JPH07308961A - Thermally molded processed product of polylactic acid polymer - Google Patents

Thermally molded processed product of polylactic acid polymer

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Publication number
JPH07308961A
JPH07308961A JP10130094A JP10130094A JPH07308961A JP H07308961 A JPH07308961 A JP H07308961A JP 10130094 A JP10130094 A JP 10130094A JP 10130094 A JP10130094 A JP 10130094A JP H07308961 A JPH07308961 A JP H07308961A
Authority
JP
Japan
Prior art keywords
sheet
polylactic acid
molded
product
molding
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
JP10130094A
Other languages
Japanese (ja)
Other versions
JP3563436B2 (en
Inventor
Jun Takagi
潤 高木
Shigenori Terada
滋憲 寺田
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.)
Shimadzu Corp
Mitsubishi Plastics Inc
Original Assignee
Shimadzu Corp
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 Shimadzu Corp, Mitsubishi Plastics Inc filed Critical Shimadzu Corp
Priority to JP10130094A priority Critical patent/JP3563436B2/en
Publication of JPH07308961A publication Critical patent/JPH07308961A/en
Application granted granted Critical
Publication of JP3563436B2 publication Critical patent/JP3563436B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To provide a thermally molded and processed product improved in fragility and good in transparency composed of a polylactic acid polymer being a degradable polymer. CONSTITUTION:A thermally molded and processed product of a polylactic acid polymer is obtained by molding a sheet with glass transition temp. of 35 deg. or higher composed of a polylactic acid polymer with a wt. average mol. wt. of 60,000 or more under such a condition that molding temp. is 50-90 deg.C and stretching area magnification is 2-20 times and characterized by that the average of the in-plane orientation degree AP of the molded and processed part of the molded product is 2X10<-3>-30X10<-3>.

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、ポリL−乳酸、ポリD
−乳酸またはこれらの共重合体などのポリ乳酸系重合体
からなる分解性のブリスター容器やPTP容器などの熱
成形加工品に関する。
FIELD OF THE INVENTION The present invention relates to poly-L-lactic acid and poly-D.
-A thermoformed product such as a degradable blister container or a PTP container made of polylactic acid-based polymer such as lactic acid or a copolymer thereof.

【0002】[0002]

【従来の技術とその課題】各種商品の展示包装用に広く
用いられているブリスター加工品は、樹脂製シートを作
っておき、次いでそのシートを真空成形、圧空成形など
の熱成形方法で成形して作られるのが一般的である。ブ
リスター加工品としては、包装体を通して中の商品を透
視できるように、透明なものが好まれる。このような点
から、実際に用いられるブリスター加工品用の素材シー
トとしては、ポリ塩化ビニル、ポリエチレンテレフタレ
ート、ポリスチレンなどのシートが多用されている。
2. Description of the Related Art Blister processed products, which are widely used for display and packaging of various products, are made by forming a resin sheet and then forming the sheet by a thermoforming method such as vacuum forming or pressure forming. It is generally made by. The blister processed product is preferably transparent so that the product inside can be seen through the package. From this point of view, sheets of polyvinyl chloride, polyethylene terephthalate, polystyrene and the like are often used as the material sheets for the blister processed products that are actually used.

【0003】また、医薬品の錠剤やカプセルなどの包装
に使用されるPTP(プレススルーパツク)包装用の容
器も、同様の熱成形方法で成形され、素材シートとして
は、透明性、成形性、水蒸気バリア性などの点から、ポ
リ塩化ビニル、ポリエチレンテレフタレート、ポリプロ
ピレンなどのシートが多用されている。
Further, a container for PTP (press through pack) packaging used for packaging tablets, capsules and the like of pharmaceuticals is also formed by the same thermoforming method, and as a material sheet, transparency, formability and steam are used. From the viewpoint of barrier properties, sheets of polyvinyl chloride, polyethylene terephthalate, polypropylene, etc. are often used.

【0004】しかしながら、これらの材料は化学的、生
物的に安定なため自然環境下に放置されてもほとんど分
解されることなく残留、蓄積される。これらは自然環境
中に散乱して動植物の生活環境を汚染するだけでなく、
ゴミとして埋め立てられた場合にもほとんど分解せずに
残り、埋め立て地の寿命を短くするという問題がある。
However, since these materials are chemically and biologically stable, they remain and accumulate with almost no decomposition even when left in a natural environment. These not only scatter in the natural environment and pollute the living environment of plants and animals,
Even if it is landfilled, it remains without being decomposed and shortens the life of the landfill.

【0005】[0005]

【課題を解決するための手段】本発明は、廃棄処理や環
境汚染の問題がなく、かつ強靭で透明性がよく、さらに
は経時的な形状安定性に優れた熱成形加工品を提供する
ものであって、その要旨は、重量平均分子量が60,0
00以上であるポリ乳酸系重合体からなりガラス転移温
度が35℃以上であるシートを、成形温度50〜90
℃、延伸面積倍率2〜20倍の範囲で成形してなり、該
成形品の成形加工部分の面内配向度ΔPの平均が2×1
-3〜30×10-3の範囲内にあることを特徴とするポ
リ乳酸系重合体の熱成形加工品にある。
DISCLOSURE OF THE INVENTION The present invention provides a thermoformed product which has no problems of disposal and environmental pollution, is tough and has good transparency, and is excellent in shape stability over time. However, the gist is that the weight average molecular weight is 60,0.
A sheet made of a polylactic acid-based polymer having a temperature of 00 or higher and having a glass transition temperature of 35 ° C. or higher is molded at a molding temperature of 50 to 90
Molded in the range of 2 ° C. and a draw area ratio of 2 to 20, and the average in-plane orientation degree ΔP of the molded portion of the molded product is 2 × 1.
It is a thermoformed product of a polylactic acid polymer characterized by being in the range of 0 −3 to 30 × 10 −3 .

【0006】ポリ乳酸は、土壌中において自然に加水分
解が進行し、土中に原形が残らず、ついで微生物により
無害な分解物となる、いわゆる生分解性を有することが
知られている。しかしポリ乳酸系重合体は脆さを有して
おり、シート状などの形態ではそのままでは使用し難い
が、本発明においては熱成形により成形加工部分に分子
配向を付与するとともに、未成形部分には紙などの支持
体が当接されることになるので、全体として流通や保管
に耐える強靭な熱成形加工品が得られるものである。
[0006] It is known that polylactic acid has a so-called biodegradability in which hydrolysis is naturally carried out in the soil, the original form is not left in the soil, and then the product is harmlessly decomposed by microorganisms. However, the polylactic acid-based polymer has brittleness, and it is difficult to use it as it is in the form of a sheet, but in the present invention, the molecular orientation is imparted to the molding processed portion by thermoforming, and the unmolded portion is formed. Since a support such as paper comes into contact with the product, a tough thermoformed product that can withstand distribution and storage as a whole can be obtained.

【0007】以下、本発明を詳しく説明する。本発明に
用いられるポリ乳酸系重合体とは、ポリ乳酸または乳酸
と他のヒドロキシカルボン酸との共重合体、もしくはこ
れらの混合物であり、本発明の効果を阻害しない範囲で
他の高分子材料が混入されても構わない。また、成形加
工性、シートや加工品の物性を調整する目的で、可塑
剤、滑剤、無機フイラー、紫外線吸収剤などの添加剤、
改質剤を添加することも可能である。
The present invention will be described in detail below. The polylactic acid-based polymer used in the present invention is polylactic acid or a copolymer of lactic acid and another hydroxycarboxylic acid, or a mixture thereof, and other polymer materials within a range that does not impair the effects of the present invention. May be mixed. In addition, additives such as plasticizers, lubricants, inorganic fillers, and ultraviolet absorbers for the purpose of adjusting molding processability and physical properties of sheets and processed products,
It is also possible to add modifiers.

【0008】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代表的に挙げられる。
Lactic acid includes L-lactic acid and D-lactic acid, and other hydroxycarboxylic acids include glycolic acid, 3-hydroxybutyric acid, 4-hydroxybutyric acid, 3-hydroxyvaleric acid and 4-hydroxyvaleric acid. Typical examples include 6-hydroxycaproic acid and the like.

【0009】これらの重合法としては、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、さらには、分子量増大を目的として少量の鎖
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、酸無水物などを使用しても構わない。重合体の
重量平均分子量としては、60,000から1000,
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ず、また熱成形時にシートが強
度を保持でき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。
As these polymerization methods, any known method such as condensation polymerization method and ring-opening polymerization method can be adopted. Furthermore, a small amount of a chain extender for the purpose of increasing the molecular weight, for example, You may use a diisocyanate compound, a diepoxy compound, an acid anhydride. The weight average molecular weight of the polymer is 60,000 to 1,000,
The range of 000 is preferable, and if it is less than the range, practical physical properties are hardly expressed, and the sheet cannot retain strength during thermoforming. On the other hand, if it exceeds, the melt viscosity becomes too high and the moldability becomes poor.

【0010】本発明熱成形加工品の素材シートは、これ
らの重合体を十分に乾燥して水分を除去した後、押出
法、カレンダー法、プレス法などの一般的な溶融成形法
によりシート状に成形し、次いで、急冷することにより
得られる。実用的には、シート状に溶融押出成形された
重合体を、回転するキヤステイングドラム(冷却ドラ
ム)に接触させて急冷するのが好ましい。キヤステイン
グドラムの温度は50℃以下が適当であり、これより高
いと重合体がキヤステイングドラムに粘着して引取りが
困難になり、また結晶化が促進されて球晶が発達し透明
性が低下するとともに熱成形加工も困難になる。従っ
て、上記温度範囲でシートを急冷して、実質上非晶質の
シートとするのが好ましい。
The raw material sheet of the thermoformed product of the present invention is formed into a sheet by a general melt-forming method such as an extrusion method, a calendering method and a pressing method after sufficiently drying these polymers to remove water. It is obtained by molding and then quenching. Practically, it is preferable to bring the polymer melt-extruded into a sheet into contact with a rotating casting drum (cooling drum) to quench it. It is suitable that the temperature of the casting drum is 50 ° C. or lower. If the temperature is higher than 50 ° C., the polymer adheres to the casting drum and it becomes difficult to take it off. Further, crystallization is promoted and spherulites develop to make transparency. As the temperature decreases, thermoforming becomes difficult. Therefore, it is preferable to rapidly cool the sheet within the above temperature range to obtain a substantially amorphous sheet.

【0011】また得られたシートのガラス転移温度は3
5℃以上、特に好ましくは40℃以上であることが、本
発明においては重要である。ガラス転移温度が35℃未
満であると、熱成形加工品に成形した後、室温で経時的
に寸法変化しやすく、好ましくない。また室温に放置中
にシートや加工品に球晶が成長し、シートにおいては成
形困難になったり、加工品では脆化や透明性低下などの
問題が生じる。ガラス転移温度は、ポリ乳酸系重合体の
組成、分子量、含有オリゴマ量、可塑剤などの添加剤の
種類と量などに主に依存する。
The glass transition temperature of the obtained sheet is 3
It is important in the present invention that the temperature is 5 ° C or higher, particularly preferably 40 ° C or higher. When the glass transition temperature is lower than 35 ° C., it is not preferable because the dimension tends to change with time at room temperature after molding into a thermoformed product. Further, spherulites grow on the sheet or the processed product while it is left at room temperature, which makes it difficult to form the sheet, and the processed product causes problems such as brittleness and reduced transparency. The glass transition temperature mainly depends on the composition of the polylactic acid-based polymer, the molecular weight, the content of oligomers, and the kind and amount of additives such as a plasticizer.

【0012】次に熱成形について説明する。上記のよう
にして得られたシートを、赤外線ヒータ、熱板ヒータ、
熱風などにより成形温度に予熱し熱成形する。熱成形の
方法としては、真空成形法、プラグアシスト成形法、圧
空成形法、雄雌型成形法、成形雄型に沿ってシートを変
形した後成形雄型を拡張する方法などがある。シートの
厚さは特に限定されず、通常の熱成形技術に使用できる
程度の厚さであればよい。具体的にはおよそ30〜10
00μmの範囲を包含する。
Next, thermoforming will be described. The sheet obtained as described above, infrared heater, hot plate heater,
It is preheated to the molding temperature with hot air and then thermoformed. As the thermoforming method, there are a vacuum forming method, a plug assist forming method, a pressure forming method, a male / female forming method, a method of deforming a sheet along the forming male die, and then expanding the forming male die. The thickness of the sheet is not particularly limited as long as it can be used in a usual thermoforming technique. Specifically, about 30 to 10
The range of 00 μm is included.

【0013】熱成形加工品は、熱成形加工を施した凸部
と、シートがそのまま残る平面部とからなる。平面部は
熱成形時に延伸されないので物性の改良は見られず強度
に劣るが、通常紙などを貼り合わせるなどして支持され
る。一方、凸部はその形態上強度が要求され脆さを改良
する必要がある。本発明においては、凸部の分子配向を
増大させることにより、強度を向上させ、脆さを改良す
ることができる。分子配向度をあらわす尺度として面内
配向度ΔPがある。
The thermoformed product comprises a thermoformed convex portion and a flat portion on which the sheet remains. Since the flat portion is not stretched during thermoforming, physical properties are not improved and the strength is poor, but it is usually supported by pasting paper or the like. On the other hand, the convex portion is required to have high strength because of its morphology, and it is necessary to improve brittleness. In the present invention, the strength and the brittleness can be improved by increasing the molecular orientation of the protrusions. The degree of in-plane orientation ΔP is a measure of the degree of molecular orientation.

【0014】面内配向度ΔPは、成形加工部分壁の厚み
方向に対する面方向の配向度を表わし、通常直交3軸方
向の屈折率を測定し以下の式で算出される。 ΔP={(γ+β)/2} − α (α<β<γ) ここで、γ、βがシート面(壁面)に平行な直交2軸の
屈折率、αはシート厚さ方向の屈折率である。
The in-plane orientation degree ΔP represents the orientation degree in the surface direction with respect to the thickness direction of the wall of the molded part, and is usually calculated by the following formula by measuring the refractive index in the directions of three orthogonal axes. ΔP = {(γ + β) / 2} −α (α <β <γ) where γ and β are biaxial refractive indices orthogonal to the sheet surface (wall surface), and α is a refractive index in the sheet thickness direction. is there.

【0015】ΔPは、結晶化度や結晶配向にも依存する
が、大きくは面内の分子配向に依存する。つまり面内に
対し分子配向を増大させることにより、無配向シートで
は1.0×10-3未満であるΔPを本発明で規定する2
×10-3以上、好適には3×10-3以上に増大させるこ
とができる。ただし30×10-3を越えるΔPを得よう
とすると、安定した成形ができず、シートの破断が多発
する。
ΔP depends on the crystallinity and the crystal orientation, but largely depends on the in-plane molecular orientation. That is, by increasing the molecular orientation with respect to the in-plane, ΔP which is less than 1.0 × 10 −3 in the non-oriented sheet is defined in the present invention. 2
It can be increased to × 10 -3 or more, preferably 3 × 10 -3 or more. However, if ΔP exceeding 30 × 10 −3 is attempted, stable molding cannot be performed and the sheet frequently breaks.

【0016】また、ブリスター加工品などの熱成形加工
品はその用途上透明であることが重要であり、熱成形時
に白化するのを避けなければならない。透明性はヘーズ
であらわすことができ、本発明では20%以下、好適に
は10%以下のヘーズを有する熱成形加工品を得ること
ができる。
Further, it is important that the thermoformed products such as the blister processed products are transparent for their use, and it is necessary to avoid whitening during the thermoforming. The transparency can be represented by haze, and in the present invention, a thermoformed product having a haze of 20% or less, preferably 10% or less can be obtained.

【0017】上記範囲のΔPおよびヘーズを有する加工
品を得るための熱成形は、成形温度50〜90℃の範囲
内で、成形加工部分の延伸面積倍率が2〜20倍、好ま
しくは4〜15倍の範囲となるように行なう。成形温度
(即ち延伸温度)が50℃未満ではシートの軟化が不足
して熱成形できずに破断したり、金型への密着が不足し
たりする。また90℃よりも高いと、ΔPが小さく強度
が改良されないばかりか、シートが加熱によりドローダ
ウンして成形が困難になったり、結晶化白化して透明性
を失う場合がある。
Thermoforming to obtain a processed product having a ΔP and haze in the above range is within a molding temperature range of 50 to 90 ° C., and a stretched area ratio of the molded part is 2 to 20 times, preferably 4 to 15 times. Do so that the range is doubled. If the molding temperature (that is, the stretching temperature) is less than 50 ° C., the softening of the sheet is insufficient, the sheet cannot be thermoformed, and the sheet is broken, or the adhesion to the mold is insufficient. On the other hand, when the temperature is higher than 90 ° C., ΔP is small and the strength is not improved, and the sheet may draw down due to heating to make molding difficult, or crystallization may be whitened to lose transparency.

【0018】また、成形加工部分の延伸面積倍率が2倍
よりも小さいと、ΔPは2×10-3に達せず物性の改良
はみられない。一方、20倍を越える延伸面積倍率では
成形体に破断が生じ、安定して成形品を得ることができ
ない。
If the stretched area ratio of the molded portion is less than 2 times, ΔP does not reach 2 × 10 -3 and no improvement in physical properties is observed. On the other hand, if the stretched area ratio exceeds 20 times, the molded product is broken, and a molded product cannot be stably obtained.

【0019】本発明熱成形加工品は、その成形加工部分
の強度・透明性、水蒸気バリア性などを生かして、ブリ
スター包装や、PTP容器などの、内容物透視性が必要
で使用時に紙などの支持体に当接して使用されるものと
して好適である。例えば商品の包装、展示に用いるブリ
スター包装体の場合、凸状の成形加工部分に商品を収納
してその開口部に成形加工部分からその周囲の未加工部
にかけて台紙を取り付けるのが通例である。台紙として
は、厚紙のほかに金属箔、各種プラチツクシートなどが
適用可能であるが、ブリスター加工品を台紙とともに廃
棄する場合を想定すると、台紙としては生分解性を有す
る紙製のものが好適である。台紙は、ブリスター加工品
と熱融着したり、接着剤、好適には未加硫天然ゴム系、
カゼインなどのタンパク質系、でんぷん、にかわなどの
生分解性を有する接着剤により密着接合される。また、
未成形部分(いわゆるフランジ)の両側縁を裏面側に1
80゜折り曲げ、その溝内に別の台紙をスライド可能に
取り付けてもよい。
The thermoformed product of the present invention requires the transparency of contents such as blister packaging and PTP containers by utilizing the strength / transparency of the processed part, the water vapor barrier property, etc. It is suitable for being used in contact with a support. For example, in the case of a blister package used for product packaging and display, it is customary to store the product in a convex shaped processed portion and attach a mount to the opening from the molded processed portion to the surrounding unprocessed portion. As the mount, in addition to cardboard, metal foil, various plastic sheets, etc. can be applied, but assuming that the blister processed product is discarded together with the mount, a biodegradable paper is suitable as the mount. Is. The mount is heat-sealed with a blister processed product, or an adhesive, preferably unvulcanized natural rubber,
It is closely joined by a protein system such as casein and a biodegradable adhesive such as starch and glue. Also,
1 on both sides of the unformed part (so-called flange) on the back side
It may be bent at 80 ° and another mount may be slidably mounted in the groove.

【0020】またPTP容器は、通常アルミニウム箔の
蓋材で密封される。アルミニウムは、環境を汚染せず自
然還元性であるため、ポリ乳酸系重合体シートと接着さ
れた状態でも廃棄することができる。以下に実施例を示
すが、これらにより本発明は何ら制限を受けるものでは
ない。 なお、実施例中に示す測定値は次に示すような
条件で測定を行い、算出した。
The PTP container is usually sealed with an aluminum foil lid member. Since aluminum does not pollute the environment and is naturally reducible, it can be discarded even when it is bonded to the polylactic acid-based polymer sheet. Examples will be shown below, but the present invention is not limited thereto. The measured values shown in the examples were measured and calculated under the following conditions.

【0021】(1)ΔPの平均値 成形加工部分の延伸面積倍率に相当する部分、即ち、原
シートの厚さを延伸面積倍率で割った値に相当する厚さ
を有する部分数箇所からシート状の試料を切りだし、ア
ツベ屈折計によって直交3軸方向の屈折率(α,β,
γ)を測定し、次式で算出した。
(1) Average value of ΔP Sheet-shaped from a portion corresponding to the stretched area ratio of the molded portion, that is, a portion having a thickness corresponding to a value obtained by dividing the thickness of the original sheet by the stretched area ratio. The sample of is cut out and the refractive index (α, β,
γ) was measured and calculated by the following formula.

【0022】 ΔP={(γ+β)/2} − α (α<β<γ) γ:試料面内の最大屈折率 β:それに直交する試料面内方向の屈折率 α:試料厚さ方向の屈折率ΔP = {(γ + β) / 2} −α (α <β <γ) γ: Maximum refractive index in the sample surface β: Refractive index in the sample in-plane direction orthogonal thereto α: Refraction in the sample thickness direction rate

【0023】(2)延伸面積倍率 成形後の成形加工部の表面積を、延伸加工を施した原シ
ートの面積で割って、延伸面積倍率とした。 (3)ヘーズ JIS−K7105に基づいて測定した。 (4)成形性 熱成形時の延伸性が良好なものを○、延伸はできるが延
伸ムラが生じるものを△、延伸時に破断するものを×で
あらわす。
(2) Stretching Area Magnification The surface area of the molded portion after molding was divided by the area of the stretched original sheet to obtain the stretching area ratio. (3) Haze It was measured based on JIS-K7105. (4) Moldability Good stretchability during thermoforming is indicated by ◯, stretchable but uneven stretching is indicated by Δ, and breakage during stretching is indicated by x.

【0024】(5)外観 成形後、外観の良好なものを○、粒状の白化部分がごく
わずかに見られるものを△、流れ状のムラやすじ状の白
化部分をもつものを×であらわす。 (6)脆さ 触感にて判断し、脆さが感じられないものを○、やや脆
いものを△、脆いものを×であらわす。 (7)総合評価 上記評価項目(4)、(5)、(6)を総合的に判断
し、良好なものを○、やや劣るものを△、劣るものを×
とした。 (8)ガラス転移温度 パーキンエルマー製DSC−7を用い、JIS−K71
21に基づいて測定した。
(5) Appearance After molding, a product having a good appearance is represented by ◯, a product having a slight amount of granular whitening parts is represented by Δ, and a product having flow-like unevenness or streak-like whitening parts is represented by x. (6) Brittleness Judgment by touch is indicated by ○ when brittleness is not felt, Δ when slightly brittle, and X when brittle. (7) Comprehensive evaluation Comprehensively judging the above-mentioned evaluation items (4), (5), and (6), good ones are ○, slightly inferior ones, and inferior ones ×.
And (8) Glass transition temperature Using DSC-7 manufactured by Perkin Elmer, JIS-K71
21 was measured.

【0025】[0025]

【実施例】【Example】

(実施例1)重量平均分子量約200,000のポリL
−乳酸を180℃でTダイより溶融押出し、35℃に保
持したキヤステイングドラム上で急冷し、厚さ500μ
mの未延伸シートを得た。ガラス転移温度は50℃であ
る。
(Example 1) Poly L having a weight average molecular weight of about 200,000
-Lactic acid is melt extruded from a T-die at 180 ° C and rapidly cooled on a casting drum kept at 35 ° C to give a thickness of 500μ.
An unstretched sheet of m was obtained. The glass transition temperature is 50 ° C.

【0026】得られたシートを熱成形機(三和興業社製
PLAVAC−FE36PH型)にクランプし、赤外線
ヒータで成形温度に予熱した後、プラグにより金型内に
押し込んで予備成形を行ない、次いで金型内を真空にし
てカツプ状に成形した。成形温度および延伸面積倍率を
変化させて表1に示すサンプルを得た。延伸面積倍率
は、プラグおよび金型を種々取替えることにより変更し
た。
The obtained sheet was clamped in a thermoforming machine (PLAVAC-FE36PH type manufactured by Sanwa Kogyo Co., Ltd.), preheated to the forming temperature by an infrared heater, and then pushed into the mold by a plug to carry out preforming, and then. The inside of the mold was evacuated to form a cup. The samples shown in Table 1 were obtained by changing the molding temperature and the stretching area ratio. The stretched area ratio was changed by changing various plugs and molds.

【0027】[0027]

【表1】 [Table 1]

【0028】表1の結果から、No.3および6は本発
明の成形条件の範囲内にあり、脆さが改良され、透明性
に優れた成形品が得られた。No.5はやや脆く、N
o.8は透明性が低下し若干欠点を有するが、成形性に
優れ実用範囲内と判断される。一方、No.2は成形温
度が低く良好な成形ができず、No.4は延伸倍率が低
くΔPが上がらず脆さが改良されなかった。No.7は
延伸倍率が高すぎて安定した成形ができない。No.9
〜10は、成形温度が高すぎ、成形性も悪く、脆さ、透
明性とも問題があった。
From the results in Table 1, No. Nos. 3 and 6 were within the range of the molding conditions of the present invention, brittleness was improved, and molded articles having excellent transparency were obtained. No. 5 is slightly brittle, N
o. No. 8 has a low transparency and some defects, but is excellent in moldability and judged to be in a practical range. On the other hand, No. No. 2 had a low molding temperature and could not be molded satisfactorily. In No. 4, the draw ratio was low and ΔP did not increase, and the brittleness was not improved. No. No. 7 has a too high draw ratio and cannot be stably molded. No. 9
In Nos. 10 to 10, the molding temperature was too high, the moldability was poor, and there were problems in brittleness and transparency.

【0029】(実施例2)実施例1、No.5のカツプ
状成形品の側面から、縦・横30mm×30mmのシー
ト状試料を、また底面からも30mm×30mmのシー
ト状試料を切り出し、30℃の恒温槽中に1ケ月置いて
その寸法を計り、元の寸法に対する収縮率を算出したと
ころ、成形加工部側面においては縦方向2.5%、横方
向2.0%、底面においては1.6%×1.8%であ
り、経時的な寸法変化が小さく元の寸法を保持している
ことが確認された。
(Embodiment 2) Embodiment 1, No. 1 From the side surface of the cup-shaped molded product of No. 5, a 30 mm x 30 mm sheet-shaped sample is cut out from the side and from the bottom side, a 30 mm x 30 mm sheet-shaped sample is cut out and placed in a constant temperature bath at 30 ° C for 1 month to measure its dimensions. When measured and calculated the shrinkage ratio with respect to the original dimension, it was 2.5% in the longitudinal direction on the side surface of the molded part, 2.0% in the lateral direction, and 1.6% x 1.8% on the bottom surface, which was It was confirmed that the dimensional change was small and the original size was maintained.

【0030】(比較例1)L−乳酸85重量%とカプロ
ラクトン15重量%とからなり、平均分子量約200,
000のポリ乳酸共重合体を、170℃でTダイより溶
融押出し、25℃に保持したキヤステイングドラム上で
急冷し、未延伸シートを得た。ガラス転移温度は33℃
であった。
COMPARATIVE EXAMPLE 1 L-lactic acid (85% by weight) and caprolactone (15% by weight) were used, and the average molecular weight was about 200.
000 polylactic acid copolymer was melt extruded from a T-die at 170 ° C. and rapidly cooled on a casting drum kept at 25 ° C. to obtain an unstretched sheet. Glass transition temperature is 33 ° C
Met.

【0031】得られたシートを実施例1のNo.5と同
様の条件でカツプ状に熱成形し、実施例2と同様にして
収縮率を測定したところ、成形加工部側面においては縦
方向26%、横方向22%、底面においては19%×2
1%であり、経時的な寸法変化が大きく成形加工部分が
大きく収縮していた。
The obtained sheet was No. 1 in Example 1. When heat-molded into a cup shape under the same conditions as in Example 5, and the shrinkage ratio was measured in the same manner as in Example 2, the side surface of the molded portion was 26% in the vertical direction, 22% in the horizontal direction, and 19% in the bottom surface.
It was 1%, and the dimensional change with time was large, and the molding portion was greatly shrunk.

【0032】(比較例2)重量平均分子量約50,00
0のポリL−乳酸を180℃でTダイより溶融押出し、
35℃に保持したキヤステイングドラム上で急冷し、厚
さ500μmの未延伸シートを得た。ガラス転移温度は
50℃である。
(Comparative Example 2) Weight average molecular weight of about 50,000
0 poly L-lactic acid was melt extruded from a T die at 180 ° C.,
It was rapidly cooled on a casting drum kept at 35 ° C. to obtain an unstretched sheet having a thickness of 500 μm. The glass transition temperature is 50 ° C.

【0033】得られたシートを実施例1と同様にして、
成形温度65℃で熱成形しようとしたところ、軟化状態
での張力が低く、シートがドローダウンして成形が困難
となり、偏肉や破れが生じた。
The obtained sheet was processed in the same manner as in Example 1,
When an attempt was made to perform thermoforming at a forming temperature of 65 ° C., the tension in the softened state was low, the sheet was drawn down, making it difficult to form, and uneven thickness and breakage occurred.

【0034】[0034]

【発明の効果】本発明によれば、分解性重合体であるポ
リ乳酸系重合体から特定の特性の熱成形品を成形するこ
とにより、成形加工部分においては脆さが改良されて強
度的に優れ、未成形部は支持体に当接して同じく実用的
な強度を示し、さらには経時的な寸法変化の小さい透明
性熱成形加工品を得ることができる。
According to the present invention, by molding a thermoformed article having specific characteristics from a polylactic acid polymer which is a degradable polymer, brittleness is improved and strength is improved in the molded portion. It is possible to obtain a transparent thermoformed product which is excellent and shows the same practical strength as the unformed part comes into contact with the support and has a small dimensional change with time.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 重量平均分子量が60,000以上であ
るポリ乳酸系重合体からなりガラス転移温度が35℃以
上であるシートを、成形温度50〜90℃、延伸面積倍
率2〜20倍の範囲で成形してなり、該成形品の成形加
工部分の面内配向度ΔPの平均が2×10-3〜30×1
-3の範囲内にあることを特徴とするポリ乳酸系重合体
の熱成形加工品。
1. A sheet made of a polylactic acid-based polymer having a weight average molecular weight of 60,000 or more and having a glass transition temperature of 35 ° C. or more is molded at a molding temperature of 50 to 90 ° C. and a stretching area ratio of 2 to 20 times. The average in-plane orientation degree ΔP of the molded portion of the molded product is 2 × 10 −3 to 30 × 1.
A thermoformed product of a polylactic acid-based polymer characterized by being in the range of 0 -3 .
JP10130094A 1994-05-16 1994-05-16 Thermoformed product of polylactic acid polymer Expired - Lifetime JP3563436B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10130094A JP3563436B2 (en) 1994-05-16 1994-05-16 Thermoformed product of polylactic acid polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10130094A JP3563436B2 (en) 1994-05-16 1994-05-16 Thermoformed product of polylactic acid polymer

Publications (2)

Publication Number Publication Date
JPH07308961A true JPH07308961A (en) 1995-11-28
JP3563436B2 JP3563436B2 (en) 2004-09-08

Family

ID=14296971

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3563436B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08252895A (en) * 1995-03-16 1996-10-01 Mitsubishi Plastics Ind Ltd Decomposable laminated material
JP2001150531A (en) * 1999-12-01 2001-06-05 Mitsubishi Plastics Ind Ltd Molding of polylactic acid-based polymer and method for molding thereof
WO2003008178A1 (en) * 2001-07-19 2003-01-30 Toyo Seikan Kaisha, Ltd. Molded object obtained through stretching and thermal fixing and process for producing the same
JP2003212270A (en) * 2002-10-30 2003-07-30 Mitsubishi Plastics Ind Ltd Container for seeing through contents
WO2004007197A1 (en) * 2002-07-11 2004-01-22 Mitsubishi Plastics, Inc. Biodegradable laminate sheet and molded item from biodegradable laminate sheet
JP2005255839A (en) * 2004-03-11 2005-09-22 Daiwa Can Co Ltd Container made of polylactic acid polymer excellent in impact resistance and heat resistance, and method for forming the same
US7439283B2 (en) 2002-09-06 2008-10-21 Mitsubishi Plastics, Inc. Flame retardant resin composition and flame-retardant injection-molding

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08252895A (en) * 1995-03-16 1996-10-01 Mitsubishi Plastics Ind Ltd Decomposable laminated material
JP2001150531A (en) * 1999-12-01 2001-06-05 Mitsubishi Plastics Ind Ltd Molding of polylactic acid-based polymer and method for molding thereof
WO2003008178A1 (en) * 2001-07-19 2003-01-30 Toyo Seikan Kaisha, Ltd. Molded object obtained through stretching and thermal fixing and process for producing the same
US7390543B2 (en) 2001-07-19 2008-06-24 Toyo Seikan Kaisha Ltd. Molded object obtained through stretching and thermal fixing and process for producing the same
WO2004007197A1 (en) * 2002-07-11 2004-01-22 Mitsubishi Plastics, Inc. Biodegradable laminate sheet and molded item from biodegradable laminate sheet
US7320773B2 (en) 2002-07-11 2008-01-22 Mitsubishi Plastics, Inc. Biodegradable laminate sheet and molded item from biodegradable laminate sheet
US7439283B2 (en) 2002-09-06 2008-10-21 Mitsubishi Plastics, Inc. Flame retardant resin composition and flame-retardant injection-molding
KR100954924B1 (en) * 2002-09-06 2010-04-27 미쓰비시 쥬시 가부시끼가이샤 Flame-retardant resin composition and flame-retardant injection molding
JP2003212270A (en) * 2002-10-30 2003-07-30 Mitsubishi Plastics Ind Ltd Container for seeing through contents
JP2005255839A (en) * 2004-03-11 2005-09-22 Daiwa Can Co Ltd Container made of polylactic acid polymer excellent in impact resistance and heat resistance, and method for forming the same

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