TW201945353A - Cyclic poly(arylene ether ketone) and production method therefor - Google Patents
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Abstract
Description
本發明係有關環狀聚伸芳基醚酮及其製造方法者。The present invention relates to a cyclic polyarylene ether ketone and a method for producing the same.
聚伸芳基醚酮已於機械物性、耐熱性、耐藥品性優異之產業領域利用於各種用途。又,將聚合物含浸於粒子或纖維等之基材作成複合材料,而可兼具有樹脂所具有之成形性與基材具有之各種特性,而可於各種用途廣泛實用化。其中由聚伸芳基醚酮與玻璃纖維或碳纖維等之強化纖維所成之纖維強化複合材料被作為飛機或汽車用素材而期待日後範圍擴大。Polyarylene ether ketone has been used in various applications in industrial fields having excellent mechanical properties, heat resistance, and chemical resistance. In addition, when a polymer is impregnated with a base material such as particles or fibers to form a composite material, it can have both the moldability of a resin and various characteristics of the base material, and can be widely used in various applications. Among them, a fiber-reinforced composite material made of poly (arylene ether ketone) and reinforcing fibers such as glass fiber or carbon fiber is used as a material for airplanes or automobiles, and is expected to expand in the future.
然而,聚伸芳基醚酮等之超級工程塑膠具有非常高的熔點,難以對纖維素材均一含浸。作為該等聚合物之有效含浸方法,有將比較低分子量之環狀寡聚物在纖維存在下加熱熔融含浸於強化纖維後,使環狀寡聚物藉由開環聚合而轉化成高聚合度之聚合物獲得纖維強化複合材料之方法(例如專利文獻1)。然而,專利文獻1揭示之環狀寡聚物於其合成時必須抑制高稀釋條件下之分子間反應,而有收率低的問題。必然地,成為基質樹脂之前驅物的環狀寡聚物之收率就獲得纖維強化複合材料上就成本上、技術上成為瓶頸。However, super engineering plastics such as polyarylene ether ketone have a very high melting point, making it difficult to impregnate the fiber material uniformly. As an effective impregnation method for these polymers, a relatively low molecular weight cyclic oligomer is heated and melted in the presence of fibers to impregnate the reinforcing fibers, and the cyclic oligomer is converted into a high degree of polymerization by ring-opening polymerization. A method for obtaining a fiber-reinforced composite material by using a polymer (for example, Patent Document 1). However, the cyclic oligomer disclosed in Patent Document 1 must suppress the intermolecular reaction under high dilution conditions during synthesis, and has a problem of low yield. Inevitably, the yield of the cyclic oligomer that becomes the precursor of the matrix resin becomes a bottleneck in terms of cost and technology in obtaining the fiber-reinforced composite material.
[發明欲解決之課題][Questions to be Solved by the Invention]
本發明之課題在於賦予可以高收率獲得之環狀聚伸芳基醚酮。
[用以解決課題之手段]The object of the present invention is to impart a cyclic polyarylene ether ketone that can be obtained in a high yield.
[Means to solve the problem]
本發明之環狀聚伸芳基醚酮係以下述化學式(I)表示之環狀體的聚伸芳基醚酮,其係化學式(I)中之Ar1 及Ar3 之至少一部分的伸芳基係以間位鍵結之伸芳基的環狀聚伸芳基醚酮。The cyclic poly (arylene ether ketone) of the present invention is a cyclic poly (arylene ether ketone) represented by the following chemical formula (I), which is at least a part of Ar 1 and Ar 3 in chemical formula (I). Cyclic poly (arylene ether ketone) based on an arylene group bonded in meta position.
(但,X為醚基或酮基,Ar1 、Ar2 、Ar3 分別表示可具有取代基之伸芳基,n為正整數)。(However, X is an ether group or a keto group, and Ar 1 , Ar 2 , and Ar 3 each represent an arylene group which may have a substituent, and n is a positive integer).
本發明之環狀聚伸芳基醚酮較好係化學式(I)之Ar1 具有間伸苯基單位及對伸苯基單位之2種構成單位之環狀聚伸芳基醚酮,Ar1 之間伸苯基單位(m1 )與對伸苯基單位(p1 )之莫耳比率(m1 /p1 )較好為0.05以上1以下。The cyclic poly (arylene ether ketone) of the present invention is preferably a cyclic poly (arylene ether ketone) having Ar 2 of a meta-phenylene unit and a para-phenylene unit of the chemical formula (I), Ar 1 The molar ratio (m 1 / p 1 ) between the phenylene unit (m 1 ) and the p-phenylene unit (p 1 ) is preferably 0.05 or more and 1 or less.
又,亦較好係化學式(I)之Ar3 具有間伸苯基單位及對伸苯基單位之2種構成單位之環狀聚伸芳基醚酮,Ar3 之間伸苯基單位(m3 )與對伸苯基單位(p3 )之莫耳比率(m3 /p3 )較好為0.05以上1以下。且,本發明中,環狀聚伸芳基酮較好重複單位n為2的環狀二聚物成分為30質量%以下。Further, Ar 3 having a chemical formula (I) of cyclic poly (arylene ether ketone) having two constituent units of m-phenylene unit and p-phenylene unit is also preferred, and phenylene unit (m) between Ar 3 3 ) The molar ratio (m 3 / p 3 ) to the p-phenylene unit (p 3 ) is preferably 0.05 or more and 1 or less. In the present invention, the cyclic polyarylidene preferably has a cyclic dimer component having a repeating unit n of 2 of 30% by mass or less.
本發明之環狀聚伸芳基醚酮可藉由下述製造方法獲得:使二鹵化芳香族酮、間-二羥基芳香族化合物及對-二羥基芳香族化合物反應之環狀聚伸芳基醚酮之製造方法;或使間-二鹵化醯基芳香族化合物、對-二鹵化醯基芳香族化合物及二芳基醚反應之環狀聚伸芳基醚酮之製造方法。The cyclic polyarylidene ether ketone of the present invention can be obtained by the following production method: a cyclic polyarylate which reacts a dihalogenated aromatic ketone, a m-dihydroxy aromatic compound, and a p-dihydroxy aromatic compound. A method for producing ether ketone; or a method for producing cyclic polyarylidene ether ketone by reacting m-dihalofluorenyl aromatic compound, p-dihalofluorenyl aromatic compound and diaryl ether.
本發明包含將本發明之環狀聚伸芳基醚酮含浸於纖維強化基材而成之成形材料,及將本發明之環狀聚伸芳基醚酮含浸於纖維強化基材後,使環狀聚伸芳基醚酮開環聚合之纖維強化複合材料之製造方法。
[發明效果]The present invention includes a molding material obtained by impregnating the cyclic poly (arylene ether ketone) of the present invention with a fiber-reinforced substrate, and impregnating the cyclic poly (arylene ether ketone) of the present invention with a fiber-reinforced substrate. Method for producing ring-shaped polymer-reinforced fiber-reinforced composite material of poly (arylene ether ketone).
[Inventive effect]
本發明之環狀聚伸芳基醚酮由於主鏈構造中具有以間位鍵結之伸芳基,故可以高收率獲得。本發明之環狀聚伸芳基醚酮由於對強化纖維之含浸性優異,故可藉具有優異物性之纖維強化複合而獲得材料。The cyclic polyarylidene ether ketone of the present invention can be obtained in a high yield because it has an arylate group bonded in the meta position in the main chain structure. The cyclic polyarylidene ether ketone of the present invention is excellent in impregnation with reinforcing fibers, and thus can be obtained by a fiber-reinforced composite having excellent physical properties.
依據本發明之環狀聚伸芳基醚酮之製造方法,可以高收率製造環狀聚伸芳基醚酮。According to the method for producing a cyclic poly (arylene ether ketone) of the present invention, a cyclic poly (arylene ether ketone) can be produced in a high yield.
以下詳細說明本發明。The present invention is explained in detail below.
本發明之環狀聚伸芳基醚酮係具有以下述化學式(I)表示之環狀體構造之聚伸芳基醚酮,係化學式(I)中之Ar1 及Ar3 之至少一部分的伸芳基係以間位鍵結之伸芳基的環狀聚伸芳基醚酮。本發明中,只要化學式(I)中之Ar1 、Ar3 之至少一者中之一部分的伸芳基係以間位鍵結之伸芳基即可。亦可Ar1 、Ar3 之兩者具有以間位鍵結之伸芳基。The cyclic poly (arylene ether ketone) of the present invention is a poly (arylene ether ketone) having a cyclic structure represented by the following chemical formula (I), which is at least a part of Ar 1 and Ar 3 in the chemical formula (I). Aryl is a cyclic poly (arylene ether ether ketone) of an arylene group bonded in meta position. In the present invention, the arylidene group of at least one of Ar 1 and Ar 3 in the chemical formula (I) may be an arylate group bonded by meta position. Both Ar 1 and Ar 3 may have an arylene group bonded in meta position.
(但,X為醚基或酮基,Ar1
、Ar2
、Ar3
分別表示可具有取代基之伸芳基,n為正整數)。
化學式(I)中以n表示之重複單位為正整數,較好為2以上20以下,更好為2以上15以下,又更好為2以上10以下。n在該範圍時,容易合成,且成為對纖維等之含浸容易之環狀聚伸芳基醚酮。n過小時,有合成易變困難之傾向,n過大時,環狀聚伸芳基醚酮之熔點變高,而有對纖維等之含浸效率性易降低之傾向。(However, X is an ether group or a keto group, and Ar 1 , Ar 2 , and Ar 3 each represent an arylene group which may have a substituent, and n is a positive integer).
The repeating unit represented by n in Chemical Formula (I) is a positive integer, preferably 2 or more and 20 or less, more preferably 2 or more and 15 or less, and even more preferably 2 or more and 10 or less. When n is in this range, it is easy to synthesize, and it becomes a cyclic polyarylene ether ketone which is easy to impregnate fibers and the like. When n is too small, the synthesis tends to be difficult to change. When n is too large, the melting point of the cyclic polyarylene ether ketone becomes high, and the impregnation efficiency of fibers and the like tends to decrease.
又,本發明中,相對於以化學式(I)表示之環狀聚伸芳基醚酮總量,重複單位n為2的環狀二聚物成分較好為30質量%以下。重複單位n為2的環狀二聚物成分更好為20%以下,又更好為10%以下。藉由使二聚物成分在該範圍時,可提高環狀聚伸芳基醚酮加熱熔融時之流動性。又,環狀二聚物成分含0.01%以上時,由於使環狀聚伸芳基醚酮開環聚合所得之高分子量聚伸芳基醚酮之耐衝擊性提高故而較佳。In the present invention, the cyclic dimer component having a repeating unit n of 2 is preferably 30% by mass or less based on the total amount of the cyclic polyarylene ether ketone represented by the chemical formula (I). The cyclic dimer component having a repeating unit n of 2 is more preferably 20% or less, and still more preferably 10% or less. When the dimer component is in this range, the fluidity at the time of heating and melting of the cyclic polyarylene ether ketone can be improved. When the cyclic dimer component contains 0.01% or more, the impact resistance of the high molecular weight poly (arylene ether ketone) obtained by ring-opening polymerization of the cyclic poly (arylene ether ketone) is improved.
化學式(I)中之X為醚基或酮基。化學式(I)中之X為醚基之環狀聚伸芳基醚酮亦稱為環狀聚伸芳基醚醚酮(PEEK),可藉由二鹵化芳香族酮化合物與二羥基芳香族化合物之共聚合等而獲得。化學式(I)中之X為酮基之環狀聚伸芳基醚酮亦稱為環狀聚伸芳基醚酮酮(PEKK),可藉由二鹵化醯基芳香族化合物與二芳基醚之共聚合等而獲得。X in Chemical Formula (I) is an ether group or a ketone group. In formula (I), X is an ether-based cyclic polyarylidene ether ketone. Also known as cyclic polyarylidene ether ether ketone (PEEK), dihalogenated aromatic ketone compounds and dihydroxy aromatic compounds can be used. Obtained by copolymerization and the like. Cyclic poly (arylene ether ketone) in which X is a keto group in chemical formula (I) is also known as cyclic poly (arylene ether ketone ketone) (PEKK). Obtained by copolymerization and the like.
化學式(I)中之Ar1 、Ar2 、Ar3 分別為可具有取代基之伸芳基,較好Ar2 係以對位鍵結之伸芳基(對伸苯基構造)。本發明係化學式(I)中之Ar1 及Ar3 之至少一部分的伸芳基係以間位鍵結之伸芳基(間伸苯基構造)之環狀聚伸芳基醚酮。主鏈中存在間伸苯基構造時,由於聚伸芳基醚鏈彎曲,故容易生成環狀構造體。因此,可以高收率獲得環狀聚伸芳基醚酮。又,具有此等彎曲構造之環狀聚伸芳基醚酮對強化纖維之含浸性優異。因此本發明之環狀聚伸芳基醚酮作為基質樹脂之前驅物使用時,可藉具有優異物性之纖維強化複合獲得材料。Ar 1 , Ar 2 , and Ar 3 in the chemical formula (I) are respectively an arylene group which may have a substituent, and it is preferable that Ar 2 is an arylene group (para-phenylene structure) bonded in a para position. The present invention is a cyclic polyarylidene ether ketone in which at least a part of Ar 1 and Ar 3 in chemical formula (I) is an arylene group (meta-phenylene structure) bonded in meta position. When a m-phenylene structure is present in the main chain, a cyclic structure is easily formed because the poly (arylene ether) chain is bent. Therefore, a cyclic polyarylene ether ketone can be obtained in a high yield. In addition, the cyclic polyarylene ether ketone having such a curved structure is excellent in impregnation with reinforcing fibers. Therefore, when the cyclic polyarylene ether ketone of the present invention is used as a precursor of a matrix resin, a material can be obtained by a fiber-reinforced composite having excellent physical properties.
本發明中,化學式(I)中之Ar1 或Ar3 未必均須為間位鍵結,只要化學式(I)中之重複單位內之一部分Ar1 或Ar3 為間位鍵結之伸芳基即可。本發明中,未間位鍵結之Ar1 及Ar3 較好為對位鍵結之伸芳基(對伸苯基構造)。In the present invention, Ar 1 or Ar 3 in chemical formula (I) may not necessarily be meta-bonded, as long as a part of Ar 1 or Ar 3 in the repeating unit in chemical formula (I) is meta-bonded arylene Just fine. In the present invention, Ar 1 and Ar 3 which are not meta-bonded are preferably para-bonded arylene (p-phenylene structure).
本發明之環狀聚伸芳基醚酮較好係化學式(I)之Ar1 具有間伸苯基單位及對伸苯基單位之2種構成單位之環狀聚伸芳基醚酮。Ar1 具有間伸苯基單位及對伸苯基單位之2種構成單位時,Ar1 之間伸苯基單位(m1 )與對伸苯基單位(p1 )之莫耳比率(m1 /p1 )較好為0.05以上1以下。莫耳比率(m1 /p1 )為該範圍內時,可以較好收率獲得環狀聚伸芳基醚酮。又使此等環狀聚伸芳基醚酮開環聚合時,可獲得耐熱性、機械特性優異之高分子量聚伸芳基醚酮。莫耳比率(m1 /p1 )過大時,彎曲構造較多,有使環狀聚伸芳基醚酮開環聚合所得之高分子量聚伸芳基醚酮之耐熱性、機械特性降低之傾向。另一方面,莫耳比率(m1 /p1 )過小時,分子鏈易變剛直,有所得環狀聚伸芳基醚酮之收率易降低之傾向。The cyclic poly (arylene ether ketone) of the present invention is preferably a cyclic poly (arylene ether ketone) in which Ar 1 of formula (I) has two constituent units of a m-phenylene unit and a p-phenylene unit. Ar 1 with inter-phenylene units and when the two kinds of the constituent units of the phenylene units, Ar-phenylene units (1 m) between 1 and the molar ratio of the phenylene units (P 1) of the (m 1 / p 1 ) is preferably 0.05 or more and 1 or less. When the molar ratio (m 1 / p 1 ) is within this range, a cyclic poly (arylene ether ketone) can be obtained in a good yield. When these cyclic poly (arylene ether ketone) s are subjected to ring-opening polymerization, a high molecular weight poly (arylene ether ketone) having excellent heat resistance and mechanical properties can be obtained. When the molar ratio (m 1 / p 1 ) is too large, there are many bending structures, and the heat resistance and mechanical properties of the high molecular weight poly (arylene ether ketone) obtained by ring-opening polymerization of cyclic poly (arylene ether ketone) tend to decrease. . On the other hand, when the molar ratio (m 1 / p 1 ) is too small, the molecular chain tends to become rigid and the yield of the obtained cyclic polyarylene ether ketone tends to decrease.
Ar1 包含間伸苯基單位之環狀聚伸芳基醚酮可藉由使二鹵化芳香族酮化合物與包含間位異構體之二羥基芳香族化合物共聚合而獲得。莫耳比率(m1 /p1 )可藉由共聚合所用之單體之間位異構體比率而調整。The cyclic polyarylene ether ketone in which Ar 1 contains a m-phenylene unit can be obtained by copolymerizing a dihalogenated aromatic ketone compound and a dihydroxy aromatic compound containing a meta-isomer. The Mohr ratio (m 1 / p 1 ) can be adjusted by the ratio of the isomers between the monomers used in the copolymerization.
又,本發明之環狀聚伸芳基醚酮亦較好為化學式(I)之Ar3 具有間伸苯基單位及對伸苯基單位之2種構成單位之環狀聚伸芳基醚酮。Ar3 具有間伸苯基單位及對伸苯基單位之2種構成單位時,Ar3 之間伸苯基單位(m3 )與對伸苯基單位(p3 )之莫耳比率(m3 /p3 )較好為0.05以上1以下。莫耳比率(m3 /p3 )為該範圍內時,可以較好收率獲得環狀聚伸芳基醚酮。又使此等環狀聚伸芳基醚酮開環聚合時,可獲得耐熱性、機械特性優異之高分子量聚伸芳基醚酮。莫耳比率(m3 /p3 )過大時,彎曲構造較多,有使環狀聚伸芳基醚酮開環聚合所得之高分子量聚伸芳基醚酮之耐熱性、機械特性降低之傾向。另一方面,莫耳比率(m3 /p3 )過小時,分子鏈易變剛直,有所得環狀聚伸芳基醚酮之收率易降低之傾向。In addition, the cyclic polyarylene ether ketone of the present invention is also preferably a cyclic polyarylene ether ketone having Ar 2 of a meta-phenylene unit and a para-phenylene unit in the chemical formula (I). . Ar 3 has the inter-phenylene units and when the two kinds of the constituent units of the phenylene units, Ar-phenylene unit (m 3) molar ratio of between 3 and phenylene units (P 3) of the (m 3 / p 3 ) is preferably 0.05 or more and 1 or less. When the molar ratio (m 3 / p 3 ) is within this range, a cyclic poly (arylene ether ketone) can be obtained in a good yield. When these cyclic poly (arylene ether ketone) s are subjected to ring-opening polymerization, a high molecular weight poly (arylene ether ketone) having excellent heat resistance and mechanical properties can be obtained. When the molar ratio (m 3 / p 3 ) is too large, there are many bending structures, and there is a tendency that the heat resistance and mechanical properties of high molecular weight poly (arylene ether ketone) obtained by ring-opening polymerization of cyclic poly (arylene ether ketone) tend to decrease. . On the other hand, if the molar ratio (m 3 / p 3 ) is too small, the molecular chain tends to become rigid, and the yield of the obtained cyclic polyarylene ether ketone tends to decrease.
Ar3 包含間伸苯基單位之環狀聚伸芳基醚酮可藉由使包含於至少一個芳基之間位鍵結有鹵素之間位異構體之二鹵化芳香族酮化合物與二羥基芳香族化合物之共聚合,或使包含間位異構體之二鹵化醯基芳香族化合物與二芳基醚之共聚合等而獲得。莫耳比率(m3 /p3 )可藉由共聚合所用之單體之間位異構體比率而調整。Ar 3 A cyclic polyarylene ether ketone containing a m-phenylene unit can be obtained by dihalogenated aromatic ketone compounds containing di-halo isomers and dihydroxy groups contained in at least one aryl group. It is obtained by copolymerization of an aromatic compound, or copolymerization of a dihalogenated fluorenyl aromatic compound containing a meta-isomer and a diaryl ether, and the like. The Moire ratio (m 3 / p 3 ) can be adjusted by the ratio of the isomers between the monomers used in the copolymerization.
如上述之本發明之環狀聚伸芳基醚酮由於主鏈中存在間位伸苯基構造,故聚伸芳基醚鏈彎曲容易生成環狀構造體,可以高收率獲得。又具有此等彎曲構造之環狀聚伸芳基醚酮由於對強化纖維之含浸性優異,故本發明之環狀聚伸芳基醚酮作為基質樹脂之前驅物使用時,可獲得具有優異物性之纖維強化複合材料。As described above, the cyclic poly (arylene ether ketone) of the present invention has a meta-phenylene structure in the main chain, so the poly-arylene ether chain is easily bent to form a cyclic structure, which can be obtained in high yield. Since the cyclic poly (arylene ether ketone) having such a curved structure is excellent in impregnation with reinforcing fibers, the cyclic poly (arylene ether ketone) of the present invention can have excellent physical properties when used as a matrix resin precursor. Fiber reinforced composites.
<環狀聚伸芳基醚酮之製造方法>
本發明之環狀聚伸芳基醚酮可藉由使用包含間位異構體之單體合成環狀聚伸芳基醚酮而獲得。環狀聚伸芳基醚酮可組合二鹵化芳香族酮化合物與二羥基芳香族化合物、或組合二鹵化醯基芳香族化合物與二芳基醚進行共聚合反應,或進行鹵化醯基羥基芳香族之聚合反應而獲得。聚合方法並未特別限制,可使用溶液聚合、熔融聚合、懸浮聚合、界面聚合等之以往習知之聚合方法。又,環狀聚伸芳基醚酮可藉由使線狀聚伸芳基醚進行加熱反應而獲得。<Production method of cyclic polyarylene ether ketone>
The cyclic poly (arylene ether ketone) of the present invention can be obtained by synthesizing a cyclic poly (arylene ether ketone) using a monomer containing a meta isomer. The cyclic polyarylidene ether ketone may be combined with a dihalogenated aromatic ketone compound and a dihydroxy aromatic compound, or a dihalogenated fluorenyl aromatic compound and a diaryl ether for copolymerization reaction, or a halogenated fluorenyl hydroxy aromatic Obtained by polymerization. The polymerization method is not particularly limited, and conventionally known polymerization methods such as solution polymerization, melt polymerization, suspension polymerization, and interfacial polymerization can be used. The cyclic poly (arylene ether ketone) can be obtained by subjecting a linear poly (arylene ether) to a heating reaction.
作為獲得環狀聚伸芳基醚酮之方法,舉例為例如以下之(a)~(g)之方法。
(a)使至少包含二鹵化芳香族酮化合物、二羥基芳香族化合物、鹼及有機極性溶劑之混合物加熱並反應之製造方法。
(b)使至少包含二鹵化醯基芳香族化合物、二芳基醚、鹼及有機極性溶劑之混合物加熱並反應之製造方法。
(c)使至少包含線狀聚伸芳基醚、二鹵化芳香族酮化合物、二羥基芳香族化合物、鹼及有機極性溶劑之混合物加熱並反應之製造方法。
(d)使至少包含線狀聚伸芳基醚酮、二鹵化醯基芳香族化合物、二芳基醚、鹼及有機極性溶劑之混合物加熱並反應之製造方法。
(e)使至少包含線狀聚伸芳基醚酮、至少無機鹼金屬鹽或有機鹼金屬鹽之任一種以上、有機極性溶劑之混合物加熱並反應之製造方法。
(f)使至少包含二鹵化芳香族酮化合物、二羥基芳香族酮化合物、鹼及有機極性溶劑之混合物加熱並反應之製造方法。
(g)使至少包含羥基鹵化芳香族酮化合物、二羥基芳香族化合物、鹼及有機極性溶劑之混合物加熱並反應之製造方法。Examples of the method for obtaining the cyclic polyarylene ether ketone include the following methods (a) to (g).
(a) A production method of heating and reacting a mixture containing at least a dihalogenated aromatic ketone compound, a dihydroxy aromatic compound, a base, and an organic polar solvent.
(b) A production method of heating and reacting a mixture containing at least a dihalofluorenyl aromatic compound, a diaryl ether, a base, and an organic polar solvent.
(c) A manufacturing method of heating and reacting a mixture containing at least a linear polyarylene ether, a dihalogenated aromatic ketone compound, a dihydroxy aromatic compound, a base, and an organic polar solvent.
(d) A method of heating and reacting a mixture containing at least a linear polyarylene ether ketone, a dihalofluorenyl aromatic compound, a diaryl ether, a base, and an organic polar solvent.
(e) A production method of heating and reacting a mixture of an organic polar solvent containing at least one or more of a linear polyarylene ether ketone, at least an inorganic alkali metal salt or an organic alkali metal salt.
(f) A production method of heating and reacting a mixture containing at least a dihalogenated aromatic ketone compound, a dihydroxy aromatic ketone compound, a base, and an organic polar solvent.
(g) A production method of heating and reacting a mixture containing at least a hydroxy halogenated aromatic ketone compound, a dihydroxy aromatic compound, a base, and an organic polar solvent.
組合二鹵化芳香族酮化合物與二羥基芳香族化合物製造本發明之環狀聚伸芳基醚酮時,作為二羥基芳香族化合物使用間-二羥基芳香族化合物,可獲得本發明之環狀聚伸芳基醚酮(環狀聚伸芳基醚醚酮)。When a dihalogenated aromatic ketone compound and a dihydroxy aromatic compound are combined to produce the cyclic polyarylidene ether ketone of the present invention, a meta-dihydroxy aromatic compound is used as the dihydroxy aromatic compound to obtain the cyclic polyarylidene of the present invention. Arylene ether ketone (cyclic polyarylene ether ether ketone).
本發明中,作為二羥基芳香族化合物較好併用間-二羥基芳香族化合物及對-二羥基芳香族化合物。此時,間-二羥基芳香族化合物/對-二羥基芳香族化合物之莫耳比較好為0.05以上1以下。藉由使間-二羥基芳香族化合物/對-二羥基芳香族化合物之莫耳比在該範圍,可以較佳收率獲得環狀聚伸芳基醚酮。且使此等環狀聚伸芳基醚酮開環聚合時,可獲得耐熱性、機械特性優異之高分子量聚伸芳基醚酮。間-二羥基芳香族化合物/對-二羥基芳香族化合物之莫耳比率過小時,分子鏈成為剛直而有所得環狀聚伸芳基醚酮之收率容易降低之傾向。另一方面,莫耳比率過大時,因彎曲構造佔分子鏈之過半數而有藉由後述之開環聚合所得之高分子量聚伸芳基醚酮之耐熱性、機械特性易於降低之傾向。In the present invention, as the dihydroxy aromatic compound, it is preferred to use a meta-dihydroxy aromatic compound and a para-dihydroxy aromatic compound together. In this case, the mole of the meta-dihydroxy aromatic compound / p-dihydroxy aromatic compound is preferably 0.05 or more and 1 or less. By setting the molar ratio of the meta-dihydroxy aromatic compound / p-dihydroxy aromatic compound to be in this range, a cyclic polyarylidene ether ketone can be obtained in a good yield. In addition, when these cyclic poly (arylene ether ketone) s are subjected to ring-opening polymerization, a high molecular weight poly (arylene ether ketone) having excellent heat resistance and mechanical properties can be obtained. When the molar ratio of the meta-dihydroxy aromatic compound / p-dihydroxy aromatic compound is too small, the molecular chain becomes rigid and the yield of the obtained cyclic polyarylene ether ketone tends to decrease. On the other hand, when the molar ratio is too large, the bent structure occupies more than half of the molecular chain, and the heat resistance and mechanical properties of the high molecular weight poly (arylene ether ketone) obtained by the ring-opening polymerization described later tend to decrease.
作為二鹵化芳香族酮化合物舉例為例如二氟二苯甲酮、二氯二苯甲酮、二溴二苯甲酮及其衍生物等。其中基於反應性之觀點,較好為二氟二苯甲酮。該等二鹵化芳香族酮化合物亦可使用單獨化合物,作為2種以上之混合物使用亦不成問題。Examples of the dihalogenated aromatic ketone compound include difluorobenzophenone, dichlorobenzophenone, dibromobenzophenone and derivatives thereof. Among them, from the viewpoint of reactivity, difluorobenzophenone is preferred. These dihalogenated aromatic ketone compounds may be used alone, and it is not a problem to use them as a mixture of two or more kinds.
作為間-二羥基芳香族化合物舉例為間苯二酚(間-二羥基苯)、2,4-甲苯二酚、3,5-甲苯二酚、對-二甲苯-2,6-二酚、間-二甲苯-4,6-二酚等。其中較好使用間苯二酚。Examples of m-dihydroxy aromatic compounds include resorcinol (m-dihydroxybenzene), 2,4-toluenediol, 3,5-toluenediol, p-xylene-2,6-diphenol, M-xylene-4,6-diphenol and the like. Among them, resorcinol is preferably used.
作為對-二羥基芳香族化合物舉例為對苯二酚(對-二羥基苯)、2,5-甲苯二酚、對-二甲苯-2,5-二酚等。其中較好使用對苯二酚。Examples of para-dihydroxy aromatic compounds include hydroquinone (p-dihydroxybenzene), 2,5-toluenediol, p-xylene-2,5-diphenol, and the like. Among them, hydroquinone is preferably used.
併用間-二羥基芳香族化合物與對-二羥基芳香族化合物之二羥基芳香族化合物之使用量,相對於二鹵化芳香族酮化合物1.0莫耳,較好為0.8~1.2莫耳之範圍,更好為0.9~1.1莫耳之範圍,又更好為0.95~1.05莫耳之範圍,特佳為0.98~1.03莫耳之範圍。藉由使二羥基芳香族化合物之使用量在上述較佳範圍,可抑制所生成之環狀聚伸芳基醚酮之分解反應,且有亦可抑制與環狀聚伸芳基醚酮之分離困難的線狀聚伸芳基醚酮的生成,故而較佳。The amount of the dihydroxy aromatic compound used in combination of m-dihydroxy aromatic compound and para-dihydroxy aromatic compound is preferably in the range of 0.8 to 1.2 mol relative to the dihalogenated aromatic ketone compound, more preferably It is preferably in the range of 0.9 to 1.1 moles, more preferably in the range of 0.95 to 1.05 moles, and particularly preferably in the range of 0.98 to 1.03 moles. By setting the amount of the dihydroxy aromatic compound in the above-mentioned preferable range, the decomposition reaction of the cyclic polyarylidene ether ketone generated can be suppressed, and the separation from the cyclic polyarylate ether ketone can also be suppressed. The formation of difficult linear polyarylene ether ketone is preferred.
組合二鹵化醯基芳香族化合物與二芳基醚製造本發明之環狀聚伸芳基醚酮時,作為二鹵化醯基芳香族化合物使用間-二鹵化醯基芳香族化合物,可獲得本發明之環狀聚伸芳基醚酮(環狀聚伸芳基醚酮酮)。When a dihalogenated fluorenyl aromatic compound and a diaryl ether are combined to produce the cyclic polyarylidene ether ketone of the present invention, a m-dihalogenated fluorenyl aromatic compound is used as the dihalogenated fluorenyl aromatic compound, and the present invention can be obtained. Cyclic poly (arylene ether ketone).
本發明中,作為二鹵化醯基芳香族化合物,較好併用間-二鹵化醯基芳香族化合物及對-二鹵化醯基芳香族化合物。此時,間-二鹵化醯基芳香族化合物/對-二鹵化醯基芳香族化合物之莫耳比較好為0.05以上1以下。藉由使莫耳比率在該範圍,可以較佳收率獲得環狀聚伸芳基醚酮。且使此等環狀聚伸芳基醚酮開環聚合時,可獲得耐熱性、機械特性優異之高分子量聚伸芳基醚酮。莫耳比率過小時,分子鏈成為剛直而有所得環狀聚伸芳基醚酮之收率容易降低之傾向。另一方面,莫耳比率過大時,因彎曲構造佔分子鏈之過半數而有藉由後述之開環聚合所得之芳香族聚伸芳基醚酮之耐熱性、機械特性易於降低之傾向。In the present invention, as the dihalogenated fluorenyl aromatic compound, a m-dihalogenated fluorenyl aromatic compound and a p-dihalogenated fluorenyl aromatic compound are preferably used in combination. In this case, the mole of the meta-dihalofluorenyl aromatic compound / p-dihalofluorenyl aromatic compound is preferably 0.05 or more and 1 or less. By setting the molar ratio within this range, cyclic polyarylene ether ketone can be obtained in a good yield. In addition, when these cyclic poly (arylene ether ketone) s are subjected to ring-opening polymerization, a high molecular weight poly (arylene ether ketone) having excellent heat resistance and mechanical properties can be obtained. When the molar ratio is too small, the molecular chain becomes rigid and the yield of the obtained cyclic polyarylene ether ketone tends to be easily reduced. On the other hand, when the molar ratio is too large, the bent structure occupies more than half of the molecular chain, and thus the heat resistance and mechanical properties of the aromatic poly (arylene ether ketone) obtained by the ring-opening polymerization described later tend to decrease.
作為間-二鹵化醯基芳香族化合物舉例為例如氯化間苯二甲醯基及其衍生物等。Examples of the m-dihalofluorenyl aromatic compound include, for example, m-xylylene chloride and derivatives thereof.
作為對-二鹵化醯基芳香族化合物舉例為例如氯化對苯二甲醯基及其衍生物等。Examples of the p-dihalofluorenyl aromatic compound include, for example, p-xylylene chloride and derivatives thereof.
作為二芳基醚舉例為例如二苯基醚及其衍生物等。Examples of the diaryl ether include diphenyl ether and derivatives thereof.
作為環狀聚伸芳基醚酮之製造中使用之鹼可舉例為碳酸鋰、碳酸鈉、碳酸鉀、碳酸銣、碳酸銫等之鹼金屬碳酸鹽,碳酸鈣、碳酸鍶、碳酸鋇等之鹼土金屬之碳酸鹽,碳酸氫鋰、碳酸氫鈉、碳酸氫鉀、碳酸氫銣、碳酸氫銫等之鹼金屬之碳酸氫鹽,碳酸氫鈣、碳酸氫鍶、碳酸氫鋇等之鹼土金屬之碳酸氫鹽,或氫氧化鋰、氫氧化鈉、氫氧化鉀、氫氧化銣、氫氧化銫等之鹼金屬之氫氧化物,氫氧化鈣、氫氧化鍶、氫氧化鋇等之鹼土金屬之氫氧化物,其中基於取得容易、反應性之觀點,較好為碳酸鈉、碳酸鉀等之碳酸鹽,及碳酸氫鈉、碳酸氫鉀等之碳酸氫鹽,又更好為碳酸鈉、碳酸鉀,再更好使用碳酸鉀。該等可單獨使用,混合2種以上使用亦不成問題。又,該等鹼較好以無水物之形態使用,但亦可作為水合物或水性混合物使用。又,此處所謂水性混合物係指水溶液,或水溶液與固體成分之混合物,或水與固體成分之混合物。Examples of the alkali used in the production of the cyclic polyarylidene ether ketone include alkali metal carbonates such as lithium carbonate, sodium carbonate, potassium carbonate, rubidium carbonate, cesium carbonate, and alkaline earths such as calcium carbonate, strontium carbonate, and barium carbonate. Carbonates of metals, Lithium bicarbonate, sodium bicarbonate, potassium bicarbonate, rubidium bicarbonate, cesium bicarbonate and other alkali metal bicarbonates, calcium bicarbonate, strontium bicarbonate, barium bicarbonate and other alkaline earth metal carbonates Hydrogen salts, or hydroxides of alkali metals such as lithium hydroxide, sodium hydroxide, potassium hydroxide, rubidium hydroxide, and cesium hydroxide; hydroxides of alkaline earth metals such as calcium hydroxide, strontium hydroxide, and barium hydroxide Among them, from the viewpoint of easy and reactivity, carbonates such as sodium carbonate and potassium carbonate, and sodium bicarbonates such as sodium bicarbonate and potassium bicarbonate are preferred, and sodium carbonate and potassium carbonate are more preferred. Better use of potassium carbonate. These can be used alone, and it is not a problem to mix two or more. These bases are preferably used in the form of an anhydrous substance, but they can also be used as a hydrate or an aqueous mixture. The term "aqueous mixture" used herein refers to an aqueous solution, a mixture of an aqueous solution and a solid component, or a mixture of water and a solid component.
作為環狀聚伸芳基醚酮之製造方法中使用之有機極性溶劑,若為不實質上引起反應阻礙或所生成之環狀聚伸芳基醚酮之分解等之不好的副反應者,則未特別限制。作為此等有機極性溶劑之具體例舉例為甲苯、N-甲基-1-吡咯啶酮(NMP)、N-甲基己內醯胺、N,N-二甲基甲醯胺(DMF)、N,N-二甲基乙醯胺(DMAc)、1,3-二甲基-2-咪唑啶酮(DMI)、六甲基磺醯胺、四甲基脲等之含氮極性溶劑,二甲基亞碸(DMSO)、二甲基碸、二苯基碸、環丁碸等之亞碸・碸系溶劑,苯甲腈等之腈系溶劑,二苯醚等之二芳基醚類,二苯甲酮、苯乙酮等之酮類及該等之混合物等。As the organic polar solvent used in the production method of the cyclic poly (arylene ether ketone), if it is a bad side reaction that does not substantially cause reaction hindrance or decomposition of the cyclic poly (arylene ether ketone) produced, It is not particularly limited. Specific examples of such organic polar solvents include toluene, N-methyl-1-pyrrolidone (NMP), N-methylcaprolactam, N, N-dimethylformamide (DMF), N, N-dimethylacetamide (DMAc), 1,3-dimethyl-2-imidazolidinone (DMI), hexamethylsulfonamide, tetramethylurea, etc. Dimethylene fluorene (DMSO), dimethyl fluorene, diphenyl fluorene, cyclopentadiene and other fluorene / fluorene-based solvents, benzonitrile and other nitrile solvents, diphenyl ethers and other diaryl ethers, Ketones such as benzophenone and acetophenone and mixtures thereof.
製造環狀聚伸芳基醚酮時之混合物中之有機極性溶劑之量,期望較好相對於混合物中之苯環成分1.0莫耳包含1.20升以上,更好為1.30升以上,又更好1.50升以上,特佳為2.0升以上。又,混合物中之有機極性溶劑量之上限並未特別限制,但較好相對於混合物中之苯環成分1.0莫耳包含100升以下,更好為50升以下,又更好20升以下,特佳為10升以下。It is desirable that the amount of the organic polar solvent in the mixture when producing the cyclic polyarylidene ether ketone is preferably 1.20 liters or more, more preferably 1.30 liters or more, and 1.50 liters relative to the 1.0 benzene ring component in the mixture. Liters or more, particularly preferably 2.0 liters or more. In addition, the upper limit of the amount of the organic polar solvent in the mixture is not particularly limited, but it is preferably 100 liters or less, more preferably 50 liters or less, and more preferably 20 liters or less relative to 1.0 mol of the benzene ring component in the mixture. It is preferably less than 10 liters.
環狀聚伸芳基醚酮之製造方法中之鹼使用量,期望作為對於單體之化學計量比率的當量以上。反應溫度係根據使用之原料、鹼、有機極性溶劑等之種類、量等而有各種變化,故無法一概決定,但通常可例示120~350℃之範圍。反應時間由於依存於使用之原料種類及量,或反應溫度故而無法一概規定,但較好為0.1小時以上,更好為0.5小時以上,又更好為1小時以上。另一方面,反應時間並無特別上限,即使40小時以內反應亦可充分進行,較佳採用10小時以內,更好亦可採用6小時以內。又,製造時之環境期望為非氧化性環境下,較好於氮氣、氦氣及氬氣等之惰性環境下進行,基於經濟性及處理容易性較好於氮氣環境下進行。The amount of the alkali used in the method for producing a cyclic poly (arylene ether ketone) is preferably equal to or greater than the equivalent of the stoichiometric ratio to the monomer. The reaction temperature varies depending on the types and amounts of raw materials, bases, organic polar solvents, etc. used, so it cannot be determined uniformly, but usually ranges from 120 to 350 ° C. The reaction time cannot be specified because it depends on the type and amount of the raw materials used or the reaction temperature, but it is preferably 0.1 hours or more, more preferably 0.5 hours or more, and even more preferably 1 hour or more. On the other hand, there is no particular upper limit to the reaction time, and the reaction can proceed sufficiently within 40 hours, preferably within 10 hours, and more preferably within 6 hours. In addition, the environment at the time of manufacture is desirably performed in a non-oxidizing environment, preferably in an inert environment such as nitrogen, helium, and argon, and is preferably performed in a nitrogen environment based on economy and ease of handling.
本發明中,亦較好控制如上述所得之環狀聚伸芳基醚酮中重複單位n為2所成之環狀二聚物成分量。具體而言,環狀二聚物成分量較好為30質量%以下,更好為0.01~20質量%。藉由環狀二聚物成分量為該範圍,可提高環狀聚伸芳基醚酮加熱熔融時之流動性。In the present invention, the amount of the cyclic dimer component formed by the repeating unit n of 2 in the cyclic polyarylidene ether ketone obtained as described above is also preferably controlled. Specifically, the amount of the cyclic dimer component is preferably 30% by mass or less, and more preferably 0.01 to 20% by mass. When the amount of the cyclic dimer component is within this range, the fluidity of the cyclic poly (arylene ether ketone) during heating and melting can be improved.
作為環狀二聚物成分量之控制方法可利用使用溶劑之固液分離法。具體而言,將環狀聚伸芳基醚酮粗產物溶解於醚系溶劑後,過濾去除未溶解於醚系溶劑之未溶解物。醚系溶劑由於環狀體二聚物成分之溶解性低,重複單位n為3以上之環狀體成分之溶解性高,故藉由使用醚系溶劑進行固液分離處理,可將環狀聚伸芳基醚酮組成物中所含之環狀體二聚物成分調整在期望量。As a method for controlling the amount of the cyclic dimer component, a solid-liquid separation method using a solvent can be used. Specifically, the crude cyclic polyarylidene ether ketone was dissolved in an ether-based solvent, and then the undissolved matter that was not dissolved in the ether-based solvent was removed by filtration. The ether-based solvent has a low solubility in the cyclic dimer component and a high solubility in the cyclic component with a repeating unit n of 3 or more. Therefore, the cyclic polymer can be separated by using a ether-based solvent for solid-liquid separation treatment. The cyclic dimer component contained in the arylidene ether ketone composition is adjusted to a desired amount.
作為醚系溶劑可使用四氫呋喃、二乙醚、三乙醚、二異丙醚、乙二醇單甲醚、乙二醇單乙醚、乙二醇單丁醚、1,4-二噁烷、2-甲氧基-2-甲基丙烷,特佳為四氫呋喃。As the ether-based solvent, tetrahydrofuran, diethyl ether, triethyl ether, diisopropyl ether, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, 1,4-dioxane, and 2-methyl ether can be used. Oxy-2-methylpropane, particularly preferably tetrahydrofuran.
<聚伸芳基醚酮之製造方法>
本發明之環狀聚伸芳基醚酮藉由開環聚合,可轉化為高分子量之聚伸芳基醚酮。< Manufacturing method of polyarylene ether ketone >
The cyclic poly (arylene ether ketone) of the present invention can be converted into a high-molecular-weight poly (arylene ether ketone) by ring-opening polymerization.
開環聚合反應時之加熱溫度可對應於環狀聚伸芳基醚酮之組成或分子量、加熱時之環境而適當選擇。基於以更短時間進行反應之觀點,較好為200℃以上,更好為240℃以上。另一方面,基於抑制分解反應等副反應之觀點,加熱溫度較好為450℃以下,更好為400℃以下。加熱時間係對應於環狀聚伸芳基醚酮之各種特性、加熱溫度等條件適當選擇。基於環狀聚伸芳基醚酮充分轉化之觀點,加熱時間較好為0.01小時以上,更好為0.05小時以上。另一方面,基於抑制分解反應等之副反應之觀點,較好為100小時以下,更好為20小時以下,又更好為10小時以下,再更好為6小時以下,又再更好為3小時以下。The heating temperature during the ring-opening polymerization reaction may be appropriately selected according to the composition or molecular weight of the cyclic polyarylene ether ketone and the environment during heating. From the viewpoint of performing the reaction in a shorter time, it is preferably 200 ° C or higher, and more preferably 240 ° C or higher. On the other hand, from the viewpoint of suppressing side reactions such as decomposition reactions, the heating temperature is preferably 450 ° C or lower, and more preferably 400 ° C or lower. The heating time is appropriately selected in accordance with various characteristics of the cyclic polyarylene ether ketone and the heating temperature. From the viewpoint of sufficient conversion of the cyclic polyarylene ether ketone, the heating time is preferably 0.01 hours or more, and more preferably 0.05 hours or more. On the other hand, from the viewpoint of suppressing side reactions such as decomposition reactions, it is preferably 100 hours or less, more preferably 20 hours or less, still more preferably 10 hours or less, still more preferably 6 hours or less, and even more preferably Less than 3 hours.
環狀聚伸芳基醚酮開環聚合時,亦可根據需要使用聚合觸媒。聚合觸媒係用以加速環狀聚伸芳基醚酮之開環聚合反應的觸媒,只要具有該效果之化合物則未特別限制,可使用例如無機鹼金屬鹽或有機鹼金屬鹽等之鹼金屬鹽,作為無機鹼金屬鹽可例示氟化鈉、氟化鉀、氟化銫、氯化鋰等之鹼金屬鹵化物,且作為有機鹼金屬鹽可例示甲氧化鈉、甲氧化鉀、乙氧化鈉、乙氧化鉀、第三丁氧化鈉、第三丁氧化鉀等之鹼金屬烷氧化物或苯氧化鈉、苯氧化鉀、4-苯氧基苯氧化鈉、4-苯氧基苯氧化鉀等之鹼金屬苯氧化物,乙酸鋰、乙酸鈉、乙酸鉀等之鹼金屬乙酸鹽。該等觸媒可單獨使用,亦可混合2種以上使用。藉由使環狀聚伸芳基醚酮之開環聚合在該等較佳觸媒存在下進行,可減低反應時間。In the ring-opening polymerization of cyclic poly (arylene ether ketone), a polymerization catalyst may be used as required. The polymerization catalyst is a catalyst for accelerating the ring-opening polymerization reaction of a cyclic polyarylidene ether ketone. The compound having this effect is not particularly limited, and an alkali such as an inorganic alkali metal salt or an organic alkali metal salt can be used. Examples of the metal salt include alkali metal halides such as sodium fluoride, potassium fluoride, cesium fluoride, and lithium chloride, and examples of the organic alkali metal salt include sodium methoxide, potassium methoxide, and ethoxylate. Alkali metal alkoxides such as sodium, potassium ethoxide, sodium third butoxide, potassium third butoxide, etc. or sodium phenoxide, potassium phenoxide, sodium 4-phenoxyphenoxide, potassium 4-phenoxyphenoxide Alkali metal phenoxides such as lithium acetate, sodium acetate, potassium acetate and the like. These catalysts can be used alone or in combination of two or more. By performing the ring-opening polymerization of the cyclic poly (arylene ether ketone) in the presence of these preferred catalysts, the reaction time can be reduced.
使用之聚合觸媒量,係根據成為目的之高分子量聚伸芳基醚酮之分子量以及觸媒種類而異,但通常對於環狀聚伸芳基醚酮之主要構成單位的化學式(I)之重複單位1莫耳,為0.001~20莫耳%,更好為0.005~15莫耳%,又更好為0.01~10莫耳%。藉由添加該較佳範圍之觸媒量,而有以短時間進行環狀聚伸芳基醚酮之開環聚合之傾向。The amount of the polymerization catalyst used varies depending on the molecular weight of the target high molecular weight poly (arylene ether ketone) and the type of catalyst, but it is usually the chemical formula (I) of the main constituent unit of the cyclic poly (arylene ether ketone). The repeating unit is 1 mol, and is 0.001 to 20 mol%, more preferably 0.005 to 15 mol%, and still more preferably 0.01 to 10 mol%. By adding the amount of the catalyst in the preferable range, there is a tendency that the ring-opening polymerization of the cyclic poly (arylene ether ketone) is performed in a short time.
聚合觸媒之添加方法時並未特別限制,但可例示使聚伸芳基醚酮加熱作成熔融液,於該融溶液中混合聚合觸媒之方法,或使聚伸芳基醚酮與聚合觸媒之混合物加熱作成熔融液之方法等。The method for adding the polymerization catalyst is not particularly limited, but examples thereof include a method of heating the polyarylene ether ketone into a molten liquid, mixing the polymerization catalyst in the molten solution, or bringing the polyarylene ether ketone into contact with the polymerization catalyst. A method of heating a mixture of vehicles to form a molten liquid.
本發明之成形材料係將上述環狀聚伸芳基醚酮含浸於任意基材中,使環狀聚伸芳基醚酮開環聚合而成之以聚伸芳基醚酮為基質之成形材料。作為基材若為不阻礙環狀聚伸芳基醚酮之開環聚合反應即可,形狀並未限制。舉例為例如粒子、連續纖維、長纖維、短纖維、不織布、薄膜等。The molding material of the present invention is a molding material based on the poly (arylene ether ketone) as a matrix obtained by impregnating the above-mentioned cyclic poly (arylene ether ketone) in any substrate and ring-opening polymerization of the cyclic poly (arylene ether ketone). . The base material is not limited as long as it does not hinder the ring-opening polymerization reaction of the cyclic polyarylene ether ketone. Examples are particles, continuous fibers, long fibers, short fibers, non-woven fabrics, films, and the like.
藉由將本發明之環狀聚伸芳基醚酮含浸於纖維強化基材並開環聚合,可獲得纖維強化複合材料。使用本發明之環狀聚伸芳基醚酮製造纖維強化複合材料時,可與環狀聚伸芳基醚酮含浸於纖維強化基材同時進行開環聚合,亦可將環狀聚伸芳基醚酮含浸於纖維強化基材之成形材料作為中間體。The fiber-reinforced composite material can be obtained by impregnating the fiber-reinforced base material with the cyclic polyarylene ether ketone of the present invention and performing ring-opening polymerization. When the fiber-reinforced composite material is produced by using the cyclic poly (arylene ether ketone) of the present invention, the cyclic poly (arylene ether ketone) can be impregnated with the fiber-reinforced substrate to perform ring-opening polymerization at the same time, or the cyclic poly (arylene) aryl group can be used Ether ketone impregnates the forming material of the fiber-reinforced substrate as an intermediate.
使用本發明之環狀聚伸芳基醚酮製造纖維強化複合材料時,環狀聚伸芳基醚酮可單獨使用,亦可作為包含前述聚合觸媒之樹脂組成物而使用。樹脂組成物中,亦可包含線狀聚伸芳基醚酮或聚伸芳基醚酮以外之樹脂,且在不損及目的之範圍,亦可含有無機填充材、難燃劑、導電性賦予劑、結晶核劑、紫外線吸收劑、抗氧化劑、制振劑、抗菌劑、防蟲劑、防臭劑、防著色劑、熱安定劑、脫模劑、抗靜電劑、可塑劑、滑劑、著色劑、顏料、染料、發泡劑、抑泡劑、偶合劑等之各種添加劑。When the fiber-reinforced composite material is produced using the cyclic poly (arylene ether ketone) of the present invention, the cyclic poly (arylene ether ketone) may be used alone or as a resin composition containing the aforementioned polymerization catalyst. The resin composition may contain resins other than linear polyarylene ether ketone or polyarylene ether ketone, and may also contain inorganic fillers, flame retardants, and conductivity imparting to the extent that the purpose is not impaired. Agents, crystal nucleating agents, ultraviolet absorbers, antioxidants, vibration suppressants, antibacterial agents, insect repellents, deodorants, anti-colorants, heat stabilizers, release agents, antistatic agents, plasticizers, lubricants, colorants Additives, pigments, dyes, foaming agents, foam inhibitors, coupling agents and other additives.
本發明之成形材料係將上述環狀聚伸芳基醚酮含浸於纖維強化基材而成之成形材料。The molding material of the present invention is a molding material obtained by impregnating the above-mentioned cyclic polyarylene ether ketone into a fiber-reinforced substrate.
作為強化纖維材料並未特別限制,舉例為例如碳纖維、玻璃纖維、聚芳醯胺纖維、碳化矽纖維、聚酯纖維、陶瓷纖維、氧化鋁纖維、硼纖維、金屬纖維、礦物纖維、岩石纖維及礦渣纖維等。The reinforcing fiber material is not particularly limited, and examples thereof include carbon fiber, glass fiber, polyamide fiber, silicon carbide fiber, polyester fiber, ceramic fiber, alumina fiber, boron fiber, metal fiber, mineral fiber, rock fiber, and Slag fiber and so on.
該等強化纖維中,較佳為碳纖維、玻璃纖維、聚芳醯胺纖維。基於獲得比強度、比彈性率良好,輕量且高強度之纖維強化複合材料之觀點,更好為碳纖維。就拉伸強度優異之觀點特佳為聚丙烯腈(PAN)系碳纖維。Among these reinforcing fibers, carbon fibers, glass fibers, and polyamide fibers are preferred. From the viewpoint of obtaining a fiber-reinforced composite material having a specific strength, a high specific elasticity, a light weight and a high strength, carbon fibers are more preferred. From the viewpoint of excellent tensile strength, polyacrylonitrile (PAN) -based carbon fibers are particularly preferred.
強化纖維使用PAN系碳纖維時,其拉伸彈性率較好為100~600GPa,更好為200~500GPa,特佳為230~450GPa。又,拉伸強度較好為2000MPa~10000MPa,更好為3000~8000MPa。碳纖維直徑較好為4~20μm,更好為5~10μm。藉由使用此等碳纖維,可提高所得纖維強化複合材料之機械性質。When the PAN-based carbon fiber is used as the reinforcing fiber, the tensile elastic modulus is preferably 100 to 600 GPa, more preferably 200 to 500 GPa, and particularly preferably 230 to 450 GPa. The tensile strength is preferably 2000 MPa to 10,000 MPa, and more preferably 3000 to 8000 MPa. The carbon fiber diameter is preferably 4 to 20 μm, and more preferably 5 to 10 μm. By using these carbon fibers, the mechanical properties of the fiber-reinforced composite material obtained can be improved.
較好將強化纖維形成為薄片狀使用。作為強化纖維薄片,可舉例為例如將多數根強化纖維於一方向對齊之薄片,或平織或綾織等之二方向織物、多軸織物、不織布、方平組織(matt)、針織、編帶、將強化纖維抄紙而得之紙。該等中,使用以強化纖維作為連續纖維形成為薄片狀之於一方向對齊之薄片或二方向織物、多軸織物基材時,由於可獲得機械物性更優異之纖維強化複合材料故而較佳。薄片狀強化纖維基材厚度較好為0.01~3mm,更好為0.1~1.5mm。The reinforcing fibers are preferably used in a sheet form. Examples of the reinforcing fiber sheet include, for example, a sheet in which a plurality of reinforcing fibers are aligned in one direction, or a bidirectional fabric such as plain woven or woven fabric, a multiaxial fabric, a non-woven fabric, a matt, knitted, braided, Reinforced fiber made from paper. Among these, when a reinforcing fiber is used as a continuous fiber and formed into a thin sheet, a unidirectionally aligned sheet, a bidirectional fabric, or a multiaxial fabric base material is preferable because a fiber-reinforced composite material having more excellent mechanical properties can be obtained. The thickness of the sheet-like reinforcing fiber substrate is preferably 0.01 to 3 mm, and more preferably 0.1 to 1.5 mm.
成形材料全體中之環狀聚伸芳基醚酮含有率,以成形材料總質量為基準,較好為15~60質量%。樹脂含有率較好為20~55質量%,更好為25~50質量%。The content of the cyclic polyarylene ether ketone in the entire molding material is preferably 15 to 60% by mass based on the total mass of the molding material. The resin content is preferably from 20 to 55 mass%, more preferably from 25 to 50 mass%.
於強化纖維基材中含浸環狀聚伸芳基醚酮之方法,並未特別限制,可採用以往習知之任何方法。具體而言,可較好地採用熱熔法或溶劑法。The method of impregnating the cyclic polyarylene ether ketone into the reinforcing fiber substrate is not particularly limited, and any method conventionally known can be adopted. Specifically, a hot-melt method or a solvent method can be preferably used.
熱熔法係於脫模紙上將包含環狀聚伸芳基醚酮之樹脂組成物塗佈為薄的薄膜狀形成樹脂組成物薄膜,將該樹脂組成物薄膜積層於強化纖維基材上於加壓下加熱而將樹脂組成物含浸於強化纖維基材層內之方法。The hot-melt method is to apply a resin composition containing a cyclic polyarylidene ether ketone to a thin film to form a resin composition film on a release paper, and laminate the resin composition film on a reinforcing fiber substrate. A method of impregnating a resin composition into a reinforcing fiber substrate layer by heating under pressure.
作為將樹脂組成物作成樹脂組成物薄膜之方法並未特別限制,亦可使用以往習知之任一方法。具體而言進行模嘴擠出,使用敷料機、逆輥塗佈機、缺角輪塗佈機等,於脫模紙或薄膜等之支撐體上流延、澆鑄樹脂組成物,而可獲得樹脂組成物薄膜。製造薄膜時之樹脂溫度係根據樹脂組成物之組成或黏度適當決定。樹脂組成物對強化纖維基材層內之含浸可進行一次,亦可分複數次進行。The method for forming the resin composition into a resin composition film is not particularly limited, and any conventionally known method may be used. Specifically, the die is extruded, and a resin composition is cast and cast on a support such as a release paper or a film using an applicator, a reverse roll coater, a notch wheel coater, etc. to obtain a resin composition.物 Film. The temperature of the resin when manufacturing the film is appropriately determined according to the composition or viscosity of the resin composition. The resin composition may be impregnated into the reinforcing fiber base material layer once or in a plurality of times.
溶劑法係使用適當溶劑將樹脂組成物作成清漆狀,將該清漆含浸於強化纖維基材層內之方法。該等以往方法中,藉由不使用溶劑之熱熔法可更好地製造。The solvent method is a method in which a resin composition is formed into a varnish using an appropriate solvent, and the varnish is impregnated into a reinforcing fiber base material layer. Among these conventional methods, it can be manufactured better by a hot-melt method without using a solvent.
本發明之環狀聚伸芳基醚酮含浸於纖維強化基材後,進行開環聚合,將環狀聚伸芳基醚酮轉化為高分子量之聚伸芳基醚酮,可獲得纖維強化複合材料。After impregnating the fiber-reinforced substrate with the cyclic polyarylene ether ketone of the present invention, ring-opening polymerization is performed to convert the cyclic polyarylene ether ketone into a high-molecular-weight polyarylene ether ketone to obtain a fiber-reinforced composite. material.
開環聚合反應時之加熱溫度可對應於環狀聚伸芳基醚酮之組成或分子量、加熱時之環境適當選擇。基以於更短時間進行反應之觀點,較好為200℃以上,更好為250℃以上,又更好為280℃以上。另一方面,基於抑制分解反應等副反應之觀點,加熱溫度較好為450℃以下,更好為400℃以下。加熱時間可對應於環狀聚伸芳基醚酮之各種特性、加熱溫度等之條件適當選擇。基於環狀聚伸芳基醚酮充分轉化之觀點,加熱時間較好為0.01小時以上,更好為0.05小時以上。另一方面,基於抑制分解反應等副反應之觀點,加熱時間較好為100小時以下,更好為20小時以下,又更好10小時以下,再更好6小時以下,又再更好3小時以下。The heating temperature during the ring-opening polymerization reaction may be appropriately selected corresponding to the composition or molecular weight of the cyclic polyarylidene ether ketone and the environment during heating. From the viewpoint of reacting in a shorter time, it is preferably 200 ° C or higher, more preferably 250 ° C or higher, and even more preferably 280 ° C or higher. On the other hand, from the viewpoint of suppressing side reactions such as decomposition reactions, the heating temperature is preferably 450 ° C or lower, and more preferably 400 ° C or lower. The heating time can be appropriately selected according to various characteristics of the cyclic polyarylene ether ketone, heating conditions, and the like. From the viewpoint of sufficient conversion of the cyclic polyarylene ether ketone, the heating time is preferably 0.01 hours or more, and more preferably 0.05 hours or more. On the other hand, from the viewpoint of suppressing side reactions such as decomposition reactions, the heating time is preferably 100 hours or less, more preferably 20 hours or less, still more preferably 10 hours or less, still more preferably 6 hours or less, and still more preferably 3 hours. the following.
作為本發明之纖維強化複合材料之成形方法並未特別限制,可舉例為例如射出成形、樹脂轉注成形、反應射出成形、高壓釜成形、加壓成形、纖絲捲繞成形、沖壓成形等之生產性優異之成形方法,該等可組合使用。The method for forming the fiber-reinforced composite material of the present invention is not particularly limited, and examples thereof include production of injection molding, resin injection molding, reaction injection molding, autoclave molding, pressure molding, filament winding molding, and press molding. A molding method with excellent properties, which can be used in combination.
如此所得之本發明之纖維強化複合材料可較好地使用於汽車、飛機、電氣・電子機器、醫療用品、運動・休閒用品等之用塗。
[實施例]The fiber-reinforced composite material of the present invention thus obtained can be suitably used for coatings for automobiles, airplanes, electrical and electronic equipment, medical supplies, sports and leisure products, and the like.
[Example]
以下,藉由實施例更具體說明本發明。但本發明之範圍不限定於該等實施例。Hereinafter, the present invention will be described more specifically with reference to examples. However, the scope of the present invention is not limited to these examples.
[測定方法]
<玻璃轉移點、熔點>
使用示差式掃描型熱量測定裝置(TA Instruments公司製DSC Q2000)作為測定裝置,由自基準線之偏移測定玻璃轉移溫度,由熔解峰測定熔點。於氮氣流入下(20ml/min)、20℃/min之升溫速度,於自30℃至400℃之溫度範圍進行測定。[test methods]
< Glass transition point and melting point >
A differential scanning calorimeter (DSC Q2000, manufactured by TA Instruments) was used as a measuring device, and the glass transition temperature was measured from the deviation from the reference line, and the melting point was measured from the melting peak. The measurement was performed at a temperature range from 30 ° C to 400 ° C under a nitrogen inflow (20 ml / min) and a temperature increase rate of 20 ° C / min.
<開始流動溫度>
使用熔點測定計(BUCHI公司製Melting Point B-545)作為測定裝置。以5℃/min之升溫速度,於自室溫至350℃之溫度範圍進行測定。以目視確認熔解的環狀化合物開始流動之溫度。< Starting flow temperature >
As a measuring device, a melting point meter (Melting Point B-545 manufactured by BUCHI Corporation) was used. The measurement was performed at a temperature rising rate of 5 ° C / min in a temperature range from room temperature to 350 ° C. The temperature at which the molten cyclic compound started to flow was visually confirmed.
<環狀二聚物>
使用藉由液體層析測定所得之圖譜,自相當於環狀二聚物之波峰面積比算出。測定裝置係使用液體層析儀(日立高科技股份有限公司製L-2000系列),檢測器係使用L-2400(日立高科技股份有限公司製),檢測波長設為270nm。管柱使用Mightysil RP-18GP150-4.6(關東化學股份有限公司製),移動相使用四氫呋喃・0.1%三氟乙酸水溶液,於40℃之測定溫度進行測定。<Cyclic Dimer>
The spectrum obtained by the liquid chromatography measurement was used to calculate from the peak area ratio corresponding to the cyclic dimer. The measurement device used a liquid chromatograph (L-2000 series manufactured by Hitachi High-Technology Co., Ltd.), the detector used L-2400 (made by Hitachi High-Technology Co., Ltd.), and the detection wavelength was set to 270 nm. Mightysil RP-18GP150-4.6 (manufactured by Kanto Chemical Co., Ltd.) was used for the column, and tetrahydrofuran · 0.1% trifluoroacetic acid aqueous solution was used for the mobile phase at a measurement temperature of 40 ° C.
<實施例1>
作為二鹵化芳香族酮使用4,4’-二氟二苯甲酮,作為間-二羥基芳香族化合物使用間苯二酚,作為對-二羥基芳香族化合物使用對苯二酚,以將間伸苯基單位(m1
)與對伸苯基單位(p1
)之莫耳比率(m1
/p1
)設為0.1之方式,進行環狀聚伸芳基醚醚酮之合成。<Example 1>
4,4'-difluorobenzophenone was used as the dihalogenated aromatic ketone, resorcinol was used as the meta-dihydroxy aromatic compound, and hydroquinone was used as the p-dihydroxy aromatic compound to separate the meta- The synthesis of the cyclic poly (arylene ether ether ketone) was performed in such a manner that the molar ratio (m 1 / p 1 ) of the phenylene unit (m 1 ) and the p-phenylene unit (p 1 ) was set to 0.1.
亦即,將4,4’-二氟二苯甲酮2.4g、間苯二酚0.11g、對苯二酚0.99g、無水碳酸鉀2.28g溶解於DMF 150mL、甲苯10mL中,於140℃進行加熱攪拌1小時,於145℃進行加熱攪拌4小時。間苯二酚與對苯二酚之莫耳比為0.11。That is, 2.4 g of 4,4'-difluorobenzophenone, 0.11 g of resorcinol, 0.99 g of hydroquinone, and 2.28 g of anhydrous potassium carbonate were dissolved in 150 mL of DMF and 10 mL of toluene at 140 ° C. Heated and stirred for 1 hour, and heated and stirred at 145 ° C for 4 hours. The molar ratio of resorcinol to hydroquinone is 0.11.
反應結束後於1%乙酸水300mL中於70℃洗淨30分鐘後,洗淨後以純水洗淨獲得餅狀物。所得粗產物使用氯仿藉由索氏萃取器萃取而洗淨,獲得環狀化合物(C-1)。所得環狀化合物之收率為7.8%而為較高者。After completion of the reaction, it was washed in 300 mL of 1% acetic acid water at 70 ° C. for 30 minutes, and then washed with pure water to obtain a cake. The obtained crude product was washed with a Soxhlet extractor using chloroform to obtain a cyclic compound (C-1). The yield of the obtained cyclic compound was 7.8%, which was the higher.
<實施例2>
除了各劑之使用量設為10倍以外,與實施例1進行同樣操作,獲得環狀化合物(C-2)。所得環狀化合物之收率為7.8%而為較高者。環狀二聚物成分之比例與開始流動溫度示於表1。<Example 2>
A cyclic compound (C-2) was obtained in the same manner as in Example 1 except that the amount of each agent was set to 10 times. The yield of the obtained cyclic compound was 7.8%, which was the higher. Table 1 shows the ratio of the cyclic dimer component and the onset temperature.
所得環狀化合物(C-2) 0.5g與氟化銫0.013g混合,於氮氣環境下於300℃加熱60分鐘,獲得聚合反應物(P-2)。藉由DSC測定所測得之玻璃轉移溫度為162℃,熔點為339℃。0.5 g of the obtained cyclic compound (C-2) was mixed with 0.013 g of cesium fluoride, and heated at 300 ° C. for 60 minutes under a nitrogen atmosphere to obtain a polymerization reaction product (P-2). The glass transition temperature measured by DSC measurement was 162 ° C, and the melting point was 339 ° C.
將所得聚合反應物(P-2)粉碎秤量15mg,於四氫呋喃10g中攪拌10分鐘萃取未反應環狀寡聚物成分,進行液體層析測定後,未確認到未反應環狀寡聚物成分。The obtained polymerization reaction product (P-2) was pulverized and weighed 15 mg, and stirred in 10 g of tetrahydrofuran for 10 minutes to extract an unreacted cyclic oligomer component. After performing liquid chromatography measurement, no unreacted cyclic oligomer component was confirmed.
<實施例3>
將實施例2所得之環狀化合物(C-2) 1.65g於四氫呋喃50g中於常溫攪拌10分鐘而溶解。自所得溶液藉過濾去除未溶解物。自過濾後之溶液使用旋轉蒸發器去除溶劑之四氫呋喃,獲得純化環狀化合物(C-3) 1.27g。環狀二聚物成分之比例與開始流動溫度示於表1。環狀二聚物成分之量為30質量%以下之實施例3,於260℃開始流動,係對纖維束含浸時之流動性優異之環狀化合物。<Example 3>
1.65 g of the cyclic compound (C-2) obtained in Example 2 was dissolved in 50 g of tetrahydrofuran at room temperature with stirring for 10 minutes. Undissolved matter was removed from the obtained solution by filtration. From the filtered solution, tetrahydrofuran of the solvent was removed using a rotary evaporator to obtain 1.27 g of a purified cyclic compound (C-3). Table 1 shows the ratio of the cyclic dimer component and the onset temperature. Example 3, in which the amount of the cyclic dimer component was 30% by mass or less, started to flow at 260 ° C, and is a cyclic compound having excellent fluidity when impregnated into a fiber bundle.
接著,將所得純化環狀化合物(C-3) 0.5g與氟化銫0.013g混合,於氮氣環境下於300℃加熱60分鐘,獲得聚合反應物(P-3)。藉由DSC測定所測得之玻璃轉移溫度為148℃,熔點為333℃,維持優異耐熱性。Next, 0.5 g of the obtained purified cyclic compound (C-3) and 0.013 g of cesium fluoride were mixed, and heated at 300 ° C. for 60 minutes under a nitrogen atmosphere to obtain a polymerization reaction product (P-3). The glass transition temperature measured by DSC measurement was 148 ° C and the melting point was 333 ° C, maintaining excellent heat resistance.
將所得聚合反應物(P-3)粉碎秤量15mg,於四氫呋喃10g中攪拌10分鐘萃取未反應環狀寡聚物成分,進行液體層析測定後,未確認到未反應環狀寡聚物成分。The obtained polymerization reaction product (P-3) was pulverized and weighed 15 mg, and stirred in 10 g of tetrahydrofuran for 10 minutes to extract an unreacted cyclic oligomer component. After performing liquid chromatography measurement, no unreacted cyclic oligomer component was confirmed.
<實施例4>
以m1
/p1
成為0.25之方式,進行環狀聚伸芳基醚醚酮之合成。除了使用間苯二酚0.22g、對苯二酚0.88g,以使間苯二酚與對苯二酚之莫耳比成為0.25以外,與實施例1進行同樣操作,獲得環狀化合物(C-4)。所得環狀化合物之收率為11.6%而較高。<Example 4>
Synthesis of cyclic poly (arylene ether ether ketone) was performed so that m 1 / p 1 was 0.25. Except that 0.22 g of resorcinol and 0.88 g of hydroquinone were used so that the molar ratio of resorcinol to hydroquinone was 0.25, the same operation as in Example 1 was performed to obtain a cyclic compound (C- 4). The yield of the obtained cyclic compound was high at 11.6%.
<實施例5>
以m1
/p1
成為0.4之方式,進行環狀聚伸芳基醚醚酮之合成。除了使用間苯二酚0.33g、對苯二酚0.77g,以使間苯二酚與對苯二酚之莫耳比成為0.43以外,與實施例1進行同樣操作,獲得環狀化合物(C-5)。所得環狀化合物之收率為19.5%而非常高。<Example 5>
Synthesis of cyclic poly (arylene ether ether ketone) was performed such that m 1 / p 1 was 0.4. Except that 0.33 g of resorcinol and 0.77 g of hydroquinone were used so that the molar ratio of resorcinol to hydroquinone was 0.43, a cyclic compound (C- 5). The yield of the obtained cyclic compound was very high at 19.5%.
<實施例6>
除了各劑之使用量設為10倍以外,與實施例5進行同樣操作,獲得環狀化合物(C-6)。所得環狀化合物之收率為19.5%而為非常高者。環狀二聚物成分之比例與開始流動溫度示於表1。<Example 6>
A cyclic compound (C-6) was obtained in the same manner as in Example 5 except that the amount of each agent was set to 10 times. The yield of the obtained cyclic compound was 19.5%, which was very high. Table 1 shows the ratio of the cyclic dimer component and the onset temperature.
<實施例7>
將實施例6所得之環狀化合物(C-6) 1.65g溶解於四氫呋喃50g中於常溫進行10分鐘攪拌。自所得溶液藉過濾去除未溶解物,使用旋轉蒸發器去除四氫呋喃,獲得純化環狀化合物(C-7) 1.5g。環狀二聚物成分之比例與開始流動溫度示於表1。環狀二聚物成分之量為30質量%以下之實施例7,於240℃開始流動,係對纖維束含浸時之流動性優異之環狀化合物。由DSC測定所測得之玻璃轉移溫度為142℃,維持優異耐熱性。又,未觀測到熔點,而為非晶性。<Example 7>
1.65 g of the cyclic compound (C-6) obtained in Example 6 was dissolved in 50 g of tetrahydrofuran and stirred at room temperature for 10 minutes. Undissolved matter was removed from the obtained solution by filtration, and tetrahydrofuran was removed using a rotary evaporator to obtain 1.5 g of a purified cyclic compound (C-7). Table 1 shows the ratio of the cyclic dimer component and the onset temperature. Example 7 in which the amount of the cyclic dimer component was 30% by mass or less, started to flow at 240 ° C., and was a cyclic compound having excellent fluidity when impregnated with a fiber bundle. The glass transition temperature measured by DSC measurement was 142 ° C, maintaining excellent heat resistance. In addition, no melting point was observed, and it was amorphous.
接著,將所得純化環狀化合物(C-7) 0.5g與氟化銫0.013g混合,於氮氣環境下於300℃加熱60分鐘,獲得聚合反應物(P-7)。Next, 0.5 g of the obtained purified cyclic compound (C-7) and 0.013 g of cesium fluoride were mixed and heated at 300 ° C. for 60 minutes in a nitrogen atmosphere to obtain a polymerization reaction product (P-7).
將所得聚合反應物(P-7)粉碎秤量15mg,於四氫呋喃10g中攪拌10分鐘萃取未反應環狀寡聚物成分,進行液體層析測定後,未確認到未反應環狀寡聚物成分。The obtained polymerization reaction product (P-7) was pulverized and weighed 15 mg, and stirred in 10 g of tetrahydrofuran for 10 minutes to extract an unreacted cyclic oligomer component. After performing liquid chromatography measurement, no unreacted cyclic oligomer component was confirmed.
<比較例1>
未使用間-二羥基芳香族化合物,以使m1
/p1
成為0之方式,進行環狀聚伸芳基醚醚酮之合成。亦即,除了不使用間苯二酚而使用對苯二酚1.10g以外,與實施例1進行同樣操作,獲得環狀化合物(C-8)。未使用間位異構物之比較例1所得之環狀化合物收率為6.5%而較低。〈Comparative example 1〉
The synthesis of a cyclic polyarylidene ether ether ketone was performed without using m-dihydroxy aromatic compound so that m 1 / p 1 became 0. That is, a cyclic compound (C-8) was obtained in the same manner as in Example 1 except that 1.10 g of hydroquinone was used instead of resorcinol. The yield of the cyclic compound obtained in Comparative Example 1 without using the meta isomer was 6.5%, which was low.
<比較例2>
除了各劑之使用量設為10倍以外,與比較例1進行同樣操作,獲得環狀化合物(C-9)。所得環狀化合物之收率為6.5%而較低者。環狀二聚物成分之比例與開始流動溫度示於表1。比較例2之環狀化合物於直至350℃之溫度未確認到流動。〈Comparative example 2〉
A cyclic compound (C-9) was obtained in the same manner as in Comparative Example 1 except that the used amount of each agent was set to 10 times. The yield of the obtained cyclic compound is 6.5%, which is lower. Table 1 shows the ratio of the cyclic dimer component and the onset temperature. The cyclic compound of Comparative Example 2 had no flow at a temperature up to 350 ° C.
將所得環狀化合物(C-9) 0.5g與氟化銫0.013g混合,於氮氣環境下於300℃加熱60分鐘,獲得聚合反應物(P-9)。藉由DSC測定所測得之玻璃轉移溫度為163℃,熔點為351℃。0.5 g of the obtained cyclic compound (C-9) was mixed with 0.013 g of cesium fluoride, and heated at 300 ° C. for 60 minutes under a nitrogen atmosphere to obtain a polymerization reaction product (P-9). The glass transition temperature measured by DSC measurement was 163 ° C, and the melting point was 351 ° C.
將所得聚合反應物(P-9)粉碎秤量15mg,於四氫呋喃10g中攪拌10分鐘萃取未反應環狀寡聚物成分,進行液體層析測定後,未確認到未反應環狀寡聚物成分。The obtained polymerization reaction product (P-9) was pulverized and weighed 15 mg, and stirred in 10 g of tetrahydrofuran for 10 minutes to extract an unreacted cyclic oligomer component. After performing liquid chromatography measurement, no unreacted cyclic oligomer component was confirmed.
[先前技術文獻]
[專利文獻]
[Prior technical literature]
[Patent Literature]
專利文獻1:國際公開第2011/081080號Patent Document 1: International Publication No. 2011/081080
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