TW201130806A - Process for production of glycidyl ether compounds, and monoallyl monoglycidyl ether compound - Google Patents

Process for production of glycidyl ether compounds, and monoallyl monoglycidyl ether compound Download PDF

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TW201130806A
TW201130806A TW099145227A TW99145227A TW201130806A TW 201130806 A TW201130806 A TW 201130806A TW 099145227 A TW099145227 A TW 099145227A TW 99145227 A TW99145227 A TW 99145227A TW 201130806 A TW201130806 A TW 201130806A
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compound
ether
allyl
group
carbon atoms
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TW099145227A
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TWI458717B (en
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Hiroshi Uchida
Yoshikazu Arai
Kazuhiko Sato
Takefumi Chishiro
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Showa Denko Kk
Nat Inst Of Advanced Ind Scien
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D301/00Preparation of oxiranes
    • C07D301/02Synthesis of the oxirane ring
    • C07D301/03Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
    • C07D301/12Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with hydrogen peroxide or inorganic peroxides or peracids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24Chromium, molybdenum or tungsten
    • B01J23/30Tungsten
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D303/00Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
    • C07D303/02Compounds containing oxirane rings
    • C07D303/12Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
    • C07D303/18Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by etherified hydroxyl radicals
    • C07D303/20Ethers with hydroxy compounds containing no oxirane rings
    • C07D303/22Ethers with hydroxy compounds containing no oxirane rings with monohydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D303/00Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
    • C07D303/02Compounds containing oxirane rings
    • C07D303/12Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
    • C07D303/18Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by etherified hydroxyl radicals
    • C07D303/20Ethers with hydroxy compounds containing no oxirane rings
    • C07D303/24Ethers with hydroxy compounds containing no oxirane rings with polyhydroxy compounds
    • C07D303/27Ethers with hydroxy compounds containing no oxirane rings with polyhydroxy compounds having all hydroxyl radicals etherified with oxirane containing compounds

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Epoxy Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Provided are: a process by which a compound having an allyl ether linkage can be efficiently converted into the corresponding glycidyl ether compound under mild conditions using hydrogen peroxide as the oxidizing agent; and a novel monoallyl monoglycidyl ether compound having a biphenyl skeleton. Specifically provided are: a process for the production of glycidyl ether compounds which comprises reacting a compound having an allyl ether linkage with hydrogen peroxide to epoxidize the carbon-carbon double bond of the allyl group and thus form the corresponding glycidyl ether compound, characterized by using, as the reaction catalyst, a tungsten compound, a tertiary amine, and phenylphosphonic acid; and a monoallyl monoglycidyl ether compound having a biphenyl skeleton. The monoallyl monoglycidyl ether compound can be produced by the process.

Description

201130806 六、發明說明: 【發明所屬之技術領域】 本發明係關於環氧丙基醚化合物之製造方 基單環氧丙基醚化合物。更詳言之,本發明係 用既定之觸媒,而使具有烯丙基醚鍵結之化合 基之碳-碳雙鍵以過氧化氫進行氧化,可效率 環氧化爲其特徵之環氧丙基醚化合物之製造方 使具有烯丙基醚鍵結之化合物之該烯丙基之在 過氧化氫進行氧化而生成之單烯丙基單環氧丙 【先前技術】 作爲環氧樹脂之原料而周知之環氧丙基醚 性大規模地生產,且廣泛使用於各種領域。 以往所知之環氧丙基醚之製造方法,有將 酚,在觸媒之存在下或不存在下,以鹼性條件 氧氯丙烷反應,而得到環氧丙基醚之方法。於 有機氯化合物必然殘留,在若干用途上,例如 電機用途上,則有絶緣特性變得降低之缺點。 因此,亦檢討著對烯丙基醚利用氧化劑使 碳-碳雙鍵直接進行環氧化一事。以下之專利Z 特表平1 0- 5 1 1 722號公報)及專利文獻2(曰本 6 0 1 23號公報)中揭示,使雙酚-A之二烯丙基 漆型苯酚樹脂之聚烯丙基醚,在甲苯等之有機 法及單烯丙 關於藉由使 物之該烯丙 良好地進行 法,及藉由 吴-碳雙鍵以 基醚化合物 ,係被工業 對應之醇、 下使其與環 此方法中, 使用於電子 該烯丙基之 t獻1(曰本 特開昭60-醚或酚醛清 溶劑中,使 -5- 201130806 用鎢酸鈉與磷酸觸媒,在4級銨鹽之存在下,藉由過氧化 氫進行環氧化之方法。此方法中,鎢化合物之使用量必須 爲非常多,且環氧化速度並不充分,無法實施作爲工業上 之製造方法。 以下之專利文獻3 (美國專利第5 6 3 3 3 9 1號公報)中揭 示,使烯烴在有機溶劑中、氧化銶觸媒之存在下,藉由使 其與作爲氧化劑之過氧化雙(三甲基矽烷基)接觸,而將烯 烴環氧化之方法,但其需要高價之觸媒與氧化劑,且於製 造苯基嫌丙基醒時,其收率亦不充分。 以下之專利文獻4(日本特開平7-145221號公報)及專 利文獻5(特開昭5 8- 1 73 1 1 8號公報)中揭示,使苯酚酚醛 清漆樹脂藉由鹵化烯丙基進行烯丙基醚化後,於有機溶劑 中以過酸進行環氧化之方法,而有使用高危險性之過酸之 必要。 又,以下之專利文獻6(日本特表2002-526483號公報 )中揭示,在含鈦之沸石觸媒、及3級胺、3級胺氧化物或 彼等之混合物之存在下,藉由過氧化氫進行環氧化之方法 ,此方法雖然在將分子量小之烯烴化合物作爲基質時爲有 用者,但如苯基醚般之分子量大之基質時,觸媒效率差, 而無法適用。 [先前技術文獻] [專利文獻] [專利文獻1]曰本特表平10-511722號公報 [專利文獻2]日本特開昭60-60 1 23號公報 -6- 201130806 [專利文獻3]美國專利第5633391號公報 [專利文獻4]日本特開平7_ 1 45 22 1號公報 [專利文獻5]日本特開昭58-173118號公報 [專利文獻6]日本特表2〇〇2·526483號公報 【發明內容】201130806 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to a methacrylic propyl ether compound which is a epoxidized propyl ether compound. More specifically, the present invention uses a predetermined catalyst to oxidize a carbon-carbon double bond having an allyl ether-bonded compound with hydrogen peroxide, and is characterized by efficient epoxidation. The base ether compound is produced by subjecting the allyl group of the compound having an allyl ether bond to oxidation of hydrogen peroxide to form a monoallyl monoepoxypropane [previous art] as a raw material of the epoxy resin It is widely known to be produced on a large scale and is widely used in various fields. The conventionally known method for producing a glycidyl propyl ether is a method in which phenol is reacted with oxychloropropane under basic conditions in the presence or absence of a catalyst to obtain a glycidyl propyl ether. The organic chlorine compound is inevitably left to be present, and in some applications, for example, in motor applications, there is a disadvantage that the insulating property is lowered. Therefore, the direct epoxidation of the carbon-carbon double bond by the oxidizing agent for the allyl ether was also reviewed. The following patents are disclosed in Japanese Patent Application Laid-Open No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. Allyl ether, an organic method in toluene or the like, a monoethylene-based method in which the allylic substance is favorably carried out, and a ketone-carbon double bond-based hydroxy group compound are industrially corresponding alcohols, To make it with the ring, use this in the electrons of the allyl group 1 (曰本特开昭60-ether or phenolic solvent, make -5-201130806 with sodium tungstate and phosphate catalyst, at 4 The method of epoxidation by hydrogen peroxide in the presence of a per-ammonium salt. In this method, the amount of the tungsten compound used must be very large, and the epoxidation rate is not sufficient, and it cannot be implemented as an industrial production method. Patent Document 3 (U.S. Patent No. 5,663,391) discloses the use of an olefin in an organic solvent in the presence of a ruthenium oxide catalyst to cause oxidation with bismuth as an oxidant. a method of epoxidizing an olefin based on an alkyl group, but requiring a high-priced catalyst The oxidizing agent is not sufficient in the production of a phenyl propyl group. Patent Document 4 (Japanese Laid-Open Patent Publication No. Hei. No. 7-145221) and Patent Document 5 (Japanese Patent Laid-Open Publication No. Hei No. Hei No. Hei No. Hei. In the No. 8 publication, it is disclosed that the phenol novolak resin is subjected to allyl etherification by a halogenated allyl group, and then epoxidized by a peracid in an organic solvent, and it is necessary to use a high-risk peracid. Further, in the presence of a titanium-containing zeolite catalyst, a tertiary amine, a tertiary amine oxide or a mixture thereof, by the following Patent Document 6 (Japanese Patent Publication No. 2002-526483) A method of epoxidizing hydrogen peroxide. This method is useful when a olefin compound having a small molecular weight is used as a matrix. However, when a matrix having a large molecular weight like a phenyl ether has a poor catalyst efficiency, it is not applicable. [Patent Document 1] [Patent Document 1] Japanese Patent Laid-Open Publication No. Hei 10-- No. Hei. No. Hei. No. Hei. Japanese Patent Publication No. 5633391 [Patent Document 4] Japanese Patent Laid-Open No. 7_1 45 22 No. 1 [Patent Document 5] JP-A-58-173118 [Patent Document 6] Japanese Patent Publication No. 2〇〇2·526483 [Contents of the Invention]

[發明所欲解決之課題J 本發明所欲解決之課題爲提供在溫和條件下,使用過 氧化氫爲氧化劑’由具有烯丙基醚鍵結之化合物有效率地 製造環氧丙基醚化合物之方法。 目前尙無已合成具有聯苯骨架之單烯丙基單環氧丙基 醚化合物之例報告。單烯丙基單環氧丙基醚化合物,由於 具有烯丙基而可使其與具有Si-H基之化合物矽氫化反應 ’進而可對具有各種Si-H基之化合物導入聯苯基環氧丙 基醚基。例如,在合成抗蝕劑類或密封材類等所利用之環 氧樹脂時,以使其與具有各種Si-H基之矽氧烷化合物進 行矽氫化,因1段階之反應,被認爲可同時導入高耐熱性 、高蝕刻耐性之聯苯骨架與硬化所必要之環氧基,而極爲 有用。故,本發明所欲解決之課題亦在於提供具有高耐熱 性、高蝕刻耐性之聯苯骨架的新穎單烯丙基單環氧丙基醚 化合物。 [用以解決課題之手段] 本發明者們爲了解決前述課題經過銳意硏究及實驗之 201130806 結果,發現藉由使用鎢化合物、3級有機胺、及苯膦酸作 爲觸媒,並使過氧化氫水溶液與烯丙基醚化合物反應,而 可高效率選擇性地生成其所對應之環氧丙基醚化合物一事 ,進而完成本發明。 即,本發明爲如以下般者》 [1] 一種環氧丙基醚化合物之製造方法,其係使具有烯 丙基醚鍵結之化合物與過氧化氫反應,藉由使該烯丙基之 碳-碳雙鍵環氧化而製造對應之環氧丙基醚化合物之方法 ’其特徵爲使用鎢化合物、3級胺、及苯膦酸作爲反應觸 媒。 [2] 如前述[1]之環氧丙基醚化合物之製造方法,其中 前述鎢化合物係使用鎢酸之部分中和鹽。 [3] 如前述[1]或[2]之環氧丙基醚化合物之製造方法, 其中前述鎢化合物爲鎢酸鈉與鎢酸之混合物、鎢酸鈉與礦 酸之混合物,或鎢酸與鹼化合物之混合物。 [4] 如前述[1]〜[3]中任一項之環氧丙基醚化合物之製 造方法,其中前述3級胺爲三烷基胺,鍵結於其氮原子之 烷基之碳數之合計爲6以上50以下。 [5] 如前述[1]〜[4]中任一項之環氧丙基醚化合物之製 造方法’其中前述具有烯丙基醚鍵結之化合物爲具有複數 之烯丙基醚鍵結之化合物。 [6] 如前述[1]〜[4]中任一項之環氧丙基醚化合物之製 造方法,其中前述具有烯丙基醚鍵結之化合物爲具有2個 嫌丙基醚鍵結之化合物,並更具有自反應生成物將僅有一 -8- 201130806 方之烯丙基醚鍵結受到環氧化之單烯丙基單環氧丙基醚化 合物予以單離之步驟。 [7] 如前述[1]〜[6]中任一項之環氧丙基醚化合物之製 造方法,其中不使用有機溶劑作爲反應溶劑。 [8] 如前述[1]〜[7]中任一項之環氧丙基醚化合物之製 造方法,其中前述具有烯丙基醚鍵結之化合物具有如以下 之式(1 ): 【化1】[Problem to be Solved by the Invention] The problem to be solved by the present invention is to provide an epoxy propyl ether compound efficiently produced from a compound having an allyl ether bond under mild conditions using hydrogen peroxide as an oxidizing agent. method. At present, there is no report on the synthesis of a monoallyl monoepoxypropyl ether compound having a biphenyl skeleton. The monoallyl monoepoxypropyl ether compound can be hydrogenated by reacting with a compound having a Si-H group by having an allyl group. Further, a compound having various Si-H groups can be introduced into a biphenyl epoxy group. Propyl ether group. For example, in the case of synthesizing an epoxy resin used for a resist or a sealing material, it is considered to be capable of hydrogenation with a sulfonium compound having various Si-H groups, and is considered to be a one-step reaction. It is extremely useful to introduce a biphenyl skeleton having high heat resistance and high etching resistance and an epoxy group necessary for hardening. Therefore, the object of the present invention is to provide a novel monoallyl monoepoxypropyl ether compound having a biphenyl skeleton having high heat resistance and high etching resistance. [Means for Solving the Problem] The inventors of the present invention have found that the use of a tungsten compound, a tertiary organic amine, and a phenylphosphonic acid as a catalyst and a peroxidation by using the results of 201130806, which have been carefully studied and tested. The present invention can be completed by reacting an aqueous hydrogen solution with an allyl ether compound to efficiently produce a correspondingly epoxidized propyl ether compound. That is, the present invention is as follows: [1] A method for producing a glycidyl propyl ether compound by reacting a compound having an allyl ether bond with hydrogen peroxide by using the allyl group A method of producing a corresponding epoxy propyl ether compound by epoxidation of a carbon-carbon double bond is characterized in that a tungsten compound, a tertiary amine, and a phenylphosphonic acid are used as a reaction catalyst. [2] The method for producing a glycidyl propyl ether compound according to the above [1], wherein the tungsten compound is a partially neutralized salt of tungstic acid. [3] The method for producing a glycopropyl ether compound according to the above [1] or [2] wherein the tungsten compound is a mixture of sodium tungstate and tungstic acid, a mixture of sodium tungstate and mineral acid, or tungstic acid and a mixture of base compounds. [4] The method for producing a glycidyl ether compound according to any one of the above [1] to [3] wherein the tertiary amine is a trialkylamine, and the carbon number of the alkyl group bonded to the nitrogen atom thereof The total is 6 or more and 50 or less. [5] The method for producing a glycidyl ether compound according to any one of the above [1] to [4] wherein the compound having an allyl ether bond is a compound having a complex allyl ether bond . [6] The method for producing a glycidyl ether compound according to any one of the above [1] to [4] wherein the compound having an allyl ether bond is a compound having two propyl ether linkages And more has the step of separating the monoallyl monoepoxypropyl ether compound which is only epoxidized from the reaction product by only one -8 to 201130806. [7] The method for producing a glycidyl propyl ether compound according to any one of the above [1] to [6], wherein an organic solvent is not used as a reaction solvent. [8] The method for producing a glycidyl ether compound according to any one of the above [1] to [7] wherein the compound having an allyl ether bond has the following formula (1): 】

{式中,R1、及R2各自獨立爲氫原子、碳數1〜6之烷基 、碳數2〜6之烯基、碳數3〜12之環烷基或碳數6〜10 之芳基,或,R1與R2與一起形成碳數2〜6之亞烷基或碳 數3〜12之環亞烷基亦可。113、114、115、及116各自獨立 爲氫原子、碳數1〜10之烷基、碳數2〜10之烯基、碳數 3〜12之環烷基或碳數6〜10之芳基,且,η表示0或1 之整數}所表示之構造。 [9]如前述[1]〜[8]中任一項之環氧丙基醚化合物之製 造方法,其中前述具有烯丙基醚鍵結之化合物係選自由雙 酚-Α之二烯丙基醚、雙酚_F之二烯丙基醚、及3,3,,5,5,_ 四甲基聯苯基-4,4,-二烯丙基醚所成群之至少一種。 -9 - 201130806 [10] 如前述[1]〜[7]中任一項之環氧丙基醚化合物之 製造方法,其中前述具有烯丙基醚鍵結之化合物係選自由 碳數2〜20之α,ω-聚烯烴二醇二烯丙基醚、1,4-環己烷二 甲醇二烯丙基醚、及三環[5.2.1. 02’6]癸烷二甲醇二烯丙基 醚所成群之至少一種。 [11] 如前述[1]〜[7]中任一項之環氧丙基醚化合物之 製造方法,其中前述具有烯丙基醚鍵結之化合物爲酚-甲 醛•烯丙醇聚縮合物或甲酚-甲醛•烯丙醇聚縮合物。 [12] —種具有聯苯骨架之單烯丙基單環氧丙基醚化合 物,其係爲如以下之一般式(2): 【化2】In the formula, R1 and R2 each independently represent a hydrogen atom, an alkyl group having 1 to 6 carbon atoms, an alkenyl group having 2 to 6 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms or an aryl group having 6 to 10 carbon atoms. Or, R1 and R2 together may form an alkylene group having 2 to 6 carbon atoms or a cycloalkylene group having 3 to 12 carbon atoms. 113, 114, 115, and 116 are each independently a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, an alkenyl group having 2 to 10 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms or an aryl group having 6 to 10 carbon atoms. And η represents a configuration represented by an integer of 0 or 1. [9] The method for producing a glycidyl ether compound according to any one of the above [1] to [8] wherein the compound having an allyl ether bond is selected from a diallyl group derived from bisphenol-indole At least one of a group of ether, bisphenol-F diallyl ether, and 3,3,5,5,-tetramethylbiphenyl-4,4,-diallyl ether. The method for producing a glycidyl ether compound according to any one of the above [1] to [7] wherein the compound having an allyl ether bond is selected from a carbon number of 2 to 20 α,ω-polyolefin diol diallyl ether, 1,4-cyclohexanedimethanol diallyl ether, and tricyclo[5.2.1. 02'6]decane dimethanol diallyl At least one of a group of ethers. [11] The method for producing a glycidyl ether compound according to any one of [1] to [7] wherein the compound having an allyl ether bond is a phenol-formaldehyde/allyl alcohol polycondensate or Cresol-formaldehyde-allyl alcohol polycondensate. [12] A monoallyl monoepoxypropyl ether compound having a biphenyl skeleton, which is a general formula (2) as follows:

(2) {式中,117、118、119、及R1()各自獨立爲氫原子、碳數1 〜1〇之烷基、碳數2〜10之烯基、碳數3〜10之環烷基或 碳數6〜10之芳基}所表示者。 [13]如前述[12]之具有聯苯骨架之單烯丙基單環氧丙 基醚化合物,其中式中之R7、R8、R9、及R1Q爲甲基。 [發明之效果] 依據本發明之環氧丙基醚化合物之製造方法,藉使用 鎢化合物、3級有機胺、及苯膦酸作爲觸媒,使過氧化氫 -10- 201130806 與烯丙基醚化合物反應,而可製造所對應之環氧丙基醚化 合物,並在極力抑制有機氯系之雜質混入,可同時以簡便 操作下安全並收率良好且低成本地製造於電子材料領域, 或以化學工業爲首之各種產業領域被廣泛使用作爲接著劑 、塗料樹脂之各種聚合物之原料之有用物質的環氧樹脂。 故,本發明之環氧丙基醚化合物之製造方法在工業上可產 生巨大之效果。又,本發明之單烯丙基單環氧丙基醚化合 物由於具有烯丙基,可使其與具有Si-H基之化合物進行 矽氫化反應,由於可對具有各種Si-H基之化合物導入聯 苯基環氧丙基醚基,而可極有用地作爲抗蝕劑類或密封材 類等等所利用之環氧樹脂原料。 【實施方式】 以下,詳細說明本發明。 本發明之環氧丙基醚化合物之製造方法中,氧化劑係 使用過氧化氫。過氧化氫可使用爲過氧化氫水溶液。過氧 化氫之濃度並無特別限制,一般爲選自1〜8 0 %,較佳爲5 〜8 0% ’更佳爲1〇〜60%之範圍。由工業生產性之觀點, 及由分離時之能源成本之觀點,過氧化氫以高濃度爲佳, 另一方面’由經濟性、安全性等之觀點,以不使用過度之 高濃度及/或過剩量之過氧化氫爲佳。過氧化氫之濃度若 未滿1 %時則反應性爲低。過氧化氫之使用量亦無特別限 制’相對於所欲進行環氧化之具有烯丙基醚鍵結之化合物 之烯丙基之碳-碳雙鍵,選自由0.5〜10當量,較佳爲0.8 -11 - 201130806 〜2當量範圍。若在此範圍之外,其中一方之原料變得過 剩殘留而不經濟。 本發明之環氧丙基醚化合物之製造方法中,作爲觸媒 所使用之鎢化合物,以在水中生成鎢酸陰離子之化合物爲 適宜,例如可舉出鎢酸、三酸化鎢、三硫化鎢、六氯化鎢 、磷鎢酸、鎢酸銨、鎢酸鉀二水合物、鎢酸鈉二水合物等 ,且以鎢酸、三酸化鎢、磷鎢酸、鎢酸鈉二水合物等爲佳 。此等鎢化合物可單獨使用,亦可將2種以上混合使用。 此等之在水中生成鎢酸陰離子之化合物之觸媒活性, 相對於鎢酸陰離子1 ·〇,以存在0.2〜0.8之相對陽離子爲 高。此般鎢組成物之調製法,例如可將鎢酸與鎢酸之鹼金 屬鹽以前述比率進行混合,可將鎢酸與鹼化合物(鹼金屬 或鹼土類金屬之氫氧化物、碳酸鹽等)混合,或可將鎢酸 之鹼金屬鹽或鹼土類金屬鹽與磷酸、硫酸等之礦酸般之酸 性化合物組合’藉由此般調製法,可形成鎢酸之部分中和 鹽。此等之較佳具體例,可舉出鎢酸鈉與鎢酸之混合物、 鎢酸鈉與礦酸之混合物、或鎢酸與鹼化合物之混合物。 鎢化合物之作爲觸媒之使用量,鎢元素係以將基質之 具有烯丙基醚鍵結之化合物之烯丙基之碳-碳雙鍵數爲基 準’選自0.0001〜20莫耳%,較佳爲〇·〇ι〜20莫耳%之範 圍。若少於0.0001莫耳%則反應性爲低’若多於20莫耳% ,則不利於成本》 作爲觸媒所使用之3級胺,以鍵結於其氮原子之烷基 之碳數之合計爲6以上’較佳爲丨〇以上之3級有機胺(三 -12- 201130806 烷基胺),因環氧化反應之活性高而爲佳。 此般3級有機胺’可舉出三乙基胺 '三丁基胺、三-η-辛基胺、三-(2-乙基己基)胺、Ν,Ν-二甲基辛基胺、Ν,Ν·二 甲基月桂基胺、Ν,Ν-二甲基十四基胺、Ν,Ν-二甲基十六醯 基胺、Ν,Ν-二甲基十八醯基胺、Ν,Ν-二甲基山嵛基胺、 Ν,Ν-二甲基椰油烷基胺、Ν,Ν-二甲基牛脂烷基胺、Ν,Ν ·二 甲基硬化牛脂烷基胺、Ν,Ν-二甲基十八烯基胺、Ν,Ν-二異 丙基-2-乙基己基胺、Ν,Ν-二丁基-2-乙基己基胺、Ν_甲基 二辛基胺、Ν-甲基二癸基胺、Ν-甲基二椰油烷基胺、N—甲 基硬化牛脂烷基胺、Ν-甲基貳十八烯基胺等。鍵結於3級 胺之氮原子之烷基碳數之合計’若考慮到身爲反應基質之 具有烯丙基醚鍵結之化合物之溶解性,以5 0以下爲佳, 更佳爲3 0以下。 此等之3級胺可單獨使用,亦可將2種以上混合使用 。其使用量係以基質之具有烯丙基醚鍵結之化合物之烯丙 基之碳-碳雙鍵數爲基準’係以選自〇.〇〇〇1〜1〇莫耳%爲 佳’更佳爲ο. ο 1〜1 〇莫耳%之範圍。若少於〇 · 0 〇 〇 1莫耳% 則反應性低’右多於1 〇吴耳%則不利於成本。 本發明之環氧丙基醚化合物之製造方法中,更使用苯 膦酸作爲(助)觸媒。其使用量係以基質之具有烯丙基醚鍵 結之化合物之烯丙基之碳-碳雙鍵數爲基準,以選自 〇_〇〇〇1〜10莫耳%爲佳’更佳爲〇 〇1〜10莫耳Q/。之範圍。 右少於0.0 0 0 1莫耳%則反應性低,若多於1 〇莫耳。/。則不利 於成本。 -13- 201130806 本發明之環氧丙基醚化合物之製造方法中,作爲進行 環氧化之基質,只要係具有烯丙基醚鍵結之化合物則無特 別限制,化合物中所含之烯丙基醚鍵結數可爲1個,亦可 爲2個以上。烯丙基醚鍵結數爲1個之化合物,可例示苯 基烯丙基醚、〇-,m-,p-甲酚單烯丙基醚、聯苯基-2-醇單烯 丙基醚、聯苯基-4-醇單烯丙基醚、丁基烯丙基醚、環己基 烯丙基醚、環己烷甲醇單烯丙基醚等。 烯丙基醚鍵結數爲2個之化合物,可舉出1,5-戊二醇 二烯丙基醚、1,6-己二醇二烯丙基醚、1,9-壬二醇二烯丙 基醚、1,1〇-癸二醇二烯丙基醚 '新戊二醇二烯丙基醚等之 碳數爲2〜20之α,ω -伸烷二醇二烯丙基醚類、碳數2〜20 之α,ω-聚烯烴二醇二烯丙基醚類、1,4-環己烷二甲醇二烯 丙基醚、三環[5.2.1.02’6]癸烷二甲醇二烯丙基醚,或以下 之一般式(1): 【化3】(2) In the formula, 117, 118, 119, and R1() are each independently a hydrogen atom, an alkyl group having 1 to 1 ring of carbon, an alkenyl group having 2 to 10 carbon atoms, and a cycloalkane having 3 to 10 carbon atoms. The base or the aryl group having a carbon number of 6 to 10 is represented by. [13] The monoallyl monoglycidyl ether compound having a biphenyl skeleton according to the above [12], wherein R7, R8, R9, and R1Q in the formula are a methyl group. [Effects of the Invention] According to the method for producing a glycidyl ether compound of the present invention, hydrogen peroxide-10-201130806 and allyl ether are obtained by using a tungsten compound, a tertiary organic amine, and a phenylphosphonic acid as a catalyst. By reacting the compound, the corresponding epoxy propyl ether compound can be produced, and the organic chlorine-based impurities can be inhibited from being mixed as much as possible, and can be simultaneously manufactured in the field of electronic materials with ease and convenience in a simple operation, and at a low cost, or An epoxy resin which is widely used as a raw material for various polymers of a binder and a coating resin in various industrial fields, including the chemical industry. Therefore, the production method of the epoxypropyl ether compound of the present invention can produce a huge effect industrially. Further, since the monoallyl monoepoxypropyl ether compound of the present invention has an allyl group, it can be subjected to a hydrazine hydrogenation reaction with a compound having a Si-H group, since a compound having various Si-H groups can be introduced. It is a biphenyl epoxypropyl ether group which is extremely useful as an epoxy resin raw material used for a resist or a sealing material or the like. [Embodiment] Hereinafter, the present invention will be described in detail. In the method for producing a glycidyl ether compound of the present invention, hydrogen peroxide is used as the oxidizing agent. Hydrogen peroxide can be used as an aqueous hydrogen peroxide solution. The concentration of hydrogen peroxide is not particularly limited and is generally selected from the range of 1 to 80%, preferably 5 to 80%, more preferably 1 to 60%. From the viewpoint of industrial productivity, and from the viewpoint of energy costs at the time of separation, hydrogen peroxide is preferably at a high concentration, and on the other hand, from the viewpoint of economy, safety, etc., without using excessively high concentrations and/or Excess amount of hydrogen peroxide is preferred. If the concentration of hydrogen peroxide is less than 1%, the reactivity is low. The amount of hydrogen peroxide used is also not particularly limited to a carbon-carbon double bond of an allyl group having an allyl ether-bonded compound to be epoxidized, and is selected from 0.5 to 10 equivalents, preferably 0.8. -11 - 201130806 ~ 2 equivalent range. If it is outside this range, the raw materials of one of them become excessive and uneconomical. In the method for producing a glycidyl ether compound of the present invention, a tungsten compound used as a catalyst is preferably a compound which forms a tungstate anion in water, and examples thereof include tungstic acid, tungsten trisulfide, and tungsten trisulfide. Hexachlorochloride, phosphotungstic acid, ammonium tungstate, potassium tungstate dihydrate, sodium tungstate dihydrate, etc., and tungstic acid, tungsten trioxide, phosphotungstic acid, sodium tungstate dihydrate, etc. . These tungsten compounds may be used singly or in combination of two or more. The catalytic activity of such a compound which forms a tungstic anion in water is higher than that of the tungstic anion 1 · 以 in the presence of a relative cation of 0.2 to 0.8. For the preparation method of the tungsten composition, for example, an alkali metal salt of tungstic acid and tungstic acid can be mixed at the above ratio, and tungstic acid and an alkali compound (hydroxide, carbonate, etc. of an alkali metal or an alkaline earth metal) can be used. Mixing, or by combining an alkali metal salt or an alkaline earth metal salt of tungstic acid with a mineral acid-like acidic compound such as phosphoric acid or sulfuric acid, a partial neutralizing salt of tungstic acid can be formed by this preparation method. Preferred examples of such a compound include a mixture of sodium tungstate and tungstic acid, a mixture of sodium tungstate and mineral acid, or a mixture of tungstic acid and an alkali compound. The tungsten compound is used as a catalyst. The tungsten element is selected from 0.0001 to 20 mol% based on the number of carbon-carbon double bonds of the allyl group of the compound having an allyl ether bond. Good for 〇·〇ι~20% of the range. If less than 0.0001% by mole, the reactivity is low 'if more than 20% by mole, which is disadvantageous to cost." The tertiary amine used as a catalyst, the carbon number of the alkyl group bonded to the nitrogen atom thereof. The total of 6 or more organic acids (three-12-201130806 alkylamine) which is preferably 丨〇 or more is preferable because of the high activity of the epoxidation reaction. Examples of the tertiary organic amines include triethylamine 'tributylamine, tri-η-octylamine, tris-(2-ethylhexyl)amine, hydrazine, hydrazine-dimethyloctylamine, Ν,Ν·Dimethyl laurylamine, hydrazine, hydrazine-dimethyltetradecylamine, hydrazine, hydrazine-dimethylhexadecanylamine, hydrazine, hydrazine-dimethyloctadecylamine, hydrazine , Ν-dimethyl behenylamine, hydrazine, hydrazine-dimethyl cocoalkylamine, hydrazine, hydrazine-dimethyl tallow alkylamine, hydrazine, hydrazine, dimethyl hardened tallow alkylamine, hydrazine , Ν-dimethyloctadecylamine, hydrazine, hydrazine-diisopropyl-2-ethylhexylamine, hydrazine, hydrazine-dibutyl-2-ethylhexylamine, hydrazine-methyldioctyl Amine, hydrazine-methyl dimethyl decylamine, hydrazine-methyl dicocoalkylamine, N-methyl hardened tallow alkylamine, hydrazine-methyl octadecylamine, and the like. The total number of alkyl carbon atoms bonded to the nitrogen atom of the tertiary amine 'if it is considered to be the solubility of the compound having an allyl ether bond as a reaction substrate, preferably 5 or less, more preferably 3 0 the following. These tertiary amines may be used singly or in combination of two or more. The amount used is based on the number of carbon-carbon double bonds of the allyl ether-bonded compound of the matrix, and is selected from the group consisting of 〇.〇〇〇1~1〇mol% is better. Good for ο. ο 1~1 〇 Moer% range. If less than 〇 · 0 〇 〇 1 mol%, the reactivity is low. Right more than 1 〇 耳 耳 ear% is not conducive to cost. In the method for producing a glycopropyl ether compound of the present invention, phenylphosphonic acid is further used as a (helper) catalyst. The amount thereof is based on the number of carbon-carbon double bonds of the allyl group of the compound having an allyl ether bond in the matrix, and is preferably selected from the group consisting of 〇_〇〇〇1 to 10 mol%. 〇〇 1~10 Moh Q/. The scope. If the right is less than 0.00 0 1%, the reactivity is low, if more than 1 mole. /. It is not good for cost. In the method for producing a epoxidized propyl ether compound of the present invention, the epoxidized substrate is not particularly limited as long as it is a compound having an allyl ether bond, and the allyl ether contained in the compound is not particularly limited. The number of key knots may be one or two or more. a compound having a number of allyl ether linkages, which may be exemplified by phenyl allyl ether, hydrazine-, m-, p-cresol monoallyl ether, biphenyl-2-ol monoallyl ether And biphenyl-4-ol monoallyl ether, butyl allyl ether, cyclohexyl allyl ether, cyclohexane methanol monoallyl ether and the like. The compound having two groups of allyl ether linkages may, for example, 1,5-pentanediol diallyl ether, 1,6-hexanediol diallyl ether, 1,9-nonanediol II α,ω-alkylene glycol diallyl ether having a carbon number of 2 to 20, such as allyl ether, 1,1 fluorene-decanediol diallyl ether, neopentyl glycol diallyl ether α,ω-polyolefin diol diallyl ether, 1,4-cyclohexanedimethanol diallyl ether, tricyclo[5.2.1.0'6] decane II Methanol diallyl ether, or the following general formula (1): [Chemical 3]

{式中,R1、及R2各自獨立爲氫原子、碳數1〜6之院基 、碳數2〜6之烯基、碳數3〜12之環烷基、或碳數6〜10 之芳基,或,R1與R2可一起形成碳數2〜6之亞烷基或碳 數3〜12之環亞烷基。113、1^4、1^5、及尺6各自獨立爲氫 -14- 201130806 原子、碳數1〜10之烷基、碳數2〜10之烯基、 12之環院基或碳數6〜10之芳基,且η表示0或 }所表示之化合物。在此,η爲0時則表示2個 地鍵結(聯苯骨架)。此等之中,以R1〜R6各自獨 子或甲基,η爲1或0者爲更佳。 此般化合物,具體地可舉出雙酚-Α之二烯 雙酚-F之二烯丙基醚、2,6,2’,6’-四甲基雙酚-八 醚、2,2’-二烯丙基雙酚-Α二烯丙基醚、2,2’-二 酚-Α二烯丙基醚、4,4’ -聯酚二烯丙基醚、2,2’-聯酚二烯丙基醚、4,4’-亞乙基雙酣二稀丙基醚、 己基雙酚二烯丙基醚、4,4’-(1-α -甲基亞亨基)雙 基醚、4,4’-(3,3,5-三甲基環亞己基)雙酚二烯 4,4’-(1-甲基-亞苄基)雙酚二烯丙基醚、3,3,,5,ί 聯苯基-4,4’-二烯丙基醚等。 又’烯丙基醚鍵結數爲3個以上之化合物 酚-甲醛•烯丙醇聚縮合物或甲酚-甲醛.烯丙醇 等。 此等基質可不使用有機溶劑,或依據需要使 劑,使過氧化氫水溶液與前述之觸媒混合而使環 進行,於不使用有機溶劑而進行環氧化反應,在 減低、製造設備之簡略化(例如防爆設備之省略| 物處理、作業環境之改善等之面上爲有利。在使 ,因有反應速度變慢且依據溶劑有水解反應等之 應變得容易進行之情形,而有適宜選擇之必要。 碳數3〜 1之整數 苯環直接 立爲氫原 丙基醚、 二烯丙基 -t-丁基雙 二異丙基 4,4’-環亞 酚二烯丙 丙基醚、 四甲基 ,可舉出 聚縮合物 用有機溶 氧化反應 製造成本 爭)、廢棄 用溶劑時 不理想反 在作爲反 -15 - 201130806 應基質之具有烯丙基醚鍵結之化合物之黏度過高時,或在 固體時,可使用其必要之最小限度之有機溶劑。可使用之 有機溶劑,以芳香族烴、脂肪族烴或脂環式烴爲佳,例如 可舉出甲苯、茬、己烷、辛烷、環己烷等。其使用量,以 保留在其必要之最小限度,由製造成本等之觀點爲有利, 相對於具有烯丙基醚鍵結之化合物1 00質量份,較佳使用 5 0質量份以下,更佳爲使用3 0質量份以下。有機溶劑之 使用量,相對於具有烯丙基醚鍵結之化合物1 00質量份, 若超過5 0質量份時,則基質濃度變低,反應性下降。 又,作爲進行環氧化之方法,若考慮到工業上安定的 生產,可將觸媒與基質最先置於反應器中,極力地保持反 應溫度爲固定溫度,並確認過氧化氫因反應而被消費之情 況,同時徐徐地加入。若採用此般方法,在反應器內即使 過氧化氫異常分解而產生氧氣體,過氧化氫之積存量爲少 而可使壓力上昇至於最小限度。 由於反應溫度若過高時則有副反應變多,且,過氧化 氫亦變得容易分解,在過低時則有過氧化氫之消費速度變 慢,積存於反應系統內,故反應溫度選自較佳爲-10〜120 °C,更佳爲20°C〜l〇〇°C之範圍。 反應結束後,水層與有機層之比重差有幾乎無差異之 情況,此時藉由對水層混合無機化合物之飽和水溶液,使 其與有機層產生比重差,即使係不用使用有機萃取溶劑亦 可進行二層分離。特別係,由於鎢化合物之比重爲重,爲 了使水層沉於下層,亦可使用超過本來觸媒所需要之前述 -16- 201130806 使用量之鎢化合物。此時,以再使用來自水層之鎢化合物 ,而提高鎢化合物之效率爲佳。 又,反之,根據基質而亦有有機層之比重變得接近 1 .2者,於此時,再添加水,藉由使水層之比重接近於1 ,而亦可使上層爲水層,下層爲有機層。又,反應液之萃 取使用甲苯、環己烷、己烷、二氯甲烷等之有機溶劑實施 萃取亦可,可因應狀況選擇最適合之分離方法。 如此般將與水層分離後之有機層予以濃縮後,藉由蒸 餾、層析分離、再結晶或昇華等之通常方法,可取出所得 之環氧丙基醚化合物。具有烯丙基醚鍵結之化合物爲具有 2個烯丙基醚鍵結之化合物時,藉由進行上述分離純化操 作,可從反應生成物將僅一方之烯丙基醚鍵結受到環氧化 之單烯丙基單環氧丙基醚化合物予以單離。例如,將具有 聯苯骨架之二烯丙基醚化合物作爲基質使用時,有機層中 含有單烯丙基單環氧丙基醚、二環氧丙基醚、及未反應之 二烯丙基醚化合物,從此等中可藉由後述之實施例1 6中 記載之管柱層析法等之純化,而得到例如以下之一般式(2) 【化4】In the formula, R1 and R2 are each independently a hydrogen atom, a carbon number of 1 to 6, a carbon number of 2 to 6 alkenyl groups, a cycloalkyl group having a carbon number of 3 to 12, or a carbon number of 6 to 10 Or, R1 and R2 may together form an alkylene group having 2 to 6 carbon atoms or a cycloalkylene group having 3 to 12 carbon atoms. 113, 1^4, 1^5, and 6 are each independently hydrogen-14-201130806 atom, carbon number 1~10 alkyl group, carbon number 2~10 alkenyl group, 12 ring hospital base or carbon number 6 An aryl group of ~10, and η represents a compound represented by 0 or }. Here, when η is 0, it means two bond bonds (biphenyl skeleton). Among these, it is more preferable that each of R1 to R6 is a single or a methyl group, and η is 1 or 0. Specific examples of the compound include diallyl ether of bisphenol-indene diene bisphenol-F, 2,6,2',6'-tetramethylbisphenol-octaether, 2,2' -Diallyl bisphenol-indole diallyl ether, 2,2'-diphenol-decadienyl ether, 4,4'-biphenol diallyl ether, 2,2'-biphenol Diallyl ether, 4,4'-ethylenebisguanidinium diisopropyl ether, hexyl bisphenol diallyl ether, 4,4'-(1-α-methylheptylene) bis-ether , 4,4'-(3,3,5-trimethylcyclohexylene) bisphenol diene 4,4'-(1-methyl-benzylidene) bisphenol diallyl ether, 3,3 ,, 5, ί biphenyl-4,4'-diallyl ether, and the like. Further, a compound having three or more allylic ether linkages is a phenol-formaldehyde/allyl alcohol polycondensate or cresol-formaldehyde. Allyl alcohol. These substrates may be subjected to an epoxidation reaction without using an organic solvent by mixing an aqueous hydrogen peroxide solution with the above-mentioned catalyst, without using an organic solvent, or by pulsing the hydrogen peroxide aqueous solution, and reducing the manufacturing equipment. For example, it is advantageous to omit the use of the explosion-proof equipment, the improvement of the work environment, and the improvement of the working environment, etc., and it is necessary to select it because the reaction rate is slow and the hydrolysis reaction is required depending on the solvent. An integer number of benzene rings having a carbon number of 3 to 1 is directly represented by hydrogen propyl ether, diallyl-t-butyl bisdiisopropyl 4,4'-cyclo arylene diallyl ether, tetramethyl The base may be exemplified by the fact that the polycondensate is produced by the organic solution oxidation reaction, and the solvent for disposal is not ideal. When the viscosity of the compound having the allyl ether bond as the substrate is too high, Or in the case of a solid, the minimum necessary organic solvent can be used. The organic solvent which can be used is preferably an aromatic hydrocarbon, an aliphatic hydrocarbon or an alicyclic hydrocarbon, and examples thereof include toluene, hydrazine, hexane, octane, and cyclohexane. The amount of use thereof is preferably from the viewpoint of the production cost and the like, and is preferably 50 parts by mass or less, more preferably 50 parts by mass or less, based on the production cost of the compound having an allyl ether bond. Use 30 parts by mass or less. When the amount of the organic solvent used is more than 50 parts by mass based on 100 parts by mass of the compound having an allyl ether bond, the substrate concentration is lowered and the reactivity is lowered. Further, as a method of performing epoxidation, in consideration of industrially stable production, the catalyst and the substrate can be placed in the reactor first, and the reaction temperature is kept at a fixed temperature as much as possible, and it is confirmed that hydrogen peroxide is reacted by the reaction. The situation of consumption, while slowly joining. According to this method, even if hydrogen peroxide is abnormally decomposed in the reactor to generate oxygen gas, the amount of hydrogen peroxide stored is small, and the pressure can be increased to a minimum. When the reaction temperature is too high, there are many side reactions, and hydrogen peroxide is also easily decomposed. When the temperature is too low, the consumption rate of hydrogen peroxide is slow and accumulated in the reaction system. It is preferably in the range of -10 to 120 ° C, more preferably in the range of 20 ° C to 10 ° C. After the completion of the reaction, there is almost no difference in the difference in specific gravity between the water layer and the organic layer. At this time, by mixing the aqueous layer with a saturated aqueous solution of the inorganic compound, the specific gravity difference is caused to the organic layer, even if the organic extraction solvent is not used. Two layers of separation are possible. In particular, since the specific gravity of the tungsten compound is heavy, in order to sink the water layer to the lower layer, it is also possible to use a tungsten compound which exceeds the amount of the above-mentioned -16-201130806 required for the original catalyst. At this time, it is preferable to further increase the efficiency of the tungsten compound by reusing the tungsten compound derived from the water layer. On the other hand, depending on the substrate, the specific gravity of the organic layer becomes close to 1.2. At this time, water is further added, and by making the specific gravity of the water layer close to 1, the upper layer may be the water layer and the lower layer. It is an organic layer. Further, the extraction of the reaction liquid may be carried out by using an organic solvent such as toluene, cyclohexane, hexane or dichloromethane, and the most suitable separation method may be selected depending on the conditions. After the organic layer separated from the aqueous layer is concentrated in this manner, the obtained epoxy propyl ether compound can be taken out by a usual method such as distillation, chromatography, recrystallization or sublimation. When the compound having an allyl ether bond is a compound having two allyl ether bonds, by performing the above separation and purification operation, only one of the allyl ether bonds can be epoxidized from the reaction product. The monoallyl monoepoxypropyl ether compound is isolated. For example, when a diallyl ether compound having a biphenyl skeleton is used as a substrate, the organic layer contains monoallyl monoepoxypropyl ether, diepoxypropyl ether, and unreacted diallyl ether. The compound can be purified by column chromatography as described in Example 16 to be described later, and the following general formula (2) can be obtained, for example.

{式中’ R7、R8、R9、及RIQ各自獨立表示氫原子、碳數 201130806 1〜10之烷基、碳數2〜10之烯基、碳數3〜丨〇之環烷基 或碳數6〜10之芳基}所表示之單烯丙基單環氧丙基醚。 R7、R8、R9、及R10亦可爲甲基。 [實施例] 以下’依據實施例更具體說明本發明,但本發明並非 係受以下之實施例所限定者^ [實施例1] 對裝備有滴入漏斗、戴氏冷凝器之300mL三頸燒杯放 入鎢酸鈉(日本無機化學工業(股)製)0.95 0g(2.88mmol)、鎢 酸(日本無機化學工業(股)製)0.720g(2.88mmol)、三辛基胺 (廣榮化學(股)製)2.04g(5_76mmol)、苯膦酸(日產化學(股) 製)0.911g(5_76mmol)、烯丙基苯基醚 80g(0.576mol),以 磁攪拌器進行攪拌且同使以油浴加溫至70 °C後,使反應溫 度不超過75 °C而滴下35 %過氧化氫水溶液84.0g(0.864 mol)。滴下結束後,持續攪拌2小時,並使反應液冷卻至 室溫。其後’追加乙酸乙酯40g,使上層爲有機層而下層 爲水層,並將有機層分離。 分析此有機層之結果,烯丙基苯基醚之轉化率爲 55.8%,且對環氧丙基苯基醚之選擇率爲66.3%。 尙且,轉化率及選擇率係以藉氣相層析法所分析之結 果爲基準,依據以下之計算式所計算者。 -18- 201130806 轉化率(%) = (1-殘留之原料莫耳數/已使用之原料莫耳數)χ1〇〇 選擇率(%)={(目的化合物之莫耳數/已使用之原料莫耳數)χ10000}/轉化率(%) [比較例1] 除了未添加苯膦酸以外’其他與實施例1同樣之條件 下進行反應。其結果’嫌丙基苯基酸之轉化率爲3.6%, 以氣相層析法僅檢測出極少量之環氧丙基苯基醚。 [比較例2 ] 除了未添加三辛基胺以外,其他與實施例1同樣之條 件下進行反應。其結果,烯丙基苯基醚之轉化率爲5 . 3 % ,以氣相層析法僅檢測出極少量之環氧丙基苯基酸。 [實施例2〜10] 以以下之表1所示之觸媒成分、置放莫耳比,與實施 例1同樣地進行環氧化反應。將其結果一倂表示於以下之 表1。 -19- 201130806 環氧丙基苯基醚 選擇率 66. 3% 54. 8% 59.1% 59. 9% 68. 4% 43. 5% 67. 2% 77. 1% 44. 2% 56. 7% 收率 37.0% 33. 9% 32. 8% 35. 9% 26.8% 17.6% 25.2% 36. 9% 21.7% 18.5% 轉化率 55.8% 61. 9% 55. 6% 59. 9% 39. 1% 40. 6% 37. 5% 47. 5% 49. 2% 32. 6% g ft « «VI rn S g S S S S S τ— S Q in Ο LO 其他 0. 25 in CD 2: « r— Ο- τ τ— *— 1 11 τ— W CNJ LO Ο LO 〇 ID d LO LO Ο LO Ο ir> ο in ci m CP LO d ΙΓ3 ir> c> c> LO o 觸媒 其他 50%硫酸 NaOH ζ 三辛基胺 甲基二辛基胺 甲基二辛基胺 甲基二辛基胺 甲基二辛基胺 三乙基胺 三丁基胺 三己基胺 二甲基辛基胺 Kl§ ά糊 niru 〇u 苯基膦酸 (日產化學) 苯基膦酸 苯基膦酸 苯基膦酸 苯基膦酸 苯基膦酸 誦酸1 苯基膦酸 --—-1 苯基膦酸 苯基膦酸\ (曰產化學) .^ T Ps« h2wo4 H2W〇4 (St HjW04 NazW04-2H?0 個形) 〇 〇 E 法一 Na2W04 ·2Η20 個形) NazW04 ·2Η20 個形) Na2W04-2H20 個形) Naz W0, ·2ΗΖ0 涸形) Na2W04.2H20 個形) NazW04 ·2Η20 (固形) o . <Si □C C?画 3= ^ CM CQ CVJ CO xr LT3 卜 GO σ) 〇 -20- 201130806 [合成例1]:雙酚-F之二烯丙基醚之合成 對2000ml之茄型燒杯放入雙酚-F-ST(三井化學(股)製 )200g(0.999mol)、50%含水 5%-Pd/C-STD 型(N.E.CHEMCAT(股) 製)2.13g(0.499mm〇l)、三苯基膦(北興化學(股)製)2.62g (9.99mmol)、碳酸鉀(旭硝子(股)製)276g(2.00mol)、乙酸 烯丙酯(昭和電工(股)製)220g(2.20mol)、及異丙醇200g, 於氮環境中’以8 5 °C反應8小時。反應後,採樣一部份, 以乙酸乙酯稀釋後,以氣相層析法進行分析,確認了雙 酚-F二烯丙基醚對單烯丙基醚之比率變至99: 1。 此後,對反應液加入甲苯400g,將Pd/C與析出之固 體以過濾去除,並藉由蒸發器將異丙醇與甲苯餾去。將此 反應、後處理操作重複4次後,藉由分子蒸餾裝置(大科 工業(股)製),而得到餾出物748 g(單離收率66%、雙酚-F 二烯丙基醚98.7%、剩餘爲單烯丙基醚)、非餾出物3 68 g( 雙酚-F二烯丙基醚8 8%)。此等之分析係藉由氣相層析法 所進行。餾出物之25°C中之黏度爲25mPa. s(以B型黏度 計(BROOKFIELD 製 D V - E (型式:L V D V - E))測定)。又,異 構物比爲〇,〇,-: o,p’-: p,p’- = 17: 52: 31(由氣相層析法 所得之分析値)。 [合成例2]:3,3’,5,5’-四甲基聯苯基-4,4’-二烯丙基醚之合成 對2000ml之茄型燒杯,放入3,3’,5,5’-四甲基·4,4’-聯苯基二醇(中國:甘肅省化工硏究院製)150g(0.619mol) 、50% 含水 5%-Pd/C-STD 型(N.E.CHEMCAT(股)製 -21 - 201130806 )1.32g(0.310mmol)、三苯基膦(北興化學(股)製)i.624g (6.19 mmol)、碳酸鉀(日本曹達(股)製)i71g(1.24mol)、乙酸烯丙酯( 昭和電工(股)製)136g(1.36mol)、及異丙醇68.1g,於氮環 境中,以85 °C反應8小時。反應後,採樣一部份,以乙酸 乙酯稀釋後,由氣相層析法所得之分析,確認了 3,3’,5,5’-四甲基聯苯基-4,4’-二烯丙基醚對單烯丙基醚之 比率變爲至97: 3。 之後,對反應液加入甲苯200g,將Pd/C與析出之固 體過濾去除,並藉由蒸發器將異丙醇與甲苯餾去。重複此 反應、後處理操作4次後,藉由分子蒸餾裝置(大科工業( 股)製)而得到餾出物127.5g(單離收率66%、二烯丙基醚 97.9%、剩餘爲單烯丙基醚)、非餾出物31 .7g(二烯丙基醚 97.5%)。此等分析係以氣相層析法所進行。餾出物係融點 爲51.7°C之固體,60°C中之黏度爲29mPa. s(以B型黏度 計(BROOKFIELD 製 DV-E(型式:LVDV-E))測定)。 [合成例3]: 1,4-環己烷二甲醇二烯丙基醚之合成 對 1000ml 之燒杯放入 1,4 -環己二醇(Eastman Chemicals 製)100g(0.693mol)、50% 氫氧化鈉水溶液 110.9g(1.39mol) 、溴化四 丁基銨(LION AKZO(股)製)1.12g(3.47mmol)、氯 化烯丙基132.7g(1.73mol),於氮氣流下,首先進行以4〇 °C加熱,伴隨反應之進行而徐徐地提高反應溫度,經時3 小時升溫至70°C後,更使其反應1 7小時。使反應液冷卻 至室溫,加入甲苯200ml而萃取反應物,將有機層以純水 -22- 201130806 洗淨2次。藉由蒸發器將甲苯餾去後,藉由減壓蒸餾,將 初餾份除去後,得到沸點8 〇 . 4 t /2 8 P a之餾出分8 4 · 6 g (二 稀丙基醚94% '剩餘爲單烯丙基醚)。此等分析係以氣相 層析法進行。又,餾出物之25t中之黏度爲8.5mPa.s( 以B型黏度計(BROOKFIELD製DV-E(型式:LVDV-E))測 定)。 [合成例4]: 1,6-己二醇二烯丙基醚之合成 對1 000ml之燒杯放入16 —己二醇(東京化成(股)製) 1 00g(0.846mol)、50%氫氧化鈉水溶液 1 3 5 · 4 g (1 · 6 9 m ο 1)、 溴化四 丁基銨(LION AKZO(股)製)1.36g(4.23mmol)、氯化 烯丙基161.9g(2.12mol),於氮氣流下,首先進行以40T: 加熱,伴隨反應之進行,徐徐地提高反應溫度,經時2小 時升溫至70°C後,更使其反應1 0小時。使反應液冷卻至 室溫,加入甲苯200ml而萃取反應物,將有機層以純水洗 淨2次。藉由蒸發器將甲苯餾去後,並藉由減壓蒸餾將初 餾份除去後,得到沸點7 2 °C /1 3 3 P a之餾出分8 4.6 g (二烯 丙基醚97%、剩餘爲單烯丙基醚)。此等分析係以氣相層 析法進行。又,餾出物之25°C中之黏度爲2.3mPa . s(以B 型黏度計(BROOKFIELD製DV-E(型式:LVDV-E))測定)。 [實施例1 1〜1 5 ] 除將實施例1之烯丙基苯基醚取代爲以下之表2中所 示之化合物以外,其他與實施例1同樣地進行環氧化反應 -23- 201130806 。將其結果一倂表示於以下之表2。In the formula, R7, R8, R9, and RIQ each independently represent a hydrogen atom, an alkyl group having a carbon number of 201130806, 1 to 10, an alkenyl group having 2 to 10 carbon atoms, a cycloalkyl group having a carbon number of 3 to fluorene, or a carbon number. Monoallyl monoepoxypropyl ether represented by 6 to 10 aryl}. R7, R8, R9, and R10 may also be a methyl group. [Examples] Hereinafter, the present invention will be more specifically described based on the examples, but the present invention is not limited by the following examples. [Example 1] A 300 mL three-necked beaker equipped with a dropping funnel and a Daicel condenser 0.95 0g (2.88mmol) of tungstate sodium (made by Nippon Inorganic Chemical Industry Co., Ltd.), 0.720g (2.88mmol) of tungstic acid (made by Nippon Inorganic Chemical Industry Co., Ltd.), and trioctylamine (Growong Chemical ( (manufactured by the company) 2.04 g (5-76 mmol), phenylphosphonic acid (manufactured by Nissan Chemical Co., Ltd.), 0.911 g (5-76 mmol), allyl phenyl ether 80 g (0.576 mol), stirred with a magnetic stirrer After the bath was warmed to 70 ° C, the reaction temperature was not more than 75 ° C and 84.0 g (0.864 mol) of a 35 % aqueous hydrogen peroxide solution was dropped. After the completion of the dropwise addition, stirring was continued for 2 hours, and the reaction liquid was allowed to cool to room temperature. Thereafter, 40 g of ethyl acetate was added, and the upper layer was an organic layer and the lower layer was an aqueous layer, and the organic layer was separated. As a result of analyzing the organic layer, the conversion of allyl phenyl ether was 55.8%, and the selectivity to p- propyl propyl ether was 66.3%. Further, the conversion rate and the selectivity are based on the results analyzed by gas chromatography, and are calculated based on the following calculation formula. -18- 201130806 Conversion rate (%) = (1 - residual raw material moles / used raw material moles) χ 1 〇〇 selectivity (%) = { (molar of the target compound / used raw materials Molar number) χ 10000} / conversion ratio (%) [Comparative Example 1] The reaction was carried out under the same conditions as in Example 1 except that phenylphosphonic acid was not added. As a result, the conversion ratio of the propyl phenyl acid was 3.6%, and only a very small amount of the epoxypropyl phenyl ether was detected by gas chromatography. [Comparative Example 2] The reaction was carried out under the same conditions as in Example 1 except that trioctylamine was not added. As a result, the conversion of allyl phenyl ether was 5.3 %, and only a very small amount of glycidyl phenyl acid was detected by gas chromatography. [Examples 2 to 10] The epoxidation reaction was carried out in the same manner as in Example 1 except that the catalyst components shown in Table 1 below were placed and the molar ratio was placed. The results are shown in Table 1 below. -19- 201130806 Epoxypropyl phenyl ether selectivity rate of 66.3% 54.8% 59.1% 59.9% 68. 4% 43. 5% 67. 2% 77. 1% 44. 2% 56. 7 % yield 37.0% 33. 9% 32. 8% 35. 9% 26.8% 17.6% 25.2% 36. 9% 21.7% 18.5% Conversion rate 55.8% 61. 9% 55. 6% 59. 9% 39. 1 % 40. 6% 37. 5% 47. 5% 49. 2% 32. 6% g ft « «VI rn S g SSSSS τ — SQ in Ο LO Other 0. 25 in CD 2: « r — Ο- τ τ—*— 1 11 τ—W CNJ LO Ο LO 〇ID d LO LO Ο LO Ο ir> ο in ci m CP LO d ΙΓ3 ir>c>c> LO o catalyst other 50% sulfuric acid NaOH ζ trioctyl Aminomethyldioctylaminemethyldioctylaminemethyldioctylaminemethyldioctylaminetriethylaminetributylaminetrihexylaminedimethylamine amide Kl§ niniru 〇u benzene Phosphonic acid (Nissan Chemical) phenylphosphonic acid phenylphosphonic acid phenylphosphonic acid phenylphosphonic acid phenylphosphonic acid decanoic acid 1 -phenylphosphonic acid --1 phenylphosphonic acid phenylphosphonic acid \ (曰Production Chemistry) .^ T Ps« h2wo4 H2W〇4 (St HjW04 NazW04-2H?0 Shape) 〇〇E Method One Na2W04 ·2Η20 Shapes) NazW 04 · 2Η20 Shapes) Na2W04-2H20 Shape) Naz W0, ·2ΗΖ0 涸 Shape) Na2W04.2H20 Shape) NazW04 ·2Η20 (Solid) o . <Si □CC?Draw 3= ^ CM CQ CVJ CO xr LT3卜GO σ) 〇-20- 201130806 [Synthesis Example 1]: Synthesis of diallyl ether of bisphenol-F In a 2000 ml eggplant type beaker, bisphenol-F-ST (manufactured by Mitsui Chemicals Co., Ltd.) 200 g (0.999mol), 50% aqueous 5%-Pd/C-STD type (NECHEMCAT), 2.13g (0.499mm〇l), triphenylphosphine (Beixing Chemical Co., Ltd.) 2.62g (9.99) Methyl), potassium carbonate (manufactured by Asahi Glass Co., Ltd.) 276 g (2.00 mol), allyl acetate (manufactured by Showa Denko Co., Ltd.) 220 g (2.20 mol), and isopropanol 200 g, in a nitrogen atmosphere '8 5 The reaction was carried out for 8 hours at °C. After the reaction, a part was sampled, diluted with ethyl acetate, and analyzed by gas chromatography to confirm that the ratio of bisphenol-F diallyl ether to monoallyl ether was changed to 99:1. Thereafter, 400 g of toluene was added to the reaction liquid, and Pd/C and the precipitated solid were removed by filtration, and isopropyl alcohol and toluene were distilled off by an evaporator. After repeating this reaction and the post-treatment operation four times, a distillate of 748 g (66% yield, bisphenol-F diallyl) was obtained by a molecular distillation apparatus (manufactured by Daikoku Co., Ltd.). The ether was 98.7%, the remainder was monoallyl ether), and the non-distillate was 3 68 g (bisphenol-F diallyl ether 8 8%). These analyses were carried out by gas chromatography. The viscosity of the distillate at 25 ° C was 25 mPa·s (determined by B-type viscosity meter (DRO-E (type: L V D V - E)). Further, the isomer ratio is 〇, 〇, -: o, p'-: p, p'- = 17: 52: 31 (analytical enthalpy obtained by gas chromatography). [Synthesis Example 2]: Synthesis of 3,3',5,5'-tetramethylbiphenyl-4,4'-diallyl ether For a 2000 ml eggplant type beaker, put in 3,3',5 , 5'-Tetramethyl·4,4'-biphenyldiol (China: Gansu Chemical Research Institute) 150g (0.619mol), 50% water 5%-Pd/C-STD type (NECHEMCAT (Stock)-21 - 201130806 ) 1.32g (0.310mmol), triphenylphosphine (Beixing Chemical Co., Ltd.) i.624g (6.19 mmol), potassium carbonate (made by Japan Soda Co., Ltd.) i71g (1.24mol) 136 g (1.36 mol) of allylic acetate (manufactured by Showa Denko Co., Ltd.) and 68.1 g of isopropyl alcohol were reacted at 85 ° C for 8 hours in a nitrogen atmosphere. After the reaction, a portion was sampled and diluted with ethyl acetate, and analyzed by gas chromatography to confirm 3,3',5,5'-tetramethylbiphenyl-4,4'-di The ratio of allyl ether to monoallyl ether was changed to 97:3. Thereafter, 200 g of toluene was added to the reaction liquid, and Pd/C and the precipitated solid were removed by filtration, and isopropyl alcohol and toluene were distilled off by an evaporator. After repeating this reaction and the post-treatment operation four times, 127.5 g of a distillate was obtained by a molecular distillation apparatus (manufactured by Daikoku Co., Ltd.) (the yield was 66%, the diallyl ether was 97.9%, and the balance was Monoallyl ether), non-distillate 31.7 g (diallyl ether 97.5%). These analyses were carried out by gas chromatography. The distillate had a melting point of 51.7 ° C and a viscosity at 60 ° C of 29 mPa·s (measured by B-type viscosity (DRO-E (type: LVDV-E)). [Synthesis Example 3]: Synthesis of 1,4-cyclohexanedimethanol diallyl ether In a 1000 ml beaker, 1,4-cyclohexanediol (manufactured by Eastman Chemicals) 100 g (0.693 mol), 50% hydrogen was placed. 110.9 g (1.39 mol) of an aqueous sodium oxide solution, 1.12 g (3.47 mmol) of tetrabutylammonium bromide (manufactured by LION AKZO Co., Ltd.), and 132.7 g (1.73 mol) of allyl chloride, were firstly flowed under a nitrogen stream. After heating at 4 ° C, the reaction temperature was gradually increased as the reaction progressed, and the temperature was raised to 70 ° C over 3 hours, and further reacted for 17 hours. The reaction solution was cooled to room temperature, and toluene (200 ml) was added to extract the mixture, and the organic layer was washed twice with pure water -22-201130806. After the toluene is distilled off by an evaporator, the initial fraction is removed by distillation under reduced pressure to obtain a boiling point of 8 〇. 4 t / 2 8 P a of 8 4 · 6 g (di-l-propyl ether) 94% 'remaining monoallyl ether'). These analyses were carried out by gas chromatography. Further, the viscosity in the 25 t of the distillate was 8.5 mPa·s (measured by a B-type viscometer (DV-E (type: LVDV-E) manufactured by BROOKFIELD). [Synthesis Example 4]: Synthesis of 1,6-hexanediol diallyl ether In a beaker of 1 000 ml, 16-hexanediol (manufactured by Tokyo Chemical Industry Co., Ltd.) 100 g (0.846 mol), 50% hydrogen Aluminium oxide aqueous solution 1 3 5 · 4 g (1 · 6 9 m ο 1), tetrabutylammonium bromide (manufactured by LION AKZO Co., Ltd.) 1.36 g (4.23 mmol), allyl chloride 161.9 g (2.12 mol) The mixture was first heated at 40 T: under a nitrogen stream, and the reaction temperature was gradually increased as the reaction progressed. After the temperature was raised to 70 ° C over 2 hours, the reaction was further carried out for 10 hours. The reaction solution was cooled to room temperature, and 200 ml of toluene was added thereto to extract the reactant, and the organic layer was washed twice with pure water. After the toluene was distilled off by an evaporator, and the initial fraction was removed by distillation under reduced pressure, a distillation fraction of 82.6 ° C / 1 3 3 P a was obtained, 84.6 g (diallyl ether 97%). The remainder is monoallyl ether). These analyses were carried out by gas phase chromatography. Further, the viscosity of the distillate at 25 ° C was 2.3 mPa·s (measured by a B-type viscosity meter (DV-E (type: LVDV-E) manufactured by BROOKFIELD). [Example 1 1 to 1 5] An epoxidation reaction was carried out in the same manner as in Example 1 except that the allylphenyl ether of Example 1 was substituted with the compound shown in Table 2 below. The results are shown in Table 2 below.

-24- 201130806 [實施例1 6 ] 由貫施例13所得之生成物將單環氧丙基單烯丙基醚 予以單離’於本實施例中予以鑑定。其實驗順序如以下之 說明。 對裝備有滴入漏斗、戴氏冷凝器之3〇〇niL三頸燒杯放 入鎢酸鈉(日本無機化學工業(股)製)0.95 0g(2.88mm〇1)、鎢 酸(日本無機化學工業(股)製)0.720§(2.88111111〇1)、三辛基胺 (廣榮化學(股)製)2.04g(5.76mmol)、苯膦酸(日產化學(股) 製)0.911g(5.76mmol)、3,3’,5,5,-四甲基聯苯基-4,4,-二烯 丙基醚92.9g(0.288mol),以磁攪拌器進行攪拌之同時,以 油浴加溫至70°C後’使反應溫度不超過75t而滴入35% 過氧化氫水溶液8 4 _ 0 g (〇 . 8 6 4 m ο 1)。滴入結束後,持續攪拌 2小時,使反應液冷卻至室溫。其後,再添加乙酸乙酯 4 0g,使上層爲有機層,下層爲水層,並將有機層予以分 離。 對此有機層進行分析之結果,3,3 ’,5,5 ’ -四甲基聯苯 基-4,4’-二烯丙基醚之轉化率爲54.2%,單環氧體之選擇 率爲64.9%,且對二環氧體之選擇率爲15.5 %(實施例13、 表2參照)。 其後,將有機層以亞硫酸鈉水溶液洗淨,使用蒸發器 、真空泵進行有機層之溶劑餾去及乾燥’而得到粗製之反 應物,其後藉由管柱層析法純化(二氧化矽凝膠60N(球狀 、中性):關東化學製、顯影溶劑;己烷:乙酸乙酯=1 〇 -25- 201130806 :1〜3 : 1),而得到3,3’,5,5’-四甲基聯苯基-4,4’-二環氧 丙基醚及3,3’,5,5’-四甲基聯苯基-4,4’-單烯丙基單環氧丙 基醚。由所得之生成物之NMRdH、13C)及質量分析(MS) 之結果,確定所得之生成物爲3,3’,5,5’-四甲基聯苯基-4,4’-二環氧丙基醚及3,3’,5,5’-四甲基聯苯基-4,4’-單烯丙 基單環氧丙基醚。單烯丙基單環氧丙基醚體之測定結果如 圖1〜3所示。 MS之測定條件係如以下般:-24-201130806 [Example 1 6] The product obtained in Example 13 was subjected to isolation from monoepoxypropyl monoallyl ether in the present example. The experimental sequence is as follows. For a 3〇〇niL three-neck beaker equipped with a drip funnel and a Daisy condenser, put sodium tungstate (made by Nippon Inorganic Chemical Industry Co., Ltd.) 0.95 0g (2.88mm〇1), tungstic acid (Japan Inorganic Chemical Industry) (stock) system: 0.720 § (2.88111111〇1), trioctylamine (manufactured by Kwong Wing Chemical Co., Ltd.) 2.04g (5.76mmol), phenylphosphonic acid (Nissan Chemical Co., Ltd.) 0.911g (5.76mmol) , 3,3',5,5,-tetramethylbiphenyl-4,4,-diallyl ether 92.9 g (0.288 mol), while stirring with a magnetic stirrer, warm in an oil bath until After 70 ° C, the reaction temperature was not more than 75 t and 35% aqueous hydrogen peroxide solution was added dropwise to 8 4 _ 0 g (〇. 8 6 4 m ο 1). After the completion of the dropwise addition, stirring was continued for 2 hours, and the reaction liquid was cooled to room temperature. Thereafter, 40 g of ethyl acetate was further added to make the upper layer an organic layer and the lower layer an aqueous layer, and the organic layer was separated. As a result of analysis of the organic layer, the conversion of 3,3 ',5,5 '-tetramethylbiphenyl-4,4'-diallyl ether was 54.2%, and the selectivity of the monoepoxide was selected. It was 64.9%, and the selectivity to the diepoxide was 15.5% (refer to Example 13, Table 2). Thereafter, the organic layer was washed with an aqueous solution of sodium sulfite, and the solvent of the organic layer was distilled off and dried using an evaporator and a vacuum pump to obtain a crude reactant, which was then purified by column chromatography (cerium oxide gel). 60N (spherical, neutral): manufactured by Kanto Chemical Co., Ltd.; hexane: ethyl acetate = 1 〇 -25 - 201130806 : 1~3 : 1), and 3,3', 5,5'-four Methylbiphenyl-4,4'-diepoxypropyl ether and 3,3',5,5'-tetramethylbiphenyl-4,4'-monoallyl monoepoxypropyl ether . From the results of NMRdH, 13C) and mass analysis (MS) of the obtained product, it was confirmed that the obtained product was 3,3',5,5'-tetramethylbiphenyl-4,4'-diepoxy. Propyl ether and 3,3',5,5'-tetramethylbiphenyl-4,4'-monoallyl monoepoxypropyl ether. The results of the measurement of the monoallyl monoepoxypropyl ether body are shown in Figs. The measurement conditions of MS are as follows:

裝置:JEOL JMS-SX102ADevice: JEOL JMS-SX102A

試料加熱溫度:80°C —〔 32°C /min〕— 400°C 試料濃度:將NMR測定用溶液以二氯甲烷稀釋10倍Sample heating temperature: 80 ° C - [ 32 ° C / min] - 400 ° C Sample concentration: NMR measurement solution diluted 10 times with dichloromethane

試料量:0.5μ1 *以80t加熱藉由溶劑揮發除去後導入於MS 離子化法:EI(電子離子化法) 掃猫範圍:m/zlO〜800 [實施例17] 對裝備有迴流冷卻器、溫度計、攪拌裝置及橡皮帽之 50ml三頸燒杯添加實施例16中合成之單烯丙基單環氧丙 基醚體 0.18(0.30111111〇1)、1,1,1,3,5,5,5-七甲基三矽氧烷 〇.〇7 7g(0.3 5mmol)、及甲苯lml,於氬氣流中,在室溫下 攪拌。對此混合溶液加入3 %二乙烯四甲基二矽氧烷鉑錯 合物異丙醇溶液0.002 g(鉑量:6.0M 0_5g),將反應溶液在 室溫下進行攪拌。在室溫下攪拌6小時後,在減壓下去除 甲苯溶劑,而得到粗製之反應物〇. 1 3g。其後,藉由管柱 -26- 201130806 層析法純化(二氧化矽凝膠60N(球狀、中性):關東化學製 、顯影溶劑;甲苯··乙酸乙酯=1 〇 ·· 1 ),而得到下述構造 式(3): 【化5】Sample amount: 0.5 μl * Heated by 80 t by solvent evaporation and then introduced into MS. Ionization method: EI (electron ionization method) Sweeping cat range: m/z10 to 800 [Example 17] equipped with a reflux cooler, The monoallyl monoepoxypropyl ether body 0.18 (0.30111111〇1), 1,1,1,3,5,5,5 synthesized in Example 16 was added to a 50 ml three-neck beaker of a thermometer, a stirring device and a rubber cap. - Heptamethyltrioxane oxime. 7 7 g (0.35 mmol) and 1 ml of toluene were stirred at room temperature under a stream of argon. To the mixed solution, 0.002 g of a solution of 3% diethylenetetramethyldioxane platinum complex isopropanol (platinum amount: 6.0 M 0_5 g) was added, and the reaction solution was stirred at room temperature. After stirring at room temperature for 6 hours, the toluene solvent was removed under reduced pressure to give a crude material. Thereafter, it was purified by column chromatography -26-201130806 (cerium oxide gel 60N (spherical, neutral): manufactured by Kanto Chemical Co., Ltd.; toluene·ethyl acetate = 1 〇·· 1 ) And the following structural formula (3) is obtained: [Chemical 5]

H3C-Si-〇-Si-〇-Si-CH3 CH3 ch3 ch3 所示之單環氧丙基醚0.13g。由所得之生成物之NMRdH、 13C、29Si)及質量分析(MS)的結果,確定所得之生成物爲 構造式(3)所示之化合物(參考圖4〜7)。即,其顯示實施 例16中所合成之單烯丙基單環氧丙基醚化合物可藉由矽 氫化反應,而與具有Si-H基之化合物反應。 MS之測定條件係如以下般=0.13 g of monoepoxypropyl ether represented by H3C-Si-〇-Si-〇-Si-CH3 CH3 ch3 ch3. From the results of NMRdH, 13C, 29Si) and mass analysis (MS) of the obtained product, it was confirmed that the obtained product was a compound of the formula (3) (refer to Figs. 4 to 7). Namely, it shows that the monoallyl monoepoxypropyl ether compound synthesized in Example 16 can be reacted with a compound having a Si-H group by a hydrogenation reaction of hydrazine. The measurement conditions of MS are as follows =

裝置:JEOL JMS-SX 1 02 ADevice: JEOL JMS-SX 1 02 A

試料加熱溫度:80°C —〔 32°C /min〕—40(TC 試料濃度:將N M R測定用溶液以二氯甲烷稀釋1 〇倍Sample heating temperature: 80 ° C - [ 32 ° C / min] - 40 (TC sample concentration: N M R determination solution diluted 1 × times with dichloromethane

試料量:0·5μ1 *以80°C加熱藉由溶劑揮發除去後導入於MS 離子化法:EI(電子離子化法) 掃瞄範圍:m/zlO〜800 [產業上之可利用性] -27- 201130806 依據本發明之環氧丙基醚化合物之製造方法,藉使用 鎢化合物、3級有機胺、及苯鱗酸作爲觸媒’使過氧化氫 與烯丙基醚化合物反應,而可製造所對應之環氧丙基醚化 合物,並在極力抑制有機氯系之雜質混入,可同時以簡便 操作下安全並收率良好且低成本地製造於電子材料領域, 或以化學工業爲首之各種產業領域被廣泛使用作爲接著劑 、塗料樹脂之各種聚合物之原料之有用物質的環氧樹脂。 又,本發明之單烯丙基單環氧丙基醚化合物,藉由使其與 具有Si-H基之化合物進行矽氫化反應,由於可對具有各 種Si-H基之化合物導入聯苯基環氧丙基醚基,而極有用 於高耐熱性、高蝕刻耐性之抗蝕劑類或密封材類等所利用 之環氧樹脂之合成。 【圖式簡單說明】Sample amount: 0·5μ1 * Heated at 80 ° C by solvent evaporation and then introduced into MS. Ionization method: EI (electronic ionization method) Scanning range: m/zlO~800 [Industrial availability] - 27-201130806 The method for producing a glycidyl propyl ether compound according to the present invention can be produced by reacting hydrogen peroxide with an allyl ether compound by using a tungsten compound, a tertiary organic amine, and benzoic acid as a catalyst The corresponding epoxidized propyl ether compound is used in the field of electronic materials, which is safe and yield-efficient and low-cost, and can be easily produced at a low cost. An epoxy resin which is a useful material of a raw material of various polymers of an adhesive or a coating resin is widely used in the industrial field. Further, the monoallyl monoepoxypropyl ether compound of the present invention is subjected to a hydrazine hydrogenation reaction with a compound having a Si-H group, since a biphenyl ring can be introduced to a compound having various Si-H groups. An oxypropyl ether group is excellent in the synthesis of an epoxy resin used for a resist or a sealing material for high heat resistance and high etching resistance. [Simple description of the map]

[圖1]圖1係表示實施例16中所得之生成物之1H-NMR 之測定結果。 [圖2]圖2係表示實施例16中所得之生成物之13C-NMR 之測定結果。 [圖3 ]圖3係表示實施例丨6中所得之生成物之質量分 析(MS)之測定結果。 [圖4]圖4係表示實施例17中所得之生成物之1h-NMR 之測定結果。Fig. 1 is a graph showing the results of 1H-NMR measurement of the product obtained in Example 16. Fig. 2 is a graph showing the results of 13C-NMR measurement of the product obtained in Example 16. [Fig. 3] Fig. 3 shows the results of measurement of mass analysis (MS) of the product obtained in Example 丨6. Fig. 4 is a graph showing the results of 1h-NMR measurement of the product obtained in Example 17.

[圖5]圖5係表示實施例17中所得之生成物之13C-NMR 之測定結果。 -28- 201130806 [圖6]圖6係表示實施例17中所得之生成物之29Si-NMR 之測定結果。 [圖7]圖7係表示實施例17中所得之生成物之質量分 析(MS)之測定結果。 -29-Fig. 5 is a graph showing the results of 13C-NMR measurement of the product obtained in Example 17. -28-201130806 [Fig. 6] Fig. 6 shows the results of measurement of 29Si-NMR of the product obtained in Example 17. Fig. 7 is a graph showing the results of measurement of mass analysis (MS) of the product obtained in Example 17. -29-

Claims (1)

201130806 七、申請專利範圍: 1. 一種環氧丙基醚化合物之製造方法,其係使具有烯 丙基醚鍵結之化合物與過氧化氫反應,藉由使該烯丙基之 碳-碳雙鍵環氧化而製造對應之環氧丙基醚化合物,其特 徵爲:使用鎢化合物、3級胺、及苯膦酸作爲反應觸媒, 2. 如請求項1之環氧丙基醚化合物之製造方法,其中 前述鎢化合物係使用鎢酸之部分中和鹽。 3. 如請求項1或2之環氧丙基醚化合物之製造方法, 其中前述鎢化合物爲鎢酸鈉與鎢酸之混合物、鎢酸鈉與礦 酸之混合物,或鎢酸與鹼化合物之混合物。 4. 如請求項1〜3中任一項之環氧丙基醚化合物之製 造方法,其中前述3級胺爲三烷基胺,鍵結於其氮原子之 烷基之碳數之合計爲6以上50以下。 5. 如請求項1〜4中任一項之環氧丙基醚化合物之製 造方法’其中具有前述烯丙基醚鍵結之化合物爲具有複數 烯丙基醚鍵結之化合物。 6. 如請求項1〜4中任一項之環氧丙基醚化合物之製 造方法,其中前述具有烯丙基醚鍵結之化合物爲具有2個 烯丙基醚鍵結之化合物,並更具有自反應生成物將僅有一 方之烯丙基醚鍵結受到環氧化之單烯丙基單環氧丙基醚化 合物予以單離之步驟。 7 ·如請求項1〜6中任一項之環氧丙基醚化合物之製 造方法’其中不使用有機溶劑作爲反應溶劑。 8.如請求項1〜7中任一項之環氧丙基醚化合物之製 -30- 201130806 造方法,其中前述具有烯丙基醚鍵結之化合物具有如以卞 之式(1): 【化1】201130806 VII. Patent Application Range: 1. A method for producing a glycopropyl ether compound, which is a reaction of a compound having an allyl ether bond with hydrogen peroxide, by making the allyl carbon-carbon double The bond is epoxidized to produce a corresponding epoxy propyl ether compound characterized by using a tungsten compound, a tertiary amine, and a phenylphosphonic acid as a reaction catalyst, 2. The manufacture of the epoxy propyl ether compound of claim 1 The method wherein the tungsten compound is a partially neutralized salt of tungstic acid. 3. The method for producing a glycidyl ether compound according to claim 1 or 2, wherein the tungsten compound is a mixture of sodium tungstate and tungstic acid, a mixture of sodium tungstate and mineral acid, or a mixture of tungstic acid and an alkali compound. . 4. The process for producing a glycidyl propyl ether compound according to any one of claims 1 to 3, wherein the tertiary amine is a trialkylamine, and the total number of carbon atoms bonded to the alkyl group of the nitrogen atom is 6 Above 50 or less. 5. Process for producing a epoxidized propyl ether compound according to any one of claims 1 to 4, wherein the compound having the above allyl ether bond is a compound having a complex allyl ether bond. 6. The method for producing a glycidyl ether compound according to any one of claims 1 to 4, wherein the compound having an allyl ether bond is a compound having two allyl ether bonds, and further has The step of separating the one-only allyl ether bond from the mono-allyl monoepoxypropyl ether compound which is epoxidized from the reaction product. The method for producing a glycidyl propyl ether compound according to any one of claims 1 to 6, wherein an organic solvent is not used as a reaction solvent. 8. The method for producing a epoxidized propyl ether compound according to any one of claims 1 to 7, wherein the compound having an allyl ether bond has a formula (1): 1] {式中,R1、及R2各自獨立爲氫原子、碳數1〜6之烷基 、碳數2〜6之烯基、碳數3〜12之環烷基或碳數6〜1〇 之芳基,或,R1與R2 —起形成碳數2〜6之亞烷基或碳數 3〜12之環亞烷基亦可;R3、R4、R5、及R6各自獨立爲氫 原子、碳數1〜10之烷基、碳數2〜10之烯基、碳數3〜 12之環烷基或碳數6〜10之芳基’且’ η表示0或1之整 數丨所表示之構造。 9.如請求項1〜8中任一項之環氧丙基醚化合物之製 造方法,其中前述具有烯丙基醚鍵結之化合物係選自由雙 酹-Α之二烯丙基醚、雙酚-F之二烯丙基醚、及3,3’,5,5’-四甲基聯苯基-4,4’-二烯丙基醚所成群之至少一種。 1 〇 .如請求項1〜7中任一項之環氧丙基醚化合物之製 造方法,其中前述具有烯丙基醚鍵結之化合物係選自由碳 數2〜20之α,ω-聚烯烴二醇二烯丙基醚、1,4-環己烷二甲 醇二烯丙基醚、及三環[5.2.1. 02’6]癸烷二甲醇二烯丙基醚 所成群之至少一種。 -31 - 201130806 11. 如請求項1〜7中任一項之環氧丙基醚化合物之製 造方法,其中前述具有烯丙基醚鍵結之化合物爲酚-甲醛 •烯丙醇聚縮合物或甲酚·甲醛.烯丙醇聚縮合物。 12. —種具有聯苯骨架之單烯丙基單環氧丙基醚化合 物,其係爲如以下之一般式(2):In the formula, R1 and R2 are each independently a hydrogen atom, an alkyl group having 1 to 6 carbon atoms, an alkenyl group having 2 to 6 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, or a aryl group having 6 to 1 carbon atoms. Or, R1 and R2 together form an alkylene group having 2 to 6 carbon atoms or a cycloalkylene group having 3 to 12 carbon atoms; R3, R4, R5 and R6 are each independently a hydrogen atom and have a carbon number of 1 An alkyl group of ~10, an alkenyl group having 2 to 10 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms or an aryl group having a carbon number of 6 to 10' and 'η' represents a structure represented by an integer 0 of 0 or 1. The method for producing a glycidyl propyl ether compound according to any one of claims 1 to 8, wherein the compound having an allyl ether bond is selected from the group consisting of diallyl ether of bismuth-fluorene, bisphenol At least one of a group of -F diallyl ether and 3,3',5,5'-tetramethylbiphenyl-4,4'-diallyl ether. The method for producing a glycidyl ether compound according to any one of claims 1 to 7, wherein the compound having an allyl ether bond is selected from the group consisting of α,ω-polyolefin having a carbon number of 2 to 20. At least one of a group of diol diallyl ether, 1,4-cyclohexane dimethanol diallyl ether, and tricyclo [5.2.1. 02'6] decane dimethanol diallyl ether . The method for producing a glycidyl ether compound according to any one of claims 1 to 7, wherein the compound having an allyl ether bond is a phenol-formaldehyde-allyl alcohol polycondensate or Cresol-formaldehyde. Allyl alcohol polycondensate. 12. A monoallyl monoepoxypropyl ether compound having a biphenyl skeleton which is of the following general formula (2): {式中,R7、R8' R9、及Rl<)各自獨立表示氫原子、碳數 1〜10之烷基、碳數2〜10之烯基 '碳數3〜10之環院基 或碳數6〜10之芳基丨所表示者。 13.如請求項12之具有聯苯骨架之單稀丙基單環氧丙 基醚化合物,其中式中之R7、R8、r9及R10爲甲基。 -32-In the formula, R7, R8' R9, and Rl<) each independently represent a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, an alkenyl group having 2 to 10 carbon atoms, and a carbon number of 3 to 10 or a carbon number. 6 to 10 of the aryl group represented by. 13. The mono-l-propyl monoglycidyl ether compound having a biphenyl skeleton according to claim 12, wherein R7, R8, r9 and R10 in the formula are a methyl group. -32-
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