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JP2001098104A - Biodegradable expanded particles and molded products thereof - Google Patents

Biodegradable expanded particles and molded products thereof

Info

Publication number
JP2001098104A
JP2001098104A JP27779099A JP27779099A JP2001098104A JP 2001098104 A JP2001098104 A JP 2001098104A JP 27779099 A JP27779099 A JP 27779099A JP 27779099 A JP27779099 A JP 27779099A JP 2001098104 A JP2001098104 A JP 2001098104A
Authority
JP
Japan
Prior art keywords
particles
polylactic acid
weight
higher fatty
foamed
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.)
Pending
Application number
JP27779099A
Other languages
Japanese (ja)
Inventor
Takayoshi Kubo
孝敬 久保
Sei Yoshimoto
聖 吉本
Shinko Yama
真弘 山
Tsunahiro Nakae
綱大 中江
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.)
Kanebo Synthetic Fibers Ltd
Kanebo Ltd
Research Institute of Innovative Technology for the Earth RITE
Original Assignee
Kanebo Synthetic Fibers Ltd
Kanebo Ltd
Research Institute of Innovative Technology for the Earth RITE
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 Kanebo Synthetic Fibers Ltd, Kanebo Ltd, Research Institute of Innovative Technology for the Earth RITE filed Critical Kanebo Synthetic Fibers Ltd
Priority to JP27779099A priority Critical patent/JP2001098104A/en
Publication of JP2001098104A publication Critical patent/JP2001098104A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W90/00Enabling technologies or technologies with a potential or indirect contribution to greenhouse gas [GHG] emissions mitigation
    • Y02W90/10Bio-packaging, e.g. packing containers made from renewable resources or bio-plastics

Landscapes

  • Containers Having Bodies Formed In One Piece (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

(57)【要約】 【課題】微生物による分解が可能で、使用後処分するに
際しても地球環境への負荷が少なく、高い生産性を有
し、実用に耐えうる発泡粒子及びその成形物を提供す
る。 【解決手段】L体とD体からなる実質的に非晶性のポリ
乳酸に低沸点の有機化合物を含浸させた発泡性粒子から
発泡粒子を得るに際し、予め発泡核剤としてタルクを1
〜20重量%混合、分散させた非晶性ポリ乳酸を使用
し、該有機化合物を含浸させた発泡性粒子の表面に高級
脂肪酸又はその金属塩、エステル、アミドから選ばれた
化合物を0.01〜1重量%を配合して得られることを
特徴とする発泡粒子及びその成形物。
PROBLEM TO BE SOLVED: To provide foamed particles which can be decomposed by microorganisms, have little impact on the global environment even when disposed after use, have high productivity, and can withstand practical use, and molded articles thereof. . Kind Code: A1 Abstract: To obtain expanded particles from expandable particles obtained by impregnating a substantially amorphous polylactic acid comprising an L-form and a D-form with an organic compound having a low boiling point, talc is previously used as a foam nucleating agent.
-20% by weight of an amorphous polylactic acid mixed and dispersed, and the surface of the expandable particles impregnated with the organic compound is coated with 0.01% of a higher fatty acid or a compound selected from metal salts, esters and amides thereof. A foamed particle and a molded product thereof, which are obtained by blending from 1 to 1% by weight.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、生分解性を有し、
地球環境保全に資する乳酸を原料として、主として包装
材料として用いられる発泡成形体に使用される発泡性粒
子及び該発泡性粒子から得られる発泡粒子とその成形物
に関する。
The present invention relates to a biodegradable composition,
TECHNICAL FIELD The present invention relates to expandable particles used for a foamed molded article mainly used as a packaging material, a foamed particle obtained from the foamable particle, and a molded product thereof, using lactic acid that contributes to global environmental protection as a raw material.

【0002】[0002]

【従来の技術】軽量性、緩衝性、成形加工性を生かした
プラスチック発泡体が包装、梱包材として多量に用いら
れており、その素材はポリスチレン(PS)、ポリオレ
フィンといった石油を原料とする化学製品で、使用後の
処分が困難で、焼却するにしても燃焼カロリーが高く、
焼却炉をいためたり、埋め立てをしても分解しない上に
容積が大きいために処分場のスペースを占有してしまう
といった大きな社会問題となってきている。
2. Description of the Related Art Plastic foams utilizing light weight, cushioning properties, and moldability are widely used as packaging and packing materials, and are made of petroleum-based chemical products such as polystyrene (PS) and polyolefin. It is difficult to dispose after use, and even if it is incinerated, it has a high calorie burn,
It has become a major social problem that it does not decompose even if it is damaged by incinerators or landfilled, and because it has a large volume, it occupies the space of the disposal site.

【0003】又、処分されずに投棄された発泡体が及ぼ
す、河川、海洋など、自然生態系への影響も無視できな
くなってきている。そこで、生態系の中で分解し、地球
環境への影響が少ない樹脂が開発された。例えば、微生
物の体内で合成されるポリヒドロキシブチレート系樹脂
や、脂肪族グリコールと脂肪族カルボン酸からなるポリ
エステル又は、カプロラクトンを主成分とするポリエス
テル系樹脂などが発表されているが、前者は、微生物が
作り出すため、純度が低い上、極めて生産性が悪く、利
用は制限される。
[0003] In addition, the effects of natural foams, such as rivers and oceans, caused by foams that are discarded without being disposed of have become insignificant. Therefore, resins that decompose in the ecosystem and have less impact on the global environment have been developed. For example, a polyhydroxybutyrate resin synthesized in the body of a microorganism, a polyester composed of an aliphatic glycol and an aliphatic carboxylic acid, or a polyester resin containing caprolactone as a main component, etc., have been announced. Due to the production of microorganisms, the purity is low, the productivity is extremely low, and the use is limited.

【0004】また、後者は、原料が石油・天然ガスとい
った安価で多量に入手できるものであるから生産性は確
かに良いが、結晶性樹脂である上にガラス転移点が低い
ため、生分解性包装材料としては実用性においてその用
途が制限される。更に原料を石油・天然ガスとしている
ため、分解すると地球上に存在する炭酸ガスに新たに炭
酸ガスが加算されるため、炭酸ガスの増加抑制に寄与し
ない。又、長期的にみた場合原料ソースが有限であるた
め、やがて入手が困難となり、本当の意味での地球環境
保全に資し得ない。
The latter is certainly good in productivity because the raw material is inexpensive and available in large quantities such as petroleum and natural gas. However, since it is a crystalline resin and has a low glass transition point, it is biodegradable. As a packaging material, its use is limited in practicality. Further, since the raw materials are petroleum and natural gas, when decomposed, carbon dioxide is newly added to carbon dioxide existing on the earth, and thus does not contribute to suppressing an increase in carbon dioxide. In the long term, since the raw material source is limited, it becomes difficult to obtain the material source soon, and it cannot contribute to global environmental protection in the true sense.

【0005】更に、生分解性の素材としてグリコール酸
や乳酸などもグリコリドやラクチドの開環重合によりポ
リマーが得られ、医療用徐放剤として、又、医療用等の
繊維として利用されているが、そのままでは発泡体とし
て、包装容器や緩衝材として大量に使用されるに至って
いない。
Further, as a biodegradable material, glycolic acid, lactic acid and the like can be obtained as a polymer by ring-opening polymerization of glycolide or lactide, and are used as a sustained-release agent for medical use or as a fiber for medical use. However, as it is, it has not been used in a large amount as a foam, as a packaging container or as a cushioning material.

【0006】[0006]

【発明が解決しようとする課題】本発明は、生分解性を
有し、生産性に優れる発泡粒子及びその成形物、即ち、
微生物による分解が可能で、使用後処分するに際しても
地球環境への負荷が少なく、高い生産性を有し、実用に
耐えうる発泡粒子及びその成形物を提供することにあ
る。
SUMMARY OF THE INVENTION The present invention relates to a foamed particle having biodegradability and excellent productivity, and a molded product thereof,
An object of the present invention is to provide foamed particles which can be decomposed by microorganisms, have little impact on the global environment even when disposed after use, have high productivity, and can withstand practical use, and molded articles thereof.

【0007】ポリ乳酸組成物の発泡性粒子及び発泡粒子
に関しては、既に特開平5−17965、特開平5−1
7966に提案されている。しかし、本発明者らが詳細
に追試した結果、いずれの提案もその効果は期待出来な
いものであった。特開平5−17965には発泡粒子が
提案されているが、明細書中に詳述してある方法を忠実
に再現しても高発泡の発泡粒子を安定して、且つ、大量
に製造することは出来なかった。その原因は、水分散系
で高温高圧下で処理したポリ乳酸組成物を高温下に大気
中に噴出させると綿状になり粒子とはならない為であ
る。発泡性ポリスチレンビーズのように発泡性ビーズを
予備発泡し、該発泡粒子を型枠成形するためには真球に
近い球状粒子が必要であり、綿状物では型枠成形は不可
能である。また、該処理ポリ乳酸組成物を100℃付近
まで冷却して噴出させると発泡倍率の低い変形した発泡
粒子しか得られれず、型枠成形に耐えうるものではな
い。更に、特開平5−17965には他の製造方法は何
ら記載されておらず、該提案でもって発泡粒子を得るこ
とは期待出来ない。
[0007] Regarding the expandable particles and expanded particles of the polylactic acid composition, Japanese Patent Laid-Open Nos. 5-17965 and 5-1 have already been disclosed.
7966. However, as a result of a detailed examination by the present inventors, none of the proposals was expected to be effective. JP-A-5-17965 proposes foamed particles. However, even if the method detailed in the specification is faithfully reproduced, it is necessary to stably produce a large amount of foamed particles in large quantities. Could not. The reason for this is that when the polylactic acid composition treated at high temperature and high pressure in an aqueous dispersion system is spouted into the atmosphere at high temperature, it becomes flocculent and does not become particles. Pre-expanding expandable beads such as expandable polystyrene beads and forming the expanded particles into a form requires spherical particles close to a true sphere, and it is impossible to form the form with a cotton-like material. In addition, when the treated polylactic acid composition is cooled to around 100 ° C. and jetted, only deformed expanded particles having a low expansion ratio are obtained, which is not resistant to mold forming. Furthermore, JP-A-5-17965 does not disclose any other production method, and it cannot be expected that foamed particles can be obtained by this proposal.

【0008】一方、特開平5−17966に提案されて
いる発泡性粒子は一般に採用されている方法とかけ離れ
た方法で製造することが明細書中に記載され現実性に乏
しく、仮にこの提案により製造した発泡性粒子から発泡
粒子を得るにしても、発泡粒子が互いに融着するブロッ
キング現象が発生し、型枠成形を効率よく行うことは到
底不可能である。
On the other hand, it is described in the specification that the expandable particles proposed in Japanese Patent Application Laid-Open No. Hei 5-17966 are manufactured by a method that is far from the method generally employed, and the method is not realistic. Even if foamed particles are obtained from the expanded foamed particles, a blocking phenomenon occurs in which the foamed particles are fused to each other, and it is almost impossible to efficiently perform mold forming.

【0009】本発明者等は、発泡性ポリスチレンビーズ
のように高効率で発泡性ビーズを予備発泡し、該発泡粒
子を型内成形することが出来る高発泡粒子について鋭意
研究を行い、ここに提案するものである。
The present inventors have conducted intensive studies on high-expandable particles which can be pre-expanded with high efficiency, such as expandable polystyrene beads, and in which the expanded particles can be molded in a mold. Is what you do.

【0010】本発明者等は、既に高い発泡性を有する生
分解性樹脂として不可欠な条件であるベースポリマー、
高分子量化するための添加剤、発泡させるための添加剤
等について詳細に検討を重ねた結果、実用上十分な生産
性を有する生分解性樹脂組成物を見いだし、発明提案
(特開平)を行った。しかし、該発明で得られる樹脂組
成物は高発泡倍率を有する発泡粒子は得られるものの、
発泡性粒子から熱処理により発泡粒子を得る工程におい
て、発泡粒子が互いに融着し、いわゆるブロッキング現
象を起こし未融着の独立した発泡粒子の取得率が低下す
ることが判明した。特開平8−253617においてブ
ロッキング防止剤の提案がされているが、本発明者らが
追試した結果、該提案でもブロッキングを十分には回避
できないことが判明した。即ち、ブロッキング防止剤の
添加量が少量ではその効果が殆ど期待できず、添加量を
増加させるとブロッキング防止効果は向上するが、得ら
れた発泡粒子から成形物、特に厚さ50mm以上の成形
物を得ようとすると該成形物の表面層と内層で発泡粒子
間の融着に差が生じ、均一な発泡成形物を得ることが困
難である。この原因は、発泡スチレン粒子に比較してガ
ラス転移点が低いため、適正な成形温度範囲が狭いこと
がその一因と推定される。
The present inventors have proposed a base polymer, which is an essential condition as a biodegradable resin having a high foaming property.
As a result of detailed studies on additives for increasing the molecular weight, additives for foaming, etc., a biodegradable resin composition having practically sufficient productivity was found, and an invention was proposed (JP-A-Hei). Was. However, although the resin composition obtained by the invention can obtain expanded particles having a high expansion ratio,
In the process of obtaining expanded particles by heat treatment from the expandable particles, it has been found that the expanded particles are fused to each other, causing a so-called blocking phenomenon, and the acquisition rate of unfused independent expanded particles is reduced. Japanese Patent Application Laid-Open No. 8-253617 proposes a blocking inhibitor, but as a result of additional tests by the present inventors, it has been found that even with this proposal, blocking cannot be sufficiently avoided. That is, when the added amount of the anti-blocking agent is small, the effect can hardly be expected, and when the added amount is increased, the anti-blocking effect is improved. However, a molded product from the obtained expanded particles, particularly a molded product having a thickness of 50 mm or more. However, it is difficult to obtain a uniform foamed molded product because of the difference in fusion between the foamed particles in the surface layer and the inner layer of the molded product. This is presumably because the glass transition point is lower than that of the expanded styrene particles, and the appropriate molding temperature range is narrow.

【0011】[0011]

【課題を解決するための手段】本発明者らは、大量に生
産、使用するためにはかかる課題を克服することが必須
と判断し鋭意研究の結果、本発明に到達したものであ
る。即ち、本発明はL体とD体からなる実質的に非晶性
のポリ乳酸に低沸点の有機化合物を含浸させた発泡性粒
子から発泡粒子を得るに際し、予め発泡核剤としてタル
クを1〜20重量%混合、分散させた非晶性ポリ乳酸を
使用し、該有機化合物を含浸させた発泡性粒子の表面に
高級脂肪酸又はその金属塩、エステル、アミドから選ば
れた化合物を0.01〜1重量%を配合して得られるこ
とを特徴とする発泡粒子及びその成形物である。タルク
を一般に使用される量を超えた添加量と高級脂肪酸の金
属塩、エステル、アミドから選ばれた化合物の組み合わ
せによる相乗効果により本発明は達成されたものであ
る。
Means for Solving the Problems The present inventors have determined that it is essential to overcome such problems in order to produce and use in large quantities, and as a result of earnest research, have arrived at the present invention. That is, in the present invention, when foaming particles are obtained from foaming particles obtained by impregnating a substantially amorphous polylactic acid composed of L-form and D-form with an organic compound having a low boiling point, talc is previously used as a foam nucleating agent. A compound selected from a higher fatty acid or a metal salt, an ester, or an amide thereof is used on the surface of expandable particles impregnated with the organic compound by using amorphous polylactic acid mixed and dispersed at 20% by weight. A foamed particle obtained by blending 1% by weight and a molded product thereof. The present invention has been achieved by the synergistic effect of a combination of a compound selected from metal salts, esters and amides of higher fatty acids, in which the amount of talc added exceeds the amount generally used.

【0012】[0012]

【発明の実施の形態】本発明のD体とL体からなる実質
的に非晶性のポリ乳酸とは、融点は有するもののその融
解熱が小さいポリ乳酸まで含むものである。即ち、DS
C測定による融解熱(2nd scan△H)が0.1
J/g以下のポリ乳酸でありD体共重合比率では5モル
%以上に相当する。これはmacromolecule
s 255719−5729(1992)記載のXD
0.048以上に近似するものである。従って、本発明
に使用されるポリ乳酸のD体とL体の共重合比率はD体
が5〜40モル%が必要であり、更には、8〜20モル
%が好ましく使用される。特に、高発泡倍率の発泡粒子
が要求される場合、融解熱(2nd scan△H)の
無いD体が8〜20モル%が好ましい。
BEST MODE FOR CARRYING OUT THE INVENTION The substantially amorphous polylactic acid comprising a D-form and an L-form according to the present invention includes polylactic acid having a melting point but a small heat of fusion. That is, DS
The heat of fusion (2nd scan @ H) by C measurement is 0.1
It is a polylactic acid of J / g or less and corresponds to 5 mol% or more in D-form copolymerization ratio. This is macromolecule
X D described in s 255719-5729 (1992) =
It is close to 0.048 or more. Therefore, the copolymerization ratio of the D-form and the L-form of the polylactic acid used in the present invention needs to be 5 to 40 mol% for the D-form, and more preferably 8 to 20 mol%. In particular, when expanded particles having a high expansion ratio are required, the D-form having no heat of fusion (2nd scan @ H) is preferably 8 to 20 mol%.

【0013】D体のモル比率が5%未満だと、ポリ乳酸
の結晶性が高くなり発泡倍率が上がらなくなったり、発
泡が不均一になる。又、D体のモル比率が40%を超え
ると、耐熱性が劣り、利用に適さない。
If the molar ratio of the D-form is less than 5%, the crystallinity of the polylactic acid is increased, so that the expansion ratio cannot be increased or the foaming becomes uneven. On the other hand, when the molar ratio of the D-form exceeds 40%, the heat resistance is inferior and is not suitable for use.

【0014】本発明に使用されるポリ乳酸は溶融粘度が
JIS K7210(荷重2.16kgf)に準拠した
メルトインデックス値(MI)で1〜10の範囲にある
高分子量のポリ乳酸が好ましい。しかし、該ポリ乳酸を
そのまま使用しても発泡倍率の高い発泡粒子は得ること
が出来ない。発泡倍率の高い発泡粒子を得るにはポリイ
ソシアネート等の粘度増加剤と反応させて更に超高粘度
化したポリ乳酸組成物とする必要がある。例えば、10
倍以上の高発泡倍率の発泡粒子を得るには、該組成物の
溶融粘度(MI)が5以下、好ましくは1以下であるこ
とが望ましい。
The polylactic acid used in the present invention is preferably a high molecular weight polylactic acid having a melt viscosity in the range of 1 to 10 by a melt index value (MI) according to JIS K7210 (load: 2.16 kgf). However, even if the polylactic acid is used as it is, expanded particles having a high expansion ratio cannot be obtained. In order to obtain expanded particles having a high expansion ratio, it is necessary to react with a viscosity-increasing agent such as polyisocyanate to obtain a polylactic acid composition having an even higher viscosity. For example, 10
In order to obtain expanded particles having a high expansion ratio of 2 times or more, it is desirable that the melt viscosity (MI) of the composition is 5 or less, preferably 1 or less.

【0015】溶融粘度が1未満のポリ乳酸は、通常用い
られる乳酸又は二量体であるラクチドから直接に製造す
ることは困難であり、一方、10を越える溶融粘度を有
するポリ乳酸は容易に得られるが、該ポリ乳酸を使用し
て得られる発泡性粒子は発泡倍率が極端に低下し実用上
使用できない。その理由は、ポリイソシアネート等の粘
度増加剤と反応させて高粘度化しても、分岐密度が高く
なり、架橋構造をとりやすく、該構造が発泡を阻害する
と推定される。
Polylactic acid having a melt viscosity of less than 1 is difficult to produce directly from commonly used lactic acid or dimer lactide, while polylactic acid having a melt viscosity of more than 10 is easily obtained. However, the expandable particles obtained by using the polylactic acid have an extremely low expansion ratio and cannot be used practically. The reason is presumed that, even when the viscosity is increased by reacting with a viscosity increasing agent such as polyisocyanate, the branch density increases, a crosslinked structure is easily formed, and the structure inhibits foaming.

【0016】本発明に使用され得るポリイソシアネート
としては、芳香族、脂環族、脂肪族系のいずれのポリイ
ソシアネートでも良い。例えば、芳香族ポリイソシアネ
ートとしてはトリレン、ジフェニルメタン、ナフチレ
ン、トリジン、キシレン、トリフェニルメタンを骨格と
するポリイソシアネート。脂環族ポリイソシアネートと
してはイソホロン、水素化ジフェニルメタンを骨格とす
るポリイソシアネート、脂肪族ポリイソシアネートとし
てはヘキサメチレン、リジンを骨格とするポリイソシア
ネートがある。その中で汎用性、取り扱い性、耐候性等
からトリレン、ジフェニルメタン、特にジフェニルメタ
ンが好ましく使用される。
The polyisocyanate that can be used in the present invention may be any of aromatic, alicyclic and aliphatic polyisocyanates. For example, as the aromatic polyisocyanate, a polyisocyanate having a skeleton of tolylene, diphenylmethane, naphthylene, tolidine, xylene, or triphenylmethane is used. Examples of the alicyclic polyisocyanate include polyisocyanates having a skeleton of isophorone or hydrogenated diphenylmethane, and examples of the aliphatic polyisocyanates include polyisocyanates having a skeleton of hexamethylene or lysine. Among them, tolylene, diphenylmethane, and especially diphenylmethane are preferably used from the viewpoint of versatility, handleability, weather resistance and the like.

【0017】次に本発明に使用するポリ乳酸に混合、分
散させるタルクは、該ポリ乳酸に対して1〜20重量%
が必要であり、更に好ましくは、該使用量は2〜10重
量%である。特開平8−253617においてタルクを
含む無機質粉末は1.5重量%以下、なかでも0.00
5〜1.0重量%であることが望ましいと記載されてい
る如く、一般的にその使用量は0.5重量%以下であ
る。
Next, talc to be mixed and dispersed in the polylactic acid used in the present invention is 1 to 20% by weight based on the polylactic acid.
Is required, and more preferably, the amount is 2 to 10% by weight. In Japanese Patent Application Laid-Open No. 8-253617, the content of the inorganic powder containing talc is 1.5% by weight or less, especially 0.00%.
Generally, the amount used is 0.5% by weight or less, as described above as being desirably 5 to 1.0% by weight.

【0018】これに対して、後述する高級脂肪酸の金属
塩、エステル、アミドから選ばれた化合物と併用して本
発明の目的であるブロッキング性の極めて少ない発泡粒
子を効率よく得るには、タルクの使用量は1重量%未満
では不十分であり、未融着の独立した発泡粒子の取得率
は低下する。一方、タルクの使用量が20重量%を越え
ると、ポリ乳酸の分子量が低下し発泡倍率が低下すると
共に発泡粒子から得られる成形物は剛直となり包装材と
しての機能が低下し好ましくない。
On the other hand, in order to efficiently obtain expanded particles having extremely low blocking properties, which is the object of the present invention, it is necessary to use talc in combination with a compound selected from metal salts, esters and amides of higher fatty acids described later. If the amount used is less than 1% by weight, it is insufficient, and the acquisition rate of unfused, independent foamed particles will be reduced. On the other hand, when the use amount of talc exceeds 20% by weight, the molecular weight of polylactic acid decreases, the expansion ratio decreases, and the molded product obtained from the expanded particles becomes rigid, and the function as a packaging material deteriorates, which is not preferable.

【0019】本発明に使用するタルクはその平均粒子径
が10μm以下が好ましく、更に好ましくは5μm以
下、特に好ましくは3μm以下である。平均粒子径がこ
の範囲にあると、発泡核剤としての起泡開始点が十分有
り、発泡セル膜の延伸を阻害せず、結果として高発泡倍
率が得られやすくなる。発泡セル膜の膜厚は多くの場合
数μmである。
The talc used in the present invention has an average particle diameter of preferably 10 μm or less, more preferably 5 μm or less, particularly preferably 3 μm or less. When the average particle size is within this range, there is a sufficient foaming starting point as a foam nucleating agent, and the stretching of the foam cell membrane is not hindered. As a result, a high foaming ratio is easily obtained. In many cases, the thickness of the foam cell membrane is several μm.

【0020】タルクを本発明に使用するポリ乳酸に添
加、分散させる方法はラクチドからポリ乳酸を得る重合
工程、ポリ乳酸とタルクを混練機等で溶融混練する方法
のいずれでも良いが、高濃度のタルクを添加、分散させ
るためには二軸混練機を使用して溶融混練する方法が好
ましい。
The method of adding and dispersing talc to the polylactic acid used in the present invention may be any of a polymerization step of obtaining polylactic acid from lactide and a method of melt-kneading polylactic acid and talc with a kneader or the like. In order to add and disperse talc, a method of melt-kneading using a twin-screw kneader is preferable.

【0021】かくして得られたポリ乳酸樹脂組成物に、
発泡剤、発泡助剤を含浸させ、発泡処理を行うと高発泡
倍率の発泡体が得られる。ここで用いる発泡剤として
は、プロパン、n−ブタン、イソブタン、n−ペンタ
ン、イソペンタン、シクロペンタン、ヘキサン等の炭化
水素、塩化メチレン、塩化メチル、ジクロロジフルオロ
メタン等のハロゲン化炭化水素類、ジメチルエーテル、
メチルエチルエーテル等のエーテル類が使用される。
又、発泡助剤としては炭素数1〜4のアルコール、ケト
ン類、エーテル、ベンゼン、トルエン等が主として用い
られる。
The polylactic acid resin composition thus obtained contains
When a foaming agent and a foaming aid are impregnated and subjected to a foaming treatment, a foam having a high expansion ratio is obtained. Examples of the blowing agent used herein include propane, n-butane, isobutane, n-pentane, isopentane, cyclopentane, hydrocarbons such as hexane, methylene chloride, methyl chloride, halogenated hydrocarbons such as dichlorodifluoromethane, dimethyl ether,
Ethers such as methyl ethyl ether are used.
Alcohols having 1 to 4 carbon atoms, ketones, ether, benzene, toluene and the like are mainly used as foaming assistants.

【0022】発泡剤、発泡助剤の含浸は通常の方法が使
用でき、水分散系又は非水系で、加熱下、高圧下で行う
ことが出来る。例えば、オートクレーブにポリ乳酸、発
泡剤、発泡助剤を所定量投入し、内温80〜90℃に保
持しながら数時間加熱すると容易に発泡性粒子を得るこ
とが出来る。
The impregnating of the foaming agent and the foaming aid can be carried out by a usual method, and can be carried out in an aqueous dispersion or non-aqueous system under heating and under high pressure. For example, a predetermined amount of polylactic acid, a foaming agent, and a foaming aid are charged into an autoclave, and the foamed particles can be easily obtained by heating for several hours while maintaining the internal temperature at 80 to 90 ° C.

【0023】次に本発明の目的である未融着の独立した
発泡粒子を効率よく取得率よく生産するためには、高級
脂肪酸又はその金属塩、エステル、アミドから選ばれた
化合物を上記発泡性粒子の表面に0.01〜3重量%、
好ましくは0.02〜0.1重量%配合することが必要
である。
Next, in order to efficiently produce the unfused independent foamed particles, which is an object of the present invention, at a high acquisition rate, a compound selected from a higher fatty acid or a metal salt, ester, or amide thereof is mixed with the above foamable foam. 0.01 to 3% by weight on the surface of the particles,
Preferably, 0.02 to 0.1% by weight is required.

【0024】本発明に言う高級脂肪酸とは、炭素数12
以上の脂肪族カルボン酸を意味する。高級脂肪酸の金属
塩も同様に炭素数12以上の脂肪族カルボン酸の金属塩
である。炭素数12未満のカルボン酸は不快臭があり、
また、その金属塩はその化合物の融点が上昇し不適であ
る。
The higher fatty acid referred to in the present invention is a compound having 12 carbon atoms.
The above aliphatic carboxylic acids are meant. Similarly, metal salts of higher fatty acids are metal salts of aliphatic carboxylic acids having 12 or more carbon atoms. A carboxylic acid having less than 12 carbon atoms has an unpleasant odor,
Further, the metal salt is unsuitable because the melting point of the compound increases.

【0025】炭素数12以上のカルボン酸としては、例
えばラウリン酸、パルミチン酸、ステアリン酸等のモノ
カルボン酸、又はダイマー酸等のジカルボン酸があり、
その金属塩の金属イオンはアルミニウム、亜鉛、カルシ
ウム、バリウム、マグネシウムがあげられる。これら高
級脂肪酸の金属塩の中でステアリン酸アルミニウム、亜
鉛、マグネシウムが好ましく使用される。該高級脂肪酸
のエステルとしては、脂肪族アルコールならいずれでも
良いが炭素数の多いアルコールを使用するのがブロッキ
ング防止には有利である。該高級脂肪酸のアミドとして
は、脂肪族アミンならいずれでも良いが加水分解時の毒
性について配慮する必要があり、それらを考慮するとス
テアリン酸アミド、パルミチン酸アミドが好ましい。
Examples of the carboxylic acids having 12 or more carbon atoms include monocarboxylic acids such as lauric acid, palmitic acid and stearic acid, and dicarboxylic acids such as dimer acid.
The metal ion of the metal salt includes aluminum, zinc, calcium, barium, and magnesium. Of these metal salts of higher fatty acids, aluminum, zinc and magnesium stearate are preferably used. As the ester of the higher fatty acid, any aliphatic alcohol may be used, but the use of an alcohol having a large number of carbon atoms is advantageous for preventing blocking. As the amide of the higher fatty acid, any aliphatic amine may be used, but it is necessary to consider the toxicity at the time of hydrolysis. In view of these, stearic amide and palmitic amide are preferable.

【0026】高級脂肪酸又はその金属塩、エステル、ア
ミドから選ばれた化合物の添加、配合量は既に記載の如
く発泡性粒子の表面に0.01〜1重量%、好ましくは
0.02〜0.1重量%配合することが必要である。
0.01重量%未満では実質的効果は認められず、1重
量%を越えるとブロッキング防止としての作用は十分で
あるが、例えば厚さ50mm以上の成形物を得ようとし
た場合成形物の表面層と内層とで均一な発泡粒子の融着
が困難となる。
As described above, the amount of the higher fatty acid or a compound selected from metal salts, esters, and amides thereof is 0.01 to 1% by weight, preferably 0.02 to 0. It is necessary to add 1% by weight.
When the content is less than 0.01% by weight, no substantial effect is recognized. When the content exceeds 1% by weight, the effect of preventing blocking is sufficient. It becomes difficult to uniformly fuse the expanded particles between the layer and the inner layer.

【0027】本発明の発泡性粒子に高級脂肪酸又はその
金属塩、エステル、アミドから選ばれた化合物を配合す
る方法としては、公知のいずれの方法で行っても良い
が、例えばタンブラーような回転式の混合機を使用する
と効率よく生産できる。混合時は発泡性粒子の温度が上
昇しないよう配慮することが好ましい。
The compound selected from the higher fatty acids or metal salts, esters and amides thereof may be added to the expandable particles of the present invention by any known method, for example, a rotary type such as a tumbler. If the mixer is used, it can be produced efficiently. It is preferable to take care not to raise the temperature of the expandable particles during mixing.

【0028】しかし、前述の仕様でタルクを単独に、又
は、高級脂肪酸又はその金属塩、エステル、アミドから
選ばれた化合物を単独に使用しても本発明の目的は達成
されない。本発明の目的の発泡粒子は、前述仕様のタル
クと前述仕様の高級脂肪酸又はその金属塩、エステル、
アミドから選ばれた化合物を併用し、相乗効果によりそ
の目的が初めて達成される。
However, the object of the present invention is not attained by using talc alone or the compound selected from higher fatty acids or metal salts, esters and amides according to the above specifications. Expanded particles for the purpose of the present invention, talc of the above specifications and higher fatty acids of the above specifications or their metal salts, esters,
The purpose is achieved for the first time by a synergistic effect by using a compound selected from amides in combination.

【0029】また、本発明の発泡粒子には、目的に応じ
その他の添加剤についても適宜添加することが出来、例
えば熱安定剤、酸化防止剤、難燃剤、紫外線吸収剤、可
塑剤等がある。但し、難燃剤等は塩素等のハロゲン化物
であることが多く、生分解性や焼却処分時の有害物質発
生という観点からその使用量は最小限に留めておくのが
よい。
Further, other additives can be appropriately added to the expanded particles of the present invention according to the purpose. Examples thereof include a heat stabilizer, an antioxidant, a flame retardant, an ultraviolet absorber, and a plasticizer. . However, the flame retardant or the like is often a halide such as chlorine, and the amount of the flame retardant is preferably minimized from the viewpoint of biodegradability and generation of harmful substances during incineration.

【0030】[0030]

【実施例】以下に実施例及び比較例により、本発明を更
に具体的に説明する。尚、評価は下記の方法で行った。
The present invention will be described more specifically with reference to the following examples and comparative examples. In addition, evaluation was performed by the following method.

【0031】(評価方法) ポリ乳酸のMI:JIS
K7210に準拠した方法で測定。(測定温度190
℃、オリフィス径2mm、2.16kg荷重の条件)
(Evaluation method) MI of polylactic acid: JIS
Measured by a method according to K7210. (Measurement temperature 190
℃, orifice diameter 2mm, 2.16kg load)

【0032】ポリ乳酸組成物のMI:JIS K721
0に準拠した方法で測定。(測定温度190℃、オリフ
ィス径2mm、21.6kg荷重の条件)
MI of polylactic acid composition: JIS K721
Measured according to method 0. (Measurement temperature 190 ° C, orifice diameter 2 mm, load of 21.6 kg)

【0033】発泡倍率:メスシリンダーを用いて、発泡
前の発泡性粒子の体積及び発泡粒子の体積を測定し、発
泡倍率を次式により求めた。 発泡倍率(倍)=予備発泡粒子の体積/発泡剤含浸ペレ
ットの体積
Expansion ratio: The volume of the expandable particles before expansion and the volume of the expanded particles were measured using a measuring cylinder, and the expansion ratio was determined by the following equation. Expansion ratio (times) = volume of pre-expanded particles / volume of pellets impregnated with blowing agent

【0034】発泡成形物の評価 引張強度:JIS K−6767に準じて測定。 試料:300×300×30mmの成形物から切り出し
て作成。 成形性評価:300×300×60mmの成形物又は3
00×300×30mmの成形物の中央部を切断し、成
形の均一性を目視で評価した。 表層と内層が同じ状態で均一に融着:○(良) 内層中心部に発泡粒子がやや融着性不十分で存在:△ 内層中心部に発泡粒子が明らかに融着性不十分で存在:
×(不可)
Evaluation of foamed molded article Tensile strength: Measured according to JIS K-6767. Sample: Prepared by cutting out from a molded product of 300 × 300 × 30 mm. Moldability evaluation: 300 × 300 × 60 mm molded product or 3
The central part of the molded product of 00 × 300 × 30 mm was cut, and the uniformity of molding was visually evaluated. The surface layer and the inner layer are uniformly fused in the same state: ○ (good) The foamed particles are slightly inadequately fusible at the center of the inner layer: 発 泡 The foamed particles are clearly poorly fusible in the center of the inner layer:
× (impossible)

【0035】耐熱性:上記成形物より100×100×
30mmの試験片を切り出し、60℃でオーブン中2時
間処理したときの寸法変化で評価した ◎:全く変化なし ○:1%以下の変化 △:1〜5%の変化 ×:5%以上の変化
Heat resistance: 100 × 100 ×
A test piece of 30 mm was cut out and evaluated by dimensional change when treated at 60 ° C. in an oven for 2 hours. :: No change at all 変 化: Change of 1% or less :: Change of 1 to 5% ×: Change of 5% or more

【0036】製造例1:ポリ乳酸の製造例 市販のL−ラクチド、D−ラクチドをそれぞれ酢酸エチ
ルを用いて再結晶して精製した。精製したL−ラクチ
ド、D―ラクチド及び触媒としてオクチル酸スズをスズ
として10ppm添加し、表1の組成になるように攪拌
機付きオートクレーブに仕込み、減圧脱気した後、N2
雰囲気下で各々の重合条件で開環重合した。反応終了
後、オートクレーブよりポリマーを取り出し、ポリマー
を得た。
Production Example 1: Production Example of Polylactic Acid Commercially available L-lactide and D-lactide were each purified by recrystallization using ethyl acetate. Purified L- lactide, stannous octoate as D- lactide and the catalyst was 10ppm added as tin, were charged into an autoclave equipped with a stirrer so that the composition of Table 1, after vacuum degassing, N 2
Ring-opening polymerization was performed under each polymerization condition under an atmosphere. After completion of the reaction, the polymer was taken out of the autoclave to obtain a polymer.

【0037】製造例2:ポリ乳酸組成物の製造例 次いで、該ポリマーを水分が1000ppm以下になる
まで乾燥させた後、種々の平均粒子径を有するタルクを
所定量、粘度増加剤として官能基の当量2.8のジフェ
ニルメタンポリイソシアネートを該ポリマーに対して1
重量%をブレンドした後、二軸混練機に供給し、回転数
100rpm、溶融温度180℃、滞留時間3〜5分、
吐出量10kg/時の条件下に反応混練した。得られた
ポリ乳酸組成物を切断し、直径約1.5mmの粒子を得
た。結果を表1に示した。
Production Example 2: Production Example of Polylactic Acid Composition Next, the polymer was dried until the water content became 1000 ppm or less, and then a predetermined amount of talc having various average particle diameters was added. 2.8 equivalents of diphenylmethane polyisocyanate was added to the polymer at 1 equivalent.
After blending the weight%, the mixture is supplied to a twin-screw kneader, the number of rotations is 100 rpm, the melting temperature is 180 ° C, the residence time is 3 to 5 minutes,
The reaction was kneaded under the conditions of a discharge rate of 10 kg / hour. The obtained polylactic acid composition was cut to obtain particles having a diameter of about 1.5 mm. The results are shown in Table 1.

【0038】[0038]

【表1】 [Table 1]

【0039】製造例3:発泡性粒子の製造例 製造例2に例示したポリ乳酸組成物1000部、イソペ
ンタン300部、メタノール50部を回転式オートクレ
ーブに仕込み、温度80〜90℃、回転数3rpm、2
時間保持した後冷却し、含浸率13〜20%の発泡性粒
子を得た。
Production Example 3: Production Example of Expandable Particles 1000 parts of the polylactic acid composition exemplified in Production Example 2, 300 parts of isopentane, and 50 parts of methanol were charged in a rotary autoclave, and the temperature was 80 to 90 ° C., the number of rotations was 3 rpm, 2
After keeping for a time, the mixture was cooled to obtain expandable particles having an impregnation ratio of 13 to 20%.

【0040】製造例4:発泡粒子の製造例 該発泡性粒子及び高級脂肪酸又はその金属塩、エステ
ル、アミドから選ばれた化合物を所定量予めブレンドし
た混合物を予備発泡機(ダイセン工業(株)DYHL−
300)に約3kg投入し、水蒸気にて80〜90℃に
30秒〜1分保持した。得られた発泡粒子を風乾した
後、目開き5mmの篩を使用し融着粒子と未融着の独立
粒子とを分別し、次式により未融着の独立粒子の取得率
を算出した。 独立粒子の取得率(%)=(独立粒子重量/処理した発
泡粒子重量)×100 ブロッキング性(%)=100−独立粒子の取得率
(%)
Production Example 4: Production Example of Expanded Particles A mixture obtained by preliminarily blending the expandable particles and a compound selected from a higher fatty acid or a metal salt, an ester, or an amide thereof in a predetermined amount is subjected to a prefoaming machine (DYHL Industrial Co., Ltd. DYHL). −
About 300 kg), and kept at 80 to 90 ° C. for 30 seconds to 1 minute with steam. After the obtained foamed particles were air-dried, the fused particles and the unfused independent particles were separated using a sieve having a mesh size of 5 mm, and the acquisition rate of the unfused independent particles was calculated by the following equation. Acquisition rate of independent particles (%) = (weight of independent particles / weight of treated expanded particles) × 100 Blocking property (%) = 100−acquisition rate of independent particles (%)

【0041】製造例5:成形物の製造例 発泡成形機(ダイセン工業(株)DS−300L−M
C)に300×300×30mm又は300×300×
60mmの金型を設置し、製造例4に例示した発泡粒子
を24時間エージングした後充填し、スチーム圧0.5
kgf/cm2、10〜30秒処理し成形加工し成形物
を得た。
Production Example 5: Production Example of Molded Product Foam molding machine (DS-300L-M, Daisen Industries Co., Ltd.)
C) 300x300x30mm or 300x300x
A mold having a size of 60 mm was set, and the foamed particles exemplified in Production Example 4 were aged for 24 hours and then filled, and then steam pressure was 0.5
The mixture was treated at a rate of 10 kg / cm 2 for 10 to 30 seconds and molded to obtain a molded product.

【0042】実施例1〜4、比較例1〜2 製造例1、2に例示した方法により製造したポリ乳酸組
成物P1,P2,P6,P15,P16,P17を、製
造例3に例示した方法により発泡性粒子を得、該粒子に
ステアリン酸マグネシウム0.05重量%をブレンド
し、製造例4に例示した方法によりそれぞれの発泡粒子
を得、発泡倍率及びブロッキング性を評価し、該発泡粒
子を製造例5に例示した方法により得られる成形物の耐
熱性を評価した。
Examples 1-4, Comparative Examples 1-2 Polylactic acid compositions P1, P2, P6, P15, P16 and P17 produced by the methods exemplified in Production Examples 1 and 2 were prepared by the method exemplified in Production Example 3. The foamed particles are obtained by blending 0.05% by weight of magnesium stearate with the particles, and the respective foamed particles are obtained by the method exemplified in Production Example 4, and the expansion ratio and the blocking property are evaluated. The heat resistance of the molded product obtained by the method exemplified in Production Example 5 was evaluated.

【0043】[0043]

【表2】 [Table 2]

【0044】評価結果 P1は結晶性、且つ、結晶化度が高いため、発泡倍率が
極端に低く発泡体としては使用できない。P2は結晶化
度がP1に比して非常に小さいため発泡性は向上し、ブ
ロッキング性、耐熱性ともに良好であった。P6,P1
5,P16はいずれも完全非晶であるため、発泡性は良
好であり、ブロッキング性、耐熱性も良好であった。し
かし、P17は非晶性であるにもかかわらず、樹脂の耐
熱性がやや低下傾向にあり、発泡性が減少し、ブロッキ
ング性悪化が認められた。更に、成形体の耐熱性も不良
であった。
Evaluation Results Since P1 has high crystallinity and high crystallinity, it has an extremely low expansion ratio and cannot be used as a foam. Since the crystallinity of P2 was very small as compared with that of P1, the foaming property was improved, and both the blocking property and the heat resistance were good. P6, P1
5 and P16 were completely amorphous, and thus had good foaming properties and good blocking properties and heat resistance. However, despite the fact that P17 was amorphous, the heat resistance of the resin tended to decrease slightly, the foaming property was reduced, and the blocking property was deteriorated. Further, the heat resistance of the molded product was also poor.

【0045】実施例2,5〜10、比較例3〜5 製造例1、2に例示した方法により製造したポリ乳酸組
成物P3〜P11を、製造例3に例示した方法により発
泡性粒子を得、該粒子にステアリン酸マグネシウム0.
05重量%をブレンドし、製造例4に例示した方法によ
りそれぞれの発泡粒子を得、発泡倍率及びブロッキング
性を評価し、該発泡粒子を製造例5に例示した方法によ
り得られる成形物の耐熱性を評価した。ただし、比較例
5ではステアリン酸マグネシウムは添加しなかった。
Examples 2 to 5 and Comparative Examples 3 to 5 The polylactic acid compositions P3 to P11 produced by the methods exemplified in Production Examples 1 and 2 were used to obtain expandable particles by the method exemplified in Production Example 3. , The particles contain magnesium stearate.
The foamed particles were blended in an amount of 0.05% by weight, and the respective foamed particles were obtained by the method exemplified in Production Example 4. The expansion ratio and the blocking property were evaluated. Was evaluated. However, in Comparative Example 5, magnesium stearate was not added.

【0046】[0046]

【表3】 [Table 3]

【0047】評価結果 比較例3は非晶性ポリ乳酸組成物P3を使用しているに
もかかわらず、ブロッキング性が高く生産効率が低い。
この原因は、タルクの添加量が0.5重量%と低い為で
あり、発泡倍率も低め傾向であった。タルクの添加量と
共にブロッキング性は減少し、P4〜P10に示したよ
うに1重量%、とりわけ通常使用されない範囲である2
重量%以上ではブロッキング性は大幅に改善された。発
泡倍率も同様な傾向があり、成形物の評価も良好であっ
た。。一方、P11のタルク添加量が20重量%を越え
ると、ブロッキング性は良好であるものの、発泡倍率が
低下した。更に、比較例5に示したようにP6樹脂組成
物を使用しても、ステアリン酸マグネシウムを添加しな
いとブロッキング性が非常に高く、生産性不良で使用で
きない。
Evaluation Results In Comparative Example 3, although the amorphous polylactic acid composition P3 was used, the blocking property was high and the production efficiency was low.
This is because the amount of talc added was as low as 0.5% by weight, and the expansion ratio also tended to be low. The blocking property decreases with the addition amount of talc, and as shown in P4 to P10, 1% by weight, especially in a range not usually used.
Above the weight%, the blocking properties were significantly improved. The expansion ratio also had the same tendency, and the evaluation of the molded product was good. . On the other hand, when the talc addition amount of P11 exceeds 20% by weight, the blocking ratio is good, but the expansion ratio decreases. Furthermore, as shown in Comparative Example 5, even if the P6 resin composition is used, the blocking property is extremely high unless magnesium stearate is added, and the product cannot be used due to poor productivity.

【0048】実施例2,11〜12、比較例6 製造例1、2に例示した方法により製造したポリ乳酸組
成物P6,P12〜P13を、製造例3に例示した方法
により発泡性粒子を得、該粒子にステアリン酸亜鉛0.
05重量%をブレンドし、製造例4に例示した方法によ
りそれぞれの発泡粒子を得、発泡倍率及びブロッキング
性を評価し、該発泡粒子を製造例5に例示した方法によ
り得られる成形物の耐熱性を評価した。
Examples 2, 11 to 12, Comparative Example 6 Expandable particles were obtained from the polylactic acid compositions P6, P12 to P13 produced by the methods exemplified in Production Examples 1 and 2 by the method exemplified in Production Example 3. , The particles containing zinc stearate at 0.
The foamed particles were blended in an amount of 0.05% by weight, and the respective foamed particles were obtained by the method exemplified in Production Example 4. The expansion ratio and the blocking property were evaluated. Was evaluated.

【0049】[0049]

【表4】 [Table 4]

【0050】評価結果 タルクの粒子径を変更してもステアリン酸亜鉛が無添加
の場合は比較例6に示すようにブロッキング性が悪く使
用できない。
Evaluation Results Even if the particle size of talc was changed, when zinc stearate was not added, as shown in Comparative Example 6, the blocking property was poor and it could not be used.

【0051】実施例2,13〜26、比較例7〜10 製造例1、2に例示した方法により製造したポリ乳酸組
成物P6を、製造例3に例示した方法により発泡性粒子
を得、該粒子に高級脂肪酸又はその金属塩、エステル、
アミドから選ばれた化合物を所定量ブレンドし、製造例
4に例示した方法によりそれぞれの発泡粒子を得、発泡
倍率及びブロッキング性を評価し、該発泡粒子を製造例
5に例示した方法により得られる成形物の耐熱性を評価
した。
Examples 2, 13 to 26, Comparative Examples 7 to 10 The polylactic acid composition P6 produced by the method exemplified in Production Examples 1 and 2 was used to obtain expandable particles by the method exemplified in Production Example 3. Higher fatty acids or metal salts, esters,
A predetermined amount of a compound selected from amides is blended, each expanded particle is obtained by the method exemplified in Production Example 4, the expansion ratio and the blocking property are evaluated, and the expanded particles are obtained by the method exemplified in Production Example 5. The heat resistance of the molded product was evaluated.

【0052】[0052]

【表5】 [Table 5]

【0053】評価結果 高級脂肪酸で炭素数12未満の脂肪酸は不快臭(比較例
7、8)があり、包装材としては使用できない。炭素数
12以上の高級脂肪酸は不快臭も殆どなく、これら高級
脂肪酸を0.05重量%ブレンドしたものは、実施例1
3,14,15にみられるようにブロッキング性発泡倍
率、成形物評価いずれも良好であった。脂肪酸の金属塩
について種々評価した結果、金属塩としてはマグネシウ
ム、亜鉛、アルミニウム、カルシウムの塩が好ましい結
果が得られた。これらのステアリン酸塩、ブレンド量
0.05重量%の例を実施例2、実施例21〜23に示
した。一方、高級脂肪酸金属塩のブレンド量について検
討した結果、0.01重量%未満ではブロッキング性の
改善があまり期待できず、0.01重量%以上で急激に
改善され、発泡倍率、成形物評価も良好であった。しか
し、ブレンド量が1重量%を越えるものはブロッキング
性は良好であるが、成形時における発泡粒子の融着性が
低下し、成形表面と内層とで発泡粒子の融着に差が生じ
た。特に、厚さ50mm以上の成形物で顕著であった
(比較例9,10、実施例2,16〜20)。更にブレ
ンド量が1重量%を越えるものは機械強度も急激に低下
した。
Evaluation Results Higher fatty acids having less than 12 carbon atoms have an unpleasant odor (Comparative Examples 7 and 8) and cannot be used as a packaging material. Higher fatty acids having 12 or more carbon atoms have almost no unpleasant odor, and those obtained by blending 0.05% by weight of these higher fatty acids are described in Example 1.
As seen in 3, 14, and 15, both the blocking expansion ratio and the molded product evaluation were good. As a result of various evaluations of fatty acid metal salts, magnesium, zinc, aluminum, and calcium salts were preferable. Examples of these stearates and a blend amount of 0.05% by weight are shown in Example 2 and Examples 21 to 23. On the other hand, as a result of examining the blending amount of the higher fatty acid metal salt, if the amount is less than 0.01% by weight, the improvement of the blocking property cannot be expected so much. It was good. However, when the blending amount exceeds 1% by weight, the blocking property is good, but the fusion property of the foamed particles at the time of molding is reduced, and a difference occurs in the fusion of the foamed particles between the molding surface and the inner layer. In particular, it was remarkable in a molded product having a thickness of 50 mm or more (Comparative Examples 9, 10 and Examples 2, 16 to 20). Further, those having a blend amount of more than 1% by weight showed a sharp decrease in mechanical strength.

【0054】[0054]

【発明の効果】以上、本発明の生分解を有する発泡粒子
及びその成形物は、包装材料としての機能を十分保有し
ており発泡性、耐熱性、機械物性等、従来から用いられ
てきた発泡ポリスチレン(PS)と同程度のものが生産
効率よく得られ、地球環境保全に資するものである。
As described above, the biodegradable foamed particles of the present invention and the molded product thereof have a sufficient function as a packaging material, and have been used for foaming, heat resistance and mechanical properties. Polystyrene (PS) can be obtained at a high production efficiency and contributes to global environmental protection.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉本 聖 山口県防府市鐘紡町4番1号 カネボウ合 繊株式会社内 (72)発明者 山 真弘 山口県防府市鐘紡町4番1号 カネボウ合 繊株式会社内 (72)発明者 中江 綱大 山口県防府市大字大崎276番地の516 Fターム(参考) 3E033 AA20 BA13 BB04 CA20 4F074 AA65 AC32 AD10 AD11 AD13 BA35 BA36 BA37 BA38 BA39 BA44 BA45 BA53 BA75 BC11 CA32 CA34 CA45 CC47 DA02 DA08 DA33  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Satoshi Yoshimoto 4-1 Kanebo-cho, Hofu-shi, Yamaguchi Prefecture Inside Kanebo Goden Co., Ltd. (72) Inventor Masahiro 4-1 4-1 Kanebo-cho, Hofu City, Yamaguchi Prefecture Kanebo God Co., Ltd. (72) Inventor Tsunadai Nakae 516 F-term at 276 Osaki, Hofu City, Yamaguchi Prefecture (Reference) 3E033 AA20 BA13 BB04 CA20 4F074 AA65 AC32 AD10 AD11 AD13 BA35 BA36 BA37 BA38 BA39 BA44 BA45 BA53 BA75 BC11 CA32 CA34 CA45 CC47 DA02 DA08 DA33

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 L体とD体からなる実質的に非晶性のポ
リ乳酸を主体とする発泡粒子であって、該ポリ乳酸がL
体とD体との比が95/5〜60/40の範囲にあり、
予め増粘剤と発泡核剤としてタルクを1〜20重量%混
合、分散させた非晶性ポリ乳酸組成物に低沸点有機化合
物を含浸させた発泡性粒子の表面に高級脂肪酸又はその
金属塩、エステル、アミドから選ばれた化合物を0.0
1〜1重量%を配合して得られることを特徴とする発泡
粒子。
1. A foamed particle mainly composed of substantially amorphous polylactic acid comprising an L-form and a D-form, wherein said polylactic acid is L-form.
The ratio of body to D-form is in the range of 95/5 to 60/40,
A higher fatty acid or a metal salt thereof on the surface of expandable particles obtained by impregnating a low-boiling organic compound into an amorphous polylactic acid composition in which 1 to 20% by weight of talc is previously mixed and dispersed as a thickener and a foam nucleating agent; 0.0% of a compound selected from an ester and an amide
A foamed particle obtained by mixing 1 to 1% by weight.
【請求項2】 L体とD体との比が92/8〜80/2
0の範囲にあるポリ乳酸を使用することを特徴とする請
求項1に記載の発泡粒子。
2. The ratio between L-form and D-form is 92/8 to 80/2.
The foamed particles according to claim 1, wherein polylactic acid in the range of 0 is used.
【請求項3】 タルクの配合量がポリ乳酸に対して2〜
10重量%であることを特徴とする請求項1に記載の発
泡粒子。
3. The compounding amount of talc is 2 to polylactic acid.
The foamed particle according to claim 1, wherein the content is 10% by weight.
【請求項4】 高級脂肪酸の金属塩化合物がステアリン
酸マグネシウム、亜鉛又はアルミニウムから選ばれる群
であることを特徴とする請求項1に記載の発泡粒子。
4. The expanded particles according to claim 1, wherein the metal salt compound of a higher fatty acid is a group selected from magnesium stearate, zinc and aluminum.
【請求項5】 高級脂肪酸のエステル化合物がステアリ
ン酸又は脂肪族アルコールとのエステルであることを特
徴とする請求項1に記載の発泡粒子。
5. The expanded particles according to claim 1, wherein the ester compound of a higher fatty acid is an ester with stearic acid or an aliphatic alcohol.
【請求項6】 高級脂肪酸のアミド化合物がステアリン
酸アミドであることを特徴とする請求項1に記載の発泡
粒子。
6. The foamed particles according to claim 1, wherein the amide compound of a higher fatty acid is stearic acid amide.
【請求項7】 請求項1乃至6に記載の発泡粒子よりな
る成形物。
7. A molded article comprising the expanded particles according to claim 1.
JP27779099A 1999-09-30 1999-09-30 Biodegradable expanded particles and molded products thereof Pending JP2001098104A (en)

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