JPH0251926B2 - - Google Patents
Info
- Publication number
- JPH0251926B2 JPH0251926B2 JP56038374A JP3837481A JPH0251926B2 JP H0251926 B2 JPH0251926 B2 JP H0251926B2 JP 56038374 A JP56038374 A JP 56038374A JP 3837481 A JP3837481 A JP 3837481A JP H0251926 B2 JPH0251926 B2 JP H0251926B2
- Authority
- JP
- Japan
- Prior art keywords
- polybutadiene
- polymer
- hydrogenated
- copolymer
- hexamethylene diamine
- 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 - Lifetime
Links
- 239000005062 Polybutadiene Substances 0.000 claims description 29
- 229920002857 polybutadiene Polymers 0.000 claims description 29
- 229920000642 polymer Polymers 0.000 claims description 24
- 125000002843 carboxylic acid group Chemical group 0.000 claims description 8
- 125000003277 amino group Chemical group 0.000 claims description 7
- 229920006122 polyamide resin Polymers 0.000 claims description 7
- 239000004952 Polyamide Substances 0.000 claims description 6
- 229920002647 polyamide Polymers 0.000 claims description 6
- 125000004956 cyclohexylene group Chemical group 0.000 claims 2
- 125000000843 phenylene group Chemical group C1(=C(C=CC=C1)*)* 0.000 claims 2
- 125000006838 isophorone group Chemical group 0.000 claims 1
- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 description 23
- 229920001577 copolymer Polymers 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- PBLZLIFKVPJDCO-UHFFFAOYSA-N 12-aminododecanoic acid Chemical compound NCCCCCCCCCCCC(O)=O PBLZLIFKVPJDCO-UHFFFAOYSA-N 0.000 description 12
- 238000010521 absorption reaction Methods 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 238000002844 melting Methods 0.000 description 9
- 230000008018 melting Effects 0.000 description 9
- -1 diamine salts Chemical class 0.000 description 6
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 6
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 5
- 229920001519 homopolymer Polymers 0.000 description 5
- RLSSMJSEOOYNOY-UHFFFAOYSA-N m-cresol Chemical compound CC1=CC=CC(O)=C1 RLSSMJSEOOYNOY-UHFFFAOYSA-N 0.000 description 5
- 229940100630 metacresol Drugs 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 229920000299 Nylon 12 Polymers 0.000 description 4
- TVIDDXQYHWJXFK-UHFFFAOYSA-N dodecanedioic acid Chemical compound OC(=O)CCCCCCCCCCC(O)=O TVIDDXQYHWJXFK-UHFFFAOYSA-N 0.000 description 4
- 238000005984 hydrogenation reaction Methods 0.000 description 4
- 238000006116 polymerization reaction Methods 0.000 description 4
- 229920002292 Nylon 6 Polymers 0.000 description 3
- 229920000572 Nylon 6/12 Polymers 0.000 description 3
- 150000004985 diamines Chemical class 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- RNLHGQLZWXBQNY-UHFFFAOYSA-N 3-(aminomethyl)-3,5,5-trimethylcyclohexan-1-amine Chemical compound CC1(C)CC(N)CC(C)(CN)C1 RNLHGQLZWXBQNY-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
- 239000002253 acid Substances 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 2
- YMHQVDAATAEZLO-UHFFFAOYSA-N cyclohexane-1,1-diamine Chemical compound NC1(N)CCCCC1 YMHQVDAATAEZLO-UHFFFAOYSA-N 0.000 description 2
- 238000000921 elemental analysis Methods 0.000 description 2
- 229920005570 flexible polymer Polymers 0.000 description 2
- 125000004836 hexamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 2
- 239000012456 homogeneous solution Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N vinyl-ethylene Natural products C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- GEYOCULIXLDCMW-UHFFFAOYSA-N 1,2-phenylenediamine Chemical compound NC1=CC=CC=C1N GEYOCULIXLDCMW-UHFFFAOYSA-N 0.000 description 1
- GUOSQNAUYHMCRU-UHFFFAOYSA-N 11-Aminoundecanoic acid Chemical compound NCCCCCCCCCCC(O)=O GUOSQNAUYHMCRU-UHFFFAOYSA-N 0.000 description 1
- SLXKOJJOQWFEFD-UHFFFAOYSA-N 6-aminohexanoic acid Chemical compound NCCCCCC(O)=O SLXKOJJOQWFEFD-UHFFFAOYSA-N 0.000 description 1
- 239000004609 Impact Modifier Substances 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 125000005263 alkylenediamine group Chemical group 0.000 description 1
- 238000005576 amination reaction Methods 0.000 description 1
- 229960002684 aminocaproic acid Drugs 0.000 description 1
- 150000004984 aromatic diamines Chemical class 0.000 description 1
- 230000021523 carboxylation Effects 0.000 description 1
- 238000006473 carboxylation reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- QYQADNCHXSEGJT-UHFFFAOYSA-N cyclohexane-1,1-dicarboxylate;hydron Chemical compound OC(=O)C1(C(O)=O)CCCCC1 QYQADNCHXSEGJT-UHFFFAOYSA-N 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- QFTYSVGGYOXFRQ-UHFFFAOYSA-N dodecane-1,12-diamine Chemical compound NCCCCCCCCCCCCN QFTYSVGGYOXFRQ-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 150000004986 phenylenediamines Chemical class 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- DJZKNOVUNYPPEE-UHFFFAOYSA-N tetradecane-1,4,11,14-tetracarboxamide Chemical compound NC(=O)CCCC(C(N)=O)CCCCCCC(C(N)=O)CCCC(N)=O DJZKNOVUNYPPEE-UHFFFAOYSA-N 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Polyamides (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
Description
本発明は新規な共重合ポリアミド樹脂に関す
る。
ポリアミド樹脂は繊維はじめ広範な用途に用い
られているが、主に成形品として用いられる場合
の大きな欠点として水分によつて寸法、物性が大
きく変わることがあげられる。
本発明者は、水分の影響の少い、即ち吸水率の
低いポリアミド樹脂を得るべく鋭意探索研究した
結果、既に両末端がカルボン酸基又はアミノ基で
あるポリブタジエン又はブタジエン共重合体が、
一般に用いられているポリアミド樹脂モノマーと
共重合することを見出し、更にその共重合体の吸
水率が低いことを見出した(特願昭55−123135)。
しかしながら、この共重合ポリアミドは比較的
熱によつて変質し易く、このため2つの欠点を有
する。1つは、重合時、変質を避けるため温度を
下げる等特別の配慮を要することと、更に1つ
は、高温雰囲気での使用により短期間に脆化する
ことである。
本発明の目的は、水分の影響が少く、かつ熱安
定の改良された新規共重合ポリアミドを提供する
ことにある。
本発明者は、ポリブタジエン又はブタジエン共
重合体との共重合ポリアミドの熱安定性の劣る原
因が、その二重結合にあると考え、鋭意検討を重
ねた結果、両末端がカルボン酸基又はアミノ基で
ある二重結合に水素添加されたポリブタジエンが
一般に用いられているポリアミド樹脂モノマーと
共重合することを見出し、更にその共重合体の吸
水率が低く、熱安定性が良好であることを見出し
て本発明に到つたものである。即ち、本発明は下
記一般式(1)又は(2)で表わされる繰返し単位を一種
以上有するポリアミド高分子成分99〜5重量部と
両末端がカルボン酸基又はアミノ基である平均分
子量500〜10000の二重結合に水素添加されたポリ
ブタジエン成分1〜95重量部を共重合してなる吸
水率が低く、熱安定性の良好な新規共重合ポリア
ミド樹脂を提供するものである。
−NH(CH2)oCO− (1)
(式中、nは5〜11の整数)
−NHXNHCOYCO− (2)
(式中、XはCnH2n(mは6〜12の整数)、イソホ
ロン基、フエニレン基又はシクロヘキシレン基を
表わし、YはClH2l(lは4〜10の整数)、フエニ
レン基又はシクロヘキシレン基を表わす)
本発明の共重合ポリアミドは低吸水率であり、
水分による寸法、物性の変化が少く、かつ熱安定
性が良好であるため、射出・押出等による成形品
に好適に用いられる。又、この共重合体は吸水率
の低い熱接着剤としても用いられ得る。更に、こ
の共重合体中、二重結合に水素添加されたポリブ
タジエンの量が30重量%以上のものは柔軟であ
り、かつ耐衝撃性に優れるため、柔軟性を要求さ
れる用途または衝撃改良剤として有利に用いられ
得る。
本発明の共重合ポリアミドのポリアミド高分子
成分を構成する単量体としては、たとえば、カプ
ロラクタム、ラウリルラクタム、11アミノウンデ
カン酸、12アミノドデカン酸、ヘキサメチレンア
ジパミド、ヘキサメチレンセパシミド、ヘキサメ
チレンドデカミド等の外、テレフタル酸、シクロ
ヘキサンジカルボン酸等の環を有する二塩基酸の
ジアミン塩、フエニレンジアミン、シクロヘキサ
ンジアミン、イソホロンジアミン等のジアミンの
二塩基酸塩等があげられる。
両末端がカルボン酸基又はアミノ基である二重
結合に水素添加されたポリブタジエンは、両末端
がカルボン酸基又はアミノ基であるポリブタジエ
ンを水添して製造される。水添されるポリブタジ
エンは1,2結合、1,4トランス結合、1,4
シス結合等いかなる結合を含んでいてもよいが、
水素添加の容易さからは1,2結合の割合の多い
ことが望ましい。水素添加を完全に行うことは技
術的に困難であり、従つて水素添加率70%以上の
ポリブタジエンが好適に用いられ、水素添加率90
%以上のポリブタジエンが更に好適に用いられ
る。ポリブタジエンの両末端を100%カルボン酸
化又はアミノ化することは技術的に困難であり、
従つて水添されたポリブタジエンの末端も100%
カルボン酸基又はアミノ基とはなり難い。カルボ
ン酸末端率又はアミノ末端率60%以上の水添され
たポリブタジエンが好適に用いられ、同末端率75
%以上の水添されたポリブタジエンが更に好適に
用いられる。水添されたポリブタジエンの分子量
が500未満であると吸水性を低下させる効果が少
く、10000より大きいと物性的に望ましいものが
得難い。
本発明の共重合ポリアミド樹脂においてポリア
ミド高分子成分が99重量部を越えると各性質が水
添されたポリブタジエンを含まないポリアミドと
ほヾ同じとなり、又水添されたポリブタジエン成
分が95重量部を越えると、水添されたポリブタジ
エンとほゞ同等の性質となるため、何れも好まし
くない。
本発明の共重合ポリアミド樹脂を得るための共
重合方法は縮重合、又は開環重合のいずれでも良
い。
なお、共重合体の分子量を調整するために水添
されたポリブタジエンのモル数を考慮して、ジア
ミン又はジカルボン酸を添加することができる。
ジアミンとしては、たとえばヘキサメチレンジ
アミン、ドデカメチレンジアミンのようなアルキ
レンジアミン、たとえばシクロヘキサンジアミン
のような脂環族ジアミン、たとえばフエニレンジ
アミンのような芳香族ジアミン、あるいはイソホ
ロンジアミン等が用いられ得る。
ジカルボン酸としてはアジピン酸、セバシン
酸、ドデカン二酸のような脂肪族ジカルボン酸、
脂環族カルボン酸、フタル酸のような芳香族ジカ
ルボン酸が用いられ得る。
次に本発明を実施例について説明する。
実施例 1
12アミノドデカン酸76.40g、ヘキサメチレンジ
アミン1.57g、両末端カルボン酸水素添加ポリブ
タジエン(1,2ビニル結合80%以上のポリブタ
ジエンを98%水添、末端カルボン酸基濃度
0.935meg/g)28.92gを500ml三角フラスコに入
れ、三角フラスコ中に窒素を流しながらこれを
250℃に加熱した。12アミノドデカン酸の溶融と
共に縮合が始まり、水分が泡となつて出てくる。
250℃で3時間加熱した後冷却して三角フラスコ
を割り、重合物を取り出した。淡黄色半透明で衝
撃に強い重合体が得られた。この重合体はナイロ
ン12成分/水添ポリブタジエン−ヘキサメチレン
ジアミン縮合体成分の比率が70/30に相当する。
この重合体をメタクレゾールに溶解して0.5%
溶液とし、オストワルド粘度計により25℃に於け
る相対粘度を測定すると1.43であつた。この重合
体をプレス成形により平板として40℃水中に10日
間浸漬後、デユポン式水分計により吸水率を測定
すると1.21%であつた。
また、DSC(Differential Scanning Calori−
metar)によつて測定した融点は172℃であつた。
なお、ナイロン12ホモポリマーを同様の方法に
より測定すると、吸水率1.6%、融点178℃であつ
た。
実施例 2
12アミノドデカン酸49.11g、ヘキサメチレンジ
アミン0.26g、実施例1で用いた水添ポリブタジ
エン4.82gを300ml三角フラスコに仕込み、実施例
1と同様にして重合を行い、冷却後重合物を取り
出した。淡黄色半透明で硬くて耐衝撃性のある重
合体が得られた。この重合体はナイロン12成分/
水添ポリブタジエン−ヘキサメチレンジアミン縮
合体成分の比率が90/10に相当する。
この重合体を実施例1と同様にして測定した結
果、相対粘度1.70、吸水率1.49%、融点176℃で
あつた。
実施例 3
12アミノドデカン酸54.57g、ヘキサメチレンジ
アミン2.61g、実施例1で用いた水添ポリブタジ
エン48.20gを500ml、セパラブルフラスコに仕込
み窒素を流し、撹拌しながら220℃で2時間加熱
した。淡黄色でほとんど透明の柔軟な重合体が得
られた。この重合体はナイロン12成分/水添ポリ
ブタジエン−ヘキサメチレンジアミン縮合体成分
の比率が50/50に相当する。
この重合体を実施例1と同様にして測定した結
果、相対粘度1.30、吸水率1.07、融点167℃であ
つた。
実施例 4
12アミノドデカン酸32.74g、ヘキサメチレンジ
アミン3.66g、実施例1で用いた水添ポリブタジ
エン67.48gを500mlセパラブルフラスコに仕込み、
実施例3と同様に重合を行つた。淡黄色で極めて
柔軟な重合体が得られた。
この重合体はナイロン12成分/水添ポリブタジ
エン−ヘキサメチレンジアミン縮合体成分の比率
が30/70に相当する。
この重合体を実施例1と同様にして測定した結
果、相対粘度1.18、吸水率0.95、融点155℃であ
つた。
実施例 5
εカプロラクタム81g、εアミノカプロン酸
10.43g、ヘキサメチレンジアミン0.52g、実施例
1で用いた水添ポリブタジエン9.64gを500mlフラ
スコに仕込み、窒素を流し、撹拌し乍ら、180℃
で30分加熱し、1時間かけて250℃に昇温し、250
℃で4時間加熱を続けた。淡黄色半透明の重合体
が得られた。
この重合体を液体窒素中で粉砕後、60℃温水で
24時間抽出すると、抽出減量は約5%であつた。
抽出物はほとんどカプロラクタムと推定されるた
め、この重合体は、ナイロン6成分/水添ポリブ
タジエン−ヘキサメチレンジアミン縮合体成分の
比率がほぼ85/10に相当する共重合体である。
抽出後の共重合体は、プレス成形により強靭な
シートに成形できた。
この共重合体をメタクレゾールに溶解すると、
均一な溶液が得られた。0.5%メタクレゾール溶
液の25℃に於ける相対粘度は1.62であつた。こ共
重合体のDSCによつて測定した融点は214℃であ
つた。一方、水添ポリブタジエンとヘキサメチレ
ンジアミンを除いて、本実施例と同様に重合し、
水抽出した重合体ナイロン6ホモポリマーの融点
は216℃であつた。
共重合体およびナイロン6ホモポリマーの元素
分析を行うと表−1のような結果となつた。
The present invention relates to a novel copolyamide resin. Polyamide resins are used in a wide range of applications including fibers, but a major drawback when used primarily as molded products is that their dimensions and physical properties change greatly depending on moisture. As a result of intensive exploration and research in order to obtain a polyamide resin that is less affected by moisture, that is, has a lower water absorption rate, the present inventor has found that polybutadiene or butadiene copolymer having carboxylic acid groups or amino groups at both ends has already been found.
It was discovered that the copolymer copolymerized with commonly used polyamide resin monomers, and furthermore, the copolymer was found to have a low water absorption rate (Japanese Patent Application No. 123135/1982). However, this copolyamide is relatively easily altered by heat, and therefore has two drawbacks. One is that special considerations such as lowering the temperature are required to avoid deterioration during polymerization, and the other is that it becomes brittle in a short period of time when used in a high temperature atmosphere. An object of the present invention is to provide a new copolyamide that is less affected by moisture and has improved thermal stability. The inventor of the present invention believes that the cause of poor thermal stability of polyamide copolymerized with polybutadiene or butadiene copolymer is the double bond, and as a result of extensive studies, it has been found that both terminals have a carboxylic acid group or an amino group. They discovered that polybutadiene with hydrogenated double bonds copolymerized with commonly used polyamide resin monomers, and further discovered that the copolymer had low water absorption and good thermal stability. This has led to the present invention. That is, the present invention uses 99 to 5 parts by weight of a polyamide polymer component having one or more types of repeating units represented by the following general formula (1) or (2) and an average molecular weight of 500 to 10,000, which has carboxylic acid groups or amino groups at both ends. The object of the present invention is to provide a new copolymerized polyamide resin having a low water absorption rate and good thermal stability, which is obtained by copolymerizing 1 to 95 parts by weight of a polybutadiene component whose double bonds are hydrogenated. -NH( CH2 ) o CO- (1) (In the formula, n is an integer from 5 to 11) -NHXNHCOYCO- (2) (In the formula, X is C n H 2n (m is an integer from 6 to 12), The copolyamide of the present invention has a low water absorption rate,
It is suitable for use in molded products made by injection, extrusion, etc. because it has little change in dimensions and physical properties due to moisture and has good thermal stability. This copolymer can also be used as a thermal adhesive with low water absorption. Furthermore, copolymers containing 30% by weight or more of polybutadiene with hydrogenated double bonds are flexible and have excellent impact resistance, so they can be used in applications that require flexibility or as impact modifiers. It can be advantageously used as Examples of monomers constituting the polyamide polymer component of the copolyamide of the present invention include caprolactam, lauryllactam, 11-aminoundecanoic acid, 12-aminododecanoic acid, hexamethylene adipamide, hexamethylene sepacimide, hexamethylene In addition to methylenedodecamide, diamine salts of ring-containing dibasic acids such as terephthalic acid and cyclohexanedicarboxylic acid, dibasic acid salts of diamines such as phenylenediamine, cyclohexanediamine, and isophoronediamine, and the like. Polybutadiene in which a double bond having a carboxylic acid group or an amino group at both ends is hydrogenated is produced by hydrogenating polybutadiene having a carboxylic acid group or an amino group at both ends. Polybutadiene to be hydrogenated includes 1,2 bonds, 1,4 trans bonds, 1,4
It may contain any bond such as a cis bond, but
From the viewpoint of ease of hydrogenation, it is desirable to have a high proportion of 1,2 bonds. It is technically difficult to perform complete hydrogenation, so polybutadiene with a hydrogenation rate of 70% or more is preferably used;
% or more of polybutadiene is more preferably used. It is technically difficult to carry out 100% carboxylation or amination of both ends of polybutadiene.
Therefore, the ends of hydrogenated polybutadiene are also 100%
It is unlikely to become a carboxylic acid group or an amino group. Hydrogenated polybutadiene with a carboxylic acid terminal ratio or amino terminal ratio of 60% or more is preferably used, and the same terminal ratio is 75%.
% or more of hydrogenated polybutadiene is more preferably used. If the molecular weight of the hydrogenated polybutadiene is less than 500, the effect of reducing water absorption will be small, and if it is greater than 10,000, it will be difficult to obtain desirable physical properties. In the copolymerized polyamide resin of the present invention, when the polyamide polymer component exceeds 99 parts by weight, each property becomes almost the same as that of hydrogenated polyamide not containing polybutadiene, and when the hydrogenated polybutadiene component exceeds 95 parts by weight. Both are unfavorable because the properties are almost the same as those of hydrogenated polybutadiene. The copolymerization method for obtaining the copolyamide resin of the present invention may be either condensation polymerization or ring-opening polymerization. In addition, in order to adjust the molecular weight of the copolymer, a diamine or a dicarboxylic acid can be added in consideration of the number of moles of hydrogenated polybutadiene. Examples of diamines that can be used include alkylene diamines such as hexamethylene diamine and dodecamethylene diamine, alicyclic diamines such as cyclohexane diamine, aromatic diamines such as phenylene diamine, and isophorone diamine. Dicarboxylic acids include aliphatic dicarboxylic acids such as adipic acid, sebacic acid, and dodecanedioic acid;
Alicyclic carboxylic acids, aromatic dicarboxylic acids such as phthalic acid may be used. Next, the present invention will be explained with reference to examples. Example 1 76.40 g of 12-aminododecanoic acid, 1.57 g of hexamethylene diamine, polybutadiene with hydrogenated carboxylic acid at both ends (98% hydrogenation of polybutadiene with 80% or more of 1,2 vinyl bonds, terminal carboxylic acid group concentration)
0.935meg/g) 28.92g was placed in a 500ml Erlenmeyer flask, and the flask was flushed with nitrogen.
Heated to 250°C. As 12-aminododecanoic acid melts, condensation begins and water comes out in the form of bubbles.
After heating at 250°C for 3 hours, the mixture was cooled, the Erlenmeyer flask was broken, and the polymer was taken out. A light yellow, translucent, impact-resistant polymer was obtained. This polymer has a ratio of nylon 12 component/hydrogenated polybutadiene-hexamethylene diamine condensate component of 70/30. This polymer was dissolved in metacresol and 0.5%
The relative viscosity of the solution was measured at 25°C using an Ostwald viscometer and found to be 1.43. This polymer was pressed into a flat plate and immersed in water at 40°C for 10 days.The water absorption was measured using a DuPont moisture meter and found to be 1.21%. Additionally, DSC (Differential Scanning Calori−
The melting point was 172°C as determined by METAR). When nylon 12 homopolymer was measured in the same manner, it had a water absorption rate of 1.6% and a melting point of 178°C. Example 2 49.11 g of 12-aminododecanoic acid, 0.26 g of hexamethylene diamine, and 4.82 g of the hydrogenated polybutadiene used in Example 1 were placed in a 300 ml Erlenmeyer flask, and polymerization was carried out in the same manner as in Example 1. After cooling, the polymerized product was I took it out. A light yellow, translucent, hard and impact resistant polymer was obtained. This polymer consists of 12 nylon components/
The ratio of hydrogenated polybutadiene-hexamethylene diamine condensate components corresponds to 90/10. This polymer was measured in the same manner as in Example 1 and found to have a relative viscosity of 1.70, a water absorption rate of 1.49%, and a melting point of 176°C. Example 3 54.57 g of 12-aminododecanoic acid, 2.61 g of hexamethylene diamine, and 48.20 g of the hydrogenated polybutadiene used in Example 1 were charged into a separable flask (500 ml), nitrogen was flushed, and the flask was heated at 220° C. for 2 hours with stirring. A pale yellow, almost transparent, flexible polymer was obtained. This polymer has a ratio of nylon 12 component/hydrogenated polybutadiene-hexamethylene diamine condensate component of 50/50. This polymer was measured in the same manner as in Example 1 and found to have a relative viscosity of 1.30, a water absorption rate of 1.07, and a melting point of 167°C. Example 4 32.74 g of 12-aminododecanoic acid, 3.66 g of hexamethylene diamine, and 67.48 g of the hydrogenated polybutadiene used in Example 1 were charged into a 500 ml separable flask.
Polymerization was carried out in the same manner as in Example 3. A pale yellow and extremely flexible polymer was obtained. This polymer has a ratio of nylon 12 component/hydrogenated polybutadiene-hexamethylene diamine condensate component of 30/70. This polymer was measured in the same manner as in Example 1 and found to have a relative viscosity of 1.18, a water absorption rate of 0.95, and a melting point of 155°C. Example 5 ε-caprolactam 81g, ε-aminocaproic acid
10.43g of hexamethylene diamine, 0.52g of hexamethylene diamine, and 9.64g of the hydrogenated polybutadiene used in Example 1 were placed in a 500ml flask, and heated to 180°C under nitrogen flow and stirring.
Heat for 30 minutes, raise the temperature to 250℃ over 1 hour,
Heating was continued for 4 hours at °C. A pale yellow, translucent polymer was obtained. After crushing this polymer in liquid nitrogen, it was washed with 60℃ hot water.
When extracted for 24 hours, the extraction loss was about 5%.
Since the extract is estimated to be mostly caprolactam, this polymer is a copolymer with a ratio of nylon 6 component/hydrogenated polybutadiene-hexamethylene diamine condensate component of approximately 85/10. The extracted copolymer could be molded into a strong sheet by press molding. When this copolymer is dissolved in metacresol,
A homogeneous solution was obtained. The relative viscosity of the 0.5% metacresol solution at 25°C was 1.62. The melting point of this copolymer measured by DSC was 214°C. On the other hand, polymerization was carried out in the same manner as in this example except for hydrogenated polybutadiene and hexamethylene diamine,
The water-extracted polymer nylon 6 homopolymer had a melting point of 216°C. Elemental analysis of the copolymer and nylon 6 homopolymer yielded the results shown in Table 1.
【表】
実施例 6
ドデカン二酸/ヘキサメチレンジアミン塩
89.29g、ヘキサメチレンジアミン1.03g、実施例
1で用いた水添ポリブタジエン19.29gを500mlフ
ラスコに仕込み、窒素を流し、撹拌し乍ら、200
℃で30分加熱、内容物を溶融させ、30分かけて
徐々に240℃に昇温した。240℃で2時間加熱した
後、260℃で更に2時間加熱し、淡黄色半透明の
重合体が得られた。
この重合体はナイロン612成分/水添ポリブタ
ジエン−ヘキサメチレンジアミン縮合体成分の比
率が80/20に相当する共重合体である。
この重合体はプレス成形により強靭なシートに
成形できた。
この共重合体をメタクレゾールに溶解すると、
均一な溶液が得られた。0.5%メタクレゾール溶
液の25℃に於ける相対粘度は1.63であつた。この
共重合体のDSCによつて測定した融点は212℃で
あつた。一方、水添ポリブタジエンとヘキサメチ
レンジアミンを除いて、本実施例と同様に重合し
た重合体ナイロン612ホモポリマーの融点は217℃
であつた。
共重合体およびナイロン612ホモポリマーの元
素分析を行うと表−2のような結果となつた。[Table] Example 6 Dodecanedioic acid/hexamethylene diamine salt
89.29 g, hexamethylene diamine 1.03 g, and 19.29 g of the hydrogenated polybutadiene used in Example 1 were charged into a 500 ml flask, and while nitrogen was flushed and stirred, 200 g of hexamethylene diamine was added.
It was heated at ℃ for 30 minutes to melt the contents, and the temperature was gradually raised to 240℃ over 30 minutes. After heating at 240°C for 2 hours, the mixture was further heated at 260°C for 2 hours to obtain a pale yellow translucent polymer. This polymer is a copolymer having a ratio of nylon 612 component/hydrogenated polybutadiene-hexamethylene diamine condensate component of 80/20. This polymer could be formed into a strong sheet by press molding. When this copolymer is dissolved in metacresol,
A homogeneous solution was obtained. The relative viscosity of the 0.5% metacresol solution at 25°C was 1.63. The melting point of this copolymer measured by DSC was 212°C. On the other hand, the melting point of the polymer nylon 612 homopolymer polymerized in the same manner as in this example except for hydrogenated polybutadiene and hexamethylene diamine was 217°C.
It was hot. Elemental analysis of the copolymer and nylon 612 homopolymer yielded the results shown in Table 2.
Claims (1)
位を一種以上有するポリアミド高分子成分99〜5
重量部と両末端がカルボン酸基、又はアミノ基で
ある平均分子量500〜10000の二重結合に70%以上
水素添加されたポリブタジエン成分1〜95重量部
を共重合してなる新規共重合ポリアミド樹脂。 −NH(CH2)oCO− (1) (式中、nは5〜11の整数) −NHXNHCOYCO− (2) (式中、XはCnH2n(mは6〜12の整数)、イソホ
ロン基、フエニレン基又はシクロヘキシレン基を
表わし、YはClH2l(lは4〜10の整数)、フエニ
レン基又はシクロヘキシレン基を表わす)[Claims] 1 Polyamide polymer component 99-5 having one or more repeating units represented by the following general formula (1) or (2)
A new copolymerized polyamide resin obtained by copolymerizing 1 to 95 parts by weight of a polybutadiene component hydrogenated by 70% or more to a double bond having an average molecular weight of 500 to 10,000 and having carboxylic acid groups or amino groups at both ends. . -NH( CH2 ) o CO- (1) (In the formula, n is an integer from 5 to 11) -NHXNHCOYCO- (2) (In the formula, X is C n H 2n (m is an integer from 6 to 12), represents an isophorone group, a phenylene group or a cyclohexylene group, Y represents C l H 2l (l is an integer from 4 to 10), a phenylene group or a cyclohexylene group)
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3837481A JPS57151622A (en) | 1981-03-16 | 1981-03-16 | Interpolyamide resin |
EP82900827A EP0073838B2 (en) | 1981-03-16 | 1982-03-16 | Copolymerized polyamide resin |
US06/651,633 US4555566A (en) | 1981-03-16 | 1982-03-16 | Copolymer polyamide resin containing polyolefin moiety |
PCT/JP1982/000068 WO1982003219A1 (en) | 1981-03-16 | 1982-03-16 | Copolymerized polyamide resin |
DE8282900827T DE3278735D1 (en) | 1981-03-16 | 1982-03-16 | Copolymerized polyamide resin |
US06/888,095 US5025070A (en) | 1981-03-16 | 1986-07-17 | Copolymer polyamide resin from hydrogenated polyolefin condensate |
US07/475,184 US5093421A (en) | 1981-03-16 | 1990-02-02 | Copolymer polyamide resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3837481A JPS57151622A (en) | 1981-03-16 | 1981-03-16 | Interpolyamide resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57151622A JPS57151622A (en) | 1982-09-18 |
JPH0251926B2 true JPH0251926B2 (en) | 1990-11-09 |
Family
ID=12523502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3837481A Granted JPS57151622A (en) | 1981-03-16 | 1981-03-16 | Interpolyamide resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS57151622A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59202220A (en) * | 1983-05-02 | 1984-11-16 | Mitsui Petrochem Ind Ltd | Production of copolyamide |
AU3682500A (en) * | 2000-04-06 | 2001-10-23 | Jang Hon Lee | Power control apparatus and the method |
FR3049281B1 (en) * | 2016-03-24 | 2019-11-01 | Arkema France | BLOCK COPOLYMER FOR THE PROTECTION OF METAL-BASED PARTS |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5580435A (en) * | 1978-10-30 | 1980-06-17 | Monsanto Co | Molding resin composition |
JPS57149329A (en) * | 1981-02-13 | 1982-09-14 | Bayer Ag | Block copolymer |
-
1981
- 1981-03-16 JP JP3837481A patent/JPS57151622A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5580435A (en) * | 1978-10-30 | 1980-06-17 | Monsanto Co | Molding resin composition |
JPS57149329A (en) * | 1981-02-13 | 1982-09-14 | Bayer Ag | Block copolymer |
Also Published As
Publication number | Publication date |
---|---|
JPS57151622A (en) | 1982-09-18 |
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