TW420685B - Process for preparing organosiloxane terminated with silanol group - Google Patents

Process for preparing organosiloxane terminated with silanol group Download PDF

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TW420685B
TW420685B TW84104067A TW84104067A TW420685B TW 420685 B TW420685 B TW 420685B TW 84104067 A TW84104067 A TW 84104067A TW 84104067 A TW84104067 A TW 84104067A TW 420685 B TW420685 B TW 420685B
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Taiwan
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patent application
scope
group
exchange resin
hydrolysis
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TW84104067A
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Chinese (zh)
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Minoru Igarashi
Masaharu Takahashi
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Shinetsu Chemical Co
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Priority claimed from JP07081706A external-priority patent/JP3079939B2/en
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Abstract

Hydrolysis of an alkoxysiloxane of the formula: R<1>a(R<2>O)bSiO(4-a-b)/2, wherein R1 is a monovalent hydrocarbon group, R2 is an alkyl group having 1 to 4 carbon atoms, letter a = 0 to 2.2, b = 0.2 to 3, 2 <= a + b <= 3, and the number of silicon atoms in a molecule is 2 to 5, is effected in the presence of a cation exchange resin by adding water therereto in an amount of 1 to 10 mol per mol of the alkoxy group in the alkoxysiloxane and agitating the mixture. Low molecular weight, linear organosiloxanes having a silanol terminal group including dimer diol trimer diol are produced in high yields.

Description

A7 經濟部中央標芈局負工消费合作社印1i 〇β8η &quot;4_Βτ___五、發明説明(1 ) 本發明係有關末端具有矽烷醇基之低分子量有機基聚 矽氧烷的簡便製造方法。 兩末端具有羥基之直鏈狀有機基聚矽氧烷係製造聚矽 氧橡膠複合物時做爲分散劑極有效者。有各種分散劑被使 用。分散劑之功能與羥基含有量成正比例,羥基含有量多 之聚矽氧烷,即末端基具有羥基之低分子量直鏈狀有機基 聚矽氧烷係使用少量即可,又,考慮聚矽氧橡膠複合物之 加工性亦較爲有效,惟現今工業上被使用者係有機基四矽 氧烷以上之直鏈狀有機基聚矽氧烷,較其更有效之.單體二 醇,二聚物二醇,三聚物二醇之類的具有矽烷醇之有機基 矽烷或矽氧烷則至今尙未有人提案工業上更有利地獲得之 方法。 即,以往曾被硏究各種合成短鏈羥基矽烷及矽氧烷之 方法。實驗室規模中周知者有使用緩衝溶液等,保持烷氧 基矽烷之溶液爲中性之狀態,予以水解之方法,惟此方法 很難在工業上實施。又,亦有混合二甲氧基矽烷於過量之 中性蒸餾水,使其回流之方法,但目的物之收率並未顯著 提髙。 具有羥基末端之低分子量直鏈狀有機基聚矽氧烷係工 業上以弱鹼性水溶液水解而末端具有氯原子之直鏈狀有機 氯化矽氧烷使其不致於成爲環狀體予以製造。惟此方法係 由於矽烷醇基對於酸或鹼不安定,常會因水解生成之 HC 而引起縮合反應,目的之有機基聚矽氧烷以外’邇 會有生成較高分子之有機基聚矽氧烷或環狀之聚矽氧烷等 (請先閱讀背面之注意事項再填寫本頁) 訂 本紙張尺度適用中國國家標準(CNS ) A4規格(2l〇X 297公釐) 42 0685 經濟部中央標準局員工消費合作社印敦 A7 B7五、發明説明(2 ) 問題。因此該方法中必須嚴格地保持水解水爲中性,除採 取此手段以外很難合成上述直鏈狀有機基聚矽氧烷。 又,使用乙酸使上述有機基氯化聚矽氧烷予以酿氧化 ,再使其水解之方法亦爲人所知。惟以此方法無法完全水 解,生成物中會殘留醯氧基,並不適於使用做爲聚矽氧橡 膠之分散劑。 另一方面,美國專利第3 9 2 5 2 8 5號中係記載使 六甲基瑱三矽氧垸,甲醇,甲酸,水反應,合成稍殘留甲 氧基之具有矽烷醇未端基的低分子量直鏈狀有機基.聚矽氧 烷的方法,惟因使較高價之六甲基環三矽氧烷,所以成本 較高,又無法生成3以下D單位〔(CH3)2SiO〕之 具有矽烷醇末基的低分子量直鏈狀有機基聚矽氧烷,又, 反應上無法生成爲較1 ,5 —二羥基三矽氧烷短者,有羥 基含量受限制之問題。 另外,美國專利第5 0 5 7 6 4 0號中係記載將相對 應之氯矽氧烷滴下含水之環氧丙烷,環氧丁烷之類環氧系 溶劑中的方法,惟此方法係除使用較高價之六甲基環三矽 氧烷以外,尙有溶劑爲低沸點者易於靜電著火之安全上問 題。 又,特公昭6 4 — 5 6 0 4號中係記載以活性化白土 之_固體體酸ϋ:以水解烷氧基矽烷之短鏈矽烷醇的合成 方法,惟此方法因必須中和固體酸,所以操作煩雜。除此 外,此方法中係得到各種短鏈矽烷醇之混合物,二聚物二 醇之收率只爲5 0 %左右。又,有關單體二醇則如實施例 (請先閱讀背面之注意事項再填寫本頁) 本紙张尺度適州中國國家梂準(CN'S Μ4規格(210Χ297公釐) 4 2 06 85 A7 B7 五、發明説明 2 9所示, 又,美 子交換樹脂 法。惟卻完 物二醇之合 本發明 且簡便,廉 烷的方法爲 本發明 發現在陽離 氧基矽氧烷 基之二院氧 1 . 0倍莫 高收率地得 醇基之低分 8 4莫 國專利 以水解 全未提 成,收 係有鑑 價地製 目的者 人係爲 子交換 ,尤其 基矽氧 爾以上 到做爲 子量有 爾%純 第3 3 院氧基 及短鏈 率等。 於上述 造具有 0 達成上 樹脂存 最好對 烷添加 的水, 聚矽氧 機基砂 度者只能得1Q%以下之收率。 〇 4 3 1 8號中係揭示使用陽離 矽烷,以製造高聚合度樹脂之方 矽烷醇,尤其二聚物二醇,三聚 情況而予以開發者,提供高收率 矽烷醇基之低分子量有機基矽氧 述目的經再三深入檢討之.結果, 在下,對於以下式(1)所示烷 以下式(2 )所示末端具有烷氧 對此等烷氧基矽氧烷之烷氧基爲 經搅拌進行水解,即可極容易且 橡膠之分散劑極有用的具有矽烷 氧烷。 (請先閱讀背面之注意事項再填寫本頁) 訂A7 Printed by the Central Bureau of Standards of the Ministry of Economic Affairs and Consumer Cooperatives 1i 〇β8η &quot; 4_Βτ ___ V. Description of the Invention (1) The present invention relates to a simple method for manufacturing a low molecular weight organic polysiloxane having a silanol group at the end. A linear organopolysiloxane with hydroxyl groups at both ends is a highly effective dispersant when producing silicone rubber compounds. Various dispersants are used. The function of the dispersant is proportional to the hydroxyl content. Polysiloxanes with a large hydroxyl content, that is, low-molecular-weight linear organic polysiloxanes with hydroxyl groups at the end groups, can be used in small amounts. Consider polysiloxanes. The rubber compound is more effective in processability, but today the industrial users are more linear organic polysiloxanes than organic tetrasiloxanes. Monomer diols, dimerization Organic silanes or siloxanes with silanols such as biodiols, trimer diols, etc. have not yet been proposed for industrially more advantageous methods. That is, various methods for synthesizing short-chain hydroxysilanes and siloxanes have been studied in the past. It is known in the laboratory scale to use a buffer solution or the like to keep the solution of the alkoxysilane in a neutral state and to hydrolyze it, but this method is difficult to implement industrially. In addition, there is a method of mixing dimethoxysilane in an excessive amount of neutral distilled water to make it reflux, but the yield of the target product has not been significantly improved. Low-molecular-weight linear organic polysiloxanes having a hydroxyl terminal are industrially hydrolyzed with a weakly alkaline aqueous solution and linear organic chlorinated siloxanes having a chlorine atom at the terminal to prevent them from being made into a ring. However, this method is because silanol groups are unstable to acids or bases, and often cause condensation reactions due to HC generated by hydrolysis. In addition to the intended organic polysiloxanes, there will be higher molecular organic polysiloxanes. Or ring-shaped polysiloxane (please read the notes on the back before filling this page) The size of the paper is applicable to China National Standard (CNS) A4 (210 × 297 mm) 42 0685 Central Bureau of Standards, Ministry of Economic Affairs Employee Consumer Cooperatives Indun A7 B7 V. Invention Description (2) Question. Therefore, in this method, it is necessary to strictly maintain the hydrolysis water as neutral, and it is difficult to synthesize the linear organic polysiloxane other than this method. In addition, a method of oxidizing the above organic-based chlorinated polysiloxane with acetic acid and then hydrolyzing the same is also known. However, it cannot be completely hydrolyzed by this method, and fluorene will remain in the product, which is not suitable for use as a dispersant for silicone rubber. On the other hand, U.S. Patent No. 3 9 2 5 2 8 5 describes the reaction of hexamethylphosphonium trisiloxane, methanol, formic acid, and water to synthesize a low residual methoxy group with a silanol end group. Molecular weight linear organic group. The method of polysiloxane, but because of the higher price of hexamethylcyclotrisiloxane, the cost is high, and it is not possible to generate silanes with D units [(CH3) 2SiO] below 3 The low molecular weight linear polyorganosiloxane of the alcohol end group cannot be formed shorter than 1,5-dihydroxytrisiloxane in the reaction, which has the problem of limited hydroxyl content. In addition, U.S. Patent No. 5 0 7 6 40 describes a method of dripping corresponding chlorosiloxane into an epoxy solvent such as propylene oxide and butylene oxide. In addition to the use of higher-priced hexamethylcyclotrisiloxane, those with low boiling point solvents are prone to electrostatic ignition and safety issues. In addition, Japanese Patent Publication No. 6 4-5 6 0 4 describes a method for synthesizing _solid acid of activated white clay: a short-chain silanol that hydrolyzes alkoxysilane, but this method must neutralize the solid acid , So the operation is complicated. In addition, in this method, a mixture of various short-chain silanols is obtained, and the yield of the dimer glycol is only about 50%. In addition, the related monomer diols are as in the example (please read the precautions on the back before filling this page) The paper size is suitable for China's national standard (CN'S Μ4 specification (210 × 297 mm) 4 2 06 85 A7 B7 V. Description of the invention is shown in FIG. 9 as well as the Miko exchange resin method. However, the combination of finished diols of the present invention is simple and convenient. 0 times the high yield of the alcohol group with a low score of 8 4 Mozambique's patent for the hydrolysis of all non-commissioned, the collection system for the purpose of the evaluation of the human exchange for the child, especially above the silicon silyl to the sub-quantity There are 1% pure 3rd oxygen and short chain ratio, etc. Based on the above, it is best to add water to the alkane to achieve resin retention. Polysiloxane based sand can only get a yield below 1Q%. 〇 4 3 1 8 is the development of the use of cationic silanes to produce highly polymerized silanols, especially dimer diols and trimers, and has been developed by developers to provide low yield silanols. The purpose of molecular weight organosilicone has been thoroughly reviewed. The results show that The alkoxy group represented by the following formula (1) has an alkoxy group at the end represented by the following formula (2): The alkoxy group of these alkoxysiloxanes is hydrolyzed by stirring, which can be extremely easy and the dispersant of rubber is extremely easy. It is useful to have a siloxane. (Please read the notes on the back before filling this page)

R】》(RO)bSiO ⑴ 經濟部中央標隼局W工消资合作社印製 (式中R 1係表示相同或不同之取代或不取代之一價烴基 ,R 2係表示相同或不同之碳數1〜4烷基,a係〇〜 2. 2,1?係0.2〜3之數,3 + 13係2〜3。惟分子 中之矽原子數係2〜5)。 本紙张尺度適用中國國家標隼(CNS ) Λ4規樁(2ΐϋ X 29&quot;?公釐) 420685 A 7 B7 五、發明説明(4 ) R1 RO-fSiO^R2 (2) (式中R1,R2係如上述所定義,η係2〜5之整數) 又,這時發現上述式(2 )的二烷氧基矽氧烷係在陽 離子交換樹脂存在下,於以下式(3 ) R^S i (OR2) (3) (請先聞讀背面之注意事項再填寫本頁)R]》 (RO) bSiO 印 Printed by the Industrial Standards Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (where R 1 represents the same or different substituted or unsubstituted monovalent hydrocarbon group, and R 2 represents the same or different carbon The number is 1 to 4 alkyl, a is 0 to 2.2, 1? Is 0.2 to 3, 3 + 13 is 2 to 3. However, the number of silicon atoms in the molecule is 2 to 5). This paper scale is applicable to Chinese National Standard (CNS) Λ4 gauge pile (2ΐϋ X 29 &quot;? mm) 420685 A 7 B7 V. Description of the invention (4) R1 RO-fSiO ^ R2 (2) (where R1, R2 are As defined above, η is an integer of 2 to 5.) At this time, it was found that the dialkoxysiloxane of the above formula (2) is in the presence of a cation exchange resin, and is represented by the following formula (3) R ^ S i (OR2 ) (3) (Please read the notes on the back before filling in this page)

、tT 所示二烷基矽烷中添加上述式(3 )之二烷氧基矽烷分子 中存在之烷氧基的〇. 1〜1倍莫爾水,經撹拌進行第一 階段的水解即可以極容易地獲得,又繼續如上述地水解上 述所得式(2 )之二烷氧基矽氧烷時,即可以以簡便方法 自較廉價之二甲氧基二甲基矽烷等二烷基氧基矽烷有利地 得到例如以下式(4 ),( 5 )所示低分子量有機基聚矽 氧烷,遂而完成本發明。 R1 經濟部中央標準局員工消費合作社印製 HO-^SiO)rH R' R1 HO-(SiO)j-H I R1 (4) (5) (式中R 1係如上述所定義)。 因此,本發明係在於提供一種具有矽烷醇基之低分子 ^張尺度適用1國家標芈(CNS ) 規格(2】0Χ297公康)_ 7 _ 42 0685 經濟部中夬標準局貝工消費合作社印製 A7 _ B7___五、發明説明(5 ) 量有機基矽氧烷的製造方法,其特徵爲在ΙΪ離子交換樹脂 存在下,在上述式(1 )所示烷氧基矽氧烷中添加上述烷 氧基矽氧烷之烷氧基的1. 0倍莫爾以上水,經攪拌予以 水解者。 這時,本發明係做爲較好實施形態提供在陽離子交換 樹脂存在下,於上述式(3),所示二烷基矽烷中添加相 當於上述式(3 )之二烷氧基矽烷分子中存在之烷氧基的 0. 1〜1倍莫爾水,經攪拌進行第一階段的水解,生成 爲上述式&lt; 2 )所示末端具有烷氧基之二烷氧基砍氧烷後 ,在陽離子交換樹脂存在下,在上述式(2 )之二烷氧基 矽氧烷中添加化學計量上過量的水,經撹拌進行第2階段 之水解爲特徵的低分子量直鏈狀有機基聚矽氧烷之製造方 法0 以下更詳細說明本發明,本發明之具有矽烷醇基的低 分子量有機基矽氧烷之製造方法係在陽離子交換樹脂存在 下,以如上述之烷氧基矽烷爲原料進行水解之方法。依本 發明之方法時可以抑制矽烷醇之縮合反應,得到環狀聚矽 氧烷或鏈長被延長之聚有機基矽氧烷含有量極少,具有矽 烷醇基的低分子量有機基矽氧烷。即,水解原料之烷氧基 矽氧烷,以製造對應之羥基矽氧烷的方法。 在此上述烷氧基矽氧烷係使用以下式(1 )所示者。 R1.(R2Q)bSi〇4-i.^ (1) (請先閱讀背面之注意事項再填寫本頁) 本紙張&amp;度適用中國國家標準(CNS ) Λ4^格(210X2^7公釐) 經濟部中央標準局員工消费合作社印製 420685 A7 __________B7 五'發明説明(6 ) 這時R1係取代或不取代之一價烴基,較佳係碳數1 〜1 0 ,尤其1〜6者。具體言可爲甲基,丙基,丁基, 戊基,己基,辛基,癸基,十二烷基等烷基:乙烯基等烯 基;苯基,甲苯基等芳基:点一苯乙基等芳烷基:以及— 部份或全部結合於此等烴類中碳原子的氬原被氟等自素原 子或氰基所取代之基(例如3,3,3 -三氟化丙基或氣 乙基)等。其中以甲基,乙烯基,苯基爲宜。又,r 2係 碳數1〜4之烷基,較佳係甲基,乙基,雨者同時存在於 —分子中亦無妨。另外,a,b係如上述範圍之數.。 此式(1 )之烷氧基矽氧烷聚合度,即一分子中的矽 原子數係以2〜5,尤其以2〜3爲宜,此等烷氧基矽氧 烷以下述式(2 )所示之二烷氧基矽氧烷最適於使用。 R1 RO-^SiO^R2 ^ ⑵ (式中R1,R2係如上述所定義,η係2〜5之整數)。 上述烷氧基矽氧烷之具體例可爲1 ,3 _二甲氧四甲 基二矽氧烷,1 ,1—二甲氧四甲基二矽氧烷,i 一甲氧 五甲基二矽氧烷,1 ,5 —二甲氧六甲基三矽氧烷,1 , 7 —二甲氧八甲基四矽氧烷,3_甲氧七甲基三矽氧烷, 1 ,3 —二甲氧_1 ,3 —二乙烯基一1 ,3 —二甲二矽 氧烷等。此烷氧基矽氧烷可以單獨使用,亦可混合複數種 使用。惟混合複數種烷氧基矽氧烷使用時,由於二者之水 本紙掁Κ度適用中阐阈家橾卒(CN'S ) Λ4坭格Uiox 297公釐) ^^1 ^^1 ^^1 I ^ I &gt;· (請先閱讀背面之注意事項再填舄本頁} ,1Τ 經濟部中央標準局員工消资合作社印製 4 2 06 85 ' A7 B7五、發明説明(7 ) 解速度不同,有時無法均一地反應,必須加以注意。 式(1 )之烷氧基矽氧烷係可依公知方法在三乙胺, 尿素,吡啶等存在下使R、C 5 b S i 0C4-a-b)/2( R1,a,b係如上述所定義)與具有相對應於R2之烷基 的醇類反應,即可製得,尤其上述式(2 )之烷氧基矽氧 烷係可在以下式(3 ) Rl2Si(〇R2)2 (3) (式中R1,!?2如上述) - 所示二烷氧基矽烷之陽離子交換樹脂存在下水解較爲適宜 Ο 更詳細說明藉由式(3 )二烷氧基矽烷之水解以製得 式(2 )二烷氧基矽氧烷的方法。具體言,此式(3 )二 烷氧基矽烷可爲例如二甲基二甲氧基矽烷,苯基甲基二甲 氧基矽烷,甲基乙烯基二甲氧基矽烷,二甲基二乙氧基矽 烷,苯基甲基甲氧基乙氧基矽烷等,在以二甲基二甲氧基 矽烷爲宜。又,此等二烷氧基矽氧烷可以單獨使用,亦可 混合複數種使用。惟混合複數種烷氧基矽氧烷使用時,由 於二者之水解速度不同,有時無法均一地反應,必須加以 注意。 . 又,上述式(3 )之二烷氧基矽氧烷係最好使用氯成 份少者。即,本發明目的物質之短鏈矽烷醇係在酸性,鹸 性條件下不安定,爲得短鏈矽烷醇,反應中及減壓蒸餾時 必須保持系中爲中性,通常烷氧基矽烷係可以自相對應之 本紙张尺度適用中國國家標芈{〔、奶)六4規格(210&gt;&lt; 297公釐) * iU &quot; (請先閱讀背面之注意事項再填寫本頁) 經濟部中失標準局員工消費合作杜印製 420685 A7 __B7__ 五、發明説明(8 ) 氯化矽烷予以合成,所以其中若含有氯化矽烷,此等氯化 矽烷會很快地與水反應生成爲鹽酸,所以反應系會變成酸 性,引起不佳之矽烷醇縮合反應。所以爲得短鏈矽烷醇, 最好使用氯化矽烷含量少之二烷氧基矽烷爲宜。因此上述 式(3 )二烷氧基矽烷中所含氯成份係以1 〇 P pm以下 ,最好以lOppm以下爲宜。 其次,使用於此二烷氧基矽烷之水解的水係以離子交 換樹脂除去Na,Ca,Mg等離子,使其在較低溫,且 在矽烷醇多之狀態下水解所必須之成份,使用導電.率爲 1 0 1 Q Μ Ω以上,較佳以1 0 1 2 Μ Ω以上,更佳以 1 Ο 15Μ Ω以上之離子交換水最適於使用。導電率爲 1 Ο 1αΜΩ以下時,離子交換樹脂與水解水中所含離子會 引起離子交換,水解之水會變成酸性,所以並不適宜。 另外,加入上述二烷氧基矽烷與離子交換水之混合物 中的陽離子交換樹脂係爲保持水解之水的D Η値於中性附 近,且溫和地起水解必須之成份。 在此,陽離子交換樹脂之種類係首先架構爲以聚苯乙 烯或二乙烯苯之懸濁聚合高分子爲宜。陽離子交換樹脂之 型態係有凝膠型與大孔型,此等中空洞體係以水銀注入法 測定時爲具有〇. Imi2/g以上的大孔型陽離子交換樹 脂爲最適宜。又附在樹脂之酸性基以磺酸基,丙烯醯基等 Η +型爲宜,磺酸基爲更佳。可以滿足此等條件之離子交 換樹脂有例如Amberiist 15(羅門哈斯公司製),Diaion PK-208H,PK-216H,PK-228H( 本紙張尺適用中阁國家標準(CNS ) Λ4规樁(2丨0 X 297公釐)i . (請先閱讀背面之注意事項再填寫本頁) 訂 4 2 06 85 A7 經濟部中央標準局負工消費合作社印製 ________ B7______五、發明説明(9 ) 以上爲三菱化成製)Peuro丨ite CT — 1 7 5 ’ CT_ 1 7 1 ,CT 一 1 6 9 (以上爲Peuro丨ite公司製)等, 尤以PeurolUe CT — 1 7 5 (Peuro丨ite公司製)爲宜 Ο 上述式(3 )二烷氧基矽烷的水解中,水解所用水的 董係上述式(3)二烷氧基矽烷分子中的烷氧基之〇. 1 倍莫爾〜1倍莫爾,較堆係0· 2〜0. 6倍莫爾。 〇. 1倍莫爾以下時不能充分進行水解,會殘留大量之原 料烷氧基矽烷並不適宜,1倍莫爾以上時無法得式(2) 二烷氧基矽氧烷,會變成羥基矽烷,羥基烷氧基,無法有 效率地生成具有矽烷醇基之低分子量有機基矽氧烷。 又,陽離子交換樹脂之添加量係對1 0 0重量份上述 式(3 )二烷氧基矽烷與水解之水的合計量而言爲 0. 0001〜30重量份,尤其以0. 01〜1重量份 爲宜。離子交換樹脂之量若爲3 0重量以上時會促進生成 之矽烷醇基進行縮合,有時無法得短鏈者,又,爲 0 . Ί] 0 0 1重置份以下時有時無法得到可充分進行水解 之活性。 又,二烷氧基矽烷之水解反應時間可以隨意,惟太長 時藉由水解生成之二烷氧基矽氧烷的矽氧烷鍵會被切斷, 會生成爲不佳之環狀物...,鏈長較長之矽氧烷,所以爲得到 短鏈二烷氧基矽氧烷,以5 0小時以內之反應時間爲宜。 又,反應溫度係通常可爲室溫,太高時會有發生同樣之反 應,反應溫度係在5 0°C以下,尤其在2 5 以下實施爲 本紙悵尺度適用中闺國家標华·( CNS &gt; A4規格(2丨0X297公缝)~~~* '~~' • 1^ - --Γ--.------------訂 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消费合作杜印策 4 2 06 85 ' A7 B7五、發明説明(10 ) 宜0 上述式(3 )之二烷氧基矽烷的水解反應係在二烷基 矽烷與水之存在下藉由陽離子交換樹脂進行水解,所以水 解初期係分離爲二烷氧基矽烷相與水相。隨著進行水解, 水被消耗,生成醇類而使系爲均一°另外,離子交換樹脂 係固體,無法溶解於溶液中,反應係在固體表面進行。所 以未充分混合撹拌時有時無法進行均一之反應,爲此反應 必須一邊充分地搅拌混合一邊進行。 如上述在陽離子交換樹脂存在下,使上述式(.3 )二 烷氧基矽烷與其烷氧基之0.1倍莫爾〜1倍莫爾水時, 可得末端具有烷氧基之鏈長之2〜5的上述式(2 )所示 二烷氧基矽氧烷,與藉由水解生成之醇類等副生成物的混 合物。 上述生成之混合物係視其需要經由蒸餾等操作,即可 以極容易地分離爲所望鏈長之烷氧基矽氧烷。例如以二甲 氧二甲基矽烷爲原料,使用烷氧基之〇. 3倍莫爾的水, 藉由本發明所得反應混合物中係因反應條件而不同,通常 含有5 0% 1 ,3_二甲氧基四甲基二矽氧烷,2 5% 1 ,5 —二甲氧基六甲基三矽氧烷,6% 1 ,7 —二 甲氧基八甲基四矽氧烷,2% 1 ,9 _二甲基十甲基五 矽氧烷。其餘係未反應之二甲氧基二甲基矽烷。此等鏈長 不同之二甲氧基矽氧烷可以藉由蒸餾分離。又,反應完後 ,水解觸媒之陽離子交換樹脂可以藉由過滤之操作即極易 除去。 本紙張尺度適用中國阉家標隼(CNS ) A4規格(210χ2&lt;^7公釐)_ η - — (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局負工消費合作社印裝 420685 、 A7 ____B7_五、發明説明(11 ) 所以本發明中係在離子交換樹脂存在下,水解如上述 所得式(2 )之二烷氧基矽氧烷等式(1 )所示烷氧基矽 氧烷,得到具有矽烷醇基之低分子量有機基矽氧烷者。 這時使用之烷氧基矽氧烷係與如上述理由一樣的理由 ,以使用分子中所含氯成份爲1 0 0 p pm以下,尤其 1 0 ppm以下者爲宜。 又,水解所用之水係爲抑制生成環狀矽氧烷,鏈長被 延長之有機基矽氧烷,通常使用以離子交換樹脂等除去 N a,C a,Mg等離子之離子交換水,或不含此.等離子 之蒸餾水。若有如上述離子性物質含於水解之水中時,會 與做爲水解觸媒使用之離子交換樹脂,例如磺酸基之H + 發生離子交換,使水解之水成爲酸性。爲此水解後生成之 短鏈矽烷醇無法穩定地存在於其中,有時會生成不適宜之 環狀聚矽氧烷,被延長鏈長之有機基矽氧烷。因此水解之 水的導電率係較佳爲1 0 1()ΜΩ以上,更佳爲1 0 12ΜΩ 以上,最佳係1 0 15 Μ Ω以上。 另一方面*陽離子交換樹脂係一邊可以保持水解之水 的Ρ Η値爲中性,一邊引起溫和之水解所需之成份,做爲 水解觸媒使用陽離子交換樹脂可以抑制生成環狀物等縮合 生成物,得到對應之二烷氧基矽氧烷的二羥基矽氧烷者’ 此陽離子交換樹脂可以使用相同於上述二烷氧基矽的水解 時使用之陽離子交換樹脂者。 上述水解時使用之水量係相當於烷氧基矽氧烷中之焼 氧基的1倍莫爾以上,最好係1倍莫爾以上之化學計量上 本紙張尺度過圯中國國家標辛·( CNS ) Λ4规格(21〇Χ29ΐ公釐)_- (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局貝工消費合作社印製 4 2 Π 6 85 'k Α7 Β7 五、發明説明(12 ) 爲過量,又以1 0倍莫爾以下,尤其5倍莫爾以下爲宜。 添加之水量太少時烷氧基矽氧烷分子中的烷氧基無法地水 解,會有羥基生成量少之問題發生,10倍莫爾以上時雖 然可以減少殘存之烷氧基量,但反應完後必須自混合物中 除去多量之水,不合乎經濟原則。 上述陽離子交換樹脂的添加量係對1 0 0重量份烷氧 基矽氧烷及水的合計量,較佳爲0. 0 0 0 1〜3 0重量 份,更佳係0. 01〜1重量份。離子交換樹脂之量太多 時生成之矽烷醇基會進而縮合,無法得短鏈者,又.,太少 時則無法得水解時所需之充分活性。 反應時間係因使用之烷氧基矽氧烷,觸媒量等而異, 雖可以隨意設定,但時間太長時經由水解生成之矽氧烷會 被切斷其矽氧烷鍵,或引起矽烷醇基之縮合反應,生成不 適宜之環狀物,鏈長被延長之有機基矽氧烷,所以爲得短 鏈矽烷醇之矽氧烷,反應時間以5 0小時以內爲宜。 又,反應溫度亦可以隨意,惟太高之溫度下亦會起同 樣之反應,所以反應溫度係以8 0 °C以下,尤其在5 0 °C 以下實施爲宜。 另外,與說明二烷氧基矽烷之水解時所述之同樣理由 ,水解反應必須在充分地攪拌混合下進行,未充分攪拌混 合時有時無法均一地進行反應。 又,使用如上述水解式(3 )之二烷氧基矽烷所得式 (2 )之二烷氣基矽氧烷予以水解以得到含有矽烷醇之有 機基矽氧烷時,此式(2 )二烷氧基矽氧烷之水解雖可以 本紙張尺度通用中阐阐家標準(CNS &gt; Λ4現格(2ΐυχ;!97公釐)_ _ (請先閲讀背面之注意事項再填寫本頁)1 ~ 1 times Mohr water of the alkoxy group present in the dialkoxysilane molecule of the above formula (3) is added to the dialkylsilane represented by tT, and the first stage of hydrolysis can be performed by mixing. When it is easily obtained and continues to hydrolyze the dialkoxysilane of the formula (2) obtained as described above, a dialkyloxysilane such as a less expensive dimethoxydimethylsilane can be obtained in a simple method. Advantageously, for example, a low molecular weight organic polysiloxane represented by the following formulae (4) and (5) is obtained, and the present invention has been completed. R1 Printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs HO- ^ SiO) rH R 'R1 HO- (SiO) j-H I R1 (4) (5) (where R 1 is as defined above). Therefore, the present invention is to provide a low-molecular-weight sheet with a silanol group that is applicable to 1 national standard (CNS) specification (2) 0 × 297 Gongkang_ 7 _ 42 0685 printed by the Shellfish Consumer Cooperative of the China Standards Bureau of the Ministry of Economic Affairs A7 _ B7___ V. Description of the invention (5) A method for producing a quantity of organosiloxanes, which is characterized in that the above-mentioned alkane is added to the alkoxysiloxane represented by the above formula (1) in the presence of 1Ϊ ion exchange resin. Water of 1.0 times mole or more of alkoxy group of oxysiloxane, which is hydrolyzed by stirring. At this time, the present invention is provided as a preferred embodiment in the presence of a cation exchange resin, which is added to the dialkyl silane shown in the above formula (3), corresponding to the dialkoxy silane molecule of the above formula (3). 1 ~ 1 times Mohr's water of alkoxy group, and the first-stage hydrolysis is carried out by stirring to form a dialkoxychooxyalkane having an alkoxy group at the end represented by the above formula &lt; 2). In the presence of a cation exchange resin, a low molecular weight linear organic polysiloxane characterized by adding a stoichiometric excess of water to a dialkoxysilane of the above formula (2), and undergoing the second-stage hydrolysis by mixing. Method for producing alkane 0 The present invention will be described in more detail below. The method for producing a low-molecular-weight organic siloxane having a silanol group according to the present invention is to hydrolyze an alkoxysilane as described above in the presence of a cation exchange resin. Method. When the method according to the present invention is used, the condensation reaction of silanol can be inhibited to obtain a cyclic polysiloxane or a polyorganosiloxane having an extended chain length and having a low content, and a low molecular weight organosiloxane having a silanol group. That is, a method of hydrolyzing the alkoxysiloxane of the raw material to produce a corresponding hydroxysiloxane. Herein, the alkoxysiloxane is represented by the following formula (1). R1. (R2Q) bSi〇4-i. ^ (1) (Please read the notes on the back before filling out this page) This paper &amp; degree applies Chinese National Standard (CNS) Λ4 ^ grid (210X2 ^ 7 mm) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 420685 A7 __________ B7 Five 'Invention Description (6) At this time, R1 is a substituted or unsubstituted monovalent hydrocarbon group, preferably a carbon number of 1 to 10, especially 1 to 6. Specifically, it may be methyl, propyl, butyl, pentyl, hexyl, octyl, decyl, dodecyl and other alkyl groups: alkenyl such as vinyl; aryl groups such as phenyl and tolyl: p-benzene Aralkyl groups such as ethyl: and — groups in which some or all of the argon atoms bonded to the carbon atoms in these hydrocarbons are replaced by a prime atom such as fluorine or a cyano group (such as 3,3,3-trifluoropropane Or ethyl). Among them, methyl, vinyl and phenyl are preferred. In addition, r 2 is an alkyl group having 1 to 4 carbon atoms, preferably a methyl group, an ethyl group, and a rainer may be present in the molecule at the same time. In addition, a and b are numbers in the above range. The degree of polymerization of alkoxysiloxanes of the formula (1), that is, the number of silicon atoms in one molecule is preferably 2 to 5, especially 2 to 3. These alkoxysiloxanes are represented by the following formula (2 The dialkoxysiloxanes shown in) are most suitable for use. R1 RO- ^ SiO ^ R2 ^ ⑵ (where R1 and R2 are as defined above, and η is an integer of 2 to 5). Specific examples of the above alkoxysiloxanes may be 1,3-dimethoxytetramethyldisilazane, 1,1-dimethoxytetramethyldisilazane, and i-methoxypentamethyldisiloxane. Siloxane, 1,5-dimethoxyhexamethyltrisiloxane, 1,7-dimethoxyoctamethyltetrasiloxane, 3-methoxyheptamethyltrisiloxane, 1, 3— Dimethoxy_1,3-divinyl-1,3-dimethyldisiloxane and so on. These alkoxysiloxanes can be used alone or in combination. However, when a plurality of alkoxysiloxanes are used in combination, since the two papers are used, the paper is suitable for use (CN'S) Λ4 grid Uiox 297 mm) ^^ 1 ^^ 1 ^^ 1 I ^ I &gt; · (Please read the notes on the back before filling out this page}, 1T printed by the Consumers 'Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 4 2 06 85' A7 B7 V. Explanation of the invention (7) The solution speed is different, In some cases, it is not possible to react uniformly, so care must be taken. The alkoxysiloxanes of formula (1) can be reacted with R, C 5 b S i 0C4-ab in the presence of triethylamine, urea, pyridine, etc. according to known methods. / 2 (R1, a, b are as defined above) can be prepared by reacting with alcohols having an alkyl group corresponding to R2, especially the alkoxysiloxane of formula (2) can be Formula (3) Rl2Si (〇R2) 2 (3) (wherein R1,!? 2 is as described above)-the hydrolysis of the dialkoxysilane shown in the presence of a cation exchange resin is more suitable 〇 More detailed description by the formula ( 3) A method of hydrolyzing a dialkoxysilane to obtain a dialkoxysilane of formula (2). Specifically, the formula (3) dialkoxysilane can be, for example, dimethyldimethoxysilane, phenylmethyldimethoxysilane, methylvinyldimethoxysilane, dimethyldiethyl Oxysilane, phenylmethylmethoxyethoxysilane and the like are preferably dimethyldimethoxysilane. These dialkoxysiloxanes may be used alone or in combination. However, when a plurality of alkoxysiloxanes are used in combination, they may not react uniformly due to the different hydrolysis rates of the two, so care must be taken. In addition, it is preferable to use a small amount of a chlorine component for the dialkoxysiloxane based on the formula (3). That is, the short-chain silanols of the target substance of the present invention are unstable under acidic and alkaline conditions. In order to obtain short-chain silanols, they must remain neutral during the reaction and under reduced pressure distillation. Generally, the alkoxysilanes are The Chinese paper standard can be applied from the corresponding paper size {[, milk) 6 4 specifications (210 &gt; &lt; 297 mm) * iU &quot; (Please read the precautions on the back before filling this page) in the Ministry of Economic Affairs Consumption Cooperation of Employees of the Bureau of Substandard Production Du 420685 A7 __B7__ V. Description of the Invention (8) Chlorinated silane is synthesized, so if it contains chlorinated silane, these chlorinated silanes will react with water to form hydrochloric acid, so The reaction system becomes acidic, causing a poor silanol condensation reaction. Therefore, in order to obtain short-chain silanols, it is preferable to use a dialkoxysilane with a small content of chlorinated silane. Therefore, the chlorine component contained in the dialkoxysilane of the formula (3) is preferably 10 P pm or less, and preferably 10 ppm or less. Secondly, the water system used in the hydrolysis of the dialkoxysilane is used to remove Na, Ca, Mg and other ions by ion exchange resin, so that it is a component necessary for hydrolysis at a relatively low temperature and in the state of a large number of silanols, using conductivity. Ion-exchanged water having a rate of 10 1 Q Ω or more, preferably 10 1 2 Ω or more, and more preferably 10 15 Ω or more is most suitable for use. When the conductivity is less than 10 μMΩ, ion exchange resin and ions contained in the hydrolyzed water cause ion exchange, and the hydrolyzed water becomes acidic, which is not suitable. In addition, the cation exchange resin added to the mixture of the dialkoxysilane and ion-exchanged water is a component that keeps the D of the water to be hydrolyzed near neutrality, and gently hydrolyzes the necessary components. Here, the type of the cation exchange resin is preferably a suspension polymerization polymer made of polystyrene or divinylbenzene. The types of the cation exchange resins are gel type and macroporous type. These hollow systems are most suitable when they are measured by a mercury injection method and have a macroporous cation exchange resin having a pore size of 0.1 mm2 / g or more. The acidic group attached to the resin is preferably a sulfonate type such as a sulfonic acid group, an acrylic fluorenyl group, and the sulfonic acid group is more preferable. Ion exchange resins that can satisfy these conditions include, for example, Amberiist 15 (manufactured by Rohm and Haas), Diaion PK-208H, PK-216H, PK-228H (This paper rule applies to China National Standard (CNS) Λ4 gauge pile (2丨 0 X 297 mm) i. (Please read the notes on the back before filling in this page) Order 4 2 06 85 A7 Printed by the Consumers ’Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs ________ B7______ 5. Description of the invention (9) The above are manufactured by Mitsubishi Chemical Corporation) Peuro 丨 ite CT — 1 7 5 'CT_ 1 7 1, CT-1 169 (the above are manufactured by Peuro 丨 ite Corporation), etc., especially the PeurolUe CT — 1 7 5 (made by Peuro 丨 ite Corporation) ) Is preferably 0 in the hydrolysis of dialkoxysilanes of the above formula (3), the water used in the hydrolysis of the above formula (3) dialkoxysilanes in the molecule of the alkoxy group is 0.1 times mole ~ 1 times Moore, 0.2 ~ 0. 6 times more than Moore. 〇1. When it is less than 1 mole, the hydrolysis cannot be performed sufficiently, and a large amount of raw material alkoxysilane is not suitable. When it is more than 1 mole, the formula (2) dialkoxysilane cannot be obtained, and it becomes hydroxysilane. The hydroxyalkoxy group cannot efficiently produce a low molecular weight organosiloxane having a silanol group. 01〜1。 Also, the amount of cation exchange resin is added to 100 parts by weight of the above formula (3) dialkoxysilane and the total amount of hydrolyzed water is 0. 0001 ~ 30 parts by weight, especially from 0.01 to 1 Part by weight is preferred. If the amount of the ion exchange resin is more than 30 weight, the generated silanol groups will be promoted to condense, and sometimes short-chain chains cannot be obtained, and it is 0. Ί] 0 0 1 Fully hydrolyzed. In addition, the hydrolysis reaction time of dialkoxysilane can be arbitrary, but when it is too long, the siloxane bond of dialkoxysiloxane generated by hydrolysis will be cut off, and a bad ring will be formed .. . Siloxane with a long chain length, so in order to obtain short-chain dialkoxysiloxanes, a reaction time of less than 50 hours is appropriate. In addition, the reaction temperature can usually be room temperature. When the temperature is too high, the same reaction occurs. The reaction temperature is below 50 ° C, especially below 25. Implementation of this standard &gt; A4 size (2 丨 0X297 common stitching) ~~~ * '~~' • 1 ^---Γ --.------------ Order (please read the precautions on the back first) (Fill in this page again.) Consumption cooperation between employees of the Central Bureau of Standards, Ministry of Economic Affairs, Du Yinze 4 2 06 85 'A7 B7 V. Description of the invention (10) should be 0 The hydrolysis reaction of dialkoxysilanes of formula (3) above is based on dialkane Hydrolyzed by cation exchange resin in the presence of silane and water, the initial stage of hydrolysis is separated into the dialkoxysilane phase and water phase. With the hydrolysis, water is consumed and alcohols are formed to make the system uniform. Ion-exchange resin-based solids cannot be dissolved in solution, and the reaction proceeds on the surface of the solid. Therefore, when the mixture is not sufficiently mixed, a uniform reaction may not be performed. For this reason, the reaction must be performed while stirring and mixing thoroughly. In the presence of an exchange resin, the above formula (.3) dialkoxysilane and When the amount of alkoxy group is from 0.1 to 1 mol of water, a dialkoxysiloxane represented by the above formula (2) having a chain length of 2 to 5 having an alkoxy group at the end can be obtained, and hydrolyzed by A mixture of by-products such as alcohols produced. The above-mentioned mixture can be easily separated into alkoxysiloxanes of the desired chain length by operations such as distillation if necessary. For example, dimethoxydimethyl Silane is used as a raw material, and 0.3 times mole of alkoxy is used. The reaction mixture obtained by the present invention is different due to reaction conditions, and usually contains 50% 1, 3-dimethoxytetramethyldisilazane. Oxane, 2 5% 1, 5-dimethoxyhexamethyltrisiloxane, 6% 1, 7-dimethoxyoctamethyltetrasiloxane, 2% 1, 9 _dimethyldeca Methylpentasiloxane. The rest are unreacted dimethoxydimethylsilane. These dimethoxysiloxanes with different chain lengths can be separated by distillation. In addition, after the reaction is completed, the catalyst is hydrolyzed. The cation exchange resin can be easily removed by filtering. This paper size is applicable to the Chinese standard (CNS) A4 (210χ2 &lt; ^ 7mm) ) _ Η-— (Please read the notes on the back before filling out this page) Printed by the Central Standards Bureau of the Ministry of Economic Affairs and Consumer Cooperatives 420685, A7 ____B7_V. Description of the invention (11) Therefore, the present invention is based on ion exchange resin In the presence, hydrolyze the alkoxysiloxane represented by the formula (1) of the dialkoxysiloxane of the formula (2) obtained above to obtain a low-molecular-weight organic siloxane having a silanol group. Use at this time For the same reason as for the above-mentioned reason, the alkoxysiloxane is preferably the one having a chlorine component of 100 ppm or less, especially 10 ppm or less. In addition, as the water used for the hydrolysis is an organic siloxane having a cyclic siloxane, and the chain length is extended, ion-exchanged water such as N a, C a, Mg or the like is generally used with an ion exchange resin or the like. Distilled water containing this plasma. If the ionic substance is contained in the hydrolyzed water as described above, it will undergo ion exchange with an ion exchange resin used as a hydrolysis catalyst, such as H + of a sulfonic acid group, to make the hydrolyzed water acidic. For this reason, the short-chain silanols generated after hydrolysis cannot be stably present, and sometimes unsuitable cyclic polysiloxanes and organosiloxanes with extended chain lengths are sometimes formed. Therefore, the conductivity of the hydrolyzed water is preferably 101 (MΩ) or more, more preferably 1012MΩ or more, and most preferably 1015MΩ or more. On the other hand, cation exchange resins can keep the hydrolyzed P Η 値 neutral, while causing mild hydrolysis. The cation exchange resin can be used as a hydrolysis catalyst to prevent condensation and other condensation The cation exchange resin can be the same as the cation exchange resin used in the hydrolysis of the dialkoxysilicone. The amount of water used in the above hydrolysis is equal to or more than 1 mole of the alkoxy group in the alkoxysiloxane, and it is preferable that the amount of water is more than 1 mole of the stoichiometry. CNS) Λ4 specification (21〇 × 29ΐmm) _- (Please read the notes on the back before filling in this page) Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 4 2 Π 6 85 'k Α7 Β7 V. Description of the invention (12) It is an excess, and it is preferably 10 times the mole or less, especially 5 times the mole or less. When the amount of water added is too small, the alkoxy group in the alkoxysiloxane molecule cannot be hydrolyzed, and a problem of a small amount of hydroxyl groups occurs. Although the amount of residual alkoxy groups can be reduced when the amount is more than 10 times the mole, the reaction It is not economical to remove a large amount of water from the mixture afterwards. 01〜1 重量。 The cation exchange resin is added in an amount of 1 0 0 parts by weight of the total amount of alkoxysiloxane and water, preferably 0. 0 0 0 1 ~ 3 0 parts by weight, more preferably 0. 01 ~ 1 weight Serving. When the amount of the ion exchange resin is too large, the silanol group formed will be further condensed, and short-chain ones cannot be obtained, and when it is too small, sufficient activity required for hydrolysis cannot be obtained. The reaction time varies depending on the alkoxysiloxane used, the amount of catalyst, etc. Although it can be set arbitrarily, the siloxane formed by hydrolysis when the time is too long will cut its siloxane bond or cause silane. The condensation reaction of alcohol groups produces unsuitable cyclic materials and organosiloxanes with extended chain lengths. Therefore, to obtain short-chain silanols, the reaction time is preferably within 50 hours. In addition, the reaction temperature can be arbitrary, but the same reaction will occur at too high a temperature, so the reaction temperature is preferably below 80 ° C, especially below 50 ° C. In addition, for the same reason as described in the explanation of the hydrolysis of dialkoxysilane, the hydrolysis reaction must be performed with sufficient stirring and mixing, and the reaction may not proceed uniformly when the stirring and mixing are insufficient. In addition, when the dialkoxysilane of the formula (2) obtained by hydrolyzing the dialkoxysilane of the formula (3) is hydrolyzed to obtain an organosiloxane containing a silanol, the formula (2) Although the hydrolysis of alkoxysiloxane can be interpreted in the paper standard (CNS &gt; Λ4 now (2ΐυχ;! 97mm)) _ _ (Please read the precautions on the back before filling this page)

,1T 420685 A7 B7 五、發明説明(13 ) 在式&lt; 3 )二烷氧基矽烷水解後不必特別分離精製式(2 )之烷氧基矽氧烷,水解此化合物與副生物之混合物亦可 得鏈長η爲2〜5之末端上具有羥基的矽氧烷,惟藉由蒸 餾等方法自上述第一階段之水解混合物中分離出鏈長度爲 可對應於所欲鏈長之二羥基矽氧烷的二烷氧基矽氧烷後, 以過量之水進行水解,藉此即可得到純度極佳之ΗΟ - &lt; S i RSO) η— Η (η二2〜5 )所示目的物。例如藉 由蒸嬸自如上述以二甲氧基二甲基矽烷爲原料予以水解所 得含5 0% 1 ,3—二甲氣四甲基二矽氧烷之二烷氧基 矽氧烷混合物分離出1 ,3 —二甲氧四甲基二矽氧烷,繼 而予以水解即可得高純度白色結晶之1 ,3 —二羥四甲基 二矽氧烷。又,本發明中所得有機基矽氧烷係η == 2之二 聚物二醇,η == 3之三聚物二醇最爲有用。 經濟部中央標準局員工消費合作社印&quot; (請先閲讀背面之注意事項再填寫本頁} 上述反應完後除去陽離子交換樹脂。水解觸媒之陽離 子交換榭脂可以用過濾等方法極輕易地自反應混合物中除 去。自系內除去陽離子交換樹脂即可以停止水解及矽烷醇 之縮‘合反應,所以不必添加鹼等中和劑。即,本發明中之 一種實施形態係使用磺醯基於二乙烯基共聚物等之苯環所 成者做爲陽離子交換樹脂。此苯環中因化學結合有磺醯基 ,反應中此等磺醯基不會溶於反應溶液,反應溶液可以保 有中性。又,以過濾除去離子交換樹脂時可以中止水解反 應。因此過濾後之反應混合物中並不包含酸性物質者。 另外,自反應混合物中分離之陽離子交換樹脂並不不 需特別處理,例如不必施予再生等操作即可再使用做爲水 本紙張尺度適用中國國家標準(CNS ) Λ4規格(2U)xm公釐_ μ ^ 經濟部中央標準局員工消費合作社印製 420685 A7 B7 五、發明説明(14 ) 解觸媒。 其次,反應混合物係被汽提,被除去醇類以及殘留下 之少暈水等揮發成份,這時最好爲所欲之矽烷醇不會被汽 提之條件爲宜,汽提壓力雖可以隨意決定,但溫度則考慮 矽烷醇之安定性,以8 0°C以下爲宜。 依本發明之製造方法時,可在極佳收率下獲得具有矽 烷醇末端基之低分子置,尤其含有二聚物二醇,三聚物二 醇之直鏈狀有機基矽氧烷,此有機基矽氧烷係製造聚矽氧 橡膠物料時有效地利用做爲分散劑。 以下藉由實施例,比較具體說明本發明,惟本發明並 不受以下實施例所限制自不待言。 實施例1 二甲氣基二甲基矽烷之水解 (第一階段之水解) 在具備溫度計,攪拌葉片之以N 2置換的 2 0Ό Omi燒瓶中,於2 0 0 g二甲氧基二甲基矽烷( 含氯量5ppm)中添加17. 8g (對烷氧基爲 0 . 3 0莫爾)之導電率爲1 Ο 15ΜΩ的離子交換水,形 成爲二相系。在此添加1. 〇g(〇. 4 6重量%)陽離 子交換樹脂(CT — 1 7 5,Peuroiite公司製),於 2 0°C攬拌4 0分鐘,結果溶液相成爲均—。再繼績燙拌 4小時。藉由氣相層析分析,結果此反應混合物中含有 11. 1%未反應之二甲氧基二甲基矽烷,5 0. 0 % 本紙張尺度適州中國國家標牟(C’NS ) Λ4規格(210X 297公釐)~~~ —17 - (請先閒讀背面之注意事項再填寫本頁) 訂 A7 B7 420685 五、發明説明(15 ) 1 ,3 —二甲氧基四甲基二矽氧烷,25_ 1 % 1 ,5 —二甲氧基六甲基三矽氧烷,6. 1% 1 ,7 —二甲氧 基八甲基四矽氧烷,1· 7% 1 ,9 —二甲氧基十甲基 五妙氧焼。 (第二階段之水解) 繼而在上述反應混合物中加入1 2 5 g ( 6 . 9 4莫 爾)導電率爲1 〇15ΜΩ之離子交換水,撹拌5 0分鐘° 經由過濾除去固體之離子交換樹脂後,於5mm ifg ’ 5 0 eC條件下除去副生之甲醇,水等,結果得1 D 9 g無 色透明之液體。藉由氣相層析分析之結果,獲知其中含有 3. 1 % 二羥二甲基矽烷,45. 1% i,3 —二羥 四甲基二矽氧烷,2 0. 5% 1 ,5-二羥六甲基三矽 氧烷,5. 5 % 1 ,7-二羥八甲基四矽氧烷,1. 7 % 1 ,9 —二羥十甲基五矽氧烷。 實施例2 二甲氧基甲基乙烯基矽烷之水解 (第一階段之水解) 在具備溫度計,攪拌葉片之WN2置換的 2 0 Omj?燒瓶中,於2 0 . 〇 g二甲氧基甲基乙烯基矽 烷(含氯量5ppm)中添加1. 6 2g (對烷氧基爲 0 . 3 0莫爾)之導電率爲1 〇 的離子交換水,形 成爲二相系。在此添加〇, l〇g(〇. 46重量%)陽 本紙诙尺度適用中國國家標隼(CNS ) Μ規格(2]〇X 297公煃)10 1〇 訂 (讨先閉讀背面之注意事項再填寫本頁)1T 420685 A7 B7 V. Description of the invention (13) It is not necessary to specifically separate and refine the alkoxysilane of the formula (2) after the hydrolysis of the formula &lt; 3) dialkoxysilane, and the mixture of the compound and the parabiotic is also hydrolyzed. Siloxane having a hydroxyl group at the end of a chain length η of 2 to 5 can be obtained, but a dihydroxysilicone having a chain length corresponding to a desired chain length can be separated from the hydrolysis mixture in the first stage by means such as distillation. After the dialkoxysiloxane of hydroxane is hydrolyzed with an excess of water, a target compound represented by ΗΟ-&lt; S i RSO) with excellent purity can be obtained. . For example, by distilling from a dialkoxysilane mixture containing 50% 1, 3-dimethoxytetramethyldisilazane, which is hydrolyzed using dimethoxydimethylsilane as a raw material, as described above, the mixture is separated. 1,3-Dimethoxytetramethyldisilaxane, and then hydrolyzed to obtain 1,3-dihydroxytetramethyldisilaxane with high purity. In addition, the organosiloxane-based dimer diol of η == 2 and the trimer diol of η == 3 obtained in the present invention are most useful. Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling in this page) After the above reaction, remove the cation exchange resin. The cation exchange resin of the hydrolysis catalyst can be easily filtered by other methods. Removed from the reaction mixture. Removing the cation exchange resin from the system can stop the hydrolysis and condensation reaction of silanol, so it is not necessary to add a neutralizing agent such as a base. That is, one embodiment of the present invention uses sulfonium based on diethylene The benzene ring formed by the base copolymer is used as a cation exchange resin. Since the benzene ring is chemically bonded with a sulfofluorene group, these sulfofluorene groups will not dissolve in the reaction solution, and the reaction solution can remain neutral. The hydrolysis reaction can be stopped when the ion exchange resin is removed by filtration. Therefore, the reaction mixture after filtration does not include acidic substances. In addition, the cation exchange resin separated from the reaction mixture does not need special treatment, such as regeneration. Can be re-used after waiting for operation. The paper size is applicable to China National Standard (CNS) Λ4 specification (2U) xm. _ μ ^ Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 420685 A7 B7 V. Description of the invention (14) Dissolve the catalyst. Second, the reaction mixture is stripped to remove alcohols and the remaining volatile components such as halo and water. At this time, it is better that the desired silanol is not stripped. Although the stripping pressure can be arbitrarily determined, the stability of the silanol is considered at the temperature, which is preferably 80 ° C or lower. According to the present invention In the manufacturing method, a low molecular weight silanol terminal group can be obtained in an excellent yield, especially a linear organic siloxane containing dimer diol and trimer diol. This organic silicon The siloxane is effectively used as a dispersant when manufacturing the silicone rubber material. The present invention will be described in more detail with reference to the following examples, but the present invention is not limited by the following examples. Hydrolysis of Gas-Based Dimethyl Silane (First Stage Hydrolysis) In a 20mi Omi flask equipped with a thermometer and stirring blades and replaced with N 2, 200 g of dimethoxydimethylsilane (chlorine content) 5ppm) was added to 17.8g (p-alkoxy 0.30 Moore) ion-exchanged water having a conductivity of 10 15MΩ to form a two-phase system. 1.0 g (0.46% by weight) of a cation exchange resin (CT — 1 7 5) was added here. 1% ,, Peuroiite company), stirred at 20 ° C for 40 minutes, the solution phase became homogeneous. After another 4 hours of hot stirring. By gas chromatography analysis, the reaction mixture was found to contain 11. 1% Unreacted dimethoxydimethylsilane, 5 0. 0% This paper is suitable for China's National Standard (C'NS) Λ4 size (210X 297 mm) ~~~ —17-(Please read first Note on the back, please fill in this page again) Order A7 B7 420685 V. Description of the invention (15) 1, 3-dimethoxytetramethyldisilazane, 25-1% 1, 5-dimethoxyhexamethyl Trisiloxane, 6.1% 1, 7-dimethoxyoctamethyltetrasiloxane, 1.7% 1, 9-dimethoxydecylpentaoxamine. (Hydrolysis in the second stage) Then, 1.25 g (6.94 Moore) of ion-exchange water having a conductivity of 1015MΩ was added to the above reaction mixture, and stirred for 50 minutes. The ion-exchange resin was filtered to remove solids. Then, the byproduct methanol, water and the like were removed under the condition of 5mm ifg '50 eC, and 1 D 9 g of colorless and transparent liquid was obtained. According to the results of gas chromatography analysis, it was found that it contained 3.1% dimethylol dimethylsilane, 45.1% i, 3-dihydroxytetramethyldisilazane, 20.5% 1, 5 -Dihydroxyhexamethyltrisiloxane, 5.5% 1, 7-Dihydroxyoctamethyltetrasiloxane, 1. 7% 1, 9-Dihydroxydecamethylpentasiloxane. Example 2 Hydrolysis of Dimethoxymethyl Vinyl Silane (First Stage Hydrolysis) In a 20 Omj? Flask equipped with a thermometer and a stirring blade of WN2 substitution, 20 g of dimethoxymethyl Ionic exchange water having a conductivity of 10 was added to vinyl silane (containing 5 ppm of chlorine) at an amount of 1.6 2 g (0.3 mol for alkoxy group) to form a two-phase system. Add 0.10 g (0.46% by weight) of this paper to the Chinese standard (CNS) M specification (2) 0X 297 gong) 10 10 order (discussion of the back reading first) (Fill in this page again)

經濟部中央標隼局負工消費合作社印狀 4 2 06 85 一 A7 B7 五、發明説明(16 ) 離子交換樹脂(CT 一 1 7 5,Peurolite公司製),於 2 0°C撹拌4 G分鐘,結果溶液相成爲均一。再繼績攪泮 4小時。藉由氣相層析分析,結果此反應混合物中含有 8. 1 %未反應之二甲氧基甲基乙稀基砂焼,4 5. 9% 1 ,3 —二甲氧基一1 ,3 —二乙嫌基—1 ,3 —二甲 基二矽氧烷,28. 8% 1 ,5 —二甲氧基一 ;[,3, 5 —三乙烯基—1 ,3,5-三甲基三矽氧烷,7. 9% 1 ,7 —二甲氧基一1 ,3 ,5 ,7 —四乙嫌基一1 , 3,5,7 —四甲基四矽氧烷,2. 9% 1_,9._二甲 氧基一1,3,5,7,9 —五甲基 _1,3,5,7, 9 —五甲基五矽氧烷。 (第二階段之水解) 繼而在上述反應混合物中加入1 2. 0 g ( 〇. 6 6 7莫爾)導電率爲1〇15^10之離子交換水,攪 拌4 0分鐘。經由過濾除去固體之離子交換樹脂後,於5 mmHg,5 Q°C條件下除去副生之甲醇,水等,結果得 (請先閱讀背面之注意事項再填寫本頁) -a 經濟部中央標準局員工消費合作it印製 , , -—&lt; 基 9 果 1 I , 烯, 結 I 基烷乙 1 之,基羥氧四 析烷烯二矽 1% 分矽乙 I 三 7 5 析基二 5 基 , 層嫌 I ,甲 5 2 相乙 3 1 三 ,, 氣基, I 3 烷 由甲 1%5 ,氧 .藉基 i 8 , 1 砂 。 羥基 3 | 四 體二羥 5 ,基基 液 二 2 1 羥甲 之%_ , _ 二四 明 3 3 院基 | 一 透 .,氧嫌 7 7 色 2 一—_ 较 乙,, 無有 二三 1 5 g 含%基 I , 3 中 3 甲 5%3 其.二 1 知 1 I 1SI4 3Printed by the Central Bureau of Standards, Ministry of Economic Affairs, Consumer Cooperatives 4 2 06 85 1 A7 B7 V. Description of the invention (16) Ion exchange resin (CT 1 75, manufactured by Peurolite), mixed for 4 G minutes at 20 ° C As a result, the solution phase becomes homogeneous. Stir for another 4 hours. Analysis by gas chromatography revealed that the reaction mixture contained 8.1% unreacted dimethoxymethylethenyl oxalate, 45.9% 1, 3-dimethoxy-1, 3 —Diethoxy-1,3-dimethyldisilaxane, 28.8% 1, 5-dimethoxy-1; [, 3, 5-trivinyl-1,3,5-trimethyl Trisiloxane, 7.9% 1,7-dimethoxy-1,3,5,7-tetraethanyl-1, 3,5,7-tetramethyltetrasiloxane, 2. 9% 1_, 9._dimethoxy-1,3,5,7,9-pentamethyl_1,3,5,7,9-pentamethylpentasiloxane. (Hydrolysis in the second stage) Then, 12.0 g (0.667 Moore) of ion-exchanged water having a conductivity of 1015 ^ 10 was added to the above reaction mixture, and stirred for 40 minutes. After removing the solid ion exchange resin by filtration, the byproduct methanol, water, etc. were removed under the conditions of 5 mmHg, 5 Q ° C. (Please read the precautions on the back before filling this page) -a Central Standard of the Ministry of Economy It is printed by the bureau's consumer cooperation,--&lt; radical 9 I 1 alkene, alkene, alkane 1 alkane 1 1, hydroxytetradecane siloxane 1%, silicon I 3 7 5 5 radicals, layer I, methyl 5 2 phase, ethyl 3 1 tris, gas radical, I 3 alkane from methyl 1% 5, oxygen. Boryl i 8, 1 sand. Hydroxyl 3 | tetrasodium dihydroxy 5, base liquid 2 2 1% of hydroxymethyl _, _ tetramethamine 3 3 Yuanji | one through., Oxygen is 7 7 color 2 one —_ more than B, no two Three 1 5 g containing% I, 3 of 3 A 5% 3 Its. 2 1 Know 1 I 1SI4 3

♦.我浪&lt;度適州巾國囷家標隼(CNS ) Λ4規格(210X297公釐)_ 19 - 經濟部中央標準局β:工消費合作社中裝 4^06 85 , A7 B7 —___五、發明説明(17 ) 一二羥基一 1 ,3 ,5 ,7 ,9 一五甲基一 1 ,3 ,5, 7 ,9 一五甲基五矽氧烷。 實施例3 依實施例1之方法進行第一階段水解’完後予以蒸飽 ,自反應混合物中分離1 ,3 _二甲氧基四甲基二矽氧燒 ,如以下進行第二階段之水解。 (第二階段之水解) 在1 0. 〇g 1 ,3 —二甲氧基四甲基二矽氧烷中 加入2 . 0 g導電率爲1 0 15ΜΩ之離子交換水,在其中 加入0. 0 3 0g陽離子交換樹脂(CT-17 5) Peurolite公司製),於2 0°C搅拌8 0分鐘。經過濾除 去固體之離子交換樹脂後,於5mniHg,5 0°C條件下 除去副生之甲醇,水等,結果得7. 7g白色結晶。予以 氣相層析分析之結果獲知含有8 8 · 2 % 1 ,3 -二羥 四甲塞二矽氧烷。 實施例4 依實施例1之方法進行第一階段水解,完後予以蒸餾 ,自反應混合物中分離1 ,5 —二甲氧基五甲基三矽氧烷 ,如以下進行第二階段之水解。 (第二階段之水解) (請先閱讀背面之注意事項再填寫本莧)♦. Wolang &lt; Dushizhou National Standard (CNS) Λ4 Specification (210X297 mm) _ 19-Central Standards Bureau of the Ministry of Economic Affairs β: Industrial and consumer cooperatives 4 ^ 06 85, A7 B7 —___ V. Description of the invention (17) A dihydroxy-1,3,5,7,9 pentamethyl-1,3,5,7,9 pentamethylpentasiloxane. Example 3 The first-stage hydrolysis was carried out according to the method of Example 1. After completion of the hydrolysis, the 1,3-dimethoxytetramethyldisilazol was separated from the reaction mixture, and the second-stage hydrolysis was performed as follows. . (Second-stage hydrolysis) In 10.0 g of 1,3-dimethoxytetramethyldisilazane, 2.0 g of ion-exchanged water having a conductivity of 10 15MΩ was added, and 0. 0 3 0 g of a cation exchange resin (CT-17 5) manufactured by Peurolite, was stirred at 20 ° C. for 80 minutes. 7g 白晶。 After removing the solid ion exchange resin by filtration, the byproduct methanol, water, etc. were removed under the conditions of 5mniHg, 50 ° C, and 7.7 g of white crystals were obtained. As a result of gas chromatography analysis, it was found that it contained 8 8% 1, 3-dihydroxytetramethyldisilazane. Example 4 The first-stage hydrolysis was carried out according to the method of Example 1, and after the completion of the distillation, 1,5-dimethoxypentamethyltrisiloxane was separated from the reaction mixture, and the second-stage hydrolysis was performed as follows. (Second stage of hydrolysis) (Please read the notes on the back before filling in this card)

ltT 本紙張尺度適用中國國家橾準(CM ) Λ4規格(2丨0:&lt;2刃公釐) 20 經濟部中央標準局員工消费合作社印製 42U685 A7 _B7____ 五、發明説明(18 ) 在10. 0g 1,5 —二甲氧基五甲基三矽氧烷中 加入2. 0 g ( 0 . Ill莫爾)導電率爲1015ΜΩ之 離子交換水,在其中加入(3. 0 30 g陽離子交換樹脂( C T - 1 7 5 ) Peurolite 公司製),於 2 0°C 攪拌 1 5 0分鐘。經過濾除去固體之離子交換樹脂後,於 5mmHg,5 0°C條件下除去副生之甲醇,水等,結果 得8. 0無色透明液體。予以氣相層析分析之結果獲知含 有9 0. 5% 1 ,5 —二羥五甲基三矽氧垸。 實施例5 直接再次使用實施例1之經過濾分離之離子交換樹脂 做爲水解觸媒,以實施例1 —樣之方法進行水解。 重覆此方法1 0次後,以氣相層析分析所得水解物, 結果獲知含有2. 5%二羥二甲基矽烷,44. 0% 1 ,3 —二羥四甲基二矽氧烷,2 0. 1 % 1 ,5_二羥 五甲基三矽氧烷,4. 4% 1 ,7-二羥八甲基四矽氧 烷,‘1. 3 % 1 ,9 一二羥十甲基五矽氧烷。 由此實施例之結果可知,本發明中使用過之陽離子交 換樹脂係不必施予特別之再生等處理即可回收,再使用。 比較例1 在具備有溫度計,搅拌器,以N 2取代之5 OmJ?燒 瓶中,在2 0. 0 g ( 0 . 16 6莫耳)二甲氧基二甲基 矽烷中添加調整爲p Η値4 . 2之6 . 5 8 g ( 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨0X297公疮) _ 2丄- (請先閱讀背面之注意事項再填寫本頁) 訂 42ub85 .' A7 B7__ 五、發明説明(19 ) Ο . 3 6 6莫爾)鹽酸水,即達到4 0 eC之最高溫度,成 爲均一之溶液。繼績攬拌5分鐘後,加入〇. 2s ( 4. 9 6X1 0_3 莫爾)氧化鎂,及 1 5g (0 12 5 莫爾)硫酸鎂,攪拌3小時。過濾此油狀物後於2 0°C, 5 mm H g壓力下汽提。以氣相層析分析此油狀物時獲知 含有15. 7% 1,3 —二羥四甲基二矽氧烷, 24. 5 % 1 ,5 -二羥五甲基三矽氧烷,15· 1 % 1 ,7_二羥八甲基四矽氧烷,9. 3%之1. 9 一二 羥十甲基五矽氧烷。 此比較例之方法中係引起矽烷醇基之縮合,與上述實 施例相比較短鏈矽烷醇之1,3 —二羥四甲基二矽氧烷的 生成量顯然較低,又,此方法中雖可得羥基化合物之混合 物,但自此混合物很難分離出所欲鏈長之羥基化合物。 比較例2 經濟部中央標準局員工消費合作杜印製 j - 11 ^^—^1 1, ^^^1 ^^^1 ^^^1 ^^^1 ^^^1 ^^^1 (請先閲讀背面之注意事項再填寫本頁) 在具備有溫度計,攪拌器,以N 2取代之5 Omj?燒 瓶中、在10. Og(〇. 514莫耳)1’ 3 -二甲氧 基四甲基二矽氧烷中添加調整爲pH値4. 2之2. 0g (〇 . G 1 1 1莫爾)鹽酸水,即達到4 0 °C之最髙溫度 ,成爲均一之溶液。繼績攪拌8分鐘後,加入〇. lg( 2. 48X10-3莫爾)氧化鎂,及3g(0. 025莫 爾)硫酸鎂,攪拌1小時。過濾此油狀物後於2 0 ,5 mm H g壓力下汽提。以氣相層析分析此油狀物時獲知含 有1 6. 3 % 1 ,3 —二羥四甲基二矽氧烷,25. 5 本紙張尺度適用中國國家標準(CNS ) A4規格(2IOX 297公釐)_ 2 - 420685 ·ν Λ7 B7 五、發明説明(20 ) % 1,5 —二羥五甲基三矽氧烷,23. 8% 1,7 —二羥八甲基四矽氧烷,8. 6%之1. 9_二羥十甲基 五矽氧烷。 此比較例之方法中係引起矽烷醇基之縮合,與上述實 施例相比較短鍵矽烷醇之1,3 _二羥四甲基二矽氧烷的 生成置顯然較低,又,此方法中雖可得羥基化合物之混合 物,但自此混合物很難分離出所欲鏈長之羥基化合物。 實施例6 二甲氣某二甲某矽烷之水解 (第一階段之水解) 在具備溫度計,搅拌葉片之以&gt;12置換的2 0 Omj? 燒瓶中,於2 0. Og二甲氧基二甲基矽烷(含氯量 5ppm)中添加1.19g(對烷氧基爲0. 2莫爾) 之導電率爲1 〇15ΜΩ的離子交換水,形成爲二相系。在 此添加0. 10g(0. 4 6重量%)陽離子交換樹脂( 經濟部中央標準局負工消費合作社印製 (請先閱讀背面之注意事項再填寫本I ) CT1一 1 7 5,Peurolite 公司製),於 2 0°C 攬拌 4 0 分鐘。結果溶液相成爲均一。再繼續攬拌4小時。藉由氣 相層析分析,結果此反應混合物中含有3 3. 2 %未反應 之二甲氧基二甲基矽烷,4 5. 4% 1 ,3 —二甲氧基 四甲基二矽氧烷,1 2. 8% 1 ,5 —二甲氧基六甲基 三矽氧烷,2. 5 % 1,7 -二甲:氧基八甲基四矽氧烷 ,0. 6 % 1 ,9~二甲氧基十甲基五矽氧烷。 本紙张尺度適用t阐闼家標準(CNS ) A4规格(210X297公釐)_ 42 0685 A7 B7 經濟部t央標準局員工消費合作社印裝 五、發明説明(21 ) (第二階段之水解) 繼而在上述反應混合物中加入1 2 . 5 g導電率爲 1 015ΜΩ之離子交換水,攪拌4 0分鏵。經由過濾除去 固體之離子交換樹脂後,於5mmHg,5 0°C條件下除 去副生之甲醇,水等,結果得11. 0&amp;無色透明之液體 。藉由氣相層析分析之結果,獲知其中含有2 5. 7 % 二羥二甲基矽烷,4 3. 0% 1 ,3 —二羥四甲基二矽 氧烷,1 3. 5% 1 ,5 —二羥四甲基三矽氧烷, 2. 4 % 1,7 —二羥八甲基四矽氧烷,〇. 6·% 1 ,9 一二羥十甲基五矽氧烷。 寅施例7 除將實施例6中使用於第一階段水解的離子交換水量 改爲3. Og (對烷氧基爲0. 5倍莫爾)以外’其他均 一樣水解。結果反應混合物中含有2· 1 %二甲氧基二甲 基矽烷,4 8. 9 % 1 , 3 一二甲氧基二甲基二矽氧烷 ,2*9. 1 % 1 ,5 -二甲氧基六甲基三矽氧垸, 8 . 8 % 1 ,7_二甲氧八甲基四矽氧烷’ 2· 2% 1 ,9 —二甲氧十甲基五矽氧烷。 其次,與實施例6 —樣進行第2階段之水解,結果得 11. 6%無色透明液體,其中含有〇· 9%二徑二甲基 矽烷,4 6. 3 % 1,3 —二羥四甲基二较氧院’ 28. 0 % 1,5 —二羥六甲基三砂氧院’9- 1 % 1,7-二羥四甲基四矽氧烷,3. 0 % 1,9 — 一翔 τ - 來 1-IT {請先閲讀背面之注意事项再填寫本頁) 本紙张足度適用中國國家標皁(CNS )八4故格(210X297公釐)_ 24 - 420685 A7 B7 經濟部中央榇準局員工消費合作社印製 五、發明説明(π ) 十甲基五矽氧烷。 比較例3 除將實施例6中使用於第一階段之水解的離子交換水 量改爲8. 9% (對烷氧基爲1. 5倍莫爾)以外,其他 均一樣水解,結果反應混合物中含有70. 1 % 二羥二 甲基矽烷,8. 5% 1 ,3-二羥四甲基二矽氧烷, 3.2% 1 ,5_二羥六甲基三矽氧烷,12. 5% 羥基甲氧基二甲基矽烷,3. 0% 1_羥基一3._甲氧 基四甲基二矽氧烷。 如上述,在第一階段水解時若使用對烷氧基矽烷之烷 氧基爲化學計量上過量之水時,幾乎不會生成二烷氧基矽 氧烷,而會生成爲羥基化合物。這時1,3 -二羥四甲基 二矽氧烷之收量少,且很難且如上述羥基化合物混合物中 分離所欲鏈長之矽氧烷。 實施例8 在具備溫度計,搅拌葉片之&amp;N2置換的 50m又燒瓶中,於10. 0g(0. 0458倍莫爾) 1 ,5 —二甲氧基一1 ,5 —二乙烯基二甲基二矽氧烷中 添加8g(0. 10莫爾)之導電率爲1〇15ΜΩ的 離子交換水。在此添加0. 3 0g陽離子交換樹脂(CT —1 7 5,Peurolil:e公司製),於2 0°C携伴8 0分鐘 。經由過濾除去固體之離子交換樹脂後,於5mmHg, 本紙張尺度適用中國國家標隼(CNS ) Λ4規格(210X297公釐)_ - (讀先閱讀背面之注意事項再填寫本頁) 訂 A7 B7 420685 五、發明説明(23 ) 5 0°C條件下除去副生之甲醇,水等,結果得7. 6g白 色結晶。藉由氣相層分析之結果,獲知其中含有8 0 . 3 (請先閱讀背面之注意事項再填寫本頁) % 1 ,5 —二羥基一1 ,5 —二乙烯基二甲基二矽氧院 Ο 實施例9 在具備溫度計,攪拌葉片之ΗΝ2置換的5 Om又燒 瓶中,於10. 0g(0. 514莫爾)1,1-二甲氧 基四甲基矽氧烷中添加2. 0 g ( 0 . 111莫爾.)之導 罨率爲1015ΜΩ的離子交換水。在此添加〇. 〇30g 陽離子交換樹脂(CT — 1 7 5,Peurolite公司製), 於2 0°C攪拌8 0分鐘。經由過濾除去固體之離子交換樹 脂後,於5 m m H g * 5 0 °C條件下除去副生之甲醇,7K 等,結果得7. 4g白色結晶。藉由氣相層分析之結果, 獲知其中含有8 2. 0% 1 ,1_二羥四甲基二矽氧烷 經濟部中央標準局員工消費合作社印裝 實施例1 0 在具備溫度計,撹拌葉片之WN2置換的5 OmJ?燒 瓶中,於10. 0g(0. 0561倍莫爾)1—甲氧基 五甲基二矽氧烷中添加1. llg(0. 6 2莫爾)之導 電率爲1 0 15ΜΩ的離子交換水。在此添加0 · 0 3 0 g 陽離子交換樹脂(CT - 1 7 5 ,Peurolite公司製), 於2 0°C搅拌8 0分鐘。經由過濾除去固體之離子交換樹 本紙垠又度適用中國國家標準(( 各(210X297公釐)- 420685 A7 _ B7 五、發明説明(24 · 脂後,於5 m m H g,5 0 °C條件下除去副生之甲醇,7_R 等,結果得7. 6g無色透明油。藉由氣相層分析之結果 ,獲知其中含有8 1. 3 % 1—羥基五甲基二矽氧烷。 實施例1 1 在具備溫度計,攪拌葉片之以N 2置換的5 Omi?燒 瓶中,於10. 0g(0. 0396莫爾)3 —甲氧七甲 基三矽氧烷中添加0. 7 8 4 g ( 0 . 〇. 436奠爾) 之導電率爲1〇15ΜΩ的離子交換水。在此添加3 0 g陽離子交換樹脂(CT — 175, Peurolite公司製 ),於2 0 °C搅拌8 0分鐘。經由過濾除去固體之離子交 換樹脂後,於5mmHg,5 0°C條件下除去副生之甲醇 ,水等,結果得8. 〇g白色結晶。藉由氣相層分析之結 果,獲知其中含有9 . 3 % 1 ,3 -羥基七甲基三矽氧 烷。 實施‘例1 2 經濟部中央標準局員工消費合作社印裝 ^ipi I - ^^^^1 tti^i ^^^^1 ^^^^1 1— I 1 d « · (請先閲讀背面之注意事項再填寫本頁) 在具備溫度計,搅拌葉之以N2®換的5 0 m ί燒瓶 中,於2 0 g由 9. 8 %二甲氧二甲基矽烷 51. 〇%1,3—二甲氧四甲基二矽氧烷 2 6 . 0%1 ,5 —二甲氧六甲基三矽氧烷 7 3%1 ,7 —二甲氧八甲基四砂氧院 2 4 %1 ,9 一二甲氧十甲基五矽氧烷 本紙i良尺度通用中阐國家標準(CNS ) A4規格(2IOX2町公釐)-27 - 經濟部中央標率局員Η消費合作社印製 420685 A7 __B7 ________五、發明説明(25 ) 所成烷氧基矽氧烷混合物中加入5. 〇g導電率爲 1 0 15ΜΩ的離子交換水,攪拌5 0分鐘。經由過濾除去 固體之離子交換樹脂後,於5mmHg,5 0°C條件下除 去副生之甲醇,水等,結果得15.lg無色透明之液體 。藉由氣相層析分析之結果,獲知其中含有 2. 7%二羥基二甲基矽烷 4 7. 8%1 ,3_二羥基四甲基二矽氧烷 2 2. 3%1 ,5 —二羥基六甲基三矽氧烷 5. 9%1 ,7_二羥基八甲基四矽氧烷 2. 4%1 ,9 —二羥基十甲基五矽氧烷 實施例1 3 在具備溫度計,搅拌葉之以N2置換的5 OmJ?燒瓶 中,於2 0 g由 7. 5 %二甲氧甲基乙烯矽烷 4 6. 8%1 ,3—二甲氧基一 1 ,二乙烯基一1 , ‘ 3 —二甲基二矽氧烷 2 7 . 1%1 ,5 —二甲氧基—1 ,3 ,5 —三乙烯基一 i ,3 ,5 —三甲基三矽氧烷 6. 1%1 ,7 —二甲氧基—1,3 ,5 ,7 —四乙烯 基一1 ,3 ,5 ,7 -四甲基四矽氧烷 2. 9%1 ,9 一二甲氧基-1 ,3 ,5 ,7 ,9 —五 乙烯基一 1 ,3 ,5 ,7 ,9 —五甲基五矽氧 烷 本紙張尺度適用中國國家標準(cns 規格(2丨0x297公釐)_ 28 _ _---I ! - ^^^1 —1 - 1 ·^-I 1 : -I I &gt;^1 n (請先閱讀背面之注意事項再填寫本頁) A7 420685 __B7_ 五、發明説明(26 ) 所成烷氧基矽氧烷混合物中加入4· 5g導電率爲 1 015ΜΩ的離子交換水,攪拌4 0分鐘。經由過濾除去 固體之離子交換樹脂後,於5mmHg,5 0°C條件下除 去副生之甲醇’水等’結果得1 6 . 7 g無色透明之液體 。藉由氣相層分析之結果,獲知其中含有 2. 0%二羥基甲基乙烯矽烷 4 2. 4%1 ,3 —二羥基-1 ,3 —二乙烯基一 1, 3 —二甲基二矽氧烷 2 4. 5%1,5_ 二羥基-1,3,5 -三乙嫌.基― 1 ,3,5 —三甲基三矽氧烷 7· 5%1 ,7-二羥基一1 ’ 3 ,5 ,7 — 四乙烯 基一1 ,3,5,7 —四甲基四矽氧烷 2. 9%1,9_ 二羥基—1,3,5,7,9 —五 乙烯基一1 ,3 ,5 ,7,9 一五甲基五矽氧 焼 (請先閲請背面之注意事項再填寫未頁) 訂 經濟部中央螵準局員工消費合作'社印聚 本紙ft尺度通用中國國家標準(CNS ) A4規格(2丨OX2W公缝)ltT This paper size is applicable to China National Standard (CM) Λ4 specification (2 丨 0: &lt; 2 blade mm) 20 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 42U685 A7 _B7____ 5. Description of the invention (18) at 10. 0g 1,5-Dimethoxypentamethyltrisiloxane was added with 2.0 g (0.11 Moore) of ion exchange water having a conductivity of 1015MΩ, and (3.00 g cation exchange resin was added thereto. (CT-175) manufactured by Peurolite), and stirred at 20 ° C for 150 minutes. After removing the solid ion exchange resin by filtration, the byproduct methanol, water, etc. were removed under the conditions of 5mmHg, 50 ° C, and the result was 8.0 colorless transparent liquid. As a result of gas chromatography analysis, it was found to contain 90.5% 1,5-dihydroxypentamethyltrisiloxane. Example 5 The ion exchange resin separated by filtration in Example 1 was directly used again as a hydrolysis catalyst, and hydrolysis was performed in the same manner as in Example 1. After repeating this method 10 times, the obtained hydrolysate was analyzed by gas chromatography. As a result, it was found that it contained 2.5% dimethylol dimethyl silane, 44.0% 1, 3-dihydroxytetramethyl dimethyl siloxane. , 2 0.1% 1, 5-dihydroxypentamethyltrisiloxane, 4.4% 1, 7-dihydroxyoctamethyltetrasiloxane, '1.3% 1, 9 one dihydroxydeca Methylpentasiloxane. From the results of the examples, it can be seen that the cation exchange resin used in the present invention can be recovered and used without being subjected to a special treatment such as regeneration. Comparative Example 1 In a 5 OmJ? Flask equipped with a thermometer, a stirrer, and substituted with N 2, 20.0 g (0.166 mol) of dimethoxydimethylsilane was added and adjusted to Η値 4.2 2 6. 8 8 g (This paper size applies to Chinese National Standard (CNS) A4 specifications (2 丨 0X297 male ulcers) _ 2 丄-(Please read the precautions on the back before filling out this page). Order 42ub85. 'A7 B7__ 5. Description of the invention (19) 〇. 3 6 6 Moore) hydrochloric acid water, that is to reach a maximum temperature of 40 eC, to become a uniform solution. After stirring for 5 minutes, 0.2s (4.96X1 0_3 mole) of magnesium oxide and 15g (0 12 5 mole) of magnesium sulfate were added and stirred for 3 hours. This oil was filtered and stripped at 20 ° C and 5 mm H g. When the oil was analyzed by gas chromatography, it was found to contain 15.7% 1,3-dihydroxytetramethyldisilazane, 24.5% 1,5,5-dihydroxypentamethyltrisiloxane, 15 · 1% 1,7-dihydroxyoctamethyltetrasiloxane, 9.3% of 1.9-dihydroxydecamethylpentasiloxane. In the method of this comparative example, condensation of silanol groups is caused. Compared with the above examples, the amount of 1,3-dihydroxytetramethyldisilanes produced by short-chain silanols is obviously lower. Moreover, in this method, Although a mixture of hydroxy compounds can be obtained, it is difficult to isolate a hydroxy compound of a desired chain length from this mixture. Comparative Example 2 Consumption Cooperation by Employees of the Central Bureau of Standards, Ministry of Economic Affairs, J-11 ^^ — ^ 1 1, ^^^ 1 ^^^ 1 ^^^ 1 ^^^ 1 ^^^ 1 ^^^ 1 (Please Read the precautions on the back before filling in this page) In a 5 Omj? Flask equipped with a thermometer, stirrer, and N 2, at 10. Og (〇. 514 mol) 1 '3 -dimethoxy tetra Methyldisilazane was added to adjust pH 2.0 to 2.0 g (0. G 1 11 Moore) of hydrochloric acid water to reach a maximum temperature of 40 ° C, and became a uniform solution. After stirring for 8 minutes, 0.1 g (2.48 × 10-3 mole) of magnesium oxide and 3 g (0.025 mole) of magnesium sulfate were added and stirred for 1 hour. This oil was filtered and stripped under a pressure of 20,5 mm H g. When the oil was analyzed by gas chromatography, it was found that it contained 16.3% 1,3,2-dihydroxytetramethyldisilazane, 25.5. This paper is in accordance with China National Standard (CNS) A4 (2IOX 297). Mm) _ 2-420685 · ν Λ7 B7 V. Description of the invention (20)% 1,5-Dihydroxypentamethyltrisiloxane, 23.8% 1,7-Dihydroxyoctamethyltetrasiloxane , 8.6% of 1.9_dihydroxydecamethylpentasiloxane. In the method of this comparative example, the condensation of silanol groups is caused. Compared with the above examples, the formation of 1,3-dihydroxytetramethyldisilanes of short-bonded silanols is obviously lower. Moreover, in this method, Although a mixture of hydroxy compounds can be obtained, it is difficult to isolate a hydroxy compound of a desired chain length from this mixture. Example 6 Hydrolysis of Dimethan, Dimethan and Silane (First Stage Hydrolysis) In a 20 Omj? Flask equipped with a thermometer and stirring blades replaced with &gt; 12, in a 2.0 Og dimethoxydi To methylsilane (5 ppm chlorine content), 1.19 g (0.2 mole for alkoxy group) of ion-exchanged water having a conductivity of 1015 MΩ was added to form a two-phase system. Add 0.10g (0.46% by weight) of cation exchange resin (printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (please read the notes on the back before filling in this I) CT1 1 1 5 , Peurolite Company System), and stir at 20 ° C for 40 minutes. As a result, the solution phase became homogeneous. Continue stirring for another 4 hours. Analysis by gas chromatography revealed that the reaction mixture contained 33.2% unreacted dimethoxydimethylsilane, 45.4% 1, 3, -dimethoxytetramethyldisilazane. 1%, 2.8% 1, 5-dimethoxyhexamethyltrisiloxane, 2.5% 1,7-dimethyl: oxyoctamethyltetrasiloxane, 0.6% 1 , 9 ~ dimethoxydecylpentasiloxane. This paper size is applicable to CNS A4 specifications (210X297 mm) _ 42 0685 A7 B7 Printed by the Consumers ’Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (21) (Second stage hydrolysis) To the above reaction mixture was added 12.5 g of ion-exchanged water having a conductivity of 1 015 MΩ, and stirred for 40 minutes. After removing the solid ion exchange resin by filtration, the byproduct methanol, water, etc. were removed under the conditions of 5mmHg, 50 ° C, and the result was 11. 0 &amp; colorless and transparent liquid. From the results of gas chromatography analysis, it was found that it contained 25.7% dimethyl dimethyl silane, 4 3. 0% 1, 3-dihydroxytetramethyl dimethyl siloxane, 1 3. 5% 1 , 5-Dihydroxytetramethyltrisiloxane, 2.4% 1,7-Dihydroxyoctamethyltetrasiloxane, 0.6 ·% 1, 9,9-dihydroxydecamethylpentasiloxane. Example 7 Except that the amount of ion-exchanged water used in the first-stage hydrolysis in Example 6 was changed to 3.0 Og (0.5 times mole for alkoxy group), the same hydrolysis was performed. Results The reaction mixture contained 2.1% dimethoxydimethylsilane, 48.9% 1, 3,3-dimethoxydimethyldisilazane, 2 * 9.1% 1, 5-two Methoxyhexamethyltrisiloxane, 8.8% 1, 7-dimethoxyoctamethyltetrasiloxane ', 2.2% 1, 9-dimethoxydecamethylpentasiloxane. Secondly, the hydrolysis in the second stage was performed in the same manner as in Example 6. As a result, 11.6% was obtained as a colorless and transparent liquid, which contained 0.9% of dimethyldimethylsilane, 46.3% of 1,3-dihydroxytetrazine. Methyldioxane '28. 0% 1,5-Dihydroxyhexamethyltrisoxacin' 9-1% 1,7-Dihydroxytetramethyltetrasiloxane, 3.0% 1,9 — Yixiang τ-Come 1-IT {Please read the precautions on the back before filling this page) This paper is fully applicable to China National Standard Soap (CNS) 8 4 old grid (210X297 mm) _ 24-420685 A7 B7 Ministry of Economic Affairs Printed by the Consumers' Cooperatives of the Central Bureau of Quasi-Bureaus 5. Description of Invention (π) Decamethylpentasiloxane. Comparative Example 3 Except that the amount of ion-exchanged water used in the first-stage hydrolysis in Example 6 was changed to 8.9% (1.5 times mole for alkoxy group), the rest were hydrolyzed in the same manner. Contains 70. 1% Dihydroxydimethyl Silane, 8. 5% 1, 3-Dihydroxytetramethyldisilazane, 3.2% 1, 5-Dihydroxyhexamethyltrisiloxane, 12. 5% Hydroxylmethoxydimethylsilane, 3.0% 1_hydroxyl-3._methoxytetramethyldisilazane. As described above, when the alkoxy group of p-alkoxysilane is used in a stoichiometric excess of water during the first-stage hydrolysis, dialkoxysiloxane is scarcely formed, but a hydroxy compound is formed. At this time, the yield of 1,3-dihydroxytetramethyldisilazane is small, and it is difficult to separate the siloxane of a desired chain length from the above-mentioned hydroxyl compound mixture. Example 8 In a 50m flask equipped with a thermometer and stirring blades replaced with &amp; N2, at 10.0g (0.0458 times mole) 1,5 -dimethoxy-1,5-divinyldimethylformate 8 g (0.10 mol) of ion-exchanged water having a conductivity of 1015 MΩ was added to the disiloxane. 0.30 g of cation exchange resin (CT-17.5, manufactured by Peurolil: e) was added here, and it was carried at 20 ° C for 80 minutes. After removing the solid ion exchange resin by filtration, the paper size is applicable to the Chinese National Standard (CNS) Λ4 specification (210X297 mm) at 5mmHg.-(Read the precautions on the back before filling this page) Order A7 B7 420685 V. Description of the invention (23) Remove methanol, water, etc., which are byproducts at 50 ° C, and obtain 7.6 g of white crystals. Based on the results of the gas phase layer analysis, it was found that it contained 80.3 (please read the precautions on the back before filling in this page)% 1,5-dihydroxy-1,5-divinyldimethyldisiloxane 〇 Ο Example 9 In a 5 Om flask equipped with a thermometer, stirring blade of ΗΝ2 replacement, in 10. 0g (0. 514 Moore) 1,1-dimethoxytetramethylsilane was added 2. Ion-exchanged water with a conductivity of 0 g (0.111 Moore.) Of 1015 MΩ. 0.030 g of a cation exchange resin (CT-17.5, manufactured by Peurolite) was added thereto, and the mixture was stirred at 20 ° C. for 80 minutes. After removing the solid ion-exchange resin by filtration, the byproduct methanol, 7K, etc. were removed under the conditions of 5 m m H g * 50 ° C, and 7.4 g of white crystals were obtained. Based on the results of gas-phase layer analysis, it was found that it contained 82.0% 1, 1_dihydroxytetramethyldisilaxane, printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. Example 1 0 In a 5 OmJ? Flask replaced by WN2, 1.10 g (0. 62 Moore) was added to 10. 0 g (0.0561 times mole) of 1-methoxypentamethyldisilazane. It is 10 15 MΩ of ion-exchanged water. 0. 0 300 g of cation exchange resin (CT-1 75, manufactured by Peurolite) was added here, and it stirred at 20 ° C for 80 minutes. Ion-exchange tree paper sheets with solids removed by filtration are again applicable to Chinese national standards ((each (210X297 mm)-420685 A7 _ B7) V. Description of the invention (after 24 · fat, at 5 mm H g, 50 ° C) After removing byproduct methanol, 7_R, etc., 7.6 g of colorless transparent oil was obtained. From the results of gas phase layer analysis, it was found that it contained 8 1.3% 1-hydroxypentamethyldisilazane. Example 1 1 In a 5 Omi? Flask equipped with a thermometer and stirring blades replaced with N 2, 10. 7 g (0.0396 Moore) 3-methoxyheptamethyltrisiloxane was added 0.7 8 4 g ( 0. 〇. 436 Moore) ion-exchange water having a conductivity of 1015 MΩ. 30 g of a cation exchange resin (CT-175, manufactured by Peurolite) was added thereto, and the mixture was stirred at 20 ° C for 80 minutes. After removing the solid ion exchange resin by filtration, the byproduct methanol, water, etc. were removed under the conditions of 5mmHg, 50 ° C, and 8.0 g of white crystals were obtained. From the results of gas phase layer analysis, it was found to contain 9%. 3% 1, 3-Hydroxyheptamethyltrisiloxane. Implementation Example 1 2 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs ^ ipi I-^^^^ 1 tti ^ i ^^^^ 1 ^^^^ 1 1— I 1 d «(Please read the notes on the back before filling this page) With a thermometer, stir the leaves In a 50 m flask replaced with N2®, 20 g of 9.8% dimethoxydimethylsilane 51.0% 1,3-dimethoxytetramethyldisiloxane 26.0% 1,5-Dimethoxyhexamethyltrisiloxane 7 3% 1, 7-Dimethoxyoctamethyltetroxaline 2 4% 1,9 Dimethoxydecamethylpentasiloxane paper i Good-standard general-purpose national standard (CNS) A4 specification (2IOX2 mm) -27-Printed by a member of the Central Standards Bureau, Ministry of Economic Affairs and Consumer Cooperative, 420685 A7 __B7 ________ V. Description of the invention (25) Add 5.0 g of ion-exchanged water with a conductivity of 10 15MΩ to the oxane mixture and stir for 50 minutes. After removing the solid ion-exchange resin by filtration, remove the byproduct methanol at 5mmHg, 50 ° C, Water, etc., as a result, 15.lg was obtained as a colorless and transparent liquid. According to the results of gas chromatography analysis, it was found that it contained 2.7% dihydroxydimethylsilane 4 7. 8% 1, 3-dihydroxytetramethyl. Disiloxane 2 2.3% 1, 5-Dihydroxy Hexamethyltrisiloxane, 5.9% 1, 7-dihydroxyoctamethyltetrasiloxane, 2.4% 1, 9-dihydroxydecamethylpentasiloxane Example 1 3 With a thermometer, In a 5 OmJ? Flask with agitating leaves replaced by N2, 20 g of 7.5% dimethoxymethylethylene silane 46.8% 1, 3-dimethoxy-1, divinyl-1 , '3-Dimethyldisilazane 27.1% 1, 5-Dimethoxy-1, 3, 5-trivinyl-i, 3, 5-trimethyltrisiloxane 6. 1% 1,7-dimethoxy-1,3,5,7-tetravinyl-1,3,5,7-tetramethyltetrasiloxane 2.9% 1,9-dimethoxy -1,3,5,7,9-pentavinyl-1,3,5,7,9-pentamethylpentasilane This paper size applies to Chinese national standards (cns specification (2 丨 0x297 mm) _ 28 _ _--- I!-^^^ 1 —1-1 · ^ -I 1: -II &gt; ^ 1 n (Please read the precautions on the back before filling this page) A7 420685 __B7_ V. Description of the invention (26) Add 4.5 g of ion-exchanged water with a conductivity of 1,015MΩ to the resulting alkoxysilane mixture, and stir for 40 minutes. After removing the solid ion exchange resin by filtration, the byproduct methanol 'water, etc.' was removed under the conditions of 5 mmHg and 50 ° C to obtain 16.7 g of a colorless and transparent liquid. From the results of gas phase layer analysis, it was found that it contained 2.0% dihydroxymethyl vinyl silane 4 2.4% 1, 3-dihydroxy-1, 3- divinyl-1, 3-dimethyldisiloxane Siloxane 2 4. 5% 1,5_ dihydroxy-1,3,5-triethylamine. 1 — 3,5-trimethyltrisiloxane 7.5% 1, 7-dihydroxy-1 1 '3, 5, 7 —tetravinyl-1,3,5,7 —tetramethyltetrasiloxane 2. 9% 1,9_dihydroxy —1,3,5,7,9 —pentavinyl One 1,3,5,7,9 One pentamethylpentasiloxane (please read the precautions on the back before filling in the unpaged page) Order the Central Government Procurement Bureau's Consumer Cooperation of the Ministry of Economic Affairs' Common printed paper ft standard universal China National Standard (CNS) A4 specification (2 丨 OX2W male stitch)

Claims (1)

89· 8,1 年/) 補充 420685 Hh Cb DH 本 六、申請專利範圍 ' 第84104067號專利申請案 中文申請專利範圍修正本 (請先閱讀背面之注意事項再填寫本頁) 民國8 9年8月修正 1 . 一種具有矽烷醇基之低分子量有機基矽氧烷的製 造方法’其特徵爲在空孔體積以水銀注入法測定時爲 0 lmi/g以上的粗多孔型陽離子交換樹脂存在下, 於以下式(1 ) • · 1 ^CROWiO^ (1) ~Ζ (式中RM系表示碳數1〜4之烷基,碳數2〜4之鏈烯 基’苯基’ R2係表示相同或不同之碳數1〜4院基,a 係0〜2. 2,b係〇· 2〜3之數,a+b係2〜3, 惟分子中之矽原子數係2〜5), 所示烷氧基矽氧烷中添加上述烷氧基矽氧烷之烷氧基的 1. 0倍莫爾以上之水*經攪拌,進行水解者。 經濟部智慧財產局員工消費合作杜印製 2.如申請專利範圍第1項之製造方法,其中做爲式 (1 )之烷氧基矽氧烷係使用下式(2 ) Ri RO-^SiOV-R1 ( 2) I R1 (式中R1» R2係如上述所示定義,η係2〜5之整數) 所示之二烷氧基矽氧烷。 本紙張尺度適用中國國家標準0:.\$)Λ4規恪(210x 297公S ) 0685 Η8 1)8 κ、曱請專利範圍 3 _如申請專利範圍第2項之製造方法,其中上述式 (2 )之二焼氧基矽氧烷爲在陽離子交換樹脂之存在下, 在下式(3 ) R\Si/〇RJ 记/ \〇纪 (3) (式中R1’ R 2係如上述所定義)所示二烷氧基矽烷中, 添加上述二烷氧基矽烷分子中存在之烷氧基的〇 1倍莫 爾〜1倍莫爾之水’經攪拌予以水解所得者。 4.如申請專利範圍第2項或第3項之製造方法,其 中具有矽烷醇基之低分子量有機基聚矽氧烷爲以式(4 ) 或(5 )所示者, 經泫部智慧財產局員工消費合作社印製 R1 HOKSiOkH R1 R1 HCHSiO)rK Rl (4) (5) (式中R1係如上述所定義)。 5. 如申請專利範圍第1項之製造方法,其中水解使 用之水爲導電率1 ΟιαΜΩ以上之離子交換水。 6. 如申請專利範圍第1項之製造方法,其中上述式 本紙張尺度適用_國國家標準規络do X 297公g ) ---— — — — — — —-- -----訂---I -----線 (請先閱讀背面之注意事項再填寫本頁) l;8 1)8 六、申請專利範圍 3.如申請專利範圍第2項之製造方法,其中上述式 (2 )之二烷氧基矽氧烷爲在陽離子交換樹脂之存在下, 在下式(3 ) Rlv y〇R2 NSi R1/ \〇RZ (3) (式中R1,R 2係如上述所定義)所示二烷氧基矽烷中, 添加上述二烷氧基矽烷分子中存在之烷氧基的〇. i倍莫 爾〜1倍莫爾之水,經攪拌予以水解所得者。 4.如申請專利範圍第2項或第3項之製造方法,其 中具有矽烷醇基之低分子量有機基聚矽氧烷爲以式(4) 或(5 )所示者, R1 HO-iSiOir-t R1 ¢4) (請先閱讀背面之注意事項再填寫本頁) -------訂--------線 經濟部智慧財產局員工消費合作社印1¾ R1 HCMSiOVH Rl (5) (式中R1係如上述所定義)。 5. 如申請專利範圍第1項之製造方法,其中水解使 用之水爲導電率1 〇10ΜΩ以上之離子交換水。 6. 如申請專利範圍第1項之製造方法,其中上述式 本紙張尺度適用φ國國家標準(CNS)A4規格(210 X 297公餐) ^ ϋ b 85 tif B8 ’ CH 1)8 六、申請專利範圍 (3 )之二烷氧基矽烷中殘留之氯成份爲1 Ο 0 p pm以 下。 (請先閱讀背面之注意事項再填寫本 -n n I— It n n n 經濟部智慧財產局員工消費合作社印製 本紙張又度適用中國國家標準(CNS)A4規格(210x297公釐) 申請曰期 84年 4 月 25 日 案 號 84104067 類 别 (以上各攔由本局填註) 公告本 A4 C4 4206i5 霉蜃專利説明書(修正筲) 中 文 具有矽烷酵基之低分子置有機基矽《烷的製迪方法 發明 新型 名稱 英文 Process for preparing organosiloxane terminated with silanol group 姓 名 (1)五十嵐実 0高橋政晴 國 籍 (1)曰本 {25曰本 發明 創作 人 住、居所 姓 名 (名稱) 國 籍 ⑴日本囲群馬縣碓氷郡松并田町大字人見一番地 —Ο Q日本國群馬縣碓氷郡松井田町大字人見一番地 —〇 ⑴倍越化學工業股份有限公司 倍越化学工業株式会社 .私裝------訂I 綵 申請人 住、居所 (事務所) (1)日本 ⑴日本國東京都千代田匾大手町二丁目六番一號 代表人 姓 名 ⑴金川千尋 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨0X297公釐) 89· 8,1 年/) 補充 420685 Hh Cb DH 本 六、申請專利範圍 ' 第84104067號專利申請案 中文申請專利範圍修正本 (請先閱讀背面之注意事項再填寫本頁) 民國8 9年8月修正 1 . 一種具有矽烷醇基之低分子量有機基矽氧烷的製 造方法’其特徵爲在空孔體積以水銀注入法測定時爲 0 lmi/g以上的粗多孔型陽離子交換樹脂存在下, 於以下式(1 ) • · 1 ^CROWiO^ (1) ~Ζ (式中RM系表示碳數1〜4之烷基,碳數2〜4之鏈烯 基’苯基’ R2係表示相同或不同之碳數1〜4院基,a 係0〜2. 2,b係〇· 2〜3之數,a+b係2〜3, 惟分子中之矽原子數係2〜5), 所示烷氧基矽氧烷中添加上述烷氧基矽氧烷之烷氧基的 1. 0倍莫爾以上之水*經攪拌,進行水解者。 經濟部智慧財產局員工消費合作杜印製 2.如申請專利範圍第1項之製造方法,其中做爲式 (1 )之烷氧基矽氧烷係使用下式(2 ) Ri RO-^SiOV-R1 ( 2) I R1 (式中R1» R2係如上述所示定義,η係2〜5之整數) 所示之二烷氧基矽氧烷。 本紙張尺度適用中國國家標準0:.\$)Λ4規恪(210x 297公S )89 · 8, 1 year /) Supplement 420685 Hh Cb DH This VI. Application for Patent Scope 'Patent Application No. 84104067 Patent Application Amendment for Chinese Patent Application (Please read the notes on the back before filling this page) Republic of China 8 9 years 8 Month correction 1. A method for producing a low-molecular-weight organosiloxane having a silanol group, which is characterized by the presence of a coarse porous cation exchange resin having a pore volume of 0 lmi / g or more when measured by a mercury injection method. In the following formula (1) • · 1 ^ CROWiO ^ (1) ~ Z (where RM is an alkyl group having 1 to 4 carbon atoms, alkenyl 'phenyl' R2 group having 2 to 4 carbon atoms is the same or The different carbon numbers are 1 to 4 radicals, a is 0 to 2.2, b is 0.2 to 3, a + b is 2 to 3, but the number of silicon atoms in the molecule is 2 to 5), so Shows that alkoxysiloxane is added to the above-mentioned alkoxysiloxane alkoxy group of 1.0 times mole of water * or more, and is subjected to hydrolysis. Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs for consumer cooperation. 2. If the manufacturing method of the first scope of the patent application is applied, the formula (1) for the alkoxysiloxane is the following formula (2) Ri RO- ^ SiOV -R1 (2) I R1 (where R1 »R2 is defined as shown above, and η is an integer of 2 to 5). This paper size applies the Chinese national standard 0:. \ $) Λ4 (210x 297 male S) 0685 Η8 1) 8 κ, please apply for the patent scope 3 _ If the manufacturing method of the second scope of the patent application, the above formula ( 2) Dioxosiloxane is in the presence of a cation exchange resin in the following formula (3) R \ Si / 〇RJ Note / \ 〇 纪 (3) (where R1 'R 2 is as defined above To the dialkoxysilane shown in (1), water obtained by adding 0-1 mol to 1 mol of alkoxy present in the above dialkoxysilane molecules was hydrolyzed by stirring. 4. The manufacturing method according to item 2 or item 3 of the scope of patent application, wherein the low-molecular-weight organic polysiloxane having a silanol group is represented by formula (4) or (5). R1 HOKSiOkH R1 R1 HCHSiO) rK Rl (4) (5) (R1 is as defined above). 5. The manufacturing method according to item 1 of the scope of patent application, wherein the water used for the hydrolysis is ion-exchanged water having a conductivity of 10 μαΜΩ or more. 6. If the manufacturing method of the scope of patent application is the first one, in which the above-mentioned paper size is applicable _ national national standard profile do X 297g g) ----- — — — — — — — ----- order --- I ----- line (please read the precautions on the back before filling out this page) l; 8 1) 8 VI. Patent Application Scope 3. For the manufacturing method of the second scope of patent application, where the above formula (2) The dialkoxysilane is in the presence of a cation exchange resin, in the following formula (3) Rlv y〇R2 NSi R1 / \ 〇RZ (3) (where R1 and R2 are as defined above) ) Shown in the above dialkoxysilane, adding 0.1 mol to 1 mol of alkoxy present in the above dialkoxysilane molecules, and stirring and hydrolyzing. 4. The manufacturing method according to item 2 or item 3 of the scope of patent application, wherein the low molecular weight organic polysiloxane having a silanol group is one represented by formula (4) or (5), R1 HO-iSiOir- t R1 ¢ 4) (Please read the notes on the back before filling out this page) ------- Order -------- Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 1¾ R1 HCMSiOVH Rl (5 ) (Where R1 is as defined above). 5. The manufacturing method according to item 1 of the scope of patent application, wherein the water used for the hydrolysis is ion-exchange water having a conductivity of 1010 MΩ or more. 6. For the manufacturing method of item 1 in the scope of patent application, in which the above paper size is applicable to the national standard (CNS) A4 specification (210 X 297 meals) ^ ϋ b 85 tif B8 'CH 1) 8 6. Application The residual chlorine content in the dialkoxysilane of the patent range (3) is below 100 p pm. (Please read the precautions on the back before filling in this -nn I— It nnn This paper printed by the Consumers' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs is again applicable to the Chinese National Standard (CNS) A4 specification (210x297 mm). The application period is 84 years Case No. 84104067 on April 25 (Categories above are filled out by the Bureau) Notice A4 C4 4206i5 Patent Specification for Mold (Amendment) Chinese Low-molecular-weight organosilane with silanease group The name of the new invention in English Process for preparing organosiloxane terminated with silanol group Name (1) Igarashi 実 0 Takahashi Masaru Nationality (1) Japanese version {25: Name of the creator, residence of the present invention (name) Nationality ⑴ Japan 囲 Gunma Prefecture 碓 Ice-gun pine Meet the big characters of Wadata — Q Q See the great characters of Matsuda-machi, Ogami-gun, Gunma Prefecture, Japan — 0⑴Betsu Chemical Industry Co., Ltd. Betsu Chemical Industry Co., Ltd. ------ Order I Ai applicant's residence, residence (office) (1) Japan, Japan, Chiyoda, Tokyo, Japan Representative name of Fanyi 一 Jinchuan Chihiro This paper size is applicable to Chinese National Standard (CNS) A4 specification (2 丨 0X297 mm) 89 · 8, 1 year /) Supplement 420685 Hh Cb DH The sixth, the scope of patent application 'No. 84104066 Patent Application No. Chinese Patent Application Amendment (please read the precautions on the back before filling out this page) Republic of China August 1989 Amendment 1. A method for producing low molecular weight organosiloxanes with silanol groups' its It is characterized by the presence of a coarse porous cation exchange resin with a pore volume of 0 lmi / g or more when measured by the mercury injection method. In the following formula (1) • · 1 ^ CROWiO ^ (1) ~ Z (where RM system is Represents an alkyl group having 1 to 4 carbon atoms, and an alkenyl 'phenyl' group having 2 to 4 carbon atoms. R2 represents the same or different carbon group having 1 to 4 carbon atoms, a is 0 to 2.2, and b is 0. The number of 2 to 3, a + b is 2 to 3, but the number of silicon atoms in the molecule is 2 to 5). The alkoxysiloxane shown above is added with 1 of the alkoxyl of the above alkoxysiloxane. Water with more than 0 times Moore * is stirred and hydrolyzed. Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs for consumer cooperation. 2. If the manufacturing method of the first scope of the patent application is applied, the formula (1) for the alkoxysiloxane is the following formula (2) Ri RO- ^ SiOV -R1 (2) I R1 (where R1 »R2 is defined as shown above, and η is an integer of 2 to 5). This paper size applies Chinese national standard 0:. \ $) Λ4 (210x 297mm S)
TW84104067A 1995-03-14 1995-04-25 Process for preparing organosiloxane terminated with silanol group TW420685B (en)

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