JPH07207041A - Polylactic acid film - Google Patents
Polylactic acid filmInfo
- Publication number
- JPH07207041A JPH07207041A JP6001375A JP137594A JPH07207041A JP H07207041 A JPH07207041 A JP H07207041A JP 6001375 A JP6001375 A JP 6001375A JP 137594 A JP137594 A JP 137594A JP H07207041 A JPH07207041 A JP H07207041A
- Authority
- JP
- Japan
- Prior art keywords
- film
- polylactic acid
- polymer
- heat
- dimensional stability
- 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
Links
- 229920006381 polylactic acid film Polymers 0.000 title claims abstract description 7
- 229920000747 poly(lactic acid) Polymers 0.000 claims abstract description 14
- 238000002425 crystallisation Methods 0.000 claims abstract description 11
- 230000008025 crystallization Effects 0.000 claims abstract description 11
- 239000013078 crystal Substances 0.000 claims abstract description 10
- 229920000642 polymer Polymers 0.000 claims description 17
- 239000004626 polylactic acid Substances 0.000 claims description 10
- 230000004927 fusion Effects 0.000 claims description 4
- 238000002844 melting Methods 0.000 abstract description 3
- 230000008018 melting Effects 0.000 abstract description 3
- 229920006237 degradable polymer Polymers 0.000 abstract description 2
- 101100491857 Columba livia ASL gene Proteins 0.000 abstract 1
- 238000000034 method Methods 0.000 description 19
- 238000010438 heat treatment Methods 0.000 description 5
- AEMRFAOFKBGASW-UHFFFAOYSA-N Glycolic acid Chemical compound OCC(O)=O AEMRFAOFKBGASW-UHFFFAOYSA-N 0.000 description 4
- JVTAAEKCZFNVCJ-REOHCLBHSA-N L-lactic acid Chemical compound C[C@H](O)C(O)=O JVTAAEKCZFNVCJ-REOHCLBHSA-N 0.000 description 4
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- WHBMMWSBFZVSSR-UHFFFAOYSA-N 3-hydroxybutyric acid Chemical compound CC(O)CC(O)=O WHBMMWSBFZVSSR-UHFFFAOYSA-N 0.000 description 2
- REKYPYSUBKSCAT-UHFFFAOYSA-N 3-hydroxypentanoic acid Chemical compound CCC(O)CC(O)=O REKYPYSUBKSCAT-UHFFFAOYSA-N 0.000 description 2
- FMHKPLXYWVCLME-UHFFFAOYSA-N 4-hydroxy-valeric acid Chemical compound CC(O)CCC(O)=O FMHKPLXYWVCLME-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 235000014655 lactic acid Nutrition 0.000 description 2
- 239000004310 lactic acid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- -1 polyethylene terephthalate Polymers 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- SJZRECIVHVDYJC-UHFFFAOYSA-N 4-hydroxybutyric acid Chemical compound OCCCC(O)=O SJZRECIVHVDYJC-UHFFFAOYSA-N 0.000 description 1
- 229940006015 4-hydroxybutyric acid Drugs 0.000 description 1
- IWHLYPDWHHPVAA-UHFFFAOYSA-N 6-hydroxyhexanoic acid Chemical compound OCCCCCC(O)=O IWHLYPDWHHPVAA-UHFFFAOYSA-N 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000271566 Aves Species 0.000 description 1
- 239000004970 Chain extender Substances 0.000 description 1
- 229930182843 D-Lactic acid Natural products 0.000 description 1
- JVTAAEKCZFNVCJ-UWTATZPHSA-N D-lactic acid Chemical compound C[C@@H](O)C(O)=O JVTAAEKCZFNVCJ-UWTATZPHSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 229940022769 d- lactic acid Drugs 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000000113 differential scanning calorimetry Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920001432 poly(L-lactide) Polymers 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000001757 thermogravimetry curve Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Polyesters Or Polycarbonates (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ポリ乳酸系重合体から
なるフイルムに関するものである。FIELD OF THE INVENTION The present invention relates to a film made of a polylactic acid polymer.
【0002】[0002]
【従来の技術】現在、透明性が良く、強度、熱寸法安定
性に優れたフイルムとしては、例えばポリエチレンテレ
フタレート延伸フイルムをはじめとして、多くの高分子
材料フイルムが知られており産業界で広く利用され、消
費されている。しかしながら、これらのフイルムは自然
環境下に棄却されると、その安定性のため分解すること
なく残留し、景観を損ない、魚、野鳥などの生活環境を
汚染するなどの問題を引き起こしている。2. Description of the Related Art At present, as a film having excellent transparency, strength and thermal dimensional stability, many polymer material films including polyethylene terephthalate stretched film are known and widely used in industry. Have been consumed. However, when these films are discarded in the natural environment, they remain without being decomposed due to their stability, causing problems such as spoiling the landscape and polluting living environments such as fish and wild birds.
【0003】そこで、これらの問題を生じない分解性重
合体からなる材料が要求されており、実際多くの研究、
開発が行なわれている。その一例として、ポリ乳酸があ
る。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
解物となることが知られている。Therefore, there is a demand for a material composed of a decomposable polymer that does not cause these problems.
Development is underway. One example is polylactic acid. It is known that polylactic acid is hydrolyzed naturally in soil, does not remain in its original form in soil, and then becomes a decomposition product harmless by microorganisms.
【0004】しかし、ポリ乳酸のフイルムについては、
これまでほとんど知られておらず、特に工業的に有用な
強度、熱寸法安定性ともに優れたフイルムはいまだ知ら
れていなかった。However, regarding the polylactic acid film,
Up to now, little has been known, and no industrially useful film excellent in both strength and thermal dimensional stability has been known.
【0005】[0005]
【本発明が解決しようとする課題】本発明は、実用的な
強度と熱寸法安定性を有するポリ乳酸系フイルムを提供
することを目的とする。SUMMARY OF THE INVENTION It is an object of the present invention to provide a polylactic acid film having practical strength and thermal dimensional stability.
【0006】[0006]
【課題を解決するための手段】本発明者らは鋭意検討の
結果、ポリ乳酸系重合体からなり、フイルムの面配向度
ΔPが3.0×10-3以上であり、かつ、フイルムを昇
温したときの結晶融解熱量ΔHmと昇温中の結晶化によ
り発生する結晶化熱量ΔHcとの差(ΔHm−ΔHc)
が20J/g以上である場合に、強度、熱寸法安定性に
優れたポリ乳酸系フイルムが得られることを見い出し、
本発明も完成した。Means for Solving the Problems As a result of intensive investigations by the present inventors, the present inventors have made a polylactic acid-based polymer, have a plane orientation degree ΔP of 3.0 × 10 −3 or more, and raise the film. Difference between heat of crystal fusion ΔH m when heated and heat of crystallization ΔH c generated by crystallization during heating (ΔH m −ΔH c ).
Of 20 J / g or more, it was found that a polylactic acid film excellent in strength and thermal dimensional stability can be obtained,
The present invention has also been completed.
【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、フイルム物性を調整する目的で、可塑剤、滑剤、
無機フィラー、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. Further, for the purpose of adjusting molding processability and film physical properties, a plasticizer, a lubricant,
It is also possible to add additives such as inorganic fillers and ultraviolet absorbers, and 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、1万から100万が好まし
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、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 preferably from 10,000 to 1,000,000. When the weight average molecular weight is less than this range, practical physical properties are hardly exhibited, and when it exceeds the above range, the melt viscosity becomes too high and the moldability becomes poor.
【0010】本発明におけるポリ乳酸系フイルムは、こ
れらの重合体を押出法、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、平面状または円筒状の未延
伸シートまたはシート状溶融体にし、次いで、これをロ
ール法、テンター法、チユーブラ法、インフレーシヨン
法などにより一軸または二軸延伸することによって得ら
れる。The polylactic acid film in the present invention is obtained by converting these polymers into a flat or cylindrical unstretched sheet or a sheet-like melt by a general melt molding method such as an extrusion method, a calender method or a pressing method. Then, it is obtained by uniaxially or biaxially stretching it by a roll method, a tenter method, a cubula method, an inflation method or the like.
【0011】本発明においては、重合体の組成と成形加
工条件との兼ねあいにより、フイルムの面配向度ΔP
と、フイルムの結晶融解熱量と結晶化熱量との差(ΔH
m−ΔHc)とを、一定の値以上にすることが最も重要
である。すなわち、ポリ乳酸系フイルムにおいては、素
材が本来有しているところの脆性をΔPを増大させるこ
とにより改良し、ΔPの上昇に伴い低下する熱寸法安定
性を(ΔHm−ΔHc)を増大させることにより改良で
きるのである。In the present invention, the degree of plane orientation ΔP of the film is determined by the balance between the composition of the polymer and the molding processing conditions.
And the difference between the heat of crystal fusion and the heat of crystallization of the film (ΔH
It is most important that m −ΔH c ) and a certain value or more. That is, in the polylactic acid-based film, the original brittleness of the material is improved by increasing ΔP, and the thermal dimensional stability that decreases with the increase of ΔP is increased (ΔH m −ΔH c ). This can be improved.
【0012】ΔPは、フイルム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がフイルム面に平行な直交2軸の屈折
率、αはフイルム厚さ方向の屈折率である。ΔP represents the degree of orientation in the plane direction relative to the thickness direction of the film, 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) Here, γ and β are biaxial refractive indices orthogonal to the film surface, and α is a refractive index in the film thickness direction.
【0013】ΔPは結晶化度や結晶配向にも依存する
が、大きくはフイルム面内の分子配向に依存する。つま
りフイルム面内、特にフイルムの流れ方向および/また
はそれと直交する方向の1または2方向に対し、分子配
向を増大させることにより、無配向シート・フイルムで
は1.0×10-3以下であるΔPを本発明で規定する
3.0×10-3以上に増大させることができる。ΔPを
増大させる方法としては、既知のあらゆるフイルム延伸
法に加え、電場や磁場を利用した分子配向法を採用する
こともできる。ΔP depends on the crystallinity and the crystal orientation, but largely depends on the molecular orientation in the film plane. That is, by increasing the molecular orientation in the plane of the film, particularly in one or two directions of the flow direction of the film and / or the direction orthogonal thereto, in the non-oriented sheet / film, ΔP is 1.0 × 10 −3 or less. Can be increased to 3.0 × 10 −3 or more specified in the present invention. As a method for increasing ΔP, in addition to all known film stretching methods, a molecular orientation method using an electric field or a magnetic field can be adopted.
【0014】テンター法による2軸延伸を採用する場合
の延伸条件としては、延伸温度50〜100℃、延伸倍
率1.5倍〜5倍、延伸速度100%/分〜10000
%/分が一般的ではあるが、この適正範囲は重合体の組
成や、未延伸シートの熱履歴によって異なってくるの
で、ΔPの値を見ながら適宜決められる。チユーブラ延
伸法など他の延伸法を採用する場合も同様である。ΔP
が3.0×10-3を下まわる場合には、ポリ乳酸系フイ
ルムは強度に乏しく脆いため実用に供し難いが、3.0
×10-3以上とすることで強度・脆さが改善され実用上
問題がなくなる。When biaxial stretching by the tenter method is adopted, the stretching conditions are as follows: stretching temperature 50 to 100 ° C., stretching ratio 1.5 to 5 times, stretching speed 100% / min to 10000.
% / Min is generally used, but the appropriate range varies depending on the composition of the polymer and the thermal history of the unstretched sheet, so it can be appropriately determined while looking at the value of ΔP. The same applies to the case where another stretching method such as the cubula stretching method is adopted. ΔP
When it is less than 3.0 × 10 −3 , the polylactic acid-based film is poor in strength and brittle, so it is difficult to put it to practical use.
When it is set to × 10 -3 or more, strength and brittleness are improved and practically no problem occurs.
【0015】しかし、ΔPが3.0×10-3以上となる
と、フイルムの熱寸法安定性が不良となり、フイルムと
しての実用特性が大きく損われる。熱寸法安定性とは、
フイルムを常温よりやや高い温度の雰囲気にさらした時
に、フイルムが収縮せず元の寸法のままいられるかどう
かの指標であり、フイルムの使用される多くの用途にお
いては、通常熱寸法安定性が高いものが求められる。However, if ΔP is 3.0 × 10 -3 or more, the thermal dimensional stability of the film becomes poor, and the practical properties of the film are greatly impaired. What is thermal dimensional stability?
It is an indicator of whether the film can retain its original dimensions without shrinking when exposed to an atmosphere at a temperature slightly higher than room temperature.In many applications where the film is used, the thermal dimensional stability is usually High prices are required.
【0016】ΔPが3.0×10-3以上のポリ乳酸系フ
イルムにおいては、実用的な熱寸法安定性を得るため
に、フイルムの(ΔHm−ΔHc)を20J/g以上に
制御することが重要である。すなわち、(ΔHm−ΔH
c)が20J/gを下まわる場合は、フイルムの熱寸法
安定性が不良であり、多くの用途で実用に供せず、20
J/g以上であれば、熱寸法安定性が良好となる。In a polylactic acid type film having a ΔP of 3.0 × 10 −3 or more, the (ΔH m −ΔH c ) of the film is controlled to 20 J / g or more in order to obtain practical thermal dimensional stability. This is very important. That is, (ΔH m −ΔH
When c ) is less than 20 J / g, the thermal dimensional stability of the film is poor and it cannot be put to practical use in many applications.
If it is at least J / g, the thermal dimensional stability will be good.
【0017】ΔHm、ΔHcは、フイルムサンプルの示
差走査熱量測定(DSC)により求められるもので、Δ
Hmは昇温速度10℃/分でフイルムを昇温したときの
全結晶を融解させるのに必要な熱量であって、重合体の
結晶融点付近に現れる結晶融解による吸熱ピークの面積
から求められる。またΔHcは、昇温過程で生じる結晶
化の際に発生する発熱ピークの面積から求められる。ΔH m and ΔH c are obtained by differential scanning calorimetry (DSC) of the film sample, and ΔH m and ΔH c are
H m is the amount of heat required to melt all the crystals when the film is heated at a temperature rising rate of 10 ° C./min, and is calculated from the area of the endothermic peak due to crystal melting that appears near the crystal melting point of the polymer. . Further, ΔH c can be obtained from the area of the exothermic peak generated during crystallization that occurs during the temperature rising process.
【0018】ΔHmは、主に重合体そのものの結晶性に
依存し、結晶性が大きい重合体では大きな値をとる。ち
なみに共重合のないホモのL−乳酸重合体では、約50
J/gとなる。またΔHcは、重合体の結晶性に対する
その時のフイルムの結晶化度に関係する指標であり、Δ
Hcが大きい時は、昇温過程でフイルムの結晶化が進行
する、すなわち重合体が有する結晶性を基準にフイルム
の結晶化度が相対的に低かったことを表わす。逆に、Δ
Hcが小さい時は、重合体が有する結晶性を基準にフイ
ルムの結晶化度が相対的に高かったことを表わす。ΔH m mainly depends on the crystallinity of the polymer itself, and takes a large value in a polymer having a large crystallinity. By the way, in the homo-L-lactic acid polymer without copolymerization, about 50
J / g. Further, ΔH c is an index relating to the crystallinity of the film at that time with respect to the crystallinity of the polymer, and ΔH c is
When the H c is large, the crystallization of the film proceeds during the temperature rising process, that is, the crystallinity of the film is relatively low based on the crystallinity of the polymer. Conversely, Δ
When H c is small, it means that the crystallinity of the film was relatively high based on the crystallinity of the polymer.
【0019】すなわち、(ΔHm−ΔHc)を増大させ
るための1つの方向は、結晶性が高い重合体を原料に、
結晶化度の比較的高いフイルムをつくることである。フ
イルムの結晶化度は、重合体の組成に少なからず依存す
るが、フイルムの成形加工条件によっても、大きく影響
される。That is, one direction for increasing (ΔH m -ΔH c ) is to use a polymer having high crystallinity as a raw material.
To make a film with a relatively high degree of crystallinity. The crystallinity of the film depends to a large extent on the composition of the polymer, but is also greatly influenced by the processing conditions of the film.
【0020】成形加工工程、特にテンター法2軸延伸に
おいてフイルムの結晶化度を上げるためには、延伸倍率
を上げ配向結晶化を促進する、延伸後結晶化温度以上の
雰囲気で熱処理を行うなどの方法が有効である。In order to increase the crystallinity of the film in the molding step, especially in the biaxial stretching by the tenter method, the stretching ratio is increased to promote oriented crystallization, and after the stretching, heat treatment is performed in an atmosphere having a crystallization temperature or higher. The method is effective.
【0021】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。(1)ΔP 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。Examples are 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. (1) By ΔP Atsube refractometer, the refractive index (α, β,
γ) was measured and calculated by the following formula.
【0022】 ΔP={(γ+β)/2} − α (α<β<γ) γ:フイルム面内の最大屈折率 β:それに直交するフイルム面内方向の屈折率 α:フイルム厚さ方向の屈折率ΔP = {(γ + β) / 2} −α (α <β <γ) γ: Maximum refractive index in the film plane β: Refractive index in the in-plane direction of the film orthogonal thereto α: Refraction in the film thickness direction rate
【0023】(2)ΔHm−ΔHc パーキンエルマー製DSC−7を用い、フイルムサンプ
ル10mgをJIS−K7122に基づいて、昇温速度
10℃/分で昇温したときのサーモグラムから結晶融解
熱量ΔHmと結晶化熱量ΔHcを求め、算出した。(2) ΔH m -ΔH c Using DSC-7 manufactured by Perkin Elmer, a film sample 10 mg was heated according to JIS-K7122 at a temperature rising rate of 10 ° C./min from a thermogram to determine the heat of crystal fusion. ΔH m and heat of crystallization ΔH c were calculated and calculated.
【0024】(3)引張り強度と脆さ 引張り強度は東洋精機テンシロンII型機を用い、JIS
−K7127に基づいて測定した。また、脆さは触感に
て判断した。MDはフイルムの流れ方向、TDはフイル
ムの流れに対し直交する方向を示す。 (4)熱寸法安定性 フイルムサンプルを100mm×100mmに切り出
し、80℃の温水バスに10秒浸漬した後、縦横の寸法
を計り、その値を(縦×横)で表記し、熱寸法安定性の
指標とした。(3) Tensile strength and brittleness The tensile strength was measured using a Toyo Seiki Tensilon II machine according to JIS
-Measured based on K7127. Further, the brittleness was judged by touch. MD indicates the flow direction of the film, and TD indicates the direction orthogonal to the flow of the film. (4) Thermal Dimensional Stability A film sample is cut into 100 mm x 100 mm, immersed in a hot water bath at 80 ° C for 10 seconds, and then the vertical and horizontal dimensions are measured. Was used as an index.
【0025】[0025]
(実施例1〜2)重量平均分子量10万のポリL−乳酸
を30mmφ単軸エクストルダーにて、Tダイより押出
し、キヤステイングロールにて急冷し、厚み200μm
の未延伸シートを得た。続いて長手方向にロール延伸、
次いで、幅方向にテンターで延伸し、引き続きテンター
内で熱処理した。延伸条件およびそれに続く熱処理条件
を種々変化させ、表1に示すフイルムサンプルを得た。
フイルムの流れ速度は3m/分、延伸・熱処理各ゾーン
の通過時間はそれぞれ20秒である。(Examples 1 and 2) Poly L-lactic acid having a weight average molecular weight of 100,000 was extruded from a T-die with a 30 mmφ uniaxial extruder and rapidly cooled with a casting roll to a thickness of 200 μm.
To obtain an unstretched sheet. Then roll stretching in the longitudinal direction,
Then, it was stretched in the tenter in the width direction and subsequently heat-treated in the tenter. The stretching conditions and the subsequent heat treatment conditions were variously changed to obtain film samples shown in Table 1.
The flow rate of the film is 3 m / min, and the passing time through each stretching / heat treatment zone is 20 seconds.
【0026】[0026]
【表1】 [Table 1]
【0027】表1の結果から、ΔPおよび(ΔHm−Δ
Hc)が本発明の範囲内にあるフイルムは、脆さがなく
強度的に優れ、また熱寸法安定性も良好なことが分か
る。From the results of Table 1, ΔP and (ΔH m −Δ
It can be seen that the film having H c ) within the range of the present invention is not brittle and has excellent strength, and also has good thermal dimensional stability.
【0028】(実施例3)L−乳酸97重量%とグリコ
ール酸3重量%からなる分子量20万の共重合体を用
い、延伸・熱処理条件を変えるのみで実施例1と同様の
方法によりポリ乳酸系フイルムを得た結果を表2に示
す。(Example 3) Polylactic acid was prepared in the same manner as in Example 1 except that a copolymer of 97% by weight of L-lactic acid and 3% by weight of glycolic acid having a molecular weight of 200,000 was used and the stretching and heat treatment conditions were changed. Table 2 shows the results of obtaining the system films.
【0029】[0029]
【表2】 [Table 2]
【0030】[0030]
【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、強度、熱寸法安定性に優れたフイ
ルムを得ることができる。According to the present invention, a film having excellent strength and thermal dimensional stability can be obtained from a polylactic acid polymer which is a degradable polymer.
Claims (1)
Pが3.0×10-3以上であり、かつ、フイルムを昇温
したときの結晶融解熱量ΔHmと昇温中の結晶化により
発生する結晶化熱量ΔHcとの差(ΔHm−ΔHc)が
20J/g以上であることを特徴とするポリ乳酸系フイ
ルム。1. A plane orientation degree Δ comprising a polylactic acid-based polymer.
P is 3.0 × 10 −3 or more, and the difference between the heat of crystal fusion ΔH m when the film is heated and the heat of crystallization ΔH c generated by crystallization during temperature increase (ΔH m −ΔH A polylactic acid film characterized in that c ) is 20 J / g or more.
Priority Applications (1)
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JP137594A JP3330712B2 (en) | 1994-01-11 | 1994-01-11 | Method for producing polylactic acid-based film |
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---|---|---|---|
JP137594A JP3330712B2 (en) | 1994-01-11 | 1994-01-11 | Method for producing polylactic acid-based film |
Related Child Applications (2)
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JP2002174903A Division JP2003002984A (en) | 2002-06-14 | 2002-06-14 | Polylactic acid film |
JP2002174582A Division JP2002371144A (en) | 2002-06-14 | 2002-06-14 | Polylactide film |
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JPH07207041A true JPH07207041A (en) | 1995-08-08 |
JP3330712B2 JP3330712B2 (en) | 2002-09-30 |
Family
ID=11499747
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JP137594A Ceased JP3330712B2 (en) | 1994-01-11 | 1994-01-11 | Method for producing polylactic acid-based film |
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