JPH08157705A - Biodegradable resin composition - Google Patents
Biodegradable resin compositionInfo
- Publication number
- JPH08157705A JPH08157705A JP6300949A JP30094994A JPH08157705A JP H08157705 A JPH08157705 A JP H08157705A JP 6300949 A JP6300949 A JP 6300949A JP 30094994 A JP30094994 A JP 30094994A JP H08157705 A JPH08157705 A JP H08157705A
- Authority
- JP
- Japan
- Prior art keywords
- resin composition
- phb
- poly
- biodegradable resin
- molecular weight
- 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
- 239000011342 resin composition Substances 0.000 title claims abstract description 9
- 229920006167 biodegradable resin Polymers 0.000 title claims abstract description 7
- 229920003232 aliphatic polyester Polymers 0.000 claims abstract description 12
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims abstract description 7
- 125000001931 aliphatic group Chemical group 0.000 claims abstract description 4
- 150000002334 glycols Chemical class 0.000 claims description 7
- WHBMMWSBFZVSSR-UHFFFAOYSA-N 3-hydroxybutyric acid Chemical compound CC(O)CC(O)=O WHBMMWSBFZVSSR-UHFFFAOYSA-N 0.000 claims description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000465 moulding Methods 0.000 abstract description 4
- 229920000070 poly-3-hydroxybutyrate Polymers 0.000 abstract 3
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 abstract 1
- 229920000331 Polyhydroxybutyrate Polymers 0.000 description 22
- 238000000034 method Methods 0.000 description 7
- 244000005700 microbiome Species 0.000 description 5
- 230000001580 bacterial effect Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 238000009864 tensile test Methods 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- -1 clothing Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000004151 fermentation Effects 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 238000005096 rolling process Methods 0.000 description 3
- 238000009987 spinning Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 241000589323 Methylobacterium Species 0.000 description 2
- 239000002253 acid Chemical class 0.000 description 2
- 150000008065 acid anhydrides Chemical class 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000012770 industrial material Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- BDJRBEYXGGNYIS-UHFFFAOYSA-N nonanedioic acid Chemical compound OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-UHFFFAOYSA-N 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- RTBFRGCFXZNCOE-UHFFFAOYSA-N 1-methylsulfonylpiperidin-4-one Chemical compound CS(=O)(=O)N1CCC(=O)CC1 RTBFRGCFXZNCOE-UHFFFAOYSA-N 0.000 description 1
- 241000588986 Alcaligenes Species 0.000 description 1
- 241000589151 Azotobacter Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000589350 Methylobacter Species 0.000 description 1
- 241000187654 Nocardia Species 0.000 description 1
- 108091005804 Peptidases Proteins 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 241000589516 Pseudomonas Species 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000012773 agricultural material Substances 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- JFCQEDHGNNZCLN-UHFFFAOYSA-N anhydrous glutaric acid Natural products OC(=O)CCCC(O)=O JFCQEDHGNNZCLN-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 238000000071 blow moulding Methods 0.000 description 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 150000001990 dicarboxylic acid derivatives Chemical class 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000010101 extrusion blow moulding Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000010102 injection blow moulding Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000010103 injection stretch blow moulding Methods 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 229920002601 oligoester Polymers 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000003856 thermoforming Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、優れた成形性、機械的
性能を有し、薬品、化粧品、食品及び産業資材・機械類
の包装部材、機械部品、繊維、モノフィラメント及び衣
料等として使用される生分解性に優れる樹脂組成物に関
する。INDUSTRIAL APPLICABILITY The present invention has excellent moldability and mechanical performance, and is used as a packaging member for medicines, cosmetics, foods and industrial materials / machines, machine parts, fibers, monofilaments, clothing and the like. The present invention relates to a resin composition having excellent biodegradability.
【0002】[0002]
【従来の技術】従来、数多くのプラスチックが、包装材
料、衣料、繊維、モノフィラメント及び工業機械部品用
の成形材料として、各種の産業において利用されてい
る。しかし近年、環境保護の立場から、プラスチックの
再利用が叫ばれるとともに、再利用が不可能な利用分野
において、微生物の働き、または加水分解等により分解
する生分解性樹脂の利用が社会的に強く要請されてきて
いる。芳香族化合物を使用したポリエステルは、通常高
い融点を持つかあるいは高いガラス転移点を示すため成
形体として使用できることが知られているものの、一般
的には生分解性がない。一方、脂肪族ポリエステルは、
微生物により分解されることが知られている。2. Description of the Related Art Many plastics have hitherto been used in various industries as molding materials for packaging materials, clothing, fibers, monofilaments and industrial machine parts. However, in recent years, from the standpoint of environmental protection, the reuse of plastics has been exclaimed, and in fields of application where reuse is not possible, the use of biodegradable resins that decompose due to the action of microorganisms or hydrolysis is strongly socially strong. It has been requested. Polyesters using aromatic compounds are generally known to have a high melting point or a high glass transition point and thus can be used as molded articles, but they are generally not biodegradable. On the other hand, aliphatic polyester is
It is known to be decomposed by microorganisms.
【0003】ポリ−3−ヒドロキシ酪酸(以下PHBと
略す)は、一般的に微生物による発酵法により製造され
る。PHBは、自然界に広く分布している微生物の働き
により完全に分解する生分解性を有し、かつ熱可塑性で
あることから、既存の成形法による各種用途への利用が
積極的に検討されつつある。しかしながら、PHBにつ
いては、溶融状態での熱安定性が不足し、成形が困難で
あり、また得られた成形物も伸びが小さく、硬くてもろ
いことが知られている。また、PHBの結晶化度は高
く、ガスバリアー性に優れているが、充分に結晶化した
PHBは延伸が困難であり、溶融紡糸、延伸により実用
可能な機械的性能を有する糸の製造は難しい。Poly-3-hydroxybutyric acid (hereinafter abbreviated as PHB) is generally produced by a fermentation method using a microorganism. PHB has biodegradability that is completely decomposed by the action of microorganisms widely distributed in nature, and is thermoplastic, so its use for various purposes by existing molding methods is being actively investigated. is there. However, it is known that PHB lacks thermal stability in a molten state and is difficult to mold, and the molded product obtained has a small elongation and is hard and brittle. Further, PHB has a high crystallinity and an excellent gas barrier property, but a sufficiently crystallized PHB is difficult to draw, and it is difficult to produce a yarn having practical mechanical performance by melt spinning or drawing. .
【0004】グリコール類と脂肪族ジカルボン酸とから
合成された脂肪族ポリエステル類は、一般的に弾性率が
小さく、また融点が100℃前後であり、このために耐
熱性が充分でない。このため、これら合成された脂肪族
ポリエステルとPHBは、環境保護に関する社会的要請
に応えられるだけの優れた生分解性を有しているにもか
かわらず、いまだ充分に利用されるには至っていない。Aliphatic polyesters synthesized from glycols and aliphatic dicarboxylic acids generally have a low elastic modulus and a melting point of about 100 ° C., and therefore the heat resistance is not sufficient. Therefore, although these synthesized aliphatic polyesters and PHBs have excellent biodegradability to meet social demands for environmental protection, they have not yet been fully utilized. .
【0005】[0005]
【発明が解決しようとする課題】本発明は、従来技術に
見られる前記問題を解決し、成形性、機械的性能および
耐熱性に優れる、高い実用性を有する生分解性樹脂組成
物を提供することをその課題とする。DISCLOSURE OF THE INVENTION The present invention solves the above problems found in the prior art and provides a biodegradable resin composition having excellent moldability, mechanical performance and heat resistance and having high practicality. That is the subject.
【0006】[0006]
【課題を解決するための手段】本発明者らは、前記課題
を解決すべく鋭意検討を重ねた結果、本発明を完成する
に至った。すなわち、グリコール類と脂肪族ジカルボン
酸またはその誘導体から合成された脂肪族ポリエステル
とPHBとからなる生分解性樹脂組成物が、機械的性能
と耐熱性を有する材料であることを見いだし本発明を完
成させた。The present inventors have completed the present invention as a result of intensive studies to solve the above problems. That is, a biodegradable resin composition comprising an aliphatic polyester synthesized from glycols and an aliphatic dicarboxylic acid or its derivative and PHB was found to be a material having mechanical performance and heat resistance, and the present invention was completed. Let
【0007】本発明で示される脂肪族ポリエステルとは
グリコール類と脂肪族ジカルボン酸、その酸無水物また
は低級アルキルエステル等の酸誘導体とから化学合成さ
れるポリエステルを主成分とするものであり、イソシア
ネートあるいは、カーボネート結合を形成し得る化合物
と上記脂肪族ポリエステルのオリゴエステルあるいはポ
リエステルとを反応させ分子量を充分高くしたものも含
まれる。The aliphatic polyester shown in the present invention is mainly composed of polyester chemically synthesized from glycols and an aliphatic dicarboxylic acid, its acid anhydride or an acid derivative such as a lower alkyl ester. Alternatively, a compound having a sufficiently high molecular weight is also included by reacting a compound capable of forming a carbonate bond with an oligoester or polyester of the above aliphatic polyester.
【0008】本発明で用いられるグリコール類として
は、例えばエチレングリコール、1,3および1,4−
ブタンジオール、トリメチレングリコール等が例示され
る。これらのグリコール類は併用しても良い。Examples of glycols used in the present invention include ethylene glycol, 1,3 and 1,4-
Examples are butanediol and trimethylene glycol. These glycols may be used in combination.
【0009】グリコール類と反応して脂肪族ポリエステ
ルを形成する脂肪族ジカルボン酸またはその酸誘導体と
しては、琥珀酸、アジピン酸、マロン酸、グルタル酸、
アゼライン酸等が例示され、これらのエステルあるいは
酸無水物も使用可能である。またジカルボン酸とその酸
誘導体は併用しても良い。Aliphatic dicarboxylic acids or acid derivatives thereof which react with glycols to form aliphatic polyesters include succinic acid, adipic acid, malonic acid, glutaric acid,
Azelaic acid and the like are exemplified, and esters or acid anhydrides thereof can also be used. The dicarboxylic acid and its acid derivative may be used in combination.
【0010】また、本発明の組成物のもう一つの構成成
分であるPHBは、化学合成したものでもよく、また微
生物が生産したものでもよい。例えばアルカリゲネス
(Alcaligenes )属、アゾトバクター(Azotobacter )
属、メチロバクテリウム(Methylobacterium)属、ノカ
ルジア(Nocardia)属、シュードモナス(Pseudo mona
s )属等の細菌を用いた公知の発酵法により製造するこ
とができる。発酵法により得られたPHBを含有する菌
体からPHBを分離精製する方法に関しては、例えば、
米国特許第3036959、同第4101533、同第
3275610、ヨーロッパ特許第15123に、ピリ
ジン、塩化メチレン、1,2−プロピレンカーボネー
ト、クロロホルム、1,2−ジクロロエタン等の溶剤を
用いた精製法が記載されており、また特願平5−323
019には細菌菌体を高圧ホモゲナイザーで破砕後、P
HBを分離し、分離したPHBを酸素系漂白剤で処理す
る方法が記載されている。本発明に使用するPHBは、
重量平均分子量40,000以上のPHBが良い。その
理由は、PHBの熱安定性が劣るためそれ以下の分子量
のPHBを使用すると溶融成形時に溶融粘度が低くなり
すぎ、満足な成形品が得られない、あるいは成形品の機
械的性能が充分ではない等の不都合が生じるためであ
る。PHB which is another constituent of the composition of the present invention may be chemically synthesized or may be produced by a microorganism. For example, the genus Alcaligenes, Azotobacter
Genus, Methylobacterium, Nocardia, Pseudomona
s) It can be produced by a known fermentation method using a bacterium of the genus or the like. Regarding the method for separating and purifying PHB from the bacterial cells containing PHB obtained by the fermentation method, for example,
U.S. Pat. Or, Japanese Patent Application No. 5-323
For 019, the bacterial cells were crushed with a high pressure homogenizer, and then P
A method for separating HB and treating the separated PHB with an oxygen-based bleach is described. The PHB used in the present invention is
PHB having a weight average molecular weight of 40,000 or more is preferable. The reason is that since PHB is poor in thermal stability, if PHB having a molecular weight lower than that is used, the melt viscosity becomes too low at the time of melt molding, and a satisfactory molded product cannot be obtained, or the mechanical performance of the molded product is insufficient This is because inconveniences such as not occurring occur.
【0011】本発明の樹脂組成物には、無機充填剤や顔
料、酸化防止剤、可塑剤等の慣用の補助添加物を配合す
ることができる。本発明の組成物は、射出成形、射出ブ
ロー成形、射出延伸ブロー成形、押出、押出ブロー成
形、押出延伸ブロー成形、延伸、圧延、熱成形、紡糸、
延伸を伴う紡糸、紡績、紡織等の一般に熱成形性樹脂に
適用され得る成形加工法により、シート、フィルム、軟
質および硬質の容器・ボトル、チューブ、モノフィラメ
ント、繊維、不織布、織布、機械部品、スポーツ用具部
品の製品に転化させることができる。The resin composition of the present invention may contain conventional auxiliary additives such as inorganic fillers, pigments, antioxidants and plasticizers. The composition of the present invention includes injection molding, injection blow molding, injection stretch blow molding, extrusion, extrusion blow molding, extrusion stretch blow molding, stretching, rolling, thermoforming, spinning,
By a molding processing method that can be generally applied to thermoformable resins such as spinning accompanied by stretching, spinning, and weaving, sheets, films, soft and hard containers / bottles, tubes, monofilaments, fibers, nonwoven fabrics, woven fabrics, machine parts, It can be converted into sports equipment parts products.
【0012】これら成形加工品のとくに具体的な用途と
して、使用後の回収または再利用が不可能または困難な
資材、例えば医療用器具及び備品、食品、薬剤、香料等
の容器、ゴミ袋、釣り糸、漁網等の糸、網、医療用、工
業用の布、その他の工業および農業用資材等を示すこと
ができる。As a particularly specific use of these molded products, materials that cannot be collected or reused after use or are difficult, such as medical instruments and equipment, containers for foods, drugs, fragrances, garbage bags, fishing lines. , Yarn such as fishing nets, nets, medical and industrial cloths, and other industrial and agricultural materials.
【0013】[0013]
【実施例】次に実施例により本発明を詳細に説明する
が、本発明はこれに限定されるものではない。なお、以
下において示す引張特性は以下のようにして測定した。 装置:引張試験機 試験片形状:短冊型 長さ100mm、幅10mm、チ
ャック間50mm 引張速度:50mm/min 測定条件:温度23℃または80℃、相対湿度50%EXAMPLES Next, the present invention will be described in detail with reference to examples, but the present invention is not limited thereto. The tensile properties shown below were measured as follows. Apparatus: Tensile tester Test piece shape: Strip length 100 mm, width 10 mm, chuck distance 50 mm Peeling speed: 50 mm / min Measuring conditions: temperature 23 ° C or 80 ° C, relative humidity 50%
【0014】実施例1〜3 工業技術院生命工学工業技術研究所に寄託してある細
菌、プロトモナス エクストルクエンス (Protomonas e
xtorquens) K(受託番号:FERM BP−354
8)を用い、メタノールを炭素源として好気的に連続培
養を行った。培養条件は培養温度32℃、培養pH6.
5、平均滞留時間40時間であり、窒素の供給速度が菌
体増殖の律速なるよう連続培養を行った。なお、最近の
文献によれば本菌はメチロバクテリウム(Methylobacter
ium)属に属するとされている (I.J.Bousfield and P.N.
Green; Int.J.Syst.Bacteriol.,35,209(1985) 、T.Urak
ami etal.; Int.J.Syst.Bacteriol.,43,504-513(1993))
。連続培養により得られた菌体を上記特願平5−32
3019に記載のPHBの分離精製方法に従い、高圧ホ
モゲナイザーで破砕後、PHBを遠心分離し、分離した
PHBを先ずプロテアーゼで処理し次いで過酸化水素処
理を行い高純度のPHBを得た。この精製したPHBの
分子量は1,000,000であった。このPHBをス
クリュー型押出機を用いてペレット化した。ペレット化
した時点での分子量は700,000であった。こうし
て得られたPHBペレットと脂肪族ポリエステル(昭和
高分子社製「ビオノーレ #1010」)とをPHB重
量部30%、60%、80%、となるようにそれぞれ両
者を混合し、単軸押出機[(株)東洋精機製、ラボプラ
ストミル、スクリュー直径:20mm]を使用してシリ
ンダー温度を170〜190℃としてTダイ・冷却ロー
ル法により(冷却ロール温度:25〜55℃)、厚さ約
200μmのシートを作製した。Examples 1 to 3, Protomonas e, a bacterium, which has been deposited at the Institute of Biotechnology, Institute of Biotechnology, AIST.
xtorquens) K (consignment number: FERM BP-354
Using 8), continuous culture was performed aerobically using methanol as a carbon source. The culture conditions are a culture temperature of 32 ° C. and a culture pH of 6.
5, the average residence time was 40 hours, and continuous culture was performed so that the nitrogen supply rate was the rate-determining factor for bacterial growth. According to recent literature, this bacterium is Methylobacter
(Iium Bousfield and PN)
Green; Int.J.Syst.Bacteriol., 35,209 (1985), T. Urak
ami et al .; Int.J.Syst.Bacteriol., 43,504-513 (1993))
. The bacterial cells obtained by continuous culturing are described in Japanese Patent Application No. 5-32 mentioned above.
According to the method for separating and purifying PHB described in 3019, after crushing with a high-pressure homogenizer, PHB was centrifuged, and the separated PHB was first treated with protease and then treated with hydrogen peroxide to obtain high-purity PHB. The molecular weight of this purified PHB was 1,000,000. The PHB was pelletized using a screw type extruder. The molecular weight at the time of pelletization was 700,000. The PHB pellets thus obtained and the aliphatic polyester (“Bionore # 1010” manufactured by Showa High Polymer Co., Ltd.) were mixed so that the PHB parts by weight were 30%, 60% and 80%, respectively, and a single screw extruder was used. [Toyo Seiki Co., Ltd., Labo Plastomill, screw diameter: 20 mm] is used, and the cylinder temperature is set to 170 to 190 ° C. by the T-die / cooling roll method (cooling roll temperature: 25 to 55 ° C.), thickness approximately. A 200 μm sheet was prepared.
【0015】得られたシートから長さ100mm、幅1
0mmの短冊型試験片を切り出し、23℃での引張試験
を行った。その結果を表1に示す。 比較例1 脂肪族ポリエステル(昭和高分子社製「ビオノーレ#1
010」)を単軸押出機[(株)東洋精機製、ラボプラ
ストミル、スクリュー直径:20mm]を使用してシリ
ンダー温度を170〜190℃としてTダイ・冷却ロー
ル法により(冷却ロール温度:25〜55℃)、厚さ約
200μmのシートを作製した。得られたシートから長
さ100mm、幅10mmの短冊型試験片を切り出し、
23℃での引張試験を行った。その結果を表1に示す。From the obtained sheet, length 100 mm, width 1
A 0 mm strip-shaped test piece was cut out and a tensile test was performed at 23 ° C. Table 1 shows the results. Comparative Example 1 Aliphatic polyester (“Bionore # 1” manufactured by Showa High Polymer Co., Ltd.
010 ") using a single-screw extruder [manufactured by Toyo Seiki Co., Ltd., Labo Plastomill, screw diameter: 20 mm] with a cylinder temperature of 170 to 190 ° C. and a T-die / cooling roll method (cooling roll temperature: 25 A sheet having a thickness of about 200 μm was prepared. A strip type test piece having a length of 100 mm and a width of 10 mm was cut out from the obtained sheet,
A tensile test was performed at 23 ° C. Table 1 shows the results.
【0016】実施例4〜7 実施例1〜4で得られたシートを80℃での引張試験を
行った。その結果を表2に示す。 比較例2 比較例1で得られたシートを80℃での引張試験を行っ
た。その結果を表2に示す。Examples 4 to 7 The sheets obtained in Examples 1 to 4 were subjected to a tensile test at 80 ° C. The results are shown in Table 2. Comparative Example 2 The sheet obtained in Comparative Example 1 was subjected to a tensile test at 80 ° C. The results are shown in Table 2.
【0017】[0017]
【表1】 [Table 1]
【0018】[0018]
【表2】 [Table 2]
【0019】[0019]
【発明の効果】本発明の組成物は、成形性に優れるとと
もに、機械的性能、耐熱性、ガスバリアー性および生分
解性に優れた成形物を与える。INDUSTRIAL APPLICABILITY The composition of the present invention provides a molded product having excellent moldability and mechanical properties, heat resistance, gas barrier properties and biodegradability.
Claims (2)
はその誘導体とから合成された脂肪族ポリエステルとポ
リ−3−ヒドロキシ酪酸とからなる生分解性樹脂組成
物。1. A biodegradable resin composition comprising an aliphatic polyester synthesized from glycols and an aliphatic dicarboxylic acid or a derivative thereof and poly-3-hydroxybutyric acid.
リ−3−ヒドロキシ酪酸を使用する請求項1記載の生分
解性樹脂組成物。2. The biodegradable resin composition according to claim 1, wherein poly-3-hydroxybutyric acid having a weight average molecular weight of 400,000 or more is used.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6300949A JPH08157705A (en) | 1994-12-05 | 1994-12-05 | Biodegradable resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6300949A JPH08157705A (en) | 1994-12-05 | 1994-12-05 | Biodegradable resin composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08157705A true JPH08157705A (en) | 1996-06-18 |
Family
ID=17891033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6300949A Pending JPH08157705A (en) | 1994-12-05 | 1994-12-05 | Biodegradable resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08157705A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2020516712A (en) * | 2017-04-05 | 2020-06-11 | バイオ−テック ビオローギッシュ ナチューフェアパックンゲン ゲーエムベーハー ウント コンパニ カーゲー | Biodegradable film |
-
1994
- 1994-12-05 JP JP6300949A patent/JPH08157705A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2020516712A (en) * | 2017-04-05 | 2020-06-11 | バイオ−テック ビオローギッシュ ナチューフェアパックンゲン ゲーエムベーハー ウント コンパニ カーゲー | Biodegradable film |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0996670B1 (en) | Pha compositions and methods for their use in the production of pha films | |
US7175917B2 (en) | Biaxially oriented polylactic acid-based resin films | |
KR100233184B1 (en) | Oriented polyglycolic acid film and production process thereof | |
EP1593705B1 (en) | Use of organic phosphonic or phosphinic acids, or of oxides, hydroxides or carboxylic acid salts of metals as thermal stabilizers for polyhydroxyalcanoates | |
KR100244057B1 (en) | Polyglycolic acid sheet and production process thereof | |
US5773562A (en) | Melt-stable semi-crystalline lactide polymer film and process for manufacture thereof | |
KR100515274B1 (en) | Biodegradable film and process for producing the same | |
WO2008004490A1 (en) | Aliphatic polyester composition and method for producing the same | |
JP2005501927A (en) | Processing of polyhydroxyalkanoates using nucleating agents and plasticizers | |
JP2001261797A (en) | Aliphatic polyester resin and molded product | |
JPH1072529A (en) | Polyglycolic acid injection-molded articles and production thereof | |
JP2008169239A (en) | Polyester film | |
JP5145695B2 (en) | Method for producing polylactic acid resin film | |
JP2001500174A (en) | Biaxially stretched, biodegradable and compostable film with improved properties | |
JP3518954B2 (en) | Polyethylene oxalate, molded product thereof, and production method thereof | |
AU676191B2 (en) | Polymer compositions | |
JP2004143432A (en) | Polylactic acid-based resin oriented film and method for producing the same | |
JPH08157705A (en) | Biodegradable resin composition | |
JP2005139280A (en) | Polyester resin composition and film | |
JP2000129143A (en) | Biodegradable molded product, its material and its production | |
JP2005126701A (en) | Molded product made from polylactic acid-based polymer composition | |
JP2005105150A (en) | Polyester film | |
JPH1160917A (en) | Biodegradable resin composition and its production | |
JP3623053B2 (en) | Biodegradable resin molding | |
JPH11323116A (en) | Biodegradable molding material, biodegradable molded article, and molding method for the biodegradable molding material |