JP2000129143A - Biodegradable molded product, its material and its production - Google Patents
Biodegradable molded product, its material and its productionInfo
- Publication number
- JP2000129143A JP2000129143A JP10304293A JP30429398A JP2000129143A JP 2000129143 A JP2000129143 A JP 2000129143A JP 10304293 A JP10304293 A JP 10304293A JP 30429398 A JP30429398 A JP 30429398A JP 2000129143 A JP2000129143 A JP 2000129143A
- Authority
- JP
- Japan
- Prior art keywords
- biodegradable
- hydroxybutyric acid
- natural organic
- poly
- cellulose powder
- 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
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、木粉、セルロース
パウダー等の天然有機材を配合した生分解性成形材料、
該生分解性成形材料よりなる生分解性成形品及び該生分
解性成形品の製造方法に関する。さらに詳しくは、高剛
性、高い形状安定性、無機物配合材に比べ低い比重を示
すなど優れた物理的性能、及び優れた生分解性を有する
木粉、セルロースパウダーなどの天然有機材を配合した
生分解性樹脂成形材料、該生分解性成形材料よりなる生
分解性成形品及び該生分解性成形品の製造方法に関す
る。TECHNICAL FIELD The present invention relates to a biodegradable molding material containing a natural organic material such as wood flour or cellulose powder.
The present invention relates to a biodegradable molded article comprising the biodegradable molding material and a method for producing the biodegradable molded article. More specifically, high physical properties such as high rigidity, high shape stability, low specific gravity compared to inorganic compounding materials, and excellent biodegradable wood flour, natural biomaterials such as cellulose powder, etc. The present invention relates to a biodegradable resin molding material, a biodegradable molded product comprising the biodegradable molding material, and a method for producing the biodegradable molded product.
【0002】[0002]
【従来の技術】従来、数多くのプラスチックスが産業資
材、機械部品、自動車部品などの成形材料として利用さ
れてきている。同時に、環境保護の立場から、プラスチ
ックス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、又は加水分解等によ
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。生分解性樹脂は脂肪族ポリエステルや澱粉
を変性させた澱粉系が知られている。2. Description of the Related Art Conventionally, many plastics have been used as molding materials for industrial materials, machine parts, automobile parts and the like. At the same time, from the standpoint of environmental protection, the recycling of plastics is called for, and the use of biodegradable resins, which degrade by the action of microorganisms or hydrolysis, is strongly used in applications where recycling is not possible. It has been requested. Known biodegradable resins are aliphatic polyesters and starch modified starch.
【0003】脂肪族ポリエステルは、微生物による発酵
法や化学合成法などによって製造することができる。発
酵法で得られる脂肪族ポリエステルは、一般的にポリヒ
ドロキシアルカノエートであり、通常3−ヒドロキシ酪
酸単位を含むが、その分子組成やモル比率により、用途
に見合った性能を引き出すことが広く検討されている。
化学合成法では、ポリカプロラクトンやポリブチレンサ
クシネート、ポリエチレンサクシネート、ポリエステル
カーボネート、ポリ乳酸などがよく知られており、それ
ぞれの特徴に応じた用途開発が広く検討されている。澱
粉系では、その改質技術により、耐水性の改良や成形性
の改良が行われ、用途開発が進められている。高剛性が
必要とされる用途、例えば、接合部材、硬質日用雑貨
類、その他の硬質医療用、工業用及び農業用資材には、
3−ヒドロキシ酪酸単位を多く含む脂肪族ポリエステル
やポリ乳酸の利用が期待されている。[0003] Aliphatic polyesters can be produced by a fermentation method using a microorganism, a chemical synthesis method, or the like. The aliphatic polyester obtained by the fermentation method is generally a polyhydroxyalkanoate and usually contains a 3-hydroxybutyric acid unit. However, it has been widely studied that its molecular composition and molar ratio bring out performances suitable for the intended use. ing.
In the chemical synthesis method, polycaprolactone, polybutylene succinate, polyethylene succinate, polyester carbonate, polylactic acid, and the like are well known, and application development according to their characteristics is widely studied. With respect to starch, improvement of water resistance and improvement of moldability have been carried out by the modification technology, and application development has been promoted. For applications where high rigidity is required, for example, joining members, rigid daily necessities, other rigid medical, industrial and agricultural materials,
The use of aliphatic polyesters and polylactic acids containing a large amount of 3-hydroxybutyric acid units is expected.
【0004】しかしながら、3−ヒドロキシ酪酸単位を
多く含む脂肪族ポリエステルやポリ乳酸では、用途によ
っては剛性が不足し対応できず、さらにポリ乳酸では、
成形条件によっては60℃以上での形状安定性に劣る場
合がある。特公平7−37560号公報、特願平10−
128996号公報には、生分解性樹脂に炭酸カルシュ
ーム、炭酸マグネシューム、ガラス繊維などを配合した
材料について記載がある。しかし、生分解後、これら無
機物の堆積を嫌う用途には向かない。また、これら無機
物は比重が大きいため得られる成形品の比重が大きくな
り用途が限定される可能性がある。加えてガラス繊維の
場合、長時間使用による押出機のスクリューの磨耗、バ
レルの磨耗などが問題となる。この様な理由により高剛
性が必要な分野への積極的な生分解性樹脂の利用は達成
されていないのが現状である。However, aliphatic polyesters and polylactic acids containing a large amount of 3-hydroxybutyric acid units cannot be used due to insufficient rigidity in some applications.
Shape stability at 60 ° C. or higher may be poor depending on molding conditions. Japanese Patent Publication No. Hei 7-37560, Japanese Patent Application No. Hei 10-
Japanese Patent No. 128996 describes a material in which calcium carbonate, magnesium carbonate, glass fiber, and the like are mixed with a biodegradable resin. However, after biodegradation, it is not suitable for applications that dislike the deposition of these inorganic substances. Further, since these inorganic substances have a large specific gravity, the specific gravity of the obtained molded article becomes large, and there is a possibility that the use thereof is limited. In addition, in the case of glass fiber, there is a problem that the screw of the extruder and the barrel are worn due to long-term use. For these reasons, at present, active use of biodegradable resins in fields requiring high rigidity has not been achieved.
【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、機械的性能、生分解性に優
れる、生分解性成形材料及び該生分解性成形材料からな
る成形品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-mentioned problems in the prior art, and has excellent mechanical performance and biodegradability, and a biodegradable molding material and a molded article comprising the biodegradable molding material. Is to provide
【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、生分解性樹脂に木粉、セルロース
パウダーなどの天然有機材を配合することにより、機械
的性能及び形状安定性の改善がなされ、比較的低い比重
でも成形材料として充分使用に耐えうる性能となること
を見いだし、さらには、木粉を用い場合、成形方法によ
っては木材調の風合いの成形品を得ることが可能である
ことを見いだし、本発明を完成させた。Means for Solving the Problems The present inventors have made intensive studies to solve the above problems, and as a result, have completed the present invention. In other words, by blending a natural organic material such as wood powder and cellulose powder with a biodegradable resin, the mechanical performance and shape stability are improved, and the performance can be sufficiently used as a molding material even at a relatively low specific gravity. It has been found that, when wood powder is used, it is possible to obtain a molded product having a wood-like texture depending on the molding method, and the present invention has been completed.
【0007】本発明の要旨は、(1)生分解性樹脂に天
然有機材を配合してなる生分解性成形材料、(2)生分
解性樹脂に天然有機材を配合した生分解性成形材料から
なる生分解性成形品、及び(3)ポリ−3−ヒドロキシ
酪酸単位を含む脂肪族ポリエステルに水分含量が5重量
%以下の木粉及び/又はセルロースパウダーを1〜60
重量%配合し、130〜250℃で成形する生分解性成
形品の製造方法に関する。[0007] The gist of the present invention is to provide (1) a biodegradable molding material comprising a biodegradable resin and a natural organic material, and (2) a biodegradable molding material comprising a biodegradable resin and a natural organic material. And (3) an aliphatic polyester containing poly-3-hydroxybutyric acid units containing 1 to 60 wood flour and / or cellulose powder having a water content of 5% by weight or less.
The present invention relates to a method for producing a biodegradable molded article, which is blended at 130 to 250 ° C by weight.
【0008】[0008]
【発明の実施形態】本発明で示される生分解性樹脂と
は、微生物が産生する3−ヒドロキシ酪酸単位を含むポ
リヒドロキシアルカノエート、ポリ乳酸、グリコール類
と脂肪族カルボン酸などからの重合体、澱粉、変性した
澱粉などやこれらの混合体が含まれる。3−ヒドロキシ
酪酸単位を含むポリヒドロキシアルカノエートは、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(Methylobact
erium)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。BEST MODE FOR CARRYING OUT THE INVENTION The biodegradable resin represented by the present invention refers to a polyhydroxyalkanoate containing a 3-hydroxybutyric acid unit produced by a microorganism, a polylactic acid, a polymer derived from a glycol and an aliphatic carboxylic acid, etc. Starch, modified starch and the like and mixtures thereof are included. Polyhydroxyalkanoates containing 3-hydroxybutyric acid units include, for example, the genera Alcaligenes, Azotobacter, and Methylobact.
erium), Nocardia, Pseudomonas, etc. by a known fermentation method.
【0009】発酵法により得られたポリヒドロキシアル
カノエートを分離精製する方法に関しては、例えば、米
国特許第3036959号公報、同第4101533号
公報、同第3275610号公報、ヨーロッパ特許第1
5123号公報に、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
ロロエタンなどの溶剤を用いた精製法が記載されてお
り、また特開平7−177894号公報には細菌菌体を
高圧ホモジナイザーで破砕後、ポリヒドロキシアルカノ
エートを分離し、分離したポリヒドロキシアルカノエー
トを酵素系漂白剤で処理する方法が示されている。最近
では、発酵法によらずとも化学合成による3−ヒドロキ
シ酪酸単位を含むポリヒドロキシアルカノエートの製造
法が報告されている。また、ポリ乳酸は、化学合成法あ
るいは発酵法により得られる乳酸を原料とし、例えばラ
クチドとした後開環重合させる方法や、乳酸を直接重合
させる方法により製造することができる。グリコール類
と脂肪族カルボン酸などからの重合体は、例えば、コハ
ク酸とブタンジオールなどから製造することができ、必
要に応じてウレタン結合やカーボネート結合によって分
子量を調節することができる。Regarding the method of separating and purifying the polyhydroxyalkanoate obtained by the fermentation method, for example, US Pat. Nos. 3,036,959, 4,015,533, 3,275,610, and European Patent No. 1
No. 5123, pyridine, methylene chloride, 1,2-
A purification method using a solvent such as propylene carbonate, chloroform, and 1,2-dichloroethane is described, and JP-A-7-177894 crushes bacterial cells with a high-pressure homogenizer and then separates polyhydroxyalkanoate. A method of treating the separated polyhydroxyalkanoate with an enzyme bleach is disclosed. Recently, a method for producing a polyhydroxyalkanoate containing a 3-hydroxybutyric acid unit by chemical synthesis without using a fermentation method has been reported. Further, polylactic acid can be produced by using lactic acid obtained by a chemical synthesis method or a fermentation method as a raw material, for example, a method of ring-opening polymerization after forming lactide, or a method of directly polymerizing lactic acid. The polymer from glycols and aliphatic carboxylic acids can be produced, for example, from succinic acid and butanediol, and the molecular weight can be adjusted by urethane bonds or carbonate bonds as needed.
【0010】本発明で示される木粉、セルロースパウダ
ーなどの天然有機材として、木材を石臼、スタンプミ
ル、ロールミル、インパクトミルなどの方法により粉砕
した木粉(樹皮などの異物を取り除くことが好まし
い)、木粉に含まれるリグニンを取り除き精製したセル
ロースパウダーを例示することができる。材料となる木
材の種類は特に限定することはなく、例えば米栂などを
示すことができる。木粉、セルロースパウダーなどの天
然有機材は、吸湿性があり、空気中に放置すると数重量
部の水分を含む。生分解性樹脂に木粉、セルロースパウ
ダーなどの天然有機材を配合する際には、これら有機材
の水分を5重量部以下にすることが好ましい。さらに
は、1重量部以下にすることが好ましい。なぜなら、生
分解性樹脂は水による成形性の低下、性能の低下が見ら
れる場合が多く、強化材の持ち込みによる水分により、
この様な不具合が生じる可能性があるからである。As natural organic materials such as wood flour and cellulose powder shown in the present invention, wood is crushed by a millstone, stamp mill, roll mill, impact mill or the like (preferably removing foreign matter such as bark). And a cellulose powder purified by removing lignin contained in wood flour. The type of wood used as the material is not particularly limited, and may be, for example, rice toga. Natural organic materials such as wood powder and cellulose powder are hygroscopic and contain several parts by weight of moisture when left in the air. When natural organic materials such as wood powder and cellulose powder are blended with the biodegradable resin, it is preferable that the water content of these organic materials be 5 parts by weight or less. Further, the content is preferably 1 part by weight or less. This is because biodegradable resins often show reduced moldability and performance due to water.
This is because such a problem may occur.
【0011】本発明において、生分解性樹脂に木粉、セ
ルロースパウダーなどの天然有機材を配合する場合、溶
融混練するのが好ましい。なぜなら、溶融混練すること
によりこれら強化材が生分解性樹脂に均一に分散し、よ
り良い性能引き出すとともに、製品の性能のバラツキが
少なくなるからである。溶融混練するにはいくつかの方
法があるが、スクリュー型押出機を用いスクリューの回
転により混練する方法やヘンシェルミキサー中で加熱
し、溶融混練、造粒する方法を例示することができる。In the present invention, when a natural organic material such as wood powder or cellulose powder is blended with the biodegradable resin, it is preferable to carry out melt kneading. This is because the melt-kneading disperses these reinforcing materials evenly in the biodegradable resin, brings out better performance, and reduces the variation in the performance of the product. There are several methods for melt-kneading, and examples thereof include a method of kneading by rotation of a screw using a screw-type extruder and a method of melting, kneading, and granulating by heating in a Henschel mixer.
【0012】本発明による天然有機材配合材の成形方法
は特に限定することはなく、一般的な射出成形、押出成
形に共することができ、その中には木材調の風合いを得
るために、添加物をサイドフィードから添加する方法を
含めることができる。木粉、セルロースパウダーなどの
天然有機材は、1〜60重量%の割合で配合するのが好
ましい。さらには1〜40重量%が好ましい。なぜな
ら、1重量%以下であると剛性付与、強度付与の効果が
充分に発揮されず、性能が優れた成形物を得ることがで
きない。また60重量%を越えると、成形材料の円滑な
製造が困難になり、成形物の外観が悪くなるなどの欠点
が目立ち好ましくない。The molding method of the natural organic material compounding material according to the present invention is not particularly limited, and can be used for general injection molding and extrusion molding. A method of adding additives from a side feed can be included. Natural organic materials such as wood flour and cellulose powder are preferably blended at a ratio of 1 to 60% by weight. Further, the content is preferably 1 to 40% by weight. When the content is less than 1% by weight, the effects of imparting rigidity and imparting strength are not sufficiently exhibited, and a molded article having excellent performance cannot be obtained. On the other hand, if it exceeds 60% by weight, smooth production of the molding material becomes difficult, and disadvantages such as deterioration of the appearance of the molded product are noticeable, which is not preferable.
【0013】本発明による成形品を得る場合、樹脂温度
を130〜250℃として成形するのが好ましく、さら
には、140〜200℃とするのが好ましい。なぜな
ら、130℃以下であると生分解性樹脂が充分に可塑化
していないかあるいは粘度が高すぎて外観不良などの不
具合を生じるからである。また250℃を越えると、生
分解性樹脂の劣化、木粉の炭化などが顕著となり期待す
る性能が得られない可能性があるためである。本発明に
よる成形品を得る場合、成形後の冷却に用いる金型部材
の温度を20℃〜100℃とするのが好ましく、さらに
好ましくは、40℃〜80℃とするのが好ましい。なぜ
なら、射出成形の場合の成形サイクル時間を短くする、
あるいは、押出成形でシート・フィルム作製の場合の引
き取り速度を増加させるためには、この温度範囲が適当
であるからである。When the molded article according to the present invention is obtained, the molding is preferably performed at a resin temperature of 130 to 250 ° C., more preferably 140 to 200 ° C. This is because if the temperature is lower than 130 ° C., the biodegradable resin is not sufficiently plasticized or the viscosity is too high, which causes problems such as poor appearance. On the other hand, if the temperature exceeds 250 ° C., deterioration of the biodegradable resin, carbonization of wood powder, etc. become remarkable, and the expected performance may not be obtained. When the molded article according to the present invention is obtained, the temperature of the mold member used for cooling after molding is preferably 20 ° C to 100 ° C, and more preferably 40 ° C to 80 ° C. The reason is that the molding cycle time for injection molding is shortened,
Alternatively, this temperature range is appropriate in order to increase the take-up speed in the case of sheet / film production by extrusion molding.
【0014】本発明の範囲を逸脱せず、本発明の目的を
損なわない範囲において、生分解性樹脂、木粉、セルロ
ースパウダーなどの天然有機材以外の物質、例えば無機
充填剤、着色剤、可塑剤、結晶核剤、離型剤、滑剤、紫
外線吸収剤、帯電防止剤、難燃化剤、酸化防止剤などの
慣用の添加剤を目的に応じて添加することができる。本
発明の生分解性成形材料は、射出成形、押出成形など一
般の熱可塑性樹脂に適用されうる成形加工法により、工
業用・土木用・農業用・漁業用資材、機械部品、医療用
部材、繊維などを得ることができる。これら成形品の特
に具体的な用途として、使用後の回収又は再利用が不可
能又は困難な資材、例えば建材、土木用接合部材、医療
用器具及び備品、食品・薬剤・香料などの包装材、結束
部材、買い物袋、コンポスト用袋、漁業用ネット・不織
布、衣料用繊維、工業用不織布、農業用フィルム・シー
トなどを示すことができる。[0014] Substances other than natural organic materials such as biodegradable resins, wood flours and cellulose powders, such as inorganic fillers, coloring agents, plasticizers, etc., do not depart from the scope of the present invention and do not impair the objects of the present invention. Conventional additives such as an agent, a nucleating agent, a release agent, a lubricant, an ultraviolet absorber, an antistatic agent, a flame retardant, and an antioxidant can be added according to the purpose. The biodegradable molding material of the present invention is injection molding, extrusion molding and other molding methods applicable to thermoplastic resins, industrial, civil engineering, agricultural and fishing materials, machine parts, medical parts, Fibers and the like can be obtained. Particularly specific uses of these molded articles include materials that are impossible or difficult to recover or reuse after use, such as building materials, joining members for civil engineering, medical instruments and equipment, packaging materials for food, medicine, and fragrances, Examples include binding members, shopping bags, compost bags, fishing nets / nonwoven fabrics, clothing fibers, industrial nonwoven fabrics, agricultural film / sheets, and the like.
【0015】[0015]
【発明の効果】本発明により、機械的性能、生分解性に
優れ、高剛性である成形物を提供し、各種部材に適用さ
せることができる。According to the present invention, a molded article having excellent mechanical performance and biodegradability and having high rigidity is provided, and can be applied to various members.
【0016】[0016]
【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。尚、各種
測定は以下に示す方法で行った。 比重測定 : 水中置換法 引張試験 : JIS K 7213 曲げ試験 : JIS K 7203 荷重たわみ温度 : JIS K 7207(荷重1
8.6kg/cm2 ) 衝撃強度測定 : JIS K 7110Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples. Various measurements were performed by the following methods. Specific gravity measurement: Underwater displacement method Tensile test: JIS K 7213 Bending test: JIS K 7203 Deflection temperature under load: JIS K 7207 (Load 1
8.6 kg / cm 2 ) Impact strength measurement: JIS K 7110
【0017】実施例1〜2 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)属に属されている(I.J.Bousfield and P.N.Gr
een;Int.J.Syst.Bacteriol.,35,209(1985)、T.Urakami
etal.;Int.J.Syst.Bcteriol.,43,504-513(1993))。連
続培養により得られた菌体を上記特開平7−17789
4号公報に記載のポリ−3−ヒドロキシ酪酸の分離精製
法に従い、高圧ホモゲナイザーで破砕後、遠心分離し、
分離したポリ−3−ヒドロキシ酪酸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ポリ−3
−ヒドロキシ酪酸を得た。このポリ−3−ヒドロキシ酪
酸に水分率を0.7%とした木粉(販売元 島田商会、
セルロシン100M)又はセルロースパウダー(日本製
紙社製 KCフロックW100)を10重量%となるよ
うに加え(表1参照)、さらに結晶核剤として窒化ホウ
素を0.5%混合した後、スクリュー型2軸押出機を用
いてペレット化を行った。その際の樹脂温度は180℃
で行った。こうして得られたペレットを型締め圧力10
0ton/cm2 の射出成形機を用いて引張試験、曲げ
試験、衝撃試験、荷重たわみ温度測定用試験片の作製を
行った。その際、樹脂温度は185℃、金型温度は60
℃で行った。各種測定を行い、表1に上記試験結果を示
した。Examples 1-2 A bacterium, Protomonas e, deposited with the Institute of Biotechnology and Industrial Technology, National Institute of Advanced Industrial Science and Technology.
xtorquens) K (Accession number: FERM BP-354)
Using 8), continuous culture was performed aerobically using methanol as a carbon source. The culture conditions were a culture temperature of 32 ° C. and a culture pH of 6.
5. Continuous cultivation was performed so that the average residence time was 40 hours, and the nitrogen supply rate was the rate-determining rate of bacterial cell growth. According to recent literature, this bacterium is methylobacterium (Methylobac
terium) (IJBousfield and PNGr)
een; Int.J.Syst.Bacteriol., 35,209 (1985), T. Urakami
etal .; Int. J. Syst. Bcteriol., 43, 504-513 (1993)). The cells obtained by continuous culturing were subjected to the method described in JP-A-7-17789.
According to the method for separating and purifying poly-3-hydroxybutyric acid described in JP-A-4, after crushing with a high-pressure homogenizer, centrifugation was performed.
The separated poly-3-hydroxybutyric acid is first treated with a protease and then treated with hydrogen peroxide to obtain high-purity poly-3.
-Hydroxybutyric acid was obtained. Wood flour with a moisture content of 0.7% was added to this poly-3-hydroxybutyric acid (Shimada Shokai,
Cellulosine 100M) or cellulose powder (KC Floc W100 manufactured by Nippon Paper Industries) was added to 10% by weight (see Table 1), and 0.5% of boron nitride was further mixed as a crystal nucleating agent. Pelletization was performed using an extruder. The resin temperature at that time is 180 ° C
I went in. The pellets thus obtained are clamped at a mold clamping pressure of 10
Using a 0 ton / cm 2 injection molding machine, a tensile test, a bending test, an impact test, and a test piece for measuring a deflection temperature under load were performed. At that time, the resin temperature was 185 ° C and the mold temperature was 60.
C. was performed. Various measurements were made, and the test results are shown in Table 1.
【0018】比較例1 実施例1〜2と同手法により菌体から精製したポリ−3
−ヒドロキシ酪酸に窒化ホウ素0.5重量%加え、スク
リュー型2軸押出機を用いてペレット化を行った。その
際の樹脂温度は180℃であった。こうして得られたペ
レットを実施例1〜2と同手法で引張試験、曲げ試験、
衝撃試験、荷重たわみ温度測定用試験片の作製を行っ
た。その際、樹脂温度は185℃、金型温度は60℃で
行った。各種測定を行い、表1に上記試験結果を示し
た。Comparative Example 1 Poly-3 purified from cells by the same method as in Examples 1 and 2.
-0.5% by weight of boron nitride was added to -hydroxybutyric acid and pelletized using a screw type twin screw extruder. The resin temperature at that time was 180 ° C. The pellets thus obtained were subjected to a tensile test, a bending test, and the same method as in Examples 1 and 2.
An impact test and a test piece for measuring a deflection temperature under load were produced. At that time, the resin temperature was 185 ° C. and the mold temperature was 60 ° C. Various measurements were made, and the test results are shown in Table 1.
【0019】比較例2 実施例1〜2と同手法により菌体から精製したポリ−3
−ヒドロキシ酪酸に炭酸カルシュウム(日東粉化工業社
製、NS100)を30重量%となるように加え、さら
に結晶核剤として窒化ホウ素を0.5%混合した後、ス
クリュー型2軸押出機を用いてペレット化を行った。そ
の際の樹脂温度は180℃で行った。こうして得られた
ペレットを型締め圧力100ton/cm2 の射出成形
機を用いて引張試験、曲げ試験、衝撃試験、荷重たわみ
温度測定用試験片の作製を行った。その際、樹脂温度は
185℃、金型温度は60℃で行った。各種測定を行
い、表1に上記試験結果を示した。Comparative Example 2 Poly-3 purified from cells by the same method as in Examples 1 and 2.
After adding calcium carbonate (NS100, manufactured by Nitto Powder Chemical Co., Ltd.) to hydroxybutyric acid so as to be 30% by weight, and further mixing 0.5% of boron nitride as a crystal nucleating agent, using a screw type twin screw extruder. And pelletized. The resin temperature at that time was 180 ° C. The pellets thus obtained were subjected to a tensile test, a bending test, an impact test, and a test piece for measuring a deflection temperature under load using an injection molding machine having a mold clamping pressure of 100 ton / cm 2 . At that time, the resin temperature was 185 ° C. and the mold temperature was 60 ° C. Various measurements were made, and the test results are shown in Table 1.
【0020】[0020]
【表1】 表1 実施例 実施例 比較例 比較例 実施例(比較例) 1 2 1 2 配合材料 木粉 C.P * − CaCO3 配合量(重量部) 10 10 30 比重 1.27 1.27 1.25 1.48 引張性能 引張強度(kgf/cm2) 341 370 330 310 曲げ性能 曲げ強度(kgf/cm2) 554 579 552 530 曲げ弾性率(tonf/cm2) 39 41 36 44 衝撃強度 ノッチ付き(kgf・ cm/cm) 2.3 2.3 2.0 1.3 荷重たわみ温度(℃) 97 101 87 125 C.P: セルロースパウダー TABLE 1 Example Example Comparative Example Comparative Example Example Comparative Example 1 2 1 2 compounding materials wood flour CP * - CaCO 3 Amount (parts by weight) 10 10 30 density 1.27 1.27 1.25 1.48 Tensile Properties Tensile strength (kgf / cm 2) 341 370 330 310 bending properties flexural strength (kgf / cm 2) 554 579 552 530 flexural modulus (tonf / cm 2) 39 41 36 44 bar impact strength notched (kgf · cm / cm) 2.3 2.3 2.0 1.3 Deflection temperature under load (℃) 97 101 87 125 CP: Cellulose powder
フロントページの続き Fターム(参考) 4F071 AA09 AA44 AA73 AF14 AF52 AH12 AH17 BA01 BB05 BB06 BC07 4J002 AB01X AH00X CF03W GA00 GB01 GE00 GG00 GK00 GL00Continued on the front page F term (reference) 4F071 AA09 AA44 AA73 AF14 AF52 AH12 AH17 BA01 BB05 BB06 BC07 4J002 AB01X AH00X CF03W GA00 GB01 GE00 GG00 GK00 GL00
Claims (7)
ることを特徴とする生分解性成形材料。1. A biodegradable molding material comprising a biodegradable resin and a natural organic material.
酸単位を含む脂肪族ポリエステルである請求項1記載の
生分解性成形材料。2. The biodegradable molding material according to claim 1, wherein the biodegradable resin is an aliphatic polyester containing a poly-3-hydroxybutyric acid unit.
ースパウダーを1〜60重量%配合した請求項1記載の
生分解性成形材料。3. The biodegradable molding material according to claim 1, wherein 1 to 60% by weight of wood powder and / or cellulose powder is blended as a natural organic material.
分解性成形材料からなることを特徴とする生分解性成形
品。4. A biodegradable molded article comprising a biodegradable molding material obtained by blending a biodegradable resin with a natural organic material.
酸単位を含む脂肪族ポリエステルである請求項4記載の
生分解性成形品。5. The biodegradable molded article according to claim 4, wherein the biodegradable resin is an aliphatic polyester containing a poly-3-hydroxybutyric acid unit.
ースパウダーを1〜60重量%配合した生分解性成形材
料からなる請求項4記載の生分解性成形品。6. The biodegradable molded product according to claim 4, comprising a biodegradable molding material containing 1 to 60% by weight of wood powder and / or cellulose powder as a natural organic material.
肪族ポリエステルに水分含量が5重量%以下の木粉及び
/又はセルロースパウダーを1〜60重量%配合し、1
30〜250℃で成形することを特徴とする生分解性成
形品の製造方法。7. An aliphatic polyester containing poly-3-hydroxybutyric acid units is blended with 1 to 60% by weight of wood flour and / or cellulose powder having a water content of 5% by weight or less.
A method for producing a biodegradable molded article, comprising molding at 30 to 250 ° C.
Priority Applications (1)
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JP10304293A JP2000129143A (en) | 1998-10-26 | 1998-10-26 | Biodegradable molded product, its material and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10304293A JP2000129143A (en) | 1998-10-26 | 1998-10-26 | Biodegradable molded product, its material and its production |
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JP2000129143A true JP2000129143A (en) | 2000-05-09 |
Family
ID=17931298
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JP10304293A Pending JP2000129143A (en) | 1998-10-26 | 1998-10-26 | Biodegradable molded product, its material and its production |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003001987A (en) * | 2001-06-20 | 2003-01-08 | Toppan Printing Co Ltd | Card |
JP2005035134A (en) * | 2003-07-18 | 2005-02-10 | Toray Ind Inc | Manufacturing method of resin composition |
JP2005060556A (en) * | 2003-08-14 | 2005-03-10 | Unitika Ltd | Resin composition and molded product comprising the same |
JP2005179446A (en) * | 2003-12-17 | 2005-07-07 | Toray Ind Inc | Resin composition and molded product made of the same |
KR100512813B1 (en) * | 2001-04-27 | 2005-09-07 | 캐논 가부시끼가이샤 | Granular structure and process of production thereof |
JP2006045366A (en) * | 2004-08-05 | 2006-02-16 | Kaneka Corp | Poly(3-hydroxybutylate-co-3-hydroxyhexanoate) composition and its molding |
JP2009263414A (en) * | 2008-04-22 | 2009-11-12 | Kanai Educational Institution | Thermoformable material excellent in biodegradability, method for producing the same, and thermoformed article |
CN109627724A (en) * | 2018-12-24 | 2019-04-16 | 王剑英 | A kind of preparation method of culled wood/powdered rice hulls/PHA composite environmental-friendly hard plate material |
-
1998
- 1998-10-26 JP JP10304293A patent/JP2000129143A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100512813B1 (en) * | 2001-04-27 | 2005-09-07 | 캐논 가부시끼가이샤 | Granular structure and process of production thereof |
JP2003001987A (en) * | 2001-06-20 | 2003-01-08 | Toppan Printing Co Ltd | Card |
JP2005035134A (en) * | 2003-07-18 | 2005-02-10 | Toray Ind Inc | Manufacturing method of resin composition |
JP4572516B2 (en) * | 2003-07-18 | 2010-11-04 | 東レ株式会社 | Method for producing resin composition |
JP2005060556A (en) * | 2003-08-14 | 2005-03-10 | Unitika Ltd | Resin composition and molded product comprising the same |
JP4637466B2 (en) * | 2003-08-14 | 2011-02-23 | ユニチカ株式会社 | Resin composition and molded body comprising the same |
JP2005179446A (en) * | 2003-12-17 | 2005-07-07 | Toray Ind Inc | Resin composition and molded product made of the same |
JP2006045366A (en) * | 2004-08-05 | 2006-02-16 | Kaneka Corp | Poly(3-hydroxybutylate-co-3-hydroxyhexanoate) composition and its molding |
JP2009263414A (en) * | 2008-04-22 | 2009-11-12 | Kanai Educational Institution | Thermoformable material excellent in biodegradability, method for producing the same, and thermoformed article |
CN109627724A (en) * | 2018-12-24 | 2019-04-16 | 王剑英 | A kind of preparation method of culled wood/powdered rice hulls/PHA composite environmental-friendly hard plate material |
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