JP3490241B2 - Degradable films or sheets, molded articles made of these, and methods for decomposing them - Google Patents

Degradable films or sheets, molded articles made of these, and methods for decomposing them

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Publication number
JP3490241B2
JP3490241B2 JP04286297A JP4286297A JP3490241B2 JP 3490241 B2 JP3490241 B2 JP 3490241B2 JP 04286297 A JP04286297 A JP 04286297A JP 4286297 A JP4286297 A JP 4286297A JP 3490241 B2 JP3490241 B2 JP 3490241B2
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JP
Japan
Prior art keywords
sheet
film
weight
parts
lactic acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP04286297A
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Japanese (ja)
Other versions
JPH10219088A (en
Inventor
滋憲 寺田
潤 高木
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 Plastics Inc
Original Assignee
Mitsubishi Plastics Inc
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Priority to JP04286297A priority Critical patent/JP3490241B2/en
Publication of JPH10219088A publication Critical patent/JPH10219088A/en
Application granted granted Critical
Publication of JP3490241B2 publication Critical patent/JP3490241B2/en
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Expired - Lifetime legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Biological Depolymerization Polymers (AREA)

Description

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

【0001】[0001]

【発明の属する技術分野】 この発明は、L−乳酸もし
くはD−乳酸の混合比率が94%以上であるポリ乳酸系
重合体の未延伸の分解性フィルム・シート、または該フ
ィルム・シートからなる成形品、及びこれらフィルム・
シート或いは成形品の分解方法に関するものである。
TECHNICAL FIELD The present invention relates to an unstretched degradable film / sheet of a polylactic acid-based polymer having a mixing ratio of L-lactic acid or D- lactic acid of 94% or more, or a molding comprising the film / sheet. Products and these films
The present invention relates to a method for disassembling a sheet or a molded product .

【0002】[0002]

【従来の技術】生分解性樹脂の中では、脂肪族ポリエス
テルが、分解時に生成するアルコールおよびカルボン酸
が毒性がきわめて低い点で注目され、市販されるように
なってきた。代表的には、ポリカプロラクトン、ポリヒ
ドロキシブチレート、ポリヒドロキシブチレート・バリ
レート共重合体、ポリエチレンサクシネート、ポリブチ
レンサクシネートなどがある。しかし、これらの樹脂
は、ガラス転移点が−60℃〜10℃とかなり低いのが
問題点であった。
2. Description of the Related Art Among biodegradable resins, aliphatic polyesters have come to the market due to the fact that alcohols and carboxylic acids formed upon decomposition have extremely low toxicity. Typical examples include polycaprolactone, polyhydroxybutyrate, polyhydroxybutyrate-valerate copolymer, polyethylene succinate, and polybutylene succinate. However, these resins have a problem that the glass transition point is as low as −60 ° C. to 10 ° C.

【0003】[0003]

【発明が解決しようとする課題】一方、脂肪族ポリエス
テルの中でも、ポリ乳酸系重合体は、ガラス転移点も高
く、ポリエチレンテレフタレートと類似した性質を示
し、結晶性があり、二軸延伸により配向し、また押出キ
ャスト可能で、透明性も良好であるが、生分解性が非常
に悪いことが問題とされていた。
On the other hand, among aliphatic polyesters, polylactic acid-based polymers also have a high glass transition point, exhibit properties similar to those of polyethylene terephthalate, have crystallinity, and are oriented by biaxial stretching. Moreover, although it is extrudable and castable and has good transparency, it has been a problem that biodegradability is extremely poor.

【0004】[0004]

【課題を解決するための手段】本発明者は、ポリ乳酸系
重合体の分解機構について子細に検討した結果、ポリ乳
酸系重合体は、まず水によって加水分解を受け、しかる
後微生物によって生分解を受けるものであり、微生物に
よる生分解は、低温では極めて緩徐であるが、高温にす
ると十分に速いこと、また、水による加水分解は、成形
品の初期の崩壊、例えばフィルム・シートの表面に生じ
るひび(クラック)によって促進されることが解った。
しかも、無機粒子の配合が、この初期の崩壊を生じさせ
るのに有効であることを知見した。
Means for Solving the Problems As a result of detailed examination of the decomposition mechanism of the polylactic acid polymer, the present inventor found that the polylactic acid polymer is first hydrolyzed by water and then biodegraded by microorganisms. Biodegradation by microorganisms is extremely slow at low temperatures, but it is sufficiently fast at high temperatures, and hydrolysis by water causes initial disintegration of molded articles, such as on the surface of film sheets. It was found to be accelerated by the resulting cracks.
Moreover, it has been found that the compounding of inorganic particles is effective in causing this initial disintegration.

【0005】すなわち、本願発明は、L−乳酸もしくは
D−乳酸の混合比率が94%以上であるポリ乳酸重合体
100重量部に、無機粒子を1〜120重量部配合して
なる未延伸の分解性フィルム或いはシート、または当該
未延伸の分解性フィルム或いはシートから成形された成
形品、及びこれらフィルム・シート或いは成形品の分解
方法に存する。
That is, according to the present invention, 100 parts by weight of a polylactic acid polymer having a mixing ratio of L-lactic acid or D- lactic acid of 94% or more and 1 to 120 parts by weight of inorganic particles are blended to obtain an unstretched decomposed material. Film or sheet, or a molded product formed from the unstretched degradable film or sheet, and a method for disassembling the film, sheet or molded product .

【0006】[0006]

【発明の実施の形態】本発明に用いられるポリ乳酸系重
合体とは、乳酸の単独重合体(「ポリ乳酸」という。)
若しくは乳酸と他のヒドロキシカルボン酸との共重合
体、またはこれらの混合物である。乳酸としては、L−
乳酸、D−乳酸が挙げられ、他のヒドロキシカルボン酸
としては、グリコール酸、3−ヒドロキシ酪酸、4−ヒ
ドロキシ酪酸、3−ヒドロキシ吉草酸、4−ヒドロキシ
吉草酸、6−ヒドロキシカプロン酸などが挙げられる。
しかして、ポリ乳酸系重合体の結晶性を高めるために
は、L−乳酸もしくはD−乳酸の混合比率が94%以上
とするのがよい。
BEST MODE FOR CARRYING OUT THE INVENTION The polylactic acid-based polymer used in the present invention is a homopolymer of lactic acid (referred to as "polylactic acid").
Alternatively, it is a copolymer of lactic acid and another hydroxycarboxylic acid, or a mixture thereof. As lactic acid, L-
Lactic acid and D-lactic acid are mentioned, and other hydroxycarboxylic acids include glycolic acid, 3-hydroxybutyric acid, 4-hydroxybutyric acid, 3-hydroxyvaleric acid, 4-hydroxyvaleric acid, 6-hydroxycaproic acid and the like. To be
Therefore, in order to improve the crystallinity of the polylactic acid-based polymer, the mixing ratio of L-lactic acid or D-lactic acid is preferably 94% or more.

【0007】これらの重合体の重量平均分子量として
は、50,000〜100,000の範囲が好ましく、
かかる範囲を下まわると実用物性がほとんど発現されな
いなどの問題を生じる。また、上まわる場合には、溶融
粘度が高くなりすぎ成形加工性に劣る。また、熱安定性
を向上させるためには、残存モノマーや触媒が少ない方
が好ましい。かかる重合体の製造には、縮合重合法、開
環重合法など、公知のいずれの方法を採用することも可
能であり、分子量増大の目的で、少量の鎖延長剤、例え
ば、ジイソシアネート化合物、ジエポキシ化合物、酸無
水物、酸クロライドなどを使用してもよい。
The weight average molecular weight of these polymers is preferably in the range of 50,000 to 100,000,
If it falls below such a range, there arises a problem that practical physical properties are hardly exhibited. On the other hand, if it exceeds, the melt viscosity becomes too high and the moldability becomes poor. Further, in order to improve the thermal stability, it is preferable that the residual monomer and the catalyst are small. For the production of such a polymer, any known method such as condensation polymerization method and ring-opening polymerization method can be adopted. For the purpose of increasing the molecular weight, a small amount of a chain extender, for example, a diisocyanate compound, diepoxy is used. Compounds, acid anhydrides, acid chlorides and the like may be used.

【0008】本発明においては、かかるポリ乳酸系重合
体に無機粒子を配合する。用いられる無機粒子として
は、シリカ、チタニア、タルク、アルミナ、クレー、炭
酸カルシウム、炭酸マグネシウム、ガラス粉などの粒子
が挙げられる。粒子の大きさ、形状は特に制限はない
が、比表面積の大きい方が、崩壊の効果を高めるので好
ましい。また、配合の比率は、ポリ乳酸系重合体100
重量部に無機粒子1〜120重量部、好ましくは3〜1
00重量部であり、無機粒子の量が1重量部より少ない
と、分解性を高めることができず、また120重量部よ
り多いと成形品の物性、例えば引張強度が低下し実用性
を失う。
In the present invention, inorganic particles are blended with the polylactic acid polymer. Examples of the inorganic particles used include particles of silica, titania, talc, alumina, clay, calcium carbonate, magnesium carbonate, glass powder and the like. The size and shape of the particles are not particularly limited, but a larger specific surface area is preferable because the disintegration effect is enhanced. The blending ratio is 100% polylactic acid-based polymer.
1 to 120 parts by weight of inorganic particles, preferably 3 to 1 part by weight
If the amount of the inorganic particles is less than 1 part by weight, the decomposability cannot be improved, and if the amount is more than 120 parts by weight, the physical properties of the molded product, for example, the tensile strength, are reduced and the practicality is lost.

【0009】上記の配合に際し、本発明の効果を阻害し
ない範囲で、他の高分子材料を添加してもよい。また、
成形加工性、その他フィルムおよびシートの物性を調整
する目的で、可塑剤、滑剤、補強剤、紫外線吸収剤、光
安定剤、防かび剤、顔料、蛍光剤などの添加剤、改質剤
を添加することも可能である。もちろん、上記高分子材
料、添加剤、改質剤などの補助材料は、配合前のポリ乳
酸系重合体または無機粒子に、事前に添加することもで
きる。
In the above formulation, other polymer materials may be added as long as the effects of the present invention are not impaired. Also,
Additives and modifiers such as plasticizers, lubricants, reinforcing agents, UV absorbers, light stabilizers, fungicides, pigments, fluorescent agents, etc. for the purpose of adjusting molding processability and other physical properties of films and sheets. It is also possible to do so. Of course, the above-mentioned polymeric materials, additives, modifiers and other auxiliary materials can also be added in advance to the polylactic acid polymer or inorganic particles before compounding.

【0010】本発明におけるポリ乳酸系重合体と無機粒
子との配合および上記補助材料の添加は、後記のフィル
ム・シート押出時に、同時に行ってもよいが、通常は、
フィルム・シート押出に先立って、別の押出機を用いて
ストランド状に溶融押出して、ペレット化しておくのが
よい。しかして、押出機中でのポリ乳酸系重合体の溶融
温度下の加水分解を防止するため、あらかじめ原料を十
分に乾燥しておくことが望ましい。
The blending of the polylactic acid polymer and the inorganic particles and the addition of the above-mentioned auxiliary materials in the present invention may be carried out simultaneously at the time of film / sheet extrusion described later, but usually,
Prior to the film / sheet extrusion, it is preferable to melt-extrude in a strand form using another extruder and pelletize. Therefore, in order to prevent the hydrolysis of the polylactic acid polymer in the extruder at the melting temperature, it is desirable to sufficiently dry the raw materials in advance.

【0011】次いで、ペレット化されたポリ乳酸系重合
体は、通常、押出機を用い口金より溶融押し出され、フ
ィルムまたはシートに成形される。特殊なケースとして
は、溶融状態を経るならば、ペレットプレス成形やカレ
ンダー成形されてもよい。
Next, the pelletized polylactic acid-based polymer is usually melt-extruded from a die using an extruder and formed into a film or sheet. As a special case, pellet press molding or calender molding may be performed as long as it is in a molten state.

【0012】上記ペレット化またはフィルム・シート化
に用いられる押出機としては、単軸、同方向二軸、異方
向二軸押出機など、既知のあらゆる形態を使用すること
ができる。ペレット化には、混練効果の高い同方向二軸
押出機を用いるのが、一般的である。押出機の設定温度
は、ポリ乳酸系重合体の化学組成や分子量により適宜決
定されるが、170〜230℃の範囲が好ましい。すな
わち、170℃以下では、融点の高いポリ乳酸は溶融せ
ず、230℃以上では、熱分解が顕著になる。
As the extruder used for the above pelletization or film / sheet formation, any known form such as a single-screw, same-direction twin-screw, or different-direction twin-screw extruder can be used. For pelletizing, it is general to use a same-direction twin-screw extruder having a high kneading effect. The set temperature of the extruder is appropriately determined depending on the chemical composition and molecular weight of the polylactic acid polymer, but is preferably in the range of 170 to 230 ° C. That is, at 170 ° C or lower, polylactic acid having a high melting point does not melt, and at 230 ° C or higher, thermal decomposition becomes remarkable.

【0013】フィルムを得る場合には、Tダイ、Iダ
イ、丸ダイなどから溶融押出した平面状物または円筒状
物を、冷却キャスト・ロールや水、圧空などにより急冷
し、必要に応じ、引き続いてロール法、テンター法、チ
ューブラー法などにより、一軸または二軸に延伸する。
また、丸ダイから溶融押出しし、まだ溶融状態にある円
筒状物に空気を吹き込んで薄肉化する、いわゆるインフ
レーション法も望ましく採用することができる。
When a film is to be obtained, a flat product or a cylindrical product melt-extruded from a T-die, an I-die, a round die, etc. is rapidly cooled by a cooling cast roll, water, compressed air, etc. Uniaxially or biaxially by a roll method, a tenter method, a tubular method or the like.
Further, a so-called inflation method in which melt extrusion is performed from a round die and air is blown into a cylindrical object which is still in a molten state to reduce the thickness can be desirably used.

【0014】さらには、特表平5−508819号、特
開平6−23836号公報に開示されているようなフィ
ルムの延伸・熱固定技術を用いれば、透明性、機械強
度、剛性、熱寸法安定性などの卓越したポリ乳酸系フィ
ルムを得ることができる。フィルムの厚みは、用途に応
じ、10〜250μmの範囲で決められる。
Further, by using the film stretching / heat setting technique as disclosed in Japanese Patent Publication No. 5-508819 and Japanese Patent Laid-Open No. 6-23836, transparency, mechanical strength, rigidity and thermal dimensional stability can be obtained. It is possible to obtain a polylactic acid-based film having excellent properties. The thickness of the film is determined in the range of 10 to 250 μm depending on the application.

【0015】シートを得るのに最も好ましいのは、Tダ
イを用い平面状に押出して、温調装置を備えた金属キャ
スト・ロールにより急冷する方法であり、必要に応じシ
ートをキャスト・ロールと別の金属ロールでニップする
ことにより、透明性、平滑性が非常に優れたポリ乳酸系
シートを得ることができる。シートの厚みは、用途に応
じ、概ね250μm〜1mmの範囲で決められる。
The most preferable method for obtaining the sheet is a method of extruding the sheet in a plane using a T-die and quenching it with a metal cast roll equipped with a temperature control device, and separating the sheet from the cast roll if necessary. By nipping with the metal roll of No. 3, it is possible to obtain a polylactic acid-based sheet having excellent transparency and smoothness. The thickness of the sheet is determined in the range of approximately 250 μm to 1 mm depending on the application.

【0016】本発明は、上記のようにして得られた分解
性フィルム・シートおよび該フィルム・シートからなる
成形品をも対象とするものである。フィルム・シートか
ら成形品を得る方法としては、熱成形法である、真空成
形法、圧空成形法などが挙げられ、ブリスター加工品や
食品カップ、トレーなどに用いることができる。また、
シートに折り曲げ罫線を入れるなどして、箱型のパッケ
ージとして用いることもできる。さらに、紙や金属箔、
他のプラスチックフィルムとラミネートしたシートおよ
びその成形体にも用いられる。
The present invention is also directed to the degradable film sheet obtained as described above and a molded article made of the film sheet. Examples of the method for obtaining a molded article from a film or sheet include a thermoforming method such as a vacuum forming method and a pressure forming method, which can be used for blister processed products, food cups, trays and the like. Also,
It can also be used as a box-type package by putting a folding ruled line on the sheet. In addition, paper and metal foil,
It is also used for sheets laminated with other plastic films and molded products thereof.

【0017】[0017]

【実施例】以下に、実施例を示すが、これらにより本発
明はなんら制限を受けるものではない。なお、実施例中
に示す測定、評価は次に示すような条件で行った。
EXAMPLES Examples will be shown below, but the present invention is not limited thereto. The measurements and evaluations shown in the examples were carried out under the following conditions.

【0018】(1)引張強度 東洋精機テンシロンII型機を用い、JIS K712
7に基づいて、測定した。測定時の引っ張り速度は10
0mm/分とした。
(1) Tensile strength Using a Toyo Seiki Tensilon II type machine, JIS K712
It measured based on 7. Tensile speed during measurement is 10
It was set to 0 mm / min.

【0019】(2)分解性試験 簡易コンポスト試験 市販されている家庭用コンポスターに、園芸用の腐葉土
10kgに対し、市販されているドッグ・フード5kg
を混合して入れ、さらに水500mlを加え、厚み20
0mmの埋土とした。サンプルは、フィルムから40m
m×100mmに切り出し、60mm×150mmの金
網(3mm目)2枚で構成されるサンプルホルダーには
さみ込んだうえ、細い針金を網目に通してサンプルを綴
じ込んだ。サンプルが外部と接触し、かつ崩壊して散乱
することを極力抑えた。サンプルは、1実施例または1
比較例につき6枚用意し、コンポスターの埋土中に垂直
に6枚が並行するようにサンプルホルダーとともに埋設
した。各ホルダーの下底辺は、埋土の底面から25mm
の高さに、また上底辺は、埋土の表面から25mmの深
さに配置された。埋設後1週間ごとに1ホルダーづつ取
り出し、サンプルの表面の状態を観察して、崩壊の有無
を確認した。また、埋設後最初の1週間のサンプルにつ
いては、重量減少量を調べて、分解の速さの指標とし
た。なお、重量減少量から、ポリ乳酸重合体そのものの
減少量を、次の式によって算出した。 ポリ乳酸重合体の減少量(mg)=重量減少量(mg)
×比率 比率=[ポリ乳酸重合体の部数]/[ポリ乳酸重合体の
部数+無機粒子の部数]
(2) Degradability test Simple composting test In a commercially available household composter, 10 kg of horticultural leaf soil and 5 kg of commercially available dog food
And then add 500 ml of water to give a thickness of 20
The buried soil was 0 mm. Sample is 40m from the film
The sample was cut out into m × 100 mm, inserted into a sample holder composed of two 60 mm × 150 mm wire meshes (3 mm size), and a thin wire was passed through the mesh to bind the sample. The contact of the sample with the outside and the collapse and scattering of the sample were suppressed as much as possible. The sample is one embodiment or one
Six sheets were prepared for each of the comparative examples and were embedded together with the sample holder so that the six sheets were vertically aligned in the soil of the composter. The bottom of each holder is 25mm from the bottom of the soil
Was placed at a height of 25 mm and the upper base was at a depth of 25 mm from the surface of the soil. One holder was taken out every one week after embedding, and the state of the surface of the sample was observed to confirm the presence or absence of disintegration. In addition, for the sample for the first week after burying, the amount of weight loss was examined and used as an index of the decomposition rate. From the weight reduction amount, the reduction amount of the polylactic acid polymer itself was calculated by the following formula. Reduction amount of polylactic acid polymer (mg) = weight reduction amount (mg)
× Ratio Ratio = [parts of polylactic acid polymer] / [parts of polylactic acid polymer + parts of inorganic particles]

【0020】 水中浸漬分解性試験 生分解性プラスチック研究会のフィールド・テストにお
ける水中浸漬方法(「生分解性プラスチックのフィール
ドテスト」生分解プラスチック研究会技術委員会報告第
1報(1992年9月))に準じて、テストを行った。
すなわち、フィルム・シートを120mm×30mmに
切り出し、それをステンレス製サンプル・ホルダー3枚
の中央部に挟み込んだ。サンプル・ホルダーの中央部に
は、シート・サンプルと同形状の窓を開けておき、ステ
ンレス製金網(40メッシュ)2枚をかませて、シート
がそのまま流れ出さず、かつ水との接触が良好な状態に
した。淡水中に2年間浸漬後のサンプルの外観を観察し
た。
Immersion in water degradability test Immersion in water in field test of Biodegradable Plastics Study Group ("Field test of biodegradable plastics" Biodegradable Plastics Study Group Technical Committee Report 1st Report (September 1992) ), And the test was performed.
That is, a film sheet was cut out into 120 mm × 30 mm and sandwiched in the center of three stainless steel sample holders. A window with the same shape as the sheet sample is opened in the center of the sample holder, and two stainless steel wire nets (40 mesh) are chewed so that the sheet does not flow out as it is and good contact with water I was in a state. The appearance of the sample after immersing in fresh water for 2 years was observed.

【0021】[比較例1および実施例1]L−乳酸から
なる構造単位とD−乳酸からなる構造単位との割合がお
およそ98:2で、ガラス転移点58℃、融点175
℃、重量平均分子量18万のポリ乳酸ペレット100重
量部に対して、堺化学工業(株)社製アナターゼ型結晶
二酸化チタンA−170(平均粒径0.15μm)を、
それぞれ、0.5重量部(比較例1)および5重量部
(実施例1)配合し、26mmΦ二軸混練エクストルー
ダーでストランド形状に220℃で押し出し、2種類の
ペレットを作成した。この2種類の二酸化チタン配合ペ
レットを、それぞれ、30mmΦ単軸エクストルーダー
にて、210℃でTダイより押し出し、キャスティング
ロールにて急冷し、厚み約0.4mmの白色未延伸シー
トを得た。引張強度の測定および分解性試験(簡易コン
ポスト試験)の結果を、表1に示す。
Comparative Example 1 and Example 1 The ratio of the structural unit composed of L-lactic acid to the structural unit composed of D-lactic acid was approximately 98: 2, the glass transition point was 58 ° C., and the melting point was 175.
C., with respect to 100 parts by weight of polylactic acid pellets having a weight average molecular weight of 180,000, anatase type crystalline titanium dioxide A-170 (average particle size 0.15 μm) manufactured by Sakai Chemical Industry Co., Ltd.
0.5 parts by weight (Comparative Example 1) and 5 parts by weight (Example 1) were mixed, respectively, and extruded into a strand shape at 220 ° C. with a 26 mmΦ biaxial kneading extruder to prepare two types of pellets. The two types of pellets containing titanium dioxide were extruded from a T-die at 210 ° C. in a 30 mmΦ uniaxial extruder and rapidly cooled by a casting roll to obtain a white unstretched sheet having a thickness of about 0.4 mm. Table 1 shows the results of the measurement of tensile strength and the decomposability test (simple compost test).

【0022】[比較例2]実施例1において、二酸化チ
タンの配合を行わなかった外は、同実施例と全く同様に
して、厚み約0.4mmの透明未延伸シートを得た。各
測定値および評価の結果を、表1に示す。
[Comparative Example 2] A transparent unstretched sheet having a thickness of about 0.4 mm was obtained in the same manner as in Example 1 except that titanium dioxide was not added. Table 1 shows each measured value and the evaluation result.

【0023】[実施例2〜3および比較例3]実施例1
において、二酸化チタンの代わりに、富士シリシア化学
(株)社製の微粉末二酸化ケイ素サイリシア310(平
均粒径1.4μm)を10重量部(実施例2)、100
重量部(実施例3)および150重量部(比較例3)使
用した外は、同実施例と全く同様にして、厚み約0.4
mmの透明未延伸シートを得た。各測定値および評価の
結果を、表1に示す。
[Examples 2 and 3 and Comparative Example 3] Example 1
In place of titanium dioxide, 10 parts by weight of fine powder silicon dioxide Sylysia 310 (average particle size 1.4 μm) manufactured by Fuji Silysia Chemical Ltd. (average particle size 1.4 μm) (Example 2), 100
Except for the use of parts by weight (Example 3) and 150 parts by weight (Comparative Example 3), the thickness was about 0.4, in the same manner as in the same example.
A transparent unstretched sheet of mm was obtained. Table 1 shows each measured value and the evaluation result.

【0024】[実施例4および比較例4]実施例1およ
び比較例2において得られた未延伸シートを、直ちに長
手方向に70℃で2.3倍にロール延伸し、次いで幅方
向に75℃で2.6倍にテンター延伸し、さらに熱処理
ゾーンにシートを導いて、130℃で熱固定を20秒間
行った。得られた延伸シートの厚みは0.2mmであ
る。各測定値および評価の結果を、表1に示す。
[Example 4 and Comparative Example 4] The unstretched sheets obtained in Example 1 and Comparative Example 2 were immediately roll-stretched 2.3 times in the longitudinal direction at 70 ° C, and then in the width direction at 75 ° C. Was stretched 2.6 times by a tenter, the sheet was introduced into a heat treatment zone, and heat-set at 130 ° C. for 20 seconds. The thickness of the obtained stretched sheet is 0.2 mm. Table 1 shows each measured value and the evaluation result.

【0025】[0025]

【表1】 [Table 1]

【0026】表1に示す結果から、次のような事実が確
認された。未延伸フィルムにおいては、実施例1は、比
較例1〜2に比べて、また実施例2〜3では、比較例2
に比べて、初期の重量減少量が大きく、崩壊が始まるの
が早まる傾向にある。比較例3では分解は顕著である
が、実施例2〜3に比べて、引張強度の低下が著しく実
用性に劣る。また、延伸熱固定フィルムにおいても、無
機粒子を配合した実施例4では、無配合の比較例4より
も分解が早い。
From the results shown in Table 1, the following facts were confirmed. In the unstretched film, Example 1 is compared to Comparative Examples 1-2, and Examples 2-3 are Comparative Example 2
Compared with, the initial amount of weight loss is large, and there is a tendency for disintegration to begin earlier. In Comparative Example 3, the decomposition is remarkable, but in comparison with Examples 2 to 3, the tensile strength is significantly decreased and the practicality is poor. Further, also in the stretched heat-fixing film, in Example 4 in which the inorganic particles are blended, the decomposition is faster than in Comparative Example 4 in which no blending is performed.

【0027】[実施例5および比較例5]実施例1およ
び比較例2において得られた未延伸シートについて、水
中浸漬分解性試験を行った。その結果を、表2に示す。
[Example 5 and Comparative Example 5] The unstretched sheets obtained in Example 1 and Comparative Example 2 were subjected to a water immersion degradability test. The results are shown in Table 2.

【0028】[0028]

【表2】 [Table 2]

【0029】表2は、自然環境中においた場合でも、無
機粒子の配合により、分解が早まったことを示すもので
ある。
Table 2 shows that the decomposition was accelerated by the addition of the inorganic particles even in the natural environment.

【0030】[0030]

【発明の効果】本発明に従い、特定量の無機粒子を配合
することにより、実用的な強度を維持しながら、ポリ乳
酸系重合体の分解性を高めることができる。従って、本
発明の分解性フィルム・シートまたは該フィルム・シー
トからなる成形品は、自然環境中で分解が早いことが望
まれる用途、例えば1年サイクルで使用される育苗ポッ
トやつぎ木テープ、また誤って環境中に散乱しやすい釣
り具、エサ等の包装材などに好適である。
According to the present invention, by incorporating a specific amount of inorganic particles, the degradability of the polylactic acid polymer can be increased while maintaining practical strength. Therefore, the degradable film / sheet of the present invention or a molded article comprising the film / sheet is used in applications where rapid degradation is desired in a natural environment, such as seedling pots and spruce tapes used in a one-year cycle, and It is suitable for fishing tackles and packaging materials such as food that are accidentally scattered in the environment.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C08L 67/04 ─────────────────────────────────────────────────── ─── Continuation of front page (58) Fields surveyed (Int.Cl. 7 , DB name) C08L 67/04

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 L−乳酸もしくはD−乳酸の混合比率が
94%以上であるポリ乳酸重合体100重量部に、無機
粒子を1〜120重量部配合してなる未延伸の分解性フ
ィルム或いはシート。
1. An unstretched degradable film or sheet prepared by mixing 1 to 120 parts by weight of inorganic particles with 100 parts by weight of a polylactic acid polymer having a mixing ratio of L-lactic acid or D- lactic acid of 94% or more. .
【請求項2】 請求項1記載の未延伸の分解性フィルム
或いはシートから成形された成形品。
2. A molded product molded from the unstretched degradable film or sheet according to claim 1.
【請求項3】 L−乳酸もしくはD−乳酸の混合比率が
94%以上であるポリ乳酸系重合体100重量部に、無
機粒子を1〜120重量部配合した未延伸フィルム或い
はシートが加水分解により崩壊した後、さらに、微生物
により生分解を受ける未延伸フィルム或いはシートの分
解方法であって、前記加水分解による崩壊を、フィルム
或いはシート表面に無機粒子により生じるひび(クラッ
ク)により促進させた後、微生物による生分解へ移行す
ることを特徴とする分解性フィルム或いはシートの分解
方法。
3. An unstretched film or sheet prepared by mixing 1 to 120 parts by weight of inorganic particles with 100 parts by weight of a polylactic acid-based polymer having a mixing ratio of L-lactic acid or D-lactic acid of 94% or more is hydrolyzed. After disintegration, further, a method for decomposing an unstretched film or sheet that undergoes biodegradation by microorganisms, in which the disintegration by hydrolysis is promoted by cracks (cracks) generated on the surface of the film or sheet by inorganic particles, A method for decomposing a degradable film or sheet, which comprises shifting to biodegradation by microorganisms.
【請求項4】 L−乳酸もしくはD−乳酸の混合比率が
94%以上であるポリ乳酸系重合体100重量部に、無
機粒子を1〜120重量部配合した未延伸フィルム或い
はシートからなる成形品が加水分解により崩壊した後、
さらに、微生物により生分解を受ける未延伸フィルム或
いはシートからなる成形品の分解方法であって、前記加
水分解による崩壊が成形品表面に無機粒子により生じる
ひび(クラック)から始まった後に、微生物による生分
解へ移行することを特徴とする分解性フィルム或いはシ
ートからなる成形品の分解方法。
4. A molded article comprising an unstretched film or sheet in which 1 to 120 parts by weight of inorganic particles are mixed with 100 parts by weight of a polylactic acid-based polymer having a mixing ratio of L-lactic acid or D-lactic acid of 94% or more. After being disintegrated by hydrolysis,
Furthermore, a method for decomposing a molded article composed of an unstretched film or sheet that undergoes biodegradation by microorganisms, wherein the hydrolysis-induced disintegration begins with cracks caused by inorganic particles on the surface of the molded article , and A method for disassembling a molded article composed of a degradable film or sheet, characterized by shifting to disassembly.
JP04286297A 1997-02-13 1997-02-13 Degradable films or sheets, molded articles made of these, and methods for decomposing them Expired - Lifetime JP3490241B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04286297A JP3490241B2 (en) 1997-02-13 1997-02-13 Degradable films or sheets, molded articles made of these, and methods for decomposing them

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04286297A JP3490241B2 (en) 1997-02-13 1997-02-13 Degradable films or sheets, molded articles made of these, and methods for decomposing them

Publications (2)

Publication Number Publication Date
JPH10219088A JPH10219088A (en) 1998-08-18
JP3490241B2 true JP3490241B2 (en) 2004-01-26

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Country Link
JP (1) JP3490241B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2236548B1 (en) 1998-07-22 2013-01-16 Toyobo Co., Ltd. Aliphatic polyester film and gas barrier film
JP2001059029A (en) * 1999-08-23 2001-03-06 Mitsubishi Plastics Ind Ltd Biaxially oriented aliphatic polyester-based film and its production
WO2008038350A1 (en) * 2006-09-27 2008-04-03 Fujitsu Limited Resin composition, pulverized matter and method of discarding resin composition

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