價格及容易 取得亦為其一大優勢。 基於上述目的’本發日脚紐赌主要固成份包括改質含雙 鍵之石夕氧制^聚物、質子導電單體、交聯劑、及改質吸水性化合 物。本發明矽氧烷膜材的特徵在於,改質含雙鍵之石夕氧炫寡聚物 ❹為羥丙基封端二甲基矽氧烷(hydlOXypn)pyl_terminated dimethyl siloxane)與甲基丙稀酸環氧丙脂(glycidyl methacrylate)之反應產物,且曱基丙稀酸環氧丙脂(glycidyl me thacry late)重量百分比為羥丙基封端二甲基石夕氧烧 (hydroxypropyi-terminated dimethyl sil〇xane)重量 3〇%以下, 羥丙基封端二甲基矽氧烷(hydroxypropyl-terminated dimethyl sil〇xane)分子量範圍為 5〇〇 g/m〇i 至 5〇〇〇〇 g/m〇卜 ❿ 關於本發明之優點與精神可以藉由以下的發明詳述及所附圖 式得到進一步的瞭解。 【實施方式】 本發明矽氧烷膜材配方成分包括(丨)改質含雙鍵之石夕氧烷之 寡聚物’(2)質子導電單體,(3)交聯劑,(4)吸水性單體,(5)光 起始劑。在製作膜材時,僅需用UV照射在PET膜上的已攪拌的反 應產物’即可使之硬化成膜’而不須傳統的複雜合成步驟來製作 12 200924846 成膜。同時,本發明矽氧烷膜材具有高質子傳導性、耐熱、耐化 學樂xm、低曱醇及氣體透過率之特定,而符合一般對於燃料電池 質子交換膜的要求。 具體來說,本發明矽氧烷膜材的改質含雙鍵之發氧烷寡聚 物,為經丙基封端二甲基發氧烧(hydroxypropyherj^nafed dimethyl siloxane)與曱基丙稀酸環氧丙脂(glycidyl methacrylate)之反應產物,且甲基丙稀酸環氧丙脂(glycidyl 〇 methacry1 ate)重量百分比為羥丙基封端二曱基石夕氧烷 (hydroxypropyl-terminated dimethyl si loxane)重量 30%以下, 經丙基封端一甲基矽氧烧(hydr〇xypr〇py丄 Slloxane)分子量範圍為 500 g/m〇l 至 50000 g/m〇卜 在實際製作本發明發氧烧膜材時,上述反應物調整其他反應 單體種類、含量、及反應條件,可製作出不同強度、延展性 (flexibility)、及成型條件需要之各種膜材,同時低價格及容易 ❹取得亦為其一大優勢。 製作本發明矽氧烷膜材步驟為: 1.將上述配方以磁石攪拌3小時。 2·將攪拌均勻配方置於PET膜上使用刮刀使之均勻延伸,再 覆蓋另層PET膜。 3·置入UV光反應槽中(365 nm)硬化600秒成膜。 在本發明發氧烧膜材中的梦化合物及其衍生物(si 1 13 200924846 compounds and their derivatives) ’ 在其化學結構上,可基於 含石夕元素及有齡團’使得本㈣魏_材兼具錢與無機性 質,同時擁有耐熱、耐候、導電、電氣絕緣、撥水、無毒、低表 面張力等眾多優良性能。聚石夕氧燒可在_6〇ΐ〜 35〇ΐ的環境下使 用,也就是溫度敎錄’更因為舰雜好,所以也應用於電 子零件之類的物品。 矽氧烧(siloxane)分子鏈主要化學鍵有㈣與si_c兩種, ©矽氧鍵能為455KJ/mal,較C—C鍵的346鳥〇1及c—〇鍵的 258KJ/m〇l高,使得矽氧化合物較碳氧化合物有更高的熱穩定性。 而石夕氧鍵上的極性或部分離子雜,也使得魏子上的曱基比碳 j的甲基具有更高的熱穩定性與抗氧化性。故石夕氧烧化合物具熱 安定性、抗氧化性、良好的透氧性、電絕緣性、耐候性佳及低應 力化。 树姐上加人t驗目’魏⑥_分子能餘他高分子 ❿結合而生成嵌段性(Block)、交替性(Alt_ting)以及接枝 性伽⑴之_絲物。錄财高分子絲対主要分為三 大方向: ⑴侧鏈騎··帶錢官絲,與賴共聚後將 矽氧烷結構懸掛在高分子侧鏈。 ⑵騎··彻未縣餘卿魏結雛衫分子未兩 200924846 (3)交聯:帶有三個以上相同之官能基的矽氧烷,當交聯劑使 用,使矽氧烧結構成為交聯點。 為了說明本發明矽氧烷膜材中每個成分用量對膜材強度、質 子傳導性、高溫穩定與質子傳導性之影響,及此性能與膜交聯密 度、氣體透過性等膜材基本性質之關連,以鑑定方法包括DSC、 TGA、含水及水分損失測量、甲醇透過率、膨脹率、質子傳導率測 量來說明。 © 本發明矽氧烷膜材範例Polysulfone » polyaryl ether/inorganic : US 7008971 S-PEEK : US 6984713 SPES : US 6869986 , EP 0574791A1 S-PSU/PBI : DE 19817374A1 S-Polyaryletherketone : EP 574791A1 However, the above-mentioned films have some disadvantages, such as film formation. Because the solubility of the solvent is limited, the membrane of the acid Doping such as PBI/phosphoric acid is also easily depleted by the production of water to reduce the performance of the battery; for example, the heat stability is insufficient, the synthetic molding method is complicated, and the price is still high. In order to solve the above problems, the novel modified Shishioxue structure proton exchange membrane developed by the invention can make up for the price of the existing membrane material (such as Nafi〇n), limited molding, high permeability of methanol, high temperature. Proofs such as proton conductivity drop. SUMMARY OF THE INVENTION The main object of the present invention is to provide a decane film whose main solid components include a modified double oxygen-containing oxy-oligomer, a proton conductive monomer, a crosslinking agent, and a modification. a water-absorbing compound, and the modified double-bond-containing oxalate oligo is a hydroxyprop-terminated dimethyl siloxane and a glycidyl methacrylate. The reaction product. In the production of the film, it is only necessary to irradiate the agitated reaction product on the pet film with UV to harden it into a film without complicated synthesis steps to form a film. 11 200924846 The second aspect of the present invention provides the provision of oxygen-cutting thieves, adjusting the types, contents, and reaction conditions of other reactive monomers to produce various aspects of inaugurality, flexibility, and molding conditions. , _ low price and easy to obtain is also a big advantage. Based on the above objectives, the main solid components of the gambling gambling include the modification of the double-bonded yoke oxygen polymer, the proton conductive monomer, the crosslinking agent, and the modified water-absorbing compound. The oxoxane film of the present invention is characterized in that the modified double-bonded oxime oligopolymer oxime is hydroxypropyl terminated dimethyl siloxane (hydlOXypn) pyl_terminated dimethyl siloxane) and methyl acrylate Hydroxypropyl-terminated dimethyl sil〇 Xane) 3% by weight or less, hydroxypropyl-terminated dimethyl sil 〇 xane has a molecular weight ranging from 5 〇〇g/m〇i to 5 〇〇〇〇g/m The advantages and spirit of the present invention will be further understood from the following detailed description of the invention and the accompanying drawings. [Embodiment] The composition component of the oxirane film of the present invention comprises (丨) an oligomer of a ruthenium oxide containing a double bond, (2) a proton conductive monomer, (3) a crosslinking agent, (4) Water-absorbing monomer, (5) photoinitiator. In the production of the film, it is only necessary to use UV to irradiate the stirred reaction product on the PET film to harden it into a film without the need for a conventional complicated synthesis step to produce the film. At the same time, the oxime film of the present invention has high proton conductivity, heat resistance, chemical resistance xm, low sterol and gas transmission specificity, and conforms to the general requirements for a fuel cell proton exchange membrane. Specifically, the modified oxirane film of the present invention contains a double bond-containing oxane oligomer, which is a propyl-terminated dimethyl siloxane and a thiol-acrylic acid. The reaction product of glycidyl methacrylate, and the weight percentage of glycidyl 〇methacry1 ate is hydroxypropyl-terminated dimethyl si loxane The weight of 30% or less, propyl-terminated methoxy 〇 〇 〇 〇 〇 〇 ll ll ll ll 分子量 分子量 分子量 分子量 分子量 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在In the case of the above materials, the above-mentioned reactants can be adjusted to various types, contents, and reaction conditions of the other reaction monomers, and various membrane materials having different strengths, flexibility, and molding conditions can be produced, and at the same time, low prices and easy to obtain are also A big advantage. The procedure for making the oxime film of the present invention is as follows: 1. The above formulation was stirred with a magnet for 3 hours. 2. Place the evenly-mixed formulation on the PET film and spread it evenly with a spatula, then cover the other PET film. 3. Place in a UV light reaction bath (365 nm) for 600 seconds to form a film. The dream compound and its derivative (si 1 13 200924846 compounds and their derivatives) in the oxy-combustion film of the present invention can be based on the chemical structure, and can be based on the stone-bearing element and the age group It has both money and inorganic properties, and has many excellent properties such as heat resistance, weather resistance, electrical conductivity, electrical insulation, water repellency, non-toxicity and low surface tension. It can be used in the environment of _6〇ΐ~35〇ΐ, that is, the temperature record is more suitable for electronic parts and the like because of the good ship. The main chemical bonds of the siloxane molecular chain are (4) and si_c. The energy of the 矽 键 bond is 455 KJ/mal, which is higher than the 258 J 1 of the C-C bond and 258 KJ/m 〇 l of the c-〇 bond. The oxygenate is more thermally stable than the carbon oxide. However, the polar or partial ion heterozygosity on the Shixi oxygen bond also makes the sulfhydryl group on the Weizi have higher thermal stability and oxidation resistance than the methyl group of the carbon j. Therefore, Shixi oxygen-burning compound has thermal stability, oxidation resistance, good oxygen permeability, electrical insulation, good weather resistance and low stress. The tree sister adds the person's inspection. The Wei 6_ molecule can combine with the polymer to form a block, alternating (Alt_ting) and grafting gamma (1). The recording of polymer silk is mainly divided into three major directions: (1) Side chain riding ············································· (2) Riding······································································································ In order to explain the influence of the amount of each component in the siloxane oxide film on the strength, proton conductivity, high temperature stability and proton conductivity of the film, and the basic properties of the film such as film crosslink density and gas permeability. The correlation is described by identification methods including DSC, TGA, water and moisture loss measurement, methanol permeability, expansion ratio, and proton conductivity measurement. © Example of a naphthenic film of the present invention

表一為初始製作之代表性組成,於此所得結果為含水量依含 水單體與㈣成狀乡_改變,厭木叫叙加场所預期降 低含水率,但提料度,此強度提高非啡含水下降而形成。在 此初配方域中樣品7之性質最佳,其麵量、導電度、及強 15 200924846 度等表現較其他樣品均衡,導電度亦最佳(3〇ec : 2.議_3 S/cm 8GC ’ 1. lxiG-3 S/αη) ’以此進行下—步調整。 導電度測試 1·裁膜為直徑35 mm之圓至於恆溫恆濕箱中。 2.待系統穩定後以ac Impedance做導電度測試。 3·其所得阻抗值代入式即得離子導電度值。 測試條件如下: ❹ 頻率:1000000〜0.1Hz 振幅:10mV 測試溫度:30°C 測言式濕度:RH95% 4.選擇測試的頻率範圍在1〇〇〇〇〇〇妝〜丨晒Hz,設定交流電 的振幅在10 mV’若訊號受雜訊干擾過大,可將振幅調整至1〇〇mV, 直抓電壓設為〇 mV。將待測的膜材放至於電極中間於恆溫恆濕箱 ❹下進行實驗。分析實驗後所得的交流阻抗圖譜,取得膜材的阻抗 值,將其阻抗值(Rb)代入式便可求出膜材的離子導電度。Table 1 shows the representative composition of the initial production. The results obtained here are that the water content is changed according to the water-containing monomer and (4), and the water-repellent rate is expected to be reduced, but the degree of extraction is increased. The water content is formed by falling. In this initial formulation domain, sample 7 has the best properties, and its surface area, electrical conductivity, and strength 15 200924846 degrees are more balanced than other samples, and the conductivity is also the best (3〇ec: 2. Discussion _3 S/cm 8GC ' 1. lxiG-3 S/αη) 'With this step-by-step adjustment. Conductivity test 1·The film is a circle with a diameter of 35 mm as far as the constant temperature and humidity chamber. 2. After the system is stable, conduct conductivity test with ac Impedance. 3. The obtained impedance value is substituted into the formula to obtain the ion conductivity value. The test conditions are as follows: 频率 Frequency: 1000000~0.1Hz Amplitude: 10mV Test temperature: 30°C Measured humidity: RH95% 4. Select the frequency range of the test at 1 〇〇〇〇〇〇 makeup ~ 丨 Hz, set the AC The amplitude is 10 mV. If the signal is too much interference, the amplitude can be adjusted to 1〇〇mV and the direct voltage is set to 〇mV. The test piece was placed in the middle of the electrode under a constant temperature and humidity chamber. The AC impedance spectrum obtained after the analysis was analyzed to obtain the impedance value of the film, and the ionic conductivity of the film was obtained by substituting the impedance value (Rb) into the formula.

RbxA σ :導電度,S/cm L :膜厚,cmRbxA σ : conductivity, S/cm L : film thickness, cm

Rb:膜材阻抗值,Ω 200924846 A :電極與膜材接觸的面積,cm2 曱醇滲透測試 1·將待測膜夾至兩玻璃cell中間,膜材兩侧分別裝滿濃度3M 的曱醇水溶液(A槽)和蒸餾水(B槽)。 2. A槽及B槽溶液體積各為100 ml,cell保持在溫度3(TC。 3. 在室溫下每隔一小時抽取B槽的溶液2ml —至三次,用密 度計並將數值代入檢量線測量出曱醇濃度以求得曱醇的滲透量。 Ο 4·每小時取點,持續10小時取點做圖。 說明:檢量線由 1 wt%、2 wt%、3 wt%、4 wt%、5 wt%曱醇 水經密度計測得。 5.將所得的曱醇濃度代入下式求得曱醇滲透速率。 . ln(C4 — Cs(i)) = — ~——Rb: film resistance value, Ω 200924846 A : area of contact between the electrode and the film, cm2 sterol penetration test 1. The film to be tested is sandwiched between two glass cells, and both sides of the film are filled with a 3 M aqueous solution of sterol (A tank) and distilled water (B tank). 2. The volume of solution in tank A and tank B is 100 ml each, and the cell is kept at temperature 3 (TC. 3. 2 ml of solution of B tank is taken every hour at room temperature - three times, and the value is substituted by density meter. The concentration of sterol is measured by the measuring line to determine the amount of sterol permeation. Ο 4· Take points every hour for 10 hours to take a picture. Note: The calibration line is 1 wt%, 2 wt%, 3 wt%, 4 wt%, 5 wt% sterol water was measured by a densitometer. 5. The obtained sterol concentration was substituted into the following formula to determine the sterol permeation rate. ln(C4 - Cs(i)) = - ~

ApAp

Cb and Ca : the methanol concentrations(wt%) in the receiving cell and the source cell, respectively.Cb and Ca : the methanol concentrations(wt%) in the receiving cell and the source cell, respectively.

Vb : the volume of the receiving cell (cm3) A : cross-sectional area of the membrane (cm2) L : the thickness of the membrane (cm) P : the methanol permeability (cm2/s) 17 200924846 t〇 : termed the time lag t〇 = L2/6D (s) D : the methanol diffusion coefficient (cmVs) TGA測試 1.實驗前先以氮氣20 cc/roin通入l小時使爐體及管線中殘餘 氣體移除。 、 2. 各膜材樣品在乾燥環境下儲存。 3. 取l〇mg〜I5mg膜材樣品粉碎。 © 4為碎樣品置人白金盤中,開始祕升溫掃猫。 測試條件如下:Vb : the volume of the receiving cell (cm3) A : cross-sectional area of the membrane (cm2) L : the thickness of the membrane (cm) P : the methanol permeability (cm2/s) 17 200924846 t〇: termed the Time lag t〇= L2/6D (s) D : the methanol diffusion coefficient (cmVs) TGA test 1. Before the experiment, the residual gas in the furnace body and the pipeline was removed by introducing nitrogen gas at 20 cc/roin for 1 hour. 2. Each film sample is stored in a dry environment. 3. Take a sample of l〇mg~I5mg film and pulverize. © 4 For the broken sample, place it in a platinum plate and start to rub the cat. The test conditions are as follows:

氮氣流量:60ml/min 升溫速率:liTC/min 操作溫度範圍:30°C〜600°C 吸水實驗測試 ©重。 膜材於100匚供箱下3小時後秤重,即為膜材之乾 二,Γ入峨純水中24小時並軒重,即為膜材之濕重。 吸水率之百2求峡材吸水前後重量變化程度之百分比,此為 SR= { (Ws ^ / 1Nitrogen flow rate: 60ml/min Heating rate: liTC/min Operating temperature range: 30°C~600°C Water absorption test test ©Heavy. The membrane is weighed after 3 hours under the 100 匚 supply box, which is the dryness of the membrane. 2. It is rubbed into pure water for 24 hours and is heavy, which is the wet weight of the membrane. Percentage of water absorption rate is 2% of the degree of change in weight before and after water absorption, this is SR= { (Ws ^ / 1

Wd) / Ws } xlOO% 式中:Ws :财後_重量 ° 乾膜重量此實驗依據ASTM D 570之規範。 18 200924846 膜材含水率 商品化%fion-117杜邦公司以職D 57〇測試,其含 為38[實驗結果為37. 4%與杜邦相近。含水量依含水單體S與交聯 成份之多寡而改變’厭水性單體之加入如所預期降低含水率、,但 提升強度’此強度提高非只因含水下降而形成 ~r—r~~一一—_______ 2.5 0.06 〇.〇6 15 2.5 0.06 0.06L5 〇!〇3 o^og- 2·5 0.06 0.06 L5 〇1〇3 2.5 0.06 0.06~L5 〇!〇3~ 2.5 0.12 0.06 1.5 〇.〇3 ~~〇.〇6 F 5 2.5 0.12 0.06 1.5 0.06 0.12 0.12 G 5 2.5 0.06 0.06 1.5 0.03 H 5 2.5 0.06 0.06 1.5 0.06 I 5 2.5 0.06 0.06 1.5 0.06 J 5 2.5 0.06 0.06 3 表二 ❹ 〇 1. Modified Siloxane by reacting 100 parts of the hydroxypropyl-terminated dimethyl siloxane, (viscosity = 300 cS, Dow Corning Co), with the 20 parts of GMA for 3 hours at 80〇C in the presence of 0.1 part tertiary amine catalyst. 2. g-methacryloxypropyltrimethoxysilane » Dow Corning 200924846Wd) / Ws } xlOO% where: Ws: post-finance _ weight ° dry film weight This test is based on the ASTM D 570 specification. 18 200924846 Membrane moisture content Commercialized %fion-117 DuPont Company tested with a D 57〇, which contained 38 [experimental results of 37.4% similar to DuPont. The water content changes depending on the amount of the water-containing monomer S and the cross-linking component. The addition of the water-repellent monomer is as expected to lower the water content, but the strength is increased. This strength increase is not only caused by the decrease in water content, and is formed by ~r-r~~ One—_______ 2.5 0.06 〇.〇6 15 2.5 0.06 0.06L5 〇!〇3 o^og- 2·5 0.06 0.06 L5 〇1〇3 2.5 0.06 0.06~L5 〇!〇3~ 2.5 0.12 0.06 1.5 〇.〇 3 ~~〇.〇6 F 5 2.5 0.12 0.06 1.5 0.06 0.12 0.12 G 5 2.5 0.06 0.06 1.5 0.03 H 5 2.5 0.06 0.06 1.5 0.06 I 5 2.5 0.06 0.06 1.5 0.06 J 5 2.5 0.06 0.06 3 Table 2❹ 〇1. Modified Siloxane by reacting 100 parts of the hydroxypropyl-terminated dimethyl siloxane, (viscosity = 300 cS, Dow Corning Co), with the 20 parts of GMA for 3 hours at 80〇C in the presence of 0.1 part tertiary amine catalyst. -methacryloxypropyltrimethoxysilane » Dow Corning 200924846

Co. 3. Glycidyl Methacrylate (GMA),99% ’ Aldrich Chemical Co. 4. Hydroxyethyl Methacrylate (HEMA) ? Aldrich Chemical Co. 5. B0LT0RN P1000 (star) » dendritic polymer, average molecular weight of 1500 g/mole, hydroxyl number 430-490, mg KOH/g © equivalent, Perstorp Specialty Chemicals AB. 6. IRGACURE 819 (Bis(2, 4, 6-trimethylbenzoyl-phenylphosphineoxide) » Ciba Chem. 7. 2-Acry1amido-2-methy1-1-propanesu1fonic acid (Sulf-Acid) , 99% , Aldrich Chemical Co. 8. Aerosil 300 (A300),fumed silica,BET 表面積為 300 © ±30 m2/g,平均主粒徑為 7nm,Degussa Chemical Co. 9. Trimethylolpropane triacrylate (TMPTA). 在表二中,明列各成份組成,另有兩改質劑,A300為奈米級 親水性無機silica,其primary粒徑為7nm,Star代號為分枝狀 多0H基有機分子,此兩者之作用可見於下列結果。 20 200924846Co. 3. Glycidyl Methacrylate (GMA), 99% 'Aldrich Chemical Co. 4. Hydroxyethyl Methacrylate (HEMA) ? Aldrich Chemical Co. 5. B0LT0RN P1000 (star) » dendritic polymer, average molecular weight of 1500 g/mole, hydroxyl Number 430-490, mg KOH/g © equivalent, Perstorp Specialty Chemicals AB. 6. IRGACURE 819 (Bis(2, 4, 6-trimethylbenzoyl-phenylphosphineoxide) » Ciba Chem. 7. 2-Acry1amido-2-methy1-1- Propanesu1fonic acid (Sulf-Acid), 99%, Aldrich Chemical Co. 8. Aerosil 300 (A300), fumed silica, BET surface area 300 © ±30 m2/g, average primary particle size 7 nm, Degussa Chemical Co. Trimethylolpropane triacrylate (TMPTA). In Table 2, the composition of each component is clearly listed. There are two modifiers. A300 is a nano-sized hydrophilic inorganic silica with a primary particle size of 7 nm and a Star code of branched-type 0H. Organic molecules, the effects of which can be seen in the following results. 20 200924846

SamDle Water content (%) A 33、 B 40 C 40 D 43 E 38 F 40 G 44 — H 45 I 41 -- J 52 表三 表三為表二成份樣品之含水率(標準差小於值5%),樣品A美 ❹本之含水為33%,在加入0. 6phr (以si loxane作基準)微量A3〇〇 後其含水增至44% (見樣品20),此顯著增加來自奈米級胡〇〇之 含0H親水之高表面積表面(300±30,DIN66131)。 以0. 06改質Star成分加入後(樣品η)含水亦有效提升至 45%,此亦歸因於成分中之高〇H含量,但不同改質之厂组成可 影響含水。如樣品I所示,在同樣〇· 6phr添加量下含水較樣品G 為小,因GMA為低吸水油性單體。除外加改質劑外,具 ❹acid官能基單體含量增倍亦可提升含水率至52% (樣品J)。A300 及star成分同時加入後並無法再增加含水量(見樣品B、^、D), 而再增加交聯劑量,因交聯密度增加故含水降低(見樣品D及E), A300及star成分增加亦對高交聯樣品含水提升有效。 21 200924846 導電度SamDle Water content (%) A 33, B 40 C 40 D 43 E 38 F 40 G 44 — H 45 I 41 -- J 52 Table 3 Table 3 is the moisture content of the sample of the second component (standard deviation less than 5%) The sample A has a water content of 33%, and after adding 0.6 phr (based on si loxane), the water content increases to 44% (see sample 20), which is significantly increased from the nano-sized coriander. A high surface area with a hydrophilic surface of 0H (300±30, DIN66131). After the addition of the 0.6 component of the modified Star component (sample η), the water content was also effectively increased to 45%, which was also attributed to the high 〇H content in the composition, but the composition of the different modified plants could affect the water content. As shown in Sample I, the water content was smaller than that of Sample G at the same amount of 〇·6 phr, since GMA was a low water absorbing oil monomer. In addition to the modifier, doubling the content of the 官能acid functional monomer can also increase the moisture content to 52% (Sample J). After adding A300 and star components at the same time, it is no longer possible to increase the water content (see samples B, ^, D), and then increase the amount of crosslinker. As the crosslink density increases, the water content decreases (see samples D and E), A300 and star components. The increase is also effective for increasing the water content of highly crosslinked samples. 21 200924846 Conductivity

Sample Conductivity (S/cm、 A 2.6xlO'J B 1.8xl0'3 C 9.2xl(T D 7.3xl(T a 4·5χ1(Γ F 6.3xl(T 1.9x10° H 2.5xl〇-J I l.lxlO·3 J 1.5xl〇-3 表四 ❹各樣品之導電度如表四,原樣品A之導電度在2. 6xi〇-3s/cm, 增加Sulfonic單體倍數(樣品J)不但無法增加導電度,反而降 低。此結果可能肇因於Sulfonic單體之添加已超過飽和溶解度, 影響光反應進行亦影響接枝量,另水含量過高亦可能對導電度產 生影響。加入A300後導電度小幅下降至丨.9xl〇-3s/cni,無機粒子 加入增加傳導路徑,雖提升含水率但無法有效增加導電度。但有 機star成分之加人對導電度之鱗並不似纖,如樣品h其導電 ©,在2· S/cm’約同樣品A之值,在此之伽成分其〇H基 /辰度及3水親水性不似樣品丨以GMA改質者下降,故導電率亦以 樣品I下降較多。 〇預』若入綱及对虹成分同時加入亦降低導電度,如樣 ^ mur s/em ’ Λ值較樣品㈠低。而樣品c為&㈣4 S/cm ’較樣品G及!均大幅下降,顯示删與改質咖成分共 用時其變_—般算數平均,而有交互之加雜果,考量Η及」 22 200924846 含水量類以下,此可能因A300與GMA改質star表面成分互相作 用較顯著,而影響質子傳導。 當A300及兩種star成分全使用時,樣品之導電度再度下降, 此可見於樣品D、E及F之結果。最低之導電度見於樣品D(7. 3xl0_5 S/cm),但當交聯劑增加後導電度又再上升(見樣品E、F)。比較此 三樣品與前述樣品之導電度,在此又可見交聯劑與A300、star成 分之交互作用結果。 0 TGA分析 所製成si loxane膜材之熱安定性可由TGA分析了解,各配方 之受熱反應以TGA職可⑽較㈣成份㈣在高溫之裂解行 為,由起始裂解溫度(Τ〇之高低顯示材料承受熱裂解之溫度,而 熱裂解之速率可由以裂解最大速率之溫度)與Ti之差異值得知, 在同-升溫速率下’ vta越小代表裂解速率越快速。另外tga 微詡譜之波峰數亦代表了可能有多少種裂解反應進行,每一系 統相失之重1比及最狀雜量亦絲材料林同之裂解程 23 200924846Sample Conductivity (S/cm, A 2.6xlO'J B 1.8xl0'3 C 9.2xl (TD 7.3xl (T a 4.6xl (T 1.9x10° H 2.5xl〇-JI l.lxlO· 3 J 1.5xl〇-3 Table 4 The conductivity of each sample is shown in Table 4. The conductivity of the original sample A is 2. 6xi〇-3s/cm. Increasing the Sulfonic monomer multiple (sample J) can not increase the conductivity. On the contrary, this result may be due to the fact that the addition of Sulfonic monomer has exceeded the saturation solubility, affecting the photoreaction and affecting the grafting amount. The excessive water content may also affect the conductivity. After the addition of A300, the conductivity decreases slightly to丨.9xl〇-3s/cni, the addition of inorganic particles increases the conduction path, although it increases the water content but does not effectively increase the conductivity. However, the addition of the organic star component to the conductivity scale is not like fiber, such as the sample h its conductivity© In 2·S/cm′, the value of sample A is about the same. In this case, the 〇H group/initiality and the hydrophilicity of 3 water are not like the sample, and the GMA is reduced, so the conductivity is also sample I. Decrease more. If you enter the program and add the rainbow component at the same time, it will also reduce the conductivity, such as ^ mur s / em ' Λ value compared to the sample (a) The sample c is & (4) 4 S/cm' is significantly lower than the sample G and !, which shows that when the deletion and the modified coffee component are shared, the change is _-the average of the arithmetic, and there are interactions and additions, and the consideration is 22 200924846 Below the water content, this may be due to the interaction between A300 and GMA modified star surface components, which affects proton conduction. When A300 and two star components are used, the conductivity of the sample decreases again. The results of samples D, E and F. The lowest conductivity is found in sample D (7.3×10_5 S/cm), but the conductivity increases again when the crosslinker increases (see samples E, F). Compare the three samples with The conductivity of the above sample can be seen here. The interaction between the crosslinker and the A300 and star components can be seen. 0 The thermal stability of the si loxane film made by TGA analysis can be understood by TGA analysis, and the heat reaction of each formula is TGA. (10) The cracking behavior of (4) component (4) at high temperature is known from the initial cracking temperature (the temperature at which the material shows the temperature at which the material is subjected to thermal cracking, and the rate of thermal cracking can be determined by the temperature at the maximum rate of cracking) and Ti. At the same-heating rate The smaller the vta is, the faster the cracking rate is. The number of peaks of the tga micro-spectrum also represents how many kinds of cracking reactions may be carried out. The weight loss of each system is 1 and the most heterogeneous amount is also the same. Cheng 23 200924846

Sample TiCC) Tpl(°C) TP2(°C) TP3fC) 殘餘量(%) A 168.5 232.1 309.8 411.3 5.2 B 169.4 227.7 304.5 406.9 6.3 C 176.5 226.8 310.7 406.0 5.8 D 172.9 230.3 308.0—" 404.3 7,0 E 175.6 232.1 307.1 409.6 5.6 F 169.4 236.5 308.0 406.0 7.8 G 169.4 245.3 310.7 407.8 8.1 H 172.0 240.9 304.5 407.8 7.4 I 175.6 239.1 310.7 412.2 8,2 J 17L2 200.3 302.7 408.7 92 表五 表五為各代表性樣品TGA之熱裂解溫度及最終殘餘量熱重分 析測試結果,由樣品A之TGA圖譜可知製成膜分主要三個階段裂 解,100°C前為水分揮發,自170¾起始為Sulfonic官能基開始損 失’接續膜中HEM壓克力單體’ Sulfonic單體c-c鍵裂解開啟第 一階段重量損失。由TGA分析此部份重量損失近4〇%,近於HEMA 與Sulfonic單體含量。第二階段於25〇。(:附近起始,最高速率發 生於Tp2之309. 8°C ’此部份重量損失約為1〇%,只要肇因於梦氧 院鍵上之C C接枝組成’隶後自約320 C開始si loxane組成之裂 解損失’此部份重量約損失40%,依樣品之不同第三階段損失差距 在5%以内。 因TGA圖譜在此所示均相似,在此僅列代表性之三種樣品數 據’由樣品J之數據可知過量未反應之Sulfonic單體可造成反應 交聯度低之壓克力類結構,其第一階段裂解加速進行,此與前述 結果一致,殘餘量增加約80%(5. 2%增加至9. 2%)此應歸因於 24 200924846 *Sample TiCC) Tpl(°C) TP2(°C) TP3fC) Residual amount (%) A 168.5 232.1 309.8 411.3 5.2 B 169.4 227.7 304.5 406.9 6.3 C 176.5 226.8 310.7 406.0 5.8 D 172.9 230.3 308.0—" 404.3 7,0 E 175.6 232.1 307.1 409.6 5.6 F 169.4 236.5 308.0 406.0 7.8 G 169.4 245.3 310.7 407.8 8.1 H 172.0 240.9 304.5 407.8 7.4 I 175.6 239.1 310.7 412.2 8,2 J 17L2 200.3 302.7 408.7 92 Table 5 Table 5 shows the thermal cracking of representative samples TGA Temperature and final residual amount of thermogravimetric analysis test results, from the TGA spectrum of sample A, it can be seen that the film is divided into three main stages of cracking, water volatilization before 100 °C, starting from 1702⁄4 for the Sulfonic functional group to start the loss in the continuation film The HEM acrylic monomer' Sulfonic monomer cc bond cracking opens the first stage weight loss. The weight loss of this part by TGA analysis was nearly 4%, which was close to the HEMA and Sulfonic monomer content. The second stage is at 25 baht. (: Near the beginning, the highest rate occurs at 309 of Tp2. 8 °C 'The weight loss of this part is about 1〇%, as long as it is due to the CC grafting composition on the Mengyangyuan key'. The cleavage loss of the si loxane composition begins. The weight loss of this part is about 40%. The difference in the third stage loss is less than 5% depending on the sample. Since the TGA map is similar here, only the representative three samples are listed here. The data 'from the data of sample J shows that an excess of unreacted Sulfonic monomer can cause an acrylic-like structure with a low degree of reaction cross-linking, and the first-stage cracking is accelerated, which is consistent with the foregoing result, and the residual amount is increased by about 80% ( 5. 2% increase to 9.2%) This should be attributed to 24 200924846 *

Sulfonic acid g旎基之作用在高溫下形成咖厂组成。加入微量 A300對第-1¾段裂解有顯著影響,Tpl自232. π提升至245· 3。〇 且最、、殘餘量亦增加’此表示細〇之表面可改變膜成分之裂解機 構。 加入改質star成分亦對裂解有類似效果,如樣品H提升初始 裂解溫度,對Tpl亦提高,但造成Tp2、Tp3下降約4说,而樣 品I對Ti提高7°C。Tpl效果同樣品Η,但卻不影響扣2、如3, ©此亦也實不同之改質star成分造成不同效果,於此殘餘量亦如 誦者增加。編與star成分共料,縣解並無加成效果。 如樣扣B及C所見,與上述單一成分加入樣品相較,^趨勢相似, 使用恤-GMA有較高之Ti,但Τρ1均低超過肌,τρΐ及τρ2 之影響較小’但變化方向與使用star_成分較相似,此代表對壓克 力成分之影響較顯著。由TGA _譜亦可見加入麵或恤—成分 必者,第一階段裂解有-肩狀峰存在,共用時殘餘卻較單獨使用為 ❹少。此亦明確證實裂解機構改變之改f綱、咖成分全用時, 對Ti之影響遠較對Tp之變化顯著。增加交聯劑含量可提升第一 階,起始溫度,但對Τρ之影響較小(Sample7),添加倍數之改質 微量成分在高交聯劑濃度下對裂解安定性無促進效果。 25 200924846 膜材機械性質The role of Sulfonic acid g-based is to form a coffee factory at high temperatures. The addition of trace A300 had a significant effect on the cleavage of the -13⁄4 segment, with Tpl increasing from 232. π to 245·3. 〇 and the most, the residual amount is also increased' This indicates that the surface of the fine crucible can change the cracking mechanism of the film component. The addition of the modified star component also has a similar effect on cleavage. For example, sample H increases the initial cleavage temperature and increases Tpl, but causes Tp2 and Tp3 to decrease by about 4, while sample I increases Ti by 7 °C. The effect of Tpl is the same as that of the sample, but it does not affect the deduction 2, such as 3, and this also affects the different effects of the modified star component, and the residual amount is also increased as the latter. Codified with the star ingredients, the county solution has no additive effect. As seen in the samples B and C, compared with the above-mentioned single component addition, the trend is similar. The shirt-GMA has a higher Ti, but the Τρ1 is lower than the muscle, and the influence of τρΐ and τρ2 is smaller. The use of the star_ component is more similar, which represents a significant effect on the acrylic component. It can also be seen from the TGA _ spectrum that it is added to the face or the shirt - the ingredients must be, the first stage of the cracking has - the shoulder peak exists, and the residual when sharing is less than the use alone. This also clearly confirms that when the cracking mechanism changes and the coffee component is used in its entirety, the effect on Ti is much more significant than that on Tp. Increasing the cross-linking agent content can increase the first-order, initial temperature, but the effect on Τρ is small (Sample7), and the addition of multiple modifiers does not promote the cracking stability at high cross-linking agent concentration. 25 200924846 Mechanical properties of membranes

Sample Tensile Stress (kg/cm2) Tensile strmn (%) A 3.58 18 B 2.87 11 C 8.02 22 D 8.48 21 E 9.95 22 F 10.86 31 G 6.59 14 H 7.76 20 I 12.89 23 J 1.075 10 表六 Ο 各配方膜材之機械性質列於表六,在此之各sil〇xane膜均極 柔軟’延伸性亦佳,但n〇tCh-Sensitive,過量Sulf〇nic成分(樣 品J)因反應及溶解性不佳’其應力及延展性均遠較同樣品A為 低。添加A300可有效增加強度’但因無機粒子存在其延展性下降。 但以star成分加入後均可有效提升原樣品A膜材之強度及柔軟 性’此結果對加人量極少而言可見甚為顯著。stgx_GMA改質者可 得最高之強度(〜4倍)。 A300及star成分共用時,可見交互作用,纣虹―水解改質者 與A300共用反大幅降低強度’應變亦大幅下降,但star_GM_ A300合用·度及柔軟性她別侧為佳,但比_ star_GMA 為差,且雜A300及star水解樣品優良。三者同用時樣品D之 結果與樣品C類似,即A3GG與star—水解所造成之負面效果已被 消砰。加入雙倍交聯劑可再提高拉伸強度(樣品E),但不影賴變 26 200924846 (與樣品E相較)。在此較高交聯密度下,三改質成份量添加倍數, 可稱提高強度自9. 95 Kg/cm2至10. 86 Kg/cm2 (樣品F),但應變卻 大幅增加至31%’此結果顯示改質微量成分與交聯劑之用量可調整 匹配以得最佳強度及柔軟性。 曱醇透過率 所製成各配方之膜材之曱醇透過率列於表七、八。由表中可 知各膜材之甲醇透過相對速率及透過率大小,Naf i〇nl丨7在相同條 © 件下之曱醇透過率為5. 04x10—5 (單位:wt% / hr X皿〇以此為基 準。可知所有配方膜材之透過率均小於Nafi〇n Μ以倍數計,此 多數石夕氧烷膜雖含水量較Nafion 117均高,但曱醇透過率並未隨 含水增加,證實配方成分之曱醇透過選擇性較Nafi〇n 117顯著。 以樣品A而言,基本透過率值為L 95χ1〇_5,加入A3〇〇後再 略降為1.57x10 5 ’此為A300 Sil ica無機粒子增加甲醇擴散路徑 造成,加入star-水解後透過率略升為2.13χ1〇-5 (樣品H),但加 © Mtar-GMA後反較原樣品Α低為14_-5(樣品〇,此亦符合前Sample Tensile Stress (kg/cm2) Tensile strmn (%) A 3.58 18 B 2.87 11 C 8.02 22 D 8.48 21 E 9.95 22 F 10.86 31 G 6.59 14 H 7.76 20 I 12.89 23 J 1.075 10 Table VIΟ Each formulated film The mechanical properties are listed in Table 6. Here, each sil〇xane film is extremely soft, and the elongation is also good, but n〇tCh-Sensitive, excess Sulf〇nic component (sample J) is poor in reaction and solubility. Both stress and ductility are much lower than those of sample A. The addition of A300 is effective in increasing the strength' but the ductility is degraded due to the presence of inorganic particles. However, the strength and softness of the original sample A film can be effectively improved by adding the star component. This result is very noticeable in terms of the amount of addition. The stgx_GMA modifier can get the highest intensity (~4 times). When the A300 and the star components are shared, the interaction can be seen. The 纣Hong-hydrolytic modifier is shared with the A300, and the strain is greatly reduced. The strain is also greatly reduced, but the star_GM_A300 is more suitable for the degree and softness than the other side, but the ratio _ star_GMA It is poor, and the miscellaneous A300 and star hydrolysis samples are excellent. The results of sample D when the three were used together were similar to those of sample C, that is, the negative effects caused by A3GG and star-hydrolysis have been eliminated. The addition of a double crosslinker increases the tensile strength (sample E), but does not affect the change 26 200924846 (compared to sample E). At this higher crosslink density, the addition amount of the three modified components can be said to increase the strength from 9.95 Kg/cm2 to 10.86 Kg/cm2 (sample F), but the strain is greatly increased to 31%' The results show that the amount of modified trace components and crosslinker can be adjusted to achieve the best strength and softness. The sterol permeability of the membranes of each formulation prepared by the sterol permeability is shown in Tables VII and VIII. From the table, the relative rate of methanol permeation and the transmittance of each film are shown. The sterol permeability of Naf i〇nl丨7 under the same article is 5. 04x10-5 (unit: wt% / hr X dish) Based on this, it can be seen that the transmittance of all the formulated membranes is less than that of Nafi〇n ,. Although most of the oxalate membranes have higher water content than Nafion 117, the sterol permeability does not increase with water content. It was confirmed that the sterol permeation selectivity of the formulation component was significantly higher than that of Nafi〇n 117. For sample A, the basic transmittance value was L 95χ1〇_5, and after adding A3〇〇, it was slightly decreased to 1.57x10 5 'This is A300 Sil The ica inorganic particles increased the methanol diffusion path. After adding star-hydrolysis, the transmittance increased slightly to 2.13χ1〇-5 (sample H), but after adding Mtar-GMA, the lower the original sample was 14_-5 (sample 〇, This also corresponds to the former

述,不同處理之star-單體對膜材造成性質不…在此因star_GM 之含水較star-水解低,故刊此造成透過率較低。#加入樣品A 中倍數Sulfonic單體,因含水增加膜材結構反應改變,甲醇透過 率反較樣品A高。 當A300與star成分共用時:甲醇透過率均上升(見樣以及 C) ’此時使用Star-GMA反較star_水解透過率高,此與樣品η及 27 200924846 I之大小相反’顯不A300與star成分對膜曱醇透過率性質有交互 作用’此應與A300和star成分表面互相作用性質有關。但删, star-水解與star-GMA共用時(樣品D)曱醇透過率最低,為 1. 44x10 5(與樣品I同)。增加交聯劑,及三改質成分倍數量(樣品 E與F),無助於甲醇透過率減少。在此結果顯示甲醇透過率主要 X成份作用下之膜材化學結構及交聯度影響,非單一因素即可改 變0 藉由以上較佳具體實施例之詳述,係希望能更加清楚描述本 發明之特徵與精神,而並非以上述所揭露的較佳具體實施例來對 本發明之範_加以限制。相反地,其目的是希望能涵蓋各種改變 及具相等性的安排於本發明所欲申讀之專利範圍的範疇内。 【圖式簡單說明】 無 【主要元件符號說明】 無 28It is stated that the star-monomers of different treatments do not cause properties to the membrane. Here, since the water content of star_GM is lower than that of star-hydrolysis, the transmittance is low. #Adding the Sulfonic monomer in the sample A, the membrane structure reaction is changed due to the increase in water content, and the methanol permeability is higher than that of the sample A. When A300 is shared with the star component: the methanol permeability increases (see sample and C). 'Star-GMA is used at this time, and the star_hydrolyzed transmittance is higher. This is opposite to the sample η and 27 200924846 I. Interaction with the star component on membrane sterol permeability properties' This should be related to the surface interaction properties of the A300 and star components. However, when star-hydrolysis is shared with star-GMA (sample D), the sterol permeability is the lowest, 1.44x10 5 (same as sample I). Increasing the cross-linking agent and the amount of the three modified components (samples E and F) did not contribute to a decrease in methanol permeability. The results show that the chemical structure of the membrane and the degree of cross-linking under the action of the main X component of the methanol permeability can be changed by a single factor. By the detailed description of the above preferred embodiments, it is desirable to more clearly describe the present invention. The features and spirit of the invention are not limited by the preferred embodiments disclosed above. On the contrary, the intention is to cover various modifications and equivalents within the scope of the invention as claimed. [Simple description of the diagram] None [Key component symbol description] None 28

Claims (1)

200924846 十、申請專利範圍: 1. 一種矽氧烷膜材,主要固成份包括改質含 雙鍵之矽氧烷寡聚物、質子導電單體、交聯劑、及 改質吸水性化合物,其特徵在於,改質含雙鍵之矽 氧烧募聚物為經丙基封端二曱基石夕氧烧 (hydroxypropyl-terminated dimethyl siloxane) 與曱基丙稀酸環氧丙脂(glycidyl methacrylate) 之反應產物,且甲基丙稀酸環氧丙脂(glyc idyl methacrylate)重量百分比為經丙基封端二甲基石夕 氧 烧(hydroxypropyl-terminated dimethyl siloxane)重量30%以下,羥丙基封端二曱基矽氧烧 (hydroxypropyl-terminated dimethyl siloxane) 分子量範圍為500 g/mol至50000 g/mol。 ❹ 2. 如申請專利範圍第1項所述之矽氧烷膜 材,其中質子導電單體為2-丙烯醯胺-2-曱基-1-丙 烷 磺 酸 (2-Acrylamido-2-methy1-1-propanesulfonic acid)。 3. 如申請專利範圍第1項所述之矽氧烷膜 材,其中交聯劑為三羥曱基丙烷三丙烯酸酯 29 200924846 (Triraethylolpropane triacrylate) ° 4. 如申請專利範圍第1項所述之矽氧烷膜 材,其中改質吸水性化合物為曱基丙烯酸羥乙酯 (Hydroxyethy1 methacrylate,HEMA) ° 5. 如申請專利範圍第1項所述之矽氧烷膜 材,其中改質吸水性化合物為亦可為dendritic polymer ° 6. 如申請專利範圍第5項所述之矽氧烷膜 材,其中dendritic polymer數量平均分子量為 1500 g/mole, hydroxyl number 430-490 (mg KOH/g equivalent) ° ^ 7. 如申請專利範圍第1項所述之矽氧烷膜 材,其中改質吸水性化合物為石夕灰(S i 1 i ca Fume)。 8. 如申請專利範圍第7項所述之矽氧烷膜 材,其中石夕灰(SilicaFume)的BET表面積為300±30 m2/g,且平均主粒徑為7nm。 30 200924846 七、指定代表圖: (一) 本案指定代表圖為:第( )圖。 (二) 本代表圖之元件符號簡單說明: 無200924846 X. Patent application scope: 1. A siloxane oxide film, the main solid components include modified siloxane oligomers containing double bonds, proton conductive monomers, cross-linking agents, and modified water-absorbing compounds. The invention is characterized in that the modified double-bonded oxime-burning polymer is a reaction of propyl-terminated dimethyl siloxane and glycidyl methacrylate. The product, and the weight percentage of glycyl idyl methacrylate is 30% by weight of hydroxypropyl-terminated dimethyl siloxane, hydroxypropyl terminated The hydroxypropyl-terminated dimethyl siloxane has a molecular weight ranging from 500 g/mol to 50,000 g/mol. ❹ 2. The alkane membrane according to claim 1, wherein the proton conductive monomer is 2-propenylamine-2-mercapto-1-propanesulfonic acid (2-Acrylamido-2-methy1- 1-propanesulfonic acid). 3. The alkane membrane according to claim 1, wherein the crosslinking agent is trihydroxymethyl propane triacrylate 29 200924846 (Triraethylolpropane triacrylate) ° 4. As described in claim 1 a siloxane film, wherein the modified water absorbing compound is hydroxyethyl methacrylate (HEMA). 5. The oxirane film according to claim 1, wherein the water absorbing compound is modified. It can also be dendritic polymer ° 6. The alkane film according to claim 5, wherein the dendritic polymer has a number average molecular weight of 1500 g/mole and a hydroxyl number of 430-490 (mg KOH/g equivalent) ° ^ 7. The alkane film according to claim 1, wherein the modified water-absorbing compound is Si yi i mai. 8. The alkane film according to claim 7, wherein the Silica Fume has a BET surface area of 300 ± 30 m 2 /g and an average primary particle diameter of 7 nm. 30 200924846 VII. Designation of representative representatives: (1) The representative representative of the case is: ( ). (2) A brief description of the component symbols of this representative figure: None 八、本案若有化學式時,請揭示最能顯示發明特徵的 化學式: ❹8. If there is a chemical formula in this case, please reveal the chemical formula that best shows the characteristics of the invention: ❹
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Publication number Priority date Publication date Assignee Title
TWI464939B (en) * 2011-12-20 2014-12-11 Ind Tech Res Inst Separators utilized in lithium batteries
US9257725B2 (en) 2011-12-20 2016-02-09 Industrial Technology Research Institute Separator for lithium cells having porous and cured layers on a non-woven support

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