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JP2004189860A - Condensed thermoplastic resin composition and use thereof - Google Patents

Condensed thermoplastic resin composition and use thereof Download PDF

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Publication number
JP2004189860A
JP2004189860A JP2002358816A JP2002358816A JP2004189860A JP 2004189860 A JP2004189860 A JP 2004189860A JP 2002358816 A JP2002358816 A JP 2002358816A JP 2002358816 A JP2002358816 A JP 2002358816A JP 2004189860 A JP2004189860 A JP 2004189860A
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thermoplastic resin
compound
resin composition
aliphatic
hindered amine
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JP4151398B2 (en
Inventor
Seiji Sawada
誠司 沢田
Nobuyuki Uchida
信幸 内田
Yoshihiko Kobayashi
嘉彦 小林
Masashi Koide
昌史 小出
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Artience Co Ltd
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Toyo Ink Mfg Co Ltd
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Abstract

【課題】縮合型熱可塑性樹脂の加水分解に伴う劣化を抑制し、機械的物性や表面状態等が優れた縮合型熱可塑性樹脂成形品を提供すること。
【解決手段】脂肪族カルボジイミド化合物とヒンダードアミン系化合物を含有する縮合型熱可塑性樹脂組成物であって、脂肪族ポリカルボジイミド化合物の含有量が0.01〜60重量%、ヒンダードアミン系化合物の含有量が0.01〜60重量%であることを特徴とする縮合型熱可塑性樹脂組成物、及びこれを用いて得られる成形品。
【選択図】なし
An object of the present invention is to provide a condensed thermoplastic resin molded article which suppresses deterioration due to hydrolysis of a condensed thermoplastic resin and has excellent mechanical properties and surface condition.
A condensed thermoplastic resin composition containing an aliphatic carbodiimide compound and a hindered amine compound, wherein the content of the aliphatic polycarbodiimide compound is 0.01 to 60% by weight and the content of the hindered amine compound is 0.01 to 60% by weight. A condensation type thermoplastic resin composition characterized by being 0.01 to 60% by weight, and a molded product obtained by using the same.
[Selection diagram] None

Description

【0001】
【発明の属する技術分野】
本発明は、耐熱劣化、耐加水分解性に優れた縮合型熱可塑性樹脂組成物、及び当該樹脂組成物を用いて得られる成形品に関する。
【0002】
【従来の技術】
従来、熱可塑性ポリエステル樹脂は比較的耐熱性の高い樹脂として、フィルム,シート,繊維,容器等の成形品として高温下や屋外等で広く使用されている。
この熱可塑性ポリエステル樹脂は成形品製造の際の溶融混練工程において、加熱,アルカリ,水分により酸化,加水分解等の劣化が起こり易い。この劣化は無機充填材,金属,金属酸化物,染料または顔料等の存在下で促進され、変色,分子量低下,機械的物性の低下等を引き起こす。
【0003】
また、長期間経過後に樹脂中のカルボキシル基、更には樹脂自体の加水分解により生成されたカルボキシル基が触媒となって樹脂分子が加水分解を受け、物性低下を引き起こして成形品の耐久性の低下に繋がり、商品的価値を大いに損失させるという問題があった。
【0004】
このような問題点を解決する手段として、リン系化合物を添加して重合触媒を失活させることにより熱劣化防止性を防止する技術がある(例えば、特許文献1参照。)が、物性の向上が不十分であった。
モノカルボジイミド化合物により脂肪族ポリエステルのカルボキシル基末端の一部または実質的に全部を封する技術(例えば、特許文献2参照。)は、架橋しない為にポリエステル樹脂の物性向上が不十分であった。また、芳香族系ポリカルボジイミドは耐熱性がなく黄味に着色し、ゲル化が起きて成形品の外観が劣る問題があった。
【0005】
ポリカルボジイミドによるポリエステル樹脂の熱劣化、加水分解抑制の技術(例えば、特許文献3参照。)では、成形時にゲル化が起こり均質な成形品とすることが困難であるといった問題があった。
また、耐加水分解性向上を目的として生分解性プラスチックにカルボジイミド化合物を配合する技術が開示されている(例えば、特許文献4参照。)。しかしながらカルボジイミド化合物の耐熱性が不足し、これらがプラスチック成形時に気化するため十分な効果が得られず成形品の耐熱性が低く、外観が劣るなどの問題があった。
【0006】
【特許文献1】
特開平10−259296号公報
【特許文献2】
特開2001−261797号公報
【特許文献3】
特開平10−43681号公報
【特許文献4】
特開平11−80522号公報
【発明が解決しようとする課題】
【0007】
【課題を解決するための手段】
本発明の発明者らは、縮合型熱可塑性樹脂成形品の耐加水分解性を高めるには、脂肪族ポリカルボジイミド化合物とヒンダードアミン系化合物の併用が有効であることを見出し、本発明を完成するに至った。
すなわち、本発明は、熱可塑性ポリエステル樹脂の劣化の要因となるカルボキシル末端を封鎖、失活せしめる脂肪族系ポリカルボジイミド化合物と、このポリカルボジイミドの自己縮合や酸化劣化を抑制し、樹脂に効果的に作用させるヒンダードアミン系化合物とを含有した縮合型熱可塑性樹脂組成物及び当該組成物を用いてなる成形品である。
【0008】
本発明の第1の発明は、脂肪族カルボジイミド化合物とヒンダードアミン系化合物を含有することを特徴とする縮合型熱可塑性樹脂組成物である。
第2の発明は、脂肪族ポリカルボジイミド化合物の含有量が0.01〜60重量%、ヒンダードアミン系化合物の含有量が0.01〜60重量%である第1の発明に記載の縮合型熱可塑性樹脂組成物である。
【0009】
第3の発明は、縮合型熱可塑性樹脂がポリエステル樹脂である第1又は第2の発明に記載の縮合型熱可塑性樹脂組成物である。
第4の発明は、縮合型熱可塑性樹脂がポリ乳酸、ポリカプロラクトン、脂肪族ジカルボン酸と多価アルコールを主原料として得られる樹脂、微生物または植物より合成されたポリエステル樹脂である群から選択される少なくとも1種の微生物崩壊性樹脂である第1〜第3の発明いずれかに記載の縮合型熱可塑性樹脂組成物である。
【0010】
第5の発明は、第1〜第4の発明いずれかに記載の縮合型熱可塑性樹脂組成物から得られる成形品である。
第6の発明は、脂肪族カルボジイミド化合物とヒンダードアミン系化合物を含有することを特徴とする縮合型熱可塑性樹脂成形品の劣化防止方法である。
【0011】
【発明の実施の形態】
以下、本発明を具体的に詳述する。
本発明において用いられる縮合型熱可塑性樹脂としては、熱可塑性ポリエステル樹脂が挙げられる。熱可塑性ポリエステル樹脂とは、ジオールとジカルボン酸とから縮重合によって得られるポリマーである。
ジカルボン酸としてはテレフタル酸、イソフタル酸、フタル酸、ナフタレンジカルボン酸、アジピン酸、セバシン酸等が挙げられ、またジオールとしてはエチレングリコール、トリメリレングリコール、テトラメチレングリコール、シクロヘキサンジメタノール等が挙げられる。
具体的には、ポリエチレンテレフタレート、ポリエチレン−p−オキシベンゾエート、ポリ−1,4−シクロヘキシレンジメチレンテレフタレート、ポリエチレン−2,6−ナフタレンジカルボキシレート等を使用することができる。
【0012】
これらのポリエステル樹脂はホモポリエステルでもコポリエステルでもよく、共重合成分としては、例えばジエチレングリコール、ネオペンチルグリコール、ポリアルキレングリコール等のグリコール成分、アジピン酸、セバシン酸、フタル酸、イソフタル酸、2,6−ナフタレンジカルボン酸、5−ナトリウムスルホイソフタル酸等のジカルボン酸成分を用いることができる。
【0013】
本発明において用いられる縮合型熱可塑性樹脂として、微生物崩壊性樹脂も用いることができる。微生物崩壊性樹脂としてはポリ乳酸、ポリカプロラクトン、または脂肪族ジカルボン酸と多価アルコールとを原料として得られる脂肪族ポリエステル系樹脂の他、微生物または植物より合成されたポリエステル樹脂等が挙げられる。
【0014】
具体的には、市販または試作されている各社の微生物崩壊性樹脂が挙げられ、例えば昭和高分子社製や日本触媒社製のポリブチレンサクシネート、ポリエチレンサクシネート、ポリブチレンサクシネート・アジペート、三井化学社製、カーギル社製や島津社製のポリ乳酸、ダイセル化学社製のポリカプロラクトン、モンサント社製のポリ(3−ヒドロキシ酪酸−CO−3−ヒドロキシ吉草酸)(P(3HB−3HV))やポリ(3−ヒドロキシ酪酸−CO−4−ヒドロキシ酪酸)(P(3HB−4HB))やポリ(3−ヒドロキシ酪酸−CO−3−ヒドロキシプロピオネート)(P(3HB−3HP))等が挙げられる。
【0015】
本発明において用いられる脂肪族ポリカルボジイミド化合物は、カルボジイミド結合を分子内(ポリマー主鎖)に2個以上有する化合物であり、任意の脂肪族イソシアネート化合物を反応させて得られる。その重合度(n)は、大きすぎると脂肪族系ポリカルボジイミド化合物自身の安定性が悪くなる恐れがあるため、3〜20であることが好ましく、また、分子量は500以上10,000未満であることが好ましい。尚、芳香族ポリカルボジイミド化合物は、自己縮合や凝集の恐れがあり、縮合物や凝集物が成形品の表面状態や機械的強度を低下させるので本発明においては用いられない。
【0016】
原料となるイソシアネートとしては、例えばヘキサメチレンジイソシアネート,トリメチルヘキサメチレンジイソシアネート,イソホロンジイソシアネート,多官能脂肪族イソシアネート,ブロック多官能脂肪族イソシアネート,水添キシリレンジイソシアネート,水添ジフェニルメタンジイソシアネート,芳香族系イソシアネートの水添加物等が挙げられ、これらの1種又は2種以上を好ましく使用することができる。
【0017】
本発明において用いられるヒンダードアミン系化合物とはメチルピペリジン骨格を有する化合物である。例えばコハク酸ジメチル−1−(2−ヒドロキシエチル)−4−ヒドロキシ−2,2,6,6−テトラメチルピペリジン重縮合物、ポリ〔{6−(1,1,3,3−テトラメチルブチル)アミノ−1,3,5−トリアジン−2,4−ジイル}{(2,2,6,6−テトラメチル−4−ピペリジル)イミノ}ヘキサメチレン{(2,2,6,6−テトラメチル−4−ピペリジル)イミノ}〕、N,N’−ビス(3−アミノプロピル)エチレンジアミン・2,4−ビス〔N−ブチル−N−(1,2,2,6,6−ペンタメチル−4ピペリジル)アミノ〕−6−クロロ−1,3,5−トリアジン縮合物、ビス(2,2,6,6−テトラメチル−4−ピペリジル)セバケート等が挙げられる。
【0018】
ヒンダードアミン系化合物の平均分子量は450〜5000が好ましい。特に薄物成形品には平均分子量が2000以上の高分子量のものが好ましい。
【0019】
脂肪族ポリカルボジイミド化合物及びヒンダードアミン系化合物は、単独で縮合型熱可塑性樹脂に使用しても得られる効果が低いため、本件発明では用いられない。すなわち、ヒンダードアミン系化合物は脂肪族ポリカルボジイミド化合物の自己縮合や酸化劣化を抑制するので、脂肪族ポリカルボジイミド化合物を縮合型熱可塑性樹脂のカルボキシル基と効果的に反応させることができる。更に、ヒンダードアミン系化合物は脂肪族ポリカルボジイミド化合物が金属酸化物、タルク等の無機フィラー、顔料等と凝集することを防ぎ、これらの凝集物が成形品表面に吸着することを抑制し成形品の外観を良好にする作用がある。
【0020】
また、本発明の縮合型熱可塑性樹脂組成物には、本発明の効果を損なわない範囲内で必要に応じて適当な添加剤、例えば、耐熱安定剤、耐酸化安定剤、耐候安定剤、帯電防止剤、染料、顔料、分散剤、カップリング剤等を配合してもよい。
【0021】
本発明の熱可塑性縮合型樹脂組成物の製造は特に限定されるものではない。例えば、縮合型熱可塑性樹脂、脂肪族ポリカルボジイミド化合物、ヒンダードアミン系化合物と、更に必要に応じて各種添加剤や着色剤等を加え、ヘンシェルミキサーやタンブラー、ディスパー等で混合しニーダー,ロールミル,スーパーミキサー,ヘンシェルミキサー,シュギミキサー,バーティカルグラニュレーター,ハイスピードミキサー,ファーマトリックス,ボールミル,スチールミル,サンドミル,振動ミル,アトライター,バンバリーミキサーのような回分式混練機、二軸押出機、単軸押出機、ローター型二軸混練機等で混合や溶融混練分散し、ペレット状、粉体状、顆粒状あるいはビーズ状等の形状の縮合型熱可塑性樹脂組成物を得ることができる。
【0022】
本発明の縮合型熱可塑性樹脂組成物は、脂肪族ポリカルボジイミド化合物及びヒンダードアミン系化合物を比較的高濃度に含有し、成形時に被成形樹脂(ベース樹脂)で希釈されるマスターバッチであっても良いし、脂肪族ポリカルボジイミド化合物及びヒンダードアミン系化合物濃度が比較的低く、被成形樹脂で希釈せずにそのままの組成で成形に供されるコンパウンドであっても良い。
【0023】
コンパウンドまたは成形品における脂肪族ポリカルボジイミド化合物の含有量は、充分な耐加水分解性や機械的物性等を得る観点から0.01重量%以上、成形品の着色の防止や柔軟性を保つ観点から10重量%以下が好ましい。また、ヒンダードアミン系化合物の含有量は、充分な性能を発揮させる観点から0.01重量%以上、成形品の着色の防止やコスト抑制の観点から10重量%以下が好ましい。
【0024】
マスターバッチにおける脂肪族ポリカルボジイミド化合物の含有量は、少な過ぎると充分な耐加水分解性を得られにくく大量のマスターバッチを添加する必要が生じて不経済であるばかりでなく、成形品の機械物性に支障を来し易いため、1重量%以上が好ましい。また、多過ぎるとマスターバッチ自体の製造効率が悪くなったり、被成形樹脂に少量添加することになるため均一化が困難となり分配性や分散性が悪化しブツ等が発生しやすい傾向になったり、更には脂肪族ポリカルボジイミド化合物に由来するベタつきの抑制や被成形樹脂との混合性、自己縮合に伴う凝集物が成形品に発生することを抑制する観点から60重量%以下が好ましい。特に40重量%以下が好ましく、5〜30重量%の範囲が最も好ましい。
【0025】
マスターバッチにおけるヒンダードアミン系化合物の含有量は、多量のマスターバッチを添加することなく充分な性能を発揮させる観点から1重量%以上が好ましく、特に5重量%が好ましい。多量のマスターバッチを添加して成形品を得た場合、良好な機械物性を有しない恐れがある。また、含有量が多いとマスターバッチの被添加樹脂への添加量が少なくなるため、ヒンダードアミン系化合物が偏在する恐れがあり均一化が困難となるので、90重量%以下が好ましい。特に60重量%以下が好ましい。
【0026】
本発明の成形品は、押出成形、射出成形、ブロー成形のいずれかの成形方法で得られるものでもよいし、縮合型熱可塑性樹脂組成物を粉砕して得られる粉体塗料でもよい。
【0027】
【実施例】
以下、本発明を具体的に実施例をもって説明する。以下の記載において、部は重量部を、%は重量%をそれぞれ表す。
【0028】
(1)コンパウンドの製造
[実施例1〜10]
表1に示すように、成分(ア)、成分(イ)、成分(ウ)を均一混合し、直径30mm二軸押出機にてスクリュー回転数250rpmにて溶融混練し、コンパウンドを得た。溶融混練の際の温度は、成分(ウ)がPETの場合は設定温度280℃、PLAの場合は設定温度200℃で行った。
【0029】
[比較例1〜12]
表2に示すように、成分(ア)、成分(イ)、成分(ウ)を均一混合し、実施例1〜10と同様にしてコンパウンドを得た。
【0030】
(2)マスターバッチの製造
[実施例11〜20]
表1に示すように、成分(ア)、成分(イ)、成分(ウ)を均一混合し、直径30mm二軸押出機にてスクリュー回転数250rpmにて溶融混練し、マスターバッチを製造した。溶融混練の際の温度は、成分(ウ)がPETの場合は設定温度280℃、PLAの場合は設定温度200℃で行った。
【0031】
[比較例13〜24]
表2に示すように、成分(ア)、成分(イ)、成分(ウ)を均一混合し、実施例11〜20と同様にしてマスターバッチを得た。比較例21〜24はマスターバッチ製造時に二軸押出機のダイスヘッド部より発煙が生じた。
【0032】
【表1】

Figure 2004189860
【0033】
表1中、「脂肪族PC−1」は水添ジフェニルメタンジイソシアネ−トを原料とした脂肪族系ポリカルボジイミド化合物であるジシクロヘキシルメタン−4,4−ポリカルボジイミド、
「脂肪族PC−2」はヘキサメチレンジイソシアネ−トを原料とする脂肪族系ポリカルボジイミド化合物であるヘキサメチレンポリカルボジイミド、
「脂肪族PC−3」はメチルヘキサメチレンジイソシアネ−トを原料とする脂肪族系ポリカルボジイミド化合物である3−メチルヘキサメチレンポリカルボジイミド、
「HALS」はシ゛フ゛チルアミン・1,3,5−トリアシ゛ン・N,N−ヒ゛ス(2,2,6,6−テトラメチル−4−ヒ゜ヘ゜リシ゛ル−1,6−ヘキサメチメチレンシ゛アミン・N−(2,2,6,6−テトラメチル−4−ヒ゜ヘ゜リシ゛ル)フ゛チルアミンの重縮合物、
「PET」はポリエチレンテレフタレ−ト(固有粘度=0.83)、
「PLA」はポリ乳酸(固有粘度=1.90)を用いた。
【0034】
【表2】
Figure 2004189860
【0035】
表2中、表1と共通のものは表1の説明に準ずる。
「芳香族PC」はトルエンジイソシアネ−トを原料とした芳香族系ポリカルボジイミド(ラインケミ−社)、
「脂肪族MC」はジイソプロピルカルボジイミドを用いた。
【0036】
[評価試験]
以上の実施例及び比較例で得られたコンパウンドとマスターバッチについて以下の評価を行い、結果を表3、4に示した。
a.加水分解性評価
実施例1〜10、比較例1〜12で得られたコンパウンドは、そのままの組成のものを以下のa1で用いた。
また、実施例11〜20、比較例13〜24で得られたマスターバッチは、それぞれベース樹脂(各々成分(ウ)で用いた樹脂と同じ樹脂を用いた。)で10倍希釈されるように混合した。その混合物をスクリュー直径30mm、L/D値30の単軸押出機に供給し、回転数100rpmの条件でペレット化してコンパウンドを製造した。溶融混練の際の温度は、成分(ウ)がPETの場合は設定温度280℃、PLAの場合は設定温度200℃で行った。
【0037】
a1.固有粘度値
得られたコンパウンドを140℃で2時間乾燥後、100mlメスフラスコに0.5g秤量し、フェノール:1,1,2,2−テトラクロロエタン=1:1溶液100mlを正確に加えた。これを150℃で1.5時間攪拌溶解して測定サンプルとした。毛細管粘度自動測定装置(芝山科学株式会社「SS−600−L2型」)を用いて固有粘度値を測定した。被成形樹脂のみ(成分(ウ)であるPETまたはPLA)の場合を100%として、各コンパウンドの固有粘度値の保持率を求め、以下の基準に従い評価した。
○:固有粘度値の保持率96%以上
△:固有粘度値の保持率90%以上96%未満
×:固有粘度値の保持率90%未満
【0038】
a2.機械物性保持率
実施例1〜10、比較例1〜12で得られたコンパウンドは、そのままの組成のものを射出成形機にて背圧10kg/cmで射出成形し、プレ−トを得た。
また、実施例11〜20、比較例13〜24で得られたマスターバッチは、それぞれベース樹脂(各々成分(ウ)で用いた樹脂と同じ樹脂を用いた。)で10倍希釈されるように混合した。その混合物を射出成形機にて背圧10kg/cmで射出成形し、プレ−トを得た。
【0039】
各プレ−トについて、引張強度試験(JIS K7113)アイゾット衝撃試験(JIS K7110)を行い、被成形樹脂のみからなるプレ−トの値を100%としたときの各プレ−トの保持率をそれぞれ求め、以下の基準に従い評価した。
○:96%以上
△:90%以上96%未満
×:90%以下
【0040】
b.成形物表面状態評価
a2の機械物性保持率評価において作成した射出成形プレートの表面状態を電子顕微鏡及び目視により観察し、以下の基準に従い評価した。
○:表面が平滑であり、ゲル、ブツ等が見あたらない。
△:表面が平滑であるが、少数のブツが確認できる。
×:表面が凹凸であり、ゲル、ブツが多く確認できる。
【0041】
【表3】
Figure 2004189860
【0042】
【表4】
Figure 2004189860
【0043】
【発明の効果】
本発明の縮合型熱可塑性樹脂組成物は、脂肪族ポリカルボジイミド化合物とヒンダードアミン系化合物を含有するので、実用性のある充分高い耐加水分解性及び耐熱性を有する。
従ってこれを用いて得られる縮合型熱可塑性樹脂成形品は、機械物性や表面状態が良好であるので従来以上に幅広い利用が可能である。[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a condensation-type thermoplastic resin composition having excellent heat resistance and hydrolysis resistance, and a molded product obtained by using the resin composition.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, a thermoplastic polyester resin has been widely used as a resin having relatively high heat resistance, such as a film, a sheet, a fiber, and a molded article such as a container under a high temperature or outdoors.
This thermoplastic polyester resin is liable to be deteriorated by oxidation, hydrolysis and the like due to heating, alkali and moisture in the melt-kneading step in the production of molded articles. This deterioration is accelerated in the presence of an inorganic filler, a metal, a metal oxide, a dye or a pigment, and causes discoloration, a decrease in molecular weight, a decrease in mechanical properties, and the like.
[0003]
In addition, after a long period of time, the carboxyl group in the resin, and further the carboxyl group generated by hydrolysis of the resin itself, acts as a catalyst to hydrolyze the resin molecules, causing a decrease in physical properties and a decrease in the durability of the molded article. And there is a problem that the commercial value is greatly lost.
[0004]
As a means for solving such a problem, there is a technique of adding a phosphorus compound to deactivate the polymerization catalyst to prevent the property of preventing thermal degradation (see, for example, Patent Document 1). Was inadequate.
The technique of sealing a part or substantially all of the terminal of the carboxyl group of the aliphatic polyester with the monocarbodiimide compound (for example, see Patent Document 2) has not been sufficient to improve the physical properties of the polyester resin because it does not crosslink. In addition, the aromatic polycarbodiimide has a problem that it does not have heat resistance and is colored yellowish, gelation occurs, and the appearance of a molded article is deteriorated.
[0005]
The technology for suppressing thermal degradation and hydrolysis of a polyester resin by polycarbodiimide (for example, see Patent Document 3) has a problem that gelation occurs during molding and it is difficult to obtain a uniform molded product.
Further, a technique of blending a carbodiimide compound with a biodegradable plastic for the purpose of improving hydrolysis resistance has been disclosed (for example, see Patent Document 4). However, the carbodiimide compounds have insufficient heat resistance, and they are vaporized at the time of plastic molding, so that a sufficient effect cannot be obtained. Thus, there are problems such as low heat resistance of molded articles and poor appearance.
[0006]
[Patent Document 1]
JP-A-10-259296 [Patent Document 2]
JP 2001-261797 A [Patent Document 3]
Japanese Patent Application Laid-Open No. H10-43681 [Patent Document 4]
JP-A-11-80522 [Problems to be Solved by the Invention]
[0007]
[Means for Solving the Problems]
The inventors of the present invention have found that a combination use of an aliphatic polycarbodiimide compound and a hindered amine-based compound is effective for enhancing the hydrolysis resistance of a condensation-type thermoplastic resin molded article. Reached.
That is, the present invention is an aliphatic polycarbodiimide compound that blocks and deactivates the carboxyl terminus that causes the deterioration of the thermoplastic polyester resin, and suppresses the self-condensation and oxidative deterioration of the polycarbodiimide. A condensed thermoplastic resin composition containing a hindered amine compound to be acted on and a molded article using the composition.
[0008]
The first invention of the present invention is a condensation type thermoplastic resin composition comprising an aliphatic carbodiimide compound and a hindered amine compound.
In the second invention, the condensation type thermoplastic resin according to the first invention, wherein the content of the aliphatic polycarbodiimide compound is 0.01 to 60% by weight and the content of the hindered amine compound is 0.01 to 60% by weight. It is a resin composition.
[0009]
A third invention is the condensation thermoplastic resin composition according to the first or second invention, wherein the condensation thermoplastic resin is a polyester resin.
In a fourth aspect, the condensation type thermoplastic resin is selected from the group consisting of polylactic acid, polycaprolactone, a resin obtained using aliphatic dicarboxylic acid and polyhydric alcohol as main raw materials, and a polyester resin synthesized from microorganisms or plants. The condensed thermoplastic resin composition according to any one of the first to third inventions, which is at least one kind of microbial disintegrating resin.
[0010]
A fifth invention is a molded article obtained from the condensation type thermoplastic resin composition according to any one of the first to fourth inventions.
A sixth invention is a method for preventing deterioration of a condensed thermoplastic resin molded article, characterized by containing an aliphatic carbodiimide compound and a hindered amine compound.
[0011]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be described in detail.
Examples of the condensation type thermoplastic resin used in the present invention include a thermoplastic polyester resin. The thermoplastic polyester resin is a polymer obtained by condensation polymerization of a diol and a dicarboxylic acid.
Examples of the dicarboxylic acid include terephthalic acid, isophthalic acid, phthalic acid, naphthalenedicarboxylic acid, adipic acid, and sebacic acid. Examples of the diol include ethylene glycol, trimellilene glycol, tetramethylene glycol, and cyclohexane dimethanol.
Specifically, polyethylene terephthalate, polyethylene-p-oxybenzoate, poly-1,4-cyclohexylene dimethylene terephthalate, polyethylene 2,6-naphthalenedicarboxylate and the like can be used.
[0012]
These polyester resins may be a homopolyester or a copolyester. Examples of the copolymerization component include glycol components such as diethylene glycol, neopentyl glycol and polyalkylene glycol, adipic acid, sebacic acid, phthalic acid, isophthalic acid, and 2,6- Dicarboxylic acid components such as naphthalenedicarboxylic acid and 5-sodium sulfoisophthalic acid can be used.
[0013]
As the condensation type thermoplastic resin used in the present invention, a biodegradable resin can also be used. Examples of the biodegradable resin include polylactic acid, polycaprolactone, an aliphatic polyester resin obtained using aliphatic dicarboxylic acid and a polyhydric alcohol as raw materials, and a polyester resin synthesized from a microorganism or a plant.
[0014]
Specific examples include commercially available or prototype biodegradable resins of various companies, for example, polybutylene succinate, polyethylene succinate, polyethylene succinate, polybutylene succinate adipate, manufactured by Showa Polymer Co., Ltd. and Nippon Shokubai Co., Ltd., Mitsui Polylactic acid manufactured by Chemical Co., Cargill or Shimadzu, polycaprolactone manufactured by Daicel Chemical Co., Ltd., poly (3-hydroxybutyric acid-CO-3-hydroxyvaleric acid) manufactured by Monsanto (P (3HB-3HV)) And poly (3-hydroxybutyric acid-CO-4-hydroxybutyric acid) (P (3HB-4HB)) and poly (3-hydroxybutyric acid-CO-3-hydroxypropionate) (P (3HB-3HP)) No.
[0015]
The aliphatic polycarbodiimide compound used in the present invention is a compound having two or more carbodiimide bonds in the molecule (polymer main chain), and is obtained by reacting an arbitrary aliphatic isocyanate compound. If the polymerization degree (n) is too large, the stability of the aliphatic polycarbodiimide compound itself may be deteriorated, so that it is preferably 3 to 20, and the molecular weight is 500 or more and less than 10,000. Is preferred. The aromatic polycarbodiimide compound is not used in the present invention because it has a risk of self-condensation or aggregation, and the condensate or aggregate reduces the surface state or mechanical strength of the molded article.
[0016]
Examples of the isocyanate used as a raw material include water of hexamethylene diisocyanate, trimethylhexamethylene diisocyanate, isophorone diisocyanate, polyfunctional aliphatic isocyanate, block polyfunctional aliphatic isocyanate, hydrogenated xylylene diisocyanate, hydrogenated diphenylmethane diisocyanate, and aromatic isocyanate. Additives and the like can be mentioned, and one or more of these can be preferably used.
[0017]
The hindered amine compound used in the present invention is a compound having a methylpiperidine skeleton. For example, dimethyl-1- (2-hydroxyethyl) -4-hydroxy-2,2,6,6-tetramethylpiperidine succinate polycondensate, poly [{6- (1,1,3,3-tetramethylbutyl) ) Amino-1,3,5-triazine-2,4-diyl {(2,2,6,6-tetramethyl-4-piperidyl) imino} hexamethylene} (2,2,6,6-tetramethyl -4-piperidyl) imino}], N, N'-bis (3-aminopropyl) ethylenediamine 2,4-bis [N-butyl-N- (1,2,2,6,6-pentamethyl-4piperidyl) ) Amino] -6-chloro-1,3,5-triazine condensate, bis (2,2,6,6-tetramethyl-4-piperidyl) sebacate and the like.
[0018]
The average molecular weight of the hindered amine compound is preferably from 450 to 5,000. Particularly, a thin molded article having a high molecular weight having an average molecular weight of 2,000 or more is preferable.
[0019]
Aliphatic polycarbodiimide compounds and hindered amine compounds are not used in the present invention because the effects obtained when used alone in a condensation type thermoplastic resin are low. That is, the hindered amine compound suppresses the self-condensation and oxidative deterioration of the aliphatic polycarbodiimide compound, so that the aliphatic polycarbodiimide compound can be effectively reacted with the carboxyl group of the condensation type thermoplastic resin. Further, the hindered amine compound prevents the aliphatic polycarbodiimide compound from agglomerating with metal oxides, inorganic fillers such as talc, pigments, etc., and suppresses the agglomeration of these aggregates on the surface of the molded article, thereby reducing the appearance of the molded article Has the effect of improving
[0020]
In addition, the condensation type thermoplastic resin composition of the present invention may have appropriate additives as necessary within a range not impairing the effects of the present invention, for example, a heat stabilizer, an oxidation stabilizer, a weather stabilizer, and a charge stabilizer. You may mix | blend an inhibitor, a dye, a pigment, a dispersing agent, a coupling agent, etc.
[0021]
The production of the thermoplastic condensation type resin composition of the present invention is not particularly limited. For example, a condensation type thermoplastic resin, an aliphatic polycarbodiimide compound, a hindered amine compound, and, if necessary, various additives and coloring agents are added, and the mixture is mixed with a Henschel mixer, a tumbler, a disper, or the like, and the mixture is kneader, roll mill, or super mixer. , Henschel mixer, Sugi mixer, Vertical granulator, High-speed mixer, Furmatrix, Ball mill, Steel mill, Sand mill, Vibration mill, Attritor, Batch kneader such as Banbury mixer, Twin screw extruder, Single screw extruder By mixing, melt-kneading and dispersing with a rotor-type twin-screw kneader or the like, a condensation-type thermoplastic resin composition having a shape such as pellets, powders, granules, or beads can be obtained.
[0022]
The condensation type thermoplastic resin composition of the present invention may be a master batch containing an aliphatic polycarbodiimide compound and a hindered amine compound at a relatively high concentration, and diluted with a resin to be molded (base resin) at the time of molding. However, the compound may have a relatively low concentration of the aliphatic polycarbodiimide compound and the hindered amine compound, and may be used for molding with the same composition without being diluted with the resin to be molded.
[0023]
The content of the aliphatic polycarbodiimide compound in the compound or the molded article is 0.01% by weight or more from the viewpoint of obtaining sufficient hydrolysis resistance and mechanical properties and the like, from the viewpoint of preventing coloring of the molded article and maintaining flexibility. It is preferably at most 10% by weight. Further, the content of the hindered amine-based compound is preferably 0.01% by weight or more from the viewpoint of exhibiting sufficient performance, and is preferably 10% by weight or less from the viewpoint of preventing coloring of a molded article and suppressing costs.
[0024]
If the content of the aliphatic polycarbodiimide compound in the masterbatch is too small, it is difficult to obtain sufficient hydrolysis resistance, and it becomes necessary to add a large amount of masterbatch. 1% by weight or more is preferable because it easily causes trouble. In addition, if the amount is too large, the production efficiency of the master batch itself deteriorates, or uniformity becomes difficult because it is added in a small amount to the resin to be molded, and the distribution and dispersibility are deteriorated, and there is a tendency for dust to be generated. In addition, the content is preferably 60% by weight or less from the viewpoint of suppressing stickiness derived from the aliphatic polycarbodiimide compound, mixing with the resin to be molded, and suppressing generation of aggregates due to self-condensation in the molded product. In particular, it is preferably 40% by weight or less, and most preferably 5 to 30% by weight.
[0025]
The content of the hindered amine compound in the masterbatch is preferably 1% by weight or more, particularly preferably 5% by weight, from the viewpoint of exhibiting sufficient performance without adding a large amount of the masterbatch. When a molded product is obtained by adding a large amount of master batch, there is a possibility that good mechanical properties are not obtained. Further, if the content is large, the amount of the masterbatch added to the resin to be added becomes small, and there is a possibility that the hindered amine compound is unevenly distributed, and it becomes difficult to achieve uniformity. Therefore, the content is preferably 90% by weight or less. In particular, it is preferably at most 60% by weight.
[0026]
The molded article of the present invention may be obtained by any one of extrusion molding, injection molding and blow molding methods, or may be a powder coating obtained by pulverizing a condensation type thermoplastic resin composition.
[0027]
【Example】
Hereinafter, the present invention will be described specifically with reference to Examples. In the following description, “part” represents “part by weight” and “%” represents “% by weight”.
[0028]
(1) Production of compound [Examples 1 to 10]
As shown in Table 1, the components (a), (a) and (c) were uniformly mixed and melt-kneaded with a twin screw extruder having a diameter of 30 mm at a screw rotation speed of 250 rpm to obtain a compound. The melt kneading was carried out at a set temperature of 280 ° C. when the component (c) was PET, and at a set temperature of 200 ° C. when the component was PLA.
[0029]
[Comparative Examples 1 to 12]
As shown in Table 2, the components (A), (A) and (C) were uniformly mixed, and a compound was obtained in the same manner as in Examples 1 to 10.
[0030]
(2) Production of master batch [Examples 11 to 20]
As shown in Table 1, the components (A), (A) and (C) were uniformly mixed and melt-kneaded with a twin screw extruder having a diameter of 30 mm at a screw rotation speed of 250 rpm to produce a master batch. The melt kneading was carried out at a set temperature of 280 ° C. when the component (c) was PET, and at a set temperature of 200 ° C. when the component was PLA.
[0031]
[Comparative Examples 13 to 24]
As shown in Table 2, the components (A), (A) and (C) were uniformly mixed, and a master batch was obtained in the same manner as in Examples 11 to 20. In Comparative Examples 21 to 24, smoke was generated from the die head of the twin-screw extruder during production of the master batch.
[0032]
[Table 1]
Figure 2004189860
[0033]
In Table 1, "aliphatic PC-1" represents dicyclohexylmethane-4,4-polycarbodiimide which is an aliphatic polycarbodiimide compound obtained from hydrogenated diphenylmethane diisocyanate;
"Aliphatic PC-2" is hexamethylene polycarbodiimide which is an aliphatic polycarbodiimide compound using hexamethylene diisocyanate as a raw material;
"Aliphatic PC-3" is an aliphatic polycarbodiimide compound derived from methylhexamethylene diisocyanate, 3-methylhexamethylene polycarbodiimide;
“HALS” refers to dimethylamine / 1,3,5-triazine / N, N-bis (2,2,6,6-tetramethyl-4-hydroxy-1,6-hexamethylenemethylenediamine / N- (2 A polycondensate of 2,6,6-tetramethyl-4- (benzyl) butylamine;
"PET" is polyethylene terephthalate (intrinsic viscosity = 0.83),
“PLA” used polylactic acid (intrinsic viscosity = 1.90).
[0034]
[Table 2]
Figure 2004189860
[0035]
In Table 2, those common to Table 1 are in accordance with the description of Table 1.
"Aromatic PC" is an aromatic polycarbodiimide (available from Line Chem Inc.) using toluene diisocyanate as a raw material,
“Aliphatic MC” used diisopropylcarbodiimide.
[0036]
[Evaluation test]
The compounds and masterbatches obtained in the above Examples and Comparative Examples were evaluated as follows, and the results are shown in Tables 3 and 4.
a. The compounds obtained in the hydrolysis evaluation examples 1 to 10 and the comparative examples 1 to 12 were used as they were in the following compositions a1.
The master batches obtained in Examples 11 to 20 and Comparative Examples 13 to 24 were each diluted 10-fold with a base resin (each using the same resin as the component (C)). Mixed. The mixture was supplied to a single-screw extruder having a screw diameter of 30 mm and an L / D value of 30, and pelletized under the condition of a rotation speed of 100 rpm to produce a compound. The melt kneading was carried out at a set temperature of 280 ° C. when the component (c) was PET, and at a set temperature of 200 ° C. when the component was PLA.
[0037]
a1. After drying the compound obtained at an intrinsic viscosity at 140 ° C. for 2 hours, 0.5 g of the compound was weighed in a 100 ml volumetric flask, and 100 ml of a phenol: 1,1,2,2-tetrachloroethane = 1: 1 solution was accurately added. This was stirred and dissolved at 150 ° C. for 1.5 hours to obtain a measurement sample. The intrinsic viscosity value was measured using a capillary viscosity automatic measuring device (Shibayama Science Co., Ltd. “SS-600-L2”). With the case of only the resin to be molded (PET or PLA as the component (c)) as 100%, the retention of the intrinsic viscosity value of each compound was determined and evaluated according to the following criteria.
:: Retention rate of intrinsic viscosity value of 96% or more Δ: Retention rate of intrinsic viscosity value of 90% or more and less than 96% X: Retention rate of intrinsic viscosity value of less than 90%
a2. Retained mechanical properties The compounds obtained in Examples 1 to 10 and Comparative Examples 1 to 12 were injection-molded at the back pressure of 10 kg / cm 2 with an injection molding machine using the same compositions to obtain plates. .
The master batches obtained in Examples 11 to 20 and Comparative Examples 13 to 24 were each diluted 10-fold with a base resin (each using the same resin as the component (C)). Mixed. The mixture was injection molded with an injection molding machine at a back pressure of 10 kg / cm 2 to obtain a plate.
[0039]
For each plate, a tensile strength test (JIS K7113) and an Izod impact test (JIS K7110) were performed. And evaluated according to the following criteria.
:: 96% or more Δ: 90% or more and less than 96% ×: 90% or less
b. The surface state of the injection-molded plate prepared in the evaluation of the mechanical property retention in the molded article surface state evaluation a2 was observed with an electron microscope and visually, and evaluated according to the following criteria.
:: The surface is smooth, and no gels or bumps are found.
Δ: The surface is smooth, but a few small dots can be confirmed.
×: The surface is uneven, and many gels and bumps can be confirmed.
[0041]
[Table 3]
Figure 2004189860
[0042]
[Table 4]
Figure 2004189860
[0043]
【The invention's effect】
Since the condensation type thermoplastic resin composition of the present invention contains an aliphatic polycarbodiimide compound and a hindered amine compound, it has practically sufficiently high hydrolysis resistance and heat resistance.
Therefore, the condensed thermoplastic resin molded product obtained by using the same has good mechanical properties and surface condition, and thus can be used more widely than before.

Claims (6)

脂肪族カルボジイミド化合物とヒンダードアミン系化合物を含有することを特徴とする縮合型熱可塑性樹脂組成物。A condensed thermoplastic resin composition comprising an aliphatic carbodiimide compound and a hindered amine compound. 脂肪族ポリカルボジイミド化合物の含有量が0.01〜60重量%、ヒンダードアミン系化合物の含有量が0.01〜60重量%である請求項1記載の縮合型熱可塑性樹脂組成物。The condensation type thermoplastic resin composition according to claim 1, wherein the content of the aliphatic polycarbodiimide compound is 0.01 to 60% by weight and the content of the hindered amine compound is 0.01 to 60% by weight. 縮合型熱可塑性樹脂がポリエステル樹脂である請求項1又は2に記載の縮合型熱可塑性樹脂組成物。3. The condensation type thermoplastic resin composition according to claim 1, wherein the condensation type thermoplastic resin is a polyester resin. 縮合型熱可塑性樹脂がポリ乳酸、ポリカプロラクトン、脂肪族ジカルボン酸と多価アルコールを主原料として得られる樹脂、微生物または植物より合成されたポリエステル樹脂である群から選択される少なくとも1種の微生物崩壊性樹脂である請求項1〜3いずれか記載の縮合型熱可塑性樹脂組成物。At least one microbial disintegration selected from the group consisting of polylactic acid, polycaprolactone, a resin obtained using aliphatic dicarboxylic acid and polyhydric alcohol as main raw materials, and a polyester resin synthesized from microorganisms or plants; The condensation type thermoplastic resin composition according to any one of claims 1 to 3, which is a conductive resin. 請求項1〜4いずれか記載の縮合型熱可塑性樹脂組成物から得られる成形品。A molded article obtained from the condensation type thermoplastic resin composition according to claim 1. 脂肪族カルボジイミド化合物とヒンダードアミン系化合物を含有することを特徴とする縮合型熱可塑性樹脂の成形品の劣化防止方法。A method for preventing deterioration of a condensed thermoplastic resin molded article, comprising an aliphatic carbodiimide compound and a hindered amine compound.
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006152025A (en) * 2004-11-25 2006-06-15 Mitsubishi Chemicals Corp Aliphatic or alicyclic polyester resin composition
JP2006161024A (en) * 2004-11-15 2006-06-22 Umg Abs Ltd Polylactic acid-based thermoplastic resin composition and its molded article
JP2006273926A (en) * 2005-03-28 2006-10-12 Mitsubishi Chemicals Corp Process for producing aliphatic polyester resin composition
WO2007091427A1 (en) * 2006-02-07 2007-08-16 Nec Corporation Polylactic acid-modified polycarbodiimide compound, polylactic acid resin composition containing same and molded article
JP2009184139A (en) * 2008-02-04 2009-08-20 Mazda Motor Corp Manufacturing method of resin molded product
JP2011174094A (en) * 2011-06-14 2011-09-08 Mitsubishi Chemicals Corp Aliphatic or alicyclic polyester-based resin composition
JP2012036405A (en) * 2004-11-15 2012-02-23 Umg Abs Ltd Polylactic acid-based thermoplastic resin composition and its molded article
WO2017057703A1 (en) * 2015-10-01 2017-04-06 日清紡ケミカル株式会社 Resin additive, and master batch and resin composition using same
CN109069700A (en) * 2016-04-28 2018-12-21 美敦力公司 Hydrolytically stable polymer compositions, articles and methods
CN120776478A (en) * 2025-09-10 2025-10-14 东华大学 Preparation method of thermoplastic functional polyester fiber

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03153601A (en) * 1989-11-09 1991-07-01 Mitsubishi Petrochem Co Ltd Anti-mite thermoplastic resin composition
JPH07133415A (en) * 1993-11-11 1995-05-23 Mitsui Petrochem Ind Ltd palette
JPH07133357A (en) * 1993-11-11 1995-05-23 Kirin Brewery Co Ltd Container made of saturated polyester resin composition
JPH07133408A (en) * 1993-11-11 1995-05-23 Mitsui Petrochem Ind Ltd Interior and exterior materials for automobiles
JPH1180522A (en) * 1997-07-09 1999-03-26 Nisshinbo Ind Inc Biodegradable plastic composition and control of biodegradation rate of biodegradable plastic
JP2000143950A (en) * 1998-09-09 2000-05-26 Toyobo Co Ltd Polyester elastomer composition
JP2001342331A (en) * 2000-06-01 2001-12-14 Mitsubishi Chemicals Corp Polyester-based elastomer composition
JP2002030208A (en) * 2000-07-14 2002-01-31 Toray Ind Inc Polylactic acid resin composition and molded article
JP2002205367A (en) * 2001-01-09 2002-07-23 Gunze Ltd Biodegradable card base excellent in resistance to bending

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03153601A (en) * 1989-11-09 1991-07-01 Mitsubishi Petrochem Co Ltd Anti-mite thermoplastic resin composition
JPH07133415A (en) * 1993-11-11 1995-05-23 Mitsui Petrochem Ind Ltd palette
JPH07133357A (en) * 1993-11-11 1995-05-23 Kirin Brewery Co Ltd Container made of saturated polyester resin composition
JPH07133408A (en) * 1993-11-11 1995-05-23 Mitsui Petrochem Ind Ltd Interior and exterior materials for automobiles
JPH1180522A (en) * 1997-07-09 1999-03-26 Nisshinbo Ind Inc Biodegradable plastic composition and control of biodegradation rate of biodegradable plastic
JP2000143950A (en) * 1998-09-09 2000-05-26 Toyobo Co Ltd Polyester elastomer composition
JP2001342331A (en) * 2000-06-01 2001-12-14 Mitsubishi Chemicals Corp Polyester-based elastomer composition
JP2002030208A (en) * 2000-07-14 2002-01-31 Toray Ind Inc Polylactic acid resin composition and molded article
JP2002205367A (en) * 2001-01-09 2002-07-23 Gunze Ltd Biodegradable card base excellent in resistance to bending

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006161024A (en) * 2004-11-15 2006-06-22 Umg Abs Ltd Polylactic acid-based thermoplastic resin composition and its molded article
JP2012036405A (en) * 2004-11-15 2012-02-23 Umg Abs Ltd Polylactic acid-based thermoplastic resin composition and its molded article
JP2006152025A (en) * 2004-11-25 2006-06-15 Mitsubishi Chemicals Corp Aliphatic or alicyclic polyester resin composition
JP2006273926A (en) * 2005-03-28 2006-10-12 Mitsubishi Chemicals Corp Process for producing aliphatic polyester resin composition
WO2007091427A1 (en) * 2006-02-07 2007-08-16 Nec Corporation Polylactic acid-modified polycarbodiimide compound, polylactic acid resin composition containing same and molded article
JP2009184139A (en) * 2008-02-04 2009-08-20 Mazda Motor Corp Manufacturing method of resin molded product
JP2011174094A (en) * 2011-06-14 2011-09-08 Mitsubishi Chemicals Corp Aliphatic or alicyclic polyester-based resin composition
WO2017057703A1 (en) * 2015-10-01 2017-04-06 日清紡ケミカル株式会社 Resin additive, and master batch and resin composition using same
CN109069700A (en) * 2016-04-28 2018-12-21 美敦力公司 Hydrolytically stable polymer compositions, articles and methods
CN109069700B (en) * 2016-04-28 2022-03-08 美敦力公司 Hydrolytically stabilized polymer compositions, articles and methods
CN120776478A (en) * 2025-09-10 2025-10-14 东华大学 Preparation method of thermoplastic functional polyester fiber

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