TWI702235B - Toughening vitrimer and preparation method thereof - Google Patents
Toughening vitrimer and preparation method thereof Download PDFInfo
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本發明是關於一種增韌可塑性熱固型樹脂及其製備方法,特別是關於一種導入聚丙烯酸丁酯軟鏈之增韌可塑性熱固型樹脂及其製備方法。 The invention relates to a toughened plastic thermosetting resin and a preparation method thereof, in particular to a toughened plastic thermosetting resin introduced with polybutyl acrylate soft chains and a preparation method thereof.
聚甲基丙烯酸甲酯樹脂(俗稱壓克力)是日常中被廣泛使用的熱塑性樹脂之一,其優點包括可塑性、尺寸穩定性等。然而,聚甲基丙烯酸甲酯樹脂具有一些缺點,包括低耐化性、低耐熱性、低機械性質等。 Polymethyl methacrylate resin (commonly known as acrylic) is one of the thermoplastic resins that are widely used in daily life. Its advantages include plasticity and dimensional stability. However, polymethyl methacrylate resin has some disadvantages, including low chemical resistance, low heat resistance, low mechanical properties, and so on.
為了解決上述缺點,一般會於聚甲基丙烯酸甲酯樹脂中加入交聯劑使其固化形成熱固性樹脂,以提升其耐化性、耐熱性以及機械性質,但此方法會使聚甲基丙烯酸甲酯樹脂失去原本的可塑性。 In order to solve the above shortcomings, a crosslinking agent is generally added to the polymethyl methacrylate resin to cure it to form a thermosetting resin to improve its chemical resistance, heat resistance and mechanical properties. However, this method will make the polymethyl methacrylate resin The ester resin loses its original plasticity.
另外,亦有研究利用動態共價鍵結(Dynamic covalent bonds)導入交聯樹脂中形成共價適應網路(Covalent Adaptable Networks,CANs),可利於不損失材料結構下提升材料的重塑、加工及回收性。然而,儘管動態共價鍵結可使交聯樹脂展現優異的應力鬆弛與流動,但對 於樹脂的適應性及動態共價鍵結的壽命是有限的,以致材料無法再依靠動態共價鍵結來進行加工。 In addition, there are also studies using dynamic covalent bonds (Dynamic covalent bonds) to be introduced into cross-linked resins to form covalent adaptable networks (CANs), which can help improve the remodeling, processing and processing of materials without losing the material structure. Recyclability. However, although dynamic covalent bonding can make the cross-linked resin exhibit excellent stress relaxation and flow, it is not The adaptability of the resin and the life of dynamic covalent bonding are limited, so that the material can no longer rely on dynamic covalent bonding for processing.
有鑑於此,如何在改善聚甲基丙烯酸甲酯樹脂的耐化性、耐熱性以及機械性質的情況下,還能保有聚甲基丙烯酸甲酯樹脂本身的可塑性,遂成為相關業者努力的目標。 In view of this, how to improve the chemical resistance, heat resistance and mechanical properties of the polymethyl methacrylate resin while maintaining the plasticity of the polymethyl methacrylate resin itself has become the goal of the relevant industry.
本發明之一目的是在於提供一種增韌可塑性熱固型樹脂的製備方法,利用具有聚丙烯酸丁酯軟鏈段之大分子起始劑,合成不同構形之三嵌段共聚物以及具超分支核之星狀共聚物,再使用交聯劑以及酯交換催化劑,使共聚物固化交聯形成具有共價適應網路(CANs)的增韌可塑性熱固型樹脂。 One of the objectives of the present invention is to provide a method for preparing toughened plastic thermosetting resin, which uses a macromolecular initiator with polybutyl acrylate soft segment to synthesize triblock copolymers with different configurations and super branched The core-star copolymer uses crosslinking agent and transesterification catalyst to cure and crosslink the copolymer to form a toughened plastic thermosetting resin with covalent adaptation networks (CANs).
本發明之另一目的在於提供一種增韌可塑性熱固型樹脂,其具有較大的應變且可增加材料的韌性,並具有良好的耐化性及耐熱性並在高溫下亦可達到原本的可塑性及修復性。 Another object of the present invention is to provide a toughened plastic thermosetting resin, which has greater strain and can increase the toughness of the material, has good chemical resistance and heat resistance, and can achieve the original plasticity at high temperatures. And repairability.
本發明之一實施方式係在於提供一種增韌可塑性熱固型樹脂的製備方法,其包含提供一大分子起始劑、進行一合成步驟以及進行一交聯固化步驟。其中,前述大分子起始劑具有如式(I)或式(II)所示之一結構:Br-PnBA-Br 式(I)、h-P(nBA-co-BPEA) 式(II), 其中PnBA代表聚丙烯酸丁酯,h代表超分支化(hyperbranched),co代表共聚合。前述合成步驟係將一甲基丙烯酸甲酯單體以及一甲基丙烯酸縮水甘油酯單體與大分子起始劑經由原子轉移自由基聚合法合成,以獲得一共聚物。前述交聯固化步驟係將共聚物與一雙官能交聯劑在一酯交換催化劑的催化下反應,以獲得一增韌可塑性熱固型樹脂。 One embodiment of the present invention is to provide a method for preparing toughened plastic thermosetting resin, which includes providing a macromolecular initiator, performing a synthesis step, and performing a crosslinking curing step. Wherein, the aforementioned macromolecular initiator has a structure as shown in formula (I) or formula (II): Br-PnBA-Br formula (I), h -P(nBA- co -BPEA) formula (II), Wherein PnBA stands for polybutyl acrylate, h stands for hyperbranched, and co stands for copolymerization. The aforementioned synthesis step is to synthesize a methyl methacrylate monomer, a glycidyl methacrylate monomer and a macromolecular initiator through an atom transfer radical polymerization method to obtain a copolymer. The aforementioned cross-linking curing step is to react the copolymer with a bifunctional cross-linking agent under the catalysis of an ester exchange catalyst to obtain a toughened plastic thermosetting resin.
依據前述實施方式之增韌可塑性熱固型樹脂的製備方法,其中所述共聚物的分子量可為23000至40000。 According to the method for preparing toughened plastic thermosetting resin according to the foregoing embodiment, the molecular weight of the copolymer may be 23,000 to 40,000.
依據前述實施方式之增韌可塑性熱固型樹脂的製備方法,其中所述共聚物可為一三嵌段共聚物。 According to the method for preparing the toughened plastic thermosetting resin according to the foregoing embodiment, the copolymer may be a triblock copolymer.
依據前述實施方式之增韌可塑性熱固型樹脂的製備方法,其中所述三嵌段共聚物具有如式(III)所示之一結構:A-B-A 式(III),其中A為甲基丙烯酸甲酯單體以及甲基丙烯酸縮水甘油酯單體所聚合之無規共聚物嵌段,B為聚丙烯酸丁酯嵌段。 According to the preparation method of the toughened plastic thermosetting resin according to the foregoing embodiment, the triblock copolymer has a structure as shown in formula (III): ABA formula (III), wherein A is methyl methacrylate A random copolymer block polymerized by monomers and glycidyl methacrylate monomers, B is a polybutyl acrylate block.
依據前述實施方式之增韌可塑性熱固型樹脂的製備方法,其中所述共聚物可為一具超分支核之星狀共聚物。 According to the preparation method of the toughened plastic thermosetting resin according to the foregoing embodiment, the copolymer may be a star-shaped copolymer with a hyperbranched core.
依據前述實施方式之增韌可塑性熱固型樹脂的製備方法,其中所述具超分支核之星狀共聚物可包含一中心單元以及複數手臂單元,且手臂單元接枝於中心單元。 According to the preparation method of the toughened plastic thermosetting resin of the foregoing embodiment, the star-shaped copolymer with a hyperbranched core may include a central unit and a plurality of arm units, and the arm units are grafted to the central unit.
依據前述實施方式之增韌可塑性熱固型樹脂的製備方法,其中所述中心單元係由式(II)所示之大分子引發劑與十二碳烷硫醇反應而得,而手臂單元係甲基丙烯酸甲酯單體以及甲基丙烯酸縮水甘油酯單體所聚合之無規共聚物。 According to the method for preparing toughened plastic thermosetting resin according to the foregoing embodiment, the central unit is obtained by reacting the macroinitiator represented by formula (II) with dodecyl mercaptan, and the arm unit is a Random copolymer of methyl acrylate monomer and glycidyl methacrylate monomer.
依據前述實施方式之增韌可塑性熱固型樹脂的製備方法,其中所述雙官能交聯劑可為已二酸或二胺。 According to the preparation method of the toughened plastic thermosetting resin according to the foregoing embodiment, the bifunctional crosslinking agent may be adipic acid or diamine.
本發明之另一實施方式係在於提供一種增韌可塑性熱固型樹脂,所述增韌可塑性熱固型樹脂為由前述製備方法製備而得。 Another embodiment of the present invention is to provide a toughened plastic thermosetting resin, which is prepared by the aforementioned preparation method.
依據前述實施方式之增韌可塑性熱固型樹脂,其中所述增韌可塑性熱固型樹脂的應變可為1.50%至3.30%。 According to the toughened plastic thermosetting resin of the foregoing embodiment, the strain of the toughened plastic thermosetting resin may be 1.50% to 3.30%.
藉此,本發明利用原子轉移自由基聚合法合成出具有聚丙烯酸丁酯之大分子起始劑,再透過鹵素交換與原子轉移自由基聚合法與甲基丙烯酸甲酯單體及甲基丙烯酸縮水甘油酯單體進行鏈延伸,合成出不同構形之三嵌段共聚物以及具超分支核之星狀共聚物,再將共聚物、交聯劑與酯交換催化劑製備成具有共價適應網路的增韌可塑性熱固型樹脂,使本發明之增韌可塑性熱固型樹脂可改善本身的脆性並達到增韌(Toughening)效果。 Thus, the present invention uses the atom transfer radical polymerization method to synthesize the macromolecular initiator with polybutyl acrylate, and then shrinks it with methyl methacrylate monomer and methacrylic acid through the halogen exchange and atom transfer radical polymerization method. The glyceride monomer chain is extended to synthesize triblock copolymers with different configurations and star-shaped copolymers with hyperbranched cores, and then the copolymers, crosslinkers and transesterification catalysts are prepared into covalently adapted networks The toughened plastic thermosetting resin of the present invention can improve the brittleness of the toughened plastic thermosetting resin of the present invention and achieve a toughening effect.
100‧‧‧增韌可塑性熱固型樹脂的製備方法 100‧‧‧The preparation method of toughened plastic thermosetting resin
110、120、130‧‧‧步驟 110, 120, 130‧‧‧step
為讓本發明之上述和其他目的、特徵、優點與實施例能更明顯易懂,所附圖式之說明如下: In order to make the above and other objectives, features, advantages and embodiments of the present invention more comprehensible, the description of the accompanying drawings is as follows:
第1圖係繪示依照本發明之一實施方式之一種增韌可塑性熱固型樹脂的製備方法的步驟流程圖; Figure 1 is a flow chart showing the steps of a method for preparing a toughened plastic thermosetting resin according to an embodiment of the present invention;
第2A圖係繪示合成例1之ln(M0/M)與時間的關係圖; Figure 2A is a diagram showing the relationship between ln(M 0 /M) and time of Synthesis Example 1;
第2B圖係繪示合成例1之分子量分布與轉化率的關係圖; Figure 2B is a graph showing the relationship between molecular weight distribution and conversion rate of Synthesis Example 1;
第2C圖係繪示合成例1之分子量與轉化率的關係圖; Figure 2C is a graph showing the relationship between molecular weight and conversion rate of Synthesis Example 1;
第2D圖係繪示合成例1之分子量隨時間分布圖; Figure 2D shows the molecular weight distribution of Synthesis Example 1 over time;
第3A圖係繪示合成例2之ln(M0/M)與時間的關係圖; Figure 3A is a diagram showing the relationship between ln(M 0 /M) and time of Synthesis Example 2;
第3B圖係繪示合成例2之分子量分布與轉化率的關係圖; Figure 3B is a graph showing the relationship between molecular weight distribution and conversion rate of Synthesis Example 2;
第3C圖係繪示合成例2之分子量與轉化率的關係圖; Figure 3C is a graph showing the relationship between molecular weight and conversion rate of Synthesis Example 2;
第3D圖係繪示合成例2之分子量隨時間分布圖; The 3D diagram shows the molecular weight distribution diagram of Synthesis Example 2 over time;
第4圖係繪示比較例1及合成例2的1H-NMR光譜圖; Figure 4 shows the 1 H-NMR spectrum of Comparative Example 1 and Synthesis Example 2;
第5A圖係繪示tBCP之ln(M0/M)與時間的關係圖; Figure 5A shows the relationship between ln(M 0 /M) and time of tBCP;
第5B圖係繪示tBCP之分子量分布與轉化率的關係圖; Figure 5B shows the relationship between the molecular weight distribution of tBCP and the conversion rate;
第5C圖係繪示tBCP之分子量與轉化率的關係圖; Figure 5C shows the relationship between the molecular weight of tBCP and the conversion rate;
第5D圖係繪示tBCP之分子量隨時間分布圖; Figure 5D shows the molecular weight distribution of tBCP over time;
第6圖係繪示合成例3至合成例5的1H-NMR光譜圖; Figure 6 shows the 1 H-NMR spectrum of Synthesis Example 3 to Synthesis Example 5;
第7A圖係繪示hsCP之ln(M0/M)與時間的關係圖; Figure 7A shows the relationship between ln(M 0 /M) and time of hsCP;
第7B圖係繪示hsCP之分子量分布與轉化率的關係圖; Figure 7B shows the relationship between the molecular weight distribution of hsCP and the conversion rate;
第7C圖係繪示hsCP之分子量與轉化率的關係圖; Figure 7C shows the relationship between the molecular weight of hsCP and the conversion rate;
第7D圖係繪示hsCP之分子量隨時間分布圖; Figure 7D shows the distribution of hsCP molecular weight over time;
第8圖係繪示合成例6至合成例8的1H-NMR光譜圖; Figure 8 shows the 1 H-NMR spectrum of Synthesis Example 6 to Synthesis Example 8;
第9圖係繪示固化前與固化後之增韌可塑性熱固型樹脂 的FTIR圖; Figure 9 shows the toughened plastic thermosetting resin before and after curing FTIR diagram;
第10圖係繪示實施例1至實施例6的TGA分析圖; Figure 10 shows the TGA analysis diagram of Example 1 to Example 6;
第11圖係繪示實施例1至實施例3的DSC分析圖; Figure 11 shows the DSC analysis chart of Example 1 to Example 3;
第12圖係繪示實施例4至實施例6的DSC分析圖; Figure 12 shows the DSC analysis chart of Example 4 to Example 6;
第13圖係繪示實施例1、實施例3、實施例4以及實施例6的DMA分析圖; Figure 13 shows the DMA analysis diagrams of Example 1, Example 3, Example 4, and Example 6;
第14圖係繪示實施例1至實施例3的SAXS圖; Figure 14 shows the SAXS diagram of Example 1 to Example 3;
第15圖係繪示實施例4至實施例6的SAXS圖; Figure 15 shows the SAXS diagram of Example 4 to Example 6;
第16圖係繪示實施例1至實施例6的應力應變圖; Figure 16 shows the stress and strain diagrams of Example 1 to Example 6;
第17圖係繪示比較例2、比較例3、實施例3以及實施例6的應力應變圖; Figure 17 shows the stress and strain diagrams of Comparative Example 2, Comparative Example 3, Example 3, and Example 6;
第18圖係繪示實施例3、實施例5以及實施例6隨時間裂紋變化之POM圖; Fig. 18 shows the POM diagram of the cracks in Example 3, Example 5 and Example 6 over time;
第19圖係繪示實施例3、實施例5以及實施例6之修復程度隨時間變化圖;以及 Figure 19 is a graph showing the degree of repair of Example 3, Example 5 and Example 6 over time; and
第20A圖以及第20B圖係繪示增韌可塑性熱固型樹脂的可塑性示意圖。 Figures 20A and 20B are schematic diagrams showing the plasticity of the toughened plastic thermosetting resin.
下述將更詳細討論本發明各實施方式。然而,此實施方式可為各種發明概念的應用,可被具體實行在各種不同的特定範圍內。特定的實施方式是僅以說明為目的,且不受限於揭露的範圍。 The various embodiments of the present invention will be discussed in more detail below. However, this embodiment can be an application of various inventive concepts and can be implemented in various specific ranges. The specific implementation is for illustrative purposes only, and is not limited to the scope of disclosure.
請參考第1圖,其係繪示本發明之一實施方式之一種增韌可塑性熱固型樹脂的製備方法100的步驟流程圖。第1圖中,增韌可塑性熱固型樹脂的製備方法100包含步驟110、步驟120以及步驟130。
Please refer to FIG. 1, which is a flowchart of a
步驟110為提供一大分子起始劑,其具有如式(I)或式(II)所示之一結構:Br-PnBA-Br 式(I)、h-P(nBA-co-BPEA) 式(II),其中PnBA代表聚丙烯酸丁酯,h代表超分支化,co代表共聚合。詳細來說,式(I)及式(II)之大分子起始劑係分別由二溴代異丁酸乙二醇酯(2f-BiB)及2-((2-溴丙醯基)氧基)丙烯酸乙酯(Inimer BPEA)之雙官能基起始劑與一丙烯酸丁酯單體透過原子轉移自由基聚合法(Atom transfer radical polymerization,ATRP)所合成而得。 Step 110 is to provide a macromolecular initiator, which has a structure as shown in formula (I) or formula (II): Br-PnBA-Br formula (I), h- P(nBA- co- BPEA) formula (II), where PnBA represents polybutyl acrylate, h represents hyperbranched, and co represents copolymerization. In detail, the macromolecular initiators of formula (I) and formula (II) are respectively composed of ethylene dibromoisobutyrate (2f-BiB) and 2-((2-bromopropionyl) oxygen Inimer BPEA (Inimer BPEA) bifunctional initiator and a butyl acrylate monomer are synthesized by Atom transfer radical polymerization (ATRP).
步驟120為進行一合成步驟,其係將一甲基丙烯酸甲酯單體(methyl methacrylate,MMA)以及一甲基丙烯酸縮水甘油酯單體(glycidyl methacrylate,GMA)與上述之大分子起始劑經由ATRP合成,以獲得一共聚物,其中ATRP之聚合方法可實現聚合反應中的可控性,能夠精準的控制聚合物的分子量及窄的PDI,故本發明之共聚物的分子量可控制在23000至40000之間,而PDI值則可小於1.3。 Step 120 is a synthesis step in which a methyl methacrylate (MMA) and a glycidyl methacrylate (GMA) monomer and the aforementioned macromolecular initiator are passed through ATRP synthesis to obtain a copolymer, wherein the polymerization method of ATRP can realize the controllability in the polymerization reaction, can accurately control the molecular weight of the polymer and the narrow PDI, so the molecular weight of the copolymer of the present invention can be controlled from 23,000 to 23,000. Between 40,000, and the PDI value can be less than 1.3.
本發明之共聚物可為一三嵌段共聚物(triblock copolymer,以下簡稱tBCP),其係由MMA單體 以及GMA單體與式(I)之大分子起始劑經由ATRP共聚而得,並具有如式(III)所示之一結構:A-B-A 式(III),其中A為MMA單體以及GMA單體所聚合之無規共聚物嵌段,而B為聚丙烯酸丁酯嵌段。具體地,本發明之三嵌段共聚物的完整表示式為P(MMA-r-GMA)-b-PnBA-b-P(MMA-r-GMA),其中r代表隨機分布(random),b代表嵌段(block)。 The copolymer of the present invention can be a triblock copolymer (triblock copolymer, hereinafter referred to as tBCP), which is obtained by copolymerizing MMA monomer and GMA monomer with the macromolecular initiator of formula (I) through ATRP, and It has a structure as shown in formula (III): ABA formula (III), where A is a random copolymer block polymerized by MMA monomer and GMA monomer, and B is a polybutyl acrylate block. Specifically, the complete expression of the triblock copolymer of the present invention is P(MMA- r- GMA) -b- PnBA- b- P(MMA- r- GMA), where r represents random distribution (random), b Represents a block.
另外,本發明之共聚物亦可為一具超分支核之星狀共聚物(hyperbranched core star copolymer,以下簡稱hsCP),其係由MMA單體以及GMA單體與式(II)之大分子起始劑經由ATRP共聚而得。詳細來說,本發明之具超分支核之星狀共聚物包含一中心單元以及複數手臂單元,且手臂單元接枝於中心單元,其中中心單元係由式(II)之大分子引發劑與十二碳烷硫醇反應而得,而手臂單元則是MMA單體以及GMA單體所聚合之無規共聚物。具體地,本發明之具超分支核之星狀共聚物的完整表示式為s[P(MMA-r-GMA)-h-P(nBA-co-BPEA)],其中s代表星狀(star),r、h以及co所代表之涵義如上所述,在此不另贅述。 In addition, the copolymer of the present invention may also be a hyperbranched core star copolymer (hsCP), which is composed of MMA monomers and GMA monomers and macromolecules of formula (II). The starting agent is obtained by ATRP copolymerization. In detail, the star-shaped copolymer with a hyperbranched core of the present invention includes a central unit and a plurality of arm units, and the arm units are grafted to the central unit, wherein the central unit is composed of a macromolecular initiator of formula (II) and ten It is obtained by the reaction of two-carbon alkanethiol, and the arm unit is a random copolymer of MMA monomer and GMA monomer. Specifically, the complete expression of the star-shaped copolymer with a hyperbranched core of the present invention is s[P(MMA- r- GMA) -h- P(nBA- co- BPEA)], where s represents star ), the meanings represented by r , h, and co are as described above, and will not be repeated here.
步驟130為進行一交聯固化步驟,其係將所述共聚物與一雙官能交聯劑在一酯交換催化劑的催化下反應,以獲得增韌可塑性熱固型樹脂,其中本發明之雙官能交聯劑可為已二酸或二胺。詳細的說,步驟130係利用共聚物 中的甲基丙烯酸縮水甘油酯作為交聯點,再使用雙官能交聯劑以及酯交換催化劑,使共聚物固化交聯形成具有可逆交換鏈結的網路結構,因為交聯網路的關係,可使材料本身具有良好的耐熱性以及機械性質。 Step 130 is a crosslinking curing step, which is to react the copolymer and a bifunctional crosslinking agent under the catalysis of an ester exchange catalyst to obtain a toughened plastic thermosetting resin, wherein the bifunctional crosslinking agent of the present invention The crosslinking agent can be adipic acid or diamine. In detail, step 130 uses copolymers Glycidyl methacrylate is used as the cross-linking point, and then bifunctional cross-linking agent and transesterification catalyst are used to cure and cross-link the copolymer to form a network structure with reversible exchange linkages. The material itself has good heat resistance and mechanical properties.
本發明進一步提供一種由前述製備方法製備而成之增韌可塑性熱固型樹脂,其係將帶有PnBA之軟鏈段的共聚物製成增韌可塑性熱固型樹脂,藉由PMMA與PnBA主鏈段間的不相容性以形成奈米結構,並提升樹脂的韌性。本發明之增韌可塑性熱固型樹脂與純PMMA相比,具有較高的應變,其可為1.50%至3.30%。另外,本發明之增韌可塑性熱固型樹脂亦具有良好的耐化性以及耐熱性,且於高溫下,可藉由動態共價交換反應使得交聯網路內的共價鍵進行酯交換反應而達到樹脂的可塑性及修復性。 The present invention further provides a toughened plastic thermosetting resin prepared by the aforementioned preparation method, which is a toughened plastic thermosetting resin made of a copolymer with a soft segment of PnBA, which is mainly composed of PMMA and PnBA The incompatibility between the chain segments can form a nanostructure and improve the toughness of the resin. Compared with pure PMMA, the toughened plastic thermosetting resin of the present invention has a higher strain, which can be 1.50% to 3.30%. In addition, the toughened plastic thermosetting resin of the present invention also has good chemical resistance and heat resistance, and at high temperatures, the covalent bonds in the cross-linking network can undergo transesterification by dynamic covalent exchange reaction. To achieve the plasticity and repairability of the resin.
本發明之合成例1為式(I)之大分子起始劑,其合成方法係將0.5mmol的2f-BiB、200mmol的nBA單體、1.5mmol的配體PMDETA、0.8mmol的Cu0、0.2mmol的CuBr2及作為內標準品的苯甲醚依序加入舒倫克瓶中,冷凍解凍泵循環法數次,直到無氣泡冒出後氮氣回壓,放入85℃油鍋反應,並分別在適當時間取樣。反應完成後,以四氫呋喃稀釋,並以中性氧化鋁去除銅觸媒,利用-50℃冰 甲醇再沉澱,接著將沉澱物收集,再以40℃真空烘箱除去殘留的溶劑,所得之產物為透明黏稠液體之合成例1。合成例1的反應方程式如下表一所示。 Synthesis Example 1 of the present invention is a macromolecular initiator of formula (I), and its synthesis method is to combine 0.5mmol of 2f-BiB, 200mmol of nBA monomer, 1.5mmol of ligand PMDETA, 0.8mmol of Cu 0 , 0.2 Add mmol of CuBr 2 and anisole as the internal standard into Schlenk bottles in order, freeze and thaw the pump cycle several times, until there are no bubbles coming out of the nitrogen back pressure, put them into the 85 ℃ oil pan to react, and respectively Take samples at appropriate times. After the reaction is completed, dilute with tetrahydrofuran, remove the copper catalyst with neutral alumina, re-precipitate with ice methanol at -50°C, then collect the precipitate, and remove the remaining solvent in a vacuum oven at 40°C. The resulting product is transparent Synthesis Example 1 of Viscous Liquid. The reaction equation of Synthesis Example 1 is shown in Table 1 below.
請參閱第2A圖、第2B圖、第2C圖以及第2D圖,其中第2A圖係繪示合成例1之ln(M0/M)與時間的關係圖,M0為單體的起始量,M為單體在某個時刻的量。第2B圖係繪示合成例1之分子量分布與轉化率的關係圖,第2C圖係繪示合成例1之分子量與轉化率的關係圖,第2D圖係繪示合成例1之分子量隨時間分布圖。由第2A圖至第2D圖的結果可知,利用2f-BiB起始劑在85℃聚合nBA的聚合反應能夠維持穩定的成長,且在合成的過程中,PDI均控制在1.2以下,可說明所合成之合成例1為式(I)所示之大分子起始劑。 Please refer to Figure 2A, Figure 2B, Figure 2C, and Figure 2D. Figure 2A shows the relationship between ln (M 0 /M) and time of Synthesis Example 1, and M 0 is the start of the monomer The amount, M is the amount of the monomer at a certain moment. Figure 2B shows the relationship between molecular weight distribution and conversion rate of Synthesis Example 1, Figure 2C shows the relationship between molecular weight and conversion rate of Synthesis Example 1, and Figure 2D shows the relationship between molecular weight of Synthesis Example 1 and time. Distribution. From the results in Figures 2A to 2D, it can be seen that the polymerization reaction of nBA polymerized at 85°C with 2f-BiB initiator can maintain stable growth, and during the synthesis process, PDI is controlled below 1.2, which can explain Synthesis Synthesis Example 1 is the macromolecular initiator represented by formula (I).
本發明之合成例2為式(II)之大分子起始劑,其係先將10mmol的Inimer BPEA、100mmol的nBA單體、3.3mmol的配體bpy、0.11mmol的CuBr2及作為內標準品的苯甲醚依序加入舒倫克瓶中,冷凍解凍泵循環法數次,直到無氣泡冒出後加入1.1mmol的CuBr,並再冷凍解凍泵循環法數次,直到無氣泡冒出後氮氣回壓,放入85℃油鍋 反應,並分別在適當時間取樣。反應完成後,以四氫呋喃稀釋,並以中性氧化鋁去除銅觸媒,利用-50℃冰甲醇再沉澱,接著將沉澱物收集,再以40℃真空烘箱除去殘留的溶劑,所得之產物為淡黃色黏稠液體之比較例1,其為hbP(BPEA-r-nBA)。之後將0.5mmol的比較例1、0.75mmol的安息香雙甲醚、0.5mmol的十二碳烷硫醇與30mL的四氫呋喃加入舒倫克瓶中,冷凍解凍泵循環法數次,直到無氣泡冒出後氮氣回壓,並在室溫下以UV燈照射2小時,反應完成後利用-50℃冰甲醇再沉澱,接著將沉澱物收集,再以40℃真空烘箱除去殘留的溶劑,所得之產物為淡黃色黏稠液體之合成例2。合成例2的反應方程式如下表二所示。 Synthesis Example 2 of the present invention is a macromolecular initiator of formula (II), which is to first use 10mmol of Inimer BPEA, 100mmol of nBA monomer, 3.3mmol of ligand bpy, 0.11mmol of CuBr 2 and the internal standard Add the anisole to the Schlenk bottle in sequence, freeze and thaw the pump circulation method several times, add 1.1mmol CuBr until no bubbles emerge, and then freeze and thaw the pump circulation method several times, until no bubbles emerge after the nitrogen Back pressure, put it in an oil pan at 85°C for reaction, and take samples at appropriate times. After the reaction is completed, dilute with tetrahydrofuran, remove the copper catalyst with neutral alumina, re-precipitate with ice methanol at -50°C, then collect the precipitate, and remove the remaining solvent in a vacuum oven at 40°C. The resulting product is light Comparative example 1 of yellow viscous liquid is hbP (BPEA- r- nBA). Then add 0.5mmol of Comparative Example 1, 0.75mmol of benzoin dimethyl ether, 0.5mmol of dodecane mercaptan and 30mL of tetrahydrofuran into the Schlenk bottle, freeze-thaw pump circulation method several times, until no bubbles emerge After the nitrogen back pressure, and irradiate with UV lamp at room temperature for 2 hours. After the reaction is completed, use -50℃ ice methanol to reprecipitate, then collect the precipitate, and then remove the residual solvent in a 40℃ vacuum oven. The resulting product is Synthesis example 2 of light yellow viscous liquid. The reaction equation of Synthesis Example 2 is shown in Table 2 below.
請參閱第3A圖、第3B圖、第3C圖以及第3D圖,其中第3A圖係繪示合成例2之ln(M0/M)與時間的關係圖,第3B圖係繪示合成例2之分子量分布與轉化率的關係圖,第3C圖係繪示合成例2之分子量與轉化率的關係圖,第3D圖係繪示合成例2之分子量隨時間分布圖。由第3A圖至 第3D圖的結果可知,利用Inimer BPEA在85℃聚合nBA的聚合反應能夠維持穩定的成長,且在合成的過程中,高分子均為單分佈,可說明所合成之合成例2為式(II)所示之大分子起始劑。 Please refer to Figure 3A, Figure 3B, Figure 3C, and Figure 3D. Figure 3A shows the relationship between ln(M 0 /M) and time of Synthesis Example 2, and Figure 3B shows the synthesis example. Figure 2 shows the relationship between the molecular weight distribution and the conversion rate. Figure 3C shows the relationship between the molecular weight of Synthesis Example 2 and the conversion rate. Figure 3D shows the molecular weight distribution of Synthesis Example 2 over time. From the results in Figure 3A to Figure 3D, it can be seen that the polymerization reaction using Inimer BPEA to polymerize nBA at 85°C can maintain stable growth, and during the synthesis process, the polymers are all distributed uniformly, which can illustrate the synthesis example synthesized 2 is the macromolecular initiator represented by formula (II).
請參閱第4圖,其係繪示比較例1及合成例2的1H-NMR光譜圖,且由第4圖的結果可知,比較例1之末端乙烯基(a1+a2)與十二碳烷硫醇經過UV光照射下進行加成反應後,所得之合成例2中的末端乙烯基訊號消失,可證明合成例2成功接上長碳鏈。 Please refer to Figure 4, which shows the 1 H-NMR spectra of Comparative Example 1 and Synthesis Example 2, and from the results in Figure 4, it can be seen that the terminal vinyl group (a 1 +a 2 ) of Comparative Example 1 and ten After the addition reaction of dicarbanethiol under UV light irradiation, the terminal vinyl signal in the obtained synthesis example 2 disappears, which can prove that the synthesis example 2 has successfully connected the long carbon chain.
本發明之合成例3至合成例5為三嵌段共聚物(tBCP),合成例6至合成例8為具超分支核之星狀共聚物(hsCP),上述共聚物之合成方式係將0.02mmol的大分子起始劑、7.92mmol的MMA單體、1.08mmol的GMA單體、0.06mmol的配體dNbpy、0.02mmol的Cu0、0.02mmol的CuCl2及作為內標準品的苯甲醚依序加入舒倫克瓶中,冷凍解凍泵循環法數次,直到無氣泡冒出後氮氣回壓,放入80℃油鍋反應,並分別在適當時間取樣。反應完成後,將聚合物以四氫呋喃稀釋,並以中性氧化鋁去除銅觸媒,利用-50℃冰甲醇再沉澱,接著將沉澱物收集,再以40℃真空烘箱除去殘留的溶劑,所得之產物為白色固體,其中合成例3至合成例5所使用的大分子起始劑為合成例1,合成例6至合成例8所使用的大分子起始劑為合成例2。 Synthesis Example 3 to Synthesis Example 5 of the present invention are triblock copolymers (tBCP), Synthesis Example 6 to Synthesis Example 8 are star copolymers with hyperbranched cores (hsCP). The synthesis method of the above copolymers is 0.02 mmol of macromolecular initiator, 7.92 mmol of MMA monomer, 1.08 mmol of GMA monomer, 0.06 mmol of ligand dNbpy, 0.02 mmol of Cu 0 , 0.02 mmol of CuCl 2 and anisole as the internal standard Put it into a Schlenk bottle in sequence, freeze and thaw the pump for several cycles, until there are no bubbles coming out of the nitrogen back pressure, put it in a 80°C oil pot for reaction, and take samples at appropriate times. After the completion of the reaction, the polymer was diluted with tetrahydrofuran, and the copper catalyst was removed with neutral alumina, and then reprecipitated with ice methanol at -50°C. Then the precipitate was collected, and the remaining solvent was removed in a vacuum oven at 40°C. The product is a white solid, wherein the macromolecular initiator used in Synthesis Example 3 to Synthesis Example 5 is Synthesis Example 1, and the macromolecular initiator used in Synthesis Example 6 to Synthesis Example 8 is Synthesis Example 2.
請參閱第5A圖、第5B圖、第5C圖以及第5D圖,其中第5A圖係繪示tBCP之ln(M0/M)與時間的關係圖,第5B圖係繪示tBCP之分子量分布與轉化率的關係圖,第5C圖係繪示tBCP之分子量與轉化率的關係圖,第5D圖係繪示tBCP之分子量隨時間分布圖。由第5A圖至第5D圖的結果可知,利用合成例1之大分子起始劑在80℃聚合MMA及GMA的聚合反應能夠維持穩定的成長,且在合成的過程中,PDI均控制在1.3左右,可說明所合成之合成例3至合成例5為tBCP。 Please refer to Figure 5A, Figure 5B, Figure 5C and Figure 5D. Figure 5A shows the relationship between ln(M 0 /M) of tBCP and time, and Figure 5B shows the molecular weight distribution of tBCP. Figure 5C shows the relationship between the molecular weight of tBCP and the conversion rate. Figure 5D shows the molecular weight distribution of tBCP over time. From the results in Figures 5A to 5D, it can be seen that the polymerization reaction of using the macromolecular initiator of Synthesis Example 1 to polymerize MMA and GMA at 80°C can maintain stable growth, and during the synthesis process, the PDI is controlled at 1.3 From left to right, it can be explained that the synthesized synthesis example 3 to synthesis example 5 are tBCP.
請參閱第6圖,其係繪示合成例3至合成例5的1H-NMR光譜圖,上述1H-NMR光譜圖皆在CDCl3溶液中分析而得,且a、b與c分別代表GMA單體、MMA單體以及nBA單體的特徵峰。由第6圖的結果可確定合成例3至合成例5之出料比,並且利用GPC分析確認其分子量以及PDI值,GC量測單體轉化率,其中合成例3至合成例5的進料比、出料比、轉化率、分子量以及PDI值如下表三所示。 Please refer to Figure 6, which shows the 1 H-NMR spectra of Synthesis Example 3 to Synthesis Example 5. The above 1 H-NMR spectra are all analyzed in CDCl 3 solution, and a, b and c respectively represent The characteristic peaks of GMA monomer, MMA monomer and nBA monomer. From the results in Figure 6, the output ratio of Synthesis Example 3 to Synthesis Example 5 can be determined, and the molecular weight and PDI value can be confirmed by GPC analysis, and the monomer conversion rate can be measured by GC. The feed rate of Synthesis Example 3 to Synthesis Example 5 The ratio, output ratio, conversion rate, molecular weight and PDI value are shown in Table 3 below.
請參閱第7A圖、第7B圖、第7C圖以及第7D圖,其中第7A圖係繪示hsCP之ln(M0/M)與時間的關係圖,第7B圖係繪示hsCP之分子量分布與轉化率的關係圖,第7C圖係繪示hsCP之分子量與轉化率的關係圖,第7D圖係繪示hsCP之分子量隨時間分布圖。由第7A圖至第7D圖的結果可知,利用合成例2之大分子起始劑在80℃聚合MMA及GMA的聚合反應能夠維持穩定的成長,且在合成的過程中,PDI均控制在1.5以下,可說明所合成之合成例6至合成例8為hsCP。 Please refer to Figure 7A, Figure 7B, Figure 7C and Figure 7D. Figure 7A shows the relationship between hsCP ln(M 0 /M) and time, and Figure 7B shows the molecular weight distribution of hsCP. Figure 7C shows the relationship between the molecular weight of hsCP and the conversion rate, and Figure 7D shows the molecular weight distribution of hsCP over time. From the results in Figure 7A to Figure 7D, it can be seen that the polymerization reaction of using the macromolecular initiator of Synthesis Example 2 to polymerize MMA and GMA at 80°C can maintain stable growth, and during the synthesis process, the PDI is controlled at 1.5 Hereinafter, it can be explained that the synthesized synthesis example 6 to synthesis example 8 are hsCP.
請參閱第8圖,其係繪示合成例6至合成例8的1H-NMR光譜圖,上述1H-NMR光譜圖皆在CDCl3溶液中分析而得,且a、b與c分別代表GMA單體、MMA單體以及nBA單體的特徵峰。由第8圖的結果可確定合成例6至合成例8之出料比,並且利用GPC分析確認其分子量以及PDI值,GC量測其單體轉化率,其中合成例6至合成例8的進料比、出料比、轉化率、分子量以及PDI值如下表四所示。 Please refer to Fig. 8, which shows the 1 H-NMR spectra of Synthesis Example 6 to Synthesis Example 8. The above 1 H-NMR spectra are all analyzed in CDCl 3 solution, and a, b, and c respectively represent The characteristic peaks of GMA monomer, MMA monomer and nBA monomer. From the results in Figure 8, the output ratio of Synthesis Example 6 to Synthesis Example 8 can be determined, and its molecular weight and PDI value can be confirmed by GPC analysis, and its monomer conversion rate can be measured by GC. The progress of Synthesis Example 6 to Synthesis Example 8 The feed ratio, output ratio, conversion rate, molecular weight and PDI value are shown in Table 4 below.
本發明之實施例1至實施例6係分別利用合成例3至合成例8所製備而得之增韌可塑性熱固型樹脂,其製備方法係先以1H-NMR鑑定出1g的合成例3至合成例8中含有多少PGMA莫耳比,接著秤取1g的合成例3至合成例8、二分之一之PGMA莫耳比的己二酸交聯劑與5%之PGMA莫耳比的Zn(acac)2酯交換催化劑加入樣品瓶中以四氫呋喃(THF)溶解,配成固含量為25%的溶液。之後,均勻塗布在鐵氟龍紙中並放置於室溫24小時,再以80℃、100℃以及120℃分別熱壓30分鐘進行預熱,接著於真空烘箱以150℃、180℃分別加熱60分鐘完成固化,結束後待冷卻取出。 Examples 1 to 6 of the present invention are based on the toughened plastic thermosetting resins prepared in Synthesis Example 3 to Synthesis Example 8, respectively. The preparation method is that 1 g of Synthesis Example 3 is identified by 1 H-NMR. To how much PGMA molar ratio is contained in Synthesis Example 8, then weigh 1g of Synthesis Example 3 to Synthesis Example 8, half of the PGMA molar ratio of adipic acid crosslinking agent and 5% PGMA molar ratio Zn(acac) 2 transesterification catalyst was added to the sample bottle and dissolved in tetrahydrofuran (THF) to prepare a solution with a solid content of 25%. After that, it was evenly coated on Teflon paper and placed at room temperature for 24 hours, and then heated at 80°C, 100°C, and 120°C for 30 minutes to preheat, and then heated in a vacuum oven at 150°C and 180°C for 60 minutes. The solidification will be completed within minutes, and then take it out after cooling.
請參閱第9圖,其係繪示固化前與固化後之增韌可塑性熱固型樹脂的FTIR圖。由第9圖的結果可知,環氧基之特徵峰位於908cm-1之位置,其經由固化反應後,環氧基特徵峰的波峰會漸漸消失,說明增韌可塑性熱固型樹脂已完全固化。本發明之增韌可塑性熱固型樹脂可分為二種,分別為tBCP所製備之增韌可塑性熱固型樹脂(以下簡稱tBCP-V)以及hsCP所製備之增韌可塑性熱固型樹脂(以下簡稱hsCP-V)。 Please refer to Figure 9, which shows the FTIR diagram of the toughened plastic thermosetting resin before and after curing. It can be seen from the results in Figure 9 that the characteristic peak of the epoxy group is located at 908 cm -1 . After the curing reaction, the peak of the characteristic peak of the epoxy group gradually disappears, indicating that the toughened plastic thermosetting resin has been completely cured. The toughened plastic thermosetting resin of the present invention can be divided into two types, namely the toughened plastic thermosetting resin prepared by tBCP (hereinafter referred to as tBCP-V) and the toughened plastic thermosetting resin prepared by hsCP (hereinafter referred to as tBCP-V) Referred to as hsCP-V).
請參閱第10圖,其係繪示實施例1至實施例6的TGA分析圖,其中實施例1至實施例6之熱裂解溫度(Td)以及焦炭殘餘率(Char yield)的測量結果如下表五所示。 Please refer to Figure 10, which shows the TGA analysis diagrams of Examples 1 to 6. The measurement results of the thermal cracking temperature (Td) and Char yield of Examples 1 to 6 are shown in the following table Shown in five.
由上述結果可知,tBCP-V以及hsCP-V經由熱重分析儀(TGA)測量後,可以觀察到樹脂之熱裂解5%的溫度在290℃至310℃左右,說明改質後的增韌可塑性熱固型樹脂依然保持良好的熱穩定性。 From the above results, it can be seen that after tBCP-V and hsCP-V are measured by a thermogravimetric analyzer (TGA), it can be observed that the temperature of 5% of the thermal cracking of the resin is around 290°C to 310°C, indicating the toughening plasticity after modification Thermosetting resins still maintain good thermal stability.
請參閱第11圖以及第12圖,其中第11圖係繪示實施例1至實施例3的DSC分析圖,第12圖係繪示實施例4至實施例6的DSC分析圖,其中實施例1至實施例6之玻璃轉換溫度(Tg)的測量結果如下表六所示。 Please refer to Figures 11 and 12. Figure 11 shows the DSC analysis chart of Example 1 to Example 3, and Figure 12 shows the DSC analysis chart of Example 4 to Example 6. The measurement results of the glass transition temperature (Tg) of Example 1 to Example 6 are shown in Table 6 below.
由上述結果可知,經由示差掃描量測法(DSC)測量後,當鏈段中的PGMA組成增加時,因交聯密度的上升使得分子鏈運動受阻,樹脂的Tg會隨PGMA組成增加而上升。另外,比較tBCP-V以及hsCP-V在相近PGMA組成比的情況下,因hsCP-V超分支的幾何構形,網路內的立體阻礙較大,高分子鏈不易糾纏,在進入玻璃轉移區間時,分子鏈運動比線性的tBCP-V更為容易,使得hsCP-V的Tg會低於tBCP-V。 From the above results, it can be seen that after the differential scanning measurement (DSC) measurement, when the PGMA composition in the chain segment increases, the increase in crosslinking density hinders the movement of the molecular chain, and the Tg of the resin increases with the increase in the PGMA composition. In addition, comparing tBCP-V and hsCP-V in the case of similar PGMA composition ratios, due to the geometric configuration of the hsCP-V hyperbranching, the three-dimensional obstacles in the network are relatively large, and the polymer chains are not easy to entangle, and when entering the glass transition zone When the molecular chain moves more easily than linear tBCP-V, the Tg of hsCP-V will be lower than tBCP-V.
另外,利用不同PGMA組成的tBCP-V及hsCP-V樣品(L=15mm,W=5mm),測量動態機械熱分析(DMA)。請參閱第13圖,其係繪示實施例1、實施例3、實施例4以及實施例6的DMA分析圖,而由第13圖的結果可知,不同PGMA組成之tBCP-V及hsCP-V因交聯密度提高使得分子鏈運動受到阻礙,於橡膠態的儲存模數均會隨PGMA組成增加而上升。接著於相同PGMA組成下,因hsCP-V超分支狀的幾何構形,網路內的立體阻礙較大,高分子鏈不易糾纏,分子鏈運動比線性的tBCP-V更為容易,使得hsCP-V於橡膠態時的儲存模數(13.1MPa)會比tBCP-V的儲存模數(40.6MPa)來得低。 In addition, samples of tBCP-V and hsCP-V (L=15mm, W=5mm) composed of different PGMAs were used to measure dynamic mechanical thermal analysis (DMA). Please refer to Figure 13, which shows the DMA analysis diagrams of Example 1, Example 3, Example 4 and Example 6. From the results of Figure 13, it can be seen that tBCP-V and hsCP-V composed of different PGMA As the cross-linking density increases, the movement of molecular chains is hindered, and the storage modulus in the rubber state will increase with the increase of the composition of PGMA. Then under the same PGMA composition, due to the hyperbranched geometric configuration of hsCP-V, the three-dimensional hindrance in the network is greater, the polymer chain is not easy to entangle, and the molecular chain movement is easier than linear tBCP-V, making hsCP- The storage modulus of V in the rubber state (13.1MPa) will be lower than that of tBCP-V (40.6MPa).
為了瞭解於增韌可塑性熱固型樹脂中導入軟鏈段所造成的影響,利用小角度X光散色儀(SAXS),探討改
質後之增韌可塑性熱固型樹脂的內部微結構。請參閱第14圖以及第15圖,其中第14圖係繪示實施例1至實施例3的SAXS圖,第15圖係繪示實施例4至實施例6的SAXS圖。
In order to understand the influence of the introduction of soft segments into the toughened plastic thermosetting resin, a small angle X-ray scatterometer (SAXS) was used to explore
The internal microstructure of toughened plastic thermosetting resin after quality. Please refer to FIG. 14 and FIG. 15. FIG. 14 is a SAXS diagram of
由第14圖以及第15圖的結果可知,不同PGMA比例的tBCP-V在相近PnBA組成(14-20mol%)下,其在交聯過程中,因PMMA鏈段與PnBA鏈段兩者之間不相容,造成PnBA鏈段本身被PMMA排開形成一個微相區域,其第一根q訊號在0.25nm-1的位置,q訊號與其他散射峰比為1:2,判斷為Lamellae結構,並經由公式d=2 π/q,計算出層與層之間的間距為25nm左右。另外,在相近PnBA組成(15-22mol%)下的hsCP-V,因其PDI太寬,PGMA鏈段間的交聯密度與交聯速率不一致,導致實施例4的微結構不明顯,但由實施例5及實施例6可以判斷為Sphere結構,且由於hsCP-V超分支的幾何構形,使得高分子鏈間比較緻密,以致具有比tBCP-V還小的奈米尺度(~15nm)。 From the results in Figure 14 and Figure 15, it can be seen that tBCP-V with different PGMA ratios has a similar composition of PnBA (14-20mol%). During the cross-linking process, due to the difference between the PMMA segment and the PnBA segment Incompatibility, the PnBA segment itself is arranged by PMMA to form a microphase region, the first q signal is at 0.25nm -1 , and the ratio of q signal to other scattering peaks is 1:2, which is judged to be a Lamellae structure. And through the formula d = 2 π/ q , the interval between the layers is calculated to be about 25 nm. In addition, hsCP-V with a similar composition of PnBA (15-22 mol%), because its PDI is too wide, the crosslinking density between the PGMA segments is inconsistent with the crosslinking rate, resulting in the microstructure of Example 4 is not obvious, but Examples 5 and 6 can be judged to be Sphere structures, and due to the geometric configuration of the hyperbranched hsCP-V, the polymer chains are relatively dense, so that they have a smaller nanometer scale (~15nm) than tBCP-V.
請參閱第16圖以及第17圖,其中第16圖係繪示實施例1至實施例6的應力應變圖,第17圖係繪示比較例2、比較例3、實施例3以及實施例6的應力應變圖,比較例2為純PMMA,而比較例3為由ATRP合成之無規共聚物所製備的可塑性熱固型樹脂,其PGMA的組成為21mol%。將實施例1至實施例6之應力、應變及楊氏模數的測量結果如下表七所示。 Please refer to Figure 16 and Figure 17. Figure 16 shows the stress and strain diagrams of Examples 1 to 6, and Figure 17 shows Comparative Example 2, Comparative Example 3, Example 3, and Example 6. In the stress-strain diagram, Comparative Example 2 is pure PMMA, and Comparative Example 3 is a plastic thermosetting resin prepared from a random copolymer synthesized by ATRP, and its PGMA composition is 21 mol%. The measurement results of stress, strain and Young's modulus of Examples 1 to 6 are shown in Table 7 below.
由上述結果可知,利用不同PGMA組成的tBCP-V及hsCP-V樣品(L=60mm,W=3mm)經由拉力測試後,當鏈段中的PGMA組成增加時,可提高了樹脂的交聯密度,其應力及楊氏模數隨PGMA組成增加而上升,但因交聯密度上升而使得軟鏈段於網路中增韌效果變差導致應變下降。然而,比較tBCP-V及hsCP-V在相近PGMA組成比的情況下,由上述微結構分析可知,tBCP-V因其Lamellae的微結構形貌,使整體樹脂的性質變差,以致具有Sphere微結構形貌的hsCP-V應變會比tBCP-V大,但整體來說,於可塑性熱固型樹脂中加入軟鏈段可有效地改善純PMMA的脆性,且由於在鏈段中導入20mol%左右的PnBA軟鏈段,可以發現應變會比改質前的比較例3來得大,展現良好的韌性。 It can be seen from the above results that the tBCP-V and hsCP-V samples (L=60mm, W=3mm) with different PGMA composition after tensile test, when the PGMA composition in the chain segment increases, the crosslink density of the resin can be increased , Its stress and Young's modulus increase with the increase of PGMA composition, but the increase in crosslinking density makes the toughening effect of the soft segment in the network worse and the strain decreases. However, comparing tBCP-V and hsCP-V in the case of similar PGMA composition ratio, it can be seen from the above microstructure analysis that tBCP-V deteriorates the overall resin properties due to its Lamellae microstructure morphology, so that it has Sphere microstructure. The structural morphology of hsCP-V strain is larger than that of tBCP-V, but on the whole, adding soft segments to the plastic thermosetting resin can effectively improve the brittleness of pure PMMA, and because about 20mol% is introduced into the segments For the soft segment of PnBA, it can be found that the strain will be greater than that of Comparative Example 3 before modification, showing good toughness.
為了瞭解不同幾何構形之增韌可塑性熱固型樹脂對修復的表現,將實施例3、實施例5以及實施例6的表面刮一道裂紋,並於150℃熱壓下,觀察裂紋修復程度對時間的變化。 In order to understand the repair performance of toughened and plastic thermosetting resins of different geometric configurations, the surface of Example 3, Example 5 and Example 6 was scratched with a crack, and the crack repair was observed at 150°C under hot pressing. Time changes.
請參閱第18圖、第19圖、第20A圖以及第20B圖,其中第18圖係繪示實施例3、實施例5以及實施例6隨時間裂紋變化之POM圖,第19圖係繪示實施例3、實施例5以及實施例6之修復程度隨時間變化圖,第20A圖以及第20B圖係繪示增韌可塑性熱固型樹脂的可塑性示意圖。由第18圖以及第19圖的結果可知,於相同幾何構形下,具有高PGMA組成之實施例6,因其網路內能交換的鍵結密度比較高,以致其修復效果優於低PGMA組成之實施例5。另外,於相近PGMA組成下,因hsCP-V超分支狀的幾何構形,網路內的立體阻礙較大,高分子鏈不易糾纏,分子鏈運動較線性之tBCP-V更為容易,使得hsCP-V的裂紋修復效果較佳,並由第20A圖以及第20B圖的結果可知,本發明之增韌可塑性熱固型樹脂可展現良好的可塑性。 Please refer to Figure 18, Figure 19, Figure 20A, and Figure 20B. Figure 18 shows the POM diagram of the cracks in Example 3, Example 5 and Example 6 over time, and Figure 19 shows Example 3, Example 5, and Example 6 are graphs of the degree of repair over time. FIG. 20A and FIG. 20B are schematic diagrams showing the plasticity of the toughened plastic thermosetting resin. From the results in Figure 18 and Figure 19, it can be seen that under the same geometric configuration, Example 6 with high PGMA composition has a higher bond density that can be exchanged in the network, so that its repair effect is better than that of low PGMA Composition of Example 5. In addition, with a similar composition of PGMA, due to the hyperbranched geometric configuration of hsCP-V, the three-dimensional hindrance in the network is larger, the polymer chain is not easy to entangle, and the molecular chain movement is easier than linear tBCP-V, making hsCP -V has a better crack repair effect, and it can be seen from the results of Figure 20A and Figure 20B that the toughened plastic thermosetting resin of the present invention can exhibit good plasticity.
綜上所述,本發明提供一種增韌可塑性熱固型樹脂及其製備方法,利用具有PnBA軟鏈段之大分子起始劑與PMMA及GMA單體合成出不同構形之三嵌段共聚物以及具超分支核之星狀共聚物,並將上述共聚物分別交聯固化為增韌可塑性熱固型樹脂。藉由PMMA與PnBA主鏈段間的不相容性以形成奈米結構並增加材料韌性,以改善可塑性熱固型樹脂本身的脆性,且導入PnBA軟鏈段後之增韌可塑性熱固型樹脂依然保有熱穩定性、修復性以及可塑性。 In summary, the present invention provides a toughened plastic thermosetting resin and a preparation method thereof, which use a macromolecular initiator with PnBA soft segment and PMMA and GMA monomers to synthesize triblock copolymers with different configurations And a star-shaped copolymer with a hyperbranched core, and the above-mentioned copolymers are respectively cross-linked and cured into a toughened plastic thermosetting resin. The incompatibility between the main segments of PMMA and PnBA is used to form a nanostructure and increase the toughness of the material to improve the brittleness of the plastic thermosetting resin itself, and the toughening plastic thermosetting resin after the introduction of the PnBA soft segment It still retains thermal stability, repairability and plasticity.
雖然本發明已以實施方式揭露如上,然其並非用以限定本發明,任何熟習此技藝者,在不脫離本發明之精 神和範圍內,當可作各種之更動與潤飾,因此本發明之保護範圍當視後附之申請專利範圍所界定者為準。 Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention. Anyone familiar with the art will not depart from the essence of the present invention. Within the scope of Shenhe, various changes and modifications can be made. Therefore, the scope of protection of the present invention shall be subject to those defined by the attached patent application scope.
100‧‧‧增韌可塑性熱固型樹脂的製備方法 100‧‧‧The preparation method of toughened plastic thermosetting resin
110、120、130‧‧‧步驟 110, 120, 130‧‧‧step
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4230290B2 (en) * | 2003-06-16 | 2009-02-25 | サンメディカル株式会社 | Dental adhesive |
US20170044361A1 (en) * | 2014-04-24 | 2017-02-16 | Arkema France | Composition for manufacturing vitrimer resins of epoxy/anhydride type comprising a polyol |
US20170044307A1 (en) * | 2014-04-24 | 2017-02-16 | Arkema France | Titanium-based catalyst for vitrimer resins of epoxy/anhydride type |
US20170051099A1 (en) * | 2014-04-29 | 2017-02-23 | The Brigham And Women's Hospital, Inc. | Polymeric materials for bio-applications |
CN107474266A (en) * | 2017-07-19 | 2017-12-15 | 浙江大学 | A kind of thermosetting polymer and application with region plasticity |
WO2018039331A1 (en) * | 2016-08-23 | 2018-03-01 | The Regents Of The University Of Colorado, A Body Corporate | Network polymers and methods of making and using same |
WO2019183140A1 (en) * | 2018-03-19 | 2019-09-26 | The Regents Of The University Of Colorado, A Body Corporate | Tough, healable composites displaying stress relaxation at the resin-filler interface |
WO2019213134A1 (en) * | 2018-04-30 | 2019-11-07 | Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College | High performance and recyclable thermoset ink for 3d or 4d printing |
-
2019
- 2019-11-14 TW TW108141440A patent/TWI702235B/en active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4230290B2 (en) * | 2003-06-16 | 2009-02-25 | サンメディカル株式会社 | Dental adhesive |
US20170044361A1 (en) * | 2014-04-24 | 2017-02-16 | Arkema France | Composition for manufacturing vitrimer resins of epoxy/anhydride type comprising a polyol |
US20170044307A1 (en) * | 2014-04-24 | 2017-02-16 | Arkema France | Titanium-based catalyst for vitrimer resins of epoxy/anhydride type |
CN106661196A (en) * | 2014-04-24 | 2017-05-10 | 阿科玛法国公司 | Titanium-based catalyst for VITRIMER resins of expoxy/anhyride type |
US20170051099A1 (en) * | 2014-04-29 | 2017-02-23 | The Brigham And Women's Hospital, Inc. | Polymeric materials for bio-applications |
WO2018039331A1 (en) * | 2016-08-23 | 2018-03-01 | The Regents Of The University Of Colorado, A Body Corporate | Network polymers and methods of making and using same |
CN107474266A (en) * | 2017-07-19 | 2017-12-15 | 浙江大学 | A kind of thermosetting polymer and application with region plasticity |
WO2019183140A1 (en) * | 2018-03-19 | 2019-09-26 | The Regents Of The University Of Colorado, A Body Corporate | Tough, healable composites displaying stress relaxation at the resin-filler interface |
WO2019213134A1 (en) * | 2018-04-30 | 2019-11-07 | Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College | High performance and recyclable thermoset ink for 3d or 4d printing |
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