JPH08165414A - Biodegradable resin composition - Google Patents

Biodegradable resin composition

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Publication number
JPH08165414A
JPH08165414A JP6310574A JP31057494A JPH08165414A JP H08165414 A JPH08165414 A JP H08165414A JP 6310574 A JP6310574 A JP 6310574A JP 31057494 A JP31057494 A JP 31057494A JP H08165414 A JPH08165414 A JP H08165414A
Authority
JP
Japan
Prior art keywords
phb
pcl
resin composition
biodegradable resin
melt viscosity
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
Application number
JP6310574A
Other languages
Japanese (ja)
Inventor
Hiroyuki Matsushita
浩幸 松下
Masahiro Harada
正広 原田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP6310574A priority Critical patent/JPH08165414A/en
Publication of JPH08165414A publication Critical patent/JPH08165414A/en
Pending legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Biological Depolymerization Polymers (AREA)

Abstract

PURPOSE: To obtain a completely biodegradable resin composition having excellent moldability and mechanical performances. CONSTITUTION: This biodegradable resin composition comprises a poly-3- hydroxybutyric acid having >=5,000P viscosity and a polycaprolactone having >=3,000P viscosity both at 185 deg.C under conditions of 1mm diameter and 10mm length of capillary dimensions and 10kgf/cm<2> pressure. The composition is excellent in moldability and mechanical performances.

Description

【発明の詳細な説明】Detailed Description of the Invention

【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、食品および産業資材・機械
類の包装部材、機械部品、繊維、モノフィラメントおよ
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 chemicals, 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、モノフィラメントおよび工業機械部品
用の成形材料として、各種の産業分野において利用され
ている。同時に、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、自然環境条件で微生物の働
きにより完全に分解する生分解性の高分子材料により完
全に分解する生分解性の高分子材料の開発が社会的に強
く要請されている。
2. Description of the Related Art A large number of plastics have hitherto been used in various industrial fields as molding materials for packaging materials, clothing, fibers, monofilaments and industrial machine parts. At the same time, from the standpoint of environmental protection, the reuse of plastics is called for, and the development of biodegradable polymer materials that are completely decomposed by biodegradable polymer materials that are completely decomposed by the action of microorganisms under natural environmental conditions. Is socially strongly demanded.

【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、またポ
リカプロラクトン(以下PCLと略す)は化学合成によ
り製造されている。PHBおよびPCL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。
一方、PCLは伸びは大きいが、融点が60℃と低いた
めに耐熱性が低いという欠点を有している。このため、
PHBとPCL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、各種分野において、いまだ充分に利用されるには至
っていない。
Poly-3-hydroxybutyric acid (hereinafter abbreviated as PHB) is generally manufactured by a fermentation method using a microorganism, and polycaprolactone (hereinafter abbreviated as PCL) is manufactured by a chemical synthesis. PHB and PCL have the biodegradability that they are completely decomposed by the action of microorganisms widely distributed in the natural world, and because they are thermoplastic, they are actively investigated for use in various applications by existing molding methods. Is being done. 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.
On the other hand, although PCL has a large elongation, it has a drawback of low heat resistance because of its low melting point of 60 ° C. For this reason,
Although PHB and PCL have excellent biodegradability to meet social demands for environmental protection, they have not yet been fully utilized in various fields.

【0004】また、特開平3−157450には、PH
BとPCLの共重合体を存在させることにより、伸び率
の良いフィルムを得られることが示されている。しか
し、このフィルムは、逆にその共重合体の存在が原因と
なり、結晶化速度の低下やガスバリアー性能を低下させ
る。また、本発明者等は、近ごろPHBとPCLの溶融
粘度比を規定することにより実用性のある生分解性樹脂
を作製することができることを示した。しかしながらこ
の場合、PHBとPCLとを混合して生分解性樹脂を得
ようとすると溶融粘度比だけではなく、使用するPHB
およびPCLそのものの溶融粘度が低いと、溶融成形が
困難になったり、得られた成形物の機械的性能が充分満
足できないことがある。
Further, Japanese Patent Laid-Open No. 3-157450 discloses a PH
It has been shown that the presence of the copolymer of B and PCL makes it possible to obtain a film having good elongation. However, on the contrary, this film causes a decrease in crystallization rate and a gas barrier performance due to the presence of the copolymer. Further, the present inventors have recently shown that a practical biodegradable resin can be produced by defining the melt viscosity ratio of PHB and PCL. However, in this case, when trying to obtain a biodegradable resin by mixing PHB and PCL, not only the melt viscosity ratio but also the PHB used
If the melt viscosity of PCL itself is low, melt molding may become difficult, or the mechanical performance of the obtained molded product may not be sufficiently satisfied.

【0005】[0005]

【発明が解決しようとする課題】本発明は、従来技術に
見られる前記課題を解決し、成形性に優れるとともに、
優れた物性の成形品を与える、実用性の高い生分解性樹
脂組成物を提供することである。
DISCLOSURE OF THE INVENTION The present invention solves the above problems found in the prior art and is excellent in moldability.
It is an object of the present invention to provide a highly practical biodegradable resin composition that gives a molded article having excellent physical properties.

【0006】[0006]

【課題を解決するための手段】本発明者等は、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、本発明によれば、185℃におけ
る粘度が、キャピラリー寸法、直径1mmφ、長さ10
mm、圧力10kgf/cm2 の条件下で、5,000
poise以上のPHBと3,000poise以上の
PCLとからなることを特徴とする生分解性を有し、か
つ成形性および機械的性能に優れた樹脂組成物が提供さ
れる。
The inventors of the present invention have completed the present invention as a result of intensive studies to solve the above problems. That is, according to the present invention, the viscosity at 185 ° C. is as follows: capillary size, diameter 1 mmφ, length 10
mm under a pressure of 10 kgf / cm 2
A resin composition having biodegradability and excellent in moldability and mechanical performance, which is characterized by comprising PHB of poise or more and PCL of 3,000 poise or more.

【0007】本発明で使用されるPHBは、化学合成し
たものでもよく、また微生物が製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(Methyl
obacterium)属、ノカルジア(Nocardia)属、シュード
モナス(Pseudomonas )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4
101533、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5−323019には細菌菌体を高圧ホモゲナイザ
ーで破砕後、PHB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。
The PHB used in the present invention may be chemically synthesized or produced by a microorganism.
For example, genus Alcaligenes, genus Azotobacter, methylobacterium (Methyl
It can be produced by a known fermentation method using a bacterium of the genus obacterium, the genus Nocardia, the genus Pseudomonas and the like. Regarding the method for separating and purifying PHB from the PHB-containing cells obtained by the fermentation method, for example, US Pat.
101533, No. 3275610, and European Patent No. 15123 describe a purification method using a solvent such as pyridine, methylene chloride, 1,2-propylene carbonate, chloroform and 1,2-dichloroethane, and Japanese Patent Application No. 323019 describes a method of crushing bacterial cells with a high-pressure homogenizer, separating PHB, and treating the separated PHB with an oxygen-based bleaching agent.

【0008】また、本発明の組成物のもう一つの構成成
分であるPCLは、カプロラクトンの開環重合反応など
の化学的な反応により合成されるポリエステルであり、
このPCLも自然界に広く分布している微生物の働きに
より、完全に生分解されることが明らかにされている。
PCL, which is another constituent of the composition of the present invention, is a polyester synthesized by a chemical reaction such as a ring-opening polymerization reaction of caprolactone,
It has been revealed that this PCL is also completely biodegraded by the action of microorganisms widely distributed in nature.

【0009】本発明では、用いられるPHBの粘度が
5,000POISE以上、かつPCLの粘度が3,0
00POISE以上であることが必要である。なぜな
ら、PHBの粘度がこれより低いものを使用した場合、
もう一方の構成要素であるPCLの粘度によって成形性
および機械的性能が大きく依存され、結果的にPHBと
PCLの溶融粘度比を考慮した狭い範囲でしか成形でき
ず、要求した性能が得られないおそれがある。また、P
CLの粘度がこれより低いものを使用した場合、均一な
溶融混合物を与えず、成形時の吐出むらや成形物の表面
の不均一性、成形物の外観不良を生じるなどの不都合を
引き起こすおそれがある。よって、溶融粘度が5,00
0POISE以上のPHBと溶融粘度が3,000PO
ISE以上であるPCLとから成る生分解性樹脂組成物
により、溶融粘度比等の要素を考慮に入れることなく成
形性および機械的強度、耐熱性、ガスバリアー特性に優
れる生分解性樹脂組成物を得られることが可能となる。
In the present invention, the PHB used has a viscosity of 5,000 POISE or more, and the PCL has a viscosity of 3.0.
It is necessary to be 00 POISE or more. This is because if PHB having a lower viscosity is used,
The viscosity of the other component, PCL, greatly depends on the moldability and mechanical performance, and as a result, molding can be performed only in a narrow range in consideration of the melt viscosity ratio of PHB and PCL, and the required performance cannot be obtained. There is a risk. Also, P
If a CL having a viscosity lower than this is used, a uniform melt mixture is not provided, and there is a risk of inconveniences such as uneven discharge during molding, uneven surface of the molded product, and poor appearance of the molded product. is there. Therefore, the melt viscosity is 5,000
PHB of 0 POISE or more and melt viscosity of 3,000 PO
A biodegradable resin composition comprising PCL that is ISE or higher provides a biodegradable resin composition that is excellent in moldability, mechanical strength, heat resistance, and gas barrier properties without considering factors such as melt viscosity ratio. Can be obtained.

【0010】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。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。
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. As a particularly specific application of these molded products, materials that are impossible or difficult to collect or reuse after use, such as medical instruments and equipment, containers for foods, drugs, fragrances, garbage bags, fishing lines, fishing nets, etc. Yarn, net, medical cloth, industrial cloth, other industrial and agricultural materials, and the like.

【0011】[0011]

【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
下において示す溶融粘度、引張特性は以下のようにして
測定した。 (1)溶融粘度 装置 :キャピラリーレオメーター((株)
島津製作所、フローテスターCFT−500) キャピラリー寸法:直径1mmφ 長さ10mm 測定温度 :185℃ 圧力 :10kgf/cm2 (2)引張試験 装置 :引張試験機((株)東洋精機社、ス
トログラフV1−C) 試験片形状 :短冊型 長さ100mm、幅10m
m、チャック間50mm 引張速度 :50mm/min 測定条件 :温度23℃または40℃、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 melt viscosity and tensile properties shown below were measured as follows. (1) Melt viscosity device: Capillary rheometer (Co., Ltd.)
Shimadzu, Flow tester CFT-500) Capillary dimensions: Diameter 1 mm φ Length 10 mm Measuring temperature: 185 ° C. Pressure: 10 kgf / cm 2 (2) Tensile test device: Tensile tester (Toyo Seiki Co., Ltd., Strograph V1-) C) Test piece shape: strip type length 100 mm, width 10 m
m, 50 mm between chucks Peeling speed: 50 mm / min Measurement conditions: Temperature 23 ° C or 40 ° C, relative humidity 50%

【0012】実施例1〜4 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
体増殖の律速と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(Methylobac
terium)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.
Urakami et al.; Int.J.Syst.Bacteriol.,43,504-513(1
993))。連続培養により得られた菌体を上記特願平5−
323019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壊後、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。
Examples 1 to 4 Protomonas e, a bacterium that 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 cell growth. According to recent literature, this bacterium is a methylobacterium (Methylobac
terium) (IJBousfield and
PNGreen; Int. J. Syst. Bacteriol., 35,209 (1985), T.
Urakami et al .; Int.J.Syst.Bacteriol., 43,504-513 (1
993)). The bacterial cells obtained by continuous culturing were used in the above-mentioned Japanese Patent Application No. 5-
According to the method for separating and purifying PHB described in 323019, after destroying 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.

【0013】このPHBをスクリュー型押出機を用いて
ペレット化した。こうして得られたPHBペレットの溶
融粘度は6310poiseであった。このPHBと溶
融粘度35400poiseのPCL(ダイセル化学工
業株式会社製「プラクセルH−7」)とをPHB重量部
20%、40%、60%、80%となるようにそれぞれ
混合し、単軸押出機(東洋精機株式会社製、ラボプラス
トミル、スクリュー直径:20mm)を使用し、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2
00μm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、2
3℃での引張試験を行った。その結果を表1に示す。
The PHB was pelletized using a screw type extruder. The PHB pellets thus obtained had a melt viscosity of 6310 poise. This PHB and PCL having a melt viscosity of 35400 poise ("Plaxel H-7" manufactured by Daicel Chemical Industries, Ltd.) were mixed so as to be PHB parts by weight of 20%, 40%, 60% and 80%, respectively, and then a single screw extruder was used. (Manufactured by Toyo Seiki Co., Ltd., Labo Plastomill, screw diameter: 20 mm) is used, and the cylinder temperature is 170 to 190 ° C. by the T-die / cooling roll method (cooling roll temperature: 25 to 55 ° C.), thickness about 2
A sheet of 00 μm was prepared. Cut a strip-shaped test piece 100 mm long and 10 mm wide from the obtained sheet, and
A tensile test was performed at 3 ° C. Table 1 shows the results.

【0014】比較例1 溶融粘度3,400poiseのPCLを用いて、実施
例1〜4で示した方法と同様にして、厚さ約200μm
のシートを作製した。得られたシートから長さ100m
m、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。
Comparative Example 1 Using PCL having a melt viscosity of 3,400 poise, a thickness of about 200 μm was obtained in the same manner as in Examples 1 to 4.
The sheet of was produced. 100m length from the obtained sheet
A strip-shaped test piece of m and a width of 10 mm was cut out and a tensile test was performed at 23 ° C. Table 1 shows the results.

【0015】比較例2〜3 実施例1〜4で使用したPHBと溶融粘度220poi
seであるPCL(ダイセル化学工業株式会社製「プラ
クセルH−4」を加熱により溶融粘度を低下させたも
の)とをPHB重量部40%、60%となるようにそれ
ぞれブレンドを行い、実施例1〜4で示した方法と同様
に厚さ200μmのシートの作製を行った。いずれの場
合も表面の不均一性、外観不良が著しく、シート作製は
不可能であった。
Comparative Examples 2-3 PHB used in Examples 1-4 and melt viscosity of 220 poi
PCL (separated from Daicel Chemical Industries Ltd. "Plaxel H-4" whose melt viscosity has been lowered by heating), which is SE, is blended so as to have PHB parts by weight of 40% and 60%, respectively. A sheet having a thickness of 200 μm was produced in the same manner as in the method shown in FIGS. In either case, the nonuniformity of the surface and the poor appearance were remarkable, and it was impossible to prepare a sheet.

【0016】実施例5〜8 プロトモナス エクストルクエンス(Protomonas extor
quens )K(受託番号:FERM BP−3548)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
の律速となるよう連続培養を行った。このPHBをスク
リュー型押出機を用いてペレット化した。こうして得ら
れたPHBの溶融粘度は、9310poiseであっ
た。このPHBと溶融粘度3400poiseのPCL
(ダイセル化学工業株式会社製「プラクセルH−7」を
加熱により溶融粘度を低下させたもの)とをPHB重量
部20%、40%、60%、80%となるようにそれぞ
れ混合を行い、実施例1〜4で示した方法と同様に、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。
Examples 5 to 8 Protomonas extorence
quens) K (accession number: FERM BP-3548), and aerobically and continuously cultivated using methanol as a carbon source. The culturing conditions were a culturing temperature of 32 ° C., a culturing pH of 6.5, and an average residence time of 40 hours. The PHB was pelletized using a screw type extruder. The PHB thus obtained had a melt viscosity of 9310 poise. This PHB and PCL with a melt viscosity of 3400 poise
("Placcel H-7" manufactured by Daicel Chemical Industries, Ltd., whose melt viscosity has been lowered by heating) and PHB parts by weight of 20%, 40%, 60%, and 80%, respectively, and then mixed. A sheet having a thickness of about 200 μm was produced in the same manner as in the methods shown in Examples 1 to 4. A strip-shaped test piece having a length of 100 mm and a width of 10 mm was cut out from the obtained sheet and subjected to a tensile test at 23 ° C. Table 1 shows the results.

【0017】実施例9〜12 実施例1〜4で得られたシートを40℃で、引張試験を
行った。その結果を表2に示す。
Examples 9 to 12 The sheets obtained in Examples 1 to 4 were subjected to a tensile test at 40 ° C. The results are shown in Table 2.

【0018】比較例4 比較例1で得られたシートの40℃での引張試験を行っ
た。結果を比較例1とともに表2に示す。
Comparative Example 4 The sheet obtained in Comparative Example 1 was subjected to a tensile test at 40 ° C. The results are shown in Table 2 together with Comparative Example 1.

【0019】[0019]

【表1】 表1 測定 混合比 溶融粘度 引張 引張 引張 実施例 温度 PHB/PCL (POISE) 強度 伸び 弾性率 (℃) (wt/wt) PHB PCL (kgf/mm2) (%) (kgf/mm2) 実施例1 23 20/80 6310 35400 1.5 >500 42 実施例2 23 40/60 6310 35400 1.7 370 75 実施例3 23 60/40 6310 35400 2.6 17 142 実施例4 23 80/20 6310 35400 2.6 3.3 178 実施例5 23 20/80 9310 3400 1.5 >500 42 実施例6 23 40/60 9310 3400 2.0 >500 97 実施例7 23 60/40 9310 3400 2.7 126 164 実施例8 23 80/20 9310 3400 3.0 1.9 225 ──────────────────────────────────比較例1 23 0/100 - 3400 1.4 >500 26 [Table 1] Table 1 Mixing ratio Melt viscosity Melt viscosity Tension Tension Tension Example Temperature PHB / PCL (POISE) Strength Elongation Modulus (℃) (wt / wt) PHB PCL (kgf / mm 2 ) (%) (kgf / mm 2 ) Example 1 23 20/80 6310 35400 1.5> 500 42 Example 2 23 40/60 6310 35400 1.7 370 75 Example 3 23 60/40 6310 35400 2.6 17 142 Example 4 23 80/20 6310 35400 2.6 3.3 178 Example 5 23 20/80 9310 3400 1.5> 500 42 Example 6 23 40/60 9310 3400 2.0> 500 97 Example 7 23 60/40 9310 3400 2.7 126 164 Example 8 23 80/20 9310 3400 3.0 1.9 225 ────────────────────────────────── Comparative Example 1 23 0/100-3400 1.4> 500 26

【0020】[0020]

【表2】 表2 測定 混合比 引張強度 引張弾性率 実施例 温度 PHB/PCL (kgf/mm2) (kgf/mm2) (℃) (wt/wt) 実施例9 40 20/80 1.2 49 実施例10 40 40/60 1.2 51 実施例11 40 60/40 1.7 107 実施例12 40 80/20 1.8 142 ────────────────────────────── 比較例1 23 0/100 1.4 26 比較例4 40 0/100 0.7 10 [Table 2] Table 2 Measurement Mixing ratio Tensile strength Tensile elastic modulus Example Temperature PHB / PCL (kgf / mm 2 ) (kgf / mm 2 ) (℃) (wt / wt) Example 9 40 20/80 1.2 49 Implementation Example 10 40 40/60 1.2 51 Example 11 40 60/40 1.7 107 Example 12 40 80/20 1.8 142 ───────────────────────── ────── Comparative example 1 23 0/100 1.4 26 Comparative example 4 40 0/100 0.7 10

【0021】[0021]

【発明の効果】本発明により、PHB、PCLの溶融粘
度比を考慮に入れることなく、成形性に優れるととも
に、引張性能等の機械的強度に優れた完全生分解性樹脂
成形品を提供することができる。
According to the present invention, it is possible to provide a completely biodegradable resin molded product which is excellent in moldability and has excellent mechanical strength such as tensile performance without considering the melt viscosity ratio of PHB and PCL. You can

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 185℃における粘度が、キャピラリー
寸法、直径1mmφ、長さ10mm、圧力10kgf/
cm2 の条件下で、5,000poise以上のポリ−
3−ヒドロキシ酪酸と3,000poise以上のポリ
カプロラクトンとからなる成形性および機械的性能に優
れる生分解性樹脂組成物。
1. Viscosity at 185 ° C., capillary size, diameter 1 mmφ, length 10 mm, pressure 10 kgf /
Under conditions of cm 2 , poly- of 5,000 poise or more
A biodegradable resin composition comprising 3-hydroxybutyric acid and 3,000 poise or more polycaprolactone having excellent moldability and mechanical performance.
JP6310574A 1994-12-14 1994-12-14 Biodegradable resin composition Pending JPH08165414A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6310574A JPH08165414A (en) 1994-12-14 1994-12-14 Biodegradable resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6310574A JPH08165414A (en) 1994-12-14 1994-12-14 Biodegradable resin composition

Publications (1)

Publication Number Publication Date
JPH08165414A true JPH08165414A (en) 1996-06-25

Family

ID=18006880

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6310574A Pending JPH08165414A (en) 1994-12-14 1994-12-14 Biodegradable resin composition

Country Status (1)

Country Link
JP (1) JPH08165414A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1027384A2 (en) 1997-10-31 2000-08-16 The Monsanto Company Polymer blends containing polyhydroxyalkanoates and compositions with good retention of elongation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1027384A2 (en) 1997-10-31 2000-08-16 The Monsanto Company Polymer blends containing polyhydroxyalkanoates and compositions with good retention of elongation

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