TW581778B - Process for synthesis of silicone resin - Google Patents
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581778 A7581778 A7
本發明係-種水解一於每—石夕原 原子之氯彻員、以形物氧樹 :::乂三個氯 :括添加至少-種氮化三氣碎燒、四氣心有機:” 劑,-:二:::兩相混合物係包含-非極性溶 水合物、” J、百水相,及-選自燒基續酸 k基飧鉍炙鹼金屬鹽、芳基磺酸水合物及芳美# :::金屬鹽之表面活性化合物。先前技藝中已知: ^於水〈存在下會快速地轉,㈣成可縮合構成聚硬氧 醇類’進-步地’先前技藝中亦已知“錢含 二或多個自原子時,此二方法幾乎於同時進行,此快速之 水解作用與縮合作用之結果係產生具微乎其微實用價值之 不溶性膠。可參見例如美國專利第2,9〇1,46〇號。 業界已建議許多上述問題的解決之道,舉例而言, Boldebuck,supra描述利用一含四氫呋喃及水之水解媒介以 減緩膠化作用。美國專利第3,615,272號描述一種形成氫矽 倍半氧故树知之方法’其包括使一碎垸於烴溶劑之存在下 與硫酸及芳族烴反應,以水及硫酸清洗該反應混合物直至 呈中性為止,然後藉由溶劑之蒸發回收產物。 美國專利第5,〇1〇, 159號教示一種水解具有二或多個可水 解基團的氫化矽烷之方法,其包括形成一含有芳基磺酸水 合物之反應媒介,將矽烷添加至該反應媒介中,進行矽烷 之水解以形成聚酯,以及回收聚合物。Bank等人教示該含 有芳基磺酸水合物之反應媒介可藉由溶解一芳基磺酸水合 物於溶劑中而形成,或者可自使芳族烴與濃硫酸反應之較 -4- 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 裝 訂The present invention is a kind of chlorine that hydrolyzes one-per-Xiyuan atom, and forms oxygen tree :: 乂 Three chlorine: Including the addition of at least one kind of nitrogenous three-gas crushing and four-gas-core organic: " Agent,-: two ::: two-phase mixture system comprising-non-polar hydrate, "J, one hundred water phase, and-selected from the group consisting of alkanoic acid k-based bismuth alkali alkali metal salt, arylsulfonic acid hydrate和 芳 美 # ::: Surface active compounds of metal salts. It is known in the prior art: ^ In the presence of water, it will turn quickly, and it will be condensed to form polystearyl alcohols. "Progressively" It is also known in the prior art that "money contains two or more self-atoms, These two methods are carried out almost at the same time. The result of this rapid hydrolysis and condensation is to produce an insoluble gum with little practical value. See, for example, US Patent No. 2,091,46. The industry has suggested many of the above problems. The solution, for example, Boldebuck, supra describes the use of a hydrolysing medium containing tetrahydrofuran and water to slow gelation. U.S. Patent No. 3,615,272 describes a method of forming hydrogen silsesquioxane trees, which includes making a The mash is reacted with sulfuric acid and aromatic hydrocarbons in the presence of a hydrocarbon solvent, the reaction mixture is washed with water and sulfuric acid until it becomes neutral, and then the product is recovered by evaporation of the solvent. US Patent No. 5,010,159 Teach a method for hydrolyzing a hydrogenated silane having two or more hydrolyzable groups, comprising forming a reaction medium containing an arylsulfonic acid hydrate, and adding silane to the reaction medium Hydrolyze silanes to form polyesters and recover polymers. Bank et al. Teach that the reaction medium containing the arylsulfonic acid hydrate can be formed by dissolving an arylsulfonic acid hydrate in a solvent, or Comparison of the reaction between aromatic hydrocarbons and concentrated sulfuric acid -4- This paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) binding
581778 A7 B7 五、發明説明(2 ) 佳方式而產生。581778 A7 B7 V. Description of the invention (2) The best way to produce it.
Ezerets等人於SU( 11)1丨47723中教示一種在芳族烴溶劑 與水可互混洛劑之混合物中,使一具有2 · 9至3官能度之甲基 氯碎垸單獨水解、或與二有機二氯矽烷或有機三氯矽烷共 同水解之方法’該方法之特徵在於該水可互混溶劑包含醋 酸及濃鹽酸’並存在一水溶性陽離子界面活性劑,該水溶 性陽離子界面活性劑經描述係含6至20個碳原子之氯化氫 胺、四級胺鹽及質子化羧酸之鹽類。Ezerets et al., SU (11) 1, 47723 teach a method for hydrolyzing a methyl chloride fragment having a functionality of 2.9 to 3 in a mixture of an aromatic hydrocarbon solvent and a water-miscible lotion, or Method for co-hydrolysis with diorganodichlorosilane or organotrichlorosilane, the method is characterized in that the water-miscible solvent contains acetic acid and concentrated hydrochloric acid, and there is a water-soluble cationic surfactant, and the water-soluble cationic surfactant It is described as hydrogen chloride amines, quaternary amine salts and protonated carboxylic acid salts containing 6 to 20 carbon atoms.
Hacker等人於WO 98/47941中描述一種製備氫化矽氧烷 及有機氫化碎氧院樹脂之方法,該方法涉及使一麥燒單體 與一相轉移觸媒於一含非極性溶劑及極性溶劑的反應混合 物之存在下接觸之步驟,Hacker等人提及該相轉移觸媒係 四級銨鹽。Hacker et al., In WO 98/47941, describe a method for preparing hydrogenated siloxanes and organic hydrogenated oxyhydrogen resins. The method involves the use of a wheat-fired monomer and a phase transfer catalyst in a non-polar solvent and a polar solvent. The step of contacting in the presence of the reaction mixture, Hacker et al. Mentioned that the phase transfer catalyst is a quaternary ammonium salt.
Shkolnik等人於SU (1 1) 1666469中描述一種製備寡聚有 機水合物矽氧烷之方法,其包括於二乙埽苯及苯乙稀之續 酸化共聚物之存在下,進行戊基三氯矽烷或乙烯基三氯發 Ί 一甲基一氯珍燒及六甲基二氯碎燒之混合物之酸性水 解作用。 亦已知非離子性活性劑可影響二有機氯矽烷之水解作 用,舉例而言,Williams於美國專利第4,412,080號中教示環 狀二甲基聚矽氧烷可以下列方式製備:於正烷基續酸 <存在下,進行二甲基二氯矽烷及鹽酸水溶液水解作用, 而獲得良好產率之環狀聚矽氧烷。 本發明係關於一種以高產率製造可快速溶於非極性溶劑 -5- 本紙張尺度適用中g g家標準(cns) A视格⑽心7公董) 3 五、發明説明( 用石^夕乳樹月曰《万法’該方法具有以下優點··⑴不需使 手:中並⑺當溶劑與硫酸反應而形成芳基磺酸水合物時, 以作為反應物’因此使方法易於控制,(3) 二开1由混合物分離出之氯錢之水解作用的無水氣 ^式q化氫,此係可循環回方法中或 开 ::⑷該含氯化氯及表面活化劑之水層可直接循環回= 由本發明方法製得之樹脂相當獨特 ::一含量:之既定單體分布,相對於由其他程序=; …’其顯得比較易於進行分子外環化作用 对 明方法製得的熟化樹脂之薄膜對於 = 壓力裂解具有高抗力》 〈 由本發明方法製得之聚合物於熟化至其陶資態或類陶是 2,具有優艮之塗覆性及封緘特性。此等聚合物於例如 塗覆電子裝置以形成保護性障蔽方面具有實用性。 β本發明提供-種水解一於每一梦原子上鍵結了至少三個 氯原子之氯錢類、以形成聚碎氧樹脂之方法,該方法包 括添加至少-種氫化三氯钱、四氯㈣或有機三氯碎垸 於-兩相混合物中,該兩相混合物係包含—非極性溶劑, 一含0至43重量百分比鹽酸之水相,及一表為式r2s〇3H之表 面活性化合物及其驗金屬鹽類’其中,r2係具有仙個碳 原子之垸基及具有7至22個碳原子之烷苯基。 ,本發明之製備聚矽氧樹脂之方法,包括添加至少一種表 為式心们“⑴之氯我兩相混合物中,該兩相混合 581778 A7 —____ B7 五、發明説明(4 ) 物係包含一非極性溶劑,一含〇至43重量百分比鹽酸之水 相’及一表為式R2S〇sH之表面活性化合物及其鹼金屬鹽 頒,其中,R係氫或單價烴自由基。R2係具有4至16個碳原 子之烷基或具有7至22個碳原子之烷苯基,且。 本發明方法添加之氯矽烷可為氫化三氯矽烷、四氯矽 烷,有機三氯矽烷彼等之混合物。於式(1)中,…可為氫或 單k fe基自由基,舉例說明為:燒基,例如甲基、乙基、 丙基、辛基、十二烷基及十八烷基;環烷基,例如環戊基 或環己基;環烯基,例如環戊烯基或環己烯基;芳基,例 如苯基、曱苯基及奈基;烯基,例如乙缔基、烯丙基及戊 缔基;芳烷基,例如苄基及甲苯基丙基;及經取代烴基自 由基例如鼠甲基、3,3,3 -二氟丙基及五氟丙基。較佳係當 R1為氫及含1至20個碳原子之烴基自由基。較佳用於本發明 方法中之氯矽烷係三氯矽烷及甲基三氯矽烷。 表為式(1)之氣碎燒可單獨水解,或以二或多種混合物之 形式水解,另外,其可與表為SRl2SlCU之二有機二i矽烷 共同水解,其中R1係如上所定義。 琢氯矽烷類係以液體形式使用,此液體可含液態之氯矽 烷,或者包含與非極性有機溶劑混合成溶液形式之氯矽 烷。若使用溶劑,該溶劑可為任何可作為氯矽烷之溶劑的 非極性烴類或水不溶性氯化碳,此等溶劑之例子為飽和脂 族,例如十二烷、正-戊烷、正-己烷、正_庚烷及異辛烷丨曰 芳族,例如苯、甲苯及二甲苯;環狀脂族,例如環己烷; 鹵化脂族,例如三氯乙烯、過氯乙烯及3_氣丙烷;以及鹵 A7 ---__B7 五、發明説明(5~J 一~--*- :匕了族,例如溴化苯及氯化苯。此外,上述溶劑之組合亦 可用以作為氯矽烷之共溶劑。較佳之非極性有機溶劑 係芳族化合物,於此類化合物之中,甲苯係最佳者。 為獲得本發明方法之良好產物產率,氯㈣較佳係以之 彳極性1機溶劑稀釋,而〒苯係最佳之溶劑。於加入本發 明万法前所進行的氯矽烷於非極性有機溶劑中之稀釋作 用、;7可賦丁氯矽烷於兩相混合物中之較佳分散度,因此減 = <之形成並改善了產率。該氯矽烷可包含1〇至重量百 分比之氯矽烷及非極性有機溶劑混合物,較佳地,該 $可包含20至60重量百分比之氯㈣及非極性有機溶劑混 合物。 广氯矽烷可以任何技藝中已知用以水解此等氯矽烷類之 標準方法添加於本發明方法中,然而,為使產率達最大化, f佳係將氯魏以可確保氯錢會於兩相混合物中快速分 万式添加’此等方式可包括於劇烈攪拌下、緩慢添加 氯矽烷於位於液體混合物下方之流體中。 於一較佳万法中,該非極性有機溶劑中之氯矽烷係經添 加至-快速授拌的、含有一非極性溶劑、一鹽酸水溶液及 一表面活性化合物之兩相混合物中。該用語「兩相」混合 物〜、冲曰-含有有機相及水相之混合物,該兩相混合物之非 極性有機溶劑相可為任何如上所述用以稀釋氯矽烷之非極 性有機溶劑,且可與於加入本發明方法前用以稀釋氯矽烷 〈任何非極性有機溶劑相同或者不同,較佳係該兩相混合 物中 < 非極性有機溶劑成分與用以稀釋氣矽烷之任何溶劑 -8 -Shkolnik et al. In SU (1 1) 1666469 describe a method for the preparation of oligomeric organic hydrates, siloxane, which includes the pentyl trichloride in the presence of diethylstilbene and styrene-acrylic acidification copolymers. Acidic hydrolysis of a mixture of silane or vinyltrichlorohydrin monomethyl-chlorochlorine and hexamethyldichlorobenzene. It is also known that non-ionic active agents can affect the hydrolysis of diorganochlorosilanes. For example, Williams taught in US Patent No. 4,412,080 that cyclic dimethylpolysiloxanes can be prepared in the following manner: Hydrolysis of dimethyldichlorosilane and hydrochloric acid aqueous solution in the presence of a carboxylic acid <, to obtain a cyclic polysiloxane with good yield. The present invention relates to a method for producing high-yield soluble non-polar solvents in a high yield. This paper is applicable to Chinese standards (cns) A 视 格 ⑽ 心 7 公 董) 3 V. Description of the invention Shuyue said "Wanfa" This method has the following advantages: · No need to use hands: neutralization when the solvent reacts with sulfuric acid to form an arylsulfonic acid hydrate as a reactant 'so the method is easy to control, ( 3) Anhydrous gas of hydrolyzation of chloroform separated from the mixture by ^ 1, q-type hydrogen hydride, which can be recycled back to the method or open :: ⑷The water layer containing chlorine chloride and surfactant can be directly Recycling = The resin prepared by the method of the present invention is quite unique: a content: the predetermined monomer distribution, compared to other procedures =; ... 'it appears to be easier to carry out the out-molecular cyclization of the mature resin prepared by the Ming method The film has high resistance to = pressure cracking. «The polymer prepared by the method of the present invention is cured to its ceramic state or ceramic-like state 2, and has coating properties and sealing properties. These polymers are used for example in coating Cover electronics to form a protective barrier It has practicality. Β The present invention provides a method for hydrolyzing chlorins with at least three chlorine atoms bonded to each dream atom to form a polyoxygen resin, which method comprises adding at least one hydrogenated trichloride Dichloromethane, tetrachloromethane, or organic trichloromethane in a two-phase mixture comprising a non-polar solvent, an aqueous phase containing 0 to 43 weight percent hydrochloric acid, and a table of formula r2s〇3H Surface-active compounds and metal detection salts thereof, in which r2 is a fluorenyl group having 3 carbon atoms and an alkylphenyl group having 7 to 22 carbon atoms. The method for preparing a polysiloxane resin according to the present invention includes adding at least A table is the formula "In the two-phase mixture of chlorine and chlorine, the two phases are mixed 581778 A7 —____ B7 V. Description of the invention (4) The system contains a non-polar solvent, a water containing 0 to 43 weight percent hydrochloric acid Phase 'and a table are surface-active compounds of formula R2S0sH and their alkali metal salts. Among them, R is hydrogen or a monovalent hydrocarbon radical. R2 is an alkyl group having 4 to 16 carbon atoms or 7 to 22 carbon atoms. Alkyl phenyl of carbon atom, and Chlorosilane can be a mixture of hydrogenated trichlorosilane, tetrachlorosilane, and organic trichlorosilane. In formula (1), ... can be hydrogen or a single k-fe radical, which is exemplified by an alkyl group such as methyl Alkyl, ethyl, propyl, octyl, dodecyl and octadecyl; cycloalkyl, such as cyclopentyl or cyclohexyl; cycloalkenyl, such as cyclopentenyl or cyclohexenyl; aryl , Such as phenyl, fluorenyl, and naphthyl; alkenyl, such as ethylenyl, allyl, and pentenyl; aralkyl, such as benzyl, and tolylpropyl; and substituted hydrocarbyl radicals such as murine Radical, 3,3,3-difluoropropyl and pentafluoropropyl. It is preferred when R1 is hydrogen and a hydrocarbyl radical containing 1 to 20 carbon atoms. Chlorosilane is preferred for use in the method of the present invention. Trichlorosilane and methyltrichlorosilane. The gas pulverization shown in the formula (1) can be hydrolyzed alone or in the form of two or more mixtures. In addition, it can be hydrolyzed together with the two organic disilanes shown in SR12SCU, where R1 is as defined above. Chlorosilanes are used in liquid form. This liquid can contain chlorosilanes in liquid form, or chlorosilanes mixed with a non-polar organic solvent to form a solution. If a solvent is used, the solvent may be any non-polar hydrocarbon or water-insoluble carbon chloride that can be used as a solvent for chlorosilanes. Examples of such solvents are saturated aliphatics such as dodecane, n-pentane, n-hexane Alkane, n-heptane and isooctane are aromatic, such as benzene, toluene and xylene; cyclic aliphatics, such as cyclohexane; halogenated aliphatics, such as trichloroethylene, perchloroethylene, and 3-propane ; And halogen A7 ---__ B7 V. Description of the invention (5 ~ J 一 ~-*-: Drake family, such as brominated benzene and chlorinated benzene. In addition, the combination of the above solvents can also be used as a co-chlorosilane Solvents. Preferred non-polar organic solvents are aromatic compounds. Among these compounds, toluene is the best. To obtain good product yields from the process of the present invention, chlorophosphonium is preferably diluted with polar organic solvents. Benzene is the best solvent. Dilution of chlorosilane in a non-polar organic solvent before adding the present invention; 7 can give a better dispersion of chlorochlorosilane in a two-phase mixture, Thus minus formation of < and improved yields. The chlorosilanes may contain 10 to The amount of chlorosilane and non-polar organic solvent mixture, preferably, the $ may include 20 to 60 weight percent of chlorophosphonium and non-polar organic solvent mixture. The perchlorosilane can be used in any technique to hydrolyze these chlorines. Standard methods of silanes are added to the method of the present invention. However, in order to maximize the yield, the f-family will add chloroweiline to ensure that the chlorine will be quickly added to the two-phase mixture. `` These methods can include Chlorosilane is slowly added to the fluid below the liquid mixture under vigorous stirring. In a preferred method, the chlorosilane in the non-polar organic solvent is added to-rapid mixing, contains a non-polar solvent, A two-phase mixture of an aqueous solution of hydrochloric acid and a surface-active compound. The term "two-phase" mixture ~, a mixture containing an organic phase and an aqueous phase. The non-polar organic solvent phase of the two-phase mixture can be any of the above. The non-polar organic solvents used to dilute chlorosilanes can be the same as those used to dilute chlorosilanes before adding the method of the present invention (any non-polar organic solvents or Different, preferably the two-phase mixture < non-polar organic solvent component and any solvent used to dilute the gas silane -8-
五Fives
發明説明(6 係屬相同,而甲! T冬係較佳之溶劑。Description of the invention (6 series belong to the same, and A! T winter series is a better solvent.
含〇至43重V 4ρτ , 为比鹽酸之水相係兩相混合物之第二 相,相對於矽鍵蛀奢馬2 ^ .^ 遷〜氣原子而言,其應具有至少化學計量之 7又佳,為化學過量。通常,範圍介於30至100莫耳百分 迻量欠量係較佳者,而過量水量之範圍介於250至 8 0 0莫耳百分比間目丨|拉 、 4係取佳者。水相中係含〇至43重量百分 比之鹽酸,輕估Μ , 、 地,水相中係含15至37重量百分比之鹽酸。 、^發^方法之優點係該因水解反應所形成之氯化氮,於 、氯化氫飽和水相時,可以無水氯化氫氣體形式釋放出 來因此,較佳係該水相中含至少約35重量%之氯化氫,該 釋放之氯化氫可以氣體形式回收,並循環回該方法中或使 用方、其他應用巾。水相中存在之氯化氫可以—各別水溶液 之形式加入該方法中,或藉由氯矽烷之水解作用於原處產 生。 本發明万法中需要存在一表為式R2s〇3H<表面活性化合 物及其鹼金屬鹽類,其中,R2係具有4至丨6個碳原子之烷基 及具有7 土 22個故原子之燒苯基,較佳係r2所表之燒基為具 有6至12個碳原子者、而R2所表之烷苯基為具有9至18個碳 原子者。該表面活性化合物可為,例如,且戎ΓContains 0 to 43 V 4ρτ, which is the second phase of the two-phase mixture of the aqueous phase than hydrochloric acid. It should have at least 7 Preferably, it is a chemical excess. In general, the range between 30 and 100 mole percentages is better, while the amount of excess water is between 250 and 800 mole percentages. Pull, 4 is the better. The aqueous phase contains 0 to 43% by weight of hydrochloric acid, and the light phase M,, and ground are considered. The aqueous phase contains 15 to 37% by weight of hydrochloric acid. The advantage of the method is that the nitrogen chloride formed by the hydrolysis reaction can be released in the form of anhydrous hydrogen chloride gas when the aqueous phase is saturated with hydrogen chloride. Therefore, it is preferable that the aqueous phase contains at least about 35% by weight Hydrogen chloride, the released hydrogen chloride can be recovered in the form of gas and recycled back to the method or the user or other application towels. The hydrogen chloride present in the water phase can be added to the process as a separate aqueous solution or produced in situ by hydrolysis of chlorosilane. In the method of the present invention, it is necessary to have a formula of the formula R2s03H < surface-active compounds and alkali metal salts thereof, in which R2 is an alkyl group having 4 to 6 carbon atoms and 7 to 22 carbon atoms. The phenyl group is preferably one having 6 to 12 carbon atoms, and the alkylphenyl group having R2 is 9 to 18 carbon atoms. The surface-active compound may be, for example, and
八 a Lnn(2n+”b(j3H 之燒基磺酸水合物,其中η為4至16,該烷基磺酸水合物可 為’例如,C4H9S03H、C6H13S03H、C8H17S03H、Cl〇H2lS〇3H、 。該表面活性化合物可為該燒美 續酸水合物之相關驗金屬鹽,其中該驗金屬可為,例如, 钟或鈉。該烷基磺酸水合物之鹼金屬鹽可為,例如, -9- 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) " -------- 581778 A7 B7 五、發明説明(7 ) C6HuS〇3 Na 、C8H17S03'Na+ 、C1()H21SCVNa+、 C12H25S〇3-Na+、C16H33S〇3-Na+及 C8H17S03-K+。該表面活性 化合物可為芳基橫酸水合物及其相關之驗金屬鹽,例如, 苯續酸水合物與甲苯磺酸水合物之鉀鹽。用於本發明方法 中之較佳表面活性化合物係選自正-辛烷磺酸水合物、對_ 甲苯%酸水合物、苯績酸水合物、乙燒橫酸水合物、正丁 烷磺酸水合物及正-十二烷磺酸鈉。 兩相混合物的水相中之表面活性化合物濃度,基於方法 中添加之水重,可為介於⑺丨及㈧重量百分比間之範圍,通 常,較佳地,該表面活性化合物之濃度係含〇 5至2重量百分 比的添加於該方法中之水。 本發明方法可進行之溫度係不限於、但可介於〇艺至1〇〇 °c間之範圍内,介於1(rc至3(rc間之溫度範圍係較佳者。 於本發明方法中,若需要,樹脂的矽原子上之殘餘羥基 可與一有機矽烷末端加蓋劑反應,例如,表為式hSici者1 其中R係如先前描述之單價烴基,較佳係該末端加蓋 烷基氯矽烷,甚至更佳係該末端加蓋劑為三甲基氯矽烷。 待本發明方法之水解反應完全、且形成聚矽氧樹脂後, 該兩相混合物可藉由例如沈降方法分離”匕方法可藉由例 如直接停止水解混合物之攪拌、然後進行反應器中不互混 各層之同步分離而達成。所形成之層係含有聚矽氧樹脂與 溶劑之有機層’以及含氯化氫及表面活性化合物之水層。 於此刀離步驟 < 前、期間或者之後,可使有機層靜置一 段時間,以提供樹脂中碎原子上之氯原子與殘餘的石夕原子 -10-Eight a Lnn (2n + "b (j3H) alkylsulfonic acid hydrate, wherein η is 4 to 16, the alkylsulfonic acid hydrate may be 'for example, C4H9S03H, C6H13S03H, C8H17S03H, C0H2lSO3H,. The The surface-active compound may be a relevant metal test salt of the burnt acid hydrate, wherein the metal test may be, for example, bell or sodium. The alkali metal salt of the alkylsulfonic acid hydrate may be, for example, -9- This paper size applies to China National Standard (CNS) A4 specification (210 X 297 mm) " -------- 581778 A7 B7 V. Description of the invention (7) C6HuS〇3 Na, C8H17S03'Na +, C1 ( ) H21SCVNa +, C12H25S〇3-Na +, C16H33S〇3-Na + and C8H17S03-K +. The surface-active compound may be an aryl transverse acid hydrate and its related metal test salt, for example, benzoic acid hydrate and toluenesulfonic acid Potassium salt of hydrate. The preferred surface-active compound used in the method of the present invention is selected from the group consisting of n-octane sulfonic acid hydrate, p-toluene% acid hydrate, benzoic acid hydrate, and ethanoic acid hydrate , N-butanesulfonic acid hydrate and sodium n-dodecanesulfonate. Surface active compounds in the water phase of a two-phase mixture Concentration, based on the weight of water added in the method, can be in the range between ⑺ 丨 and ㈧ weight percent. Generally, preferably, the concentration of the surface-active compound is added to the method by 0.05 to 2 weight percent. The temperature at which the method of the present invention can be performed is not limited, but may be in the range of 0 ° to 100 ° C, and the temperature range of 1 (rc to 3 (rc) is the better. In the method of the present invention, if necessary, the residual hydroxyl groups on the silicon atom of the resin can be reacted with an organic silane terminal capping agent. For example, the formula is represented by the formula hSici1 where R is a monovalent hydrocarbon group as described previously, preferably the terminal The alkyl chlorosilane is capped, and even more preferably, the terminal capping agent is trimethylchlorosilane. After the hydrolysis reaction of the method of the present invention is completed and a polysiloxane resin is formed, the two-phase mixture may be subjected to, for example, a sedimentation method. The "separation" method can be achieved by, for example, directly stopping the stirring of the hydrolysis mixture and then performing simultaneous separation of the non-mixing layers in the reactor. The formed layer is an organic layer containing a polysiloxane resin and a solvent, and hydrogen chloride and The aqueous layer of this blade surface active compound from step < before, during, or after, the organic layer was allowed to stand allows a period of time, to provide a resin with a stone Xi residual chlorine atom on the broken atom -10-
581778 A7 B7 五、發明説明(8 ) 鍵結之羥基間之進一步縮合反應,因此造成聚矽氧樹脂之 結構及/或分子量之增加。通常,若欲進行增稠作用,^ 較佳係使該增稠方法於兩相分離之前進行。為賦予本發明 方法製得之聚矽氧樹脂安定性,清洗方法併用或不併用中 和作用係有用的。若欲清洗有機層,僅可使用水,然較佳 係該清洗液係硫酸水溶液,通常,含大於5%硫酸之清洗液 係較有用者。該有機層、無論經清洗或未經清洗、皆可/ 一中和劑接觸,較佳係於水存在下進行,此可促進^餘 原子之水解。該中和劑應具足夠鹼性以中和任何殘餘酸 種,例如硫酸、鹽酸及有機酸,然不造成聚矽氧樹脂之 化性重排作用或硬鍵結的氫與水間之反應。適當的驗可巴 括例如碳酸躬、碳酸鋼、碳酸二納、碳酸按、氨水、氧^ 鈣及氫氧化鈣。較佳地,該中和劑係一固體,此可 機:之分離較為容易。以及,較佳地,在清洗及 反應之後,該有機相應予乾燥,若需要,應予㈣ 以移除任何水不溶性鹽類或者會 心 他不溶性沈殿物。任何適當之二二〜封脂性質之其 或八早〜… 田《乾级劑例如硫酸鎂、硫酸鈉 此外,水可藉由潍石蒸餘法移除。 自本發明方法製得之聚矽氧樹: 劑中之溶㈣式,或者,若需要q料為存在於反應 议甘a , 而要可藉由添加一第二玄 =咖第一溶劑而進行-簡單之溶液交換。或:, 精由以例如沸石蒸餾法等標 次者 式之聚矽氧樹脂。 /多除落劑而回收固體 可經自本發明方法製得之 /矽虱树脂係依所使用之氯 與 氯 物 催 包 和 溶 劑 可 形 矽 -11 - G張尺度—適用中 x 297公釐) 581778 A7 B7 五、發明説明(9 ) 燒而變化,然而,以下所列非以限定種類之可能性水解及 共水解係特別期待者:完全縮合及幾乎完全縮合之樹脂包 括,(HSi〇3/2)m,,(HSiO^^RiSiOwh, (HSiO^MR'SiC^y及(RiSiC^/^xCR'SiCOy ;相關的部分縮 合且含矽烷醇之樹脂係描述為式(HSi〇3/2)x(H(HO)SiO)y,式 (R1Si03/2)x(Rl(H0)Si0)y , 式 (HSi03/2)w(H(H0)Si0)x(R1Si03/2)y(R1(H0)Si0)z , 式 (HSi03/2)w(H(H0)Si0)x(R12Si0)y(R12(H0)Si0)z , 式 (RlSi03/2)w(Rl(H0)Si0)x(R12Si0)y(R12(H0)Si0)z , (RSSiO^KSiOOyiXHCOSiOs/dz ;相關的三有機矽烷基終端 樹脂係描述為式(R'SiOm^HSiOwh ,式 (R13Si01/2)x(RlSi03/2)y , 式 (R13Si01/2)x(HSi〇3/2)y(R1Si〇3/2)z , 式 (R13Si01/2)x(HSi03/2)y(R12Si0)z , 式 (R^SiOwAWsiOw^R^SiO),,式(RSsiOwWSiOJy,式 (R13Si0l/2)w(HSi03/2)x(R12Si0)y(Si02)2 , 及 式 (RSSiOwdJRisiOw^R'SiO^SiOdz;其中 Ri係如先前所 述’且各個R1可為相同或不同,m係8或更大,且上述聚合 物聚碎氧樹脂之莫耳分率w+x+y+z=l。 下列貫例係以例示本發明,然此等實例並非以限定本發 明中申請專利範圍所定義之範圍。 實例1 -1 6 於實例1中,於一配置攪摔器及加料漏斗之1升燒瓶中, 添加1 5 1.5克之35重量%HC卜50.5克之甲苯磺酸單水合物 -12- 本紙張尺度適用中國國家標卓(CNS) A4規格(21〇x 297公爱) —-- 581778 A7 B7 五、發明説明(1〇 及334克之甲笨,將一本 + 一 、、斑、、、 口 4S·3克三氯矽烷於55.6克甲苯中 i- ^ ^ v ^ ,:+中。万;攪拌下將三氯矽烷溶液以一 #又起過45为鐘之時間加 ,,^ m 41 , t 门入1开瓦中。添加完畢後,燒瓶内容 物係經攪掉另外之2小眭姑、μ ^ 時然後停止攪拌並將燒瓶内容物 分離為水相及有機相,古祕^ " 機相有機相係以2次1 〇 〇毫升份量之4 7 % S以25克固態碳酸鈣中和,並以50克硫酸鎂铲 燥並予過遽。自有機相中移除甲苯後,獲得ΐ7·5 : 固體’並提供一基於济加$惊、,ί; 士 产 色 土万、添加至燒开瓦中三氯矽烷總 百分比之產率。實例2 16 α,— 垔為%莫耳 改以表1中所列之試劑用量為之。 丁,然 表581778 A7 B7 V. Description of the invention (8) The further condensation reaction between the bonded hydroxyl groups results in an increase in the structure and / or molecular weight of the silicone resin. Generally, if thickening is desired, it is preferred that the thickening method be performed before the two phases are separated. In order to impart stability to the silicone resin prepared by the method of the present invention, it is useful to use a cleaning method with or without a neutralizing system. If the organic layer is to be cleaned, only water may be used, but the cleaning liquid is preferably a sulfuric acid aqueous solution. Generally, a cleaning liquid containing more than 5% sulfuric acid is more useful. The organic layer can be contacted with a neutralizer, whether cleaned or unwashed, preferably in the presence of water, which can promote the hydrolysis of the remaining atoms. The neutralizer should be sufficiently basic to neutralize any residual acids, such as sulfuric acid, hydrochloric acid, and organic acids, without causing the chemical rearrangement of the silicone resin or the reaction between hard-bonded hydrogen and water. Appropriate tests may include, for example, carbonic acid carbonate, carbonic acid steel, dicarbonate, sodium carbonate, ammonia, calcium hydroxide and calcium hydroxide. Preferably, the neutralizing agent is a solid, and this organic: the separation is relatively easy. And, preferably, after washing and reaction, the organic should be dried accordingly, if necessary, it should be dried to remove any water-insoluble salts or be aware of other insoluble sinks. Any suitable 22 ~ Fat sealing properties or eight early ~ ... Tian "Dry grade agents such as magnesium sulfate, sodium sulfate In addition, water can be removed by Weishi evaporation method. Polysilicone prepared from the method of the present invention: the dissolving formula in the agent, or if the q material is required to be present in the reaction solution a, it can be carried out by adding a second solvent -Simple solution exchange. Or: It is composed of a silicone resin in a standard method such as a zeolite distillation method. / Multiple solids can be recovered by the method of the present invention / Siliceous resin is based on the chlorine and chlorine catalysis and solvent tangible silicon-11-G-scale-applicable x 297 mm ) 581778 A7 B7 V. Description of the invention (9) It changes with firing, however, the following list is not specifically limited to the possibility of hydrolysis and co-hydrolysis are particularly expected: resins that are fully and almost completely condensed include, (HSi〇3 / 2) m ,, (HSiO ^^ RiSiOwh, (HSiO ^ MR'SiC ^ y and (RiSiC ^ / ^ xCR'SiCOy; related partial condensation and silanol-containing resins are described by the formula (HSi〇3 / 2 ) x (H (HO) SiO) y, formula (R1Si03 / 2) x (Rl (H0) Si0) y, formula (HSi03 / 2) w (H (H0) Si0) x (R1Si03 / 2) y (R1 (H0) Si0) z, formula (HSi03 / 2) w (H (H0) Si0) x (R12Si0) y (R12 (H0) Si0) z, formula (RlSi03 / 2) w (Rl (H0) Si0) x (R12Si0) y (R12 (H0) Si0) z, (RSSiO ^ KSiOOyiXHCOSiOs / dz; the related triorganosilyl terminal resin system is described as formula (R'SiOm ^ HSiOwh, formula (R13Si01 / 2) x (RlSi03 / 2 ) y, formula (R13Si01 / 2) x (HSi〇3 / 2) y (R1Si〇3 / 2) z, formula (R13Si01 / 2) x (HSi03 / 2) y (R12Si0) z, formula (R ^ SiOwAWsiOw ^ R ^ SiO) ,, (RSsiOwW SiOJy, the formula (R13Si0l / 2) w (HSi03 / 2) x (R12Si0) y (Si02) 2, and the formula (RSSiOwdJRisiOw ^ R'SiO ^ SiOdz; where Ri is as previously described, and each R1 may be the same or Different, m is 8 or more, and the Mohr fraction w + x + y + z = l of the above polymer polyoxygenated resin. The following examples are intended to illustrate the present invention, but these examples are not intended to limit the present invention. The range defined by the scope of patent application in China. Example 1 -1 In Example 1, in a 1 liter flask equipped with a stirrer and an addition funnel, add 15 1.5 g of 35% by weight HC and 50.5 g of toluenesulfonic acid single Hydrate-12- This paper size is in accordance with China National Standards (CNS) A4 specifications (21 × 297 public love) --- 581778 A7 B7 V. Description of the invention (10 and 334 grams of Jiaben, one + one 3, 3 g of trichlorosilane in 55.6 g of toluene, i-^^ v ^, + :. Under stirring, the trichlorosilane solution was added at a time of 45 minutes for 1 minute, and ^ m 41, t door into 1 watt. After the addition is complete, the contents of the flask are agitated to remove the other two babies. When μ ^ is stopped, the stirring is stopped and the contents of the flask are separated into an aqueous phase and an organic phase. A 47% S in 100 ml portion was neutralized with 25 g of solid calcium carbonate, dried with 50 g of magnesium sulfate, and pre-treated. After the toluene was removed from the organic phase, 7.5: solid was obtained and a yield based on the total amount of trichlorosilane added to the boiled tile was provided. Example 2 16 α, — 垔 is% mole. Change the amount of reagents listed in Table 1 to it. Ding, Ran table
-13 - 展千只例2-16以類似於實例i之方式 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 581778 五 發明說明(-13-Show thousands of examples 2-16 in a similar way to example i This paper size applies the Chinese National Standard (CNS) A4 (210 X 297 mm) 581778 5 Description of the invention (
11 1 ~— H2.5 ------- 37.5 ---- 50.1 33 3.6 47.4 50 2 80.5 12 37^5 J13 50.2 332.2 50.2 50 2 5.6 13 37^5 0 12.5 333.4 48 50 2 69.2 14 —--—^ !S.8 0 6.3_ 333.5 48.3 50 2 46.5 15 '----- 15^3 0 50 83 47.9 50 2 59 16 150 〇 0 50 42 50.5 50 2 33 ---- 、人人 ^1117^33 万;貫例17 tb 、人 ^ , 中’於一配置攪拌器及加料漏斗之1升燒瓶 中’添力口 19Q古+ 1C ‘ 克之甲# 見心35重量%1*1(:1' 1.0克之辛基磺酸鈉及333 入核加將—含47·3克三氯矽烷於55克甲苯中之溶液置 分鐘之Γ漏斗中。於攪拌下將三氯矽烷溶液以一段超過5〇 掉另外、寺間加入燒瓶中。添加完畢後,燒瓶内容物係經攪 相;5古2 2小時,然後停止攪拌並將燒瓶内容物分離為水 自有機/相,有機相係以水清洗,以硫酸鎂乾燥並予過滤。 中移除甲苯後,獲得16.3克之白色固體,並提供 率。實:力:土燒瓶中三氯矽烷總重為87.9莫耳百分比之產 貫Η 1 8 - 3 6以上述之類似方★ ^ ^ 痛似万式進行,然改以表2中所 列之武劑用量為之。 π τ , -14- 581778 A7 B7 五、發明説明(12 ) 表2 初始反應器進料 添加至反應器之進料 實例 界面活性劑 溶劑 HCla 溶劑 界面活性劑 HSi03 溶劑 產率 (克) (克) (克) (克) (克) % 18 無 PhMec 200 334 0 47.1 55.7 10 19 BSAb PhMe 196 334 4 47.1 55.7 38 20 BSA 辛烷 151 271 50.5 46.9 45.1 22 21 BSA 2-ClPrd 150 333 50 59.8 55.0 51 22 C2H5SO3H PhMe 196 333 4 50.4 55.6 16 23 C2H5S〇3H PhMe 180 334 20 48.9 55.5 35 24 c2h5so3h PhMe 150 333 50 49.4 55.5 63 25 C4H9SO3H PhMe 196 333 4 49.1 55.5 42 26 c4h9so3h PhMe 190 333 10 50 55.5 43 27 c6h13so3h PhMe 196 333 4 48.4 55.4 89 28 c6h13so3h PhMe 199 334 1 49 55.5 56 29 C8H17S03Na PhMe 200 333 0.25 49.3 55.5 81.2 30 C8H17S〇3Na PhMe 199 333 1 47.3 55.5 87.9 31 C8Hl7S03Na PhMe 196 334 4 50.2 55.7 48 32 C8H17S03Na 辛烷 196 270 4 48.2 45.0 65 33 C8H17S〇3Na PhMe 180 334 20 48.3 55.5 29 a = 35重量%之HC1水溶液 c =甲苯 b =苯續酸水合物 d=2 -氯丙燒 -15- 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 58177811 1 ~-H2.5 ------- 37.5 ---- 50.1 33 3.6 47.4 50 2 80.5 12 37 ^ 5 J13 50.2 332.2 50.2 50 2 5.6 13 37 ^ 5 0 12.5 333.4 48 50 2 69.2 14 — --- ^! S. 8 0 6.3_ 333.5 48.3 50 2 46.5 15 '----- 15 ^ 3 0 50 83 47.9 50 2 59 16 150 〇 0 50 42 50.5 50 2 33 ----, everyone ^ 1117 ^ 330,000; Example 17 tb, person ^, in the 'in a 1 liter flask equipped with a stirrer and an addition funnel' Tianlikou 19Qgu + 1C '克 之 甲 # see heart 35 wt% 1 * 1 ( : 1 '1.0 grams of sodium octyl sulfonate and 333 are added to the core. A solution containing 47.3 grams of trichlorosilane in 55 grams of toluene is placed in a Γ funnel for one minute. The trichlorosilane solution is added for more than one stage with stirring. Add 50% to the flask and add to the flask. After the addition is complete, the contents of the flask are stirred; for 5 hours and 2 hours, then stop stirring and separate the contents of the flask into water from the organic phase. The organic phase is water. Washed, dried with magnesium sulfate and filtered. After removing toluene from it, 16.3 g of a white solid was obtained, and the yield was provided. Strength: The total weight of trichlorosilane in the soil flask was 87.9 mole percent. 1 8- 3 6 or more The similar formula described above is ^ ^ The pain is similar, but the amount of military agent listed in Table 2 is used instead. Π τ, -14- 581778 A7 B7 V. Description of the invention (12) Table 2 Examples of feeds added to the reactor Surfactant solvent HCla Solvent surfactant HSi03 Solvent yield (g) (g) (g) (g) (g)% 18 PhMec 200 334 0 47.1 55.7 10 19 BSAb PhMe 196 334 4 47.1 55.7 38 20 BSA octane 151 271 50.5 46.9 45.1 22 21 BSA 2-ClPrd 150 333 50 59.8 55.0 51 22 C2H5SO3H PhMe 196 333 4 50.4 55.6 16 23 C2H5S〇3H PhMe 180 334 20 48.9 55.5 35 24 c2h5so3h PhMe 150 333 50 49.4 55.5 63 25 C4H9SO3H PhMe 196 333 4 49.1 55.5 42 26 c4h9so3h PhMe 190 333 10 50 55.5 43 27 c6h13so3h PhMe 196 333 4 48.4 55.4 89 28 c6h13so3h PhMe 199 334 1 49 55.5 56 29 C8H17S03Na0.25 MeMe 81.2 30 C8H17S〇3Na PhMe 199 333 1 47.3 55.5 87.9 31 C8Hl7S03Na PhMe 196 334 4 50.2 55.7 48 32 C8H17S03Na Octane 196 270 4 48.2 45.0 65 33 C8H17S〇3Na PhMe 180 334 20 48.3 55.5 29 a = 35 wt% HC1 aqueous solution c = toluene b = benzoic acid hydrate d = 2-chloropropane -15- This paper size is applicable to China National Standard (CNS) A4 (210X297 mm) 581778
f 例 37-3Qf Example 37-3Q
裝 於貫例37中,於一配置攪拌器及加料漏斗之1升燒瓶 中添加50·〇克之苯磺酸水合物、15〇克之35重量%HC1 及3 33.6克之甲苯,於6〇〇 rpm之速度下、於攪拌中,將一 含50.5克甲基三氯矽烷於55·5克甲苯中之溶液以一段超過 65分鐘之時間加入此混合物中。添加完畢後,燒瓶内容物 係經授拌另外纟2小時,然後停止料並將燒瓶内容物分 離為水相及有機相,有機相係以2次丨〇〇毫升份量之47% 硫酸清洗,以25克固態碳酸鈣中和,並以5〇克硫酸鎂乾 燥並予過濾。自有機相中移除甲苯後,獲得16 5克之白色 固體,並提供一基於添加至燒瓶中三氯矽烷總重為73 5莫 耳百分比之產率。實例38及39以類似之方式進行,然改 以表3中所列之試劑用量為之。 表3 初始反;S &器進料 添加至反應器之進料 ----- 實例 甲苯 HC1 h2o PhS03 甲苯 MgSiCl3 速率 產率 (克) (克) (克) Η (克) (克) (毫升/分) (%) (克) 38 333.6 75 75 50 55.5 50 2 39 333.2 0 150 50 55.2 50 2 \j ^ 44 會例40-47 — 甲基矽倍半氧烷係以下列方式獲得:將甲基三氯碎统於 甲苯中之溶液添加至一含有濃鹽酸(3 6重量%之水溶液)、甲 苯及辛基磺酸鈉之燒瓶中,其濃度係如表4中所示。甲基 訂Fill in Example 37. In a 1 liter flask equipped with a stirrer and an addition funnel, add 50,000 grams of benzenesulfonic acid hydrate, 150 grams of 35% by weight HC1, and 3 33.6 grams of toluene at 600 rpm. A solution containing 50.5 g of methyltrichlorosilane in 55.5 g of toluene was added to the mixture over a period of 65 minutes while stirring at a speed. After the addition was completed, the contents of the flask were mixed for another 2 hours, and then the material was stopped and the flask contents were separated into an aqueous phase and an organic phase. The organic phase was washed with 47% sulfuric acid twice in 1000 ml portions, and 25 grams of solid calcium carbonate was neutralized and dried over 50 grams of magnesium sulfate and filtered. After the toluene was removed from the organic phase, 165 grams of a white solid was obtained and a yield based on the total weight of trichlorosilane added to the flask was 735 mole percent. Examples 38 and 39 were performed in a similar manner, except that the amounts of reagents listed in Table 3 were changed. Table 3 Initial S & reactor feed added to reactor feed ----- Example Toluene HC1 h2o PhS03 Toluene MgSiCl3 Rate Yield (g) (g) (g)) (g) (g) (g) ( Ml / min) (%) (g) 38 333.6 75 75 50 55.5 50 2 39 333.2 0 150 50 55.2 50 2 \ j ^ 44 Session 40-47 — The methyl silsesquioxane system is obtained by: A solution of the methyl trichloride in toluene was added to a flask containing concentrated hydrochloric acid (36% by weight in water), toluene, and sodium octylsulfonate. The concentrations are shown in Table 4. Methyl
線 -16- 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 581778 五 發明説明(14 三氯矽燒之添加速率係藉山、、士 & $ , ^ ΤΜ , 精由/王射泵加以控制,而進料係通 過TeflonTM試管添加,此q^种係l 此忒管係隱藏於燒瓶中。於表中,Line-16- This paper size applies Chinese National Standard (CNS) A4 specification (210 X 297 mm) 581778 Five invention description (14 The addition rate of triclosan is based on borrowing, and & $, ^ ΤΜ, refined It is controlled by the / Kingjet pump, and the feed is added through a TeflonTM test tube. The q ^ germline l This tritium tube is hidden in the flask. In the table,
該標題「初始反應器進料,伤扣a、>丄 、| T 」係私取初添加於燒瓶中之物質The title "Initial reactor feed, injury button a, > 丄, | T" refers to the material added to the flask in private.
克數’該標題「進料重」係'指在所述速率下添加於反應器 中之曱苯及三氯矽烷混合物總重,該標題「反應編號」係 指進料物質添加完畢後,用以處理樣本之方法編號’該操 作方法係如下所列依序編為方法丨、2及3,該標題「產率 %」係指基於添加至燒瓶中之曱基三氯矽烷總重之產物產 率。 表4 初始反應器進料 添加至反應器 之進料 實例 曱苯 HC1 η2ο PhS03H 甲苯 MgSiCl3 速率 反應編號 產率 (克) (克) (克) (克) (克) (克) (毫升/分) (%) 40 330 199 0 1 55 51.9 2 1 86 41 330 199 0 1 55 51.9 2 2 99 42 330 199 0 1 155 51.9 1.8 2 100 43 330 199 0 1 155 51.9 1.8 2 100 44 333.8 199 0 1 55.5 50 1.8 3 」 100 45 333.5 199 0 1 55.5 50 1.8 3 97 46 333.5 99.5 99.5 1 55.5 50 1.8 3 86 47 333.5 0 199 1 55.5 50 1.8 3 61 反應編號1 -於進料添加完畢2小時後,取64克之有機 裝 訂 -17- 本紙張尺度適用中國國家標準(CNS) Α4規格(210 X 297公釐) 581778 A7 B7 五、發明説明( 15 ) 相樣本,以100毫升整之去離子士、、主、土 A 4 太雖于水清洗6次,以沸石蒗餾 法於55°c及真空下將樣本乾燥。 反應編號2 -於進料添加完畢後,將樣本41及42以下 列万式處理19小時’樣本19則於進料添加完畢後立即處 理。對於每一樣本,將有機相分離,然後添加丨當量之 MesSiCl至該有機相中,並使有機相於室溫下攪拌3小時。 然後取64克之有機相樣本,以下列步驟處理:(ι)2χ2⑻ 耄升之50重量%H2S〇4,1〇分鐘,(2)丨χ 2〇〇毫升之去離子 水,(3)1 X 200毫升之5重量%1^!^〇3溶液,及(4)2χ2〇〇 毫升之去離子水。所得之經清洗及經中和之有機相係以沸 石蒸餾法於55°C及真空下予以乾燥。 反應編號3 -將反應混合物倒入一分液漏斗中,並移除 酸層,將有機層置入一具有底部排放孔之三頸燒瓶中,然 後,添加100毫升47%硫酸,並攪拌混合物,所得之有機 層係以5%竣酸二鈉清洗3次,隨後以! 〇〇毫升之去離子水 清洗2次。然後以2 5克之碳酸鈣於攪拌下處理有機層工〇 分鐘,並添加硫酸鎂。有機層經過濾、並於真空下除去溶 劑後,產生為白色固體之樹脂。 如上所述之選定樣本使用29Si NMR及GPC、對照聚苯乙 缔標準品而進行分析,結果列於表5中。 於表5中,具有羥基取代度之矽原子之莫耳百分比係標 為「SiOH」’而具有氯取代度之碎原子之莫耳百分比則標 為「 SiCl」。 -18- 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐)Grams' The title "Feed Weight" refers to the total weight of the toluene and trichlorosilane mixture added to the reactor at the stated rate. The title "Reaction Number" refers to the amount of The number of the method for processing the sample is' The operation method is listed below as methods 丨, 2 and 3, and the title "Yield%" refers to the product yield based on the total weight of fluorenyltrichlorosilane added to the flask. rate. Table 4 Examples of initial reactor feeds added to the reactor Feed benzene HC1 η2ο PhS03H toluene MgSiCl3 Rate reaction number Yield (g) (g) (g) (g) (g) (g) (ml / min) (%) 40 330 199 0 1 55 51.9 2 1 86 41 330 199 0 1 55 51.9 2 2 99 42 330 199 0 1 155 51.9 1.8 2 100 43 330 199 0 1 155 51.9 1.8 2 100 44 333.8 199 0 1 55.5 50 1.8 3 '' 100 45 333.5 199 0 1 55.5 50 1.8 3 97 46 333.5 99.5 99.5 1 55.5 50 1.8 3 86 47 333.5 0 199 1 55.5 50 1.8 3 61 Reaction No. 1-After 2 hours of feed addition, take 64 grams Organic binding-17- This paper size is in accordance with Chinese National Standard (CNS) A4 specification (210 X 297 mm) 581778 A7 B7 V. Description of the invention (15) Phase sample, 100 ml whole deionized, main, soil Although A 4 was washed 6 times in water, the sample was dried by zeolite retort at 55 ° C and vacuum. Reaction No. 2-Samples 41 and 42 were processed for 19 hours after feed addition. Sample 19 was processed immediately after feed addition was completed. For each sample, the organic phase was separated, and then an equivalent of MesSiCl was added to the organic phase, and the organic phase was stirred at room temperature for 3 hours. Then take a 64 g sample of the organic phase and process it in the following steps: (ι) 2 × 2⑻ liters of 50% by weight H2SO4, 10 minutes, (2) χ 200 ml of deionized water, (3) 1 X 200 ml of a 5% by weight 1 ^! ^ 03 solution, and (4) 2 × 200 ml of deionized water. The resulting washed and neutralized organic phase was dried by zeolite distillation at 55 ° C and under vacuum. Reaction No. 3-Pour the reaction mixture into a separatory funnel and remove the acid layer. Place the organic layer in a three-necked flask with a bottom drain hole. Then, add 100 ml of 47% sulfuric acid and stir the mixture. The obtained organic layer was washed 3 times with 5% disodium diacid, and then with! Wash 2 times with 00 ml of deionized water. The organic layer was then treated with 25 g of calcium carbonate with stirring for 0 minutes, and magnesium sulfate was added. The organic layer was filtered and the solvent was removed under vacuum to give a resin as a white solid. The selected samples as described above were analyzed using 29Si NMR, GPC, and a control polystyrene standard. The results are shown in Table 5. In Table 5, the mole percentage of silicon atoms with a degree of hydroxyl substitution is labeled "SiOH" and the mole percentage of broken atoms with a degree of chlorine substitution is labeled "SiCl". -18- This paper size applies to China National Standard (CNS) A4 (210 X 297 mm)
裝 訂Binding
、發明説明( 16 A7 B7And invention description (16 A7 B7
實例4S-S1 裝 訂 午夕永砂氧樹脂係藉由如表6中所述之不同氯碎燒之共 =解作用而製備,該水解作用係藉由提供一含如表6中所 I之甲冬、重:S%鹽酸及辛基確酸制之起始推 進行,如表6中所述之氯矽烷於甲苯中之混合物,係於所 列速率下進料至反應器中,於進料添加完畢後,將各樣本 芡所逑万法進行處理。基於添加至反應器中的氯矽烷之莫 耳%總重之產物產率係列於表6中。 線 表6 初始反應器進料 添加至反應器之進 實例 aTol. HC1 OctS〇3H( 甲苯 矽烷 矽烷 (克) 克) (克) (克) (克) 48 330 199 1 100 bprfSiCl3 HSiCl3 (40.2 克) (23.5 克) 49 330 199 1 60.6 MeSiCl3 Me2SiCl2Example 4S-S1 Bookbinding Midnight Permanent Oxygen Resin was prepared by the co-decomposition of different chlorine crushing as described in Table 6, and the hydrolysis was provided by providing a Winter, weight: S% hydrochloric acid and octyl acetic acid are used as starting materials. The mixture of chlorosilanes in toluene as described in Table 6 is fed into the reactor at the listed rates. After the addition is complete, the samples are processed. The product yield series based on the mole% total weight of chlorosilane added to the reactor is shown in Table 6. Table 6 Example of initial reactor feed added to the reactor aTol. HC1 OctS〇3H (toluene silane (g) (g) (g) (g) (g) 48 330 199 1 100 bprfSiCl3 HSiCl3 (40.2 g) (23.5 g) 49 330 199 1 60.6 MeSiCl3 Me2SiCl2
19- 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公爱 1 ^' ------ 581778 A7 B7 五、發明説明(17 ) (44.2 克) (6.7 克) 50 330c 199 1 80 SiCl4 (30 克) Me3SiCl (38.4 克) 2.0 5 90 51 330 199 1 155 MeSiCls (25.9 克) Me2SiCl2 (23·5 克) 2.5 6 -- 甲苯 b =三氟丙燒 亦含Me3SiCl之起始反應進料 反應編號4 -於進料添加完畢12小時後,取64克之有 機相樣本,以200毫升之50重量%112304清洗2次,此樣 本進一步以200毫升之5重量%NaH2S03溶液清洗,於此 時,樣本呈膠凝狀。 反應編號5 -於樣本22之進料及樣本23之進料添加完 畢後,將有機相樣本41及42以下列操作處理21小時,將 64克之各有機相樣本以下列步驟處理:(i)2 X 2〇〇毫升之 50重量%1^8〇4,10分鐘,(2)1X200毫升之5重量%NaHS〇3 溶液,及(3) 1 X 200毫升之去離子水,1 〇分鐘。所得之經清 洗及經中和之有機相係以沸石蒸餾法於5 5。(:及真空下予以 乾燥。 反應編號6 -將有機相樣本以過量之雙(三甲基矽烷基) 三氟乙醯胺於甲基異丁酮/甲苯溶液處理而予加蓋。 反應樣本編號49及50係使用29Si NMR及GPC、對照聚 苯乙婦標準品進行分析,結果及實驗式係列於表7中,於 此等化學式中,Μ、D、T及Q分別代表單官能性、雙官能 -20- 本紙張尺度適财國醇標準(CNS) Α4規格(21GX 297公羞) " -- 581778 A7 B7 五、發明説明(18 ) 性、三官能性及四官能性矽氧單元。 表7 實例 Mn Mw 實驗式 49 1463 73330 ((OH)Me2Si03/2)〇.95(Me2SiO)17(OSiMeOH)5.7(〇3/2SiMe )76.4 50 2570 6547 M47.7T (〇H)3.2Q49.1 實例52 於一配置攪拌器及加料漏斗之1升燒瓶中,添加199克 之35重量%HC1及333.5克之甲苯,於500 rpm之攪拌速度 下,將一含50.0克苯基三氯矽烷於55.5克甲苯中之溶液以 一段超過150分鐘之時間逐滴添加。添加完畢後,燒瓶内 容物係經攪拌另外之70小時,然後停止攪拌並將燒瓶内容 物分離為水相及有機相,將有機相以1 0 0毫升之4 7 %硫酸 清洗2次、以1 00毫升之5%碳酸二鈉溶液清洗3次、及以 1 00毫升之去離子水清洗3次,然後以25克之固體碳酸鈣 予以中和,以50克之固體硫酸鎂乾燥並過濾,自有機相中 移除溶劑後,產生3 1.0克之白色固體,並提供一基於添加 至燒瓶中三氯矽烷總重為102莫耳百分比之產率。 實例53-55 於一 9升之擋板反應器中,置入1.5公斤37%鹽酸、0.010 公斤之辛基硫酸鈉及如表8中所述之甲苯量。將攪掉器設 定於900 rpm,然後將一溶解於0.50公斤甲苯中之0.50公 斤甲基三氯矽烷以12毫升/分之速度於室溫下添加於反應 器中,添加後,使混合物於室溫下攪拌14小時。停止攪拌, -21 - 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) Λ 裝 訂19- This paper size is in accordance with Chinese National Standard (CNS) A4 specifications (210 X 297 Public Love 1 ^ '------ 581778 A7 B7 V. Description of the invention (17) (44.2 g) (6.7 g) 50 330c 199 1 80 SiCl4 (30 g) Me3SiCl (38.4 g) 2.0 5 90 51 330 199 1 155 MeSiCls (25.9 g) Me2SiCl2 (23 · 5 g) 2.5 6-Toluene b = trifluoropropane firing also contains Me3SiCl initial reaction Feed Reaction No. 4-After 12 hours of feed addition, take a sample of 64 grams of organic phase and wash it twice with 200 ml of 50% by weight 112304. This sample is further washed with 200 ml of a 5% by weight NaH2S03 solution. Here The sample is gelatinous. Reaction No. 5-After the feed of sample 22 and sample 23 are added, the organic phase samples 41 and 42 are processed for 21 hours by the following operations, and 64 grams of each organic phase sample is below Steps of processing: (i) 50% by weight of 2 × 200 ml of 1 ^ 800, 10 minutes, (2) 1 × 200 ml of 5% by weight NaHS〇3 solution, and (3) 1 × 200 ml of Ionized water, 10 minutes. The obtained washed and neutralized organic phase was zeolite distilled at 55. (: and vacuum Dry. Reaction No. 6-The organic phase sample is treated with an excess of bis (trimethylsilyl) trifluoroacetamide in methyl isobutyl ketone / toluene solution and capped. Reaction sample numbers 49 and 50 are used. 29Si NMR, GPC, and control polystyrene standards were analyzed. The results and experimental formula series are shown in Table 7. In these chemical formulas, M, D, T, and Q represent monofunctional and bifunctional -20- Paper Standards CNS A4 Specification (21GX 297 male) "-581778 A7 B7 V. Description of the Invention (18) Properties, trifunctional and tetrafunctional siloxane units. Table 7 Example Mn Mw Experimental formula 49 1463 73330 ((OH) Me2Si03 / 2) 0.95 (Me2SiO) 17 (OSiMeOH) 5.7 (〇3 / 2SiMe) 76.4 50 2570 6547 M47.7T (〇H) 3.2Q49.1 Example 52 in a configuration In a 1-liter flask with a stirrer and an addition funnel, 199 grams of 35% by weight HC1 and 333.5 grams of toluene were added. At a stirring speed of 500 rpm, a solution containing 50.0 grams of phenyltrichlorosilane in 55.5 grams of toluene was added in one stage. Add dropwise over 150 minutes. After the addition, the contents of the flask are stirred for another 70 hours. , Then stop stirring and separate the contents of the flask into an aqueous phase and an organic phase, wash the organic phase twice with 100 ml of 47% sulfuric acid, wash 100 times with 100 ml of a 5% disodium carbonate solution, and Wash three times with 100 ml of deionized water, then neutralize with 25 g of solid calcium carbonate, dry with 50 g of solid magnesium sulfate, and filter. After removing the solvent from the organic phase, 3 1.0 g of a white solid is produced, and A yield of 102 mole percent based on the total trichlorosilane weight added to the flask was provided. Examples 53-55 In a 9-liter baffled reactor, 1.5 kg of 37% hydrochloric acid, 0.010 kg of sodium octyl sulfate, and the amount of toluene as described in Table 8 were placed. The stirrer was set to 900 rpm, and then 0.50 kg of methyltrichlorosilane dissolved in 0.50 kg of toluene was added to the reactor at a rate of 12 ml / min at room temperature. After the addition, the mixture was allowed to stand in the chamber. Stir at temperature for 14 hours. Stop stirring, -21-This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) Λ Binding
581778 A7 B7 五、發明説明(19 :广二I有機相以1升份量之去離子水清洗… /人’直洗水之pH值達4為止,將有機相《 5〇克之581778 A7 B7 V. Description of the invention (19: Guanger I organic phase is washed with 1 liter of deionized water ... / person ’until the pH value of the direct washing water reaches 4, and the organic phase" 50 grams of
Mg!〇4,並以濾紙進行真空過遽。有機溶液係使用旋 轉:發益於贼下進行濃縮’乾燥之樹脂係置於直空下至 :伏以除去殘餘溶劑。自上述操作中獲得之產物係㈣公 斤…固體。絕對分子量之資料係藉由光掃描三度伯測 技㈣得,此等不同物質獲得之分子量資料係列於下 列表中。 > 表8 實例 甲苯(公斤) Mn Μ 53 1.0 --—-—-~—_ 7,220 ---—--- 丄YA W 303,900 54 2.0 6,920 " --—~—----—. 27 300 55 3.0 2,240 9,490 實例56 於-配置濃縮器、氮氣入口、機械式攪掉器、加料漏斗 及溫度探針之1升燒瓶中,添加152·37克之37重量%鹽酸 及0.9908克之辛基磺酸鈉,待辛基磺酸鈉溶解後,添加 335.34克之甲苯。製備一含34·57克之十八烷基三氯矽烷、 52.97克甲基三氯矽烷與87·37克甲苯之溶液,將此進料溶 液以一段超過1小時之時間逐滴添加,並使所得混合物於 至溫下攪拌至隔夜。停止攪拌後,將混合物分離為有機相 及水相,移去水相,然後將有機相以3⑻毫升之去離子水 於55°C下清洗4次,有機相接著以硫酸鎂乾燥,並於真空 中 >辰縮,產生37.89克(74%產率)之矽烷樹脂,其具9,68〇 -22- 本紙張尺度適用中國®家鮮(CNS) M規格(21ϋχ撕公爱) 581778 A7 B7Mg! 〇4, and vacuum filtration with filter paper. The organic solution is used for rotation: concentrated under the benefit of thieves, and the dried resin is placed under direct air to: volts to remove residual solvents. The product obtained from the above operation was ㈣kg ... solid. The absolute molecular weight data are obtained by light scanning third degree measurement. The molecular weight data series obtained for these different substances are listed in the table below. > Table 8 Examples of toluene (kg) Mn Μ 53 1.0 -------- ~ --_ 7,220 -------- 丄 YA W 303,900 54 2.0 6,920 " --- ~ -------. 27 300 55 3.0 2,240 9,490 Example 56 In a 1-liter flask equipped with a concentrator, a nitrogen inlet, a mechanical stirrer, an addition funnel, and a temperature probe, 152.37 g of 37% by weight hydrochloric acid and 0.9908 g of octylsulfonate were added. Sodium. After sodium octyl sulfonate was dissolved, 335.34 grams of toluene was added. A solution containing 34.57 grams of octadecyltrichlorosilane, 52.97 grams of methyltrichlorosilane, and 87.37 grams of toluene was prepared. This feed solution was added dropwise over a period of more than 1 hour, and the obtained The mixture was stirred at room temperature until overnight. After the stirring was stopped, the mixture was separated into an organic phase and an aqueous phase, the aqueous phase was removed, and then the organic phase was washed 4 times with 3 ⑻mL of deionized water at 55 ° C. The organic phase was then dried over magnesium sulfate and vacuumed. Medium > Chen Shrink, yielding 37.89 g (74% yield) of silane resin with 9,68〇-22-This paper size is applicable to China® Home Fresh (CNS) M specification (21ϋχ tear public love) 581778 A7 B7
五、發明説明(2〇 ) 之 Mn 及 66,8〇〇 之 mw。V. Description of the invention (20) Mn and 66,800 MW.
實例U 於-配置如同實例56所述之i升燒瓶中,添加1527 克之37重量%鹽酸及335·14克之甲苯。製備—含μ”克 之十八烷基三氣矽烷、52.74克甲基三氣矽烷與S7 〇2克甲 苯之溶液,將此進料溶液以一段超過i小時之時間逐滴枣 加,並使所得混合物於室溫下攪拌至隔夜。停止攪拌後= 將混合物分離為有機相及水相’移去水相,然後將有機相 以300毫升之去離子水於饥下清洗4次,有機相接著於 真空中以硫酸鎂乾燥並予濃縮,產生27.91克(55%產率)之 矽烷樹脂,其具1,650之^及1〇5,650之Mw。 實例5 8 於一配置如同實例56所述之丨升燒瓶中,添加ΐ5ι 〇ι 克之37重量%鹽酸及0.9967克之辛基磺酸鈉,待辛基磺酸 鈉溶解後,添加200.88克之甲苯。製備一含43.55克之十 八燒基二氣石夕燒、48·55克甲基三氯碎燒與885〇克甲苯之 溶液,將此進料溶液以一段超過36分鐘之時間逐滴添加, 並使所得混合物於室溫下攪拌至隔夜。停止揽拌後,將混 合物分離為有機相及水相’移去水相,然後將有機相以3〇〇 愛升之去離子水於6 5 C下清洗4次’有機相接著以硫酸鐵 乾燥,並於真空中濃縮成一固體。將此固體溶於2〇〇毫升 THF中,並添加1〇毫升之去離子水,於攪拌1小時後,將 混合物於真空中進行汽提,以獲得一固體,產生6〇·54克 (108%產率)之矽烷樹脂,其具7,260之Μη及51,000之Μ。 -23- 本紙張尺度適用中國國家標準(CNS) Α4規格(210 X 297公釐)Example U In an i-liter flask configured as described in Example 56, 1527 grams of 37% by weight hydrochloric acid and 335.14 grams of toluene were added. Preparation—a solution containing μ "gram of octadecyltrigassilane, 52.74 grams of methyltrigassilane and S 702 grams of toluene, this feed solution was added dropwise over a period of i hours, and the resulting The mixture was stirred at room temperature until overnight. After stirring was stopped = the mixture was separated into an organic phase and an aqueous phase. The aqueous phase was removed, and then the organic phase was washed 4 times with 300 ml of deionized water under hunger. Drying with magnesium sulfate in vacuo and preconcentration yielded 27.91 g (55% yield) of a silane resin with a Mw of 1,650 and a Mw of 105,650. Example 5 8 In a configuration as described in Example 56 丨In a 1-liter flask, add 5 μg of 37% by weight hydrochloric acid and 0.9967 g of sodium octyl sulfonate. After the sodium octyl sulfonate is dissolved, add 200.88 g of toluene. Prepare an octadecyl disulfite containing 43.55 g , 48.55 grams of methyl trichloride and 8850 grams of toluene solution, this feed solution was added dropwise over a period of more than 36 minutes, and the resulting mixture was stirred at room temperature overnight. Stop stirring After that, the mixture is separated into an organic phase and an aqueous phase ' The aqueous phase was removed, then the organic phase was washed 4 times with 300 liters of deionized water at 65 C. The organic phase was then dried over ferric sulfate and concentrated in vacuo to a solid. This solid was dissolved in 2 ° C. 0 ml of THF, and 10 ml of deionized water was added. After stirring for 1 hour, the mixture was stripped in vacuo to obtain a solid, yielding 60.54 g (108% yield) of a silane resin. , Which has a Mη of 7,260 and a M of 51,000. -23- This paper size applies to China National Standard (CNS) A4 specifications (210 X 297 mm)
裝 訂 581778 五、發明説明(a 實例5 9 於一配置如同實例56所述之1升燒瓶中, 土、 ~、、力 口 1 < 克< 37重量%鹽酸及〇·99 u克之辛基磺酸鈉,待辛5〇.83 鈉溶解後,添加200.28克之甲苯。製備一含μ%基蟥峻 基三氯矽烷、34.01克甲基三氯矽烷與8715克甲克之笨 液,將此進料溶液以一段超過4 5分鐘之時間逐滴、恭策之緣 使所得混合物於室溫下授拌至隔夜。停止授掉 並 仏、、 便將混合 为離為有機相及水相,移去水相,然後將有機相以3⑽ Φ升之去離子水清洗4次,有機相接著於真空中以硫酸鎂 乾燥並予濃縮,產生41.88克(83%產率)之矽烷樹脂,其具 9,300 之 Mn 及 204,500 之 Mw。 -24- 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐)Binding 581778 V. Description of the invention (a Example 5 9 In a 1 liter flask configured as described in Example 56, soil, ~ ,, and strength 1 < g < 37% by weight hydrochloric acid and 0.999 u of octyl Sodium sulfonate, after octanoate 0.58.83 sodium is dissolved, 200.28 grams of toluene is added. Prepare a stupid solution containing μ% sulfenyl trichlorosilane, 34.01 grams of methyltrichlorosilane, and 8715 grams of methyl chlorosilane. The material solution is dropped dropwise over a period of more than 45 minutes, and the resulting mixture is allowed to stir at room temperature until overnight. After stopping the mixing and mixing, the mixture is separated into an organic phase and an aqueous phase and removed. The aqueous phase was then washed 4 times with 3⑽ Φ liters of deionized water. The organic phase was then dried over magnesium sulfate in a vacuum and concentrated to yield 41.88 g (83% yield) of a silane resin with 9,300 Mn and Mw of 204,500. -24- This paper size applies to China National Standard (CNS) A4 (210 X 297 mm)
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TWI403540B (en) * | 2005-10-21 | 2013-08-01 | Dow Corning Toray Co Ltd | Cyclic dihydrogen polysiloxane, hydrogen polysiloxane, manufacturing method thereof, coating agent, inorganic substrate with silicon-based glass thin layer, manufacturing method thereof, and semiconductor device |
TWI408173B (en) * | 2006-01-19 | 2013-09-11 | Dow Corning | Silicone resin film, method of preparing same, and nanomaterial-filled silicone composition |
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US4412080A (en) * | 1982-08-16 | 1983-10-25 | General Electric Company | Methods for preparing cyclopolysiloxanes |
US5010159A (en) * | 1989-09-01 | 1991-04-23 | Dow Corning Corporation | Process for the synthesis of soluble, condensed hydridosilicon resins containing low levels of silanol |
JP2864817B2 (en) * | 1991-11-08 | 1999-03-08 | 信越化学工業株式会社 | Method for producing polyorganosiloxane resin |
US5516867A (en) * | 1995-05-12 | 1996-05-14 | Dow Corning Corporation | Modified hydrogen silsesquioxane resin |
US5973095A (en) * | 1997-04-21 | 1999-10-26 | Alliedsignal, Inc. | Synthesis of hydrogensilsesquioxane and organohydridosiloxane resins |
US6043330A (en) * | 1997-04-21 | 2000-03-28 | Alliedsignal Inc. | Synthesis of siloxane resins |
JP2000143810A (en) * | 1998-11-18 | 2000-05-26 | Dow Corning Asia Ltd | Preparation of hydrogen silsesquioxane resin |
US6281285B1 (en) * | 1999-06-09 | 2001-08-28 | Dow Corning Corporation | Silicone resins and process for synthesis |
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