TWI705984B - (2,6-Dimethyl-1,4-phenylene ether) oligomers and cured products prepared therefrom - Google Patents

(2,6-Dimethyl-1,4-phenylene ether) oligomers and cured products prepared therefrom Download PDF

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TWI705984B
TWI705984B TW108100304A TW108100304A TWI705984B TW I705984 B TWI705984 B TW I705984B TW 108100304 A TW108100304 A TW 108100304A TW 108100304 A TW108100304 A TW 108100304A TW I705984 B TWI705984 B TW I705984B
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cured product
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epoxy resin
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TW202026330A (en
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林慶炫
鄭家凱
陳建翰
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國立中興大學
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Abstract

一種(2,6-二甲基-1,4-苯醚)寡聚物如式(I)所示。該寡聚物能使後續所製得的固化物同時具有較高玻璃轉移溫度(Tg )與熱穩定性、較低介電常數與介電損失及較高斷裂伸長率,且該寡聚物可用來與環氧樹脂進行共固化。A (2,6-dimethyl-1,4-phenylene ether) oligomer is represented by formula (I). The oligomer can make the subsequently prepared cured product have higher glass transition temperature (T g ) and thermal stability, lower dielectric constant and dielectric loss, and higher elongation at break, and the oligomer It can be used for co-curing with epoxy resin.

Description

(2,6-二甲基-1,4-苯醚)寡聚物及由其所製得的固化物(2,6-Dimethyl-1,4-phenylene ether) oligomers and cured products prepared therefrom

本發明是有關於一種(2,6-二甲基-1,4-苯醚)寡聚物及由其所製得的固化物,特別是指一種具有乙烯基苯酯末端的(2,6-二甲基-1,4-苯醚)寡聚物及由其所製得的固化物。The present invention relates to a (2,6-dimethyl-1,4-phenylene ether) oligomer and a cured product prepared therefrom, in particular to a (2,6 -Dimethyl-1,4-phenylene ether) oligomers and cured products prepared therefrom.

隨著半導體技術日益發展,半導體元件的尺寸也開始朝微米領域邁進。而目前單層導線已不敷使用,需往三度空間發展,所以必須建構多層金屬內連線,才能滿足目前的需求。在多層金屬內連線製程中,主要有兩個問題會影響其效能,其中一個問題為金屬導線與介電質層所引起的訊號傳遞延遲(RC delay),另一問題則為金屬導線配線間的訊號干擾(cross talk),其中訊號傳遞速度會與介電常數(dielectric constant;簡稱Dk )的平方根成反比,而介電損失(dissipation factor;簡稱Df )越低則越容易保持訊號的完整性,因此發展具有低介電常數與低介電損失的材料成為目前最重要的課題。With the increasing development of semiconductor technology, the size of semiconductor components has also begun to move towards the micron area. However, the current single-layer wires are no longer sufficient and need to be developed in three dimensions. Therefore, multilayer metal interconnections must be constructed to meet current needs. In the multilayer metal interconnection process, there are two main problems that affect its performance. One of the problems is the signal transmission delay (RC delay) caused by the metal wire and the dielectric layer, and the other is the metal wire wiring. Signal interference (cross talk) in which the signal transmission speed is inversely proportional to the square root of the dielectric constant (D k ), and the lower the dielectric loss (dissipation factor; D f ), the easier it is to maintain the signal Integrity, so the development of materials with low dielectric constant and low dielectric loss has become the most important topic at present.

美國通用電氣公司於1956年研發出一種熱塑性高分子聚(2,6-二甲基-1,4-苯醚)[poly(2,6-dimethyl-1,4-phenylene oxide;簡稱PPO)]。由於PPO結構剛硬,因而具有高玻璃轉移溫度(glass transition temperature;簡稱Tg )、低熱膨脹係數(coefficient of thermal expansion;簡稱CTE)及高拉伸強度等特性,此外,PPO還同時具有低介電常數及低介電損失的電氣特性,符合目前多層金屬內連線製程的需求。然而,PPO具有高分子量,因而具有相當高的黏性,導致溶解度不佳,應用範圍受到限制。US 6,995,195 B2則針對PPO進行改良,於實施例1( Example 1)揭示一種具有下式(A)結構的(2,6-二甲基-1,4-苯醚)寡聚物(商品名為OPE-2St),其中,式(A)的t1和t2分別為0至300的整數。 [式(A)]

Figure 02_image003
In 1956, General Electric Company developed a kind of thermoplastic polymer poly(2,6-dimethyl-1,4-phenylene oxide) [poly(2,6-dimethyl-1,4-phenylene oxide; PPO)] . Due to the rigid structure of PPO, it has the characteristics of high glass transition temperature (T g ), low coefficient of thermal expansion (CTE) and high tensile strength. In addition, PPO also has low dielectric strength. The electrical characteristics of the electrical constant and low dielectric loss meet the requirements of the current multilayer metal interconnection process. However, PPO has a high molecular weight, and therefore has a relatively high viscosity, resulting in poor solubility and limited application range. US 6,995,195 B2 is aimed at improving PPO. Example 1 (Example 1) discloses a (2,6-dimethyl-1,4-phenylene ether) oligomer (trade name) with the following formula (A) structure OPE-2St), where t1 and t2 of formula (A) are integers from 0 to 300, respectively. [Formula (A)]
Figure 02_image003

然而,若針對由OPE-2St進行自身固化所得到的OPE-2St固化物之熱性質、介電性質與機械性質進行測試後發現,其玻璃轉移溫度(Tg )與熱穩定性偏低、介電常數與介電損失皆偏高,且因雙鍵固化後所造成過脆的特性,導致OPE-2St固化物的斷裂伸長率也偏低。此外,若欲將寡聚物與環氧樹脂進行共固化,以改善所製得固化物過脆的特性時,由於OPE-2St上的雙鍵無法與環氧樹脂(epoxy resins)的環氧基反應,因而OPE-2St也無法拿來與環氧樹脂進行共固化。However, if the thermal, dielectric, and mechanical properties of the cured product of OPE-2St obtained by self-curing of OPE-2St are tested, it is found that the glass transition temperature (T g ) and thermal stability of the cured product are low. Both the electric constant and the dielectric loss are relatively high, and because of the excessively brittle characteristics after the double bond is cured, the elongation at break of the cured OPE-2St is also relatively low. In addition, if the oligomer and epoxy resin are to be co-cured to improve the brittleness of the cured product, the double bond on OPE-2St cannot be combined with the epoxy group of epoxy resins. Therefore, OPE-2St cannot be co-cured with epoxy resin.

因此,為了解決前述OPE-2St的各種缺點,如何找到一種能使後續所製得的固化物同時具有較高玻璃轉移溫度(Tg )與熱穩定性、較低介電常數與介電損失及較高斷裂伸長率,且能拿來與環氧樹脂進行共固化的寡聚物,已成為目前主要的研究方向。Therefore, in order to solve the various shortcomings of the aforementioned OPE-2St, how to find a cured product that can have higher glass transition temperature (T g ) and thermal stability, lower dielectric constant and dielectric loss, and Oligomers that have higher elongation at break and can be co-cured with epoxy resin have become the main research direction at present.

鑒於前述OPE-2St所具有的各種缺點,本案申請人首先從US 6,995,195 B2專利案所列舉多種可能的寡聚物結構中找出、甚至進一步改良出一種能使後續所製得的固化物同時具有較高玻璃轉移溫度(Tg )與熱穩定性、較低介電常數與介電損失及較高斷裂伸長率,且能拿來與環氧樹脂進行共固化的寡聚物。In view of the various shortcomings of the aforementioned OPE-2St, the applicant in this case first found out from the various possible oligomer structures listed in the US 6,995,195 B2 patent case, and even further improved a kind that can make the subsequent cured product also have Higher glass transition temperature (T g ) and thermal stability, lower dielectric constant and dielectric loss and higher elongation at break, and can be used as an oligomer co-cured with epoxy resin.

因此,本發明的第一目的,即在提供一種(2,6-二甲基-1,4-苯醚)寡聚物。Therefore, the first objective of the present invention is to provide a (2,6-dimethyl-1,4-phenylene ether) oligomer.

於是,本發明(2,6-二甲基-1,4-苯醚)寡聚物,如下式(I)所示: [式(I)]

Figure 02_image001
其中, X為
Figure 02_image005
Figure 02_image007
, Y為單鍵、 CH2 C(CH3 )2 C(CF3 )2 SO2 O C(O)
Figure 02_image009
, R1 與R2 分別為氫、C1 ~C6 烷基或苯基, m、n分別為0至50的整數, q為1至3的整數。Thus, the (2,6-dimethyl-1,4-phenylene ether) oligomer of the present invention is represented by the following formula (I): [Formula (I)]
Figure 02_image001
Where X is
Figure 02_image005
or
Figure 02_image007
, Y is a single bond, CH 2 , C(CH 3 ) 2 , C(CF 3 ) 2 , SO 2 , O , C(O) or
Figure 02_image009
, R 1 and R 2 are hydrogen, C 1 to C 6 alkyl or phenyl, m and n are integers from 0 to 50, and q is an integer from 1 to 3.

因此,本發明的第二目的,即在提供一種固化物。該固化物同時具有較高玻璃轉移溫度(Tg )與熱穩定性、較低介電常數與介電損失及較高斷裂伸長率。Therefore, the second object of the present invention is to provide a cured product. The cured product has both higher glass transition temperature (T g ) and thermal stability, lower dielectric constant and dielectric loss, and higher elongation at break.

於是,本發明固化物是由一樹脂組成物於過氧化物起始劑的存在下進行固化所製得,該樹脂組成物含有前述式(I)所示的(2,6-二甲基-1,4-苯醚)寡聚物。Therefore, the cured product of the present invention is prepared by curing a resin composition in the presence of a peroxide initiator, the resin composition containing the (2,6-dimethyl-) represented by the aforementioned formula (I) 1,4-phenylene ether) oligomers.

本發明的功效在於:由於本發明式(I)的(2,6-二甲基-1,4-苯醚)寡聚物末端具有乙烯基苯酯,因此後續所製得的固化物能同時具有較高玻璃轉移溫度(Tg )與熱穩定性、較低介電常數與介電損失及較高斷裂伸長率特性,且由於該末端的乙烯基苯酯為活性酯基,因而本發明式(I)的(2,6-二甲基-1,4-苯醚)寡聚物還能拿來與環氧樹脂進行共固化。The effect of the present invention is: because the (2,6-dimethyl-1,4-phenylene ether) oligomer of the formula (I) of the present invention has vinyl phenyl ester at the end, the subsequent cured product can be simultaneously It has the characteristics of higher glass transition temperature (T g ) and thermal stability, lower dielectric constant and dielectric loss, and higher elongation at break, and because the terminal vinyl phenyl ester is an active ester group, the formula of the present invention (I) (2,6-Dimethyl-1,4-phenylene ether) oligomers can also be used for co-curing with epoxy resin.

以下將就本發明內容進行詳細說明:The content of the present invention will be described in detail below:

[(2,6-[(2,6- 二甲基Dimethyl -1,4--1,4- 苯醚Phenyl ether )) 寡聚物Oligomer ]]

本發明(2,6-二甲基-1,4-苯醚)寡聚物,如上式(I)所示。The (2,6-dimethyl-1,4-phenylene ether) oligomer of the present invention is represented by the above formula (I).

較佳地,在式(I)中,X為

Figure 02_image011
Figure 02_image013
。Preferably, in formula (I), X is
Figure 02_image011
or
Figure 02_image013
.

較佳地,在式(I)中,Y為 C(CH3 )2 Preferably, in formula (I), Y is - C (CH 3) 2 - .

較佳地,在式(I)中,R1 為氫。Preferably, in formula (I), R 1 is hydrogen.

較佳地,在式(I)中,R2 為氫。Preferably, in formula (I), R 2 is hydrogen.

較佳地,在式(I)中,m為0至30的整數。Preferably, in formula (I), m is an integer of 0-30.

較佳地,在式(I)中,n為0至30的整數。Preferably, in formula (I), n is an integer of 0-30.

較佳地,在式(I)中,q為1或2。Preferably, in formula (I), q is 1 or 2.

[[ 寡聚物的製備方法Preparation method of oligomer ]]

本發明 (2,6-二甲基-1,4-苯醚)寡聚物是由下式(II)的化合物與酸進行酯化反應所製得。該酸為下式(III)或下式(IV)所示的化合物。 [式(II)]

Figure 02_image015
[式(III)]
Figure 02_image017
[式(IV)]
Figure 02_image019
其中, Y、m、n與q的定義分別同前所述。The (2,6-dimethyl-1,4-phenylene ether) oligomer of the present invention is prepared by the esterification reaction between a compound of the following formula (II) and an acid. The acid is a compound represented by the following formula (III) or the following formula (IV). [Formula (II)]
Figure 02_image015
[Formula (III)]
Figure 02_image017
[Formula (IV)]
Figure 02_image019
Among them, the definitions of Y, m, n and q are the same as those described above.

需說明的是,該酯化反應的條件可為現有任何能使醇和酸發生酯化反應的條件,該酯化反應例如但不限於是使式(II)的化合物與酸於溶劑、二環己基碳二亞胺(N,N'- dicyclohexylcarbodiimide;簡稱DCC)與4-二甲胺基吡啶(DMAP)的存在下進行酯化反應。該溶劑例如但不限於是二氯甲烷(dichloromethane;簡稱DCM)。It should be noted that the conditions of the esterification reaction can be any existing conditions that can cause the esterification reaction of alcohol and acid. The esterification reaction is, for example, but not limited to, the compound of formula (II) and acid in a solvent, dicyclohexyl Carbodiimide (N,N'-dicyclohexylcarbodiimide; DCC for short) is esterified in the presence of 4-dimethylaminopyridine (DMAP). The solvent is, for example, but not limited to, dichloromethane (DCM for short).

[[ 固化物Cured ]]

本發明固化物是由一樹脂組成物於過氧化物起始劑的存在下進行固化所製得,該樹脂組成物含有前述式(I)所示的(2,6-二甲基-1,4-苯醚)寡聚物。The cured product of the present invention is prepared by curing a resin composition in the presence of a peroxide initiator. The resin composition contains (2,6-dimethyl-1, 4-phenylene ether) oligomer.

該過氧化物起始劑為現有任何能引發該式(I)所示的(2,6-二甲基-1,4-苯醚)寡聚物進行聚合反應的過氧化物。該過氧化物起始劑例如但不限於是二叔丁基過氧化物(di-tert-butyl peroxide;DTBP)、過氧化苯甲醯(benzoyl peroxide;BPO)、過氧化叔丁醇(tert-butyl hydroperoxide;TBHP)、叔丁基過氧化異丙苯(tert-butyl cumyl peroxide;TBCP)或前述的組合。The peroxide initiator is any existing peroxide that can initiate the polymerization reaction of the (2,6-dimethyl-1,4-phenyl ether) oligomer represented by the formula (I). The peroxide initiator is, for example, but not limited to, di-tert-butyl peroxide (DTBP), benzoyl peroxide (BPO), tert-butyl peroxide (tert-butyl peroxide), butyl hydroperoxide; TBHP), tert-butyl cumyl peroxide (TBCP) or a combination of the foregoing.

較佳地,以該(2,6-二甲基-1,4-苯醚)寡聚物的重量為100 wt%計,該過氧化物起始劑的重量範圍為0.1~5 wt%。更佳地,該過氧化物起始劑的重量範圍為0.1~2 wt%。又更佳地,該過氧化物起始劑的重量範圍為0.5~1.5wt%。Preferably, based on the weight of the (2,6-dimethyl-1,4-phenylene ether) oligomer being 100 wt%, the weight range of the peroxide initiator is 0.1-5 wt%. More preferably, the weight range of the peroxide initiator is 0.1-2 wt%. More preferably, the weight range of the peroxide initiator is 0.5 to 1.5 wt%.

較佳地,該樹脂組成物還含有環氧樹脂,且該固化物是由該樹脂組成物於過氧化物起始劑與觸媒的存在下進行固化所製得。Preferably, the resin composition further contains epoxy resin, and the cured product is prepared by curing the resin composition in the presence of a peroxide initiator and a catalyst.

該環氧樹脂可為現有任何已知的環氧樹脂。該環氧樹脂例如但不限於是雙酚A型環氧樹脂(diglycidyl ether of bisphenol A)、酚醛環氧樹脂(phenol novolac epoxy)、甲基酚醛環氧樹脂(cresol novolac epoxy)、雙環戊二烯苯酚環氧樹脂(dicyclopentadiene-phenol epoxy)、含萘環氧樹脂(naphthalene-containing epoxy)或前述的組合。在本發明的具體實施例中該環氧樹脂為雙環戊二烯苯酚環氧樹脂。The epoxy resin can be any known epoxy resin. The epoxy resin is, for example, but not limited to, diglycidyl ether of bisphenol A, phenol novolac epoxy, cresol novolac epoxy, dicyclopentadiene Dicyclopentadiene-phenol epoxy, naphthalene-containing epoxy, or a combination of the foregoing. In the specific embodiment of the present invention, the epoxy resin is dicyclopentadiene phenol epoxy resin.

該觸媒可為現有任何能催化該式(I)所示的(2,6-二甲基-1,4-苯醚)寡聚物與環氧樹脂進行共固化的觸媒。該觸媒例如但不限於是4-二甲基胺基吡啶(4-dimethylaminopyridine;DMAP)、咪唑(imidazole)、2-甲基-4-甲基咪唑(2-ethyl-4- methylimidazole)、2-甲基咪唑(2-methylimidazole)、三苯基膦(triphenylphosphine)或前述的組合。The catalyst can be any existing catalyst that can catalyze the co-curing of the (2,6-dimethyl-1,4-phenylene ether) oligomer represented by the formula (I) and epoxy resin. The catalyst is, for example, but not limited to, 4-dimethylaminopyridine (DMAP), imidazole, 2-ethyl-4-methylimidazole, 2 -2-methylimidazole, triphenylphosphine or a combination of the foregoing.

較佳地,以該環氧樹脂的重量為100 wt%計,該觸媒的重量範圍為0.1~5 wt%。更佳地,該觸媒的重量範圍為0.1~2 wt%。又更佳地,該觸媒的重量範圍為0.1~1.5 wt%。Preferably, based on the weight of the epoxy resin being 100 wt%, the weight of the catalyst ranges from 0.1 to 5 wt%. More preferably, the weight of the catalyst ranges from 0.1 to 2 wt%. More preferably, the weight of the catalyst ranges from 0.1 to 1.5 wt%.

本發明將就以下實施例來作進一步說明,但應瞭解的是,該實施例僅為例示說明,而不應被解釋為本發明實施的限制。The present invention will be further described with reference to the following embodiments, but it should be understood that this embodiment is only illustrative and should not be construed as a limitation of the implementation of the present invention.

本實施方式中所提及實施例1~2與比較例1的寡聚物,以及應用例1~4與比較應用例1~2的固化物之製備方法分別於下列詳細說明。 實施例 1 OPE-E-2St( 寡聚物 ) 實施例1之OPE-E-2St的製備方法如下:[ 反應式 I]

Figure 02_image021
(m為0至30的整數;n為0至30的整數) 見反應式I,於一個100 mL的三頸反應器中,加入0.4 g (2.86 mmol)的苯乙烯酸(4-carboxystyrene)、0.57 g (2.86 mmole)的二環己基碳二亞胺(DCC)、0.15 g (0.65 mmol)的4-二甲胺基吡啶(DMAP)與10 mL的二氯甲烷(DCM)後,於氮氣環境下冷卻至0℃攪拌30分鐘。接著,先另取2 g (1.3 mmol)末端基為酚的(2,6-二甲基-1,4-苯醚)寡聚物(SA90)溶於10 mL的二氯甲烷中,並將該含有SA90的二氯甲烷溶液逐滴加入三頸反應器中並攪拌2小時,再移除冰浴,並於室溫下反應12小時。待反應結束後,以抽氣過濾方式移除大部分二環己基脲(N,N'-dicyclohexylurea;簡稱DCU),最後將濾液倒入甲醇中析出粗產物,並以甲醇清洗該粗產物後進行抽氣過濾,所得到的濾餅再於60℃下進行真空乾燥,即得到白色粉末產物(即實施例1的OPE-E-2St;產率約90 wt%)。實施例1之OPE-E-2St的核磁共振氫譜(1 H-NMR,見圖1)、傅里葉轉換紅外光譜(FTIR)及凝膠滲透層析(GPC)分析結果: 1 H-NMR (ppm, CDCl3 ) δ=1.69 (6H, H10 );2.08 (Ar-CH3 , H6 , H8 );5.40, 5.42 (2H, Hb );5.88, 5.91 (2H, Ha ); 6.46 (Ar-H, H7 , H9 );6.75, 6.77, 6.78, 6.80 (2H, H2 );6.95 (4H, H9 );7.51, 7.53 (4H, H3 );8.15, 8.17 (4H, H4 )。FTIR (KBr, cm-1 ) ν= 1730 (C=O);1607 (Ar-ring);1311, 1185 (C-O-C);988, 916 (=C-H)。GPC (NMP) Mn = 4268; Mw = 5799。 實施例 2 OPE-E-4St( 寡聚物 ) 實施例2之OPE-E-4St的製備方法包含下列步驟(1)至(3):[ 反應式 II]
Figure 02_image023
(1) 製備化合物 BS-Mba 見反應式II,在一個100 mL三頸反應器中,加入1 g (5.94 mmol)的3,5-二羥基苯甲酸甲酯(3,5-dihydroxybenzoic acid methyl ester)、2 g (13 mmol)的氯甲基苯乙烯[1-(chloromethyl)-4-ethenylbenzene]、1.8 g (13 mmol)的碳酸鉀(K2 CO3 )及10 mL的二甲基乙醯胺(dimethylacetamide;簡稱DMAc)後,於氮氣環境下升溫至85℃並進行反應12小時,待反應結束後,倒入甲醇水溶液(甲醇與水的重量比值為1)析出粗產物。接著,以甲醇水溶液(甲醇與水的重量比值為1)清洗該粗產物數次後,先將清洗後得到的黃色油狀粗產物溶於乙酸乙酯(ethyl acetate)中並以純水萃取三次,再取有機層以無水硫酸鎂除水,最後進行減壓濃縮除去乙酸乙酯後,得到黃色透明油狀產物(即化合物BS-Mba;產率約90 wt%)。化合物BS-Mba的1 H-NMR及FTIR分析結果: 1 H-NMR (ppm, DMSO-d6 ) δ=3.83 (3H, H15 );5.13 (4H, H9 );5.25, 5.27, 5.29 (2H, Hb );5.82, 5.84, 5.85, 5.87 (2H, Ha );6.73, 6.76 (2H, H2 );6.97 (1H, H10 );7.18, 7.20 (2H, H12 );7.42, 7.47 (8H, H4 , H5 )。FTIR (KBr, cm-1 ) ν= 1721 (C=O);1600 (Ar-ring);1165, 1058 (C-O-C);990, 910 (=C-H)。[ 反應式 III]
Figure 02_image025
(2) 製備化合物 BS-Acid 見反應式III,在一個100 mL三頸反應器中,加入1 g (2.49 mmol)的BS-Mba與10 mL乙醇後,於氮氣環境下升溫至80℃並攪拌1小時。另取0.35 g (6.2 mmol)氫氧化鉀(KOH)溶於10 mL乙醇中,逐滴加入三頸反應器中並於80℃下反應16小時,待反應結束後,以減壓濃縮方法除去乙醇。接著,先加入30 mL乙酸乙酯並依序以1N鹽酸萃取三次、鹽水萃取二次及純水萃取二次,再取有機層以無水硫酸鎂除水後,進行減壓濃縮除去乙酸乙酯,得到固體。最後,先使該固體溶於二氯甲烷,且逐滴加入正己烷至析出粗產物,並經攪拌過夜後進行抽氣過濾,再將所得到的濾餅於60℃下進行真空乾燥,得白色粉末狀產物(即化合物BS-Acid;產率約80 wt%)。化合物BS-Mba的1 H-NMR及FTIR分析結果: 1 H-NMR (ppm, DMSO-d6 ) δ=5.14 (4H, H9 );5.26, 5.28, 5.29 (2H, Hb );5.82, 5.84, 5.85, 5.87 (2H, Ha );6.71, 6.73, 6.76, 6.78 (2H, H2 );6.93 (1H, H10 );7.15, 7.17 (2H, H12 );7.42, 7.48 (8H, H4 , H5 );13.00 (1H, COOH)。FTIR (KBr, cm-1 ): ν=3200-2400 (COO-H);1692 (C=O);1595 (Ar-ring);1165, 1058 (C-O-C);990, 910 (=C-H)。[ 反應式 IV]
Figure 02_image027
(m為0至30的整數;n為0至30的整數)製備 OPE-E-4St 見反應式IV,在一個100 mL三頸反應器中,加入1.06 g (2.86 mmol)的BS-Acid、0.57 g (2.86 mmol)的二環己基碳二亞胺(DCC)、0.15 g (0.65 mmol)的4-二甲胺基吡啶及10 mL的二氯甲烷後,於氮氣環境下冷卻至0℃並攪拌30分鐘。另取2 g (1.3 mmol)的SA90溶於10 mL的二氯甲烷,並將該含有SA90的二氯甲烷溶液逐滴加入三頸反應器中並攪拌2小時,再於室溫下反應12小時,待反應結束後,以抽氣過濾方式移除大部分二環己基脲(DCU)。接著,先取濾液倒入甲醇/丙酮中析出粗產物,再以甲醇/丙酮清洗該粗產物後進行抽氣過濾,所得到的濾餅於60℃下進行真空乾燥,得到白色粉末產物(即實施例2的OPE-E-4St;產率約90 wt%)。實施例2之OPE-E-4St的1 H-NMR(見圖2)、FTIR及GPC分析結果: 1 H-NMR (ppm, CDCl3 ) δ =1.68 (6H, H13 );2.07 (Ar-CH3 , H9 , H11 );5.08 (8H, H5 );5.24, 5.25, 5.26, 5.27 (4H, Hb );5.73, 5.75, 5.76, 5.77(4H, Ha );6.46 (Ar-H, H10 , H12 );6.71 (4H, H2 );6.86 (2H, H6 );6.95 (4H, H12 );7.32-7.46 (H4 ,  H5 )。FTIR (KBr, cm-1 ) ν= 1738 (C=O);1607 (Ar-ring);1311, 1185(C-O-C);988, 916 (=C-H)。GPC (NMP) Mn = 4535, Mw = 6969。 比較例 1 OPE-4St( 寡聚物 ) 比較例1之OPE-4St的製備方法包含下列步驟(1)至(3):[ 反應式 V]
Figure 02_image029
(1) 製備化合物 BS-OH 見反應式V,在一個100 mL三頸反應器中,加入0.5 g (3.6 mmol)的二烴基苯甲醇、氯甲基苯乙烯1.2 g (7.92 mmol)、碳酸鉀1.09 g (7.92 mmol)及10毫升之DMAc後,於氮氣環境下升溫至85℃並反應12小時,待反應結束後,倒入甲醇水溶液(甲醇與水的重量比值為1)析出粗產物。接著,以甲醇水溶液(甲醇與水的重量比值為1)清洗該粗產物數次後,先將清洗後得到的黃色油狀粗產物溶於乙酸乙酯中並以純水萃取三次,再取有機層以無水硫酸鎂除水,最後進行減壓濃縮除去乙酸乙酯後,得到黃色透明油狀產物(即化合物BS-OH;產率約90 wt%)。化合物BS-OH的1 H-NMR及FTIR分析結果: 1 H-NMR (ppm, DMSO-d6 ) δ=4.46 (2H, H14 );5.07(4H, H9 );5.23 (OH);5.26, 5.28, 5.30 (2H, Hb );5.83, 5.84, 5.86, 5.87 (2H, Ha );6.56 (1H, H10 ); 6.63, 6.61 (2H, H12 );6.72-6.78 (2H, H2 );7.41, 7.48 (8H, H4 , H5 )。FTIR (KBr, cm-1 ) ν=3377 (OH);1600 (Ar-ring);1165, 1048 (C-O-C);990, 910 (=C-H)。[ 反應式 VI]
Figure 02_image031
(2) 製備化合物 BS-Cl 見反應式VI,在一個100 mL的三頸反應器中,加入1 g (2.68 mmol)的BS-OH及10 mL的二氯甲烷,於室溫下與氮氣環境中分批且逐滴加入0.76 g (6.44 mmol)氯化亞碸(SOCl2 )與數滴吡啶(pyridine)進行反應3小時。待反應結束後,緩慢滴入純水並以純水萃取三次,取有機層以無水硫酸鎂除水後,以減壓濃縮方式除去二氯甲烷,得黃色透明油狀產物(即化合物BS-Cl;產率約80 wt%)。化合物BS-Cl的1 H-NMR及FTIR分析結果: 1 H-NMR (ppm, DMSO-d6 ) δ=4.67 (2H, H14 );5.08 (4H, H9 );5.26, 5.28, 5.29 (2H, Hb );5.83, 5.84, 5.86, 5.87 (2H, Ha );6.66 (1H, H10 );6.73 (2H, H12 );6.74-6.78 (2H, H2 );7.42, 7.48 (8H, H4 , H5 )。FTIR (KBr, cm-1 ) ν= 1600 (Ar-ring);1257 (CH2 -Cl); 1165, 1048 (C-O-C);990, 910 (=C-H)。[ 反應式 VII]
Figure 02_image033
(m為0至30的整數;n為0至30的整數)製備 OPE-4St 見反應式VII,在一個100 mL的三頸反應器中,加入1 g (0.62 mmol)的SA90、0.58 g (1.5 mmol)的BS-Cl、0.2 g (1.5 mmol)的碳酸鉀(K2 CO3 )及15 mL的DMAc後,於氮氣環境下升溫至100℃並進行反應24小時。待反應結束後,滴入甲醇析出粗產物,並以甲醇/丙酮混合液清洗數次,最後進行抽氣過濾後,將所得到的濾餅於60℃進行真空乾燥,得到白色粉末狀產物(即比較例1的OPE-4St;產率約85 wt%)。比較例1之OPE-4St的1 H-NMR、FTIR及GPC分析結果: 1 H-NMR (ppm, CDCl3 ) δ=1.69 (6H, H13 );2.08 (Ar-CH3 , H9 , H11 );4.68 (4H, H8 );5.03 (8H, H5 );5.23, 5.24, 5.26, 5.27 (4H, Hb );5.73, 5.74, 5.76, 5.77 (4H, Ha );6.46 (Ar-H, H10 , H12 );6.57 (2H, H6 );6.71 (4H, H7 );6.74 (4H, H2 );6.95 (4H, H12 );7.29-7.45 (16H, H4 , H5 )。FTIR (KBr, cm-1 ) ν=1605 (Ar-ring);1311, 1185 (C-O-C);990, 910 (=C-H)。GPC (NMP) Mn = 5041;Mw = 6818。 應用例 1 OPE-E-2St 的自身交聯固化物 應用例1之OPE-E-2St的自身交聯固化物製備方法如下: 先將0.5 g實施例1的OPE-E-2St與5 mg [1 wt%(以OPE-E-2St的重量為100 wt%計)]的二叔丁基過氧化物(過氧化物起始劑)加入4.5 mL(使固含量為10 wt%)的DMAc中並攪拌2小時,再以0.44 µm的針頭過濾器進行過濾後,倒入鋁盤,使其於氮氣環境下進行升溫固化,得到該OPE-E-2St的自身交聯固化物。其中,升溫固化的條件如下:80℃ (12小時)、120℃ (2小時)、180℃ (2小時)、200℃ (2小時)、220℃ (2小時)。 應用例 2 OPE-E-4St 的自身交聯固化物 應用例2之OPE-E-4St的自身交聯固化物製備方法如下: 先將0.5 g實施例2的OPE-E-4St與5 mg [1 wt%(以OPE-E-4St的重量為100 wt%計)]的二叔丁基過氧化物(過氧化物起始劑)加入4.5 mL(使固含量為10 wt%)的DMAc中並攪拌2小時,再以0.44 µm的針頭過濾器進行過濾後,倒入鋁盤,使其於氮氣環境下進行升溫固化,得到該OPE-E-4St的自身交聯固化物。其中,升溫固化的條件如下:80℃ (12小時)、120℃ (2小時)、180℃ (2小時)、200℃ (2小時)、220℃ (2小時)。 應用例 3 OPE-E-2St 與環氧樹脂共固化的固化物 應用例3之OPE-E-2St與環氧樹脂共固化的固化物製備方法如下: 先將1 g (1 mmol)實施例1的OPE-E-2St、0.28 g (1 mmol)的環氧樹脂(商品名:HP7200)、0.01 g [1 wt%(以OPE-E-2St的重量為100 wt%計)]的二叔丁基過氧化物(過氧化物起始劑)、1.4 mg [0.5 wt%(以環氧樹脂的重量為100 wt%計)]的DMAP(觸媒)加入11.4 mL(使固含量為10 wt%)的DMAc中並攪拌2小時,再以0.44 µm的針頭過濾器進行過濾後,倒入鋁盤,使其於氮氣環境下進行升溫固化,得到該OPE-E-2St與環氧樹脂共固化的固化物。其中,升溫固化的條件如下:80℃ (12小時)、120℃ (2小時)、180℃ (2小時)、200℃ (2小時)、220℃ (2小時)。 應用例 4 OPE-E-4St 與環氧樹脂共固化的固化物 應用例4之OPE-E-4St與環氧樹脂共固化的固化物製備方法如下: 先將1 g (0.86 mmol)實施例2的OPE-E-4St、0.22 g (0.86 mmol)的環氧樹脂(商品名:HP7200)、0.01 g [1 wt%(以OPE-E-4St的重量為100 wt%計)]的二叔丁基過氧化物(過氧化物起始劑)、1.1 mg [0.5 wt%(以環氧樹脂的重量為100 wt%計)]的DMAP(觸媒)加入11 mL(使固含量為10 wt%)的DMAc中並攪拌2小時,再以0.44 µm的針頭過濾器進行過濾後,倒入鋁盤,使其於氮氣環境下進行升溫固化,得到該OPE-E-4St與環氧樹脂共固化的固化物。其中,升溫固化的條件如下:80℃ (12小時)、120℃ (2小時)、180℃ (2小時)、200℃ (2小時)、220℃ (2小時)。 比較應用例 1 OPE-2St 的自身交聯固化物 比較應用例1之OPE-2St的自身交聯固化物製備方法如下: 先將0.5 g的OPE-2St(廠商:Mitsubishi Gas Chemical Company, Inc.)與5 mg [1 wt%(以OPE-2St的重量為100 wt%計)]的二叔丁基過氧化物(過氧化物起始劑)加入4.5 mL(使固含量為10 wt%)的DMAc中並攪拌2小時,再以0.44 µm的針頭過濾器進行過濾後,倒入鋁盤,使其於氮氣環境下進行升溫固化,得到該OPE-2St的自身交聯固化物。其中,升溫固化的條件如下:80℃ (12小時)、120℃ (2小時)、180℃ (2小時)、200℃ (2小時)、220℃ (2小時)。 比較應用例 2 OPE-4St 的自身交聯固化物 比較應用例2之OPE-4St的自身交聯固化物製備方法如下: 先將0.5 g比較例1的OPE-4St與5 mg [1 wt%(以OPE-4St的重量為100 wt%計)]的二叔丁基過氧化物(過氧化物起始劑)加入4.5 mL(使固含量為10 wt%)的DMAc中並攪拌2小時,再以0.44 µm的針頭過濾器進行過濾後,倒入鋁盤,使其於氮氣環境下進行升溫固化,得到該OPE-4St的自身交聯固化物。其中,升溫固化的條件如下:80℃ (12小時)、120℃ (2小時)、180℃ (2小時)、200℃ (2小時)、220℃ (2小時)。The preparation methods of the oligomers of Examples 1 to 2 and Comparative Example 1, and the cured products of Application Examples 1 to 4 and Comparative Application Examples 1 to 2 mentioned in this embodiment are respectively described in detail below. Example 1 OPE-E-2St ( oligomer ) The preparation method of OPE-E-2St in Example 1 is as follows: [ Reaction Formula I]
Figure 02_image021
(m is an integer from 0 to 30; n is an integer from 0 to 30) See Reaction Formula I, in a 100 mL three-necked reactor, add 0.4 g (2.86 mmol) of 4-carboxystyrene, After 0.57 g (2.86 mmole) of dicyclohexylcarbodiimide (DCC), 0.15 g (0.65 mmol) of 4-dimethylaminopyridine (DMAP), and 10 mL of dichloromethane (DCM), place it in a nitrogen atmosphere Cool down to 0°C and stir for 30 minutes. Next, first take another 2 g (1.3 mmol) of (2,6-dimethyl-1,4-phenylene ether) oligomer (SA90) with a phenol end group and dissolve it in 10 mL of dichloromethane, and The dichloromethane solution containing SA90 was added dropwise to a three-necked reactor and stirred for 2 hours, then the ice bath was removed, and the reaction was carried out at room temperature for 12 hours. After the reaction is over, remove most of the dicyclohexylurea (N,N'-dicyclohexylurea; DCU) by suction filtration, and finally pour the filtrate into methanol to precipitate the crude product, and wash the crude product with methanol. After suction filtration, the obtained filter cake was vacuum dried at 60° C. to obtain a white powder product (ie, the OPE-E-2St of Example 1; the yield was about 90 wt%). The proton nuclear magnetic resonance spectrum ( 1 H-NMR, see Figure 1), Fourier transform infrared spectroscopy (FTIR) and gel permeation chromatography (GPC) analysis results of OPE-E-2St in Example 1: 1 H-NMR (ppm, CDCl 3 ) : δ=1.69 (6H, H 10 ); 2.08 (Ar-CH 3 , H 6 , H 8 ); 5.40, 5.42 (2H, H b ); 5.88, 5.91 (2H, H a ) ; 6.46 (Ar-H, H 7 , H 9 ); 6.75, 6.77, 6.78, 6.80 (2H, H 2 ); 6.95 (4H, H 9 ); 7.51, 7.53 (4H, H 3 ); 8.15, 8.17 ( 4H, H 4 ). FTIR (KBr, cm -1 ) : ν= 1730 (C=O); 1607 (Ar-ring); 1311, 1185 (COC); 988, 916 (=CH). GPC (NMP) : M n = 4268; M w = 5799. Example 2 OPE-E-4St ( oligomer ) The preparation method of OPE-E-4St in Example 2 includes the following steps (1) to (3): [ Reaction formula II]
Figure 02_image023
(1) Preparation of compound BS-Mba : see reaction formula II, in a 100 mL three-neck reactor, add 1 g (5.94 mmol) of 3,5-dihydroxybenzoic acid methyl ester (3,5-dihydroxybenzoic acid methyl ester), 2 g (13 mmol) of chloromethyl styrene [1-(chloromethyl)-4-ethenylbenzene], 1.8 g (13 mmol) of potassium carbonate (K 2 CO 3 ) and 10 mL of dimethyl ethyl After dimethylacetamide (DMAc for short), the temperature is raised to 85° C. under a nitrogen atmosphere and the reaction is carried out for 12 hours. After the reaction is completed, an aqueous methanol solution (the weight ratio of methanol to water is 1) is poured into the crude product to precipitate. Next, after washing the crude product several times with a methanol aqueous solution (the weight ratio of methanol to water is 1), the yellow oily crude product obtained after washing is dissolved in ethyl acetate and extracted with pure water three times After removing the water from the organic layer with anhydrous magnesium sulfate, and finally concentrating under reduced pressure to remove ethyl acetate, a yellow transparent oily product (ie compound BS-Mba; yield is about 90 wt%) is obtained. 1 H-NMR and FTIR analysis results of compound BS-Mba: 1 H-NMR (ppm, DMSO-d 6 ) : δ=3.83 (3H, H 15 ); 5.13 (4H, H 9 ); 5.25, 5.27, 5.29 (2H, H b ); 5.82, 5.84, 5.85, 5.87 (2H, H a ); 6.73, 6.76 (2H, H 2 ); 6.97 (1H, H 10 ); 7.18, 7.20 (2H, H 12 ); 7.42 , 7.47 (8H, H 4 , H 5 ). FTIR (KBr, cm -1 ) : ν= 1721 (C=O); 1600 (Ar-ring); 1165, 1058 (COC); 990, 910 (=CH). [ Reaction formula III]
Figure 02_image025
(2) Preparation of compound BS-Acid : see reaction formula III, in a 100 mL three-necked reactor, add 1 g (2.49 mmol) of BS-Mba and 10 mL of ethanol, then heat to 80°C under a nitrogen atmosphere and Stir for 1 hour. Another 0.35 g (6.2 mmol) of potassium hydroxide (KOH) was dissolved in 10 mL of ethanol, added dropwise to a three-necked reactor and reacted at 80°C for 16 hours. After the reaction was completed, the ethanol was removed by concentration under reduced pressure . Then, first add 30 mL of ethyl acetate and sequentially extract three times with 1N hydrochloric acid, two times with brine, and two times with pure water, and then take the organic layer to remove water with anhydrous magnesium sulfate, and concentrate under reduced pressure to remove ethyl acetate. A solid is obtained. Finally, the solid was dissolved in dichloromethane, and n-hexane was added dropwise until the crude product precipitated. After stirring overnight, it was filtered with suction, and then the resulting filter cake was vacuum dried at 60°C to obtain a white Powdered product (ie compound BS-Acid; yield is about 80 wt%). 1 H-NMR and FTIR analysis results of compound BS-Mba: 1 H-NMR (ppm, DMSO-d 6 ) : δ=5.14 (4H, H 9 ); 5.26, 5.28, 5.29 (2H, H b ); 5.82 , 5.84, 5.85, 5.87 (2H, H a ); 6.71, 6.73, 6.76, 6.78 (2H, H 2 ); 6.93 (1H, H 10 ); 7.15, 7.17 (2H, H 12 ); 7.42, 7.48 (8H , H 4 , H 5 ); 13.00 (1H, COOH). FTIR (KBr, cm -1 ): ν=3200-2400 (COO-H); 1692 (C=O); 1595 (Ar-ring); 1165, 1058 (COC); 990, 910 (=CH). [ Reaction formula IV]
Figure 02_image027
(m is an integer from 0 to 30; n is an integer from 0 to 30) Preparation of OPE-E-4St : See Reaction Formula IV, in a 100 mL three-necked reactor, add 1.06 g (2.86 mmol) of BS-Acid , 0.57 g (2.86 mmol) of dicyclohexylcarbodiimide (DCC), 0.15 g (0.65 mmol) of 4-dimethylaminopyridine and 10 mL of dichloromethane, then cool to 0°C under nitrogen And stir for 30 minutes. Another 2 g (1.3 mmol) of SA90 was dissolved in 10 mL of dichloromethane, and the dichloromethane solution containing SA90 was added dropwise to a three-necked reactor and stirred for 2 hours, and then reacted at room temperature for 12 hours After the reaction is over, most of the dicyclohexylurea (DCU) is removed by suction filtration. Then, first take the filtrate and pour it into methanol/acetone to precipitate the crude product, and then wash the crude product with methanol/acetone and perform suction filtration. The resulting filter cake is vacuum dried at 60°C to obtain a white powder product (ie, Example 2 OPE-E-4St; the yield is about 90 wt%). 1 H-NMR (see Figure 2), FTIR and GPC analysis results of OPE-E-4St in Example 2: 1 H-NMR (ppm, CDCl 3 ) : δ = 1.68 (6H, H 13 ); 2.07 (Ar -CH 3 , H 9 , H 11 ); 5.08 (8H, H 5 ); 5.24, 5.25, 5.26, 5.27 (4H, H b ); 5.73, 5.75, 5.76, 5.77 (4H, H a ); 6.46 (Ar -H, H 10 , H 12 ); 6.71 (4H, H 2 ); 6.86 (2H, H 6 ); 6.95 (4H, H 12 ); 7.32-7.46 (H 4 , H 5 ). FTIR (KBr, cm -1 ) : ν = 1738 (C=O); 1607 (Ar-ring); 1311, 1185 (COC); 988, 916 (=CH). GPC (NMP) : M n = 4535, M w = 6969. Comparative Example 1 OPE-4St ( oligomer ) The preparation method of OPE-4St in Comparative Example 1 includes the following steps (1) to (3): [ Reaction formula V]
Figure 02_image029
(1) Preparation of compound BS-OH : see reaction formula V, in a 100 mL three-necked reactor, add 0.5 g (3.6 mmol) of dihydrocarbyl benzyl alcohol, 1.2 g (7.92 mmol) of chloromethyl styrene, carbonic acid After potassium 1.09 g (7.92 mmol) and 10 ml of DMAc, the temperature was raised to 85° C. and reacted for 12 hours under a nitrogen atmosphere. After the reaction was completed, the methanol solution was poured into the solution (the weight ratio of methanol to water was 1) to precipitate a crude product. Next, after washing the crude product several times with methanol aqueous solution (the weight ratio of methanol to water is 1), the yellow oily crude product obtained after washing is dissolved in ethyl acetate and extracted with pure water three times, and then the organic The layer was dehydrated with anhydrous magnesium sulfate, and finally concentrated under reduced pressure to remove ethyl acetate to obtain a yellow transparent oily product (ie, compound BS-OH; the yield was about 90 wt%). 1 H-NMR and FTIR analysis results of compound BS-OH: 1 H-NMR (ppm, DMSO-d 6 ) : δ=4.46 (2H, H 14 ); 5.07 (4H, H 9 ); 5.23 (OH); 5.26, 5.28, 5.30 (2H, H b ); 5.83, 5.84, 5.86, 5.87 (2H, H a ); 6.56 (1H, H 10 ); 6.63, 6.61 (2H, H 12 ); 6.72-6.78 (2H, H 2 ); 7.41, 7.48 (8H, H 4 , H 5 ). FTIR (KBr, cm -1 ) : ν=3377 (OH); 1600 (Ar-ring); 1165, 1048 (COC); 990, 910 (=CH). [ Reaction formula VI]
Figure 02_image031
(2) Preparation of compound BS-Cl : see reaction formula VI, in a 100 mL three-necked reactor, add 1 g (2.68 mmol) of BS-OH and 10 mL of dichloromethane, and mix with nitrogen at room temperature Add 0.76 g (6.44 mmol) of sulfite chloride (SOCl 2 ) and a few drops of pyridine to the environment in batches and dropwise to react for 3 hours. After the reaction is over, pure water is slowly dropped and extracted with pure water three times, the organic layer is removed with anhydrous magnesium sulfate to remove water, and the dichloromethane is removed by concentration under reduced pressure to obtain a yellow transparent oily product (ie, compound BS-Cl ; The yield is about 80 wt%). 1 H-NMR and FTIR analysis results of compound BS-Cl: 1 H-NMR (ppm, DMSO-d 6 ) : δ=4.67 (2H, H 14 ); 5.08 (4H, H 9 ); 5.26, 5.28, 5.29 (2H, H b ); 5.83, 5.84, 5.86, 5.87 (2H, H a ); 6.66 (1H, H 10 ); 6.73 (2H, H 12 ); 6.74 to 6.78 (2H, H 2 ); 7.42, 7.48 (8H, H 4 , H 5 ). FTIR (KBr, cm -1 ) : ν= 1600 (Ar-ring); 1257 (CH 2 -Cl); 1165, 1048 (COC); 990, 910 (=CH). [ Reaction formula VII]
Figure 02_image033
(m is an integer from 0 to 30; n is an integer from 0 to 30) Preparation of OPE-4St : see reaction formula VII, in a 100 mL three-necked reactor, add 1 g (0.62 mmol) of SA90, 0.58 g After (1.5 mmol) of BS-Cl, 0.2 g (1.5 mmol) of potassium carbonate (K 2 CO 3 ) and 15 mL of DMAc, the temperature was raised to 100° C. under a nitrogen atmosphere and the reaction was carried out for 24 hours. After the reaction is over, methanol is added dropwise to precipitate the crude product, which is washed several times with a methanol/acetone mixture, and finally after suction filtration, the resulting filter cake is vacuum dried at 60°C to obtain a white powdery product (ie OPE-4St of Comparative Example 1; the yield is about 85% by weight). 1 H-NMR, FTIR and GPC analysis results of OPE-4St of Comparative Example 1: 1 H-NMR (ppm, CDCl 3 ) : δ=1.69 (6H, H 13 ); 2.08 (Ar-CH 3 , H 9 , H 11 ); 4.68 (4H, H 8 ); 5.03 (8H, H 5 ); 5.23, 5.24, 5.26, 5.27 (4H, H b ); 5.73, 5.74, 5.76, 5.77 (4H, H a ); 6.46 ( Ar-H, H 10 , H 12 ); 6.57 (2H, H 6 ); 6.71 (4H, H 7 ); 6.74 (4H, H 2 ); 6.95 (4H, H 12 ); 7.29-7.45 (16H, H 4 , H 5 ). FTIR (KBr, cm -1 ) : ν=1605 (Ar-ring); 1311, 1185 (COC); 990, 910 (=CH). GPC (NMP) : M n = 5041; M w = 6818. Application Example 1 OPE-E-2St self-crosslinked cured product Application Example 1 OPE-E-2St self-crosslinked cured product was prepared as follows: First, 0.5 g of OPE-E-2St of Example 1 and 5 mg [ 1 wt% (based on the weight of OPE-E-2St as 100 wt%)] di-tert-butyl peroxide (peroxide initiator) is added to 4.5 mL (to make the solid content 10 wt%) of DMAc It was stirred for 2 hours, and then filtered with a 0.44 µm syringe filter, poured into an aluminum pan, and allowed to heat up and solidify in a nitrogen environment to obtain the self-crosslinked cured product of OPE-E-2St. Among them, the conditions for heating and curing are as follows: 80°C (12 hours), 120°C (2 hours), 180°C (2 hours), 200°C (2 hours), 220°C (2 hours). Application Example 2 OPE-E-4St self-crosslinked cured product Application Example 2 OPE-E-4St self-crosslinked cured product was prepared as follows: First, 0.5 g of OPE-E-4St of Example 2 and 5 mg [ 1 wt% (based on the weight of OPE-E-4St as 100 wt%)] di-tert-butyl peroxide (peroxide initiator) was added to 4.5 mL (to make the solid content 10 wt%) of DMAc It was stirred for 2 hours, and then filtered with a 0.44 µm syringe filter, then poured into an aluminum pan and allowed to heat up and cure in a nitrogen environment to obtain the self-crosslinked cured product of OPE-E-4St. Among them, the conditions for heating and curing are as follows: 80°C (12 hours), 120°C (2 hours), 180°C (2 hours), 200°C (2 hours), 220°C (2 hours). Application Example 3 OPE-E-2St co-cured with an epoxy resin cured Application Example OPE-E-2St co-cured with an epoxy resin 3 of the cured product prepared as follows: Example 1 First 1 g (1 mmol) embodiment OPE-E-2St, 0.28 g (1 mmol) epoxy resin (trade name: HP7200), 0.01 g [1 wt% (based on the weight of OPE-E-2St as 100 wt%)] di-tert-butyl Base peroxide (peroxide initiator), 1.4 mg [0.5 wt% (based on the weight of epoxy resin as 100 wt%)] DMAP (catalyst) was added to 11.4 mL (to make the solid content 10 wt% ) In DMAc and stirred for 2 hours, then filtered with a 0.44 µm syringe filter, poured into an aluminum pan, and allowed to heat up and cure in a nitrogen environment to obtain the OPE-E-2St and epoxy resin co-cured Cured matter. Among them, the conditions for heating and curing are as follows: 80°C (12 hours), 120°C (2 hours), 180°C (2 hours), 200°C (2 hours), 220°C (2 hours). The method of preparing a cured product OPE-E-4St with the epoxy resin of Example 4 Application Example 4 OPE-E-4St co-cured with an epoxy resin cured co-curing was applied as follows: first 1 g (0.86 mmol) of Example 2 OPE-E-4St, 0.22 g (0.86 mmol) epoxy resin (trade name: HP7200), 0.01 g [1 wt% (based on the weight of OPE-E-4St as 100 wt%)] di-tert-butyl Base peroxide (peroxide initiator), 1.1 mg [0.5 wt% (based on the weight of epoxy resin as 100 wt%)] DMAP (catalyst) was added 11 mL (to make the solid content 10 wt% ) In the DMAc and stirred for 2 hours, then filtered with a 0.44 µm syringe filter, poured into an aluminum pan, and allowed to heat up and cure in a nitrogen environment to obtain the OPE-E-4St and epoxy resin co-cured Cured matter. Among them, the conditions for heating and curing are as follows: 80°C (12 hours), 120°C (2 hours), 180°C (2 hours), 200°C (2 hours), 220°C (2 hours). Comparative Application Example 1 OPE-2St self-crosslinked cured product Comparative Application Example 1 OPE-2St self-crosslinked cured product was prepared as follows: First, 0.5 g of OPE-2St (manufacturer: Mitsubishi Gas Chemical Company, Inc.) And 5 mg [1 wt% (based on the weight of OPE-2St as 100 wt%)] of di-tert-butyl peroxide (peroxide initiator) added to 4.5 mL (to make the solid content 10 wt%) Stir in DMAc for 2 hours, then filter with a 0.44 µm syringe filter, pour it into an aluminum pan, and allow it to heat up and cure in a nitrogen environment to obtain a self-crosslinked cured product of OPE-2St. Among them, the conditions for heating and curing are as follows: 80°C (12 hours), 120°C (2 hours), 180°C (2 hours), 200°C (2 hours), 220°C (2 hours). Comparative Application Example 2 OPE-4St self-crosslinked cured product Comparative Application Example 2 OPE-4St self-crosslinked cured product The preparation method of the self-crosslinked cured product of OPE-4St is as follows: First, 0.5 g of OPE-4St of Comparative Example 1 and 5 mg [1 wt%( The weight of OPE-4St is 100 wt%)] di-tert-butyl peroxide (peroxide initiator) is added to 4.5 mL (to make the solid content 10 wt%) of DMAc and stirred for 2 hours, then After filtering with a 0.44 µm syringe filter, it was poured into an aluminum pan and heated and cured in a nitrogen atmosphere to obtain a self-crosslinked cured product of the OPE-4St. Among them, the conditions for heating and curing are as follows: 80°C (12 hours), 120°C (2 hours), 180°C (2 hours), 200°C (2 hours), 220°C (2 hours).

特別說明的是,現有OPE-2St與比較例1的OPE-4St寡聚物由於其末端皆不具有活性酯基,因此無法拿來與環氧樹脂進行共固化。In particular, the existing OPE-2St and the OPE-4St oligomers of Comparative Example 1 have no active ester groups at their ends, so they cannot be used for co-curing with epoxy resins.

固化物的熱性質分析Thermal properties analysis of cured products

A.A. 分析方法:Analytical method:

熱性質分析是針對應用例1~4與比較應用例1~2之固化物的玻璃轉移溫度(Tg )、熱膨脹係數(CTE)、5wt%熱重損失溫度(Td5 )與800℃的焦炭殘餘率(char yield)進行分析,其分析方法分別如下所述。1. 以動態機械分析儀 (dynamic mechanical analyzer DMA) 量測玻璃轉移溫度 (Tg ) 使用動態機械分析儀(型號:Perkin-Elmer Pyris Diamond) 針對應用例1~4與比較應用例1~2之固化物的玻璃轉移溫度進行量測。其中,前述動態機械分析條件為在5°C/分的加熱速率下量測。2. 以熱機械分析法 (thermo-mechanical analysis TMA) 量測玻璃轉移溫度 (Tg ) 與熱膨脹係數 (CTE) 以熱機械分析法(TMA)針對應用例1~4與比較應用例1~2之固化物的玻璃轉移溫度(Tg )與熱膨脹係數進行量測。其中,前述熱機械分析條件為在5°C/分的加熱速率下量測。3. 以熱重分析法 (thermo-gravimetric analysis TGA) 量測 5wt% 熱重損失溫度 (Td5 ) 800 ℃的焦炭殘餘率: 以熱重分析儀(型號: Thermo Cahn VersaTherm)針對應用例1~4與比較應用例1~2之固化物的5wt%熱重損失溫度與800°C的焦炭殘餘率進行量測。其中,前述熱重分析條件是在氮氣氣氛及20°C/分的加熱速率下進行。需說明的是,5wt%熱重損失溫度是指固化物的重量損失達5wt%時的溫度,而當5wt%熱重損失溫度越高表示固化物的熱穩定性愈高;800°C的焦炭殘餘率是指加熱溫度達800°C時的固化物所殘餘的重量比率,而當800°C的焦炭殘餘率越高表示固化物的熱穩定性愈高。The thermal property analysis is for the glass transition temperature (T g ), coefficient of thermal expansion (CTE), 5wt% thermogravimetric loss temperature (T d5 ) and 800℃ coke of the cured products of Application Examples 1 to 4 and Comparative Application Examples 1 to 2 The residual rate (char yield) is analyzed, and the analysis methods are as follows. 1. Dynamic Mechanical Analyzer (dynamic mechanical analyzer; DMA) measurement of glass transition temperature (T g): using a dynamic mechanical analyzer (Model: Perkin-Elmer Pyris Diamond) for 1 to 4 and Comparative Application Example 1 Application Example 2 The glass transition temperature of the cured product is measured. Among them, the aforementioned dynamic mechanical analysis conditions are measured at a heating rate of 5°C/min. 2. thermomechanical analysis (thermo-mechanical analysis; TMA) Measurement of glass transition temperature (T g) and the coefficient of thermal expansion (CTE): thermal mechanical analysis (TMA) for Application Examples 1 to 4 and Comparative Application Example 1 ~2 The glass transition temperature (T g ) and thermal expansion coefficient of the cured product are measured. Among them, the aforementioned thermomechanical analysis conditions are measured at a heating rate of 5°C/min. 3. Thermogravimetric Analysis (thermo-gravimetric analysis; TGA) weight measurement 5wt% heat loss temperature (T d5) of 800 deg.] C and coke residue: A thermogravimetric analyzer (Model: Thermo Cahn VersaTherm) for Application Example The 5wt% thermogravimetric loss temperature and the coke residual rate of 800°C of the cured products of 1~4 and Comparative Application Examples 1~2 were measured. Among them, the aforementioned thermogravimetric analysis conditions are performed under a nitrogen atmosphere and a heating rate of 20°C/min. It should be noted that the 5wt% thermogravimetric loss temperature refers to the temperature at which the weight loss of the cured product reaches 5wt%, and the higher the 5wt% thermogravimetric loss temperature, the higher the thermal stability of the cured product; 800°C coke The residual rate refers to the residual weight ratio of the cured product when the heating temperature reaches 800°C, and the higher the coke residual rate at 800°C, the higher the thermal stability of the cured product.

應用例1~4與比較應用例1~2之固化物的玻璃轉移溫度(T )、熱膨脹係數(CTE)、5wt%熱重損失溫度(Td5 )與800℃的焦炭殘餘率,以及固化所使用的硬化劑(寡聚物/環氧樹脂)分別整理於下表1中。 表1 固化所使用的硬化劑 Tg (DMA) ( ℃) Tg (TMA) ( ℃) CTE (ppm/ ℃) Td5 ( ℃) 焦炭殘餘率 (wt%) 比較應用例1 OPE-2St 229 204 76 394 27 應用 例1 OPE-E-2St 258 223 62 504 32 應用 例3 OPE-E-2St 與環氧樹脂 214 182 65 417 21 比較應用例2 OPE-4St 246 221 61 426 33 應用 例2 OPE-E-4St 257 225 62 488 36 應用 例4 OPE-E-4St 與環氧樹脂 218 185 59 421 26 The glass transition temperature (T g ), coefficient of thermal expansion (CTE), 5wt% thermogravimetric loss temperature (T d5 ) of the cured products of application examples 1 to 4 and comparative application examples 1 to 2 and coke residual rate at 800°C, and curing The hardeners (oligomer/epoxy resin) used are listed in Table 1 below. Table 1 Hardener used for curing T g (DMA) ( ℃) T g (TMA) ( ℃) CTE (ppm/ ℃) T d5 ( ℃) Residual coke rate (wt%) Comparative application example 1 OPE-2St 229 204 76 394 27 Application example 1 OPE-E-2St 258 223 62 504 32 Application example 3 OPE-E-2St and epoxy resin 214 182 65 417 twenty one Comparative application example 2 OPE-4St 246 221 61 426 33 Application example 2 OPE-E-4St 257 225 62 488 36 Application example 4 OPE-E-4St and epoxy resin 218 185 59 421 26

B.B. 結果與討論:Results and discussion:

由表1中以自身交聯固化所得之固化物的數據可以發現,相較於末端不具有任何酯基之OPE-2St所形成的固化物(比較應用例1),末端具有酯基之OPE-E-2St所形成的固化物(應用例1)會具有較高的玻璃轉移溫度、5wt%熱重損失溫度與焦炭殘餘率,而相較於末端不具有任何酯基之OPE-4St所形成的固化物(比較應用例2),末端具有酯基之OPE-E-4St所形成的固化物(應用例2)同樣也會具有較高的玻璃轉移溫度、5wt%熱重損失溫度與焦炭殘餘率。因此,以固化物的熱性質來看,相較於現有末端不具有任何酯基的寡聚物,本發明末端具有乙烯基苯酯的寡聚物[式(I)]能使後續所製得的固化物具有較高的玻璃轉移溫度,且同時還會具有較高的熱重損失溫度(Td5 )與焦炭殘餘率(即具有較高的熱穩定性)。From the data of the cured product obtained by self-crosslinking and curing in Table 1, it can be found that compared to the cured product formed by OPE-2St without any ester group at the end (Comparative Application Example 1), the OPE- with ester group at the end The cured product formed by E-2St (application example 1) will have a higher glass transition temperature, 5wt% thermogravimetric loss temperature and coke residual rate, compared to the one formed by OPE-4St without any ester group at the end Cured product (Comparative Application Example 2), the cured product formed by OPE-E-4St with an ester group at the end (Application Example 2) will also have higher glass transition temperature, 5wt% thermal weight loss temperature and coke residual rate . Therefore, in terms of the thermal properties of the cured product, compared to the existing oligomers without any ester groups at the ends, the oligomers with vinyl phenyl ester at the ends of the present invention [formula (I)] can make subsequent preparations The cured product has a higher glass transition temperature, and at the same time also has a higher thermogravimetric loss temperature (T d5 ) and coke residual rate (that is, higher thermal stability).

補充說明的是,前述熱穩定性的提高是因為由本發明寡聚物進行自身交聯固化所得之固化物,其會具有可與苯環共振的酯基,因而使固化物結構較穩定,進而能提高固化物的熱穩定性。It is added that the aforementioned increase in thermal stability is due to the fact that the cured product obtained by self-crosslinking and curing of the oligomer of the present invention will have an ester group that can resonate with the benzene ring, so that the structure of the cured product is more stable and can Improve the thermal stability of the cured product.

此外,比較與環氧樹脂共固化所得之應用例3與應用例4的數據可以發現,由OPE-E-4St與環氧樹脂共固化所得的固化物會具有較高的玻璃轉移溫度與較低的熱膨脹係數(即具有較高的尺寸安定性),且同時也會具有較高的熱重損失溫度與焦炭殘餘率(即具有較高的熱穩定性)。In addition, comparing the data of Application Example 3 and Application Example 4 obtained by co-curing with epoxy resin, it can be found that the cured product obtained by co-curing OPE-E-4St and epoxy resin will have a higher glass transition temperature and a lower The coefficient of thermal expansion (that is, it has higher dimensional stability), and at the same time it will have a higher thermogravimetric loss temperature and coke residual rate (that is, it has higher thermal stability).

固化物的介電性質分析Analysis of the dielectric properties of the cured product

A.A. 分析方法:Analytical method:

介電性質分析是針對應用例1~4與比較應用例1~2之固化物的介電常數(Dk )與介電損失(Df )進行分析,其分析方法為利用介電分析儀分析應用例1~4與比較應用例1~2之固化物的介電常數與介電損失。The analysis of dielectric properties is to analyze the dielectric constant (D k ) and dielectric loss (D f ) of the cured products of application examples 1 to 4 and comparative application examples 1 to 2. The analysis method is to use a dielectric analyzer to analyze The dielectric constant and dielectric loss of the cured products of Application Examples 1 to 4 and Comparative Application Examples 1 to 2.

應用例1~4與比較應用例1~2之固化物於1 GHz的介電常數(Dk )與介電損失(Df ),以及固化所使用的硬化劑(寡聚物/環氧樹脂)與固化物試片厚度分別整理於下表2中。 表2 固化所使用的硬化劑 厚度 (µm) Dk (U) Df (mU) 比較應用例 1 OPE-2St 237 2.69±0.001 6.9±0.5 應用 1 OPE-E-2St 190 2.54±0.001 5.9±0.5 應用 3 OPE-E-2St 與環氧樹脂 220 2.47±0.002 7.0±0.3 比較應用例 2 OPE-4St 184 2.64±0.002 9.0±0.2 應用 2 OPE-E-4St 140 2.52±0.002 7.0±0.2 應用 4 OPE-E-4St 與環氧樹脂 170 2.46±0.001 8.1±0.2 The dielectric constant (D k ) and dielectric loss (D f ) of the cured products of application examples 1 to 4 and comparative application examples 1 to 2 at 1 GHz, and the hardener used for curing (oligomer/epoxy resin) ) And the thickness of the cured product test piece are listed in Table 2 below. Table 2 Hardener used for curing Thickness (µm) D k (U) D f (mU) Comparative application example 1 OPE-2St 237 2.69±0.001 6.9±0.5 Application example 1 OPE-E-2St 190 2.54±0.001 5.9±0.5 Application example 3 OPE-E-2St and epoxy resin 220 2.47±0.002 7.0±0.3 Comparative application example 2 OPE-4St 184 2.64±0.002 9.0±0.2 Application example 2 OPE-E-4St 140 2.52±0.002 7.0±0.2 Application example 4 OPE-E-4St and epoxy resin 170 2.46±0.001 8.1±0.2

B.B. 結果與討論:Results and discussion:

由表2中以自身交聯固化所得之固化物的數據可以發現,相較於末端不具有任何酯基之OPE-2St所形成的固化物(比較應用例1),末端具有酯基之OPE-E-2St所形成的固化物(應用例1)會具有較低的介電常數與介電損失,而相較於末端不具有任何酯基之OPE-4St所形成的固化物(比較應用例2),末端具有酯基之OPE-E-4St所形成的固化物(應用例2)同樣也會具有較低的介電常數與介電損失。因此,以固化物的介電性質來看,相較於現有末端不具有任何酯基的寡聚物,本發明末端具有乙烯基苯酯的寡聚物[式(I)]能使後續所製得的固化物具有較低的介電常數與介電損失。From the data of the cured product obtained by self-crosslinking and curing in Table 2, it can be found that compared to the cured product formed by OPE-2St without any ester group at the end (Comparative Application Example 1), the OPE- with an ester group at the end is The cured product formed by E-2St (application example 1) will have lower dielectric constant and dielectric loss, and compared to the cured product formed by OPE-4St without any ester groups at the end (comparative application example 2) ), the cured product (Application Example 2) formed by OPE-E-4St with an ester group at the end will also have a lower dielectric constant and dielectric loss. Therefore, from the perspective of the dielectric properties of the cured product, compared to the existing oligomers without any ester groups at the ends, the oligomers with vinyl phenyl ester at the ends of the present invention [formula (I)] can make subsequent preparations The cured product obtained has a lower dielectric constant and dielectric loss.

補充說明的是,前述介電常數的降低是因為由本發明寡聚物進行自身交聯固化所得之固化物會具有酯基,因而相較於僅具有脂肪基的固化物,本發明具有酯基的固化物會具有更高的立體障礙而具有較多的自由體積,進而能降低介電常數。It is added that the aforementioned decrease in dielectric constant is due to the fact that the cured product obtained by self-crosslinking and curing of the oligomer of the present invention will have ester groups. Therefore, compared with the cured product having only fatty groups, the present invention has ester groups. The cured product will have a higher three-dimensional obstacle and more free volume, which can lower the dielectric constant.

固化物的機械性質分析Analysis of the mechanical properties of the cured product

A.A. 分析方法:Analytical method:

機械性質分析是針對應用例1~4與比較應用例1~2之固化物的楊式模數(Young's modulus)、拉伸強度與斷裂伸長率進行分析,其分析方法皆為利用拉力機進行分析。The mechanical property analysis is to analyze the Young's modulus, tensile strength and elongation at break of the cured products of Application Examples 1 to 4 and Comparative Application Examples 1 to 2. The analysis methods are all analyzed by using a tensile machine.

應用例1~4與比較應用例1~2之固化物的楊式模數、拉伸強度與斷裂伸長率,以及固化所使用的硬化劑(寡聚物/環氧樹脂)與固化物試片厚度分別整理於下表3中。 表3 固化所使用的硬化劑 厚度 (µm) 楊式 模數 (GPa) 拉伸 強度 (MPa) 斷裂 伸長率 (%) 比較應用例 1 OPE-2St 110 1.565 67.33 5.67 應用 1 OPE-E-2St 140 1.376 67.23 8.69 應用 3 OPE-E-2St 與環氧樹脂 140 1.573 98.89 8.71 比較應用例 2 OPE-4St 165 0.888 50.93 4.81 應用 2 OPE-E-4St 160 0.965 62.82 7.22 應用 4 OPE-E-4St 與環氧樹脂 175 1.275 90.27 8.15 The Young's modulus, tensile strength and elongation at break of the cured products of Application Examples 1 to 4 and Comparative Application Examples 1 to 2, as well as the curing agent (oligomer/epoxy resin) used for curing and the thickness of the cured product test piece They are summarized in Table 3 below. table 3 Hardener used for curing Thickness (µm) Young's modulus (GPa) Tensile strength (MPa) Elongation at break (%) Comparative application example 1 OPE-2St 110 1.565 67.33 5.67 Application example 1 OPE-E-2St 140 1.376 67.23 8.69 Application example 3 OPE-E-2St and epoxy resin 140 1.573 98.89 8.71 Comparative application example 2 OPE-4St 165 0.888 50.93 4.81 Application example 2 OPE-E-4St 160 0.965 62.82 7.22 Application example 4 OPE-E-4St and epoxy resin 175 1.275 90.27 8.15

B.B. 結果與討論:Results and discussion:

由表3中以自身交聯固化所得之固化物的數據可以發現,相較於末端不具有任何酯基之OPE-2St所形成的固化物(比較應用例1),末端具有酯基之OPE-E-2St所形成的固化物(應用例1)會具有較高的斷裂伸長率,而相較於末端不具有任何酯基之OPE-4St所形成的固化物(比較應用例2),末端具有酯基之OPE-E-4St所形成的固化物(應用例2)同樣也會具較高的斷裂伸長率。因此,以固化物的機械性質來看,相較於現有末端不具有任何酯基的寡聚物,本發明末端具有乙烯基苯酯的寡聚物[式(I)]能使後續所製得的固化物具有較高的斷裂伸長率(即較不易因拉伸而脆裂)。補充說明的是,斷裂伸長率的提高是因為由本發明寡聚物進行自身交聯固化所得之固化物會具有酯基,因而相較於僅具有脂肪基的固化物,本發明具有酯基的固化物會具有更高的立體障礙而具有更高的分子鏈擺動空間,進而能提高斷裂伸長率。From the data of the cured product obtained by self-crosslinking and curing in Table 3, it can be found that compared with the cured product formed by OPE-2St without any ester group at the end (Comparative Application Example 1), the OPE- with ester group at the end The cured product formed by E-2St (application example 1) will have higher elongation at break, and compared to the cured product formed by OPE-4St without any ester group at the end (comparative application example 2), the end has The cured product formed by ester-based OPE-E-4St (application example 2) also has a higher elongation at break. Therefore, in terms of the mechanical properties of the cured product, compared with the existing oligomers without any ester groups at the ends, the oligomers with vinyl phenyl ester at the ends of the present invention [formula (I)] can make subsequent preparations The cured product has a higher elongation at break (that is, it is less likely to be brittle due to stretching). It is added that the increase in elongation at break is due to the fact that the cured product obtained by self-crosslinking and curing of the oligomer of the present invention will have ester groups. Therefore, compared with the cured product having only fatty groups, the cured product of the present invention has ester groups. The object will have a higher steric barrier and a higher molecular chain swing space, which can increase the elongation at break.

此外,本發明寡聚物與環氧樹脂進行共固化後得到的固化物(應用例3~4)除了有較高的斷裂伸長率外,同時還會具有較高的楊式模數與拉伸強度,此是由於與環氧樹脂共固化後的固化物會具有網狀結構,因此能更加提高其整體的機械性質,進而使固化物更不易發生脆裂。In addition, the cured product obtained by co-curing the oligomer and epoxy resin of the present invention (application examples 3 to 4) not only has higher elongation at break, but also higher Young's modulus and tensile strength. This is because the cured product after co-curing with the epoxy resin will have a network structure, so its overall mechanical properties can be improved, and the cured product is less prone to brittle cracking.

固化物的交聯密度與透氣率分析Analysis of the crosslink density and air permeability of the cured product

A.A. 分析方法:Analytical method:

機械性質分析是針對應用例1~4與比較應用例1~2之固化物的交聯密度與透氣率進行分析,其分析方法皆為利用氣體透過率分析儀(gas permeability analysis;GTR)進行分析。其中,前述分析的條件設定為壓力1.0 atm,溫度35.5℃,測量氣體為氧氣。The analysis of mechanical properties is to analyze the crosslink density and air permeability of the cured products of application examples 1 to 4 and comparative application examples 1 to 2. The analysis methods are all analyzed by gas permeability analysis (GTR) . Among them, the conditions of the aforementioned analysis are set to a pressure of 1.0 atm, a temperature of 35.5°C, and the measurement gas is oxygen.

應用例1~4與比較應用例1~2之固化物的交聯密度與透氣率,以及固化所使用的硬化劑(寡聚物/環氧樹脂)分別整理於下表4中。 表4 固化所使用的硬化劑 交聯密度 (mmol cm-3 ) 透氣率 (barrer) 比較應用例 1 OPE-2St 1.46 8.7 應用 1 OPE-E-2St 1.54 10.0 應用 3 OPE-E-2St 與環氧樹脂 1.53 7.7 比較應用例 2 OPE-4St 2.99 6.0 應用 2 OPE-E-4St 3.25 4.8 應用 4 OPE-E-4St 與環氧樹脂 2.99 5.6 The crosslinking density and air permeability of the cured products of Application Examples 1 to 4 and Comparative Application Examples 1 to 2, and the hardener (oligomer/epoxy resin) used for curing are listed in Table 4 below. Table 4 Hardener used for curing Crosslink density (mmol cm -3 ) Air permeability (barrer) Comparative application example 1 OPE-2St 1.46 8.7 Application example 1 OPE-E-2St 1.54 10.0 Application example 3 OPE-E-2St and epoxy resin 1.53 7.7 Comparative application example 2 OPE-4St 2.99 6.0 Application example 2 OPE-E-4St 3.25 4.8 Application example 4 OPE-E-4St and epoxy resin 2.99 5.6

B.B. 結果與討論:Results and discussion:

由表4可知,不論是OPE-E-4St進行自身交聯固化或是與環氧樹脂共固化所得的固化物(應用例2、4)皆具有較低的透氣率,即會具有較優異的氧氣阻隔性。It can be seen from Table 4 that whether OPE-E-4St is cross-linked and cured by itself or co-cured with epoxy resin (Application Examples 2 and 4), the cured product has a lower air permeability, that is, it will have a better Oxygen barrier.

綜上所述,由於本發明式(I)的(2,6-二甲基-1,4-苯醚)寡聚物末端具有乙烯基苯酯,因此後續所製得的固化物能同時具有較高玻璃轉移溫度(Tg )與熱穩定性、較低介電常數與介電損失及較高斷裂伸長率特性,且由於該末端的乙烯基苯酯為活性酯基,因而本發明式(I)的(2,6-二甲基-1,4-苯醚)寡聚物還能用於與環氧樹脂進行共固化,故確實能達成本發明的目的。In summary, because the (2,6-dimethyl-1,4-phenylene ether) oligomer of formula (I) of the present invention has vinyl phenyl ester at the end, the cured product obtained subsequently can have both Higher glass transition temperature (T g ) and thermal stability, lower dielectric constant and dielectric loss, and higher elongation at break characteristics, and because the terminal vinyl phenyl ester is an active ester group, the formula of the present invention ( The (2,6-dimethyl-1,4-phenylene ether) oligomer of I) can also be used for co-curing with epoxy resin, so it can indeed achieve the purpose of the invention.

惟以上所述者,僅為本發明的實施例而已,當不能以此限定本發明實施的範圍,凡是依本發明申請專利範圍及專利說明書內容所作的簡單的等效變化與修飾,皆仍屬本發明專利涵蓋的範圍內。However, the above are only examples of the present invention. When the scope of implementation of the present invention cannot be limited by this, all simple equivalent changes and modifications made in accordance with the scope of the patent application of the present invention and the content of the patent specification still belong to Within the scope of the patent for the present invention.

本發明的其他的特徵及功效,將於參照圖式的實施方式中清楚地呈現,其中: 圖1是本發明實施例1的1 H-NMR光譜圖;及 圖2是本發明實施例1的1 H-NMR光譜圖。Other features and effects of the present invention will be clearly presented in the embodiment with reference to the drawings, in which: Figure 1 is a 1 H-NMR spectrum of Example 1 of the present invention; and Figure 2 is a view of Example 1 of the present invention 1 H-NMR spectrum.

Figure 108100304-A0101-11-0001-1
Figure 108100304-A0101-11-0001-1

Claims (9)

一種(2,6-二甲基-1,4-苯醚)寡聚物,如下式(I)所示:
Figure 108100304-A0305-02-0030-4
其中, X為
Figure 108100304-A0305-02-0030-1
, Y為-C(CH3)2-,R1為氫、C1~C6烷基或苯基,m、n分別為0至50的整數,q為1至3的整數。
A (2,6-dimethyl-1,4-phenylene ether) oligomer, as shown in the following formula (I):
Figure 108100304-A0305-02-0030-4
Where X is
Figure 108100304-A0305-02-0030-1
, Y is -C(CH 3 ) 2 -, R 1 is hydrogen, C 1 to C 6 alkyl or phenyl, m and n are each an integer from 0 to 50, and q is an integer from 1 to 3.
如請求項1所述的(2,6-二甲基-1,4-苯醚)寡聚物,其中, X為
Figure 108100304-A0305-02-0030-3
The (2,6-dimethyl-1,4-phenylene ether) oligomer according to claim 1, wherein X is
Figure 108100304-A0305-02-0030-3
.
一種固化物,是由一樹脂組成物於過氧化物起始劑的存在下進行固化所製得,該樹脂組成物含有如請求項1所述的(2,6-二甲基-1,4-苯醚)寡聚物。 A cured product is prepared by curing a resin composition in the presence of a peroxide initiator, the resin composition containing (2,6-dimethyl-1,4 -Phenyl ether) oligomers. 如請求項3所述的固化物,其中,該過氧化物起始劑是選 自於二叔丁基過氧化物、過氧化苯甲醯、過氧化叔丁醇、叔丁基過氧化異丙苯或前述的組合。 The cured product according to claim 3, wherein the peroxide initiator is selected From di-tert-butyl peroxide, benzyl peroxide, tert-butanol peroxide, tert-butyl cumene peroxide or a combination of the foregoing. 如請求項3所述的固化物,其中,以該(2,6-二甲基-1,4-苯醚)寡聚物的重量為100wt%計,該過氧化物起始劑的重量範圍為0.1~5wt%。 The cured product according to claim 3, wherein, based on the weight of the (2,6-dimethyl-1,4-phenylene ether) oligomer being 100% by weight, the weight range of the peroxide initiator It is 0.1~5wt%. 如請求項3所述的固化物,其中,該樹脂組成物還含有環氧樹脂,且該固化物是由該樹脂組成物於過氧化物起始劑與觸媒的存在下進行固化所製得。 The cured product according to claim 3, wherein the resin composition further contains an epoxy resin, and the cured product is prepared by curing the resin composition in the presence of a peroxide initiator and a catalyst . 如請求項6所述的固化物,其中,該環氧樹脂是選自於雙酚A型環氧樹脂、酚醛環氧樹脂、甲基酚醛環氧樹脂、雙環戊二烯苯酚環氧樹脂、含萘環氧樹脂或前述的組合。 The cured product according to claim 6, wherein the epoxy resin is selected from the group consisting of bisphenol A epoxy resin, novolac epoxy resin, methyl novolac epoxy resin, dicyclopentadiene phenol epoxy resin, and Naphthalene epoxy resin or a combination of the foregoing. 如請求項6所述的固化物,其中,該觸媒是選自於4-二甲基胺基吡啶、咪唑、2-甲基-4-甲基咪唑、2-甲基咪唑、三苯基膦或前述的組合。 The cured product according to claim 6, wherein the catalyst is selected from 4-dimethylaminopyridine, imidazole, 2-methyl-4-methylimidazole, 2-methylimidazole, triphenyl Phosphine or a combination of the foregoing. 如請求項6所述的固化物,其中,以該環氧樹脂的重量為100wt%計,該觸媒的重量範圍為0.1~5wt%。 The cured product according to claim 6, wherein, based on the weight of the epoxy resin being 100 wt%, the weight of the catalyst ranges from 0.1 to 5 wt%.
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