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JPH10219088A - Control of degradability of polylactic acid-based resin, degradable film/sheet and formed material from the film/sheet - Google Patents

Control of degradability of polylactic acid-based resin, degradable film/sheet and formed material from the film/sheet

Info

Publication number
JPH10219088A
JPH10219088A JP4286297A JP4286297A JPH10219088A JP H10219088 A JPH10219088 A JP H10219088A JP 4286297 A JP4286297 A JP 4286297A JP 4286297 A JP4286297 A JP 4286297A JP H10219088 A JPH10219088 A JP H10219088A
Authority
JP
Japan
Prior art keywords
sheet
polylactic acid
film
degradability
polymer
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.)
Granted
Application number
JP4286297A
Other languages
Japanese (ja)
Other versions
JP3490241B2 (en
Inventor
Shigenori Terada
滋憲 寺田
Jun Takagi
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
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 Plastics Inc filed Critical Mitsubishi Plastics Inc
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
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To obtain the subject polymer capable of effectively forming an initial degradation thereof e.g. a crack and as a result accelerating a hydrolysis by water so as to enhance the degradability of the polymer by blending a specific amount of an inorganic particles. SOLUTION: This method for controlling the degradability of a polylactic acid-based polymer is to blend (A) 100 pts.wt. polylactic acid-based polymer (e.g.; a polymer having 50,000-100,000 weight averaged molecular weight and containing >=94% lactic acid unit, with (B) 1-120 pt.wt. inorganic particles (e.g.; silica, titania, talc, alumina, a clay, calcium carbonate, magnesium carbonate and a glass powder, and having a large specific surface area) for enhancing the degradability of the component A. Further, the blending of the components A and B can be performed simultaneously with the formation, but it is more preferable to be performed by melt extruding the sufficiently dried components A and B by separate extruders for peletization before the formation.

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、ポリ乳酸系重合
体の分解性の制御方法および分解性フィルム・シートま
たは該フィルム・シートからなる成形品に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling the degradability of a polylactic acid-based polymer, and to a degradable film / sheet or a molded article comprising the film / sheet.

【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 been attracting attention because alcohols and carboxylic acids produced during decomposition are extremely low in toxicity, and have become commercially available. Typically, there are polycaprolactone, polyhydroxybutyrate, polyhydroxybutyrate / valerate copolymer, polyethylene succinate, polybutylene succinate and the like. However, these resins have a problem that the glass transition point is considerably low at -60C to 10C.

【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 the aliphatic polyesters, polylactic acid polymers have a high glass transition point, exhibit properties similar to polyethylene terephthalate, are crystalline, and are oriented by biaxial stretching. In addition, extrusion casting is possible and transparency is good, but biodegradability is very 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 a detailed study of the decomposition mechanism of polylactic acid-based polymer, the present inventors have found that polylactic acid-based polymer is firstly hydrolyzed by water and then biodegraded by microorganisms. Biodegradation by microorganisms is extremely slow at low temperatures, but is sufficiently fast at high temperatures.Hydrolysis by water causes initial disintegration of molded articles, for example, on the surface of a film or sheet. It has been found that it is promoted by the cracks that occur.
In addition, they have found that the blending of the inorganic particles is effective in causing this initial disintegration.

【0005】すなわち、本発明は、ポリ乳酸系重合体1
00重量部に、無機粒子を1〜120重量部配合し、ポ
リ乳酸系重合体の分解性を高めたことを特徴とする分解
性の制御方法および分解性フィルム・シートまたは該フ
ィルム・シートからなる成形品に存する。
That is, the present invention relates to a polylactic acid-based polymer 1
A method for controlling degradability and a degradable film or sheet comprising the polylactic acid-based polymer in an amount of from 1 to 120 parts by weight to increase the degradability of the polylactic acid-based polymer. Exists in molded products.

【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 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. Lactic acid is L-
Lactic acid, D-lactic acid, and other hydroxycarboxylic acids include glycolic acid, 3-hydroxybutyric acid, 4-hydroxybutyric acid, 3-hydroxyvaleric acid, 4-hydroxyvaleric acid, and 6-hydroxycaproic acid. Can be
Thus, in order to enhance the crystallinity of the polylactic acid-based polymer, the mixing ratio of L-lactic acid or D-lactic acid is preferably set to 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。
[0007] The weight average molecular weight of these polymers is preferably in the range of 50,000 to 100,000.
Below this range, problems such as practically no practical properties are exhibited. On the other hand, if it exceeds, the melt viscosity becomes too high and the moldability is poor. Further, in order to improve the thermal stability, it is preferable that the amount of the remaining monomer or the catalyst is small. For the production of such a polymer, any known method such as a condensation polymerization method and a 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 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, the polylactic acid-based polymer is mixed with inorganic particles. 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 it enhances the disintegration effect. In addition, the mixing ratio is 100% of the polylactic acid-based polymer.
1 to 120 parts by weight of inorganic particles, preferably 3 to 1 part by weight
When the amount of the inorganic particles is less than 1 part by weight, the decomposability cannot be enhanced, and when the amount is more than 120 parts by weight, the physical properties of the molded article, 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 compounding, 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 moldability and other physical properties of films and sheets It is also possible. Of course, auxiliary materials such as the above-mentioned polymer materials, additives, and modifiers can be added in advance to the polylactic acid-based polymer or the inorganic particles before blending.

【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。
In the present invention, the blending of the polylactic acid-based polymer with the inorganic particles and the addition of the above-mentioned auxiliary materials may be carried out simultaneously with the extrusion of the film / sheet described below.
Prior to film / sheet extrusion, it is preferred that the extruder is melt-extruded into a strand shape using another extruder and pelletized. In order to prevent the hydrolysis of the polylactic acid-based polymer at the melting temperature in the extruder, it is desirable that the raw materials are sufficiently dried 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, if it passes through a molten state, it may be pellet press-molded or calendered.

【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-mentioned pelletizing or film sheeting, any known form such as a single-screw, co-rotating twin-screw, and different-direction twin-screw extruder can be used. For pelletization, it is common to use a co-rotating 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-based 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。
In order to obtain a film, a flat or cylindrical material melt-extruded from a T-die, an I-die, a round die or the like is quenched by a cooling cast roll, water, pressurized air or the like. The film is uniaxially or biaxially stretched 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 material that is still in a molten state to reduce the thickness, can also be preferably 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 a film stretching and heat fixing technique disclosed in Japanese Patent Application Laid-Open No. 5-508819 and Japanese Patent Application Laid-Open No. 6-23836, transparency, mechanical strength, rigidity, and thermal dimensional stability can be improved. A polylactic acid-based film having excellent properties and the like can be obtained. The thickness of the film is determined in the range of 10 to 250 μm according to 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 a sheet is a method in which the sheet is extruded into a flat shape using a T-die and quenched by a metal cast roll equipped with a temperature control device. If necessary, the sheet is separated from the cast roll. By nipping with a metal roll, a polylactic acid-based sheet having extremely excellent transparency and smoothness can be obtained. The thickness of the sheet is generally determined in the range of 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 decomposable film / sheet obtained as described above and a molded product comprising the film / sheet. Examples of a method for obtaining a molded product from a film / 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-shaped package, for example, by folding a sheet with a folding ruled line. 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。
The present invention is not limited by the following examples. The measurement and evaluation shown in the examples were performed 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 Toyo Seiki Tensilon II type machine, JIS K712
7 was measured. Tensile speed during measurement is 10
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 Simplified compost test A commercially available domestic composter is compared with 10 kg of horticultural humus and 5 kg of commercially available dog food.
, And further mixed with 500 ml of water, and
The burial was 0 mm. The sample is 40m from the film
The sample was cut into mx 100 mm, inserted into a sample holder composed of two 60 mm x 150 mm wire meshes (3 mm mesh), and bound with a fine wire through the mesh. The sample was minimized from coming into contact with the outside and being disintegrated and scattered. The sample is one example or one
Six comparative samples were prepared and buried together with the sample holder so that the six posters were vertically parallel in the embedding of the composter. The lower bottom of each holder is 25mm from the bottom of the buried soil
And the upper base was placed at a depth of 25 mm from the surface of the embankment. One holder was removed every week after embedding, and the state of the surface of the sample was observed to confirm the presence or absence of collapse. The weight loss of the sample for the first week after embedding was examined and used as an index of the decomposition speed. From the weight loss, the reduction of the polylactic acid polymer itself was calculated by the following equation. Loss of polylactic acid polymer (mg) = Weight loss (mg)
X ratio Ratio = [number of polylactic acid polymer] / [number of polylactic acid polymer + number 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。
Submerged Immersion Degradation Test In-water immersion method in the field test of the Biodegradable Plastics Study Group (“Field Test of Biodegradable Plastics” Technical Committee Report of the Biodegradable Plastics Study Group Report 1 (September 1992) ), And the test was performed.
That is, a film sheet was cut out into a size of 120 mm × 30 mm, and was sandwiched between the central portions 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 meshes (40 mesh) are used to prevent the sheet from flowing out and have good contact with water. It was in a state. The appearance of the sample after immersion 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 about 98: 2, the glass transition point was 58 ° C., and the melting point was 175.
C., 100 parts by weight of polylactic acid pellets having a weight average molecular weight of 180,000 were 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 blended, respectively, and extruded in a strand shape at 220 ° C. with a 26 mmΦ biaxial kneading extruder to prepare two types of pellets. Each of the two types of titanium dioxide-containing pellets was extruded from a T-die at 210 ° C. with a 30 mmφ single-screw extruder, and rapidly cooled with 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 the tensile strength and the results of 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 the measured values and evaluation results.

【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 to 3 and Comparative Example 3]
In place of titanium dioxide, 10 parts by weight of fine powder silicon dioxide thyricia 310 (average particle size: 1.4 μm) manufactured by Fuji Silysia Chemical Ltd. (Example 2), 100 parts by weight
Except for using parts by weight (Example 3) and 150 parts by weight (Comparative Example 3), a thickness of about 0.4
mm transparent unstretched sheet was obtained. Table 1 shows the measured values and evaluation results.

【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 at 70 ° C. in the longitudinal direction, and then 75 ° C. in the width direction. Then, the sheet was stretched to 2.6 times with a, and the sheet was guided to 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 the measured values and evaluation results.

【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 was compared with Comparative Examples 1 and 2, and in Examples 2 and 3, Comparative Example 2 was used.
The weight loss in the initial stage is larger than that of, and the disintegration tends to start earlier. In Comparative Example 3, the decomposition was remarkable, but the tensile strength was significantly reduced as compared with Examples 2 and 3, and the practicality was inferior. Also, in the stretched heat-set film, the decomposition is faster in Example 4 in which the inorganic particles are blended than in Comparative Example 4 in which the inorganic particles are not blended.

【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 decomposition test. Table 2 shows the results.

【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 blending 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, the decomposability of the polylactic acid-based polymer can be increased while maintaining a practical strength by blending a specific amount of inorganic particles. Accordingly, the decomposable film / sheet of the present invention or a molded article comprising the film / sheet is used in applications where it is desired to decompose quickly in a natural environment, for example, a seedling pot or a cutting wood tape used in a one-year cycle, or It is suitable for a fishing tackle, a packaging material such as a bait or the like which is easily scattered in the environment by mistake.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】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、ポリ乳酸系重合体の分解
性を高めたことを特徴とする分解性の制御方法。
1. A method for controlling degradability, comprising adding 1 to 120 parts by weight of inorganic particles to 100 parts by weight of a polylactic acid-based polymer to enhance the decomposability of the polylactic acid-based polymer.
【請求項2】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、ポリ乳酸系重合体の分解
性を高めたことを特徴とする分解性フィルム・シートま
たは該フィルム・シートからなる成形品。
2. A decomposable film or sheet comprising 100 parts by weight of a polylactic acid-based polymer and 1 to 120 parts by weight of inorganic particles to enhance the decomposability of the polylactic acid-based polymer.・ Molded product consisting of sheet.
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 true JPH10219088A (en) 1998-08-18
JP3490241B2 JP3490241B2 (en) 2004-01-26

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ID=12647852

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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001059029A (en) * 1999-08-23 2001-03-06 Mitsubishi Plastics Ind Ltd Biaxially oriented aliphatic polyester-based film and its production
US6600008B1 (en) 1998-07-22 2003-07-29 Toyo Boseki Kabushiki Kaisha Aliphatic polyester film and gas barrier film
WO2008038350A1 (en) * 2006-09-27 2008-04-03 Fujitsu Limited Resin composition, pulverized matter and method of discarding resin composition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6600008B1 (en) 1998-07-22 2003-07-29 Toyo Boseki Kabushiki Kaisha Aliphatic polyester film and gas barrier film
US6649732B2 (en) 1998-07-22 2003-11-18 Toyo Boseki Kabushiki Kaisha 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
JP5200937B2 (en) * 2006-09-27 2013-06-05 富士通株式会社 Resin composition, pulverized product, and disposal method of resin composition

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