TW201251187A - Composite materials, production thereof and use thereof in electrical cells - Google Patents

Composite materials, production thereof and use thereof in electrical cells Download PDF

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Publication number
TW201251187A
TW201251187A TW101118846A TW101118846A TW201251187A TW 201251187 A TW201251187 A TW 201251187A TW 101118846 A TW101118846 A TW 101118846A TW 101118846 A TW101118846 A TW 101118846A TW 201251187 A TW201251187 A TW 201251187A
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Taiwan
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carbon
composite
sulfur
weight
polymer
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TW101118846A
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Chinese (zh)
Inventor
Nicole Janssen
Alexander Panchenko
Oliver Gronwald
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Basf Se
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Publication of TW201251187A publication Critical patent/TW201251187A/en

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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
    • Y02E60/10Energy storage using batteries

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Abstract

The present invention relates to composite materials comprising a reaction product of (A) at least one organic polymer, (B) sulfur, (C) carbon in a polymorph which comprises at least 60% sp2-hybridized carbon atoms, and (D) 2-20% by weight of a perfluorinated or partly fluorinated polymer, based on the total weight of components (A), (B) and (C) used before reaction, and also to a process for producing inventive composite materials and to the use of inventive composite materials.

Description

201251187 六、發明說明: 【發明所屬之技術領域】 本發明係關於包括以下組份之反應產物之複合材料: (A) 至少一種有機聚合物, (B) 硫, .· (C) 包括至少60% sp2-混成化碳原子之呈多形體之碳,及 (D) 基於反應前所使用組份及(c)之總重量計, 2至20重量%之全氟化或部分氟化聚合物。 本發明進一步係關於製備本發明複合材料之方法及本發 明複合材料之用途。 【先前技術】 蓄電池或可充電電池僅係一些可在生成後儲存電能並在 需要時使用之實施例。由於明顯更好的功率密度,故近來 已由水基蓄電池轉而發展電池中之電荷輸送係藉由鋰離子 完成之電池組。 然而,具有碳陽極及基於金屬氧化物之陰極之習知鋰離 子電池組之旎量密度受到限制。已由鋰硫電池開闢關於能 量密度之新視角。在鐘硫電池中,硫陰極中之硫經由多硫 ' ㈣還原^2·’其在電池充電時再氧化形成硫-碰鍵。 • 然而 問題係多硫化物(例如Li2S4及Li2S6)之溶解度, ,、可冷於♦劑中並可遷移至陽極^結果可包括:損失電容 及電絕緣材料沉積於電極之硫顆粒上。自陰極遷移至陽極 最終可導致受影響電池放電及電池組中之電池失效。此種 多硫離子之不期望的遷移亦稱為「穿梭(shutuing)」,,,其 164545.doc 201251187 為亦使用於本發明範圍内之術語。 有諸多抑制此穿梭之嘗試。例如,j Wang等人提出向 陰極添加硫及聚丙烯腈之反應產物;Adv Funct. Mater. 2003,13, 487 ff。由此形成產物,其係藉由自聚丙烯腈除 去氫所產生’同時形成硫化氫。 另外提出使用硫化物替代硫,例如CuS、FeS2* 2,5_二 酼基-1,3,4-噻二唑。然而,此類電池之電容並不令人滿 心參見例如 P. Wang, */.五s〇c. 2002, 么 149以及 J· Wang等人,乂 2〇〇4, 138, 2Ί\ 。 另外提出使用呈微細分散形式之硫;參見j Wang等人, J· Pwa仏2004, 27卜然而,在高電流密度 下’觀察到效率波動,作者將其料於㈣晶之沉積。此 等可係麻煩的’因其會導致内部短路。 另外提出將硫與聚丙稀腈之反應產物與碳黑混合,並將 其壓至電極;J. Wang等人,施⑽2〇〇2, ^⑹ff。 當此等電極與聚合物組合作為電解㈣,觀察到穿梭機制 降低。然而,許多聚合物電解質具有低導電性。 【發明内容】 因此’本發明之目的係提供-種易於製備且可避免先前 技術之已知弊端之陰極材料。本發明之另—目㈣提供— 種可製備相應陰極材料之方法。 因此’已發現在開頭定義之材料。 【實施方式】 164545.doc 201251187 日本:明材料為複合材料,在本發明範圍内亦稱其為本發 月複σ材料。複合材料應理解為意指固體混合物材料,其 不可人工为離且具有不同於個別組份之特性。本發明材料 尤其係顆粒複合材料。 本發明複合材料包括以下組份之反應產物: (Α)至少一種有機聚合物,簡稱為聚合物(Α)或有機聚合 物(Α) ’在本發明範圍内,片語聚合物包括均聚物及 共聚物, (Β)硫》 (C) 包括至少60。/。sp2_混成化碳原子之呈多形體之碳及 (D) 基於反應前所使用組份(A)、(B)及(C)之總重量,2 至20重量%之全氟化或部分氟化聚合物。 聚合物(A)可選自任何有機聚合物及共聚物,較佳選自 可藉由陰離子或自由基(共)聚合得到之聚合物。有機聚合 物或共聚物較佳由元素碳及氫(及視情況氮、4、氧、硫 及/或氣)之原子組成,尤其係元素碳及氫(及視情況氮、氧 及/或氣’尤其係氮)之原子。 術浯「(共)聚合」代表均聚合或共聚合。術語「(共)聚 合物」代表均聚物或共聚物。 在另一變體中,聚合物(A)可選自有機聚酯,尤其係脂 族聚酯。 在本發明之一項實施例中,聚合物係選自可藉由陰 離子、催化或自由基(共)聚合得到之(共)聚合物,尤其係 聚乙烯、聚丙烯、聚丙烯腈、聚丁二烯、聚苯乙烯及至少 164545.doc 201251187 兩種選自乙稀、丙稀、苯乙稀、(甲基)丙稀猜(尤其係丙婦 腈)及1,3-丁二烯之共聚單體之共聚物。此外,聚異戊二烯 及聚丙烯酸酯亦合適。尤其青睐聚丙烯腈,在本發明範圍 内亦稱為聚丙稀腈(A)。 在本發明範圍内,聚丙烯腈不應僅理解為意指聚丙烯腈 均聚物,並且意指丙烯腈與丨,3_ 丁二烯或苯乙烯之共聚 物。較佳為聚丙烯腈均聚物。 在本發明之一項實施例中,在反應後存在聚丙烯腈 (A)’即在本發明複合材料中,至少部分呈式⑴環化產: 之形式。 (I) 、、、N人人人人, 在本發明範圍内,聚乙烯應理解為不僅意指均聚乙烯, 而且意指乙稀共聚物’其包括至少50 mol%呈共聚形式之 乙烯及多達50 mol%之至少另一種共聚單體,例如α烯烴 (諸如丙烯、丁烯(1-丁烯)、1_己烯、辛烯、丨·癸烯、^ 十二烯、1 -戊烯及異丁烯)、乙烯基芳族化合物(例如苯乙 稀)及(曱基)丙稀酸、乙酸乙稀醋、丙酸乙稀醋 '(甲基)丙 烯酸之0:1至(:1〇烷基酯(尤其係丙烯酸曱酯、曱基丙稀酸甲 酯、丙烯酸乙酯、曱基丙烯酸乙酯、丙烯酸正丁醋、丙稀 酸-2·乙基己酯、曱基丙烯酸正丁基酯、曱基丙歸酸2_乙基 己醋)及馬來酸、馬來酸酐及衣康酸針。聚乙稀可為Hdpe 或LDPE。 164545.doc 201251187 在本發明範圍内’聚丙稀不僅應理解為意指均聚丙稀, 而且應理解為丙烯共聚物,其包括至少50 mol%呈共聚形 式之丙烯及多達5〇磁之至少另一種共聚單體例如乙 烯及&烯烴,諸如丁烯、卜己烯、卜辛烯、1-癸烯、1_十 * ^烯及1_戊烯。聚丙烯較佳為等規或基本上等規聚丙烯。 - 在本發明範圍内,聚苯乙烯不僅應理解為意指苯乙稀之 均聚物’而且應理解為苯乙烯與丙烯腈、丁二烯、(甲 基)丙烯酸、(甲基)丙烯酸之CiiCi〇烷基酯、二乙烯基 苯、1,2-二笨乙稀或α_甲基苯乙婦(尤其係與丙稀猜或Μ — 丁二烯)之共聚物。 另一較佳聚合物(Α)為聚丁二烯。 义在本發明之-實施例中,$合物⑷係選自彼等在反應 刖具有 50 〇〇〇 至5〇〇 〇〇〇 g/m〇1(較佳至 25〇 〇〇〇 g/m〇i)之平 均分子量]^1~者^ 在本發明之一實施例中,聚丙烯腈(A)係選自彼等在反 應前具有在10 000至500 000 g/m〇1範圍内(尤其係5〇 〇〇〇至 250 000 g/mol)之平均分子量Mw之聚丙烯腈。 聚合物(A)可為交聯或非交聯(共)聚合物。 • 硫(B)係本身已知,且在本發明範圍内亦可簡稱為硫。 ' 包括至少60% sp2_混成化碳原子(較佳至少75% sp2-混成 化碳原子)之呈多形體之碳,在本發明範圍内亦簡稱為碳 (C),係本身已知◎碳(C)為碳之導電性多形體。例如,碳 (C)可為石墨。 以%計之數值係基於在化學反應條件下併入本發明複合 164545.doc 201251187 材料中之所有碳(c)計,包括任何雜質,且表示重量百分 比。 在本發明之一實施例中,碳為碳黑。碳黑可(例如)係 選自燈黑、爐法碳黑、火焰碳黑、熱裂解碳黑、乙炔黑及 工業碳黑。碳黑可包括雜質,例如碳氫化合物(尤其係芳 族烴)' 或含氧化合物或含氧基團(例如〇H基團)❶此外, 碳黑中還可有含硫或含鐵雜質。 用於製備本發明複合材料之反應產物之碳(c)較佳係選 自碳黑。 在一變體中’碳(C)係經部分氧化之碳黑。 在本發明之一實施例中,碳(C)包含奈米碳管。奈米碳 營(縮稱CNT)(例如單壁奈米碳管(sw CNT)及較佳為多壁 奈米碳管(MW CNT))係本身已知的。其製備方法及一些特 陡由(例如)A. Jess 等人描述於 c/zemz.e /«geWew 2006,7<§,94-100 中。 在本發明之一實施例中,奈米碳管具有〇 4至5〇 nm範圍 内(較佳1至25 nm)之直徑》 在本發明之一實施例中,奈米碳管具有10 nm至丨mm範 圍内(較佳100 nm至500 nm)之長度。 可藉由本身已知之方法製備奈米碳管。例如,可使揮發 性碳化合物(例如曱烷或一氧化碳、乙炔或乙烯)或揮發性 碳化合.物之混合物(例如合成氣體)在一或多種還原劑(例如 氫乳及/或另一氣體,例如氮氣)存在下分解。另一合適氣 體混合物為一氧化氮及乙烯之混合物。分解之合適溫度為 164545.doc 201251187 (例如)在400至1000°C範圍内,較佳為500至800°C。分解之 合適壓力條件為(例如)在標準壓力至1 〇〇巴(較佳至1 〇巴)之 範圍内。 單壁或多壁奈米碳管可(例如)藉由在弧光下(特定言之在 存在或不存在分解催化劑下)分解含碳化合物而得到。 在一實施例中,在存在分解催化劑(例如Fe、或較佳 Νι)下進行揮發性含碳化合物或含碳化合物之分解。 用於製備本發明複合材料之反應產物之起始混合物包括 作為組份(D)之2-20重量%(較佳3-15重量%,尤其4_〗〇重量 % ;基於反應前使用之組份(A)、(B)及(c)之總重量計)之 全氟化或部分氟化聚合物。 全氟化或部分氟化聚合物(D)之實例可為氟化均聚物或 共聚物。聚合物(D)較佳係選自由聚四氟乙烯、聚氟乙 烯、聚二氟亞乙烯、四氟乙稀·六氟丙烯共聚物、二氟亞 乙烯-六氟丙烯共聚物(PVdF-HFp)、二氟亞乙烯_四氟乙烯 共聚物、全氟烷基乙烯基醚共聚物、乙烯_四氟乙烯共聚 物、二氟亞乙烯-三氟氣乙烯聚合物及乙烯-氟氯乙烯共聚 物組成之群之敗化聚合物之群。 全氟化或部分說化聚合物(D)較佳係以粉末形式使用。 尤其青睞使用具有0.1至1() _(尤其G5至2 _)之平均粒度 之粉末。 在本發明範圍内,聚四I乙 乙烯均聚物,而且意指四氟乙 之共聚物、及由四氟乙缚、六 烯應理解為不僅意指聚四氟 稀與六氟丙烯或二氟亞乙烯 氟丙烯及二氟亞乙烯所組成 164545.doc 201251187 之三元共聚物。 全氟化或部分氟化聚合物(D)較佳為聚四氟乙烯,尤其 係聚四氟乙烯均聚物。 至少兩種以上提及之起始物質已在製備本發明複合材料 期間互相化學反應,較佳為聚合物(A)與硫。在此情況, 聚合物(A)及硫不需與彼此形成共價鍵。例如,硫可僅充 當氧化劑並作為Hj從反應混合物中移除。 在本發明之一實施例中,聚合物(A)及硫(B)在形成本發 明複合材料期間形成共價鍵β 在一較佳實施例中,本發明複合材料進一步包括顆粒或 域,其包含經硫(Β)填充之碳(C)e在本發明之此一實施例 中,硫較佳係以該等顆粒或域分子分散於碳中,例如 以h環形式或以線型硫分子形式(例如線型&分子)。 此等顆粒或域可(例如)藉由電子探針微量分析檢測。 在本發明之一實施例中,此等顆粒或域中之碳(c)之孔 至少經硫(B)部份填充。 此等顆粒或域可具有10至1〇〇 μπι(較佳至7〇 μιη)範圍内 之平均直徑。 此等顆粒可以機械方式從本發明複合材料移除。域不可 以機械方式從本發明複合材料移除。域及顆粒可在顯微鏡 下容易識別。 在本發明之一實施例令,此等顆粒或域包括2:1至US (較佳1:1.5至1:10)範圍内之重量比之碳(c)及硫(Β)。 較佳地’上述顆粒或域在人眼看來為黑色。 164545.doc 201251187 在本發明之一實施例中’上述顆粒或域包含不超過5重 量%之聚合物⑷或不超過5重量%之上述反應產物。在本 發明之一特定實施例中,¾合物⑷及上述反應產物皆不 可在上述顆粒或域中檢測到。 本發明複合材料可進—步包括含顯著比例之上述反應產 物之顆粒或域,例如達至少1〇重量。/〇之程度。後者顆粒或 域可具有5至75 μηι,較佳10至5〇 μηι範圍内之直徑。其等 較佳小於先前的顆粒或域。 在本發明之一實施例中,本發明複合材料藉由元素分析 測定,包括20至80重量%,較佳30至7〇重量%範圍内之 硫。 在本發明之一實施例中,本發明複合材料包括〇.丨至3〇 重量% ’較佳1至20重量。/。範圍内之碳(C)。此碳同樣可(例 如)藉由元素分析測定,儘管在元素分析之評估中必須將 亦經由聚合物(Α)進入本發明複合材料中之碳列入考慮。 為從組份(A)、(Β)、(C)及(D)得到具有所需硫含量之本 發明複合材料之反應產物’必須考慮由於硫與聚合物(Α) 之氫原子反應形成氣態硫化氫所致之使用硫之損失。 基於反應前所用組份(A)、(Β)及(C)之總重量,組份(Α) 之比例(尤其就聚丙烯腈而言)在反應前較佳為4,9至45重量 %,尤其為10至40重量%,組份(β)之比例在反應前較佳為 35至95重量%,尤其為45至85重量%,而組份(〇之比例在 反應前較佳為0.1至20重量%,尤其為5至15重量%。 在本發明之另一實施例中,本發明複合材料可進一步包 164545.doc 201251187 含至少一種黏合劑(E)。黏合劑(E)主要用於機械穩定本發 明複合材料。 在本發明之一實施例中,黏合劑(E)係選自有機(共)聚合 物。合適有機(共)聚合物之實例可為經函化或不含齒素。 實例為聚環氧乙烷(PEO)、纖維素、羧曱基纖維素、聚乙 烯醇 '聚乙烯、聚丙烯、聚四氟乙烯、聚丙烯腈_甲基丙 烯酸甲酯共聚物、苯乙烯·丁二烯共聚物、四氟乙烯_六氟 丙稀共聚物、二氟亞乙稀_六氟丙稀共聚物(PVdF-HFP)、 二氟亞乙烯-四氟乙烯共聚物、全氟烷基乙烯基醚共聚 物、乙烯·四氟乙烯共聚物、二氟亞乙烯-三氟氣乙烯共聚 物、乙烯-氟氣乙烯共聚物、乙烯_丙烯酸共聚物(視情況經 鹼金屬鹽或氨至少部分中和)、乙烯·曱基丙烯酸共聚物(視 情況經鹼金屬鹽或氨至少部分中和)、乙烯_(甲基)丙烯酸 醋共聚物、聚醯亞胺及聚異丁烯。 合適黏合劑尤其係聚乙烯醇及鹵化(共)聚合物,例如聚 氣乙稀或聚二氣亞乙烯,尤其係氟化(共)聚合物,諸如聚 氣乙烯及尤其係聚二氟亞乙烯及聚四氟乙烯。 黏合劑(E)之平均分子量Mw可選擇範圍很廣,合適實例 為 20 〇〇〇 g/m〇l 至 1 〇〇〇 〇〇〇 g/m〇l。 若將黏合劑(E)用於製備本發明複合材料,基於最終複 合材料之質量計,本發明複合材料較佳包含〇. i至1〇重量 % ’更佳5至10重量%及最佳7至8重量%之黏合劑(E)。 可藉由多種方法將黏合劑(E)併入本發明複合材料中。 例如’可將可溶性黏合劑(E)(諸如聚乙烯醇)溶解於合適溶 164545.doc201251187 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to a composite material comprising a reaction product of the following components: (A) at least one organic polymer, (B) sulfur, (C) including at least 60 % sp2 - a polymorphic carbon of a mixed carbon atom, and (D) a 2 to 20% by weight total perfluorinated or partially fluorinated polymer based on the component used before the reaction and the total weight of (c). The invention further relates to a method of making a composite of the invention and to the use of the composite of the invention. [Prior Art] A battery or a rechargeable battery is merely an embodiment that can store electrical energy after generation and use it when needed. Due to the significantly better power density, it has recently evolved from water-based batteries to the development of charge cells in batteries that are completed by lithium ions. However, the density of conventional lithium ion batteries having a carbon anode and a metal oxide based cathode is limited. A new perspective on energy density has been opened up by lithium-sulfur batteries. In the sulphur battery, the sulfur in the sulfur cathode is reoxidized by the polysulfide '(iv) to reduce the sulfur-bonding bond when the battery is charged. • However, the problem is the solubility of polysulfides (such as Li2S4 and Li2S6), which can be colder in the agent and can migrate to the anode. The results can include: loss of capacitance and electrical insulation deposited on the sulfur particles of the electrode. The migration from the cathode to the anode can ultimately result in the discharge of the affected battery and the failure of the battery in the battery pack. The undesired migration of such polysulfide ions is also referred to as "shutuing", and 164545.doc 201251187 is a term also used within the scope of the present invention. There are many attempts to suppress this shuttle. For example, j Wang et al. propose a reaction product of adding sulfur and polyacrylonitrile to the cathode; Adv Funct. Mater. 2003, 13, 487 ff. Thus, a product is formed which is formed by the removal of hydrogen from polyacrylonitrile to simultaneously form hydrogen sulfide. It has also been proposed to use sulfur compounds instead of sulfur, such as CuS, FeS2* 2,5-dimercapto-1,3,4-thiadiazole. However, the capacitance of such batteries is not satisfactory. See, for example, P. Wang, */. five s〇c. 2002, 149 and J. Wang et al., 乂 2〇〇4, 138, 2Ί\. It is also proposed to use sulfur in a finely divided form; see j Wang et al, J. Pwa仏 2004, 27 However, at high current densities, fluctuations in efficiency were observed, which the authors expected to deposit on the (tetra) crystal. This can be cumbersome because it can cause internal short circuits. It is also proposed to mix the reaction product of sulfur and polyacrylonitrile with carbon black and press it to the electrode; J. Wang et al., Shi (10) 2〇〇2, ^(6) ff. When these electrodes were combined with the polymer as electrolysis (4), a decrease in the shuttle mechanism was observed. However, many polymer electrolytes have low electrical conductivity. SUMMARY OF THE INVENTION Accordingly, it is an object of the present invention to provide a cathode material that is easy to prepare and that avoids the disadvantages of the prior art. Another object of the invention is to provide a method for preparing a corresponding cathode material. Therefore, the material defined at the beginning has been found. [Embodiment] 164545.doc 201251187 Japan: The bright material is a composite material, and is also referred to as a hair-recovering σ material within the scope of the present invention. Composite material is understood to mean a solid mixture material that is not artificially dissociable and has properties that are different from the individual components. The material of the invention is in particular a particulate composite. The composite of the present invention comprises the reaction product of the following components: (Α) at least one organic polymer, abbreviated as polymer (Α) or organic polymer (Α). Within the scope of the present invention, the phrase polymer includes a homopolymer. And copolymer, (Β) sulfur (C) includes at least 60. /. Sp2_mixed carbon atom in the form of polymorphic carbon and (D) based on the total weight of components (A), (B) and (C) used before the reaction, 2 to 20% by weight of perfluorinated or partially fluorine Polymer. The polymer (A) may be selected from any of organic polymers and copolymers, and is preferably selected from polymers which can be obtained by anion or radical (co)polymerization. The organic polymer or copolymer preferably consists of atoms of elemental carbon and hydrogen (and optionally nitrogen, 4, oxygen, sulfur and/or gas), especially elemental carbon and hydrogen (and optionally nitrogen, oxygen and/or gas). The atom of 'especially nitrogen'. The "(co)polymerization" means homopolymerization or copolymerization. The term "(co)polymer" means a homopolymer or a copolymer. In another variation, the polymer (A) may be selected from the group consisting of organic polyesters, especially aliphatic polyesters. In one embodiment of the invention, the polymer is selected from (co)polymers obtainable by anionic, catalytic or free radical (co)polymerization, especially polyethylene, polypropylene, polyacrylonitrile, polybutylene Diene, polystyrene and at least 164545.doc 201251187 Two copolymers selected from the group consisting of ethylene, propylene, styrene, (meth) propylene (especially acrylonitrile) and 1,3-butadiene a copolymer of monomers. Further, polyisoprene and polyacrylate are also suitable. Polyacrylonitrile is especially preferred and is also known as polyacrylonitrile (A) within the scope of the present invention. Within the scope of the present invention, polyacrylonitrile should not be understood merely to mean a polyacrylonitrile homopolymer, and means a copolymer of acrylonitrile with hydrazine, 3-butadiene or styrene. A polyacrylonitrile homopolymer is preferred. In one embodiment of the invention, the polyacrylonitrile (A)' is present after the reaction, i.e., in the composite of the present invention, at least partially in the form of a cyclization of formula (1). (I) , , , N, everyone, within the scope of the present invention, polyethylene is understood to mean not only homopolyethylene, but also ethylene copolymer 'which comprises at least 50 mol% of ethylene in copolymerized form and Up to 50 mol% of at least one other comonomer, such as an alpha olefin (such as propylene, butene (1-butene), 1-hexene, octene, decene, decadiene, 1-pentyl Ole and isobutylene), vinyl aromatic compounds (such as styrene) and (mercapto) acrylic acid, ethyl acetate vinegar, ethyl vinegar propionate (meth)acrylic acid 0:1 to (:1〇 Alkyl esters (especially decyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, n-butyl acrylate, 2-ethylhexyl acrylate, n-butyl methacrylate Ester, mercaptopropionic acid 2_ethylhexanoic acid) and maleic acid, maleic anhydride and itaconic acid needle. Polyethylene can be Hdpe or LDPE. 164545.doc 201251187 Within the scope of the invention 'polypropylene It is understood to mean homopolypropylene, and is understood to mean a propylene copolymer comprising at least 50 mol% of propylene in copolymerized form and up to 5 〇 magnetic to Another comonomer such as ethylene and < olefins such as butene, hexene, octene, 1-decene, 1 - decene and 1,4-pentene. The polypropylene is preferably isotactic or basic. Superconducting polypropylene. - Within the scope of the present invention, polystyrene is understood to mean not only a homopolymer of styrene but also styrene and acrylonitrile, butadiene, (meth)acrylic acid, Copolymer of CiiCi decyl (meth) acrylate, divinyl benzene, 1,2-diphenylethylene or α-methyl phenylethylidene (especially with propylene or bismuth-butadiene) Another preferred polymer (Α) is a polybutadiene. In the embodiment of the invention, the compound (4) is selected from the group consisting of 50 〇〇〇 to 5 刖 in the reaction enthalpy. The average molecular weight of g/m〇1 (preferably to 25〇〇〇〇g/m〇i) is ^1~^ In one embodiment of the invention, the polyacrylonitrile (A) is selected from the group consisting of Polyacrylonitrile having an average molecular weight Mw in the range of 10 000 to 500 000 g/m 〇 1 (especially 5 〇〇〇〇 to 250 000 g/mol) before the reaction. The polymer (A) may be crosslinked or Non-crosslinked (co)polymerization • Sulfur (B) is known per se and may also be referred to as sulfur in the context of the present invention. 'Including at least 60% sp2_mixed carbon atoms (preferably at least 75% sp2-mixed carbon atoms) The carbon of the form, also referred to as carbon (C) in the scope of the present invention, is known per se as a conductive polymorph of carbon (C). For example, carbon (C) may be graphite. All impurities (c) included in the composite 164545.doc 201251187 material of the present invention under chemical reaction conditions include any impurities and represent weight percentages. In one embodiment of the invention, the carbon is carbon black. The carbon black can, for example, be selected from the group consisting of lamp black, furnace black, flame carbon black, thermally cracked carbon black, acetylene black, and industrial carbon black. The carbon black may include impurities such as hydrocarbons (especially aromatic hydrocarbons) or oxygenates or oxygen-containing groups (e.g., hydrazine H groups). In addition, sulfur black or iron-containing impurities may be present in the carbon black. The carbon (c) used to prepare the reaction product of the composite of the present invention is preferably selected from carbon black. In a variant, carbon (C) is a partially oxidized carbon black. In an embodiment of the invention, the carbon (C) comprises a carbon nanotube. Nanocarbon camps (reduced CNTs), such as single-walled carbon nanotubes (sw CNTs) and preferably multi-walled carbon nanotubes (MW CNTs), are known per se. The preparation thereof and some of its properties are described, for example, by A. Jess et al. in c/zemz.e / «geWew 2006, 7 < §, 94-100. In one embodiment of the invention, the carbon nanotubes have a diameter in the range of 〇4 to 5 〇 nm (preferably 1 to 25 nm). In one embodiment of the invention, the carbon nanotubes have a 10 nm to The length in the range of 丨mm (preferably 100 nm to 500 nm). The carbon nanotubes can be prepared by a method known per se. For example, a volatile carbon compound (such as decane or carbon monoxide, acetylene or ethylene) or a mixture of volatile carbon compounds (such as a synthesis gas) may be used in one or more reducing agents (eg, hydrogenated milk and/or another gas, Decomposition in the presence of, for example, nitrogen). Another suitable gas mixture is a mixture of nitric oxide and ethylene. A suitable temperature for decomposition is 164545.doc 201251187 (for example) in the range of 400 to 1000 ° C, preferably 500 to 800 ° C. Suitable pressure conditions for decomposition are, for example, in the range of standard pressures up to 1 mbar (preferably to 1 mbar). Single-walled or multi-walled carbon nanotubes can be obtained, for example, by decomposing carbon-containing compounds under arcing, in particular in the presence or absence of a decomposition catalyst. In one embodiment, the decomposition of the volatile carbonaceous compound or carbonaceous compound is carried out in the presence of a decomposition catalyst (e.g., Fe, or preferably oxime). The starting mixture for the preparation of the reaction product of the composite of the invention comprises, as component (D), from 2 to 20% by weight (preferably from 3 to 15% by weight, in particular from 4% by weight); based on the components used before the reaction. A perfluorinated or partially fluorinated polymer based on the total weight of (A), (B) and (c). An example of the perfluorinated or partially fluorinated polymer (D) may be a fluorinated homopolymer or copolymer. The polymer (D) is preferably selected from the group consisting of polytetrafluoroethylene, polyvinyl fluoride, polydifluoroethylene, tetrafluoroethylene hexafluoropropylene copolymer, and difluoroethylene-hexafluoropropylene copolymer (PVdF-HFp). , difluoroethylene ethylene_tetrafluoroethylene copolymer, perfluoroalkyl vinyl ether copolymer, ethylene_tetrafluoroethylene copolymer, difluoroethylene-trifluoroethylene polymer and ethylene-fluorovinyl chloride copolymer A group of disastrous polymers of the group. The perfluorinated or partially polymerized polymer (D) is preferably used in the form of a powder. It is especially preferred to use a powder having an average particle size of 0.1 to 1 () _ (especially G5 to 2 _). Within the scope of the present invention, polytetramethylene glycol homopolymer, and means tetrafluoroethylene copolymer, and tetrafluoroethylene, hexaene are understood to mean not only polytetrafluoroethylene and hexafluoropropylene or two Fluorinated fluoropropene and difluoroethylene are composed of a ternary copolymer of 164545.doc 201251187. The perfluorinated or partially fluorinated polymer (D) is preferably polytetrafluoroethylene, especially a polytetrafluoroethylene homopolymer. At least two of the above-mentioned starting materials have been chemically reacted with each other during the preparation of the composite of the present invention, preferably polymer (A) and sulfur. In this case, the polymer (A) and sulfur do not need to form a covalent bond with each other. For example, sulfur can only act as an oxidant and be removed from the reaction mixture as Hj. In one embodiment of the invention, polymer (A) and sulfur (B) form a covalent bond during formation of the composite of the invention. In a preferred embodiment, the composite of the present invention further comprises particles or domains. Containing sulfur (Β)-filled carbon (C)e In this embodiment of the invention, the sulfur is preferably dispersed in the carbon by the particles or domain molecules, for example in the form of a h ring or in the form of a linear sulfur molecule. (eg line type & numerator). Such particles or domains can be detected, for example, by electron probe microanalysis. In one embodiment of the invention, the pores of carbon (c) in such particles or domains are at least partially filled with sulfur (B). These particles or domains may have an average diameter in the range of 10 to 1 〇〇 μπι (preferably to 7 〇 μηη). These particles can be mechanically removed from the composite of the present invention. The domain cannot be mechanically removed from the composite of the present invention. The domains and particles are easily identifiable under the microscope. In one embodiment of the invention, the particles or domains comprise carbon (c) and sulfur (helium) in a weight ratio ranging from 2:1 to US (preferably from 1:1.5 to 1:10). Preferably, the above particles or domains are black to the human eye. 164545.doc 201251187 In one embodiment of the invention, the above particles or domains comprise no more than 5% by weight of polymer (4) or no more than 5% by weight of the above reaction product. In a particular embodiment of the invention, neither the compound (4) nor the above reaction product is detectable in the particles or domains described above. The composite of the present invention may further comprise particles or domains comprising a significant proportion of the above reaction product, for example up to at least 1 Torr. / The extent of 〇. The latter particles or domains may have a diameter in the range of 5 to 75 μηι, preferably 10 to 5 μ μη. It is preferably smaller than the previous particles or domains. In one embodiment of the invention, the composite of the invention comprises, by elemental analysis, sulfur in the range of from 20 to 80% by weight, preferably from 30 to 7% by weight. In one embodiment of the invention, the composite of the invention comprises from 〇. 丨 to 3 重量% by weight, preferably from 1 to 20 重量. /. Carbon (C) within the range. This carbon can also be determined, for example, by elemental analysis, although carbon which is also incorporated into the composite of the invention via the polymer (Α) must be taken into account in the evaluation of the elemental analysis. The reaction product of the composite of the invention having the desired sulfur content from components (A), (Β), (C) and (D) must be considered to form a gaseous state due to the reaction of sulfur with the hydrogen atom of the polymer (Α). Loss of sulfur used due to hydrogen sulfide. The proportion of the component (Α) (especially in the case of polyacrylonitrile) is preferably 4, 9 to 45% by weight before the reaction, based on the total weight of the components (A), (Β) and (C) used before the reaction. In particular, from 10 to 40% by weight, the proportion of the component (β) is preferably from 35 to 95% by weight, particularly from 45 to 85% by weight, before the reaction, and the proportion of the component (the ratio of ruthenium is preferably 0.1 before the reaction). Up to 20% by weight, especially 5 to 15% by weight. In another embodiment of the invention, the composite material of the invention may further comprise 164545.doc 201251187 comprising at least one binder (E). The binder (E) is mainly used The composite of the present invention is mechanically stabilized. In one embodiment of the invention, the binder (E) is selected from the group consisting of organic (co)polymers. Examples of suitable organic (co)polymers may be either functional or toothless. Examples are polyethylene oxide (PEO), cellulose, carboxymethyl cellulose, polyvinyl alcohol 'polyethylene, polypropylene, polytetrafluoroethylene, polyacrylonitrile-methyl methacrylate copolymer, benzene. Ethylene-butadiene copolymer, tetrafluoroethylene-hexafluoropropylene copolymer, difluoroethylene-hexafluoropropylene copolymer (P VdF-HFP), difluoroethylene-tetrafluoroethylene copolymer, perfluoroalkyl vinyl ether copolymer, ethylene·tetrafluoroethylene copolymer, difluoroethylene-trifluoroethylene copolymer, ethylene-fluorine gas Ethylene copolymer, ethylene-acrylic acid copolymer (optionally at least partially neutralized with alkali metal salt or ammonia), ethylene thioglycolic acid copolymer (optionally at least partially neutralized with alkali metal salt or ammonia), ethylene _ (A Acrylic vinegar copolymer, polyimine and polyisobutylene. Suitable binders are, in particular, polyvinyl alcohol and halogenated (co)polymers, such as polyethylene oxide or polydiethylene vinylene, especially fluorinated (total) Polymers, such as polyethylene and especially polydifluoroethylene and polytetrafluoroethylene. The average molecular weight Mw of the binder (E) can be selected from a wide range, suitable examples are 20 〇〇〇g/m〇l to 1 〇〇〇〇〇〇g/m〇l. If the binder (E) is used to prepare the composite material of the present invention, the composite material of the present invention preferably comprises 〇.1 to 1% by weight based on the mass of the final composite material. 'More preferably 5 to 10% by weight and most preferably 7 to 8% by weight of adhesion (E). The binder may be by a variety of methods (E) is incorporated in the composite material of the present invention. For example 'may be soluble binder (E) (such as polyvinyl alcohol) was dissolved in a suitable solvent 164545.doc

S 201251187 劑或溶劑混合物(例如適合於聚乙烯醇之水/異丙醇)中,並 與其匕陰極成分一起製備懸浮液。在施用至合適基材後, 移除溶劑或溶劑混合物(例如蒸發),得到本發明複合材 料。聚二氟亞乙稀之合適溶劑為Nmp。 若需要使用難溶性聚合物作為黏合劑(E)(例如其它全氟 化或部份氟化(共)聚合物,諸如聚四氟乙烯或四氟乙烯-六 氟丙烯共聚物)’則製備所論述黏合劑斤)顆粒與陰極之其 它成分之懸浮液’並在熱條件下壓縮。 在本發明之一實施例中,本發明複合材料額外包括在非 反應條件下併入至複合材料中之碳。此額外碳可選自與碳 (C)相同之物質。其在每種情況下可與碳(c)相同或不同; 例如,碳(C)及所選擇之額外碳可為兩種不同碳黑或石 墨。 在本發明之一實施例中,本發明複合材料額外包括未與 有機聚合物(A)或聚丙烯腈(A)及硫(B)反應之碳黑。 在本發明之一實施例中,基於最終複合材料之質量計, 本發明複合材料包括0.1至10重量%之額外碳,較佳為額外 碳黑。 本發明複合材料特別適合作為或用於製備電極,尤其用 於製備含鋰電池組之電極。本發明提供本發明複合材料作 為或用於製備電池之電極的用途。本發明進一步提供包括 至少一個已由(或使用)至少一種本發明複合材料製備之電 極之電池。 在本發明之一實施例中’所論述的電極為陰極,其亦可 164545.doc •13- 201251187 稱為硫陰極或s陰極。在本發明範圍内,稱為陰極之電極 係在放電(操作)時具有還原作用者。 在本發明之-實施例中,本發明複合材料係經處理以提 供電極,例如呈由電池組生產商所處理之連續帶形式。 從本發明複合材料製備之電極可(例如)具有2〇至5〇〇 μπι、較佳40至2〇〇 μιη之厚度。其等可(例如)具有棒形組 態,或以圓形、橢圓形或方形柱體形式或以立方體形式配 置,或作為扁平電極。 在本發明之一實施例中,本發明電池除本發明複合材料 外,還包括至少一個包含金屬鋅、金屬鈉或較佳金屬鋰之 電極。 在本發明之一實施例中,本發明電池除本發明複合材料 及另一電極外,還包括至少一種非水性溶劑,其在室溫下 可為液體或固體,較佳係選自聚合物、環醚或非環醚 '環 狀或非環狀縮醛、環狀或非環狀有機碳酸酯及離子性液 體。 合適聚合物之實例尤其係聚烷二醇,較佳為聚Cl_c4^ 二醇及尤其係聚乙二醇。此等聚乙二醇可包括多達2〇 mol%之一或多種呈共聚形式之Cl_C4烷二醇。聚烷二醇較 佳為兩端經甲基或乙基封端之聚烷二醇。 合適聚炫一醇及尤其合適聚乙二醇之分子量Mw可為至 少 400 g/mol 〇 合適聚坑一醇及尤其合適聚乙二醇之分子量Mw可高達5 000 000 g/mol,較佳高達 2 000 000 g/m〇i。 164545.docS 201251187 A solvent or solvent mixture (e.g., water/isopropanol suitable for polyvinyl alcohol) and a suspension prepared with its ruthenium cathode component. After application to a suitable substrate, the solvent or solvent mixture (e. g., evaporation) is removed to provide a composite of the present invention. A suitable solvent for polydifluoroethylene is Nmp. If it is desired to use a poorly soluble polymer as the binder (E) (for example, other perfluorinated or partially fluorinated (co)polymers such as polytetrafluoroethylene or tetrafluoroethylene-hexafluoropropylene copolymer) A suspension of the binder and other components of the cathode is discussed and compressed under thermal conditions. In one embodiment of the invention, the composite of the invention additionally comprises carbon incorporated into the composite under non-reactive conditions. This additional carbon may be selected from the same materials as carbon (C). It may be the same or different in carbon (c) in each case; for example, carbon (C) and the selected additional carbon may be two different carbon blacks or graphites. In one embodiment of the invention, the composite of the invention additionally comprises carbon black which is not reactive with the organic polymer (A) or polyacrylonitrile (A) and sulfur (B). In one embodiment of the invention, the composite of the invention comprises from 0.1 to 10% by weight of additional carbon, preferably additional carbon black, based on the mass of the final composite. The composite materials of the invention are particularly suitable for use in or for the preparation of electrodes, particularly for the preparation of electrodes for lithium-containing battery packs. The invention provides the use of the composite of the invention as or for the preparation of electrodes for batteries. The invention further provides a battery comprising at least one electrode that has been prepared from (or used in) at least one composite of the invention. In one embodiment of the invention, the electrode discussed is a cathode, which may also be referred to as a sulfur cathode or a s cathode, 164545.doc • 13-201251187. Within the scope of the present invention, an electrode referred to as a cathode has a reducing action upon discharge (operation). In an embodiment of the invention, the composite of the invention is treated to provide an electrode, for example in the form of a continuous strip that is processed by a battery manufacturer. The electrode prepared from the composite of the present invention may, for example, have a thickness of from 2 Å to 5 Å μm, preferably from 40 to 2 Å μηη. They may, for example, have a rod configuration, or be arranged in the form of a circle, an ellipse or a square cylinder or in the form of a cube, or as a flat electrode. In one embodiment of the invention, the battery of the present invention comprises, in addition to the composite of the present invention, at least one electrode comprising metallic zinc, metallic sodium or preferably metallic lithium. In one embodiment of the present invention, the battery of the present invention comprises, in addition to the composite material of the present invention and another electrode, at least one non-aqueous solvent, which may be liquid or solid at room temperature, preferably selected from the group consisting of polymers, A cyclic ether or acyclic ether 'cyclic or acyclic acetal, a cyclic or acyclic organic carbonate, and an ionic liquid. Examples of suitable polymers are, in particular, polyalkylene glycols, preferably polyCl_c4^diols and especially polyethylene glycols. Such polyethylene glycols may comprise up to 2 mole% of one or more of the Cl_C4 alkanediols in copolymerized form. The polyalkylene glycol is preferably a polyalkylene glycol terminated with a methyl group or an ethyl group at both ends. Suitable polystyrenes and especially suitable polyethylene glycols may have a molecular weight Mw of at least 400 g/mol, a suitable polyhydric alcohol and especially a suitable polyethylene glycol having a molecular weight Mw of up to 5 000 000 g/mol, preferably up to 2 000 000 g/m〇i. 164545.doc

S J如)二異丙醚、二正丁基醚、 乙氧基乙烷,較佳為1,2-二甲氧 201251187 合適非環謎之實例為(例 1,2-二甲氧基乙烷、1 7 A ,之-二 2 基乙烷。 合適環醚之實例為四f 氧°夫°南及1,4 -二SJ such as diisopropyl ether, di-n-butyl ether, ethoxyethane, preferably 1,2-dimethoxy 201251187. Examples of suitable acyclic mysteries are (example 1,2-dimethoxyethane) , 1 7 A, bis-diylethane. Examples of suitable cyclic ethers are tetraf-oxygens and south, and 1,4 - two

二氧雜環戊烷。 合適非環狀有機碳酸賴之實例為碳酸二 »及1,4-二氧雜環己烷。 例如)二甲醇縮甲链、二乙醇 [~一乙氧乙炫。 -二氧雜環己烷及尤其為丨,3_ 乙酯及碳酸二乙酯。 二曱S旨、碳酸甲醋 合適環狀有機碳酸醋之實例為通式及_之化合物Dioxolane. Examples of suitable acyclic organic carbonic acid salts are carbonic acid di- and 1,4-dioxane. For example, dimethanol methyl chain, diethanol [~ ethoxy ethoxy). Dioxane and especially hydrazine, 3-ethyl ester and diethyl carbonate. Example of a suitable cyclic organic carbonated vinegar, which is a compound of the formula

R FTR FT

其中’ R1、R2及R3可相同或不同’且係選自氫&Ci_C4•燒 基,例如甲基、乙基、正丙基、異丙基、正丁基、異丁 基、第二丁基及第三丁基’其中R2及R3較佳不同時為第三 丁基。 在特佳實施例中,R為甲基’及R及R3各爲氫,或r 1、 R2及R3各為氫。 164545.doc •15· 201251187 另一較佳環狀有機碳酸酯為式(ιν)之碳酸伸乙烯酯。 又 0 0 W ον) 溶劑較佳係以所謂之無水狀態使用,即水含量在1 ppnl 至〇. 1重量°/〇範圍内’可(例如)藉由卡爾費休滴定法(Karl Fischer titration)來測定 〇 在本發明之一實施例中,本發明電化電池包括一或多種 導電鹽’較佳為鋰鹽。合適鋰鹽之實例為LiPF6、LiBF4、Wherein 'R1, R2 and R3 may be the same or different' and are selected from hydrogen &Ci_C4•alkyl, such as methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, second The base and the third butyl group, wherein R2 and R3 are preferably different, are a third butyl group. In a particularly preferred embodiment, R is methyl' and R and R3 are each hydrogen, or r 1 , R 2 and R 3 are each hydrogen. 164545.doc •15· 201251187 Another preferred cyclic organic carbonate is a carbonic acid extending vinyl ester of the formula (ιν). Further, 0 0 W ον) The solvent is preferably used in a so-called anhydrous state, that is, the water content is in the range of 1 ppnl to 〇. 1 weight °/〇, which can be, for example, by Karl Fischer titration. To determine enthalpy In one embodiment of the invention, the electrochemical cell of the present invention comprises one or more conductive salts 'preferably a lithium salt. Examples of suitable lithium salts are LiPF6, LiBF4,

LiC104、LiAsF6 ' LiCF3S03、LiC(CnF2n+1S〇2)3、亞胺化鋰 諸如LiN(CnF2n+iS02)2(其中n為1至20之整數)、LiN (S02F)2、Li2SiF6、LiSbF6、LiAlCl4、及通式(CnF2n+1S02)m XLi之鹽’其中m係定義如下: 當X係選自氧及硫時,m= 1, 當X係選自氮及峨時,m=2,及 當X係選自碳及石夕時,m=3。 較佳導電鹽係選自 LiC(CF3S02;h、LiNKCF3S〇2)2、 LiPF6、LiBF4、LiC104 ’ 尤佳為 LiPF6&LiN(CF3S02)2。 在本發明之一實施例中’本發明電化電池包括一或多個 用來機械分離電極之隔離物。合適的隔離物為聚合物膜, 尤其係對金屬鋰及硫化鋰及多硫化鋰不起反應之多孔聚合 物膜。尤其合適之隔離物材料為聚烯烴,尤其係膜形式之 多孔聚乙稀及膜形式之多孔聚丙稀。 由聚烯烴製備(尤其係由聚乙烯或聚丙烯製備)之隔離物 164545.doc -16 201251187LiC104, LiAsF6 'LiCF3S03, LiC(CnF2n+1S〇2)3, lithium iminoide such as LiN(CnF2n+iS02)2 (where n is an integer from 1 to 20), LiN(S02F)2, Li2SiF6, LiSbF6, LiAlCl4 And a salt of the formula (CnF2n+1S02)m XLi' wherein m is defined as follows: when X is selected from oxygen and sulfur, m = 1, when X is selected from nitrogen and helium, m = 2, and when The X system is selected from the group consisting of carbon and Shixia, and m=3. Preferably, the conductive salt is selected from the group consisting of LiC(CF3S02; h, LiNKCF3S〇2)2, LiPF6, LiBF4, LiC104', and particularly preferably LiPF6&LiN(CF3S02)2. In one embodiment of the invention, the electrochemical cell of the present invention comprises one or more spacers for mechanically separating the electrodes. Suitable separators are polymeric membranes, especially porous polymeric membranes which do not react with metallic lithium and lithium sulfide and lithium polysulfide. Particularly suitable separator materials are polyolefins, especially porous polypropylene in the form of a film and porous polypropylene in the form of a film. Separator made of polyolefin (especially made of polyethylene or polypropylene) 164545.doc -16 201251187

梭。本發明電池極其適用於汽車、 同電谷、甚至在反復充電 夫效°可極有效地抑制穿 、飛機、船隻或靜態能量 儲存。此等用途形成本發明主題内容之另一部份。 本發明進一步提供一種製備本發明複合材料之方法在 本發明範圍内亦稱為本發明製備方法。本發明製備方法包 括至少一個製程步驟,其中使 (A) 至少一種有機聚合物, (B) 硫, (C) 包括至少60% sp2·混成化碳原子之呈多形體之碳,及 (D) 基於所使用組份(A)、(B)及(c)之總重量計,2至2〇重 量之全氟化或部分氟化聚合物 在150至400°C(較佳200至350°C)範圍内之溫度下相互反 在此方法中,有機聚合物(A)、硫(B)、碳(〇及全氟化或 部分氟化聚合物(D)分別定義如上’尤其亦關於其較佳實 施例。 有機聚合物(A)較佳係選自聚乙烯、聚丙稀、聚丙稀 腈、聚丁二烯、聚苯乙烯及至少兩種選自乙稀、丙稀、苯 164545.doc 17 201251187 乙烯、丙烯腈及1,3-丁二烯(最佳選自丙烯腈)之共聚單體 之共聚物。 組份(A)、(B)、(C)及(D)係在熱反應前以熟習此項技術 者可從熱反應後期望的最終組合物開始,並考慮可能在熱 反應中形成之氣體副產物(特定言之諸如硫化氮)以簡單方 式計算之比例相互結合。 本發明製備方法可在溶劑(例如甲苯或乙醇)存在下進 行。然而,較佳在無溶劑存在下進行本發明製備方法。 在本發明之一實施例中,本發明製備方法係在環境壓力 下(即標準壓力下)進行》 在本發明之另一實施例中,本發明製備方法係在高壓下 (例如在1 · 1至1 〇〇巴下)進行。 在本實施例之另一實施例中,本發明製備方法係在自生 壓力下進行β為此目的,可建立任何壓力(例如丨〇巴或者 標準壓力)’及在壓力容器(例如高壓釜)中進行反應。所形 成之氣體副產物(尤其係HzS)可在反應期間提高壓力,(例 如)至高達100巴或者更高之壓力。若需要在自生壓力下進 行本發明製備方法,則可使用壓力測量來監控反應。 在本發明之一實施例中,本發明製備方法可進行在10分 鐘至1 00小時範圍内之時段,較佳為二至24小時。 較佳地,在反應結束後,使所得之本發明複合材料不含 ,例如將其脫氣。脫氣可(例如)藉由抽真空或藉由用 惰性氣體(例如用氮或諸如氬之惰性氣體)沖洗而完成。 本發明複合材料通常係以粉末形式獲得。 164545.docshuttle. The battery of the present invention is extremely suitable for use in automobiles, electric valleys, and even in repeated charging. It is extremely effective in suppressing wear, aircraft, watercraft or static energy storage. These uses form part of the subject matter of the present invention. The invention further provides a process for the preparation of the composite of the invention which is also referred to as the process of the invention within the scope of the invention. The preparation method of the present invention comprises at least one process step wherein (A) at least one organic polymer, (B) sulfur, (C) comprises at least 60% sp2 of a polymorphic carbon of a mixed carbon atom, and (D) 2 to 2 Å by weight of the perfluorinated or partially fluorinated polymer at 150 to 400 ° C (preferably 200 to 350 ° C) based on the total weight of the components (A), (B) and (c) used. In the range of temperature, the organic polymer (A), sulfur (B), carbon (germanium and perfluorinated or partially fluorinated polymer (D) are respectively defined as above, especially A preferred embodiment. The organic polymer (A) is preferably selected from the group consisting of polyethylene, polypropylene, polyacrylonitrile, polybutadiene, polystyrene, and at least two selected from the group consisting of ethylene, propylene, and benzene 164545.doc 17 201251187 Copolymer of comonomers of ethylene, acrylonitrile and 1,3-butadiene (optimally selected from acrylonitrile). Components (A), (B), (C) and (D) are in thermal reaction. Those skilled in the art can start with the desired final composition after the thermal reaction and consider gaseous by-products that may form in the thermal reaction (specifically, such as nitrogen sulfide) The ratios calculated in a simple manner are combined with each other. The preparation method of the present invention can be carried out in the presence of a solvent such as toluene or ethanol. However, it is preferred to carry out the preparation method of the present invention in the absence of a solvent. The preparation method of the present invention is carried out under ambient pressure (ie, under standard pressure). In another embodiment of the present invention, the preparation method of the present invention is carried out under high pressure (for example, at 1:1 to 1 Torr). In another embodiment of the present embodiment, the method of the present invention is carried out under autogenous pressure for this purpose, any pressure (e.g., bar or standard pressure) can be established 'and in a pressure vessel (e.g., autoclave). The reaction is carried out in. The gaseous by-product formed (especially HzS) can increase the pressure during the reaction, for example up to a pressure of up to 100 bar or higher. If it is desired to carry out the preparation process according to the invention under autogenous pressure, it can be used The pressure measurement is used to monitor the reaction. In one embodiment of the present invention, the preparation method of the present invention can be carried out for a period of time ranging from 10 minutes to 100 hours, preferably Preferably, after completion of the reaction, the resulting composite of the invention is free, for example degassed. Degassing can be carried out, for example, by vacuuming or by using an inert gas (for example with nitrogen or The rinsing is accomplished by an inert gas such as argon. The composite of the invention is typically obtained in powder form. 164545.doc

S 201251187 本發明進一步提供使用至少一種本發明電池操作汽車、 飛機、船隻或靜態能量儲存之方法。 本發明藉由以下非限定實例來說明。 除非另有明確說明,否則以%表示之數值係指重量百分 比。 1. 合成複合材料 1,1合成對照複合材料C-CM.1 (碳黑-PAN-S複合物) 使20 g硫、1〇 g聚丙烯腈及6 g碳黑(以Ketjen Black自市 面購得)在研缽中均質化並導入3〇〇 ml高壓釜中。在自生壓 力下在280 c下實施轉化,同時攪拌(300 rpm)12小時。在 此期間’壓力升至43巴。隨後,經由NaOH滌氣器將所形 成之H2S排出,並用氮沖洗複合物24小時。得到29.4 g硬的 深灰色至黑色粉末C-CM. 1。 元素分析: C=43.5 g/100 g S=45.8 g/100 g N=7.5 g/l〇〇 g H= 1.4 g/l〇〇 g。 1.2合成本發明複合材料CM 2(pTFE_碳黑_pAN_s複合物) 使19.1 g硫、6.4 g聚丙烯腈、4 5 g碳黑(以Ketjen Biack 自市面購得)及2.1 g具有ΐμπι平均粒度之鐵氟龍(Tefl〇n)粉 末在研缽中均質化並導入3〇〇…高壓釜中。在自生壓力下 在280°C下實施轉化,同時攪拌(3〇〇 rpm)12小時。在此期 間,壓力升至21巴。隨後,經由Na〇H滌氣器將所形成之 164545.doc -19· 201251187 HZS排出,並用氮沖洗複合物24小時。得到25 2这細粉狀材 料 CM_2。 ’ 元素分析: C = 35.3 g/l〇〇 g S = 50.0 g/l〇〇 g N=6.3 g/lOOg H=<0.5 g /l〇〇g。 II.製備電極 II_1自C.CM.l製備對照陰極c-c.l 為製備油墨,將0·09 g鐵氟龍、o 〇5 g石墨(以KS6購自S 201251187 The invention further provides a method of operating a car, aircraft, vessel or static energy storage using at least one of the inventive batteries. The invention is illustrated by the following non-limiting examples. Values expressed in % are by weight unless otherwise indicated. 1. Synthetic composite material 1,1 synthetic control composite material C-CM.1 (carbon black-PAN-S complex) 20 g sulfur, 1 〇g polyacrylonitrile and 6 g carbon black (purchased by Ketjen Black) It was homogenized in a mortar and introduced into a 3 〇〇 ml autoclave. The conversion was carried out at 280 c under autogenous pressure while stirring (300 rpm) for 12 hours. During this period, the pressure rose to 43 bar. Subsequently, the formed H2S was discharged through a NaOH scrubber, and the composite was washed with nitrogen for 24 hours. Obtained 29.4 g of a hard dark gray to black powder C-CM. Elemental analysis: C = 43.5 g / 100 g S = 45.8 g / 100 g N = 7.5 g / l 〇〇 g H = 1.4 g / l 〇〇 g. 1.2 Synthesis of the composite material CM 2 of the invention (pTFE_carbon black_pAN_s complex) 19.1 g sulfur, 6.4 g polyacrylonitrile, 45 g carbon black (commercially available from Ketjen Biack) and 2.1 g have an average particle size of ΐμπι The Teflon powder was homogenized in a mortar and introduced into a 3 Torr autoclave. The conversion was carried out at 280 ° C under autogenous pressure while stirring (3 rpm) for 12 hours. During this period, the pressure rose to 21 bar. Subsequently, the formed 164545.doc -19·201251187 HZS was discharged through a Na〇H scrubber, and the complex was washed with nitrogen for 24 hours. 25 2 of this fine powder material CM_2 was obtained. ' Elemental analysis: C = 35.3 g/l 〇〇 g S = 50.0 g/l 〇〇 g N=6.3 g/lOOg H=<0.5 g /l 〇〇g. II. Preparation of electrode II_1 Preparation of control cathode c-c.l from C.CM.l For preparation of ink, 0.09 g of Teflon, o 〇5 g of graphite (purchased from KS6)

Timcal AG,6743 Bodio,Switzerland)及 1.67 g C-CM.1 添加 至^』g水/異丙醇中並攪拌。為進行分散,將混合物轉移 至不鏽鋼研磨容器中,然後使用球磨機(來自FHtsch之 Pulverisette),使用不鏽鋼球以300 rpm攪拌3〇分鐘。分散 操作產生具有油脂稍度之極均質油墨。藉助喷刷方法於真 空吸附平臺上將油墨喷至鋁箔上(溫度:60。〇)。使用氮氣 進行喷霧。得到2.5 mg/cm2之固體負載量。 II.2自CM.2製備本發明陰極c.2 為製備油墨’將0.04 g石墨(以KS6購自Timcal AG,6743 Bodio,Switzerland)及 1.69 g CM.2添加至 17.0 g水/異丙醇 中並攪拌混合物。為進行分散,將混合物轉移至不鏽鋼研 磨容器中,然後使用球磨機(來自Fritsch之pulverisette), 使用不鏽鋼球以3 0 0 rpm擾拌3 0分鐘。分散操作產生具有 油脂稠度之極均質油墨。藉助喷刷方法於真空吸附平臺上 164545.doc -20- 201251187 將油墨喷至鋁箔上(溫度:6〇。〇。使用氮氣進行喷霧。得 到2.5 mg/cm2之固體負載量。 III.於電化電池中測試陰極 為得到對照陰極C-C.1及本發明陰極C.2之電化特性,根 . 據圖1組裝電化電池。為此目的,除II·中所製備之陰極 • 外’在每種情況下使用以下組份: 陽極. 鐘羯,厚度50 μηι, 隔離物: 微孔、三層膜(ΡΡ/ΡΕ/ΡΡ),厚度38 μπι (以 Celgard® 2340自市面購得) 陰極: 根據實例II. 電解質: 1M LiTFSI (LiN(S02CF3)2)含於二氧雜環戊 烷及二曱氧基乙烷(1:1)之混合物中 圖1顯示用於測試本發明複合材料之經拆卸電化電池之 示意結構。 圖1中之註釋意為: 1,Γ 模頭 2, 2' 螺帽 3, 3' * 密封環一每種情況中兩個,此處未顯示每種 情況中第二個稍小的密封環 . 4 螺旋彈簧 5 由鎳製成之輸出導體 6 外殼 在1.8至2.5 V範圍内之電位下使用7.50 mA之電流進行特 定電池之充電與放電。結果彙整於表1中, 164545.doc 21 201251187 表1 :本發明及非本發明電化電池之測試結果 實例 放電容量 第5次循環 [mA-h/g S] 放電容量 第50次循環 [mA-h/g S] 放電容量 第100次循環 [mA-h/g S] 基於C-CM.1之陰 極 C-C.1 830 690 (電池組崩潰) 基於CM.2之陰極 C.2 870 850 700 【圖式簡單說明】 圖1顯示用於測試本發明複合材料之經拆卸電化電池之 示意結構。 【主要元件符號說明】 1 模頭 Γ 模頭 2 螺帽 2' 螺帽 3 密封環 3' 密封環 4 螺旋彈簧 5 鎳製輸出導體 6 外殼 164545.doc -22-Timcal AG, 6743 Bodio, Switzerland) and 1.67 g C-CM.1 were added to the water/isopropanol and stirred. For dispersion, the mixture was transferred to a stainless steel grinding vessel and then stirred using a ball mill (Pulverisette from FHtsch) using a stainless steel ball at 300 rpm for 3 minutes. The dispersion operation produces an extremely homogeneous ink with a slight grease. The ink was sprayed onto the aluminum foil by means of a spray method on a vacuum adsorption platform (temperature: 60 〇). Spray with nitrogen. A solid loading of 2.5 mg/cm2 was obtained. II.2 Preparation of cathode c.2 of the invention from CM.2 To prepare ink '0.04 g of graphite (purchased from Sigma 6 from Timcal AG, 6743 Bodio, Switzerland) and 1.69 g of CM.2 to 17.0 g of water/isopropanol Mix and stir the mixture. For dispersion, the mixture was transferred to a stainless steel grinding vessel, and then a ball mill (pulverisette from Fritsch) was used, and a stainless steel ball was used to scramble for 30 minutes at 300 rpm. The dispersion operation produces an extremely homogeneous ink with a consistency of oil. The ink was sprayed onto the aluminum foil by means of a spray method on a vacuum adsorption platform 164545.doc -20- 201251187 (temperature: 6 Torr. 〇. Spraying with nitrogen to obtain a solid loading of 2.5 mg/cm2. III. The test cathode in the battery is obtained by comparing the electrochemical characteristics of the cathode CC.1 and the cathode C.2 of the present invention. The electrochemical cell is assembled according to Fig. 1. For this purpose, except for the cathode prepared in II. The following components were used: Anode. Crypt, thickness 50 μηι, spacer: microporous, three-layer film (ΡΡ/ΡΕ/ΡΡ), thickness 38 μπι (commercially available from Celgard® 2340) Cathode: According to Example II Electrolyte: 1M LiTFSI (LiN(S02CF3)2) is contained in a mixture of dioxolane and dimethoxyethane (1:1). Figure 1 shows the disassembled electrochemical cell used to test the composite of the present invention. The schematic structure in Fig. 1 means: 1, 模 die 2, 2' nut 3, 3' * seal ring one of two in each case, here is not shown the second one in each case Small sealing ring. 4 coil spring 5 output conductor made of nickel 6 housing in 1.8 Charging and discharging of a specific battery using a current of 7.50 mA at a potential of 2.5 V. The results are summarized in Table 1, 164545.doc 21 201251187 Table 1: Test Results of the Invention and Non-Inventive Electrochemical Cell Example Discharge Capacity 5 cycles [mA-h/g S] discharge capacity 50th cycle [mA-h/g S] discharge capacity 100th cycle [mA-h/g S] Cathode CC.1 based on C-CM.1 830 690 (Battery pack collapse) Cathode C.2 870 850 700 based on CM.2 [Schematic description of the drawing] Fig. 1 shows a schematic structure of a disassembled electrochemical cell for testing the composite material of the present invention. 1 Die Γ Die 2 Nut 2' Nut 3 Sealing ring 3' Sealing ring 4 Coil spring 5 Nickel output conductor 6 Housing 164545.doc -22-

Claims (1)

201251187 七、申請專利範圍: 1 · 一種複合材料,其包括以下組份之反應產物: (A) 至少一種有機聚合物, (B) 硫, (C) 包括至少60。/〇 sp2-混成化碳原子之呈多形體之碳,及 (D) 基於反應前所使用組份、(B)及之總重量計,2 至20重量%之全氟化或部分氟化聚合物。 2. 如請求項1之複合材料,其中該複合材料包括包含經硫 (B)填充之碳(C)之顆粒或域。 3. 如請求項1或2之複合材料,其中有機聚合物係選自聚 乙烯、聚丙烯、聚丙烯腈、聚丁二烯、聚苯乙烯及至少 兩種選自乙烯、丙烯、笨乙烯、丙烯腈及丨,3-丁二烯之 共聚單體之共聚物。 4. 如請求項1之複合材料,其中有機聚合物(A)係選自聚丙 稀腈。 5. 如請求項4之複合材料’其中聚丙烯腈(A)係在反應後至 少部分以式I環化產物之形式存在201251187 VII. Patent Application Range: 1 · A composite material comprising the reaction products of the following components: (A) at least one organic polymer, (B) sulfur, (C) including at least 60. /〇 sp2 - a polymorphic carbon of a mixed carbon atom, and (D) 2 to 20% by weight of a perfluorinated or partially fluorinated polymerization based on the total amount of the component used before the reaction, (B) and the total weight thereof Things. 2. The composite of claim 1 wherein the composite comprises particles or domains comprising sulfur (B) filled carbon (C). 3. The composite material of claim 1 or 2, wherein the organic polymer is selected from the group consisting of polyethylene, polypropylene, polyacrylonitrile, polybutadiene, polystyrene, and at least two selected from the group consisting of ethylene, propylene, and stupid ethylene. Copolymer of acrylonitrile and ruthenium, a comonomer of 3-butadiene. 4. The composite of claim 1 wherein the organic polymer (A) is selected from the group consisting of polyacrylonitrile. 5. The composite material of claim 4 wherein polyacrylonitrile (A) is present in the form of at least a portion of the cyclized product of formula I after the reaction 6·如請求項4或5之複合材料,其中聚丙烯腈(A)在反應前具 有在50 〇〇〇至250 000 g/mol範圍内之平均分子量mw。 7.如請求項i、2、4及5中任一項之複合材料,其中碳(C)係 選自碳黑。 164545.doc 201251187 8. 9. 10, 11. 12. 13. 士 :求項1、2、4及5令任一項之複合材 化或部分氣化聚合物⑼為聚四氣乙稀。、中該全說 一種電池,其包括至少— 中任個製備自或使用如請求項1至8 中任項之複合材料之電極。 .如請求項9之電池,其進—牛 之電極。 步包括至少一個包括金屬鋰 如請求項9或1〇之電池’其包括至少-種選自聚合物、 環越或非環_、非環狀或環狀縮裕及環狀或非環狀有機 碳酸酯之非水性溶劑。 一種製備複合材料之方法,其包括至少-個製程步驟, 其中使 (A) 至少一種有機聚合物, (B) 硫, (C) 包括至少60% sp2·混成化碳原子之呈多形體之碳,及 (D) 基於所使用組份(A)、(B)及(c)之總重量計,2至μ重 量%之全氟化或部分氟化聚合物 在150至400eC範圍内之溫度下相互反應。 一種製備如請求項丨至8中任一項之複合材料之方法,其 包括至少一個製程步驟,其中使 (A) 至少一種有機聚合物, (B) 硫, (C) 包括至少60%邛2_混成化碳原子之呈多形體之碳,及 (D) 基於所使用組份(A) ' (B)及(c)之總重量計,2至2〇重 量%之全氟化或部分氟化聚合物 164545.doc S -2- 201251187 14. 飛機、船 在150至400°C範圍内之溫度下相互反應。 一種如請求項9至11中任一項之電池於汽車 隻或靜態能量儲存中之用途。 I64545.doc6. The composite of claim 4 or 5, wherein the polyacrylonitrile (A) has an average molecular weight mw in the range of from 50 Å to 250 000 g/mol before the reaction. The composite of any one of the claims i, 2, 4 and 5, wherein the carbon (C) is selected from the group consisting of carbon black. 164545.doc 201251187 8. 9. 10, 11. 12. 13. Division: The composite or partially gasified polymer (9) of any of items 1, 2, 4 and 5 is polytetraethylene. And a battery comprising at least one of the electrodes prepared or used in the composite material of any one of claims 1 to 8. The battery of claim 9, which is the electrode of the cow. The step comprises at least one battery comprising metal lithium as claimed in claim 9 or 1 'which comprises at least one selected from the group consisting of polymers, cyclo- or acyclic, acyclic or cyclical and cyclic or acyclic organic A non-aqueous solvent for carbonates. A method of preparing a composite material comprising at least one process step, wherein (A) at least one organic polymer, (B) sulfur, (C) comprises at least 60% sp2·mixed carbon atoms in a polymorphic carbon And (D) 2 to μ% by weight of the perfluorinated or partially fluorinated polymer at a temperature in the range of 150 to 400 eC, based on the total weight of the components (A), (B) and (c) used. React with each other. A method of preparing a composite material according to any one of the preceding claims, comprising at least one process step, wherein (A) at least one organic polymer, (B) sulfur, (C) comprises at least 60% 邛2 _ a carbon of a polymorphic carbon of a mixed carbon atom, and (D) a total of 2 to 2% by weight of perfluorinated or partially fluorine based on the total weight of the components (A)' (B) and (c) used Polymer 164545.doc S -2- 201251187 14. Aircraft and ships react with each other at temperatures ranging from 150 to 400 °C. A use of a battery according to any one of claims 9 to 11 for car or static energy storage. I64545.doc
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