TW201202284A - Polycyclopentadiene compounds with saturated cyclopentane ring - Google Patents

Polycyclopentadiene compounds with saturated cyclopentane ring Download PDF

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TW201202284A
TW201202284A TW100114628A TW100114628A TW201202284A TW 201202284 A TW201202284 A TW 201202284A TW 100114628 A TW100114628 A TW 100114628A TW 100114628 A TW100114628 A TW 100114628A TW 201202284 A TW201202284 A TW 201202284A
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polycyclopentadiene
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hydrogen
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Hefner, Jr
Michael J Mullins
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Dow Global Technologies Llc
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    • 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
    • C07D303/28Ethers with hydroxy compounds containing oxirane rings
    • C07D303/30Ethers of oxirane-containing polyhydroxy compounds in which all hydroxyl radicals are etherified with oxirane-containing hydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/02Polycondensates containing more than one epoxy group per molecule
    • C08G59/04Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof
    • C08G59/06Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols
    • C08G59/08Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols from phenol-aldehyde condensates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/20Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the epoxy compounds used
    • C08G59/22Di-epoxy compounds
    • C08G59/24Di-epoxy compounds carbocyclic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/20Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the epoxy compounds used
    • C08G59/22Di-epoxy compounds
    • C08G59/24Di-epoxy compounds carbocyclic
    • C08G59/245Di-epoxy compounds carbocyclic aromatic
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2603/00Systems containing at least three condensed rings
    • C07C2603/56Ring systems containing bridged rings
    • C07C2603/58Ring systems containing bridged rings containing three rings
    • C07C2603/60Ring systems containing bridged rings containing three rings containing at least one ring with less than six members
    • C07C2603/66Ring systems containing bridged rings containing three rings containing at least one ring with less than six members containing five-membered rings
    • C07C2603/68Dicyclopentadienes; Hydrogenated dicyclopentadienes

Abstract

Polycyclopentadiene compounds represented by compounds of the following Formula I: (Formula I) in which each X is either a hydrogen, a cyano group, a vinylbenzyl group, an allyl group, an acrylate group, or a structure of Formula II: (Formula II); n has an average value from zero to 20; each m independently has a value of zero to 3; each R is independently a halogen, a nitrile group, a nitro group, an alkyl group, an alkoxy group, an alkenyl group, or an alkenyloxy group, where the alkyl group, the alkoxy group, the alkenyl group, and the alkenyloxy group each independently contain 1 to 6 carbon atoms; each R1 is independently hydrogen or a methyl group, each Q is independently hydrogen or an alkyl group containing 1 to 6 carbon atoms, and T is either hydrogen or a structure of Formula III (Formula III) with the proviso that when X is a cyano group, then R is not an alkenyl group or an alkenyloxy group.

Description

201202284 六、發明說明: 【發明戶斤屬之技術領域3 技術領域 本揭露内容係有關於聚環戊二烯化合物,且特別地係 具有一飽和環戊烷環之聚環戊二烯化合物。 L先前技系好3 背景 聚環戊二烯二酚之各種例子係見於美國專利第 3,419,624及4,546,129號案。聚環戊二烯二酚可用以製備由 於二環戊二烯基部份存在而具有特別物理及/或機械性質 之某些促進的環氧、氰酸酯,及稀丙稀可熱固性之樹脂。 聚環戊二烯二酚典型上係經由一路易酸與聚環戊二烯及一 過量之紛化合物反應而製備。用於有效率縮合反應所需之 強路易士酸催化劑,尤其是三氟化硼,存在處理困難,特 別是由於濕氣敏感性及高反應性。再者,此等催化劑可能 易為非選擇性,導致大規模之寡聚合化及/或共同產物形 成。 【發明内容】 概要 對於各種實施例,本揭露内容之聚環戊二烯化合物係 以具下列化學式I之化合物表示: 201202284 (化學式i) (R)m201202284 VI. Description of the Invention: [Technical Field 3 of the Invention] The present disclosure relates to a polycyclopentadiene compound, and particularly to a polycyclopentadiene compound having a saturated cyclopentane ring. L. Prior Art 3 Backgrounds Various examples of polycyclopentadiene diphenols are found in U.S. Patent Nos. 3,419,624 and 4,546,129. Polycyclopentadiene diphenols can be used to prepare certain promoted epoxy, cyanate, and propylene thermosettable resins which have particular physical and/or mechanical properties due to the presence of the dicyclopentadienyl moiety. Polycyclopentadiene diphenol is typically prepared by reacting a Lewis acid with polycyclopentadiene and an excess of a compound. The strong Lewis acid catalysts required for efficient condensation reactions, especially boron trifluoride, have handling difficulties, particularly due to moisture sensitivity and high reactivity. Moreover, such catalysts may be susceptible to non-selectivity, resulting in large scale oligopolymerization and/or co-product formation. SUMMARY OF THE INVENTION For various embodiments, the polycyclopentadiene compound of the present disclosure is represented by a compound of the following formula I: 201202284 (chemical formula i) (R)m

其中,每一X係一氫、一氰基基團、一乙烯基苯甲基基 團、一烯丙基基團、一丙烯酸酯基團,或化學式II之一 結構: (化學式II)Wherein each X is a hydrogen, a cyano group, a monovinylbenzyl group, an allyl group, an acrylate group, or one of the formula II: (Formula II)

;η具有從〇至20之一平均值;每一m獨立地具有0至3之一數 值;每一 R獨立地係一鹵素、一腈基團、一石肖基基團、一 烷基基團、一烷氧基基團、一烯基基團,或一烯氧基基 團,其中,烷基基團、烷氧基基團、烯基基團,及烯氧 基基團每一者獨立地含有1至6個碳原子;每一R1獨立地 係氫或一甲基基團,每一 Q獨立地係氫或含有1至6個碳 原子之一烷基基團,且T係氫或化學式III之一結構 201202284 (化學式III) (R)mη has an average value from 〇 to 20; each m independently has a value from 0 to 3; each R is independently a halogen, a nitrile group, a stone Schottky group, an alkyl group a monoalkoxy group, a monoalkenyl group, or an alkenyloxy group, wherein the alkyl group, the alkoxy group, the alkenyl group, and the alkenyloxy group are each independently The ground contains 1 to 6 carbon atoms; each R1 is independently hydrogen or a methyl group, and each Q is independently hydrogen or an alkyl group having 1 to 6 carbon atoms, and the T is hydrogen or One of Chemical Formula III 201202284 (Chemical Formula III) (R)m

附帶條件係當X係一氰基基團時,則R不是一烯基基團或— 烯氧基基團。 本揭露内容之實施例亦包含—含有化學式j之聚環 戊二烯化合物之可固化組成物,其可選擇性包含一固化量 之一固化劑及/或一催化量之一催化劑及/或一固化加速量 之一固化加速劑。對於各種實施例,化學式丨之聚環戊二烯 化合物可用於形成一固化或部份固化之組成物。對於各種 實施例’可固化組成物可包含呈可熱固化樹脂型式之化學 式I之聚環戊二烯化合物(例如,當於化學式Γ之化合物中X 不是氫時)。對於各種實施例,可固化組成物可包含呈固化 劑(硬化劑)型式之化學式〖之聚環戊二烯化合物。 對於各種實施例’化學式I之樹脂及/或硬化劑可單獨或 與此間探討之其它化合物組合使用。例如,當化學式 係氫時,聚環戊二烯化合物可作為一硬化劑。對於各種實 施例,化學式1之化合物之硬化劑可與多種不同樹脂組合使 用,其不党限地包括自化學式I衍生之樹脂;聚胺甲酸酯樹 脂,聚酯樹脂;可熱固性之單體,如,環氧樹脂、二或聚 異氰酸酯,及二或聚馬來醯亞胺等;及其等之组合物。 本揭露内容之如上概要非意欲描述本發明之每一揭露 201202284 ㈣例或母1施。下舰明係更特別地例示說 例。於此揭露内容之多處’經由實施例提供指導,J施 她例可以各種級合使用。於每—例子,所述之列示僅專實 代表性族群,且不應被解釋為-排它之列示。作為 【實施冷式】 詳細說明 本揭露内容提供可作為環氧樹脂之固化劑及 可熱固性單體及/或可熱固性寡聚物之聚環戊 為 物。本揭露内容之聚環戊二烯化合物之例子不受限地勺合 具有-飽和環戊烧環之聚環戊二烯二驗。對於 ^ 例’本揭露内容之具有飽和環戊院環之聚環戊二埽二:施 自具有-飽和環戊燒環之聚環戊二稀科及/或單= 成。具有飽和環姐環之聚環戊二烯祕及/或單綱與—% 或一經取代之酚化合物之縮合可產生相對應之具有飽和2 戊燒%之聚環戊二烯二盼。對於各種實闕,具有飽和學 戊燒%之聚環戊H亦可自具有飽和環戊境環之 來%戊二烯單醛及/或單酮於加氫曱醯基化期間於原位氫 化而形成。然後,具有飽和環戊烷環之聚環戊二烯二酚可 用於製備本揭露内容之可熱固化單體,諸如,具有飽和環 戊烧環之聚環戊二烯二縮水甘油基醚、具有飽和環戊烷環 之聚環戍二烯二氰酸酯,及/或具有飽和環戊烷環之聚環戊 二烯二乙烯基苯曱基醚等。 對於各種實施例,使用具有一飽和環戊烷環之聚環戊 一婦單醛及/或二醛使本揭露内容之聚環戊二烯化合物以 201202284 相對較低分子量達成高程度之官能性,此能容許相對較低 熔融黏度之可固化組成物。以此等聚環戊二烯化合物形成 之可固化組成物亦可提供具有促進之玻璃轉移溫度(Tg)之 固化組成物。另外,預期本揭露内容之聚環戊二烯化合物 亦會於而ί濕性及而ί腐蚀性提供改良,與固化組成物之促進 之電性質,特別是耗散因子。 於此使用時,"一”、π—個"、”此”、”至少一”,及"一或 多個”係可互換使用。"包括’'及π包含"與其等之變體之用辭 若於說明及申請專利範圍中出現時,此等用辭並不具有一 限制性意義。 ”及/或’'之用辭係意指所列示項目之一、一或多者,或 全部。 以端點描述數值範圍係包含包括於此範圍内之所有數 值(例如,1至5 包含 1、1.5、2、2.75、3、3.80、4、5等)。 ”熱固物” 一辭於此使用時係指當加熱時可不可逆地 固化或“凝固”之聚合物。 ”可固化π、”經固化π、”可熱固化”及”經熱固化"之用辭 於各處係同義地使用,且意指組成物能接受使此組成物呈 一經固化或經熱固化之狀態或情況之條件。 "Β -階段”一辭於此使用時係指一熱固性樹脂已熱反應 超出Α-階段,使得產物於諸如醇或酮之溶劑中具有完全至 部份之可溶性。 ”烷基基團”之用辭係意指一飽和之線性或分支之單價 烴基團,包括,例如,甲基、乙基、正丙基、異丙基、第 8 201202284 三丁基、戊基、己基等。 ’’烷氧基基團"之一辭係指其中至少一烴烷基基團係與 一氧鍵結之基團。例如,以化學式-0-R或-O-R-0-R表示之 一基團係一烷氧基基團,其中,R係經烷基基圑。 ”烯基基團”一辭係意指具有一或多個烴烯不飽和基團 (例如,碳-碳雙鍵)之一不飽和之線性或分支之之單價烴基 團,諸如,一乙稀基基團。 ’’烯氧基基團"一辭係指其中至少一烴烯基基團係與一 氧鍵結之基團。 於此使用時,字首“聚”係意指具有二或更多之一特別 部份之一化合物。例如,具有二個環戊二烯部份(二環戊二 烯)之一環戊二烯化合物係一特別之聚環戊二烯。 於此使用時,“化合物”係指由二或更多種元素之原子 或離子以化學組合而組成之一特質。 對於各種實施例,本揭露内容之聚環戊二烯化合物 係以下列化學式I之一化合物表示: (化學式I) (R)mThe proviso is that when the X is a cyano group, then R is not an alkenyl group or an alkenyloxy group. Embodiments of the present disclosure also include a curable composition comprising a polycyclopentadiene compound of formula j, which optionally comprises a curing agent and/or a catalytic amount of one of the catalysts and/or one One of the curing acceleration accelerators. For various embodiments, the polycyclopentadiene compound of the formula 可 can be used to form a cured or partially cured composition. For various embodiments, the curable composition may comprise a polycyclopentadiene compound of formula I in the form of a heat curable resin (e.g., when X is not hydrogen in the compound of the formula). For various embodiments, the curable composition may comprise a polycyclopentadiene compound of the formula of a curing agent (hardener) type. For various embodiments, the resin and/or hardener of Formula I may be used alone or in combination with other compounds discussed herein. For example, when the chemical formula is hydrogen, the polycyclopentadiene compound acts as a hardener. For various embodiments, the hardener of the compound of Chemical Formula 1 can be used in combination with a plurality of different resins, including, without limitation, a resin derived from Chemical Formula I; a polyurethane resin, a polyester resin; a thermosetting monomer, For example, an epoxy resin, a di- or polyisocyanate, and a di- or polymaleimide; and the like. The above summary of the disclosure is not intended to describe each disclosure of the present invention 201202284 (four) or parent. The lower ship Ming system is more specifically illustrated. The disclosure of the present disclosure is provided by way of example, and the examples can be used in various combinations. In each of the examples, the list is for a specific representative group and should not be construed as an exclusive list. DETAILED DESCRIPTION OF THE INVENTION The present disclosure provides a polycyclopentene which can be used as a curing agent for an epoxy resin and a thermosetting monomer and/or a thermosetting oligomer. An example of a polycyclopentadiene compound of the present disclosure is not limited to a polycyclopentadiene dimer having a saturated cyclopentane ring. For the present disclosure, the polycyclopentadiene having a saturated cyclopentane ring is applied to a polycyclopentanyl group having a -saturated cyclopentane ring and/or a single =. Condensation of a polycyclopentadiene having a saturated ring ring and/or a mono- and _ or a substituted phenolic compound produces a corresponding polycyclopentadiene having a saturated 2 pentane. For various enthalpy, polycyclopentane H with saturation pentane can also be hydrogenated in situ from a pentadiene monoaldehyde and/or a monoketone having a saturated cyclopentane ring during hydrohalogenation. And formed. Then, a polycyclopentadiene diphenol having a saturated cyclopentane ring can be used to prepare the heat-curable monomer of the present disclosure, such as a polycyclopentadiene diglycidyl ether having a saturated cyclopentane ring, a polycyclodecadiene dicyanate of a saturated cyclopentane ring, and/or a polycyclopentadienyl divinyl benzoate ether having a saturated cyclopentane ring or the like. For various embodiments, the polycyclopentadiene compound of the present disclosure is used to achieve a high degree of functionality with a relatively low molecular weight of 201202284, using a polycyclopentanyl monoaldehyde having a saturated cyclopentane ring and/or a dialdehyde. This allows for a relatively low melt viscosity curable composition. The curable composition formed by such a polycyclopentadiene compound can also provide a cured composition having a promoted glass transition temperature (Tg). In addition, it is contemplated that the polycyclopentadiene compounds of the present disclosure will also provide improved properties in terms of wetness and corrosion, as well as enhanced electrical properties of the cured composition, particularly dissipative factors. As used herein, "a,""""""""""""""""Conclusions of ''and πinclude' and its variants are used in the context of the description and patent application, and such terms are not intended to be limiting. The term "and/or" is used to mean one, one or more, or all of the items listed. The range of values by endpoints is inclusive of all values included in the range (eg, 1 to 5 inclusive) 1, 1.5, 2, 2.75, 3, 3.80, 4, 5, etc.) "thermoset" as used herein refers to a polymer that irreversibly cures or "solidifies" when heated. "Curable π "cured π, "heat-curable" and "heat-cured" are used synonymously everywhere, and means that the composition is capable of accepting the composition in a cured or heat-cured state or Conditions of the situation. The term "Β-stage" as used herein means that a thermosetting resin has been thermally reacted beyond the Α-stage to render the product completely soluble in a solvent such as an alcohol or ketone. "Alkyl group" By language is meant a saturated linear or branched monovalent hydrocarbon group including, for example, methyl, ethyl, n-propyl, isopropyl, 8201202284 tributyl, pentyl, hexyl, etc. ''Alkane The term "oxy group" refers to a group in which at least one alkoxy group is bonded to an oxygen. For example, a group represented by the formula -0-R or -OR-0-R a monoalkoxy group, wherein R is via an alkyl group. The term "alkenyl group" means one of having one or more hydrocarbon ethylenically unsaturated groups (eg, a carbon-carbon double bond). Unsaturated linear or branched monovalent hydrocarbon group, such as a vinyl group. The term 'enoxy group' refers to a group in which at least one hydroalkenyl group is bonded to an oxygen bond. As used herein, the word "poly" means a compound having one or two of a particular part. For example, having two cyclopentanes One of the (dicyclopentadiene) cyclopentadiene compounds is a special polycyclopentadiene. As used herein, "compound" means a chemical combination of atoms or ions of two or more elements. One of the characteristics of the composition. For various embodiments, the polycyclopentadiene compound of the present disclosure is represented by one of the following chemical formula I: (Chemical Formula I) (R)m

9 201202284 其中,每一X係一氫、一氰基基團(N三C —-)、一乙烯基 苯曱基基團、一烯丙基基團、一丙烯酸酯基團,或化學 式II之一結構: (化學式II)9 201202284 wherein each X is a hydrogen, a cyano group (N tri C —-), a monovinyl benzoyl group, an allyl group, an acrylate group, or a formula II A structure: (Chemical Formula II)

其中,η具有從〇至20之一平均值;每一 m獨立地具有0至3 之一數值;每一 R獨立地係一鹵素、一腈基團、一石肖基基 團、一烷基基團、一烷氧基基團、一烯基基團,或一烯 氧基基圑,其中,烷基基團、烷氧基基團、烯基基團, 及烯氧基基團每一者獨立地含有1至6個碳原子;每一R1 獨立地係氫或一甲基基團,每一Q獨立地係氫或含有1至 6個碳原子之一烷基基團;且T係氫或化學式III之一化合 物 (化學式III)Wherein η has an average value from 〇 to 20; each m independently has a value from 0 to 3; each R is independently a halogen, a nitrile group, a stone Schottky group, an alkyl group a group, a monoalkoxy group, a monoalkenyl group, or an alkenyloxy group, wherein each of an alkyl group, an alkoxy group, an alkenyl group, and an alkenyloxy group Independently containing from 1 to 6 carbon atoms; each R1 is independently hydrogen or a methyl group, each Q is independently hydrogen or an alkyl group containing from 1 to 6 carbon atoms; and T-hydrogen Or a compound of formula III (chemical formula III)

附帶條件係當X係一氰基基團時,則R不是一烯基基團或一 烯氧基基團。 對於各種實施例,聚環戊二烯化合物之鹵素較佳係選 自氟、氣、溴,及其等之組合的族群。各種實施例亦提供η 10 201202284 可具有從0至20之一平均值。較佳地,n具有從〇至8之一平 均值。更佳地,η具有從〇至3之一平均值,且最佳地,η具 有從0至2之一平均值。 對於各種實施例,烷基基團及烷氧基基團可較佳地含 有1至2個碳原子。對於各種實施例,浠基基團及烯氧基基 團可較佳地含有1至3個碳原子。對於各種實施例,當q係 一烷基基團時’其可較佳地含有丨至2個碳原子。對於各種 實施例,R基團亦可為一稠合之環基團,其產生具有含_〇χ 基團的環基團之一萘結構,諸如,一萘朌(1-萘酚及/或2-秦紛)、四氫萘酌·、茚醇,及其等之組合物。 對於各種實施例,m&n可較佳地為〇,且Q及Τ可較佳 地為氫以提供化學式IV之一化合物: (化學式III)The proviso is that when the X is a cyano group, then R is not an alkenyl group or an alkenyloxy group. For the various embodiments, the halogen of the polycyclopentadiene compound is preferably selected from the group consisting of fluorine, gas, bromine, and the like. Various embodiments also provide that η 10 201202284 may have an average value from 0 to 20. Preferably, n has an average value from 〇 to 8. More preferably, η has an average value from 〇 to 3, and optimally, η has an average value from 0 to 2. For various embodiments, the alkyl group and the alkoxy group may preferably contain from 1 to 2 carbon atoms. For various embodiments, the fluorenyl group and the alkenyloxy group may preferably contain from 1 to 3 carbon atoms. For various embodiments, when q is an alkyl group, it may preferably contain from 丨 to 2 carbon atoms. For various embodiments, the R group can also be a fused ring group that produces a naphthalene structure having a ring group containing a 〇χ group, such as a naphthoquinone (1-naphthol and/or 2-Qin), tetrahydronaphthalene, sterol, and the like. For various embodiments, m&n may preferably be deuterium, and Q and deuterium may preferably be hydrogen to provide a compound of formula IV: (Formula III)

其中’ X係如此處所提供。 如所瞭解’當η係〇時,本揭露内容之聚環戍二烯化 合物亦可稱為一二環戊二烯化合物。但是,於此處使用 時’聚環戊二烯被使用,需瞭解當η係〇時,此用辭可以 201202284 二環戍二烯替代。 具有一飽和環戊烷環之聚環戊二烯二酚之製備 本揭露内容之具有飽和環戊烷環(c 5環)之聚環戊二烯 二酚可自具有—飽和環戊烷環之聚環戊二烯單醛及/或聚 環戊二烯單酮生產。對於各種實施例,聚環戊二烯單醛可 使用合成氣、一配位體,及一過渡金屬(來自.第3至1〇族) 催化劑使用’諸如,G· Longoni等人’ J. 〇f MolecularWhere 'X is as provided herein. As understood, the polycyclodecadiene compound of the present disclosure may also be referred to as a dicyclopentadiene compound when η is oxime. However, when used here, polycyclopentadiene is used, and it is necessary to understand that when η is 〇, this term can be replaced by 201202284 bicyclononadiene. Preparation of Polycyclopentadiene Diphenol with a Saturated Cyclopentane Ring The polycyclopentadiene diol having a saturated cyclopentane ring (c 5 ring) may have a self-saturated cyclopentane ring. Polycyclopentadiene monoaldehyde and / or polycyclopentadiene monoketone production. For various embodiments, polycyclopentadiene monoaldehyde can be used using syngas, a ligand, and a transition metal (from Group 3 to 1 lanthanum) catalysts such as 'G, Longoni et al.' J. 〇 f Molecular

Catalysis 68,7-21 (1991)或更普遍地於 Kirk-Othmer, ENCYCLOPEDIA OF CHEMICAL TECHNOLOGY,2001,第 1-17頁所述之方法經由聚環戊二烯,特別是二環戊二烯, 之加氫甲醯基化而生產。具有此方法之變種,包含使用 混合之極性/非極性之溶劑以減輕催化劑循環及產物分 離問題之一方法(美國專利第6307108 B1號案)。 具有一飽和環戊烷環之此一聚環戊二烯單醛之一例 子包含具有化學式V之化合物: (化學式V)Catalysis 68, 7-21 (1991) or more generally by Kirk-Othmer, ENCYCLOPEDIA OF CHEMICAL TECHNOLOGY, 2001, pages 1-17 via polycyclopentadiene, especially dicyclopentadiene, Produced by hydroformylation. Variations of this method include a method of using a mixed polar/non-polar solvent to mitigate catalyst cycling and product separation problems (U.S. Patent No. 6,307,108 B1). An example of such a polycyclopentadiene monoaldehyde having a saturated cyclopentane ring comprises a compound of formula V: (Formula V)

對於各種實施例,加氫甲醯基化可於1至250大氣壓 (atm)之一壓力及20 °C至25〇。(:之一溫度發生。對於各種實 施例,合成氣可含有不同含量之一氧化碳(CO)、氫(h2)及 可能之惰性氣體。加氫甲醯基化期間形成之中間產物可包 括其中環戊烷環具有一烯烴之化合物。依處理條件而定, 12 201202284 烯烴、飽和,或產物之混合物可被獲得。如此處所探討, 較佳地,聚環戊二烯二酚具有飽和環戊烷環,但不飽和飽 和環戊烷環可能被獲得。較佳地,少於50百分率(%)之於 加氫甲醯基化期間產生之聚環戊二烯二酚包括一烯烴(例 如,係不飽和)。 反應亦可使用US 7,321,068等所揭示之無配位體之 铑催化劑於200-350 atm之高合成壓力進行。適合配位體 之例子包含一氧化碳及具有通式PR2R3R4之有機膦配位 體,其中,每一R2、R3,及R4係一經取代或未經取代之烷 基、一芳基、一芳烧基、一烧芳基、一鹵化物,或一其等 之組合。一特別例子不受限地包括正丁基二苯基膦。一適 合催化劑之一例子不受限地包括Rh(CO)2(乙醯基丙酮酸 酯)。 於加氫曱醯基化期間,微量,典型上係總反應產物 之5-25重量% (wt·%)或更少,之聚環戊二稀二酿亦可與 聚環戊二烯單醛一起產生。若要的話,聚環戊二烯單醛 可與聚環戊二烯二醛部份或完全分離。例如,一蒸餾方 法可用以將聚環戊二烯單醛與聚環戊二烯二醛分離。 於一另外實施例,各種重量百分率之具有飽和環戊 烷環之聚環戊二烯單醛亦可與聚環戊二烯二醛混合。使 用聚環戊二烯單醛及聚環戊二烯二醛之組合物能控制形 成之可固化組成物中之官能性量。酚醛清漆化學可用以 自聚環戊二烯單醛形成聚環戊二烯二酚。寡聚物亦可存 在於聚環戊二烯二酚中。因此,聚環戊二烯二酚與具有 13 201202284 飽和環戊烷環之聚酚之組合物可以本揭露内容之一另外 實施例生產。聚環戊二烯二酚之此一寡聚物之一例子不 受限地包括具化學式vi之化合物: (化學式VI)For various embodiments, the hydroformylation can be at a pressure of from 1 to 250 atmospheres (atm) and from 20 °C to 25 Torr. (: One of the temperatures occurs. For various embodiments, the syngas may contain varying amounts of one of carbon monoxide (CO), hydrogen (h2), and possibly an inert gas. Intermediates formed during hydroformylation may include cyclopentyl The alkane ring has a compound of an olefin. Depending on the processing conditions, 12 201202284 an olefin, a saturated, or a mixture of products can be obtained. As discussed herein, preferably, the polycyclopentadiene diphenol has a saturated cyclopentane ring, However, an unsaturated saturated cyclopentane ring may be obtained. Preferably, less than 50% (%) of the polycyclopentadiene diphenol produced during hydroformylation includes an olefin (eg, unsaturated) The reaction can also be carried out using a rhodium-free catalyst disclosed in US 7,321,068, etc. at a high synthesis pressure of 200-350 atm. Examples of suitable ligands include carbon monoxide and an organophosphine ligand having the general formula PR2R3R4. Wherein each of R2, R3, and R4 is a substituted or unsubstituted alkyl group, an aryl group, an arylalkyl group, a aryl group, a halide, or a combination thereof. Restricted Butyl diphenyl phosphine. One example of a suitable catalyst includes, without limitation, Rh(CO) 2 (ethyl phthalate). During hydrogenation, a trace amount, typically the total reaction product. 5-25% by weight (wt.%) or less, the polycyclopentadiene can also be produced together with polycyclopentadiene monoaldehyde. If desired, polycyclopentadiene monoaldehyde can be combined with polycyclopentene The pentadiene dialdehyde is partially or completely separated. For example, a distillation process can be used to separate the polycyclopentadiene monoaldehyde from the polycyclopentadiene dialdehyde. In an additional embodiment, various weight percentages have saturated cyclopentane. The polycyclopentadiene monoaldehyde of the alkane ring may also be mixed with the polycyclopentadiene dialdehyde. The composition of the polycyclopentadiene monoaldehyde and the polycyclopentadiene dialdehyde can be used to control the formed curable composition. The amount of functionality. Novolac chemistry can be used to form polycyclopentadiene diphenol from polycyclopentadiene monoaldehyde. Oligomers can also be present in polycyclopentadiene diphenol. Therefore, polycyclopentadiene A composition of a diphenol and a polyphenol having a 13 201202284 saturated cyclopentane ring can be produced in another embodiment of the present disclosure. This pentadiene oligomer An example of diphenols include without restriction of a compound having the formula vi: (Formula VI)

其中,η、m、R及Q係如此處所定義。 對於各種實施例,用於本揭露内容之具有飽和環戊烷 環之聚環戊二稀單酮可經由一多步驟之合成生產,例 如,於 Tetrahedron Letters,28,769 (1987) ; Tetrahedron Letters, 27, 3033 (1986) ; Tetrahedron Letters, 27, 933 (1986) ; Journal of the American Chemical Society, 107, 7179 (1985);及 Journal of the Chemical Society: Chemical Communications, 1040 (1983)中所示之化學。用於本揭露内 容之聚環戊二烯可如Kirk-Othmer,ENCYCLOPEDIA OF CHEMICAL TECHNOLOGY,第三版,第 7冊,417-419 頁 (1979)所揭示般將環戊二烯加熱至高於1〇〇 °c之溫度而製 備。此處所提及之所有參考資料在此完整併入本案以為參 考資料。 . 如此處所提供’使用具有飽和環戊烷環之聚環戊二烯 單酿、二酸’及/或單酮之組合物可控制一特定可固化組成 14 201202284 物中之官能性量。因此,例如,本揭露内容之-可固化組 成物之父聯密度可❹成物巾使用之聚環紅缔二盼及聚 環戊二稀㈣之相對量為基準而調整(例如,減少或〜小 以此方式輕官能性量缺固她之諸如破璃轉移溫 度(Tg)之性諸修整賴欲量及/或_化組絲之其它性 質(例如,韌性)平衡。 再者,可控制本揭露内容之聚環戊二稀單酸中之二環 戊二稀及環戊4部份之量。二環紅稀及/或聚私 -烯可經由Diels-Alder化學使用環戊二稀形成,其中,如 此處所探討,化學式心的平均值可編㈣/因此^ 如,當本揭露内容之聚環戊二稀單越中之聚環戊二稀部份 係寡聚物,其可具有平均係從2至5之η值分佈。對於盆它實 施例’ 11可具有G或1之值。控制聚環戊二烯轉中之二環戊 二烯及/或聚環戊二稀部份之能力亦容許於維持或甚^增 加固化組成物之可能的耐濕性時同時控制及/或修整_ ; 固化組成物之一交聯密度之能力。 對於各種實施例,形成之具有飽和環戊院環之聚環戊 二稀轉及/或具錢和環狀社《紅料酮然後 ° ”紛交聯t成本揭露内容之具有飽和環戊院環之聚環戊 一稀—紛。對於各種實施例,聚環戍4秘及/或聚環戊 二稀相_之縮合反應可具有1:20至1:6,較佳係從1:15 至1:8,之—莫耳比率。對於各種實施例,縮合反應可於-@文催化』存在中發生,以使用之關重量為基準,此酸催 化劑較佳係從(UW重量%(wt%),且更佳係從〇⑴重量 15 201202284 %。對於各種實施例’用於縮合反應之酚類可不受限地包 括酚、經取代之酚 '鄰-甲酚、間-曱酚、對-曱酚、2,4-二曱 基酚、2,6-二甲基酚、1-萘酚、2-萘酚,及其等之組合。比 1:2〇更高之莫耳比率之酚或經取代之酚亦可被使用,但 是,如此需額外能量’因此,需用以回收及循環過量之酚 或經取代之酚的費用。對於各種實施例,過量之酚反應物 可藉由蒸餾移除。 使用大量過量之酌及/或經取代之S分的縮合反應被發 現有利於在具有一飽和環戊烷環之聚環戊二烯二酚係豐 富且於寡聚物係低之極低多分散性的產物。同樣地,當酚 及/或經取代之酚的量降低,以具有飽和環戊烷環之聚環戊 二烯二酚之含量為代價,於募聚物會增加。增加之寡聚 物含量有利於較高之羥基官能性,此對於某些最終用途 會係高度有利。因此’雖然極度大量過量之酚及/或經取 代之酴可被使用,但本揭露内容使用此處提供之莫耳比率 生產於聚環戊二烯二酚係豐富且於寡聚物係低之產物。 對於各種實施例’形成本揭露内容之聚環戊二烯二 紛之縮s反應亦可選擇性地包括使用一溶劑。對於此等實 施例/讀對於反應可呈惰性且反應產物亦可被使用,諸 洛劑亦可另外作為用於將水自縮合反 移除之補°11由具較高㈣減之某些盼反應 物或多種溶劑對於維持適當反應介質係有利。 適s之釀性催化劑 構酸;金屬氣化物,^仪,5!如,絲酸、硫酸、 軋化辞、氧化鋁、氧化鎂;有 16 201202284 機酸,諸如,對-甲苯績酸、草酸、3-巯-1-丙燒績酸,及 其等之組合。 對於各種實施例,3-酼-1-丙烷磺酸係一較佳之酸性 催化劑或共催化劑。驚人地,已發現3-毓-1-丙烷磺酸於 形成聚環戊二烯二酚亦係高選擇性,而無需將水自反應共 沸地移除。相反地,水係留於反應器内,而無需將反應淬 火。 反應溫度及時間係呈多樣性’但可為從約5分鐘至約48 小時,且從約20 °C至約175 °C之反應溫度可被使用。較佳 地,反應溫度及時間可為從15分鐘至36小時及從30。(:至約 125 °C之反應溫度。最佳地,反應溫度及時間可為從30分鐘 至24小時及從35 °C至約75 °C之反應溫度。 反應結束時’酸性催化劑可藉由中和化移除,例如, 藉由以水清洗或萃取。同樣地’於反應結束時,過量之酚 可,例如,藉由蒸餾或萃取自產物移除。 相對於習知技藝之聚環戊二烯二酚,除飽和環戊统環 外,本揭露内容之組成物結構上擁有二紛環實質上與降莰 基環附接’而習知技藝之此等組成物主要具有一紛環與降 莰基環附接及另一酚環與環戊基環附接。因此,於使用本 揭露内容之此對酚羥基基團製備之寡聚物或聚合物,相對 於寡聚物或聚合物之主鏈,聚環戊二烯部份係呈側懸。飽 和環戊烷環或聚環戊烷環之此結構容許發展中之熱固物之 鏈間疏水性締結。堆積變體亦可能,其中,於本揭露内容 之實施例中發現之側懸結構可導引鏈之堆積或其於基質内 17 201202284 之分子約束。因此,側懸聚環戊二烯部份之疏水性締結之 可能性對於本揭露内容係存在,且可促進形成之固化組成 物之物理及機械性質。 具有飽和環戊烷環之聚環戊二烯二酚具有作為,例 如,用於高性能功能性粉末塗層之環氧樹脂固化劑之用 途。當與多官能性之固化劑,例如,一聚環戊二稀四盼, 摻合時,具有飽和環戊烷環之聚環戊二烯二酚亦可作為 一“稀釋劑”以減少官能性。 本揭露内容之具有飽和環戊烷環之聚環戊二烯二酚 可用以使環氧樹脂,諸如,雙盼A之二縮水甘油基、 10-(2’,5'-二羥基苯基)-9,10-二氫-9-氧雜-10-磷雜菲-10-氧化 物(DOP-HQ)之二縮水甘油基醚、二環戊二烯二酚之二縮水 甘油基醚,及其它環氧樹脂,線性促進以產生含有側懸飽 和聚或二環戊二烯基部份之物料之可熱固性組成物。 形成之進階環氧樹脂可使用固化劑固化,或與其它可 熱固性單體,諸如,聚氰酸酯,共同反應。改良之耐濕性 及耐腐蝕性與促進之電性質,特別是耗散因子,對於此等 進階樹脂係被預期。對於各種實施例,另外認定當“η”大於 1,另外之烴本體添加至側懸之側鏈,且可有利地衝擊形成 熱固物之物理及機械性質。側懸側鍵之堆積可有利地增加 熱固基質之韌性,且可誘發鏈間之疏水性締結。 除前述之作為環氧樹脂之固化劑或用於環氧樹脂之 促進反應之用途外,本揭露内容之具有飽和環戊烷環之聚 環戊二烯二酚亦可作為另外熱固性樹脂之先質。此等熱 18 201202284 固性樹脂包括氰酸酯、環氧、烯丙基'烯丙氧義、 内歸酉曼 酯,及乙烯基笨甲基醚(及其它乙烯不飽和)樹脂,其係、 製備塗層,特別是功能性粉末塗層及具有高破續轉移於 度、耐溶劑性、耐濕性、耐磨耗性,及韌性之保護性塗地 電或結構性層合物或複合物;長絲繞捲物;模势你 、、切;鱗製 物;封裝物;多層電子電路;積體電路封裝物(諸如 基材”);航空用複合物;及與諸如聚(馬來醯亞胺)、聚 酯)之其它樹脂之配製物。由於具有飽和環戊烷環之聚俨= 二稀基部份之存在,具有改良财濕性及耐腐钱性與促進 電性質,特別是耗散因子,之熱固物係被預期。 具有飽和環戊烷環之聚環戊二烯二酚之二縮水甘油武喊 本揭露内容之具有飽和環戊烷環之聚環戊二缔二 甘油基醚及另外含有寡聚物之其組成物可如上般製備.本 揭露内容之前述組成物之製備中之起始步驟—般係由於— 驗性作用物質存在中,於一催化劑存在或缺乏中,且於 或多種溶劑存在或缺乏中,使具有飽和環戊烧環之聚淨戊 二烯二酚與表函醇反應所構成。對於各種實施例,此反應 可於從約20 °C至約120 °C,更佳係從約30 °C至約85 %, 最佳係從約4〇。(:至約75 °C之溫度發生。對於各種實施例, 此反應可於從約4 KPa至約500 KPa,更佳係從約4 KPa至約 340 KPa ’且最佳係從約8 KPa至約100 KPa( 1大氣壓)之壓力 發生。對於各種實施例,此反應可於足以完成此反應之時 間發生,通常係從約1至約120小時’更通常係從約3至約72 小時’最通常係從約4至約48小時。 19 201202284 對於各種實施例,此反應亦使用每一齡經基基图為從 約1丄1至25:1’較佳係從約18:1至約1〇1,且最佳係從約上! 至約5:1莫耳之表_ 1非催化劑係以化料量或更大量 使用之鹼金屬或鹼土金屬氫氧化物時,此起始反應產生一 鹵醇中間產物’職,其與驗性仙物質反應將鄰接函醇 基團轉化成環氧化物基團。形成之產物係一縮水甘油基醚 化合物。有關於環氧樹脂之製備的細節係於美國專利第 5,736,620 ; Lee及 Neville之 Handbook of Epoxy Resins, McGraw-Hill (1967);及 J0urnal Applied Polymer Science,第23冊,第1355-1372頁(1972);及美國專利第 4,623,701號案中提供,所有此等文獻在此被完整併入本案 以為參考資料。 可用以製備本揭露内容之組成物之適合表!|醇包括, 例如,表氯醇、表溴醇、表埃醇、曱基表氣醇、曱基表溴 醇、曱基表碘醇,及其等之組合。作為表_醇之最佳者係 表氣醇。 一適合之驗性作用物質被用以製備本揭露内容之組成 物。適合之鹼性作用物質包括,例如,鹼金屬或鹼土金屬 之氫氧化物、碳酸鹽,及碳酸氫鹽,及其等之組合。特別 適合之此等化合物包含氮氧化鈉、氫氧化鉀、氫氧化鋰、 氫氧化妈、氫氧化鋇、氮氧化錢、氫氧化鏟、碳酸納、碳 酸斜、碳酸鐘、碳酸約、破酸領、碳酸鎮、碳酸锰、碳酸 氫鈉、碳酸氫鉀、碳酸氫鎂、碳酸氫鋰、碳酸氫鈣、碳酸 氫鋇、碳酸氫鎂,及其等之組合。最佳係氫氧化鈉或氫氧 20 201202284 化鉀。對於包含具有飽和環戊烷環之聚環戊二烯二酚與鹼 金屬氫氧化物反應及其後與表ii醇反應之方法,適合之鹼 金屬氫化物包括,例如,氫化納及氫化钟,且氫化納係最 佳。 可用以製備本揭露内容之組成物之適合催化劑包括, 例如,敍或鱗之_化物,諸如,苯甲基三甲基氣化4安、苯 甲基三曱基溴化銨、四丁基氣化銨、四丁基溴化銨、四辛 基氣化銨、四丁基溴化銨、四曱基氣化銨、四甲基溴化銨、 四丁基氯化鱗、四丁基溴化鎮、四丁基碘化鱗、乙基三丁 基氣化鱗、乙基三苯基溴化鎮、乙基三苯基碘化鱗,及其 等之組合。 可用以製備本揭露内容之組成物之適合溶劑包括脂族 及芳香族烴、鹵化之脂族烴、脂族醚、脂族腈、環狀醚、 酮、醯胺、亞砜、脂族及環脂族二級及三級醇,及其等之 組合。特別適合之溶劑包括戊烧、己烧、辛烧、曱苯、二 甲苯、甲基乙基酮、曱基異丁基酮、N,N-二曱基曱醯胺、 二曱基亞砜、二乙基醚、四氫呋喃、1,4-二噁烷、二氣甲烷、 氯仿、二氯乙烷、曱基氣仿、乙二醇二曱基醚、N,N-二曱 基乙醯胺、乙腈、丙二醇單甲基醚、異丙醇,及其等之組 合。溶劑可於反應完成時使用傳統手段移除,諸如,真空 蒸餾。本揭露内容之另一方法係於缺乏溶劑中進行,且表 氯醇係以作為溶劑及反應物之量使用。 諸如高壓液相層析術(HPLC)之分析方法可用以同時監 測具有飽和環戊烷環之聚環戊二烯二酚之反應,及諸如鹵 21 201202284 醇之中間產物及最終之二縮水甘油基醚產物之形成。 本揭露内容之具有飽和環戊烷環之聚環戊二烯二縮水 甘油基醚之組成物的回收及純化可使用各種方法實施。例 如,重力過滤、真空過滤、離心處理、水清洗或萃取、溶 劑萃取、傾析、管柱層析術、真空蒸餾、降膜式蒸顧、擦 拭膜式蒸餾、靜電式凝結,及其它處理方法等可被使用。 真空蒸餾對於移除及回收較高沸點之分級物,例如,未使 用之表_醇,係最佳方法。此回收表氣醇及溶劑(若使用) 以供再循環。 寡聚物亦可存在於本揭露内容之具有飽和環戊烷環 之聚環戊二烯二縮水甘油基醚中。此等典型上係自存在 於具有飽和環戊烷環之聚環戊二烯二酚之先質中之寡聚 物組份之環氧化或自一部份之縮水甘油基醚部份之於原 位之進階反應而產生。進階反應之特徵在於於進階之環 氧樹脂產物中形成2-羥基丙基醚鍵結(化學式VII之結 構):Wherein η, m, R and Q are as defined herein. For various embodiments, the polycyclopentazenone having a saturated cyclopentane ring for use in the present disclosure can be produced via a multi-step synthesis, for example, in Tetrahedron Letters, 28, 769 (1987); Tetrahedron Letters, 27, 3033 (1986); Tetrahedron Letters, 27, 933 (1986); Journal of the American Chemical Society, 107, 7179 (1985); and Journal of the Chemical Society: Chemical Communications, 1040 (1983) . The polycyclopentadiene used in the present disclosure can be heated to above 1 揭示 as disclosed in Kirk-Othmer, ENCYCLOPEDIA OF CHEMICAL TECHNOLOGY, Third Edition, Volume 7, pages 417-419 (1979). Prepared at a temperature of 〇 °c. All references cited herein are hereby incorporated by reference in their entireties. The composition of a polycyclopentadiene mono-, di-acid and/or monoketone having a saturated cyclopentane ring as described herein controls the amount of functionality in a particular curable composition 14 201202284. Thus, for example, the parent-density density of the curable composition of the present disclosure can be adjusted based on the relative amount of polycyclic red bismuth and polycyclopentadiene (tetra) used in the towel (eg, reduced or ~ In this way, the light functional amount is lacking, and the balance such as the breaking temperature (Tg) of the glass is adjusted to the amount and/or the other properties (for example, toughness) of the silk is controlled. The disclosure of the content of the dicyclopentadiene and cyclopentane 4 in the polycyclopentadienic acid of the disclosure. The bicyclic red and/or poly-alkene can be formed by using cyclopentadiene by Diels-Alder chemistry. Wherein, as discussed herein, the average value of the chemical core can be edited (4)/thus, for example, when the polycyclopentadiene moiety of the polycyclopentadiene monomer is oligomeric, which may have an average system η value distribution from 2 to 5. For the pot, the example '11 may have a value of G or 1. The ability to control the dicyclopentadiene and/or polycyclopentadiene portion of the polycyclopentadiene It is also permissible to simultaneously control and/or trim while maintaining or possibly increasing the possible moisture resistance of the cured composition. The ability to combine densities. For various embodiments, the formation of a polycyclopentadiene with a saturated cyclopentane ring and/or the money and ring society "red ketone then °" tangled t cost disclosure content has The polycyclopentane ring of the saturated cyclopentane ring is a dilute. For the various embodiments, the condensation reaction of the polycyclic ring 4 and/or the polycyclopentadiene phase may have a ratio of 1:20 to 1:6. From 1:15 to 1:8, the molar ratio. For various embodiments, the condensation reaction can occur in the presence of -@catalyzed, based on the weight of the use, the acid catalyst is preferably from (UW) % by weight (wt%), and more preferably from 〇(1) by weight 15 201202284%. For various examples, the phenols used in the condensation reaction may include, without limitation, phenol, substituted phenol 'o-cresol, m- A combination of indophenol, p-nonanol, 2,4-dinonylphenol, 2,6-dimethylphenol, 1-naphthol, 2-naphthol, and the like, higher than 1:2〇 A molar ratio of phenol or substituted phenol can also be used, but this requires additional energy's. Therefore, it is necessary to recover and recycle excess phenol or substituted phenol. For example, an excess of the phenol reactant can be removed by distillation. A condensation reaction using a large excess of the discretion and/or substituted S is found to be advantageous for polycyclopentadiene diphenol having a saturated cyclopentane ring. a product which is abundant and has a very low polydispersity in the oligomer system. Similarly, when the amount of phenol and/or substituted phenol is reduced, a polycyclopentadiene diphenol having a saturated cyclopentane ring is used. At the expense of the content, the polymer will increase. The increased oligomer content favors higher hydroxyl functionality, which is highly advantageous for certain end uses. Therefore, 'although extremely large amounts of phenol and/or substituted Thereafter, the present disclosure can be used to produce a product rich in polycyclopentadiene diphenol and low in oligomers using the molar ratios provided herein. The s-reaction of the polycyclopentadiene which forms the present disclosure for various embodiments may also optionally include the use of a solvent. For these examples/reads, the reaction may be inert and the reaction product may also be used. The granules may additionally be used as a supplement for the self-condensation of water. The reactants or solvents are advantageous for maintaining a suitable reaction medium. Suitable for the catalyzed acidity of the catalyst; metal hydride, ^ instrument, 5! For example, silk acid, sulfuric acid, rolling, alumina, magnesium oxide; there are 16 201202284 organic acid, such as p-toluene acid, oxalic acid , 3-巯-1-propanthic acid, and combinations thereof. For various embodiments, 3-indol-1-propanesulfonic acid is a preferred acidic catalyst or cocatalyst. Surprisingly, it has been found that 3-indol-1-propane sulfonic acid is also highly selective in forming polycyclopentadiene diphenol without the need to azeotropically remove water from the reaction. Conversely, the water system remains in the reactor without quenching the reaction. The reaction temperature and time are in a variety 'but can be from about 5 minutes to about 48 hours, and a reaction temperature of from about 20 ° C to about 175 ° C can be used. Preferably, the reaction temperature and time can range from 15 minutes to 36 hours and from 30 minutes. (: to a reaction temperature of about 125 ° C. Preferably, the reaction temperature and time may be from 30 minutes to 24 hours and from 35 ° C to about 75 ° C. At the end of the reaction, the acidic catalyst can be used Neutralization is removed, for example, by washing or extraction with water. Similarly, at the end of the reaction, excess phenol can be removed from the product, for example, by distillation or extraction. Polycyclopentane relative to conventional techniques Dienediol, in addition to the saturated cyclopentane ring, the composition of the present disclosure has a structure in which the two rings are substantially attached to the phlegm-based ring, and such compositions of the prior art have a major The halo ring attachment and the attachment of another phenol ring to the cyclopentyl ring. Thus, the oligomer or polymer prepared using the phenolic hydroxyl group of the present disclosure, relative to the oligomer or polymer The main chain, the polycyclopentadiene moiety is pendant. The structure of the saturated cyclopentane ring or the polycyclopentane ring allows the intermetallic chain hydrophobic association of the developing thermoset. It is also possible to accumulate variants. Wherein, the side suspension structure that can be found in the embodiment of the disclosure can guide the pile of chains Or its molecular confinement within the matrix 17 201202284. Thus, the possibility of hydrophobic association of the pendant polycyclopentadiene moiety is present in the present disclosure and can promote the physical and mechanical properties of the formed cured composition. Polycyclopentadiene diphenol having a saturated cyclopentane ring has, for example, an epoxy resin curing agent for a high performance functional powder coating. When combined with a polyfunctional curing agent, for example, The cyclopentadiene is dilute. When blended, the polycyclopentadiene diphenol having a saturated cyclopentane ring can also serve as a "diluent" to reduce the functionality. The present invention has a saturated cyclopentane ring. Cyclopentadiene diphenol can be used to make an epoxy resin such as bis-A diglycidyl, 10-(2',5'-dihydroxyphenyl)-9,10-dihydro-9-oxa -10-phosphaphenanthrene-10-oxide (DOP-HQ) diglycidyl ether, dicyclopentadiene diphenol diglycidyl ether, and other epoxy resins, linearly promoted to produce side suspensions A thermosettable composition of a saturated poly or dicyclopentadienyl moiety. Formed Advanced Epoxy It can be cured with a curing agent or with other thermosetting monomers such as polycyanates. Improved moisture and corrosion resistance and promoted electrical properties, especially dissipation factors, for these advanced steps Resin is contemplated. For various embodiments, it is additionally recognized that when "n" is greater than 1, additional hydrocarbon bodies are added to the side suspension side chains and may advantageously impact the physical and mechanical properties of the thermoset. Side suspension side bonds The stacking can advantageously increase the toughness of the thermosetting matrix and induce hydrophobic bonding between the chains. In addition to the foregoing as a curing agent for epoxy resins or for the purpose of promoting the reaction of epoxy resins, the present disclosure has The saturated cyclopentane ring of polycyclopentadiene diphenol can also be used as a precursor to another thermosetting resin. These heats 18 201202284 solid resins include cyanate esters, epoxy, allyl 'allyloxy, internal return Mannyl ester, and vinyl stearic methyl ether (and other ethylenically unsaturated) resins, which are used to prepare coatings, especially functional powder coatings, and have high discontinuity, solvent resistance, moisture resistance Wear resistance, Protective coatings or structural laminates or composites of toughness; filament windings; mold potentials, cuts; scales; encapsulants; multilayer electronic circuits; integrated circuit packages (such as substrates) "); aerospace composites; and formulations with other resins such as poly(maleimide), polyester. Due to the presence of a polyfluorene ring having a saturated cyclopentane ring = a dilute moiety, a thermoset having improved wettability and resistance to decay and promoting electrical properties, particularly dissipation factors, is expected. A diglycidyl ether having a saturated cyclopentane ring and a polycyclopentadienyl glyceryl ether having a saturated cyclopentane ring and a composition thereof additionally containing an oligomer It can be prepared as above. The initial step in the preparation of the aforementioned composition of the present disclosure is generally due to the presence of an inhibitory substance, in the presence or absence of a catalyst, and in the presence or absence of a plurality of solvents, A polypentadiene diphenol having a saturated cyclopentane ring is reacted with an epimerol. For various embodiments, the reaction can range from about 20 ° C to about 120 ° C, more preferably from about 30 ° C to about 85%, and most preferably from about 4 Torr. (: occurs to a temperature of about 75 ° C. For various embodiments, the reaction may range from about 4 KPa to about 500 KPa, more preferably from about 4 KPa to about 340 KPa ' and preferably from about 8 KPa to A pressure of about 100 KPa (1 atm) occurs. For various embodiments, the reaction can occur at a time sufficient to complete the reaction, typically from about 1 to about 120 hours, more usually from about 3 to about 72 hours. Typically from about 4 to about 48 hours. 19 201202284 For various embodiments, this reaction also uses from about 1丄1 to 25:1' each preferred base map from about 18:1 to about 1 〇1, and the best system is from about!! to about 5:1 mole table _ 1 non-catalyst is based on the amount of chemical or a large amount of alkali metal or alkaline earth metal hydroxide used, this initial reaction produces a A halo alcohol intermediate product, which reacts with a test substance to convert an adjacent hydroxyl group into an epoxide group. The resulting product is a glycidyl ether compound. Details regarding the preparation of the epoxy resin are US Patent No. 5,736,620; Lee and Neville Handbook of Epoxy Resins, McGraw-Hill (1967); and J0urnal Applied Polymer Science, Vol. 23, pp. 1355-1372 (1972); and U.S. Patent No. 4,623, 701, the entire disclosure of each of which is incorporated herein by reference in its entirety in Suitable for the table!|Alcohol includes, for example, epichlorohydrin, epibromohydrin, epieol, sulfhydryl alcohol, sulfhydryl bromohydrin, decyl iodinol, and the like. The best alcohol is a gas alcohol. A suitable test substance is used to prepare the composition of the present disclosure. Suitable alkaline acting substances include, for example, alkali metal or alkaline earth metal hydroxides, carbonates And bicarbonate, and combinations thereof, etc. Particularly suitable for such compounds include sodium oxynitride, potassium hydroxide, lithium hydroxide, methane hydroxide, barium hydroxide, nitrous oxide money, hydrazine hydroxide, sodium carbonate, Carbonate oblique, carbonic acid clock, carbonic acid, acid breaker, carbonic acid town, manganese carbonate, sodium hydrogencarbonate, potassium hydrogencarbonate, magnesium hydrogencarbonate, lithium hydrogencarbonate, calcium hydrogencarbonate, barium hydrogencarbonate, magnesium hydrogencarbonate, etc. Combination of the best Or oxyhydrogen 20 201202284 potassium. Suitable methods for reacting a polycyclopentadiene diphenol having a saturated cyclopentane ring with an alkali metal hydroxide and then reacting with an alcohol of Table ii include For example, sodium hydride and hydrogenation clocks, and sodium hydride is preferred. Suitable catalysts for use in preparing the compositions of the present disclosure include, for example, sulphur compounds such as benzyltrimethyl gasification 4 amps. , benzyltrimethylammonium bromide, tetrabutylammonium hydride, tetrabutylammonium bromide, tetraoctyl ammonium hydride, tetrabutylammonium bromide, tetradecyl ammonium hydride, tetramethyl bromide Ammonium, tetrabutyl chlorinated scale, tetrabutyl bromide, tetrabutyl iodide scale, ethyl tributyl gasification scale, ethyl triphenyl bromide, ethyl triphenyl iodide scale , and combinations of them. Suitable solvents which can be used to prepare the compositions of the present disclosure include aliphatic and aromatic hydrocarbons, halogenated aliphatic hydrocarbons, aliphatic ethers, aliphatic nitriles, cyclic ethers, ketones, decylamines, sulfoxides, aliphatics and rings. Aliphatic secondary and tertiary alcohols, and combinations thereof. Particularly suitable solvents include pentane, hexane, octyl, terpene, xylene, methyl ethyl ketone, decyl isobutyl ketone, N,N-didecyl decylamine, dimercapto sulfoxide, Diethyl ether, tetrahydrofuran, 1,4-dioxane, di-methane, chloroform, dichloroethane, sulfhydryl gas, ethylene glycol didecyl ether, N,N-dimercaptoacetamide, A combination of acetonitrile, propylene glycol monomethyl ether, isopropanol, and the like. The solvent can be removed by conventional means when the reaction is completed, such as vacuum distillation. Another method of the present disclosure is carried out in the absence of a solvent, and epichlorohydrin is used in an amount as a solvent and a reactant. Analytical methods such as high pressure liquid chromatography (HPLC) can be used to simultaneously monitor the reaction of a polycyclopentadiene diphenol having a saturated cyclopentane ring, and an intermediate such as a halogen 21 201202284 alcohol and a final diglycidyl group. Formation of the ether product. The recovery and purification of the composition of the polycyclopentadiene diglycidyl ether having a saturated cyclopentane ring of the present disclosure can be carried out by various methods. For example, gravity filtration, vacuum filtration, centrifugation, water washing or extraction, solvent extraction, decantation, column chromatography, vacuum distillation, falling film evaporation, wipe film distillation, electrostatic condensation, and other treatment methods Etc. can be used. Vacuum distillation is the best method for removing and recovering higher boiling fractions, for example, the unused alcohol. This recycles the surface alcohol and solvent (if used) for recycling. Oligomers may also be present in the polycyclopentadiene diglycidyl ether of the present disclosure having a saturated cyclopentane ring. These are typically epoxidized from an oligomer component present in the precursor of a polycyclopentadiene diphenol having a saturated cyclopentane ring or from a portion of the glycidyl ether moiety. The position is generated by an advanced reaction. The advanced reaction is characterized by the formation of a 2-hydroxypropyl ether linkage (structure of Chemical Formula VII) in the advanced epoxy resin product:

化學式VIIChemical formula VII

其中,R1係如此處所定義。 本揭露内容之具有飽和環戊烷環之聚環戊二烯二縮 甘油基醚與其與一或多種傳統環氧樹脂之摻合物可用 以製備(1)進階之環氧樹脂(可熱固化)(2)乙烯基酯及乙稀 基酯樹脂(3)環氧樹脂加成物,其可作為(a)環氧樹脂固化 22 201202284 劑、⑻用於熱固性聚胺甲酸醋、聚尿素胺甲酸响,及聚異 氛脲酸醋之反應物(c)用於製備聚胺甲酸醋、聚尿素胺甲酸 醋,及聚異氰_⑬之多元醇之起始劑,及(4)用於其它熱 固性樹脂系統之單體,例如,於與二或聚異氰酸醋之共聚 合而產生含°惡α坐燒g同之熱固物。 具有飽和環戊烧環之聚環戊二稀二齡之二氰酸醋 對於各種實施例,本揭露内容之具有飽和環戊烧環二 * 氰酸§旨可藉由—或多種本揭露内容之具有飽和環戊烧環 之聚ί哀戊二烯二酚與每一酚羥基基團為一化學計量之量或 一些微化學計量過量(最高達約2〇%之過量)之一鹵化氰反 應而製備。對於各種實施例,此反應亦於每一酚羥基基團 為一化學計量之量或一些微化學計量過量(最高達約2〇%過 - 量)之一鹼化合物存在中及於一或多種適合溶劑存在中發 生。 從約-40°C至約60。(:之反應溫度係較佳,且_15。(3至1〇 °(:之反應溫度係更佳’且_i〇〇c至〇。(:之反應溫度係最佳。 反應時間可大量變化’例如,為使用反應物、反應溫度、 使用溶劑、反應規格等之函數,但通常係15分鐘與4小時之 間,且30分鐘至90分鐘之反應時間係較佳。 適合之鹵化氰包括氣化氰及溴化氰。另外,於由j〇hnWherein R1 is as defined herein. A polycyclopentadiene diglycidyl ether having a saturated cyclopentane ring and a blend thereof with one or more conventional epoxy resins can be used to prepare (1) advanced epoxy resin (heat curable) (2) Vinyl ester and ethylene ester resin (3) Epoxy resin adduct, which can be used as (a) epoxy resin curing 22 201202284 agent, (8) for thermosetting polyurethane urethane, polyurea formate Resin, and the reaction of polyisocyanuric acid vinegar (c) is used to prepare polyurethane vinegar, polyurea carboxylic acid vinegar, and polyisocyanate _13 polyol starter, and (4) for other The monomer of the thermosetting resin system, for example, is copolymerized with di- or polyisocyanuric acid to produce a thermosetting substance containing the same. Polycyclopentadiene di-cyanate bis- cyanate having a saturated cyclopentane ring. For various embodiments, the present disclosure has saturated cyclopentane bis- cyanate § by means of - or a plurality of A poly( pentadiene diphenol) having a saturated cyclopentane ring is reacted with one of the stoichiometric amount or some micro-stoichiometric excess (up to about 2% by weight excess) of one of the phenolic hydroxyl groups. preparation. For various embodiments, the reaction is also in the presence of one stoichiometric amount or some microstoichiometric excess (up to about 2% by weight) of one of the base compounds per phenolic hydroxyl group and in one or more suitable Occurs in the presence of a solvent. From about -40 ° C to about 60. (: The reaction temperature is preferably, and _15. (3 to 1 〇 ° (: the reaction temperature is better 'and _i 〇〇 c to 〇. (: the reaction temperature is the best. The reaction time can be large The change 'for example, is a function of the reactants, reaction temperature, solvent used, reaction size, etc., but usually between 15 minutes and 4 hours, and a reaction time of 30 minutes to 90 minutes is preferred. Suitable cyanogen halides include Gasification cyanide and cyanogen bromide. In addition, by j〇hn

Wiley and Sons 出版之Organic Synthesis,第 61 冊,35-68 頁(1983)中所述之Martin及Bauer之方法’其在此被完整併 入本案以為參考資料’可用以在原位自氰^化納及諸如氣或 溴之ii素產生所需之函化氰。 23 201202284 適。之驗化合物包括無機驗及三級胺,諸如,氫氧化 納氣氧化鉀、二甲基胺、三乙基胺,及其等之組合。三 乙基胺係作為驗之最佳。 用於氰化反應之適合溶劑包括水、脂族酮、氣化煙、 脂族及環脂_及二崎、芳香紐,及其等之組合。丙嗣 曱基乙基酮、二氣Μ,或氣仿係特別適於作為溶劑。 具飽和環錢環之二氰㈣係選擇性於-適合催化劑 存在中藉由加熱從⑽。。至約·。c,較佳係藉由加熱從 100 〇C至300 〇C ’而固化(熱固化)。適合催化劑包括,例如, &amp;L類驗類鹽類、氮及鱗化合物,諸如,路易士酸,諸 如,A1C13 BF3、FeCl3、Ticu、ZnCl2、SnCU ;質子酸,諸 如HC1 ’ H3P〇4,芳香族經基化合物,諸如,齡對石肖基 齡鄰笨一酌·、二經基萘;氫氧化鈉、甲醇鈉、苯酚納、 二甲基胺、三乙基胺、三丁基胺、二吖二環[2 2 2]辛烷、喹 啉、異喹啉、四氫異喹啉酮、四乙基氣化銨、吡啶_N氧化 物、二丁基膦、辛酸鋅、辛酸錫、環烧酸鋅、環烧酸鈷、 辛酸鈷、乙醯基丙酮酸鈷等。亦適合作為催化劑係金屬餐 合物,諸如,過渡金屬及雙配位或三配位之配位體的螯合 物’特別疋鐵、姑、辞、銅、猛、錯、欽、飢、紹及鎂之 配位體。此等其它可操作之催化劑係揭示於美國專利第 3,694,410及4,094,852號案,其等在此被完整併入本案以為 參考資料。環烧酸姑、辛酸話,及乙醯基丙鲷酸話係作為 催化劑最佳者。若有的話,使用催化劑之量係依特定催化 劑之結構、欲被固化之聚氰酸酯之結構、固化溫度、固化 24 201202284 時間等而定。一般,從約0·001至約2重量%之催化劑濃度係 較佳。 對於各種實施例,本揭露内容之具有飽和環戊烷環之 二氰酸酷之組成物之Β -階段或預聚合反應可藉由使用較低 溫度及/或較短之固化時間而完成。然後,因而形成之Β_階 段(經預聚合)之樹脂之固化可於Β_階段(預聚合反應)後之 稍後時間或立即地藉由增加溫度及/或固化時間而完成。除 非其它官能性存在於參與固化方法之聚氰酸酯中,自具有 飽和環戊烷環之二氰酸酯製得之經固化(熱固化)產物擁有 氰酸酯基團之均聚合化結構,聚三畊環。 於另外實施例’本揭露内容亦提供(1)具有飽和環戊烷 環之聚環戊二稀二氰酸酯,或此二氰酸酯之一部份聚合之 產物’與(2)—或多種之選自由一雙或聚馬來醯亞胺、—非 本揭露者之二或聚氰酸酯、一二或聚氰胺、一環氧樹脂' —可聚合之單、二,或聚乙烯不飽和單體(包括乙烯基芳香 族單體、乙烯基苯甲基醚、烯丙基,及烯丙氧基化合物)所 構成族群之組份之一摻合物.一部份聚合化(Β_階段)之產 物’或一經固化(熱固化)之產物。 具有飽和環戊烷環之聚環戊二烯二酚之乙烯基苯甲基醚 本揭露内容之具有飽和環戊烷環之聚環戊二烯二紛之 乙烯基笨曱基醚可藉由於每一酚羥基基團為一化學計量過 里之諸如氫氧化鋰之一鹼化合物存在中,且於諸如甲醇之 適合〉谷劑存在中,使一或多種之聚環戊二烯二齡與每一 酚羥基基團為一化學計量過量之一乙烯基苯曱基_化物反 25 201202284 應而製備。諸如2,6-二·第三丁基_4-曱基酚或氫醌之一自由 基起始劑典型上係作為一於原位聚合化反應抑制劑。 從約10°c至約之反應溫度係可操作,且20〇c至 75 °C之反應溫度係較佳,且25 0(:至6〇 〇c之反應溫度係最 佳。反應時間可大量變化,例如,為欲被使用之反應物、 反應溫度、使用之溶劑、反應規格等之函數,但—般係於4 小時至約5天之間。 適合之乙烯基笨甲基鹵化物包括鄰-乙烯基苯甲基氣 化物、間·乙職苯甲基氣化物、對·乙稀基苯甲基氣化物、 鄰-乙烯基苯甲基演化物、間_乙烯基苯曱基漠化物、對-乙 烯基苯甲錢化物、3_乙稀基苯曱基_5_甲基氯化物,及其 等之組合。適合之驗化合物包括無機驗及三級胺,諸如了 氫氧化經、氫氧化鈉、氫氧化卸、三甲基胺、三乙基胺, 及其之組合。氫氧鋰係作為鹼之最佳者。 用以形成乙烯基笨甲基醚之適合溶劑包括水、脂族 鲷、氣化烴、脂族及環脂_及二醚、芳香族煙,及其等 σ &amp; 甲醇,及其等之組合係特別適於作為 冷Μ驗及可於用於反應前組合,且甲醇氫氧化卸溶 液係一例子。 〃有飽和環之轉戊二烯二狀乙婦基苯甲基 Γ可選雜於—❹種適合催化劑存在中藉由加熱從約30 C至約二〇 C,較佳係藉由加熱從_ 〇c至300 〇c而固化(熱 )右有的’使用之催化劑的量係依特定催化劑之結 構奴被固化之乙烯基苯甲基社結構、固化溫度、固化 26 201202284 時間等而定。一般,從約0·001至約2重量%之催化劑濃度係 較佳。 本揭露内容之乙烯基苯曱基醚之組成物之B—階段或預 聚合反應可藉由使用較低溫度及/或較短之固化時間而完 成。然後,因而形成之Β-階段(經預聚合)之樹脂之固化可於 Β -階段(預聚合反應)後之稍後時間或立即地藉由增加溫度 及/或固化時間而完成。 具有飽和環戊烷環之聚環戊二烯二酚之烯丙基瞇 本揭露内容之具有飽和環戊烷環之聚環戊二烯二齡之 烯丙基(或1-丙烯基)醚可藉由一或多種之聚環戊二烯二酚 之烯丙基化而製備,其中,芳香族羥基基團(_〇Η)轉化成 HR5C=CR5-CH2-〇-及/或H2R5C-CR5=HC-0-,其中,每一 R5係獨立地選自由氫及具有從1至3個碳原子之烷基基團 所構成之族群。對於各種實施例,烷基基團可為未經取代 或經取代。對於一或多個實施例,較佳地係x為未經取代。 對於一或多個實施例,較佳係每一X為相同。 聚環戊二烯二酚之烯丙基醚之形成係於同此案提申之 美國新型申請案序號 / ,名稱為“聚環戍二烯聚酚之 聚(烯丙基醚)”,陶氏化學公司檔案編號68992,中探討,此 揭示内容在此併入本案以為參考資料。簡言之,聚環戊二 烯二酚之烯丙基化可經由一轉碳酸化反應完成。此轉碳酸 化反應可包括烯丙基甲基碳酸酯於一催化量之於碳上之產巴 及三苯基膦存在中與聚環戊二烯 二酚反應。 烯丙基甲基碳酸酯可自烯丙基醇及二甲基碳酸酿之反 27 201202284 應製備。此反應可提供烯丙基甲基碳酸g旨及二烯丙基碳酸 醋之混合物。此混合物及/或純的烯丙基甲基碳酸酿可用 於轉碳酸化反應。 聚環戊二烯二盼之稀丙基化可藉由可包括-論化 物、-驗试劑’及選擇性之諸如__相轉化催化劑之一催 化劑之-直接烯丙基化反應完成。鹵化物之例子不受限 地包括烯丙基画化物及甲基烯丙基鹵化物。烯丙基函化 物之例子*受限地包括_基氣化物及稀丙㈣化物。甲 基稀丙基齒化物之例子不受限地包括甲基_基氣化物及 甲基烯丙基溴化物。鹼試劑之一例子不受限地包括—鹼金 屬氫氧化物之一水溶液。鹼金屬氫氧化物之例子不受限地 包括氫氧化鉀及氫氧化鈉》催化劑之例子不受限地包括苯 曱基三烷基函化銨及四烷基函化銨。烯丙基化可包括烯 丙基甲基碳酸酯、二烯丙基碳酸酯、齒化物、鹼試劑、 催化劑,及其等與聚環戊二烯聚酚之組合物。 聚%戊一稀一盼之直接稀丙基化可於25 °C至150 °C之 溫度發生。對於某些應用,50。(:至100 〇C之溫度對於烯丙 基化係較佳。聚環戊二烯二酚之烯丙基化可具有15分鐘至8 小時之反應時間。對於某些應用,2小時至6小時之反應 時間係較佳。聚環戊二烯二酚之烯丙基化可包括一溶劑。 此溶劑之一例子不受限地包括1,4-二噁烷。 於一直接烯丙基化反應。烯丙基函化物可與聚環戊 二稀二盼之經基基團化學計量地反應。對於各種反應條 件’變化量之一Claisen重排產物可於此反應觀察到,且可 28 201202284 造成〇-及c-烯丙基化產物之混合物。 〜1比1莫耳比率之稀丙基_化物與聚環戊二稀二紛之 ,基基團之反應可提供—經烯丙基化之雙酚其中,聚 環戊二稀二盼之一主要量(約80或更多之百分率)之羥基 基團轉化成-q-CH2-CH=CH2基團⑻卜…少量(約2〇% 或更V)之烯丙基基團可進行熱誘發之㈤㈣重排,且可 存f於與發生重排之經基基團呈鄰位及/或對位之芳香 族%上。少於1比!莫耳比率之於轉碳酸化反應中之稀丙 基曱基碳酸酯或於於直接烯丙基化反應之烯丙基函化 物與經基基團之反應可提供與剩餘之一些經基基團之 部份烯丙基化。雖然經部份烯丙基化之化合物對於某些 應用係次佳,但其等仍係於本揭露内容之範圍内。 一較佳方法使用其中烯丙基曱基碳酸酯係與聚環戊 二烯二酚化學計量地反應提供聚環戊二烯二酚之羥基基團 之基本上完全之烯丙基化及提供相對應之烯丙基醚(烯丙 乳基)基團之一轉碳酸化反應。 若存在’烯丙氧基及烯丙基基團之異構化成更具反應 性之1-丙烯基基團可於一鹼存在中使用T. W. Green及P. G. M. Wuts 於 Protective Groups in Organic Synthesis ’ Wiley-Interscience,New York,67-74,708-711 (1999)中報 導之方法或於Journal of Molecular Catalysis A: Chemical volume 219,issue 1,29-40頁(2004年9月 1 日)中所述之一催 化量之一釕錯合物存在中實施。二前述參考文獻在此被完 整併入本案以為參考資料。 29 201202284 具有飽和環戊烷環之聚環戊二烯二酚之丙烯酸酯及甲基丙 烯酸酯 丙烯酸酯及甲基丙烯酸酯可使用C. Schotten,Ber. 17, 2544 (1884)及Ε· Baumann, ibid· 19, 3218 (1886)中所述之一 Schotten-Baumann型反應經由一酸氣化物,諸如,個別係丙 稀醯氣(2-丙稀醯氣)或甲基丙稀醯氣,之反應而製備。對於 此醯基化反應,一或多種驗作用物質,諸如,含水之氫氧 化鈉、三乙基胺或〇比唆,可被使用。另外,有利地係使用 多種聚合化抑制劑之一者,諸如,氫醌。轉酯化反應亦可 被用以製備丙烯酸酯及甲基丙烯酸酯。合成不具有作為可 交聯之二烯雜質的丙烯酸酐或曱基丙烯酸酐之高純度丙烯 酸酯及曱基丙烯酸酯之方法係由Stacy B. Evans,. J. Ε. Mulvaney,H. K_ Hall Jr•於2003年3月10日於線上公開之The method of Martin and Bauer described in Wiley and Sons, Organic Chemistry, Vol. 61, pp. 35-68 (1983), which is hereby incorporated by reference in its entirety herein in The sodium hydride such as gas or bromine produces the desired functional cyanide. 23 201202284 Appropriate. The test compound includes an inorganic test and a tertiary amine such as sodium oxyhydroxide, dimethylamine, triethylamine, and the like. Triethylamine is the best test. Suitable solvents for the cyanation reaction include water, aliphatic ketones, gasified fumes, aliphatic and cycloaliphatic _ and bisaki, aromatic nucleus, and combinations thereof. Propionyl mercapto ethyl ketone, dioxane, or gas imitation is particularly suitable as a solvent. The dicyano(4) with a saturated ring of money is selective in the presence of a suitable catalyst by heating from (10). . To about. c, preferably cured (heat-cured) by heating from 100 〇C to 300 〇C '. Suitable catalysts include, for example, &amp;L class salts, nitrogen and scaly compounds such as Lewis acid, such as A1C13 BF3, FeCl3, Ticu, ZnCl2, SnCU; protonic acids such as HC1 'H3P〇4, aromatic a compound of a sulfhydryl group, such as an age-dependent succinyl group, a diazepam, a dipyridyl naphthalene; sodium hydroxide, sodium methoxide, phenol sodium, dimethylamine, triethylamine, tributylamine, diterpenoid Cyclo [2 2 2]octane, quinoline, isoquinoline, tetrahydroisoquinolinone, tetraethylammonium hydride, pyridine_N oxide, dibutylphosphine, zinc octoate, tin octoate, benzoic acid Zinc, cobalt sulphonate, cobalt octoate, cobalt acetylacetonate, and the like. Also suitable as a catalyst metal complex, such as a transition metal and a chelate compound of a bi- or tri-coordinated ligand, especially 疋铁, 姑, 辞, 铜, 猛, 错, 钦, 饥, 绍And magnesium ligands. </ RTI> <RTIgt; </ RTI> <RTIgt; </ RTI> <RTIgt; </ RTI> <RTIgt; </ RTI> <RTIgt; The ring-burning acid, the octanoic acid, and the ethoxylated propionate are the best catalysts. The amount of catalyst used, if any, depends on the structure of the particular catalyst, the structure of the polycyanate to be cured, the cure temperature, the cure time 201202284, and the like. Generally, a catalyst concentration of from about 0.001 to about 2% by weight is preferred. For various embodiments, the Β-stage or prepolymerization of the composition of the cyanuric acid having a saturated cyclopentane ring of the present disclosure can be accomplished by using a lower temperature and/or a shorter curing time. The curing of the thus formed Β stage (prepolymerized) resin can then be accomplished at a later time or immediately after the Β stage (prepolymerization) by increasing the temperature and/or curing time. Unless the other functionality is present in the polycyanate participating in the curing process, the cured (thermoset) product prepared from the dicyanate having a saturated cyclopentane ring possesses a homopolymerized structure of cyanate groups, Gathering three farming rings. In a further embodiment, the present disclosure also provides (1) a polycyclopentaise diacrylate having a saturated cyclopentane ring, or a partially polymerized product of the dicyanate 'and (2) - or a plurality of selected from the group consisting of a double or polymaleimide, a non-discloser or a polycyanate, a di- or melamine, an epoxy resin - a polymerizable single, two, or polyethylene a blend of one of the components of the group consisting of unsaturated monomers (including vinyl aromatic monomers, vinylbenzyl ethers, allyl groups, and allyloxy compounds). Partially polymerized (Β The product of the stage _ or the product of curing (heat curing). Vinylbenzyl ether of polycyclopentadiene diphenol having a saturated cyclopentane ring. The present invention discloses a polycyclopentadiene having a saturated cyclopentane ring. a phenolic hydroxyl group is in the presence of a stoichiometric amount of an alkali compound such as lithium hydroxide, and in the presence of a suitable granule such as methanol, one or more polycyclopentadienes are aged and each The phenolic hydroxyl group is prepared in a stoichiometric excess of one of the vinyl benzoyl-based compounds 25 201202284. A free radical initiator such as 2,6-di-t-butyl-4-nonylphenol or hydroquinone is typically used as an inhibitor of in-situ polymerization. The reaction temperature is from about 10 ° C to about 10 ° C, and the reaction temperature is preferably from 20 ° C to 75 ° C, and the reaction temperature of 25 0 (: to 6 ° C is optimal. The reaction time can be large. The change, for example, is a function of the reactant to be used, the reaction temperature, the solvent used, the reaction specification, etc., but is generally between 4 hours and about 5 days. Suitable vinyl stray methyl halide including adjacent -vinylbenzyl vapor, m-benzyl benzyl vapor, p-ethylene benzyl vapor, o-vinylbenzyl evolution, meta-vinyl benzoyl desert, a combination of p-vinyl benzoic acid, 3 - ethyl phenyl fluorenyl _ 5-methyl chloride, and the like. Suitable compounds include inorganic and tertiary amines such as hydrogen peroxide and hydrogen. Sodium oxide, hydrogen hydroxide, trimethylamine, triethylamine, and combinations thereof. Lithium hydroxide is the best base. Suitable solvents for the formation of vinyl stupid methyl ether include water, aliphatic鲷, gasification hydrocarbons, aliphatic and cycloaliphatic _ and diethers, aromatic fumes, and their σ &amp; methanol, and combinations thereof, etc. It is suitable as a cold test and can be combined before use in the reaction, and the methanol hydroxide unloading solution is an example. The 转 转 转 转 转 转 二 二 二 二 Γ Γ Γ Γ Γ Γ Γ Γ Suitable for the presence of a catalyst by heating from about 30 C to about 2,000 C, preferably by heating from _ 〇c to 300 〇c to cure (heat) the right amount of the catalyst used, depending on the particular catalyst The structural slave is cured by a vinyl benzyl structure, a curing temperature, a curing time of 201202284, etc. Generally, a catalyst concentration of from about 0.001 to about 2% by weight is preferred. The B-stage or prepolymerization of the composition of the mercapto ether can be accomplished by using a lower temperature and/or a shorter curing time. Then, the thus formed bismuth-stage (prepolymerized) resin can be cured. Completed at a later time or immediately after the stage (prepolymerization) by increasing the temperature and/or curing time. Allyl oxime of a polycyclopentadiene diphenol having a saturated cyclopentane ring is disclosed. Content of polycyclopentadiene with a saturated cyclopentane ring Allyl (or 1-propenyl) ether can be prepared by allylation of one or more polycyclopentadiene diphenols, wherein the aromatic hydroxyl group (_〇Η) is converted to HR5C=CR5 -CH2-〇- and/or H2R5C-CR5=HC-0-, wherein each R5 is independently selected from the group consisting of hydrogen and an alkyl group having from 1 to 3 carbon atoms. For example, the alkyl group can be unsubstituted or substituted. For one or more embodiments, preferably x is unsubstituted. For one or more embodiments, preferably each X is the same. The formation of the allyl ether of polycyclopentadiene diphenol is the same as the US new application serial number given in this case, and the name is "poly(alkyl ether) of polycyclodecadiene polyphenol", Tao The company's Archives No. 68992, the disclosure of which is incorporated herein by reference. Briefly, allylation of polycyclopentadiene can be accomplished via a one-pass carbonation reaction. This transcarbonation reaction can include the reaction of allyl methyl carbonate with polycyclopentadiene diphenol in the presence of a catalytic amount of carbon and triphenylphosphine. Allyl methyl carbonate can be prepared from allylic alcohol and dimethyl carbonate. 27 201202284 should be prepared. This reaction provides a mixture of allyl methyl carbonate g and diallyl carbonate. This mixture and/or pure allyl methyl carbonate can be used in the transcarbonation reaction. The dipropylation of polycyclopentadiene can be accomplished by a direct allylation reaction which may include a catalyst, a reagent, and a selective catalyst such as a catalyst for the __ phase inversion catalyst. Examples of the halide include, without limitation, allyl halides and methallyl halides. Examples of allyl complexes* are limited to include a base gas and a propylene (tetra) compound. Examples of the methyl propyl carboxylate include, without limitation, methyl-based vapors and methallyl bromides. An example of an alkali reagent includes, without limitation, an aqueous solution of one of alkali metal hydroxides. Examples of the alkali metal hydroxide include, without limitation, potassium hydroxide and sodium hydroxide. Examples of the catalyst include, without limitation, benzoyltrialkylammonium and tetraalkylammonium. The allylation may include a combination of allyl methyl carbonate, diallyl carbonate, a dentate, an alkali reagent, a catalyst, and the like, and a polycyclopentadiene polyphenol. Direct propylation of poly% pentane can occur at temperatures between 25 ° C and 150 ° C. For some applications, 50. (The temperature to 100 〇C is preferred for allylation. The allylation of polycyclopentadiene diol can have a reaction time of 15 minutes to 8 hours. For some applications, 2 hours to 6 hours The reaction time is preferably preferred. The allylation of polycyclopentadiene diphenol may include a solvent. One example of such a solvent includes, without limitation, 1,4-dioxane. The allylic complex can be stoichiometrically reacted with a polycyclopentadienyl group. For one of the various reaction conditions, a Claisen rearrangement product can be observed for this reaction, and can be caused by 28 201202284 a mixture of 〇- and c-allylized products. The ratio of ~1 to 1 molar ratio of the propyl group and the polycyclopentadiene, the reaction of the group can provide - allylation A major amount (about 80 or more percentages) of a hydroxyl group converted to a -q-CH2-CH=CH2 group (8), a small amount (about 2% or The allyl group of more V) may be thermally induced (5) (iv) rearranged and may be present in the ortho and/or para position to the radical group where the rearrangement occurs. % of fragrance: less than 1 ratio! molar ratio of the propyl fluorenyl carbonate in the transcarbonation reaction or the reaction of the allylic group and the thiol group in the direct allylation reaction Partial allylation with some of the remaining radical groups may be provided. While partially allylated compounds are preferred for certain applications, they are still within the scope of the disclosure. A preferred method uses a stoichiometric reaction of allyl decyl carbonate with polycyclopentadiene diphenol to provide substantially complete allylation of the hydroxyl group of the polycyclopentadiene diphenol and provide corresponding One of the allyl ether (allyl emulsion) groups is converted to a carbonation reaction. If the presence of the 'allyloxy group and the allyl group isomerized to a more reactive 1-propenyl group, In the presence of a base, the method reported in TW Green and PGM Wuts in Protective Groups in Organic Synthesis 'Wiley-Interscience, New York, 67-74, 708-711 (1999) or in Journal of Molecular Catalysis A: Chemical volume 219, Issue 1, 29-40 (September 1, 2004) One of the catalytic amounts is practiced in the presence of a complex. The foregoing reference is hereby incorporated by reference in its entirety in its entirety in its entirety in the the the the the the the the the the the the the the the the Ester acrylates and methacrylates can be used in a Schotten-Baumann type reaction via an acid vapor hydride as described in C. Schotten, Ber. 17, 2544 (1884) and Ε Baumann, ibid 19, 3218 (1886). It is prepared, for example, by reacting acrylonitrile (2-acrylonitrile) or methyl propylene. For this thiolation reaction, one or more test substances such as aqueous sodium hydroxide, triethylamine or hydrazine can be used. Further, it is advantageous to use one of a plurality of polymerization inhibitors such as hydroquinone. The transesterification reaction can also be used to prepare acrylates and methacrylates. A method for synthesizing high purity acrylates and mercapto acrylates having no acrylic acid or mercaptoacrylic anhydride as crosslinkable diene impurities is by Stacy B. Evans, J. Mulvaney, H. K_ Hall Jr • Opened online on March 10, 2003

Journal of Polymer Science Part A: Polymer Chemistry,第 28 冊,第5期,第1073 - 1078頁中描述。所有前述參考文獻在 被完整此併入本案以為參考資料。 下列實施例係例示本發明,但不被作為以任何方式限 制其範圍而闡釋。 實施例 下列實施例係用以例示,但非限制,本揭露内容之範 圍。除非其它指示,所有份數及百分率係以重量計。除非 其它特定者外,使用之所有儀器及化學品係可購得。 材料Journal of Polymer Science Part A: Polymer Chemistry, Vol. 28, No. 5, pp. 1073 - 1078. All of the aforementioned references are incorporated herein by reference in its entirety. The following examples are illustrative of the invention, but are not to be construed as limiting the scope thereof in any way. EXAMPLES The following examples are intended to illustrate, but not to limit, the scope of the disclosure. All parts and percentages are by weight unless otherwise indicated. All instruments and chemicals used are commercially available unless otherwise specified. material

Rh(CO)2(乙醯基丙酮酸酯),可得自Strem Chemicals 30 201202284Rh(CO)2 (ethyl phthalate) available from Strem Chemicals 30 201202284

Inc 〇 正丁基二苯基膦,可得自 Organometallics,Inc (E. Hampstead,NH,USA)。 二環戊二烯,可得自陶氏化學公司。 合成氣,可得自 Airgas Great Lakes, Inc。 3-酼丙炫-1-確酸,鈉鹽,90%純度,可得自Sigma-A丨drich。 氫氣酸,A.C.S.試劑等級,37.5%,藉由酸鹼滴定,可得自 Mallinckrodt Baker, Inc。 酚,&gt;99%,可得自陶氏化學公司。 四氫呋喃,無水,299.9 %,無抑制劑,可得自 Sigma-Aldrich。 本甲基二乙基氯化銨’ 99% ’可得自Sigma-Aldrich。 異丙醇’ A.C.S.試劑等級,39.5%,可得自 Sigma-Aldrich 〇 氫氧化鈉,試劑等級’ 298%,丸粒,無水,可得自sigma-Aldrich 〇 曱基異丁基鲷(4-曱基-2-丙嗣),299%,由EastmanInc. n-butyldiphenylphosphine, available from Organometallics, Inc (E. Hampstead, NH, USA). Dicyclopentadiene, available from The Dow Chemical Company. Syngas is available from Airgas Great Lakes, Inc. 3-anthracene-1-acid, sodium salt, 90% purity, available from Sigma-A丨drich. Hydrogen acid, A.C.S. reagent grade, 37.5%, available from Mallinckrodt Baker, Inc by acid-base titration. Phenol, &gt; 99%, is available from The Dow Chemical Company. Tetrahydrofuran, anhydrous, 29.9%, without inhibitor, available from Sigma-Aldrich. The present methyl diethyl ammonium chloride '99%' is available from Sigma-Aldrich. Isopropanol' ACS reagent grade, 39.5%, available from Sigma-Aldrich cesium hydroxide, reagent grade '298%, pellets, anhydrous, available from sigma-Aldrich decyl isobutyl hydrazine (4-曱) Base-2-Bingo),299% by Eastman

Chemical Company製造’可得自 Sigma_Aldrich。 表氣醇,可得自陶氏化學公司。 4,4’-二胺基二苯基曱烷’仝97%氣相層析純度,可得自 Sigma-Aldrich。 二氰二胺,粉狀(未經加速)’可得自Air Products之 Amicure® CG 系列。 KBr,FT-IR等級,2 99%微量金屬基準,可得自 31 201202284Made by Chemical Company' available from Sigma_Aldrich. Epigas alcohol is available from The Dow Chemical Company. 4,4'-Diaminodiphenylnonane' is 97% gas chromatographic purity and is available from Sigma-Aldrich. Diacyanamide, powdered (unaccelerated) is available from Air Products' Amicure® CG range. KBr, FT-IR grade, 2 99% trace metal benchmark, available from 31 201202284

Sigma-Aldrich 0 石夕藻土,可得自 Celite Corporation之Celite® 545。 實施例1-具有飽和環戊烷環之二環戊二烯二酚之製備 A. 具有飽和環戊烷環之二環戊二烯單醛之製備 於稍微溫的二環戊二烯(14〇克;1.06莫耳)中之Rh(CO)2 乙醯基丙酮酸醋(70·2毫克(mg); 0.272毫莫耳(mmol))及正丁 基二笨基膦(0.33克(g); 1.36毫莫耳)之反應混合物於一沖洗 箱中於乾燥氮氣下製備,然後,置於一250毫升(mL)之Parr 反應器中,於20 °C以1:1之合成氣(1:1莫耳比率之CO:H2)喷 射三次。然後,反應混合物於90 psi之合成氣壓力下加熱至 l〇〇°C,且攪拌1天,然後,於130°C及於90psi之氣成氣壓 力下持續6天並且攪拌。自反應混合物之產物形成藉由使用 一 Agilent 6890氣相層析系統之氣相層析術(GC)監測《形成 混合物之最終GC分析顯示具有飽和環戊烷環之二環戊二 烯單醛佔65.5面積% » 反應器被冷卻,混合物被回收,且粗製產物(177.8克) 於真空下使用一 10公分之Vigreux蒸德塔蒸顧產生78.2克之 具有飽和環戊烷環之二環戊二烯單醛,其於0.17 mm Hg具 有65-68 °C之沸點。使用具有Agilent 5973質量選擇檢測器 之一 Agilent 6890 GC對透明液體蒸餾產物進行氣相層析/質 譜(GC/MS)分析支持所欲之具有飽和環戊烷環之二環戊二 烯單醛之形成:M+= 164, 146, 136, 107, 95, 79, 67。 B. 3_巯-1-丙烷磺酸催化劑之製備 3-疏丙烧-1-續酸,鈉鹽(10.75克)添加至濃氫氣酸(35.7 %水, 32 201202284 200毫升),其於一玻璃瓶杯内進行磁性攪拌。以一 parafllm “M”(American National Can,Greenwich,CT)片材覆蓋以避免攝取 大氣中之水份後,形成之白色結晶淤漿攪拌5分鐘,然後,於— 中等燒結玻璃漏斗過濾《濾液經旋轉式蒸發產生8·88克之淡黃色 黏稠狀固體產物,其於無進一步處理下作為催化劑。 C.酚化反應 具有飽和環戊烷環之二環戊二烯單醛(43.31克,0.2845 莫耳,未校正)及熔融酚(850.2克,9.0345莫耳)添加至_5 公升之玻璃三頸圓底反應器。此反應器另外裝設一環境溫 度(22。〇冷凝器及一溫度計,二者皆係經由一claisen轉接 器固定於反應器,加上一塔頂式氮氣入口,一玻璃攪拌軸, 其具有一Teflon (E.I.duPontde Nemours)授拌刀片,其與— 變速馬達偶合以提供機械式攪拌,及一恆溫控制加熱包。 開始塔頂氮氣流(〇·5公升/分鐘),其後加熱,然後攪 拌。溫度達64 °C時,查覺到一透明溶液。此時,開始添加 3-巯丙烷-1_磺酸之部份物(使用之總催化劑係2 22克,相闞 於具有飽和環戊烷環之二環戊二烯單醛係0.05莫耳。/〇)至攪 拌溶液内。起始部份之催化劑(0.42克)於2分鐘誘發最大放 熱達70 °C,溶液變成金琥珀色。加熱包自反應器移除,且 與風漏接合使反應科部冷卻至65。0添加第二部份之催 化劑(〇_31克),且停止冷卻且將加熱包重新置放回反應器 上第一部份之催化劑未誘發放熱,且於添加後一分鐘查 覺到64 0C之、;©电 ,,+ &lt;_度。此時’另外部份之催化劑於其後η分鐘 期間添加’同時將琥㈤色溶液之溫度維持於63 65 °C。反 33 201202284 應溫度於其後72小時維持於65 °C,期間’反應過程經由 HPLC分析注視。 一 Hewlett Packard 1090液相層析儀係使用具有一 Eclipse®(Agilent) XDB-C8分析防護管(5 μ,4.6 X 12.5 mm) 之一Zorbax Eclipse® (Agilent) XDB-C8分析管(5 μ,4.6 x 150 mm)而使用。此等管柱係維持於40°C之層析爐内。乙腈 及水(以0.05 %之含水的鄰-磷酸)作為洗提劑,且個別地以 一 50 / 50 %之溶液以1.000毫升/分鐘之速率經由泵而起始 遞送,且於5分鐘後改變成一90/ 10 %之溶液,且於其内維 持其後之15分鐘。使用之乙腈係HPLC等級,100.0 %純度(以 氣相層析術)’具有189 NM之UV截止。使用之鄰-磷酸公稱 上係85 °/。純度(實際分析85.1 使用之水係HPLC等級。 用於樣品分析之一二極體陣列檢測器設定為225 nm,且參 考係設定為550 nm。反應2.4小時後,HPLC分析顯示二環 戊二烯單酸完全轉化成一產物分佈,且其後於產物係極少 變化。 反應時間結束時’反應器内容物以去離子(DI)水稀釋將 5公升反應器填充至容量之95 %。授拌於1小時後停止,且 反應器内容物沈降隔夜。次日,水性層自反應器吸出,且 以廢棄物棄置。反應器以新的去離子水重新填充,且搜掉 開始持續65分鐘。停止攪拌,且反應器内容物沈降隔夜。 次曰,水性層自反應器吸出,且以廢棄物棄置。清洗程序 另外重複兩次,其後藉由經濾紙傾析而自反應器收集固 體。因而回收之固體添加至一陶瓷碟,且於1〇〇〇c之真空爐 34 201202284 内乾燥24小時,移除,研磨成細微粉末,且於真空爐内另 外乾燥48小時而提供84.32克之淡紫色粉末。 KBr丸粒之FTIR分析顯示越之徵基伸展完全消失,且 於1609.6(肩部於1595.8)及1509.8 cm—1出現強烈的芳香族 環吸收;寬的強烈O-H伸展中心係於3379.7 cm-1 ;寬的強烈 C-O伸展係於1230.4(肩部於ΙΠΙ.ΐχπΓ1。HPLC分析顯示39 個組份,且4主要組份包含18.7、7.9、6.5及5.8面積%,及 6.5面積%之殘餘未反應之酚,其於產品加工期間未被移除。 實施例2 -具有飽和環戊烷環之二環戊二烯二酚之環氧化 一 1公升之三頸玻璃圓底反應器被注以實施例丨之具有 飽和環戊烷環之二環戊二烯二酚(33_44克,0.20羥基當量, 以一 167.22公稱羥基當量為基準)及表氣醇(138 86克,丨5〇 莫耳)。反應器另外裝設一冷凝器(維持於〇。匸)、一溫度計、 一 Claisen轉接器、一塔頂氮氣入口(使用i公升/分鐘之n2), 及一攪拌器總成(Teflon™槳、玻璃軸、變速馬達)。溶於去 離子水(28.8克)中形成一氫氧化鈉水溶液之氫氧化鈉(7.2 克’ 0·18莫耳)添加至-側臂排氣式添加漏斗。開始反應器 内之淤漿攪拌,且使用一恆溫控制加熱包加熱。一旦攪拌 溶液於溫度達30。(:時形成時,添加異丙醇(74 77克,使用 35重量%之表氣醇),且持續攪拌及加熱。一旦達4〇 〇(:, 去離子水(12_08克,使用8重量%之表氣醇)藉由快速滴液添 加而添加至溶液。-旦達到50 %,開始滴液式添加氫氧化 納水✓谷液,造成反應器内之溶液開始變暗號拍色。於% 持續滴液式添加氫氧化鈉水溶液使暗琥#色溶液些微變混 35 201202284 濁。氫氧化納水溶液之添加於30分 在童 23分鐘後反應之後,停止㈣,域應器内容物添加 至—分液漏斗,並且沈降。環氧化反應之發展係藉由先前 抓时之高壓液相層析(HPLC)分析監測。於7分鐘沈降時間結 束時’水㈣被移除,以廢棄物棄置,且有機層被回收且 添加回反應㈣。重新_溶液之加熱及_以於5分鐘内 重新建立50。〇:之溫度。開始·式添加溶於去離子水(12 8 克)中之第二部份之氫氧化鈉(3.2克,〇·〇8莫耳),且於騎 鐘完成’同時將溫度維持於5〇〇c。 23分鐘後反應之後,停止攪拌,反應器内容物於一分 液漏斗内沈降5分鐘,水性層自產物移除,且些微混濁之 淡板色有機層添加回反應器内。一樣品被移除以供分 析。然後,重新加熱及授拌於7分鐘後重新建立5〇。匸之溫 度。溶於去離子水(4.0克)中之第三部份之氫氧化鈉(1〇克, 0.025莫耳)於10分鐘期間添加,且使用用於第二氫氧化鈉水 溶液之方法處理。 23分鐘後反應之後,其後自最終氫氧化鈉水溶液添加 移除水性層,有機層以一部份(15〇毫升)之去離子水清洗。 回收之有機層以曱基異丁基酮(0.5公升)稀釋,且以第二部 伤(150毫升)之去離子水清洗。水性層與約2〇克之乳化液一 起於經由於2300 RPM離心處理30分鐘溶解後移除。以去離 子水之第三及第四清洗(每一清洗係150毫升)使用用於第二 清洗之方法完成(離心處理再次需要以溶解來自每一清洗 之小$殘餘乳化液)。回收之有機溶液於填充於一600毫升 36 201202284 之中等燒結玻璃漏斗内之矽藻土床過濾,且需要時使用甲 基異丁基酮將產物自過濾床清洗至濾液内。使用75〇Ci 最大油浴溫度將有機層旋轉式蒸發至9 3 mm之Hg真空移除 大量之揮發物。於175。(:之最大油浴溫度進一步旋轉式蒸 發至0.17 mm之Hg真空,於冷卻至23 °C時產生36.11克之淡 黃色固體。 氣相層析(GC)分析[Hewlett Packard 5890系列η之氣相 層析儀,使用一 60m X 0.248mm X 0.25μιη之J&amp;W GC管柱,Sigma-Aldrich 0 Shixiazao, available from Celite® 545 from Celite Corporation. Example 1 - Preparation of dicyclopentadiene diphenol having a saturated cyclopentane ring A. Preparation of dicyclopentadiene monoaldehyde having a saturated cyclopentane ring. Preparation of slightly warm dicyclopentadiene (14 〇) Rh(CO)2 Acetylpyruvate vinegar (70. 2 mg (mg); 0.272 mmol (mmol)) and n-butyldiphenylphosphine (0.33 g (g)) The 1.36 millimolar reaction mixture was prepared in a rinse tank under dry nitrogen and then placed in a 250 mL (mL) Parr reactor at 1:1 syngas at 20 °C (1: 1 molar ratio of CO: H2) is sprayed three times. The reaction mixture was then heated to 10 ° C under a syngas pressure of 90 psi and stirred for 1 day, then at 130 ° C under a pressure of 90 psi for 6 days and stirred. Product formation from the reaction mixture was monitored by gas chromatography (GC) using an Agilent 6890 Gas Chromatography System. The final GC analysis of the resulting mixture showed a dicyclopentadiene monoaldehyde with a saturated cyclopentane ring. 65.5 area% » The reactor was cooled, the mixture was recovered, and the crude product (177.8 g) was used under vacuum to purify 78.2 g of dicyclopentadiene with a saturated cyclopentane ring using a 10 cm Vigreux distillation tower. An aldehyde having a boiling point of 65-68 ° C at 0.17 mm Hg. Gas chromatography/mass spectrometry (GC/MS) analysis of transparent liquid distillation products using an Agilent 6890 GC with one of the Agilent 5973 mass selective detectors supports the desired dicyclopentadiene monoaldehyde with a saturated cyclopentane ring. Form: M+ = 164, 146, 136, 107, 95, 79, 67. B. Preparation of 3_巯-1-propanesulfonic acid catalyst 3-Silphafur-1-ry acid, sodium salt (10.75 g) was added to concentrated hydrogen acid (35.7 % water, 32 201202284 200 ml), which was Magnetic stirring in the glass bottle. After covering with a parafllm "M" (American National Can, Greenwich, CT) sheet to avoid ingesting the moisture in the atmosphere, the white crystal slurry formed was stirred for 5 minutes, and then filtered through a medium-sintered glass funnel. Rotary evaporation gave 8.88 g of a pale yellow viscous solid product which was used as a catalyst without further work. C. Phenolization reaction Dicyclopentadiene monoaldehyde (43.31 g, 0.2845 mol, uncorrected) with saturated cyclopentane ring and molten phenol (850.2 g, 9.0345 mol) added to _5 liter glass three neck Round bottom reactor. The reactor is additionally provided with an ambient temperature (22. 〇 condenser and a thermometer, both of which are fixed to the reactor via a claisen adapter, plus a top nitrogen inlet, a glass stirring shaft, which has A Teflon (EIduPont de Nemours) mixing blade that is coupled to a variable speed motor to provide mechanical agitation and a thermostatically controlled heating pack. Start the top nitrogen flow (〇·5 liters/min), then heat and then stir At a temperature of 64 ° C, a clear solution was detected. At this point, a portion of the 3-indol propane-1 sulfonic acid was added (the total catalyst used was 22 g, which is equivalent to having a saturated cyclopentane). The dicyclopentadiene monoaldehyde of the alkane ring was 0.05 mol. / 〇) to the stirred solution. The starting portion of the catalyst (0.42 g) induced a maximum exotherm of 70 ° C in 2 minutes, and the solution became golden amber. The heating pack was removed from the reactor and joined to the air leak to cool the reaction section to 65. 0. Add the second part of the catalyst (〇_31 g) and stop cooling and reposition the heating pack back to the reactor. The first part of the catalyst did not induce an exotherm and was added after the addition. The clock was found to be 64 °C; © electricity, + &lt; _ degrees. At this time, 'the other part of the catalyst was added during the next η minutes' while maintaining the temperature of the amber (five) solution at 63 65 °C. Reverse 33 201202284 The temperature should be maintained at 65 °C for the next 72 hours, during which the 'reaction process was visualized by HPLC analysis. A Hewlett Packard 1090 liquid chromatograph was equipped with an Eclipse® (Agilent) XDB-C8 analytical protective tube ( 5 μ, 4.6 X 12.5 mm) One of the Zorbax Eclipse® (Agilent) XDB-C8 analytical tubes (5 μ, 4.6 x 150 mm). These columns are maintained in a 40 ° C chromatography furnace. And water (0.05% aqueous o-phosphoric acid) as an eluent, and individually delivered by a pump at a rate of 1.000 ml/min with a 50/50% solution, and changed to one after 5 minutes. 90/10% solution, and maintained for 15 minutes thereafter. The acetonitrile-based HPLC grade, 100.0% purity (by gas chromatography) has a UV cutoff of 189 NM. Upper system 85 ° / purity (actual analysis 85.1 water system HPLC grade used. Used for sample analysis The diode array detector was set to 225 nm and the reference frame was set to 550 nm. After 2.4 hours of reaction, HPLC analysis showed complete conversion of dicyclopentadiene monoacid to a product distribution, and thereafter little change in the product system. At the end of the time, the reactor contents were diluted with deionized (DI) water to fill a 5 liter reactor to 95% of capacity. The mixing was stopped after 1 hour and the contents of the reactor settled overnight. The next day, the aqueous layer was aspirated from the reactor and disposed of as waste. The reactor was refilled with new deionized water and the search was started for 65 minutes. Stirring was stopped and the contents of the reactor settled overnight. After a while, the aqueous layer is aspirated from the reactor and disposed of as waste. The cleaning procedure was repeated twice more, after which the solid was collected from the reactor by decantation through a filter paper. The recovered solid was thus added to a ceramic dish and dried in a vacuum oven 34 201202284 for 1 hour, removed, ground to a fine powder, and additionally dried in a vacuum oven for 48 hours to provide 84.32 grams of lavender. powder. The FTIR analysis of KBr pellets showed that the extension of the radicals disappeared completely, and strong aromatic ring absorption occurred at 1609.6 (shoulders at 1595.8) and 1509.8 cm-1; the broad strong OH stretching center was at 3379.7 cm-1; The broad strong CO stretch is at 1230.4 (shoulders are ΙΠΙ.ΐχπΓ1. HPLC analysis shows 39 components, and 4 major components contain 18.7, 7.9, 6.5, and 5.8 area%, and 6.5 area% of residual unreacted phenol , which was not removed during processing of the product. Example 2 - Epoxidation of a 1 liter three-neck glass round bottom reactor with dicyclopentadiene diphenol having a saturated cyclopentane ring is an example Dicyclopentadiene diphenol (33-44 g, 0.20 hydroxyl equivalent, based on a 167.22 nominal hydroxyl equivalent) and surface gas alcohol (138 86 g, 丨5 〇 Mo) with a saturated cyclopentane ring. Install a condenser (maintained in 〇.匸), a thermometer, a Claisen adapter, a nitrogen inlet at the top of the tower (using n2 liters per minute), and a stirrer assembly (TeflonTM paddle, glass shaft) , variable speed motor). Dissolved in deionized water (28.8 grams) to form a hydrogen Sodium hydroxide in aqueous sodium solution (7.2 g '0·18 mol) was added to the - side arm vented addition funnel. The slurry in the reactor was started to be stirred and heated using a thermostatically controlled heating pack. Once the solution was stirred, The temperature is up to 30. (: When forming, isopropanol (74 77 g, using 35 wt% of surface gas alcohol) is added, and stirring and heating are continued. Once it reaches 4 〇〇 (:, deionized water (12_08 g, Adding 8% by weight of epigas alcohol) to the solution by rapid drop addition. Once it reaches 50%, it starts to add liquid sodium hydroxide to the solution, which causes the solution in the reactor to start darkening. Add % sodium hydroxide solution in a continuous drip-type solution to make the dark amber solution slightly mixed 35 201202284 turbid. Add the sodium hydroxide aqueous solution to 30 minutes after the reaction in 23 minutes, stop (4), the contents of the domain Add to the separatory funnel and settling. The development of the epoxidation reaction was monitored by high pressure liquid chromatography (HPLC) analysis of the previous capture. At the end of the 7 minute settling time, the water (4) was removed to waste. Dispose of, and the organic layer is recycled and added Reaction (4). Reheat the solution and re-establish 50 in 5 minutes. 〇: Temperature. Start with the addition of the second part of sodium hydroxide dissolved in deionized water (12 8 grams) (3.2克, 〇·〇8mol), and finished at the rider' while maintaining the temperature at 5〇〇c. After 23 minutes, the reaction was stopped and the reactor contents were allowed to settle in a separatory funnel for 5 minutes. The layers were removed from the product and some slightly turbid light-colored organic layer was added back to the reactor. A sample was removed for analysis. Then, reheating and batching were repeated 5 minutes after 7 minutes. The temperature of 匸. A third portion of sodium hydroxide (1 g, 0.025 mol) dissolved in deionized water (4.0 g) was added over a period of 10 minutes and treated using a solution for the second aqueous sodium hydroxide solution. After the reaction after 23 minutes, the aqueous layer was removed from the final aqueous sodium hydroxide solution, and the organic layer was washed with a portion (15 mL) of deionized water. The recovered organic layer was diluted with decyl isobutyl ketone (0.5 liter) and washed with a second wound (150 ml) of deionized water. The aqueous layer was removed by dissolution with about 2 gram of emulsion after centrifugation at 2300 RPM for 30 minutes. The third and fourth washes with deionized water (150 ml per wash line) were completed using the second wash method (centrifugation was again required to dissolve the small residual emulsion from each wash). The recovered organic solution was filtered through a bed of diatomaceous earth in a sintered glass funnel filled in a 600 ml 36 201202284, and the product was washed from the filter bed into the filtrate using methyl isobutyl ketone if necessary. The organic layer was rotary evaporated to a Hg vacuum of 93 mm using a 75 〇Ci maximum oil bath temperature to remove a large amount of volatiles. At 175. (: The maximum oil bath temperature was further rotary evaporated to a Hg vacuum of 0.17 mm, yielding 36.11 g of a pale yellow solid upon cooling to 23 ° C. Gas chromatography (GC) analysis [Hewlett Packard 5890 series η gas phase layer The analyzer uses a 60m X 0.248mm X 0.25μιη J&amp;W GC column.

具有DB-1靜止相,火焰離子化檢測器係於3〇〇(&gt;c操作,3〇〇〇c 之注射器溫度,經此管柱之氦氣流係維持於丨丨毫升/分鐘, 起始50。(:之爐溫度’且12〇C/分鐘之加熱至3〇〇ΰ(:之最終溫度] 顯示包含殘餘表乳醇之基本上所有輕沸騰組份已被移除。 HPLC分析顯示具有飽和環戊烷環之二環戊二烯二酚完全 轉化成產物。一對產物等分物之滴定證明平均17 57 %之環 氧化物(244_9環氧化物當量)。環氧樹脂之滴定係由Jay,R R 於“Direct Titration of Epoxy Compounds and Aziridines,,,With a DB-1 stationary phase, the flame ionization detector is at 3 〇〇 (&gt;c operation, 3 〇〇〇c syringe temperature, and the enthalpy flow through the column is maintained at 丨丨 cc / min, starting 50. (: Furnace temperature' and heating to 3 〇〇ΰ at 12 〇C/min (: final temperature) shows that substantially all of the light boiling components containing residual galactitol have been removed. HPLC analysis shows The dicyclopentadiene diphenol of the saturated cyclopentane ring was completely converted into the product. Titration of a pair of product aliquots confirmed an average of 17 57 % of the epoxide (244_9 epoxide equivalent). The titration of the epoxy resin was determined by Jay, RR in "Direct Titration of Epoxy Compounds and Aziridines,,,

Analytical Chemistry,36, 3, 667-668 (March,1964)中描 述。簡言之,於採用此方法,經稱重之樣品(樣品重量範圍 係0.1 -0.2克’使用具3個小數位數準確性之秤)溶於二氯甲 烷(15毫升),其後添加於乙酸内之四乙基溴化銨溶液(丨万毫 升)。以3滴之結晶紫溶液((U %w/v,於乙酸中)處理之形成 溶液於一 Metrohm 665 Dosimat 滴定計(Brinkmann)以於乙 酸中之0.1N過氯酸滴定。由二氣甲烷〇5mL)及於乙酸内之 四乙基溴化銨溶液(15毫升)組成之一空白組之滴定提供溶 37 201202284 劑背影之校正。 實施例3-使用4,4,-二胺基二苯基曱烷熱誘發具有飽和環戊 烷環之二環戊二烯二縮水甘油基醚之固化 實施例2之具有飽和環戊烷環之二環戊二烯二縮水甘 油基醚(0.1220克,0.000498環氧化物當量)及4,4,-二胺基二 苯基曱烷(0.0247克,0.000498-NH當量)稱重於一玻璃瓶 内’且一起充份研磨成一均質細微粉末。部份(8.50及9.20 毫克)之摻合物之差式掃瞄量熱術(2910 Modulated DSC,TA Instruments)分析係於以35立方公分/分鐘流動之II氣流 下,使用7 °C/分鐘之加熱速率從25 °C至400 °C而完成。使 用前述條件之第二掃瞄產生220.6 °C之平均玻璃轉移溫 度。使用前述條件之第三掃瞄產生221.7 °C之平均玻璃轉移 溫度。DSC分析之產物係一透明琥珀色之剛性固體。 實施例4 -使用二氰二胺熱誘發具有飽和環戊烷環之二環 戊二烯二縮水甘油基醚之固化 實施例2之具有飽和環戊烷環之二環戊二烯二縮水甘 油基醚(0.4010克,0.00164環氧化物當量)及粉末狀(未加速) 之二氰二胺(0.0160克,4重量%之具有飽和環戊院環之一故 戊二烯二縮水甘油基醚)稱重於一玻璃瓶内’且一起充份研 磨成一均質細微粉末。部份(7.90及8.30毫克)之摻合物之 DSC分析係於以35立方公分/分鐘流動之氮氣流下,使用7 0C/分鐘之加熱速率從25 °C至350。(:而完成。觀察到平均 176 7 〇c開始,209.3。(:最小,264.2。(:端點’及 175.1 焦耳/ 克的焓之吸熱。觀察到平均281·5 °C開始,313·8 °C最大, 38 201202284 及348.3。(:端點且伴隨28.7焦耳/克的熵之放熱。使用前述條 件之第三掃瞄產生208.1。(:之平均玻璃轉移溫度。DSC分析 之產物係一透明琥珀色之剛性固體。 貫施例5 -使用具有飽和環戊烧環之二環戊二稀二齡及催化 劑熱誘發具有飽和環戊炫環之二環戊二烯二縮水甘油基醚 之固化 實施例2之具有飽和環戊烷環之二環戊二烯二縮水甘 油基醚(0.2077克,0.00085環氧化物當量),實施例丨之具有 飽和環戊烧環之一環戊二烯二齡(〇 1418克,0.00085經基當 里)’及笨曱基二乙基氣化錢(0.0037克,0.000016莫耳)於一 乾燥氮氣套箱内稱重至一玻璃瓶内,其後添加未經抑制之 無水四氫呋喃(2毫升)。實施例丨之具有飽和環戊烷環之二環 戊二烯二酚於175。(:之真空爐内另外乾燥移除殘餘之酚後 使用。形成之溶液於套箱内於環境溫度除去揮發成份,其 後於室溫(22 °C)之真空爐内乾燥2小時。部份(8 5〇及9 1〇毫 克)之摻合物之DSC分析(2910 Modulated DSC,TA Instruments)係於以35立方公分/分鐘流動之氮氣流下,使用 7 °C/分鐘之加熱速率從25义至4⑽。c而完成。使用前述條 件之第二掃瞄產生23丨2 %之平均玻璃轉移溫度。DSC分析 之產物係透明琥珀色之剛性固體。 實施例6 —複製使用具有飽和環戊烷環之二環戊二烯二酚 及催化劑熱誘發具有飽和環戊烷環之二環戊二烯二縮水甘 油基之固化 於175 C之真空爐内另外乾燥後之實施例1之具有飽和 39 201202284 環戊烷環之二環戊二烯二酚(0.1418克,0.00085公稱羥基當 量)被作為實施例2之具有飽和環戊烷環之二環戊二烯二酚 (0.2077克,0.00085環氧化物當量)之相對應環氧樹脂之固化 劑。二組份稱重於一玻璃瓶内,然後,轉移至乾燥氮氣之 套箱内。苯曱基三乙基氣化銨(0.0037克,0.000016莫耳)添 加至玻璃瓶,其後係無水四氫呋喃P毫升)。攪拌提供一溶 液,其被倒至一铭碟内,且四氫σ夫喃於套箱内蒸發掉。自 套箱移除且於真空爐内於環境條件下乾燥2小時後,一部份 (8.50毫克)之摻合物之DSC分析係於以35立方公分/分鐘流 動之氮氣流下,使用7 °C/分鐘之加熱速率從25 °C至400 °C 而完成。第二掃瞄係使用前述條件完成,造成229.7 °C之玻 璃轉移溫度。DSC分析之產物係透明琥珀色之剛性固體。 【圆式簡單說明】 (無) 【主要元件符號說明】 (無) 40Described in Analytical Chemistry, 36, 3, 667-668 (March, 1964). Briefly, in this method, the weighed sample (sample weight range 0.1 - 0.2 g 'using a scale with 3 decimal digits accuracy) is dissolved in dichloromethane (15 ml), which is then added to A solution of tetraethylammonium bromide in acetic acid (manual milliliters). The solution formed by treatment of 3 drops of crystal violet solution ((U %w/v in acetic acid) was titrated with 0.1 N perchloric acid in acetic acid in a Metrohm 665 Dosimat titrator (Brinkmann). The titration of a blank group consisting of 5 mL) and tetraethylammonium bromide solution (15 ml) in acetic acid provides correction for the dissolution of the solution of 201202284. Example 3 - Thermal Induction of Dicyclopentadiene Diglycidyl Ether with Saturated Cyclopentane Ring Using 4,4,-Diaminodiphenylnonane The cured cyclopentane ring of Example 2 was cured. Dicyclopentadiene diglycidyl ether (0.1220 g, 0.000498 epoxide equivalent) and 4,4,-diaminodiphenyl decane (0.0247 g, 0.000498-NH equivalent) weighed in a glass jar 'And fully grind together into a homogeneous fine powder. Partial (8.50 and 9.20 mg) blends of differential scanning calorimetry (2910 Modulated DSC, TA Instruments) were analyzed at a flow rate of 35 cubic centimeters per minute of II flow using 7 °C/min. The heating rate is completed from 25 °C to 400 °C. A second scan using the foregoing conditions produces an average glass transition temperature of 220.6 °C. A third scan using the foregoing conditions yielded an average glass transition temperature of 221.7 °C. The product of the DSC analysis was a clear amber rigid solid. Example 4 - Thermal induction of dicyclopentadiene diglycidyl ether having a saturated cyclopentane ring using dicyandiamide to cure dicyclopentadiene diglycidyl group having a saturated cyclopentane ring of Example 2. Ether (0.4010 g, 0.00164 epoxide equivalent) and powdered (unaccelerated) dicyandiamide (0.0160 g, 4% by weight of a pentadiene diglycidyl ether with a saturated cyclopentane ring) It is heavier than a glass bottle' and is thoroughly ground together into a homogeneous fine powder. The DSC analysis of the blend of the fractions (7.90 and 8.30 mg) was carried out under a stream of nitrogen flowing at 35 cubic centimeters per minute using a heating rate of 70 °C/min from 25 °C to 350 °C. (: Completed. Observed an average of 176 7 〇c starting, 209.3. (: minimum, 264.2. (: endpoint ' and 175.1 joules / gram of sputum endotherm. Observed an average of 281·5 °C, 313·8 °C max, 38 201202284 and 348.3. (: endpoint with an exotherm of 28.7 joules per gram of entropy. The third scan using the above conditions yields 208.1. (: average glass transition temperature. The product of DSC analysis is transparent Solid amber solid. Example 5 - Curing of a dicyclopentadiene diglycidyl ether with a saturated cyclopentane ring using a second ring of pentylene pentoxide with a saturated cyclopentane ring and a catalyst Example 2 is a dicyclopentadiene diglycidyl ether having a saturated cyclopentane ring (0.2077 g, 0.00085 epoxide equivalent), and the second embodiment of a cyclopentadiene having a saturated cyclopentane ring (实施) 1418 g, 0.00085 via base )) and a clumpy hydrazine diethylated gas (0.0037 g, 0.000016 mol) were weighed into a glass vial in a dry nitrogen box and then added unrepressed Anhydrous tetrahydrofuran (2 ml). Example with saturated cyclopentane The dicyclopentadiene diphenol is used in a vacuum furnace at 175. After drying to remove residual phenol, the formed solution is used to remove volatile components in the box at ambient temperature, and then at room temperature (22 ° C). Drying in a vacuum oven for 2 hours. DSC analysis (2910 Modulated DSC, TA Instruments) of a blend of some (85 〇 and 9.1 mg) was carried out under a nitrogen flow of 35 cubic centimeters per minute. The heating rate of 7 ° C / min was completed from 25 to 4 (10) c. A second scan using the foregoing conditions yielded an average glass transition temperature of 23 丨 2 %. The product of the DSC analysis was a clear solid of amber color. Example 6 - Reproduction using a dicyclopentadiene diphenol having a saturated cyclopentane ring and a catalyst to thermally induce the curing of a dicyclopentadiene diglycidyl group having a saturated cyclopentane ring in a vacuum oven at 175 C for additional drying The dicyclopentadiene diphenol having a saturated 39 201202284 cyclopentane ring (0.1418 g, 0.00085 nominal hydroxyl equivalent) was used as the dicyclopentadiene having a saturated cyclopentane ring of Example 2. Phenol (0.2077 g, 0.00085 epoxide equivalent) Corresponding to the epoxy resin curing agent. The two components are weighed in a glass bottle, and then transferred to a dry nitrogen box. Phenylmercaptotriethylammonium hydride (0.0037 g, 0.000016 mol) is added. To the glass bottle, followed by anhydrous tetrahydrofuran (PmL). Stirring provides a solution which is poured into a dish and the tetrahydro-sulphur is evaporated in the box. It is removed from the box and placed in a vacuum oven. After drying for 2 hours under ambient conditions, a portion of the (8.50 mg) blend was subjected to DSC analysis under a stream of nitrogen flowing at 35 cm3/min using a heating rate of 7 °C/min from 25 °C. Finished at 400 °C. The second scan was done using the conditions described above, resulting in a glass transition temperature of 229.7 °C. The product of the DSC analysis was a clear amber rigid solid. [Circular Simple Description] (None) [Explanation of Main Component Symbols] (None) 40

Claims (1)

201202284 七、申請專利範圍: 1. 一種化學式I之聚環戊二烯化合物, (化學式I) (R)m201202284 VII. Patent application scope: 1. A polycyclopentadiene compound of formula I, (Formula I) (R)m 其中,每一X係一氫、一氰基基團、一乙烯基苯曱基 基團、一烯丙基基團、一丙烯酸酯基團,或化學式II 之一結構: (化學式II) /0\ R1HC-CR1- CH2- η具有從0至20之一平均值;每一 m獨立地具有0至3之一 數值;每一 R獨立地係一 il素、一腈基團、一硝基基團、 一烷基基團、一烷氧基基團、一烯基基團,或一烯氧 基基團,其中,該烷基基團、該烷氧基基團、該烯基 基團,及該烯氧基基團每一者獨立地含有1至6個碳原 子;每一R1獨立地係氫或一曱基基團,每一Q獨立地 41 201202284 係氫或含有1至6個碳原子之一烷基基團,且T係氫或 化學式III之一結構 (化學式III)Wherein each X is a hydrogen, a cyano group, a monovinylphenylenyl group, an allyl group, an acrylate group, or a structure of the formula II: (Chemical Formula II) /0 \ R1HC-CR1-CH2- η has an average value from 0 to 20; each m independently has a value from 0 to 3; each R is independently a il, a nitrile group, a nitro group a group, an alkyl group, a monoalkoxy group, a monoalkenyl group, or an alkenyloxy group, wherein the alkyl group, the alkoxy group, the alkenyl group, And the alkenyloxy group each independently contains from 1 to 6 carbon atoms; each R1 is independently hydrogen or a mercapto group, and each Q is independently 41 201202284 hydrogen or contains 1 to 6 carbons One of the atoms of an alkyl group, and the T-hydrogen or one of the chemical formula III (chemical formula III) 附帶條件係當X係一氰基基團時,則R不是一烯基基團 或一稀氧基基團。 2. 如申請專利範圍第1項之聚環戊二烯化合物,其中,η 具有從0至8之一平均值。 3. 如申請專利範圍第1項之聚環戊二烯化合物,其中, 該烷基基團及該烷氧基基團含有1至2個碳原子。 4. 如申請專利範圍第1項之聚環戊二烯化合物,其中, 當Q係一烷基基團,其含有1至2個碳原子。 5. 如申請專利範圍第1項之聚環戊二烯化合物,其中, 該烯基基團及該烯氧基基團含有1至3個碳原子。 6. 如申請專利範圍第1項之聚環戊二烯化合物,其中,m 係0,η係0,且Q及T係氫。 7. 如申請專利範圍第1項之聚環戊二烯化合物,其中,m 係0,η係0,Q及T每一者係氫,且X係化學式II之一化合 物,其中,R1係Η。 8. —種可固化組成物,包含申請專利範圍第1項中界定之 化學式I之聚環戊二烯化合物。 42 201202284 9.如申請專利範圍第8項之可固化組成物,其中,該化學 式I之聚環戊二烯化合物係一硬化劑。 10.如申請專利範圍第8項之可固化組成物,其中,該化學 式I之聚環戊二烯化合物係一樹脂。 43 201202284 四、指定代表圖: (一) 本案指定代表圖為:第( )圖。(無) (二) 本代表圖之元件符號簡單說明: 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: (R)mThe proviso is that when the X is a cyano group, then R is not an alkenyl group or a diloxy group. 2. The polycyclopentadiene compound of claim 1, wherein η has an average value from 0 to 8. 3. The polycyclopentadiene compound according to claim 1, wherein the alkyl group and the alkoxy group have 1 to 2 carbon atoms. 4. The polycyclopentadiene compound according to claim 1, wherein Q is a monoalkyl group which has 1 to 2 carbon atoms. 5. The polycyclopentadiene compound according to claim 1, wherein the alkenyl group and the alkenyloxy group have 1 to 3 carbon atoms. 6. The polycyclopentadiene compound according to claim 1, wherein m is 0, η is 0, and Q and T are hydrogen. 7. The polycyclopentadiene compound according to claim 1, wherein m is 0, η is 0, Q and T are each hydrogen, and X is a compound of formula II, wherein R1 is Η . 8. A curable composition comprising the polycyclopentadiene compound of formula I as defined in claim 1 of the scope of the patent. The method of claim 8, wherein the polycyclopentadiene compound of the formula I is a hardener. 10. The curable composition of claim 8, wherein the polycyclopentadiene compound of the formula I is a resin. 43 201202284 IV. Designated representative map: (1) The representative representative map of this case is: ( ). (None) (2) A brief description of the symbol of the representative figure: 5. If there is a chemical formula in this case, please disclose the chemical formula that best shows the characteristics of the invention: (R)m
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US3298998A (en) * 1961-03-07 1967-01-17 Eastman Kodak Co Bisglycidyl ethers of bisphenols
US3251803A (en) * 1961-09-14 1966-05-17 Eastman Kodak Co Linear condensation polymers containing urethane and carbonate units
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US3419624A (en) 1964-02-24 1968-12-31 Union Carbide Corp Novel bisphenols of dicyclopentadiene
US4546129A (en) 1982-12-02 1985-10-08 The Dow Chemical Company Allylated di or polycyclopentadiene diphenols and thermosettable compositions containing same
US4623701A (en) 1985-07-10 1986-11-18 The Dow Chemical Company Multifunctional epoxy resins
US5463091A (en) 1989-01-17 1995-10-31 The Dow Chemical Company Diglycidyl ether of 4,4'-dihydroxy-α-methylstilbene
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