JPH06192375A - Crosslinked material of polymer composition and its production - Google Patents
Crosslinked material of polymer composition and its productionInfo
- Publication number
- JPH06192375A JPH06192375A JP4357919A JP35791992A JPH06192375A JP H06192375 A JPH06192375 A JP H06192375A JP 4357919 A JP4357919 A JP 4357919A JP 35791992 A JP35791992 A JP 35791992A JP H06192375 A JPH06192375 A JP H06192375A
- Authority
- JP
- Japan
- Prior art keywords
- molecular weight
- crosslinking
- polyurethane elastomer
- crosslinked material
- high molecular
- 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.)
- Pending
Links
- 239000000203 mixture Substances 0.000 title claims abstract description 14
- 229920000642 polymer Polymers 0.000 title claims description 6
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000011243 crosslinked material Substances 0.000 title abstract 3
- 229920001610 polycaprolactone Polymers 0.000 claims abstract description 17
- 239000004632 polycaprolactone Substances 0.000 claims abstract description 17
- 229920003225 polyurethane elastomer Polymers 0.000 claims abstract description 16
- 238000004132 cross linking Methods 0.000 claims abstract description 10
- 239000003054 catalyst Substances 0.000 claims abstract description 8
- 239000012948 isocyanate Substances 0.000 claims abstract description 7
- 150000002513 isocyanates Chemical class 0.000 claims abstract description 7
- 229920006037 cross link polymer Polymers 0.000 claims description 2
- 239000011347 resin Substances 0.000 abstract description 6
- 229920005989 resin Polymers 0.000 abstract description 6
- 229920002635 polyurethane Polymers 0.000 abstract description 2
- 239000004814 polyurethane Substances 0.000 abstract description 2
- 239000008096 xylene Substances 0.000 abstract description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- 238000011156 evaluation Methods 0.000 description 8
- 238000000465 moulding Methods 0.000 description 8
- -1 polyethylene Polymers 0.000 description 7
- 229920005862 polyol Polymers 0.000 description 7
- 239000003431 cross linking reagent Substances 0.000 description 5
- 229920001228 polyisocyanate Polymers 0.000 description 5
- 239000005056 polyisocyanate Substances 0.000 description 5
- 150000003077 polyols Chemical class 0.000 description 5
- 238000004898 kneading Methods 0.000 description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 229920003232 aliphatic polyester Polymers 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 238000009864 tensile test Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 238000012644 addition polymerization Methods 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 2
- 238000000071 blow moulding Methods 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 239000012770 industrial material Substances 0.000 description 2
- 150000002596 lactones Chemical class 0.000 description 2
- 229920000515 polycarbonate Polymers 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920001059 synthetic polymer Polymers 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical compound O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 description 2
- SPBDXSGPUHCETR-JFUDTMANSA-N 8883yp2r6d Chemical compound O1[C@@H](C)[C@H](O)[C@@H](OC)C[C@@H]1O[C@@H]1[C@@H](OC)C[C@H](O[C@@H]2C(=C/C[C@@H]3C[C@@H](C[C@@]4(O[C@@H]([C@@H](C)CC4)C(C)C)O3)OC(=O)[C@@H]3C=C(C)[C@@H](O)[C@H]4OC\C([C@@]34O)=C/C=C/[C@@H]2C)/C)O[C@H]1C.C1C[C@H](C)[C@@H]([C@@H](C)CC)O[C@@]21O[C@H](C\C=C(C)\[C@@H](O[C@@H]1O[C@@H](C)[C@H](O[C@@H]3O[C@@H](C)[C@H](O)[C@@H](OC)C3)[C@@H](OC)C1)[C@@H](C)\C=C\C=C/1[C@]3([C@H](C(=O)O4)C=C(C)[C@@H](O)[C@H]3OC\1)O)C[C@H]4C2 SPBDXSGPUHCETR-JFUDTMANSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 239000004970 Chain extender Substances 0.000 description 1
- 239000004971 Cross linker Substances 0.000 description 1
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 1
- QORUGOXNWQUALA-UHFFFAOYSA-N N=C=O.N=C=O.N=C=O.C1=CC=C(C(C2=CC=CC=C2)C2=CC=CC=C2)C=C1 Chemical compound N=C=O.N=C=O.N=C=O.C1=CC=C(C(C2=CC=CC=C2)C2=CC=CC=C2)C=C1 QORUGOXNWQUALA-UHFFFAOYSA-N 0.000 description 1
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical compound ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229920003054 adipate polyester Polymers 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006482 condensation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920000909 polytetrahydrofuran Polymers 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 150000003606 tin compounds Chemical class 0.000 description 1
- 150000003609 titanium compounds Chemical class 0.000 description 1
Landscapes
- Polyurethanes Or Polyureas (AREA)
- Biological Depolymerization Polymers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、耐熱性に優れた生分解
性を有する、高分子量ポリカプロラクトンとポリウレタ
ンエラストマーとを架橋した重合体及びその製造方法に
関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polymer obtained by cross-linking a high molecular weight polycaprolactone and a polyurethane elastomer having excellent heat resistance and biodegradability, and a method for producing the same.
【0002】[0002]
【従来の技術】最近、医療や農林漁業分野及び産業資材
分野への適用を目指し、また廃棄物処理問題とも関連し
て、生分解性を有する合成高分子化合物としてのポリカ
プロラクトン等の脂肪族ポリエステルの開発研究が行わ
れている。しかし、脂肪族ポリエステルは生分解性は示
すものの、融点が低く、耐熱性が劣り、実用上、容器、
フィルム、繊維など広範囲に利用できるものではなかっ
た。そのため、脂肪族ポリエステルと他の熱可塑性樹脂
例えばポリエチレン、ポリプロピレン、ポリスチレン、
ポリエチレンテレフタレート、ポリアミド等の樹脂との
ブレンドにより、耐熱性等を付与した組成物が検討され
たが、生分解性が必ずしも満足のゆくものではなかっ
た。2. Description of the Related Art Recently, aliphatic polyesters such as polycaprolactone as biodegradable synthetic polymer compounds have been aimed at application to the fields of medicine, agriculture, forestry and fisheries and industrial materials, and in connection with waste treatment problems. Development research is being conducted. However, although the aliphatic polyester exhibits biodegradability, it has a low melting point and poor heat resistance, and is practically used for containers and
It could not be used for a wide range of purposes such as films and fibers. Therefore, aliphatic polyester and other thermoplastics such as polyethylene, polypropylene, polystyrene,
A composition in which heat resistance and the like were imparted by blending with a resin such as polyethylene terephthalate or polyamide was investigated, but biodegradability was not always satisfactory.
【0003】[0003]
【発明が解決しようとする課題】本発明は、上記欠点を
解決するために成されたものであり、耐熱性に優れ、容
易にしかも短時間で製造し得る、生分解性にも優れた合
成高分子化合物を提供することを目的とする。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned drawbacks, and it is a synthesis which is excellent in heat resistance, can be easily produced in a short time, and is excellent in biodegradability. It is intended to provide a polymer compound.
【0004】[0004]
【課題を解決するための手段】本発明者は、耐熱性に優
れ、容易にしかも短時間で製造し得る、生分解性にも優
れた合成高分子化合物を得るべく鋭意検討した結果、生
分解性の優れた高分子量ポリカプロラクトンとポリウレ
タンエラストマーとを架橋させることにより本発明を完
成させた。Means for Solving the Problems The present inventor has conducted extensive studies to obtain a synthetic polymer compound which is excellent in heat resistance, can be easily produced in a short time, and is excellent in biodegradability. The present invention was completed by crosslinking a high molecular weight polycaprolactone having excellent properties and a polyurethane elastomer.
【0005】すなわち、本発明は、 1) 高分子量ポリカプロラクトンとポリウレタンエラ
ストマーとをイソシアネート系触媒により架橋させたポ
リマー組成物の架橋体。 2) 高分子量ポリカプロラクトン、ポリウレタンエラ
ストマー及びイソシアネート系触媒を押出機に連続的に
供給して架橋させることを特徴とするポリマー組成物架
橋体の製造方法。に関する。That is, the present invention is: 1) A crosslinked body of a polymer composition obtained by crosslinking a high molecular weight polycaprolactone and a polyurethane elastomer with an isocyanate catalyst. 2) A method for producing a crosslinked polymer composition, which comprises continuously supplying a high molecular weight polycaprolactone, a polyurethane elastomer and an isocyanate catalyst to an extruder for crosslinking. Regarding
【0006】本発明において用いられる高分子量ポリカ
プロラクトンは、ε−カプロラクトンとエチレングリコ
ールやジエチレングリコール等のジオールとを触媒の存
在下で反応させて得られる。この反応において用いられ
る触媒としては有機スズ化合物、有機チタン化合物、有
機ハロゲン化スズ化合物が一般的である。この触媒を
0.1〜5000ppm添加し、反応温度は100〜2
30℃で、好ましくは不活性気体中で重合させることに
より本発明において使用可能な高分子量ポリカプロラク
トンが得られる。この製法は例えば特公昭35−189
号、特公昭35−497号、特公昭40−23917
号、特公昭40−26557号、特公昭43−2473
号、特公昭47−14739号、特開昭56−4972
8号、特開昭58−61119号等の公報に開示されて
いる。本発明に使用する高分子量ポリカプロラクトンの
分子量は特に制限されるものではないが、数平均分子量
が1000〜200000のものが好適に用いられ、高
分子量ポリカプロラクトンを一種類使用してもよく、あ
るいは分子量の異なる高分子量ポリカプロラクトンを二
種類以上使用してもよい。The high molecular weight polycaprolactone used in the present invention is obtained by reacting ε-caprolactone with a diol such as ethylene glycol or diethylene glycol in the presence of a catalyst. As a catalyst used in this reaction, an organic tin compound, an organic titanium compound, and an organic tin halide compound are generally used. 0.1 to 5000 ppm of this catalyst is added, and the reaction temperature is 100 to 2
Polymerization at 30 ° C., preferably in an inert gas, gives the high molecular weight polycaprolactone usable in the present invention. This manufacturing method is, for example, Japanese Patent Publication No. 35-189.
No. 35, Japanese Patent Publication No. 35-497, Japanese Patent Publication No. 40-23917
No. 40-257557 and 43-2473
No. 4, JP-B-47-14739, JP-A-56-4972
No. 8 and JP-A-58-611119. The molecular weight of the high molecular weight polycaprolactone used in the present invention is not particularly limited, but those having a number average molecular weight of 1,000 to 200,000 are preferably used, and one type of high molecular weight polycaprolactone may be used, or Two or more kinds of high molecular weight polycaprolactone having different molecular weights may be used.
【0007】本発明において用いられるポリウレタンエ
ラストマーは、ポリメリックポリオールから成るソフト
セグメントと、ハードセグメントを構成する単分子鎖延
長剤とポリイソシアネートから成る。具体的には次のよ
うなタイプがある。 (1)アジペート系ポリエステルタイプ:アゾピン酸と
グリコール、トリオールとの縮合反応によるアジペート
系エステルポリオールに短鎖ポリオールの存在下ポリイ
ソシアネートを付加重合したもの。 (2)ラクトン系ポリエステルタイプ:ε−カプロラク
トンの開環重合により得られるポリラクトンエステルポ
リオールに短鎖ポリオールの存在下ポリイソシアネート
を付加重合したもの。 (3)ポリカーボネートタイプ:グリコール、例えばプ
ロピレングリコール、ヘキサメチレングリコールと活性
基を有するカーボネート、例えばジエチルカーボネー
ト、またはホスゲンを反応させて得たポリカーボネート
グリコールに短鎖ポリオールの存在下ポリイソシアネー
トを付加重合したもの。 (4)ポリエーテルタイプ:テトラヒドロフランの開環
重合により得られたポリテトラメチレンエーテルグリコ
ールに短鎖ポリオールの存在下ポリイソシアネートを付
加重合したもの。 本発明に使用するポリウレタンエラストマーは、上記に
例示したいずれのものも使用でき、ポリウレタンエラス
トマーを一種類使用してもよく、あるいは異なるポリウ
レタンエラストマーを二種類以上使用してもよい。The polyurethane elastomer used in the present invention comprises a soft segment made of a polymeric polyol, a monomolecular chain extender constituting a hard segment, and a polyisocyanate. Specifically, there are the following types. (1) Adipate-based polyester type: Polyisocyanate addition-polymerized in the presence of a short-chain polyol to an adipate-based ester polyol by a condensation reaction of azopic acid with glycol or triol. (2) Lactone-based polyester type: a polylactone ester polyol obtained by ring-opening polymerization of ε-caprolactone with a polyisocyanate in the presence of a short-chain polyol. (3) Polycarbonate type: Glycol such as propylene glycol or hexamethylene glycol and a carbonate having an active group such as diethyl carbonate, or polycarbonate glycol obtained by reacting phosgene with addition polymerization of polyisocyanate in the presence of a short chain polyol. . (4) Polyether type: Polytetramethylene ether glycol obtained by ring-opening polymerization of tetrahydrofuran with addition polymerization of polyisocyanate in the presence of short-chain polyol. As the polyurethane elastomer used in the present invention, any of those exemplified above can be used, and one kind of polyurethane elastomer may be used, or two or more kinds of different polyurethane elastomers may be used.
【0008】高分子量ポリカプロラクトンとポリウレタ
ンエラストマーとの組成比は、95/5〜30/70で
ある。この組成比が95/5より大きくなると得られた
共重合体の耐熱性が不足する。またこの組成比が30/
70より小さくなると、得られた共重合体の生分解性が
不満足になる。The composition ratio of the high molecular weight polycaprolactone and the polyurethane elastomer is 95/5 to 30/70. If this composition ratio exceeds 95/5, the heat resistance of the obtained copolymer will be insufficient. The composition ratio is 30 /
When it is less than 70, the biodegradability of the obtained copolymer becomes unsatisfactory.
【0009】本発明に使用される架橋剤は、ポリウレタ
ン用架橋剤のイソシアネート系のものが好適に使用でき
る。例えば、キシレンジイソシアネート、トリフェニル
メタントリイソシアネート、ポリメリックMDIなどで
ある。この架橋剤の添加量は特に制限されるものではな
いが、高分子量ポリカプロラクトンとポリウレタンエラ
ストマーの合計量に対して0.2〜0.8wt%が適当
である。The cross-linking agent used in the present invention is preferably an isocyanate-based cross-linking agent for polyurethane. For example, xylene diisocyanate, triphenylmethane triisocyanate, polymeric MDI and the like. The amount of the crosslinking agent added is not particularly limited, but 0.2 to 0.8 wt% is appropriate with respect to the total amount of the high molecular weight polycaprolactone and the polyurethane elastomer.
【0010】本発明の架橋体は上記組成物を押出機に連
続的に供給して混練架橋させることにより得られる。こ
のときの混練重合温度は樹脂温度で130〜300℃が
適当である。130℃より低いと混練と架橋反応が不充
分になり、300℃より高いと架橋体樹脂の色相が悪く
なる。本発明に用いる押出機は、L/Dが大きく混練性
の高い押出機が好ましい。押出機内滞留時間は1〜20
分間、好ましくは3〜15分間である。The crosslinked product of the present invention is obtained by continuously supplying the above composition to an extruder and kneading and crosslinking. At this time, the kneading polymerization temperature is suitably 130 to 300 ° C. in terms of resin temperature. If it is lower than 130 ° C, the kneading and crosslinking reaction will be insufficient, and if it is higher than 300 ° C, the hue of the crosslinked resin will be poor. The extruder used in the present invention is preferably an extruder having a large L / D and a high kneading property. Residence time in extruder is 1 to 20
Minutes, preferably 3 to 15 minutes.
【0011】[0011]
【実施例】以下実施例にて本発明を更に詳細に説明す
る。The present invention will be described in more detail with reference to the following examples.
【0012】実施例1 高分子量ポリカプロラクトン(商品名 P−787、数
平均分子量80000、米国ユニオンカーバイド・ケミ
カルズ・アンド・プラスチックス社製)50部、ポリウ
レタンエラストマー(商品名 パンデックス T−59
65、大日本インキ化学工業製 ラクトン系ポリエステ
ルタイプ)50部及び架橋剤(商品名クロスネートEM
−30、大日精化工業製)イソシアネート換算で0.5
部を下記に示したサンプル成形1及び2によりサンプル
成形して評価した。評価結果を後記の表1に示す。 Example 1 50 parts of high molecular weight polycaprolactone (trade name P-787, number average molecular weight 80,000, manufactured by Union Carbide Chemicals & Plastics, USA), polyurethane elastomer (trade name Pandex T-59)
65, Dainippon Ink and Chemicals Inc. lactone polyester type 50 parts and a cross-linking agent (trade name Crossnate EM)
-30, made by Dainichiseika Co., Ltd.) 0.5 in terms of isocyanate
The parts were sample-molded by sample molding 1 and 2 shown below and evaluated. The evaluation results are shown in Table 1 below.
【0013】実施例2 実施例1と同じだが、ポリウレタンエラストマーを次の
ものに変えた。商品名レザミンFR1090、大日精化
工業製 アジペート系ポリエステルタイプ。評価結果を
同じく表1に示す。 Example 2 Same as Example 1, but the polyurethane elastomer was changed to: Product name Resamine FR1090, Adipate polyester type manufactured by Dainichiseika. The evaluation results are also shown in Table 1.
【0014】比較例1 実施例1と同じだが、架橋剤の添加は行わなかった。評
価結果を表1に示す。比較例2 実施例2と同じだが、架橋剤の添加は行わなかった。評
価結果を表1に示す。比較例3 実施例1と同じだが、ポリウレタンエラストマーの添加
は行わなかった。評価結果を表1に示す。 Comparative Example 1 Same as Example 1, but without the addition of a cross-linking agent. The evaluation results are shown in Table 1. Comparative Example 2 Same as Example 2, but without the addition of crosslinker. The evaluation results are shown in Table 1. Comparative Example 3 Same as Example 1, but no polyurethane elastomer was added. The evaluation results are shown in Table 1.
【0015】サンプル成形1,引張試験片の調製 ブラベンダー(HAAKE BUCHLER 製、RH
EOCORD SYSTEM 40)に表1の組成物を
50g投入し、温度200℃、回転数50rpm、10
分間混練したものを、プレス成形で加熱(200℃、5
分間)及び冷却(20℃、3分間)して1mmシートを
作成した。このシートをJIS2号ダンベルで打ち抜
き、引張試験評価用試片とした。 サンプル成形2,耐熱試験等のボトルの作成 50mm一軸押出機(東芝機械製、TEM358)に表
1の組成物を連続投入した。押出樹脂温度200℃、回
転数100rpm、吐出量30kg/hr、押出機内滞
留時間6分間でポリマー組成物の架橋体を得た。次に上
記架橋体を中空成形機(日本製鋼所製、日鋼カウテック
NB3B)に投入し、樹脂温度160℃で高さ約10c
mのボトルを成形し、耐熱試験評価用のボトルとした。Sample molding 1, preparation of tensile test piece Brabender (manufactured by HAAKE BUCHLER, RH
50 g of the composition shown in Table 1 was put into EOCORED SYSTEM 40), the temperature was 200 ° C., the rotation speed was 50 rpm, and 10
Kneaded for minutes, heated by press molding (200 ℃, 5
1 min.) And cooled (20 ° C., 3 min) to prepare a 1 mm sheet. This sheet was punched with a JIS No. 2 dumbbell to obtain a test piece for tensile test evaluation. Sample molding 2, preparation of bottles for heat resistance test, etc. The composition of Table 1 was continuously charged into a 50 mm uniaxial extruder (TEM358, manufactured by Toshiba Machine). A crosslinked body of a polymer composition was obtained at an extrusion resin temperature of 200 ° C., a rotation speed of 100 rpm, a discharge rate of 30 kg / hr, and a residence time in the extruder of 6 minutes. Next, the above-mentioned cross-linked product was put into a blow molding machine (manufactured by Japan Steel Works, Nikko Kautech NB3B) and the resin temperature was 160 ° C and the height was about 10c.
m bottle was molded and used as a bottle for heat resistance test evaluation.
【0016】評価方法は次の通り。引張試験は、JIS
K7113に準拠して行った。ボトル成形性は、サン
プル成形2の中空成形機による成形において、正常なボ
トルができるか否かで評価した。耐熱性は、サンプル成
形2により成形したボトルを70℃のオーブンに入れ、
1日経過後、その形状を維持しているか否かで評価し
た。生分解性は、サンプル成形2により成形したボトル
を土壌埋没もしくは海水浸漬により、土壌埋設の場合は
12ヶ月、海水浸漬の場合は8ヶ月で完全消失するか否
かで評価した。得られた結果を下記の表1に要約する。The evaluation method is as follows. The tensile test is JIS
It carried out based on K7113. The bottle moldability was evaluated by whether or not a normal bottle was formed in the molding of the sample molding 2 by the blow molding machine. For heat resistance, put the bottle molded by sample molding 2 in an oven at 70 ° C,
After one day, it was evaluated whether the shape was maintained. The biodegradability was evaluated by whether or not the bottle molded by Sample Molding 2 completely disappears in 12 months when buried in soil or 8 months when immersed in seawater by immersing in soil or seawater. The results obtained are summarized in Table 1 below.
【0017】[0017]
【表1】 [Table 1]
【0018】[0018]
【発明の効果】本発明によって得られる架橋体は生分解
性及び耐熱性が優れるとともに機械的強度、成形加工性
にも優れる。またこの架橋体は容易にしかも短時間で製
造できるので医療や農林漁業分野及び産業資材分野への
適用が可能であり、使用後の廃棄物処理問題をも解決で
きる。The crosslinked product obtained by the present invention is excellent in biodegradability and heat resistance, as well as in mechanical strength and moldability. Further, since this crosslinked product can be easily produced in a short time, it can be applied to the fields of medical treatment, agriculture, forestry and fisheries, and industrial materials, and the problem of waste disposal after use can be solved.
Claims (2)
タンエラストマーとをイソシアネート系触媒により架橋
させたポリマー組成物の架橋体。1. A crosslinked body of a polymer composition obtained by crosslinking a high molecular weight polycaprolactone and a polyurethane elastomer with an isocyanate catalyst.
タンエラストマー及びイソシアネート系触媒を押出機に
連続的に供給して架橋させることを特徴とするポリマー
組成物架橋体の製造方法。2. A method for producing a crosslinked polymer composition, which comprises continuously supplying a high molecular weight polycaprolactone, a polyurethane elastomer and an isocyanate catalyst to an extruder for crosslinking.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4357919A JPH06192375A (en) | 1992-12-25 | 1992-12-25 | Crosslinked material of polymer composition and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4357919A JPH06192375A (en) | 1992-12-25 | 1992-12-25 | Crosslinked material of polymer composition and its production |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06192375A true JPH06192375A (en) | 1994-07-12 |
Family
ID=18456615
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4357919A Pending JPH06192375A (en) | 1992-12-25 | 1992-12-25 | Crosslinked material of polymer composition and its production |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06192375A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0780437A4 (en) * | 1995-07-10 | 2000-03-01 | Daicel Chem | CROSSLINKABLE OR CURABLE POLYLACTONE COMPOSITION, CROSSLINKED OR CURED MOLD OBTAINED FROM SAID COMPOSITION AND PROCESS FOR PRODUCING THE SAME |
JP2002336380A (en) * | 2001-05-17 | 2002-11-26 | Bridgestone Sports Co Ltd | Golf ball |
US8258254B2 (en) | 2002-06-17 | 2012-09-04 | Nec Corporation | Biodegradable resin, biodegradable resin composition, biodegradable molded object, and process for producing biodegradable resin |
KR101318474B1 (en) * | 2010-03-30 | 2013-10-16 | (주)엘지하우시스 | Compositions Comprising Crosslinked Biopolymer Having High Thermal Resistance And Elongation And Method of Producing the Same |
KR101387887B1 (en) * | 2011-07-14 | 2014-04-22 | (주)엘지하우시스 | Bio interior sheet and and manufacturing method thereof |
US9309361B2 (en) | 2012-09-21 | 2016-04-12 | Lg Hausys, Ltd. | Automobile interior sheet using bioresin and preparation method for the same |
US20210052344A1 (en) * | 2018-02-12 | 2021-02-25 | Orfit Industries N.V. | Immobilisation device |
-
1992
- 1992-12-25 JP JP4357919A patent/JPH06192375A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0780437A4 (en) * | 1995-07-10 | 2000-03-01 | Daicel Chem | CROSSLINKABLE OR CURABLE POLYLACTONE COMPOSITION, CROSSLINKED OR CURED MOLD OBTAINED FROM SAID COMPOSITION AND PROCESS FOR PRODUCING THE SAME |
JP2002336380A (en) * | 2001-05-17 | 2002-11-26 | Bridgestone Sports Co Ltd | Golf ball |
US8258254B2 (en) | 2002-06-17 | 2012-09-04 | Nec Corporation | Biodegradable resin, biodegradable resin composition, biodegradable molded object, and process for producing biodegradable resin |
KR101318474B1 (en) * | 2010-03-30 | 2013-10-16 | (주)엘지하우시스 | Compositions Comprising Crosslinked Biopolymer Having High Thermal Resistance And Elongation And Method of Producing the Same |
KR101387887B1 (en) * | 2011-07-14 | 2014-04-22 | (주)엘지하우시스 | Bio interior sheet and and manufacturing method thereof |
US9309361B2 (en) | 2012-09-21 | 2016-04-12 | Lg Hausys, Ltd. | Automobile interior sheet using bioresin and preparation method for the same |
US20210052344A1 (en) * | 2018-02-12 | 2021-02-25 | Orfit Industries N.V. | Immobilisation device |
US11944507B2 (en) * | 2018-02-12 | 2024-04-02 | Orfit Industries N.V. | Immobilisation device |
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