JPH045048B2 - - Google Patents
Info
- Publication number
- JPH045048B2 JPH045048B2 JP13882784A JP13882784A JPH045048B2 JP H045048 B2 JPH045048 B2 JP H045048B2 JP 13882784 A JP13882784 A JP 13882784A JP 13882784 A JP13882784 A JP 13882784A JP H045048 B2 JPH045048 B2 JP H045048B2
- Authority
- JP
- Japan
- Prior art keywords
- hca
- ipa
- copolyarylate
- present
- polymer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000006116 polymerization reaction Methods 0.000 claims description 8
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- 125000005843 halogen group Chemical group 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 229920000642 polymer Polymers 0.000 description 16
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 15
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 11
- 229920001230 polyarylate Polymers 0.000 description 10
- 238000002156 mixing Methods 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- -1 aromatic diol Chemical class 0.000 description 6
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000005886 esterification reaction Methods 0.000 description 5
- PKZGKWFUCLURJO-GRHBHMESSA-L (z)-but-2-enedioate;dimethyltin(2+) Chemical compound C[Sn+2]C.[O-]C(=O)\C=C/C([O-])=O PKZGKWFUCLURJO-GRHBHMESSA-L 0.000 description 4
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 4
- 238000000862 absorption spectrum Methods 0.000 description 3
- 238000000921 elemental analysis Methods 0.000 description 3
- 230000009477 glass transition Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- ACVYVLVWPXVTIT-UHFFFAOYSA-N phosphinic acid Chemical compound O[PH2]=O ACVYVLVWPXVTIT-UHFFFAOYSA-N 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 2
- ZNQVEEAIQZEUHB-UHFFFAOYSA-N 2-ethoxyethanol Chemical compound CCOCCO ZNQVEEAIQZEUHB-UHFFFAOYSA-N 0.000 description 2
- FJKROLUGYXJWQN-UHFFFAOYSA-N 4-hydroxybenzoic acid Chemical compound OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000006482 condensation reaction Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000032050 esterification Effects 0.000 description 2
- 239000003063 flame retardant Substances 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 150000002736 metal compounds Chemical class 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 238000000859 sublimation Methods 0.000 description 2
- 230000008022 sublimation Effects 0.000 description 2
- 150000003460 sulfonic acids Chemical class 0.000 description 2
- BYEAHWXPCBROCE-UHFFFAOYSA-N 1,1,1,3,3,3-hexafluoropropan-2-ol Chemical compound FC(F)(F)C(O)C(F)(F)F BYEAHWXPCBROCE-UHFFFAOYSA-N 0.000 description 1
- NCYNKWQXFADUOZ-UHFFFAOYSA-N 1,1-dioxo-2,1$l^{6}-benzoxathiol-3-one Chemical compound C1=CC=C2C(=O)OS(=O)(=O)C2=C1 NCYNKWQXFADUOZ-UHFFFAOYSA-N 0.000 description 1
- WXHLLJAMBQLULT-UHFFFAOYSA-N 2-[[6-[4-(2-hydroxyethyl)piperazin-1-yl]-2-methylpyrimidin-4-yl]amino]-n-(2-methyl-6-sulfanylphenyl)-1,3-thiazole-5-carboxamide;hydrate Chemical compound O.C=1C(N2CCN(CCO)CC2)=NC(C)=NC=1NC(S1)=NC=C1C(=O)NC1=C(C)C=CC=C1S WXHLLJAMBQLULT-UHFFFAOYSA-N 0.000 description 1
- 229940090248 4-hydroxybenzoic acid Drugs 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229920006125 amorphous polymer Polymers 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 description 1
- 150000001733 carboxylic acid esters Chemical class 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- PWEVMPIIOJUPRI-UHFFFAOYSA-N dimethyltin Chemical compound C[Sn]C PWEVMPIIOJUPRI-UHFFFAOYSA-N 0.000 description 1
- 150000002009 diols Chemical group 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 238000005227 gel permeation chromatography Methods 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229940049920 malate Drugs 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N malic acid Chemical compound OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 125000001820 oxy group Chemical group [*:1]O[*:2] 0.000 description 1
- 125000004437 phosphorous atom Chemical group 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003746 solid phase reaction Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Polyesters Or Polycarbonates (AREA)
Description
産業上の利用分野
本発明は、耐熱性に優れた新規のコポリアリレ
ートに関するものである。さらに詳しくは、リン
原子を含有する芳香族ジオールおよびビスフエノ
ールAと、イソフタル酸とから得られる耐熱性お
よび難燃性に優れた新規のコポリアリレートに関
するものである。
従来の技術
従来より、耐熱性高分子としてポリアリレート
が知られている。たとえば、4−ヒドロキシ安息
香酸ホモポリマーや同コポリマー(住友化学、商
品名 エコノール)、あるいはビスフエノールA
とテレフタル酸およびイソフタル酸からなるポリ
マ−(ユニチカ,商品名 Uポリマー)がかつて
提案され、現在では市販もされている。
かかるポリマーは、本質的に
(1) 比較例的高融点であつたり、また分解温度が
融点あるいは軟化点よりも低かつたりするた
め、成形性が悪い。
(2) 色調が悪い。
(3) 透明性が悪い。
(4) 耐熱性が不十分である。
(5) 難燃性に劣る。
といつた欠点を有していた。
発明が解決しようとする問題点
本発明の主たる目的は、プラズマ溶射被覆や、
高温で使用する成形品に特に適する耐熱性コポリ
アリレートを提供することにあり、耐熱性が良
く、しかも高度な難燃性をも有した、新規な耐熱
性コポリアリレートを提供することにある。
本発明者らは前記のごとき問題点のない新しい
耐熱性コポリアリレートについて鋭意研究の結
果、特定の構造の繰り返し単位を有する含リンコ
ポリアリレートが、極めて優れた性質を有するこ
とを見出し、本発明に到達した。
問題点を解決するための手段
本発明は、次の構成を有する。
すなわち、本発明は下記構造式()および
()で示される構造単位から主としてなり、
()と()が99:1〜1:99のモル比で線状
に不規則に配列した、平均重合度10〜300である
耐熱性コポリアリレートである。
(但し、R1,R2は同種または異種の基であつ
て、それぞれハロゲン原子及び炭素数1〜8の低
級アルキル基から選ばれたものである。また、
n1,n2はそれぞれ0〜4の整数を表す。)
作 用
本発明の耐熱性コポリアリレートは、イソフタ
ル酸(以後IPAと略称する)またはそのエステル
形成誘導体と、芳香族ジオール基を有するホスフ
イン酸(以後P−HCAと略称する)またはその
エステル形成誘導体と、ビスフエノールA(以後
BAと略称する)またはそのエステル形成誘導体
とを反応させる種々のエステル形成法を利用する
ことにより製造することができる。
IPAのエステル形成誘導体としては、イソフタ
ル酸ジアルキルエステル、イソフタル酸ジアリー
ルエステル、イソフタル酸ジハライド、一方、P
−HCAあるいはBAのエステル形成誘導体として
は、ジアシルオキシ基、ジアルカリ金属オキシ基
を有する誘導体があげられる。
本発明のコポリアリレートは、上記原料を用い
て原料段階から混合してコポリマーを製造しても
よいし、前記構造単位()(以後HCA〜IPAと
略称する)および構造単位()(以後BA〜IPA
と略称する)よりなるホモポリマーを溶融混合す
ることによつても製造することができる。
本発明にいうP−HCAおよびBAの構造式を
()および()に示す。
本発明のコポリアリレートを得るうえで経済上
好ましい一例として、IPAと下記式()で示さ
れるHCAのカルボン酸エステル誘導体(p−
HCA−2Aと略称する)および下記式()で示
されるBAのカルボン酸エステル誘導体(BA−
2Aと略称する)とを高温高減圧下に縮合させる
方法があげられるが、以後本発明の製造方法をこ
の方法に従つて詳細に説明する。
(但し、Rは同種または異種の基であつて、そ
れぞれ炭素数1〜8の低級アルキル基である。)
なお、p−HCA−2AとBA−2Aは、それぞれ
前記した式(),()で示されるHCAおよび
BAを、相当するカルボン酸無水物(たとえば無
水酢酸)中で還流下エステル化させることにより
製造できる。この時IPAを存在させ、引き続いて
ポリアリレートの製造工程へ移行してもよい。
一方、P−HCAは、下記式()で示される
ホスフイン酸とp−ベンゾキノンをエチルセロソ
ルブなどの適当な溶媒中で反応させることにより
製造できる。
三者を原料段階で混合してコポリアリレートを
製造する場合には、IPAとP−HCA−2Aおよび
BA−2Aの和のモル比は通常0.8〜1.2、好ましく
は0.9〜1.1、最適には等モルとするのが好まし
い。
また、通常縮合反応には触媒が用いられるが、
本発明のコポリアリレートを得るためには、たと
えば、各種金属化合物あるいは有機スルホン酸化
合物の中から選ばれた1種以上の化合物が用いら
れる。
かかる金属化合物としては、アンチモン、チタ
ン、ゲルマニウム、スズ、亜鉛、アルミニウム、
マグネシウム、カルシウム、マンガンあるいはコ
バルトなどの化合物が用いられ、一方、有機スル
ホン酸化合物としては、スルホサリチル酸、o−
スルホ無水安息香酸などの化合物が用いられる
が、ジメチルスズマレート(以後CSと略称する)
が特に好適に用いられる。前記触媒の添加量とし
ては、ポリアリレートの構成単位1モルに対し通
常1×10-5〜1×10-2モル、好ましくは5×10-5
〜5×10-3モル、最適には1×10-4〜1×10-3モ
ル用いられる。
また、縮合反応の温度条件及び反応時間は、ま
ず通常常圧下180〜400℃で4〜12時間、とくに
250〜360℃で6〜10時間、最適には280〜320℃で
8〜10時間とするのが好ましい。
さらに減圧下(通常0.01〜10torr)180〜400℃
で1〜10時間、とくに250〜360℃で2〜8時間、
最適には280〜340℃で4〜6時間とするのが好ま
しい。
ここで、P−HCA:BAのモル比の範囲は、
99:1〜1:99、好ましくは80:20〜40:60、最
適には80:20〜60:40である。
HCA成分が多くなると強度、弾性が低下した
り、BA成分が多くなると透明性が悪くなつた
り、難燃性に劣つたりするため好ましくない。
一方、HCA〜IPAとBA〜IPAの溶融混合によ
つて本発明のコポリアリレートを得ることもでき
る。本発明におけるHCA〜IPAとBA〜IPAの混
合条件は常圧下180〜400℃で0.1〜2時間、好ま
しくは250〜360℃で0.2〜1時間とすればよい。
さらに、必要に応じて減圧下(通常0.01〜
10torr)180〜400℃で反応させ、所定の重合度と
すればよい。
本発明の耐熱性コポリアリレートの平均重合度
(n)は、10〜300、好ましくは30〜200、最適に
は50〜150である必要がある。平均重合度が、10
より小さいと前記した耐熱性を始めとする各種の
物理的、機械的、化学的特性値が劣る。
一方、平均重合度が300より大きいと、溶融粘
度が高くなりすぎて成形性、流動性などが損われ
る。
効 果
本発明によれば、
(1) 高温で使用しても分解が起こらない。
(2) 好ましいガラス転移点温度域(150〜230℃)
および好ましい融点温度域(280〜420℃)内に
入り、耐熱性に優れている。
(3) 色調、透明性に優れている。
(4) 難燃性に著しく優れている。
など、耐熱性高分子として優れた物性を有する新
規なコポリアリレートが得られるのである。ま
た、本発明のコポリアリレートは、特に耐熱性、
難燃性を要求される用途に使用されるフイルム、
繊維、成形用素材として有用である。
実施例
以下、実施例を用いて本発明をさらに詳しく説
明する。
なお、本発明にいうポリマーの平均重合度は、
ゲルパーミエーシヨンクロマトグラフイー(東洋
曹達社製HLC801A型)を用い、ヘキサフルオロ
イソプロパノールを2.5%含有したクロロホルム
溶液を溶媒として39℃の温度で測定した数平均分
子量を繰り返し単位の分子量で割ることにより求
めたものである。
また、ガラス転移点温度(Tg)および融点
(Tm)は、差動熱量計(パーキンエルマー社製
DSC−2型)を用いて測定した。
一方、本発明のコポリアリレートは、赤外線吸
収スペクトル、NMRスペクトル、ガラス転移点
温度および元素分析により同定した。
参考例 1
前記式()で示されるホスフイン酸を、エチ
ルセロソルブ溶媒中で90℃の温度でp−ベンゾキ
ノンと反応させることにより、前記式()で示
されるp−HCAを製造した。
エステル化反応装置にこのp−HCAと無水酢
酸をモル比で1対4の割合で仕込み、無水酢酸中
で還流下エステル化させることによりジ酢酸エス
テル、すなわちp−HCA−2Aを製造した。
縮合反応装置にp−HCA−2AとIPAをモル比
で1対1の割合で仕込み、触媒としてジメチルス
ズマレート(CS)をポリアリレートの構成単位
1モルに対し、1×10-4モル加え窒素雰囲気下常
圧280℃で8時間混合しながら反応させた。
留出した酢酸の重量より、エステル化反応率は
約93%であつた。
この反応物をさらに0.1torrの減圧下280℃で反
応を行い、最終的に340℃まで温度を上げて、合
計10時間縮合してHCA〜IPAのポリアリレート
を得た。
なお、減圧反応中には原料のp−HCA−2A
や、IPAの昇華は観測されなかつた。
このポリアリレートを赤外線吸収スペクトル、
NMRスペクトルおよび元素分析により分析した
ところ、次に示すような結果が得られた。
即ち、赤外線吸収スペクトルにおいては1780k
に芳香族カルボン酸エステルのC=Oに基づく吸
収が、736k,781kにパラ置換芳香族の吸収が、
878kに非対称3置換芳香族の吸収が見られた。
また、NMRスペクトルでは、原料の酢酸エス
テルに基づくメチル基の水素原子の吸収
(1.5ppmと2.3ppm)は見られなかつた。
元素分析の結果では、C=68.6%(理論値68.7
%)、H=3.37%(理論値3.33%)、P=6.79%
(理論値6.82%)という結果が得られた。
参考例 2
エステル化反応装置に前記式()で示される
BAと無水酢酸をモル比で1対4の割合で仕込
み、無水酢酸中で還流下エステル化させることに
よりジ酢酸エステル、すなわちBA−2Aを製造し
た。
縮合反応装置にBA−2AとIPAをモル比で1対
1の割合で仕込み、触媒としてジメチルスズマレ
ート(CS)をポリアリレートの構成単位1モル
に対し、1×10-4モル加え、窒素雰囲気下常圧
280℃で8時間混合しながら反応させた。
留出した酢酸の重量より、エステル化反応率は
約95%であつた。
この固体状の反応物をさらに0.1torrの減圧下
280℃の固相反応を行い、最終的に300℃まで温度
を上げて、合計10時間縮合してBA〜IPAのポリ
アリレートを得た。
なお、減圧反応中には原料のBA−2Aや、IPA
の昇華は観測されなかつた。
実施例 1
参考例1および参考例2で得たHCA〜IPAお
よびBA〜IPAのポリアリレートをモル比で1対
1の割合で縮合反応装置に仕込み、窒素雰囲気下
常圧280℃で1時間混合した。
この反応物をさらに0.1torrの減圧下300℃で反
応を行い、最終的に320℃まで温度を上げて、合
計2時間混合してコポリアリレートを得、第1表
に記載の結果を得た。
なお、このコポリアリレートは、そのNMRス
ペクトルのメチル基プロトンと芳香環プロトンの
面積比より下記構造式単位
と
が1:1の構成比のものであることを確認した。
また、得られたポリマーを300℃でテグス状に
成形し、テグスに着火してから火源を遠ざけると
直後に消火し、良好な難燃性能を有していること
がわかつた。なお、テグス状態で観察すると、色
調はやや黄色で、透明性は極めて良好であつた。
実施例 2〜7
HCA〜IPAおよびBA〜IPAのモル比を第1表
に示すごとく変えたこと以外は実施例1と同様に
実験し、第1表に記載の結果を得た。
また、実施例2,3および7で得られたポリマ
ーは300℃で、実施例4〜6で得られたポリマー
は350℃でテグス状に成形し、テグスに着火して
から火源を遠ざけると直後に消火し、良好な難燃
性能を有していることがわかつた。
なお、テグス状態で観察すると色調は薄い茶黄
色で、透明性は極めて良好であつた。
テグス状に成形後実施例4〜6のポリマーの平
均重合度を測定すると、それぞれn=79,81,80
であり、熱分解は殆ど起こつていなかつた。
INDUSTRIAL APPLICATION FIELD The present invention relates to a novel copolyarylate with excellent heat resistance. More specifically, the present invention relates to a novel copolyarylate with excellent heat resistance and flame retardancy obtained from an aromatic diol containing a phosphorus atom, bisphenol A, and isophthalic acid. BACKGROUND ART Polyarylates have been known as heat-resistant polymers. For example, 4-hydroxybenzoic acid homopolymer or copolymer (Sumitomo Chemical, trade name Econol), or bisphenol A
A polymer consisting of terephthalic acid and isophthalic acid (Unitika, trade name U Polymer) was proposed in the past, and is now commercially available. Such polymers inherently have poor moldability because (1) they have relatively high melting points, and their decomposition temperatures are lower than their melting or softening points; (2) Poor color tone. (3) Poor transparency. (4) Insufficient heat resistance. (5) Poor flame retardancy. It had the following drawbacks. Problems to be Solved by the Invention The main purpose of the present invention is to provide plasma sprayed coatings,
The object of the present invention is to provide a heat-resistant copolyarylate that is particularly suitable for molded products used at high temperatures, and to provide a new heat-resistant copolyarylate that has good heat resistance and high flame retardancy. As a result of intensive research into new heat-resistant copolyarylates that do not have the above-mentioned problems, the present inventors discovered that phosphorus-containing polyarylates having repeating units with a specific structure have extremely excellent properties. Reached. Means for Solving the Problems The present invention has the following configuration. That is, the present invention mainly consists of structural units represented by the following structural formulas () and (),
It is a heat-resistant copolyarylate in which ( ) and ( ) are arranged irregularly in a linear manner in a molar ratio of 99:1 to 1:99, and has an average degree of polymerization of 10 to 300. (However, R 1 and R 2 are the same or different groups, each selected from a halogen atom and a lower alkyl group having 1 to 8 carbon atoms.
n 1 and n 2 each represent an integer from 0 to 4. ) Effect The heat-resistant copolyarylate of the present invention comprises isophthalic acid (hereinafter abbreviated as IPA) or its ester-forming derivative, and phosphinic acid having an aromatic diol group (hereinafter abbreviated as P-HCA) or its ester-forming derivative. , bisphenol A (hereinafter
(abbreviated as BA) or its ester-forming derivative using various ester-forming methods. Ester-forming derivatives of IPA include isophthalic acid dialkyl ester, isophthalic acid diaryl ester, isophthalic acid dihalide, while P
Examples of the ester-forming derivatives of -HCA or BA include derivatives having a diacyloxy group or a dialkali metal oxy group. The copolyarylate of the present invention may be produced by mixing the above raw materials from the raw material stage to produce a copolymer, or the structural units () (hereinafter abbreviated as HCA to IPA) and the structural units () (hereinafter referred to as BA to IPA
It can also be produced by melt-mixing homopolymers consisting of (abbreviated as ). The structural formulas of P-HCA and BA referred to in the present invention are shown in () and (). As an economically preferable example for obtaining the copolyarylate of the present invention, IPA and a carboxylic acid ester derivative of HCA (p-
(abbreviated as HCA-2A) and the carboxylic acid ester derivative of BA (BA-2A) represented by the following formula ().
2A) under high temperature and high reduced pressure.The production method of the present invention will be described in detail below according to this method. (However, R is a group of the same kind or a different kind, and each is a lower alkyl group having 1 to 8 carbon atoms.) In addition, p-HCA-2A and BA-2A are the above-mentioned formulas () and (), respectively. HCA and
BA can be prepared by esterification under reflux in the corresponding carboxylic acid anhydride (eg acetic anhydride). At this time, IPA may be present, and the process may then proceed to the polyarylate production process. On the other hand, P-HCA can be produced by reacting phosphinic acid represented by the following formula () with p-benzoquinone in a suitable solvent such as ethyl cellosolve. When producing copolyarylate by mixing the three at the raw material stage, IPA, P-HCA-2A and
The molar ratio of the sum of BA-2A is usually 0.8 to 1.2, preferably 0.9 to 1.1, and optimally equimolar. In addition, a catalyst is usually used in the condensation reaction, but
In order to obtain the copolyarylate of the present invention, for example, one or more compounds selected from various metal compounds or organic sulfonic acid compounds are used. Such metal compounds include antimony, titanium, germanium, tin, zinc, aluminum,
Compounds such as magnesium, calcium, manganese or cobalt are used, while organic sulfonic acid compounds include sulfosalicylic acid, o-
Compounds such as sulfobenzoic anhydride are used, but dimethyl tin malate (hereinafter abbreviated as CS)
is particularly preferably used. The amount of the catalyst added is usually 1 x 10 -5 to 1 x 10 -2 mol, preferably 5 x 10 -5 per mol of the structural unit of polyarylate.
~5×10 −3 mol, optimally 1×10 −4 to 1×10 −3 mol is used. In addition, the temperature conditions and reaction time of the condensation reaction are usually 4 to 12 hours at 180 to 400°C under normal pressure, especially
Preferably, the temperature is 250-360°C for 6-10 hours, optimally 280-320°C for 8-10 hours. Further under reduced pressure (usually 0.01-10torr) 180-400℃
for 1 to 10 hours, especially at 250 to 360℃ for 2 to 8 hours,
Optimally, the temperature is preferably 280-340°C for 4-6 hours. Here, the range of molar ratio of P-HCA:BA is:
99:1 to 1:99, preferably 80:20 to 40:60, optimally 80:20 to 60:40. If the HCA component increases, the strength and elasticity will decrease, and if the BA component increases, the transparency will deteriorate and the flame retardance will deteriorate, which is not preferable. On the other hand, the copolyarylate of the present invention can also be obtained by melt mixing HCA-IPA and BA-IPA. The mixing conditions for HCA-IPA and BA-IPA in the present invention are 0.1 to 2 hours at 180 to 400°C under normal pressure, preferably 0.2 to 1 hour at 250 to 360°C. Furthermore, if necessary, under reduced pressure (usually 0.01 ~
10 torr) The reaction may be carried out at 180 to 400°C to achieve a predetermined degree of polymerization. The average degree of polymerization (n) of the heat-resistant copolyarylate of the present invention must be 10-300, preferably 30-200, optimally 50-150. Average degree of polymerization is 10
If it is smaller, various physical, mechanical, and chemical property values including the heat resistance described above will be inferior. On the other hand, if the average degree of polymerization is greater than 300, the melt viscosity will become too high and moldability, fluidity, etc. will be impaired. Effects According to the present invention: (1) Decomposition does not occur even when used at high temperatures. (2) Preferred glass transition temperature range (150-230℃)
It falls within the preferred melting point temperature range (280-420°C) and has excellent heat resistance. (3) Excellent color tone and transparency. (4) Excellent flame retardancy. A new copolyarylate having excellent physical properties as a heat-resistant polymer can be obtained. In addition, the copolyarylate of the present invention has particularly high heat resistance,
Films used for applications requiring flame retardancy,
Useful as fiber and molding material. Examples Hereinafter, the present invention will be explained in more detail using examples. In addition, the average degree of polymerization of the polymer referred to in the present invention is
By dividing the number average molecular weight measured at a temperature of 39°C using gel permeation chromatography (Model HLC801A manufactured by Toyo Soda Co., Ltd.) using a chloroform solution containing 2.5% hexafluoroisopropanol as the solvent by the molecular weight of the repeating unit. It's what I asked for. In addition, the glass transition temperature (Tg) and melting point (Tm) are measured using a differential calorimeter (manufactured by PerkinElmer).
DSC-2 type) was used for measurement. On the other hand, the copolyarylate of the present invention was identified by infrared absorption spectrum, NMR spectrum, glass transition temperature, and elemental analysis. Reference Example 1 p-HCA shown by the above formula () was produced by reacting phosphinic acid shown by the above formula () with p-benzoquinone at a temperature of 90° C. in an ethyl cellosolve solvent. This p-HCA and acetic anhydride were charged into an esterification reactor at a molar ratio of 1:4 and esterified in acetic anhydride under reflux to produce diacetate, ie, p-HCA-2A. P-HCA-2A and IPA were charged in a condensation reactor at a molar ratio of 1:1, and 1 x 10 -4 mol of dimethyl tin maleate (CS) was added as a catalyst per 1 mol of the constituent unit of polyarylate. The reaction was carried out under a nitrogen atmosphere at normal pressure of 280°C for 8 hours with mixing. Based on the weight of distilled acetic acid, the esterification reaction rate was approximately 93%. This reaction product was further reacted at 280° C. under a reduced pressure of 0.1 torr, and finally the temperature was raised to 340° C. and condensed for a total of 10 hours to obtain polyarylates of HCA to IPA. In addition, during the reduced pressure reaction, the raw material p-HCA-2A
No sublimation of IPA was observed. This polyarylate has an infrared absorption spectrum,
When analyzed by NMR spectrum and elemental analysis, the following results were obtained. In other words, in the infrared absorption spectrum, it is 1780k.
absorption based on C=O of aromatic carboxylic acid ester, absorption of para-substituted aromatics at 736k and 781k,
Absorption of asymmetric trisubstituted aromatics was observed at 878k. Furthermore, in the NMR spectrum, no absorption of hydrogen atoms of methyl groups (1.5 ppm and 2.3 ppm) based on the raw material acetate ester was observed. According to the results of elemental analysis, C = 68.6% (theoretical value 68.7
%), H = 3.37% (theoretical value 3.33%), P = 6.79%
(Theoretical value 6.82%) was obtained. Reference example 2 The esterification reaction device is shown by the above formula ()
BA and acetic anhydride were charged in a molar ratio of 1:4 and esterified in acetic anhydride under reflux to produce diacetate, ie, BA-2A. BA-2A and IPA were charged in a condensation reactor at a molar ratio of 1:1, and 1 x 10 -4 mol of dimethyl tin maleate (CS) was added as a catalyst per 1 mol of the constituent unit of polyarylate, and nitrogen was added. Normal pressure under atmosphere
The reaction was carried out at 280°C for 8 hours with mixing. Based on the weight of distilled acetic acid, the esterification reaction rate was approximately 95%. This solid reactant was further removed under reduced pressure of 0.1 torr.
A solid phase reaction was carried out at 280°C, and the temperature was finally raised to 300°C for a total of 10 hours of condensation to obtain polyarylates of BA to IPA. In addition, during the reduced pressure reaction, the raw materials BA-2A and IPA
No sublimation was observed. Example 1 The HCA-IPA and BA-IPA polyarylates obtained in Reference Example 1 and Reference Example 2 were charged into a condensation reactor at a molar ratio of 1:1, and mixed for 1 hour at 280°C under nitrogen atmosphere at normal pressure. did. This reaction product was further reacted at 300° C. under a reduced pressure of 0.1 torr, and the temperature was finally raised to 320° C. and mixed for a total of 2 hours to obtain a copolyarylate, and the results shown in Table 1 were obtained. This copolyarylate has the following structural formula unit based on the area ratio of methyl group protons and aromatic ring protons in its NMR spectrum. and It was confirmed that the composition ratio was 1:1. In addition, the resulting polymer was molded into a string shape at 300°C, and when the string was ignited and the fire source was moved away, the fire extinguished immediately, indicating that it had good flame retardant properties. In addition, when observed in a transparent state, the color tone was slightly yellow and the transparency was extremely good. Examples 2 to 7 Experiments were carried out in the same manner as in Example 1, except that the molar ratios of HCA to IPA and BA to IPA were changed as shown in Table 1, and the results shown in Table 1 were obtained. In addition, the polymers obtained in Examples 2, 3, and 7 were molded at 300°C, and the polymers obtained in Examples 4 to 6 were molded into a string shape at 350°C, and after igniting the string, the fire source was moved away. The fire was extinguished immediately, and it was found that it had good flame retardant performance. In addition, when observed in a sticky state, the color tone was light brown-yellow, and the transparency was extremely good. When the average degree of polymerization of the polymers of Examples 4 to 6 was measured after molding into a string shape, n = 79, 81, and 80, respectively.
Therefore, almost no thermal decomposition occurred.
【表】
* 非晶質ポリマーとなつた。
参考例 1〜2
参考例として、ポリエチレンテレフタレートと
Uポリマー(ユニチカ,商品名U−100)の特性
値を第2表に示した。
ポリエチレンテレフタレートは、色調、透明性
は良好であるが、テグスに着火すると火源を遠ざ
けても燃え尽きる迄燃焼が続いた。また、Tgは
本発明のポリマーより低く、耐熱性が劣ることが
わかる。
また、Uポリマーは茶色の着色があり、テグス
に着火して火源を遠ざけると数秒間は燃焼が続
き、本発明のポリマーより難燃性がやや劣ること
がわかる。
なお、エコノール(住友化学,商品名E2000)
は熱変形温度293℃と耐熱性に優れているものの
着火すると数秒間は燃焼が続き、本発明のポリマ
ーより難燃性がやや劣ることがわかる。[Table] * Became an amorphous polymer.
Reference Examples 1 and 2 As reference examples, the characteristic values of polyethylene terephthalate and U polymer (Unitika, trade name U-100) are shown in Table 2. Polyethylene terephthalate has a good color tone and transparency, but when it was ignited, it continued to burn until it burned out even if the fire source was moved away. Further, it can be seen that the Tg is lower than that of the polymer of the present invention, and the heat resistance is inferior. In addition, the U polymer has a brown color, and when the flame source is ignited and the fire source is moved away, the U polymer continues to burn for several seconds, indicating that the flame retardance is slightly inferior to that of the polymer of the present invention. In addition, Econol (Sumitomo Chemical, trade name E2000)
Although it has excellent heat resistance with a heat distortion temperature of 293°C, it continues to burn for several seconds when ignited, indicating that its flame retardance is slightly inferior to that of the polymer of the present invention.
Claims (1)
単位から主としてなり、()と()が99:1
〜1:99のモル比で線状に不規則に配列した、平
均重合度10〜300である耐熱性コポリアリレート。 (但し、R1,R2,は同種または異種の基であ
つて、それぞれハロゲン原子および炭素数1〜8
の低級アルキル基から選ばれたものである。ま
た、n1,n2はそれぞれ0〜4の整数を表す。) [Claims] 1 Mainly composed of structural units represented by the following structural formulas () and (), where () and () are 99:1
A heat-resistant copolyarylate having an average degree of polymerization of 10 to 300, linearly and irregularly arranged in a molar ratio of ~1:99. (However, R1 and R2 are the same or different groups, and each has a halogen atom and a carbon number of 1 to 8
is selected from lower alkyl groups. Further, n 1 and n 2 each represent an integer of 0 to 4. )
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13882784A JPS6116924A (en) | 1984-07-04 | 1984-07-04 | Heat-resistant copolyarylate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13882784A JPS6116924A (en) | 1984-07-04 | 1984-07-04 | Heat-resistant copolyarylate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6116924A JPS6116924A (en) | 1986-01-24 |
| JPH045048B2 true JPH045048B2 (en) | 1992-01-30 |
Family
ID=15231148
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13882784A Granted JPS6116924A (en) | 1984-07-04 | 1984-07-04 | Heat-resistant copolyarylate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6116924A (en) |
-
1984
- 1984-07-04 JP JP13882784A patent/JPS6116924A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6116924A (en) | 1986-01-24 |
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