JP5222007B2 - Biodegradable synthetic resin film - Google Patents
Biodegradable synthetic resin film Download PDFInfo
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- JP5222007B2 JP5222007B2 JP2008102238A JP2008102238A JP5222007B2 JP 5222007 B2 JP5222007 B2 JP 5222007B2 JP 2008102238 A JP2008102238 A JP 2008102238A JP 2008102238 A JP2008102238 A JP 2008102238A JP 5222007 B2 JP5222007 B2 JP 5222007B2
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- 229920003002 synthetic resin Polymers 0.000 title claims description 31
- 239000000057 synthetic resin Substances 0.000 title claims description 31
- 229920002472 Starch Polymers 0.000 claims description 65
- 239000008107 starch Substances 0.000 claims description 65
- 235000019698 starch Nutrition 0.000 claims description 65
- 229920001577 copolymer Polymers 0.000 claims description 38
- 239000000203 mixture Substances 0.000 claims description 31
- 229920005989 resin Polymers 0.000 claims description 31
- 239000011347 resin Substances 0.000 claims description 31
- 239000000843 powder Substances 0.000 claims description 29
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid group Chemical group C(CCC(=O)O)(=O)O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims description 13
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical group CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 12
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical group OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims description 9
- 229920006381 polylactic acid film Polymers 0.000 claims description 4
- 240000003183 Manihot esculenta Species 0.000 claims description 3
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims description 3
- 238000000465 moulding Methods 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 12
- 239000008188 pellet Substances 0.000 description 10
- 239000002689 soil Substances 0.000 description 10
- 239000010410 layer Substances 0.000 description 8
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 6
- 239000004840 adhesive resin Substances 0.000 description 6
- 229920006223 adhesive resin Polymers 0.000 description 6
- -1 aliphatic dicarboxylic acids Chemical class 0.000 description 6
- 239000001569 carbon dioxide Substances 0.000 description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 description 6
- 235000014113 dietary fatty acids Nutrition 0.000 description 6
- 239000000194 fatty acid Substances 0.000 description 6
- 229930195729 fatty acid Natural products 0.000 description 6
- 150000004665 fatty acids Chemical class 0.000 description 6
- 238000004806 packaging method and process Methods 0.000 description 6
- 239000004645 polyester resin Substances 0.000 description 6
- 229920001225 polyester resin Polymers 0.000 description 6
- 229920000747 poly(lactic acid) Polymers 0.000 description 5
- 239000004626 polylactic acid Substances 0.000 description 5
- 235000013305 food Nutrition 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229920006280 packaging film Polymers 0.000 description 4
- 239000012785 packaging film Substances 0.000 description 4
- 229920005672 polyolefin resin Polymers 0.000 description 4
- 229920000881 Modified starch Polymers 0.000 description 3
- 239000004368 Modified starch Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 229920006167 biodegradable resin Polymers 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000004310 lactic acid Substances 0.000 description 3
- 235000014655 lactic acid Nutrition 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 235000019426 modified starch Nutrition 0.000 description 3
- 238000005453 pelletization Methods 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 230000000717 retained effect Effects 0.000 description 3
- 239000013585 weight reducing agent Substances 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 230000002542 deteriorative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001903 high density polyethylene Polymers 0.000 description 2
- 239000004700 high-density polyethylene Substances 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 241000282414 Homo sapiens Species 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 229920003354 Modic® Polymers 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 229920002675 Polyoxyl Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 244000098338 Triticum aestivum Species 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001341 hydroxy propyl starch Substances 0.000 description 1
- 235000013828 hydroxypropyl starch Nutrition 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 235000019359 magnesium stearate Nutrition 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000001254 oxidized starch Substances 0.000 description 1
- 235000013808 oxidized starch Nutrition 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 229920006122 polyamide resin Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920005606 polypropylene copolymer Polymers 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000001384 succinic acid Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Laminated Bodies (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Biological Depolymerization Polymers (AREA)
Description
この発明は、生分解性合成樹脂フィルムに関するものである。とくにこの発明は、柔軟な合成樹脂フィルムであって、地球環境を悪化させないという特性を持った合成樹脂フィルムに関するものである。 The present invention relates to a biodegradable synthetic resin film. In particular, the present invention relates to a synthetic resin film that is a flexible synthetic resin film and has a characteristic of not deteriorating the global environment.
フィルム形成用の合成樹脂としては、オレフィン樹脂、塩化ビニル樹脂、ポリアミド樹脂、ポリエステル樹脂等多くのものがある。これらは何れも耐候性にすぐれたものであるため、永い間風雨に曝されても容易に分解しない。このため、これらの樹脂で作られたフィルムは劣化して役立たなくなったあと、いつまでもフィルムの形で残る。従って、役に立たなくなったフィルムは、放置されて環境を悪化させる。 As a synthetic resin for film formation, there are many olefin resins, vinyl chloride resins, polyamide resins, polyester resins and the like. Since these are all excellent in weather resistance, they are not easily decomposed even when exposed to wind and rain for a long time. For this reason, films made from these resins will remain indefinitely after being degraded and useless. Therefore, the film that is no longer useful is left unattended and worsens the environment.
フィルムとして大量に消費されるのは、農業用と包装用のフィルムである。これらのフィルムは、柔軟なフィルムが好まれる。柔軟なフィルムは、柔軟な合成樹脂を材料としなければならないが、柔軟な合成樹脂は種類が少ない。柔軟な樹脂は軟質塩化ビニル樹脂とポリオレフィン樹脂とに限られる。従って、合成樹脂フィルムとしては、軟質塩化ビニル樹脂フィルムとポリオレフィン樹脂フィルムとが大量に生産され、また使用後に廃棄されてきた。 Agricultural and packaging films are consumed in large quantities as films. These films are preferably flexible films. A flexible film must be made of a flexible synthetic resin, but there are few types of flexible synthetic resins. Flexible resin is limited to soft vinyl chloride resin and polyolefin resin. Accordingly, as the synthetic resin film, a soft vinyl chloride resin film and a polyolefin resin film are produced in large quantities and discarded after use.
軟質塩化ビニル樹脂フィルムとポリオレフィンフィルムとは、何れも前述のように、耐候性の良好な樹脂である。従って、使用できなくなったこれらの樹脂フィルムを処分するには、焼却する以外に適当な方法が見当らない。ところが、これらのフィルムを焼却すると、一時に大量の二酸化炭素を発生するほか、時にはダイオキシンのような発癌性の毒物を発生する。発生した二酸化炭素は地球温暖化の一因となって、人類を始め生物の生息環境を悪化させる。そこで、従来のフィルムに工夫を加えて分解され易くするか、又は従来のフィルムに代わって、地球の環境を悪化させない新しいフィルムを提供することが要求された。 The soft vinyl chloride resin film and the polyolefin film are both resins having good weather resistance as described above. Therefore, in order to dispose of these resin films that can no longer be used, there is no suitable method other than incineration. However, when these films are incinerated, they generate a large amount of carbon dioxide at one time and sometimes a carcinogenic poison such as dioxin. The generated carbon dioxide contributes to global warming, deteriorating the habitat of human beings and other living organisms. Therefore, it has been required to provide a new film that does not deteriorate the environment of the earth in place of the conventional film so that the conventional film can be easily decomposed by being devised.
従来のフィルムを分解され易くする試みには、軟質塩化ビニル樹脂又はポリオレフィン樹脂に澱粉粉末を配合して、樹脂に生分解性を付与しようとするものがある。この試みは下記特許文献1と2とに記載されている。しかし、この試みでは、澱粉が分解されるだけで樹脂はそのまま残るから、この樹脂で作られたフィルムは孔あき状態となって残り、矢張り環境を悪化させる。 An attempt to make a conventional film easy to be decomposed includes blending starch powder with a soft vinyl chloride resin or polyolefin resin to impart biodegradability to the resin. This attempt is described in Patent Documents 1 and 2 below. However, in this attempt, the resin remains as it is simply by decomposing the starch, so that the film made of this resin remains perforated, which worsens the arrow tension environment.
他方、地球環境を悪化させない新しい樹脂フィルムとしては、土中に埋めて放置すると自然に分解する性質を持った合成樹脂フィルム、いわゆる生分解性の合成樹脂フィルムが推奨されている。生分解性の合成樹脂フィルムは生分解性の合成樹脂から作らなければならない。生分解性の樹脂としては、脂肪族のジカルボン酸と脂肪族のジオールとを縮合させて得られた脂肪酸ポリエステル樹脂や、乳酸のような脂肪族のオキシカルボン酸を重合させて得られたポリオキシカルボン酸樹脂が提案されている。 On the other hand, as a new resin film that does not deteriorate the global environment, a synthetic resin film having a property of decomposing spontaneously when buried in soil and being left as it is, a so-called biodegradable synthetic resin film is recommended. The biodegradable synthetic resin film must be made from a biodegradable synthetic resin. Biodegradable resins include fatty acid polyester resins obtained by condensing aliphatic dicarboxylic acids and aliphatic diols, and polyoxyls obtained by polymerizing aliphatic oxycarboxylic acids such as lactic acid. Carboxylic acid resins have been proposed.
しかし、上記の乳酸を重合させて得られたポリ乳酸は、硬質樹脂であって柔軟性に乏しいために、柔軟なフィルムとすることが困難である。また上述の脂肪酸ポリエステル樹脂は、ジカルボン酸とジオールとに何を用いるかによって、性質が大きく変化する。従って、農業用又は包装用フィルムとして使用するに適した脂肪酸ポリエステル樹脂の組成を決めることは容易でない。 However, polylactic acid obtained by polymerizing the above lactic acid is a hard resin and lacks flexibility, so it is difficult to form a flexible film. Moreover, the above-mentioned fatty acid polyester resin changes greatly depending on what is used for dicarboxylic acid and diol. Therefore, it is not easy to determine the composition of the fatty acid polyester resin suitable for use as an agricultural or packaging film.
さらに、生分解性樹脂に澱粉粉末を加える技術も知られている。例えば下記特許文献3は、ポリ乳酸に澱粉粉末を加えて、分解速度が調節できる生分解性組成物を記載している。しかし、この組成物は硬質のものであって、柔軟なフィルムにすることが困難である。また、下記特許文献4は、フィルムへの成形を容易にするために、生分解性の脂肪酸ポリエステル樹脂に澱粉を配合することを提案している。ところが、この提案も柔軟なフィルムを得ることを目的としていない。また、この提案は脂肪酸ポリエステル樹脂として分子量が3万〜7万の高分子物と、3百〜3千の低分子物とを特定の割合に配合することを必要としているだけであって、成分の脂肪酸とアルコールについては広い範囲のものが使用できるとしている。 Furthermore, a technique for adding starch powder to a biodegradable resin is also known. For example, Patent Document 3 below describes a biodegradable composition in which starch powder is added to polylactic acid to control the degradation rate. However, this composition is hard and difficult to make into a flexible film. Patent Document 4 below proposes blending starch with a biodegradable fatty acid polyester resin in order to facilitate forming into a film. However, this proposal is not aimed at obtaining a flexible film. In addition, this proposal only requires that a high molecular weight material having a molecular weight of 30,000 to 70,000 and a low molecular weight material having a molecular weight of 300 to 3,000 are blended in a specific ratio as a fatty acid polyester resin. A wide range of fatty acids and alcohols can be used.
このように、これまでは農業用又は包装用に使用するに適した柔軟性を持った生分解性の合成樹脂フィルムは提供されなかった。
この発明は、農業用及び包装用に使用するに適した柔軟性と剛性とを持った生分解性の合成樹脂フィルムを提供しようとするものである。 The present invention is intended to provide a biodegradable synthetic resin film having flexibility and rigidity suitable for use in agriculture and packaging.
この発明者は、樹脂として数平均分子量が1万〜20万の範囲内にあって、組成がコハク酸と1,4−ブタンジオールとからなるポリエステルと、乳酸とが一定の割合で共重合してなる共重合体が、軟質塩化ビニル樹脂及びポリオレフィンに相当する柔軟性を持ち、フィルムとするに適していることを見出した。ところが、この共重合体は軟化点がやや低いという欠点を持っている。この発明者は、この欠点がこの共重合体に澱粉粉末を配合することによって解決できることを見出した。さらに、この発明者は、この共重合体には大量の澱粉粉末を加えて一様な組成物とすることができ、得られた組成物は、これを加熱溶融して成形することが容易であって、しかも軟化点が向上することのほか、生分解性が高まるなど、種々の予期しない効果の得られることを見出した。この発明は、このような知見に基づいて完成されたものである。 This inventor has a number average molecular weight in the range of 10,000 to 200,000 as a resin, and a composition of polyester comprising succinic acid and 1,4-butanediol and lactic acid are copolymerized at a certain ratio. It has been found that the copolymer thus obtained has flexibility equivalent to that of a soft vinyl chloride resin and polyolefin, and is suitable for use as a film. However, this copolymer has the disadvantage that its softening point is somewhat low. The inventor has found that this disadvantage can be solved by blending starch powder into the copolymer. Furthermore, the inventor can add a large amount of starch powder to the copolymer to obtain a uniform composition, and the obtained composition can be easily melted and molded. In addition to the improvement of the softening point, it has been found that various unexpected effects such as improved biodegradability can be obtained. The present invention has been completed based on such knowledge.
この発明は、重量で10〜90部の澱粉と、90〜10部の合成樹脂とからなるフィルムであって、上記合成樹脂は、数平均分子量が1万〜20万の範囲内にあり、組成が0.02〜30モル%の乳酸単位と、35〜49.99モル%のコハク酸単位と、このコハク酸単位に等しいモル%の1,4−ブタンジオール単位とからなる共重合体であることを特徴とする、生分解性合成樹脂フィルムを提供するものである。 This invention is a film comprising 10 to 90 parts by weight of starch and 90 to 10 parts of synthetic resin, wherein the synthetic resin has a number average molecular weight in the range of 10,000 to 200,000, Is a copolymer comprising 0.02 to 30 mol% lactic acid units, 35 to 49.99 mol% succinic acid units, and mol% 1,4-butanediol units equal to the succinic acid units. The present invention provides a biodegradable synthetic resin film.
この発明は、さらに上記生分解性合成樹脂フィルムの片面又は両面に、澱粉を含まない上記合成樹脂フィルム又はポリ乳酸からなるフィルムを貼り合わせてなる、生分解性合成樹脂フィルムをも提供するものである。 The present invention also provides a biodegradable synthetic resin film obtained by laminating the above-mentioned synthetic resin film not containing starch or a film made of polylactic acid on one or both surfaces of the biodegradable synthetic resin film. is there.
この発明では、合成樹脂として、組成が0.02〜30モル%の乳酸単位と、35〜49.99モル%のコハク酸単位と、このコハク酸単位に等しいモル%の1,4−ブタンジオール単位とからなる共重合体を用いたから、この共重合体はもともと生分解性が良好であるところ、この共重合体にさらに澱粉粉末を加えて組成物としたために、これで作られたフィルムは生分解性が一層良好になっている。また、この発明では上記共重合体の数平均分子量を1万〜20万の範囲内に特定したので、これに澱粉粉末を加えても得られた組成物は加熱溶融して成形するに適しており、これをフィルムに成形すると得られるフィルムはなお強靭であって、農業及び包装用に使用するに適している。 In the present invention, as a synthetic resin, a lactic acid unit having a composition of 0.02 to 30 mol%, a succinic acid unit of 35 to 49.99 mol%, and a 1,4-butanediol having a mol% equal to the succinic acid unit. Since a copolymer consisting of units was used, this copolymer was originally excellent in biodegradability, and since a starch powder was further added to this copolymer to form a composition, the film made with this was Biodegradability is even better. Moreover, in this invention, since the number average molecular weight of the said copolymer was specified in the range of 10,000-200,000, the composition obtained even if starch powder was added to this was suitable for shape | molding by heating and melting. The film obtained by forming it into a film is still tough and suitable for use in agriculture and packaging.
また、上記共重合体だけで作られたフィルムはほぼ100℃で軟化するものであるところ、この発明ではこの共重合体90〜10重量部に10〜90重量部の澱粉粉末を加えたので、得られた組成物は、軟化点が上昇し、得られたフィルムは約110℃以上の軟化点を持ち、従って耐熱性が向上していて、広い範囲で使用することができる。 Moreover, since the film made only of the copolymer is softened at about 100 ° C., in this invention, 10 to 90 parts by weight of starch powder is added to 90 to 10 parts by weight of the copolymer. The resulting composition has an increased softening point, and the resulting film has a softening point of about 110 ° C. or higher, thus improving heat resistance and can be used in a wide range.
さらに、澱粉を含んだ上記共重合体製のフィルムは、澱粉の一部がフィルム表面に露出しているので、吸湿性を持ち、従って水分を除くことが好ましい物を包装するに適している。他方、この吸湿性が欠点となる用途では、その表面に澱粉を含まない共重合体フィルム又はポリ乳酸フィルムを貼り合わせることによって、その吸湿性を弱めることができる。 Furthermore, since the film made of the above copolymer containing starch has a portion of the starch exposed on the film surface, it has a hygroscopic property, and therefore is suitable for packaging a product which is preferable to remove moisture. On the other hand, in applications where this hygroscopicity is a drawback, the hygroscopicity can be weakened by laminating a copolymer film or polylactic acid film not containing starch on its surface.
さらに、この発明で用いる合成樹脂と澱粉とは何れも土中に埋めておくと、自然に徐々に分解して水と二酸化炭素とになる。この場合の二酸化炭素の発生は徐々であって、樹脂を焼却するときのように一時に大量に発生するものでないから環境を汚染しない。その上に、ここで用いる合成樹脂と澱粉とは何れも植物から作ることができるものであって、石油から誘導されるものでない。このため、発生する二酸化炭素は植物に吸収されて、再び合成樹脂と澱粉とになる。従って、二酸化炭素は循環して使用されることとなる。このため、この発明は、地球温暖化を防ぎ、環境汚染を防ぐ効果をもたらす。 Furthermore, if both the synthetic resin and starch used in the present invention are buried in the soil, they will gradually decompose naturally into water and carbon dioxide. The generation of carbon dioxide in this case is gradual and does not pollute the environment because it does not occur in large quantities at the same time as when the resin is incinerated. In addition, both the synthetic resin and starch used herein can be made from plants and are not derived from petroleum. For this reason, the generated carbon dioxide is absorbed by the plant and becomes a synthetic resin and starch again. Therefore, carbon dioxide is circulated and used. For this reason, this invention brings about the effect which prevents global warming and prevents environmental pollution.
この発明では合成樹脂として、組成が0.02〜30モル%の乳酸単位と、35〜49.99モル%のコハク酸単位と、このコハク酸単位に等しいモル%の1,4−ブタンジオール単位とからなる共重合体を用いる。また、この発明では、上記共重合体の中から数平均分子量が1万〜20万のものを選んで用いる。このような共重合体は、例えば三菱化学からGS Plaの商品名で、生分解性の樹脂として販売されている。この発明では、このような市販の樹脂をそのまま用いることができる。 In this invention, the synthetic resin has a composition of 0.02 to 30 mol% lactic acid units, 35 to 49.99 mol% succinic acid units, and a mol% 1,4-butanediol unit equal to the succinic acid units. A copolymer consisting of In the present invention, those having a number average molecular weight of 10,000 to 200,000 are selected from the above copolymers. Such a copolymer is sold as a biodegradable resin by, for example, Mitsubishi Chemical under the trade name GS Pla. In the present invention, such a commercially available resin can be used as it is.
この発明では澱粉粉末を用いる。澱粉としては各種のものを用いることができる。例えばトウモロコシ、小麦、米、馬鈴薯、甘藷、タピオカ等の澱粉を粉末にしたものを用いることができる。その澱粉の粒径は実質的に2〜40μmの範囲内にあるものが好ましい。
澱粉粉末としては澱粉そのままでなく、加工澱粉又は改質澱粉を用いることができる。加工澱粉又は改質澱粉としてはスターチ、酸化澱粉、ヒドロキシプロピル澱粉などを用いることができる。
In this invention, starch powder is used. Various types of starch can be used. For example, corn, wheat, rice, potato, sweet potato, tapioca and other starch powders can be used. The starch preferably has a particle size in the range of 2 to 40 μm.
As the starch powder, processed starch or modified starch can be used instead of starch as it is. As the modified starch or modified starch, starch, oxidized starch, hydroxypropyl starch or the like can be used.
この発明では、上記の共重合体と澱粉粉末とを前者10〜90重量部と後者90〜10重量部の割合で中でも前者20〜80重量部と後者80〜20重量部の割合で、とりわけ前者30〜70重量部と後者70〜30重量部の割合で混合して、合計100重量部としたものを用いる。この混合物には約5重量部の金属石鹸、例えばステアリン酸マグネシウム又は、接着性樹脂例えば無水マレイン酸とオレフィンとの共重合体を少量添加すると混練が容易となる。 In the present invention, the copolymer and starch powder are mixed in the ratio of the former 10 to 90 parts by weight and the latter 90 to 10 parts by weight, particularly the former 20 to 80 parts by weight and the latter 80 to 20 parts by weight. A mixture of 30 to 70 parts by weight and the latter 70 to 30 parts by weight to make a total of 100 parts by weight is used. When a small amount of about 5 parts by weight of a metal soap such as magnesium stearate or an adhesive resin such as a copolymer of maleic anhydride and olefin is added to the mixture, kneading is facilitated.
この混合物は、これを一様な組成にするために、例えば押出機に入れて130〜150℃に加熱して溶融し、溶融物を紐状に押し出し、これを切断して一旦ペレットとすることが好ましい。このとき、上記共重合体は他の樹脂に比べてペレット化がとくに容易である。それは、上記共重合体の代わりに他の樹脂、例えばポリエチレンやポリプロピレンを用いると、樹脂による結合が不充分でペレットにすることができないことが起こるのに、上記共重合体を用いると、そのようなことが起きないからである。 In order to make this mixture into a uniform composition, it is put into, for example, an extruder and heated to 130 to 150 ° C. to melt, the melt is extruded into a string shape, and this is cut into pellets once. Is preferred. At this time, the copolymer is particularly easy to pelletize compared to other resins. If another resin such as polyethylene or polypropylene is used in place of the copolymer, it may not be possible to form pellets due to insufficient bonding by the resin. Because nothing happens.
この発明に係る生分解性合成樹脂フィルムを作るには、上記のペレットを再び押出機に入れて加熱溶融し、溶融物をフィルム状にして押し出す。押出機の代わりに、カレンダーロールを用いることもできる。そのときのフィルムの厚みには格別制限がないが、その厚みは約100μm〜2000μmの範囲内とすることが好ましい。 In order to make a biodegradable synthetic resin film according to the present invention, the above pellets are again put into an extruder, heated and melted, and the melt is extruded into a film. A calendar roll can be used instead of the extruder. Although there is no special restriction | limiting in the thickness of the film at that time, It is preferable to make the thickness into the range of about 100 micrometers-2000 micrometers.
こうして得られたフィルムの片面又は両面に、澱粉粉末を含まない上記共重合体フィルム又はポリ乳酸フィルムを張り合わせるには、澱粉粉末を含まないフィルムを予め別に作っておいて、これを澱粉粉末を含んだフィルムに貼り合わせてもよい。このとき、接着剤を用いてもよいが、接着剤を用いないで表面を溶融しただけで貼り合わせることが好ましい。 In order to laminate the copolymer film or polylactic acid film not containing starch powder on one or both sides of the film thus obtained, a film not containing starch powder is separately prepared in advance, You may affix on the included film. At this time, an adhesive may be used, but it is preferable to bond the surfaces only by melting the surfaces without using the adhesive.
また、上述のように貼り合わせたフィルムを作るには、上述のように一旦フィルムとして取り出したものを貼り合わせるよりも、共押し出し法により、フィルムを成形すると同時に一挙に貼り合わせてフィルムにすることが好ましい。共押し出し法とは、澱粉粉末を含む樹脂と、含まない樹脂とをそれぞれ別の押出機内で溶融しておき、この溶融物を別々に1つの同じ口金内に導入して、口金の入口側で別々にフィルム状に成形し、口金の出口側でそのフィルムを合流させて貼り合わせる、と云う方法である。こうして、一挙に積層フィルムを作ることが好ましい。 Also, in order to make a film bonded as described above, rather than pasting the film once taken out as described above, by co-extrusion method, the film is formed at the same time and bonded together into a film. Is preferred. In the co-extrusion method, a resin containing starch powder and a resin not containing starch are melted in separate extruders, and the melts are separately introduced into one same die, on the inlet side of the die. In this method, the films are separately formed into a film shape, and the films are joined and bonded together at the outlet side of the die. Thus, it is preferable to make a laminated film all at once.
積層フィルムでは、澱粉粉末が含まれていない表面フィルムを澱粉粉末が含まれているフィルムよりも厚みを薄くする。その厚みは、澱粉を含んだフィルムの厚みに対して澱粉を含まないフィルムの厚みを3分の1ないし100分の1とすることが好ましい。
なお、この発明では目的物をフィルムと表現しているが、それはフィルムの厚みを意識してそのように表現したのではない。或る書物によると、厚みが0.10mm以下のものをフィルムと呼び、それ以上のものをシートと呼ぶと区別しているようであるが、この発明ではそのような区別を無視してフィルムと云う中にシートをも含めている。
In the laminated film, the surface film that does not contain starch powder is made thinner than the film that contains starch powder. The thickness of the film containing no starch is preferably 1/3 to 1/100 of the thickness of the film containing starch.
In the present invention, the object is expressed as a film, but it is not expressed as such in consideration of the thickness of the film. According to a certain book, a film having a thickness of 0.10 mm or less is called a film, and a film having a thickness of more than 0.10 mm is called a sheet. In the present invention, such a distinction is ignored, and a film is called. The seat is included.
次に実施例と比較例とを挙げて、この発明に係るフィルムのすぐれている所以を具体的に説明する。 Next, the reason why the film according to the present invention is excellent will be specifically described with reference to Examples and Comparative Examples.
〔実施例1〕
合成樹脂としては、数平均分子量が7万で、組成が乳酸単位4モル%、コハク酸単位48モル%、及び1,4−ブタンジオール単位48モル%の共重合体を用いた。澱粉としては平均粒径が17μmのタピオカ澱粉を用いた。
[Example 1]
As the synthetic resin, a copolymer having a number average molecular weight of 70,000 and a composition of 4 mol% lactic acid units, 48 mol% succinic acid units, and 48 mol% 1,4-butanediol units was used. As the starch, tapioca starch having an average particle size of 17 μm was used.
上記共重合体70重量部に上記澱粉30重量部と、さらに接着性樹脂としてポリエチレン・不飽和カルボン酸変性ポリプロピレン共重合樹脂(三菱化学社製、モディック912T)5重量部を加え、合計105重量部の混合物を作った。この混合物を二軸押出機に入れて、シリンダー温度を140〜150℃に保ち、口金温度を160℃に維持して紐状に押し出し、冷却し切断してペレットとした。このペレット化は容易であった。 30 parts by weight of the above starch and 70 parts by weight of the above copolymer and 5 parts by weight of a polyethylene / unsaturated carboxylic acid-modified polypropylene copolymer resin (manufactured by Mitsubishi Chemical Corporation, Modic 912T) as an adhesive resin are added to total 105 parts by weight. Made a mixture of. This mixture was put into a twin screw extruder, the cylinder temperature was kept at 140 to 150 ° C., the die temperature was kept at 160 ° C., extruded into a string shape, cooled and cut into pellets. This pelletization was easy.
上記のペレットを再び押出機に入れてシリンダー温度を130〜150℃とし、口金温度を160℃に保ち、フィルム状に押し出し、厚み0.3mmのフィルムを得た。
このフィルムは適度の柔軟性を持っていた。また、その軟化点は120℃であった。このフィルムはそのまま包装用フィルムとして使用するに適していた。
The above pellets were again put into an extruder, the cylinder temperature was 130 to 150 ° C., the die temperature was kept at 160 ° C., and the film was extruded into a film to obtain a film having a thickness of 0.3 mm.
This film had moderate flexibility. The softening point was 120 ° C. This film was suitable for use as a packaging film as it was.
また、このフィルムを真空成形して容器にした。この容器は乾麺のような食品を入れるに適したものであった。
また、このフィルムを5cm×18cmの大きさに切り取り、これを土壌中に埋めて生分解性を評価した。埋設後120日で原形をとどめなくなっていた。
The film was vacuum formed into a container. This container was suitable for food such as dry noodles.
The film was cut into a size of 5 cm × 18 cm and buried in soil to evaluate biodegradability. 120 days after burial, the original shape was not retained.
〔実施例2〕
この実施例では、実施例1で用いたのと同種の共重合体と澱粉と接着性樹脂とを用いて同様に実施したが、ただ共重合体の使用量を減らすとともに、澱粉の使用量を増して、前者50重量部、後者50重量部の割合に混合して、合計105重量部の混合物を作った。
[Example 2]
In this example, the same type of copolymer as used in Example 1, starch and an adhesive resin were used in the same manner. However, the amount of the starch used was reduced while the amount of the copolymer used was reduced. The mixture was further mixed at a ratio of 50 parts by weight of the former and 50 parts by weight of the latter to make a total of 105 parts by weight of the mixture.
この混合物を押出機に入れ、実施例1と同様にして、一旦ペレットを得て、これを再び押出機に入れ厚み0.3mmフィルムとした。このペレット化とフィルムの成形は容易であった。
得られたフィルムは適度の柔軟性を持っていた。このフィルムを真空成形して容器とした。この容器は軟化点が125℃であって、100℃の食品を入れても変形しなかった。
This mixture was put into an extruder, and pellets were once obtained in the same manner as in Example 1 and again put into an extruder to form a 0.3 mm thick film. This pelletization and film formation were easy.
The obtained film had moderate flexibility. This film was vacuum formed into a container. This container had a softening point of 125 ° C. and was not deformed even when food at 100 ° C. was added.
また、上記のフィルムを5cm×18cmの大きさに切り取り、これを土中に埋めて自然条件下に30日、60日、90日及び120日間放置してフィルムの重量変化を測定した。土中に埋める前のフィルムの重量をX0とし、土中に放置したあとのフィルムの重量をX1として、フィルムの重量減少率Y(%)を次式により算出した。
Y(%)=(X0−X1)÷X0×100
Further, the above film was cut into a size of 5 cm × 18 cm, buried in the soil, and allowed to stand for 30 days, 60 days, 90 days and 120 days under natural conditions, and the weight change of the film was measured. The weight reduction rate Y (%) of the film was calculated by the following equation, where X 0 was the weight of the film before being buried in the soil, and X 1 was the weight of the film after being left in the soil.
Y (%) = (X 0 −X 1 ) ÷ X 0 × 100
また、比較のために上記フィルムの組成から澱粉を除いただけの組成のもの、即ち共重合体50重量部と接着性樹脂5重量部とからなる同様のフィルムを作り、これを上記フィルムと同様に土中に埋めて放置し、重量変化を測定し、重量減少率Y(%)を算出した。その結果は次の表1のとおりであった。 In addition, for comparison, a composition having only the starch removed from the composition of the film, that is, a similar film composed of 50 parts by weight of the copolymer and 5 parts by weight of the adhesive resin was prepared, and this was the same as the above film. It was buried in the soil and allowed to stand, the change in weight was measured, and the weight reduction rate Y (%) was calculated. The results are shown in Table 1 below.
これにより、澱粉を加えると重量減少率が約1.5倍に大きくなることが確認された。 Thereby, when starch was added, it was confirmed that a weight reduction rate will increase about 1.5 times.
〔実施例3〕
この実施例では、実施例1で用いたのと同種の共重合体と澱粉とを用いて同様に実施したが、ただ共重合体の使用量をさらに少なくし、逆に澱粉の使用量を増し、接着性樹脂をそのままの量で使用した。即ち、この実施例では共重合体30重量部と、澱粉70重量部と、接着性樹脂5重量部とを配合して混合物とした。
Example 3
In this example, the same type of copolymer and starch as used in Example 1 were used. However, the amount of copolymer used was further reduced, and the amount of starch used was increased. The adhesive resin was used as it was. That is, in this example, 30 parts by weight of a copolymer, 70 parts by weight of starch, and 5 parts by weight of an adhesive resin were blended to obtain a mixture.
この混合物を押出機に入れ、実施例1と同様にして一旦ペレットを作り、これを再び押出機に入れ、実施例1と同様にして厚み300μmのフィルムを作った。この場合のペレット化もフィルム化も容易であった。
得られたフィルムは適度の柔軟性を持っていて、包装用フィルムとするに適していた。また、このフィルムは軟化点が130℃であった。
This mixture was put into an extruder, pellets were once made in the same manner as in Example 1, and this was again put into the extruder, and a film having a thickness of 300 μm was made in the same manner as in Example 1. In this case, pelletization and film formation were easy.
The obtained film had moderate flexibility and was suitable as a packaging film. Further, this film had a softening point of 130 ° C.
このフィルムを真空成形して55mm×85mm×20mmの角形容器を作った。この容器を種々の温度に保持したオーブン中に30分間入れて容器の変形を観察した。また、比較のために澱粉だけを含まない組成のフィルムを作り、このフィルムを同じ大きさの角形容器に成形して、同様にオーブンに入れて容器の変形を観察した。結果は、次の表2のとおりであった。 This film was vacuum formed to make a rectangular container of 55 mm × 85 mm × 20 mm. The container was placed in an oven maintained at various temperatures for 30 minutes and the deformation of the container was observed. For comparison, a film having a composition not containing only starch was prepared, this film was formed into a rectangular container of the same size, and similarly placed in an oven to observe the deformation of the container. The results are shown in Table 2 below.
これによって、澱粉が共重合体の軟化点を上昇させ、耐熱性を向上させていることが確認された。 This confirmed that starch increased the softening point of the copolymer and improved heat resistance.
〔実施例4〕
この実施例は澱粉含有の共重合体からなるフィルムを中間層とし、その両面に澱粉なしの共重合体からなる表面フィルムを貼り合わせて、三層からなる積層フィルムを作った場合である。
Example 4
In this example, a film made of a starch-containing copolymer is used as an intermediate layer, and a surface film made of a copolymer without starch is bonded to both sides thereof to form a laminated film made of three layers.
中間層としては、実施例3で作った澱粉粉末70重量部が含まれている組成のフィルムで厚み240μmのフィルムを用い、表面層としては実施例3で用いた澱粉を含んでいなくて共重合体だけからなるフィルムで、厚みが30μmのものを用い、これを共押出法によって貼り合わせて、30/240/30μmの三層からなる厚み0.3mmの積層フィルムを得た。この積層フィルムの製造は容易であった。 As the intermediate layer, a film having a composition of 70 parts by weight of the starch powder prepared in Example 3 and having a thickness of 240 μm was used, and as the surface layer, the starch used in Example 3 was not included. A film made of only a polymer and having a thickness of 30 μm was used and bonded by a co-extrusion method to obtain a laminated film having a thickness of 0.3 mm consisting of three layers of 30/240/30 μm. The production of this laminated film was easy.
この積層フィルムは適度の柔軟性を持ち、軟化点が130℃であった。この積層フィルムはそのまま包装用に使用できるものであった。さらに、この積層フィルムを真空成形して容器にした。この容器は調理済みの食品を入れるに適したものであった。
また、この積層フィルムを土中に埋めて自然条件の下に放置したところ、120日にして原形をとどめなくなった。
This laminated film had moderate flexibility and a softening point of 130 ° C. This laminated film can be used for packaging as it is. Further, this laminated film was vacuum formed into a container. This container was suitable for containing cooked food.
Further, when this laminated film was buried in the soil and left under natural conditions, the original shape could not be retained in 120 days.
この積層フィルムは、中間層の組成からなる同じ厚みの単層フィルムに比べると、耐熱性にすぐれ、他のフィルムと貼り合わせてシールすることが容易であり、また表面に澱粉粉末が露出していないので、湿気によるヌメリがないという利点を持っている。反面、この積層シートは澱粉粉末が表面に露出していないので、生分解性が劣るという欠点を持っている。 This laminated film is superior in heat resistance compared to a single-layer film having the same thickness composed of an intermediate layer, and can be easily bonded to another film and sealed, and the starch powder is exposed on the surface. Since there is no, there is an advantage that there is no slime due to moisture. On the other hand, this laminated sheet has the disadvantage that the biodegradability is poor because the starch powder is not exposed on the surface.
〔実施例5〕
この実施例は、澱粉含有の共重合体からなるフィルムを中間層とし、その両面に澱粉なしのポリ乳酸からなるフィルムを貼り合わせて、三層の積層フィルムを作った場合である。
Example 5
In this example, a film made of a starch-containing copolymer is used as an intermediate layer, and a film made of polylactic acid without starch is bonded to both sides thereof to form a three-layer laminated film.
中間層としては、実施例1で作られた澱粉粉末が30重量部含まれている組成のフィルムで厚み240μmのフィルムを用い、表面フィルムとしてはポリ乳酸(東レ社製、商品:名エコディア)製の厚み30μmのフィルムを用い、共押出法によって貼り合わせて積層フィルムとした。この積層フィルムの製造は容易であった。 As the intermediate layer, a film having a composition of 30 parts by weight of the starch powder produced in Example 1 and having a thickness of 240 μm was used, and the surface film was made of polylactic acid (manufactured by Toray Industries, Inc., product: name Ecodia). A film having a thickness of 30 μm was used and laminated by a coextrusion method to obtain a laminated film. The production of this laminated film was easy.
この積層フィルムは柔軟であって、軟化点120℃であった。この積層フィルムはそのまま包装用の袋として使用できるものであった。さらにこの積層フィルムを真空成形して容器にした。この容器は調理済みの食品を入れるに適していた。
また、この容器を土中に埋めて自然条件の下に放置したところ、120日にして原形をとどめなくなった。
This laminated film was flexible and had a softening point of 120 ° C. This laminated film could be used as a packaging bag as it was. Further, this laminated film was vacuum formed into a container. This container was suitable for containing cooked food.
Moreover, when this container was buried in the soil and left under natural conditions, the original shape could not be retained in 120 days.
〔比較例1〕
実施例1において、澱粉を用いないで共重合体だけを用いることとして、そのほかは実施例1と全く同様にして厚み300μmの共重合体フィルムを作った。
[Comparative Example 1]
In Example 1, a copolymer film having a thickness of 300 μm was prepared in exactly the same manner as in Example 1 except that only the copolymer was used without using starch.
このフィルムは柔軟であって、その軟化点は110℃であり、これを実施例3で得たフィルムに比べると実施例3で説明したように耐熱性が劣っていた。
また、このフィルムをそのまま土中に埋めて自然条件の下に放置したところ、生分解はするものの、実施例2で説明したように実施例2で得られたものに比べると生分解性は劣っていた。
This film was flexible, and its softening point was 110 ° C. Compared with the film obtained in Example 3, this film was inferior in heat resistance as described in Example 3.
Moreover, when this film was buried in the soil as it was and left under natural conditions, it biodegraded, but the biodegradability was inferior to that obtained in Example 2 as described in Example 2. It was.
〔比較例2〕
実施例1において、共重合体の代わりに高密度ポリエチレン(株式会社プライムポリマー社製、商品名:HDPE、548B)を用いることとした以外は、実施例1と同様にしてポリエチレン70重量部、澱粉粉末30重量部の混合物を作り、これを二軸押出機に入れてペレットを作ろうとした。
[Comparative Example 2]
In Example 1, 70 parts by weight of polyethylene and starch were used in the same manner as in Example 1 except that high-density polyethylene (manufactured by Prime Polymer Co., Ltd., trade name: HDPE, 548B) was used instead of the copolymer. A mixture of 30 parts by weight of powder was made and placed in a twin screw extruder to make pellets.
ところが、二軸押出機から紐状物として押し出すと、押出物は発泡して良好なペレットを得ることができなかった。
また、こうして得た不完全なペレットを押出機に入れてフィルムに成形しようとしたが、フィルムに成形することができなかった。
However, when extruded as a string from a twin-screw extruder, the extrudate foamed and a good pellet could not be obtained.
In addition, the incomplete pellets thus obtained were put into an extruder to be formed into a film, but could not be formed into a film.
Claims (5)
The laminated resin film according to any one of claims 1 to 4 , wherein the starch powder is tapioca starch.
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| JPH0678475B2 (en) * | 1990-10-09 | 1994-10-05 | 工業技術院長 | Biodegradability control method for plastics |
| JP4047160B2 (en) * | 1994-08-31 | 2008-02-13 | 三菱化学株式会社 | Film made of aliphatic polyester copolymer |
| JPH08323946A (en) * | 1995-06-05 | 1996-12-10 | Mitsubishi Plastics Ind Ltd | Multi-layer biodegradable plastic film |
| JP2000238194A (en) * | 1999-02-22 | 2000-09-05 | Daicel Chem Ind Ltd | Biodegradable laminated film and agricultural biodegradable film |
| JP4312764B2 (en) * | 2001-03-30 | 2009-08-12 | ダイセル化学工業株式会社 | Aliphatic polyester biodegradable resin film molding |
| JP4846202B2 (en) * | 2004-03-17 | 2011-12-28 | 旭化成ケミカルズ株式会社 | Matte film |
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