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JP2008239728A - Method for producing polylactic acid foamed molding - Google Patents

Method for producing polylactic acid foamed molding Download PDF

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JP2008239728A
JP2008239728A JP2007080700A JP2007080700A JP2008239728A JP 2008239728 A JP2008239728 A JP 2008239728A JP 2007080700 A JP2007080700 A JP 2007080700A JP 2007080700 A JP2007080700 A JP 2007080700A JP 2008239728 A JP2008239728 A JP 2008239728A
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polylactic acid
foamed molded
molded article
carbon dioxide
volatile content
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Keisuke Okuma
敬介 大熊
Tomonori Furukawa
友紀 古川
Yoshihito Yano
義仁 矢野
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Kaneka Corp
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Kaneka Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a simple method for producing a low-volatile content polylactic acid foamed molding excellent in dimensional stability under high-temperature high-humidity conditions and to provide a molding produced thereby. <P>SOLUTION: A low-volatile content polylactic acid foamed molding is produced by subjecting a polylactic acid foamed molding containing a hydrocarbon blowing agent to treatment with carbon dioxide. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、ポリ乳酸系発泡成形体の製造方法に関する。   The present invention relates to a method for producing a polylactic acid-based foamed molded article.

化石資源を原料とする発泡ポリスチレン、発泡ポリオレフィンの代替として、特許文献1において、ポリ乳酸を主たる原料とする発泡成形体が提案されている。この発泡成形体は、非石油資源である澱粉を出発原料としており、近年の石油事情、環境保全の見地から見て非常に望ましいものであると言える。当該発泡成形体は、発泡ポリスチレンと同等の機械物性、2次加工性を有しており、通常の梱包用緩衝材として十分使用できるものであった。しかしながら、特許文献1の発泡成形体は、発泡剤などの揮発分が多量に残留しており、そのため高温高湿条件下では著しく体積変化し、海外輸出等の過酷な条件下では使用できないという欠点があった。   As an alternative to expanded polystyrene and expanded polyolefin using a fossil resource as a raw material, Patent Document 1 proposes an expanded molded body using polylactic acid as a main raw material. This foamed molded article uses starch, which is a non-petroleum resource, as a starting material, and can be said to be very desirable from the viewpoint of recent petroleum circumstances and environmental conservation. The foamed molded article had mechanical properties and secondary processability equivalent to those of expanded polystyrene, and could be sufficiently used as a normal packing cushioning material. However, the foamed molded article of Patent Document 1 has a large amount of volatile components such as a foaming agent remaining, so that the volume changes significantly under high temperature and high humidity conditions, and cannot be used under severe conditions such as overseas export. was there.

ポリ乳酸系発泡成形体に耐熱性を付与する技術について、特許文献2では、炭素数3−5の炭化水素系発泡剤の含有量が0.5mol/kg(対樹脂)未満であるポリ乳酸系発泡成形体を作製することで、高温高湿条件下(60℃×80%RH)の体積膨張率を20%以下にすることができる技術が開示されている。具体的には、(1)低い発泡倍率になるが、最初の発泡剤の含有量を低減させる方法、(2)予備発泡を複数回繰り返し行うことにより段階的に残留発泡剤を低減させる方法、(3)発泡体にアルコール等の膨潤剤を塗布又は浸漬し乾燥する方法等により、成形体中の発泡剤含有量を0.5mol/kg(対樹脂)未満としており、何れも時間のかかる工程が増えて生産性が低下するし、実施例における具体的な開示では、成形体中の発泡剤含有量の下限値は0.21mol/kg(対樹脂)であった。   Regarding the technology for imparting heat resistance to a polylactic acid-based foamed molded article, in Patent Document 2, the content of the hydrocarbon-based foaming agent having 3 to 5 carbon atoms is less than 0.5 mol / kg (vs. resin). A technique is disclosed in which the volume expansion coefficient under high-temperature and high-humidity conditions (60 ° C. × 80% RH) can be reduced to 20% or less by producing a foamed molded article. Specifically, (1) the foaming ratio is low, but the method of reducing the content of the first foaming agent, (2) the method of reducing the residual foaming agent stepwise by repeating pre-foaming multiple times, (3) The foaming agent content in the molded body is less than 0.5 mol / kg (vs. resin) by applying or dipping a swelling agent such as alcohol on the foam and drying, etc., both of which take time As a result, the lowering of the foaming agent content in the molded product was 0.21 mol / kg (vs. resin).

以上のように、ポリ乳酸系発泡成形体に耐熱性を付与する技術はいくつかあるが、より簡便な方法が望まれている。
国際公開第99/21915号パンフレット 特開2005−105097号公報
As described above, there are several techniques for imparting heat resistance to the polylactic acid-based foamed molded article, but a simpler method is desired.
International Publication No. 99/21915 Pamphlet JP 2005-105097 A

高温高湿条件下での寸法安定性に優れた揮発分含有量が低減されたポリ乳酸系発泡成形体の簡便な製造方法およびそれに係る成形体を提供することである。   It is an object of the present invention to provide a simple method for producing a polylactic acid-based foamed molded article having excellent dimensional stability under high-temperature and high-humidity conditions and having a reduced volatile content, and a molded article related thereto.

本発明者らは、上述の課題を解決すべく鋭意研究を重ねた結果、炭化水素系発泡剤を含有するポリ乳酸系発泡成形体に対し、特定の条件で二酸化炭素処理を行うことで、ポリ乳酸系発泡成形体の炭化水素系発泡剤の含有量が減少し、高温高湿条件(60℃×80%RH)下での体積変化率が著しく改善された揮発分含有量が低減された発泡成形体が得られることを見出し、本発明を完成するに至った。   As a result of intensive studies to solve the above-mentioned problems, the present inventors have conducted a carbon dioxide treatment under specific conditions on a polylactic acid-based foamed molded article containing a hydrocarbon-based foaming agent. Foam with reduced volatile content, with a reduced volume content of hydrocarbon-based foaming agent in lactic acid-based foamed moldings and a significant improvement in volume change rate under high temperature and high humidity conditions (60 ° C x 80% RH) The present inventors have found that a molded body can be obtained and have completed the present invention.

即ち、本発明の第一は、炭化水素系発泡剤を含有するポリ乳酸系発泡成形体に対し、二酸化炭素処理を行うことを特徴とする揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法に関する。好ましい実施態様は、二酸化炭素処理が、ポリ乳酸系発泡成形体を0.1MPa以上、2.0MPa未満の圧力の二酸化炭素雰囲気下に曝すことを特徴とする上記記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法に関する。より好ましくは、二酸化炭素処理が、ポリ乳酸系発泡成形体を0.5分間以上、10分間未満の時間で二酸化炭素雰囲気下に曝すことを特徴とする上記記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法、更に好ましくは、炭化水素系発泡剤が炭素数3−6の脂肪族炭化水素である上記記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法、特に好ましくは、ポリ乳酸系発泡成形体が、ポリ乳酸系樹脂を主成分としており、該ポリ乳酸系樹脂をゲル化処理したものである上記記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法、に関する。   That is, the first of the present invention is a polylactic acid-based foamed molded article having a reduced volatile content, characterized by performing carbon dioxide treatment on a polylactic acid-based foamed molded article containing a hydrocarbon-based foaming agent. It relates to the manufacturing method. In a preferred embodiment, the carbon dioxide treatment is performed by exposing the polylactic acid-based foamed molded article to a carbon dioxide atmosphere having a pressure of 0.1 MPa or more and less than 2.0 MPa. The present invention also relates to a method for producing a polylactic acid-based foamed molded article. More preferably, the carbon dioxide treatment exposes the polylactic acid-based foamed molded article to a carbon dioxide atmosphere in a time of 0.5 minutes or more and less than 10 minutes, and the volatile content is reduced as described above A process for producing a polylactic acid-based foamed molded article, more preferably, the polylactic acid-based foamed molded article having a reduced volatile content as described above, wherein the hydrocarbon-based foaming agent is an aliphatic hydrocarbon having 3 to 6 carbon atoms. A production method, particularly preferably, a polylactic acid-based foamed molded article comprising a polylactic acid-based resin as a main component and gelling treatment of the polylactic acid-based resin as described above. The present invention relates to a method for producing a lactic acid-based foamed molded article.

本発明の製造方法によれば、高温高湿条件下での寸法安定性に優れる揮発分含有量が低減されたポリ乳酸系発泡成形体の簡便な製造方法およびそれに係る成形体を提供することができる。   According to the production method of the present invention, it is possible to provide a simple production method of a polylactic acid-based foamed molded article having a reduced volatile content which is excellent in dimensional stability under high temperature and high humidity conditions, and a molded article related thereto. it can.

以下、本発明につき、さらに詳細に説明する。本発明の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法は、炭化水素系発泡剤を用いて作製されたポリ乳酸系発泡成形体に、特定の条件で二酸化炭素処理を行うことを特徴とする。該ポリ乳酸系発泡成形体は、基材樹脂がポリ乳酸系樹脂であり、基材樹脂中には本発明の効果を阻害しない範囲においては、ポリ乳酸系樹脂に他の樹脂を含有しても良く、さらには着色顔料又は染料、難燃剤、帯電防止剤、耐候剤、末端封鎖剤などの添加剤を添加しても良い。   Hereinafter, the present invention will be described in more detail. In the method for producing a polylactic acid-based foam molded article with a reduced volatile content according to the present invention, carbon dioxide treatment is performed on a polylactic acid-based foam molded article produced using a hydrocarbon-based foaming agent under specific conditions. It is characterized by that. In the polylactic acid-based foam molded article, the base resin is a polylactic acid-based resin, and the base resin may contain other resins in the polylactic acid-based resin as long as the effects of the present invention are not impaired. In addition, additives such as coloring pigments or dyes, flame retardants, antistatic agents, weathering agents, and end-capping agents may be added.

本発明におけるポリ乳酸系発泡成形体とは、基材樹脂がポリ乳酸系樹脂の発泡成形体である。該ポリ乳酸系樹脂は、特に限定はないが、結晶性の高い樹脂は発泡、成形が結晶化により困難になる場合があるため、乳酸成分の異性体比率が好ましくは5%以上、より好ましくは8%以上であるポリ乳酸を主成分としたものである。本発明の効果を阻害しない範囲においては、ポリ乳酸系樹脂に他の樹脂を添加して基材樹脂とする事ができる。基材樹脂全体中にはポリ乳酸系樹脂が50重量%以上含まれることが好ましく、より好ましくは70重量%以上、更に好ましくは90重量%以上である。前記他の樹脂としては、ポリエチレン系樹脂、ポリプロピレン系樹脂、ポリスチレン系樹脂、ポリエステル系樹脂、アクリル系樹脂、ビニル系樹脂、生分解性脂肪族ポリエステル系樹脂等が挙げられ、それらの群より選ばれる少なくとも1種用いることができる。該生分解性脂肪族ポリエステル系樹脂としては、脂肪族ポリエステル成分単位を少なくとも35モル%以上含む生分解性脂肪族ポリエステル系樹脂が挙げられ、この場合の脂肪族ポリエステル系樹脂としては、ヒドロキシ酸重縮合物、ポリカプロラクトン等のラクトンの開環重合物、ポリブチレンサクシネート、ポリブチレンアジペート、ポリブチレンサクシネートアジペート、ポリ(ブチレンアジペート/テレフタレート)等の脂肪族多価アルコールと脂肪族カルボン酸との重縮合物が挙げられ、それらの群より選ばれる少なくとも1種用いることができる。   The polylactic acid-based foamed molded product in the present invention is a foamed molded product in which the base resin is a polylactic acid-based resin. The polylactic acid-based resin is not particularly limited. However, since a resin having high crystallinity may be difficult to foam and mold due to crystallization, the isomer ratio of the lactic acid component is preferably 5% or more, more preferably The main component is 8% or more of polylactic acid. As long as the effects of the present invention are not impaired, other resins can be added to the polylactic acid resin to form a base resin. The whole base resin preferably contains 50% by weight or more of polylactic acid resin, more preferably 70% by weight or more, and still more preferably 90% by weight or more. Examples of the other resins include polyethylene resins, polypropylene resins, polystyrene resins, polyester resins, acrylic resins, vinyl resins, biodegradable aliphatic polyester resins, and the like, selected from these groups. At least one kind can be used. Examples of the biodegradable aliphatic polyester-based resin include biodegradable aliphatic polyester-based resins containing at least 35 mol% of aliphatic polyester component units. Condensates, ring-opening polymers of lactones such as polycaprolactone, polybutylene succinates, polybutylene adipates, polybutylene succinate adipates, poly (butylene adipates / terephthalates) and other aliphatic polyhydric alcohols and aliphatic carboxylic acids A polycondensate is mentioned, At least 1 sort (s) chosen from those groups can be used.

また前記ポリ乳酸系樹脂は、一部モノマーが乳酸と交換可能な脂肪族ヒドロキシカルボン酸、脂肪族多価カルボン酸、脂肪族多価アルコール等で置き換わった共重合体でもよく、エポキシ化大豆油やエポキシ化亜麻仁で一部架橋されていてもよい。   The polylactic acid-based resin may be a copolymer in which a part of the monomer is replaced with an aliphatic hydroxycarboxylic acid, an aliphatic polyvalent carboxylic acid, an aliphatic polyhydric alcohol or the like that can be exchanged with lactic acid. It may be partially crosslinked with epoxidized flaxseed.

前記脂肪族ヒドロキシカルボン酸としては、グリコール酸、ヒドロキシ酪酸、ヒドロキシ吉酸、ヒドロキシカプロン酸、ヒドロキシヘプタン酸等が挙げられ、それらの群より選ばれる少なくとも1種が用いられる。また、前記脂肪族多価カルボン酸としては、コハク酸、アジピン酸、スベリン酸、セバシン酸、ドデカンジカルボン酸、無水コハク酸、無水アジピン酸、トリメシン酸、プロパントリカルボン酸、ピロメリット酸、無水ピロメリット酸等が挙げられ、それらの群より選ばれる少なくとも1種が用いられる。また、前記脂肪族多価アルコールとしては、エチレングリコール、1,4−ブタンジオール、1,6−ヘキサンジオール、1,4−シクロヘキサンジメタノール、ネオペンチルグリコール、デカメチレングリコール、グリセリン、トリメチロールプロパン、ペンタエリトリット等が挙げられ、それらの群より選ばれる少なくとも1種が用いられる。   Examples of the aliphatic hydroxycarboxylic acid include glycolic acid, hydroxybutyric acid, hydroxyvalic acid, hydroxycaproic acid, hydroxyheptanoic acid, and the like, and at least one selected from these groups is used. Examples of the aliphatic polyvalent carboxylic acid include succinic acid, adipic acid, suberic acid, sebacic acid, dodecanedicarboxylic acid, succinic anhydride, adipic anhydride, trimesic acid, propanetricarboxylic acid, pyromellitic anhydride, pyromellitic anhydride An acid etc. are mentioned, At least 1 sort (s) chosen from those groups is used. Examples of the aliphatic polyhydric alcohol include ethylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,4-cyclohexanedimethanol, neopentyl glycol, decamethylene glycol, glycerin, trimethylolpropane, Examples include pentaerythritol, and at least one selected from the group is used.

前記ポリ乳酸系樹脂の溶融粘度は、JIS K 7210(荷重2.16kg)に準拠したメルトインデックス(MI)値で0.1〜10g/10分の高分子量のポリ乳酸系樹脂であることが好ましい。MI値がこの範囲にあれば、生産性に優れ、発泡倍率の高い発泡成形体を得やすい傾向にあり、本発明の目的・効果を有効に得ることができる。   The melt viscosity of the polylactic acid resin is preferably a high molecular weight polylactic acid resin having a melt index (MI) value of 0.1 to 10 g / 10 min in accordance with JIS K 7210 (load 2.16 kg). . If the MI value is within this range, it tends to be easy to obtain a foamed molded article having excellent productivity and a high expansion ratio, and the object and effect of the present invention can be obtained effectively.

本発明においては、ポリ乳酸系発泡成形体の基材樹脂であるポリ乳酸系樹脂をゲル化処理することが、発泡性、成形性の観点から好ましい。ゲル化処理によりポリ乳酸系樹脂を発泡に適する粘度領域まで増粘させることができる。このためのゲル化処理には、従来公知の各種の方法、例えば、ポリイソシアネート化合物、過酸化物、酸無水物、エポキシ化合物等、一般的な架橋剤を少なくとも1種選択して用いる方法、電子線架橋方法、シラン架橋方法等が包含されるが、上記の中でも架橋剤を用いる方法が好ましい。   In the present invention, it is preferable from the viewpoints of foamability and moldability that the polylactic acid resin, which is the base resin of the polylactic acid foam molded article, is subjected to gelation treatment. The gelation treatment can increase the viscosity of the polylactic acid resin to a viscosity range suitable for foaming. For this gelation treatment, various conventionally known methods, for example, a method of selecting and using at least one general crosslinking agent such as a polyisocyanate compound, a peroxide, an acid anhydride, and an epoxy compound, an electron Although a wire cross-linking method, a silane cross-linking method, and the like are included, among them, the method using a cross-linking agent is preferable.

前記ポリイソシアネート化合物としては、芳香族、脂環族、脂肪族系のポリイソシアネート化合物が使用可能であり、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、トリフェニルメタンを骨格とするポリイソシアネート化合物が挙げられる。また、脂環族ポリイソシアネートとしては、イソホロン、水酸化ジフェニルメタンを骨格とするポリイソシアネート化合物が挙げられ、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化合物が挙げられる。   As the polyisocyanate compound, aromatic, alicyclic and aliphatic polyisocyanate compounds can be used. As the aromatic polyisocyanate, polyisocyanate compounds having a skeleton of tolylene, diphenylmethane, naphthylene and triphenylmethane. Is mentioned. Examples of the alicyclic polyisocyanate include polyisocyanate compounds having isophorone and diphenylmethane hydroxide as a skeleton, and examples of the aliphatic polyisocyanate include polyisocyanate compounds having hexamethylene and lysine as a skeleton.

前記過酸化物としては、ベンゾイルパーオキサイド、ビス(ブチルパーオキシ)トリメチルシクロヘキサン、ビス(ブチルパーオキシ)シクロドデカン、ブチルビス(ブチルパーオキシ)バレレート、ジクミルパーオキサイド、ブチルパーオキシベンゾエート、ジブチルパーオキサイド、ビス(ブチルパーオキシ)ジイソプロピルベンゼン、ジメチルジ(ブチルパーオキシ)ヘキサン、ジメチルジ(ブチルパーオキシ)ヘキシン、ブチルパーオキシクメン等の有機化酸化物が挙げられる。   Examples of the peroxide include benzoyl peroxide, bis (butylperoxy) trimethylcyclohexane, bis (butylperoxy) cyclododecane, butylbis (butylperoxy) valerate, dicumyl peroxide, butylperoxybenzoate, and dibutyl peroxide. And organic oxides such as bis (butylperoxy) diisopropylbenzene, dimethyldi (butylperoxy) hexane, dimethyldi (butylperoxy) hexyne, and butylperoxycumene.

前記酸無水物としては、無水トリメリット酸、無水ピロメリット酸、エチレン−無水マレイン酸共重合体、メチルビニルエーテル−無水マレイン酸共重合体、スチレン−無水マレイン酸共重合体等が挙げられる。   Examples of the acid anhydride include trimellitic anhydride, pyromellitic anhydride, ethylene-maleic anhydride copolymer, methyl vinyl ether-maleic anhydride copolymer, styrene-maleic anhydride copolymer, and the like.

前記エポキシ化合物としては、グリシジルメタクリレート−メチルメタクリレート共重合体、グリシジルメタクリレート−スチレン共重合体、グリシジルメタクリレート−スチレン−ブチルアクリレート共重合体、ポリエチレングリコールジグリシジルエーテル、トリメチロールプロパンポリグリシジルエーテル、ヤシ脂肪酸グリシジルエステル、エポキシ化大豆油、エポキシ化アマニ油等の各種グリシジルエーテル及び各種グリシジルエステル等が挙げられる。   Examples of the epoxy compound include glycidyl methacrylate-methyl methacrylate copolymer, glycidyl methacrylate-styrene copolymer, glycidyl methacrylate-styrene-butyl acrylate copolymer, polyethylene glycol diglycidyl ether, trimethylolpropane polyglycidyl ether, coconut fatty acid glycidyl. Examples thereof include various glycidyl ethers such as esters, epoxidized soybean oil, and epoxidized linseed oil, and various glycidyl esters.

前記架橋剤のうち、ポリイソシアネート化合物を用いることが好ましい。その理由は、ポリイソシアネート化合物を用いれば、混練時の架橋増粘によるトルクアップが少なく、混練後に水分の存在下で加熱することで尿素結合、ウレタン結合、アロファネート結合などによる後増粘が可能になるからである。ポリイソシアネート化合物の中でも、汎用性、取り扱い性、耐候性等の観点からトリレン、ジフェニルメタン骨格とするポリイソシアネート化合物、特にジフェニルメタンのポリイソシアネートを使用することが好ましい。架橋剤の添加量は、任意に選定することが可能であるが、ポリ乳酸系樹脂100重量部に対して0.1重量部〜6.0重量部であることが好ましく、より好ましくは0.2重量部〜5.0重量部、更に好ましくは0.5重量部〜4.0重量部である。添加量が0.1重量部〜6.0重量部の場合、ポリ乳酸系樹脂の溶融粘度を発泡に適した領域まで上昇させることができる。   Of the cross-linking agents, polyisocyanate compounds are preferably used. The reason is that if a polyisocyanate compound is used, torque increase due to cross-linking thickening during kneading is small, and post-thickening due to urea bond, urethane bond, allophanate bond, etc. is possible by heating in the presence of moisture after kneading. Because it becomes. Among the polyisocyanate compounds, it is preferable to use a polyisocyanate compound having a tolylene or diphenylmethane skeleton, particularly a polyisocyanate of diphenylmethane, from the viewpoints of versatility, handleability, weather resistance, and the like. The addition amount of the crosslinking agent can be arbitrarily selected, but it is preferably 0.1 to 6.0 parts by weight, more preferably 0.00 parts by weight with respect to 100 parts by weight of the polylactic acid resin. It is 2 to 5.0 parts by weight, more preferably 0.5 to 4.0 parts by weight. When the addition amount is 0.1 to 6.0 parts by weight, the melt viscosity of the polylactic acid resin can be increased to a region suitable for foaming.

本発明の発泡剤としては、特に限定はなく従来公知のものが使用でき、プロパン、イソブタン、ノルマルブタン、イソヘキサン、ノルマルヘキサン、シクロブタン、シクロヘキサン、イソペンタン、ノルマルペンタン、シクロペンタン等の炭化水素系発泡剤や、塩化メチル、塩化メチレン、ジクロロジフルオロメタン等のハロゲン化炭化水素系発泡剤、ジメチルエーテル、メチルエチルエーテル等のエーテル系発泡剤、窒素、二酸化炭素、アルゴン、空気等の無機系発泡剤が挙げられ、それらの群より選ばれる少なくとも1種を用いることができる。それらの内、ポリ乳酸系樹脂に対するガス散逸が少なく、発泡性粒子輸送が可能であり、所望の発泡性が得られる点から、炭素数3−6の炭化水素系発泡剤が好ましい。   The foaming agent of the present invention is not particularly limited and conventionally known ones can be used, and hydrocarbon-based foaming agents such as propane, isobutane, normal butane, isohexane, normal hexane, cyclobutane, cyclohexane, isopentane, normal pentane, cyclopentane, etc. And halogenated hydrocarbon blowing agents such as methyl chloride, methylene chloride and dichlorodifluoromethane, ether blowing agents such as dimethyl ether and methyl ethyl ether, and inorganic blowing agents such as nitrogen, carbon dioxide, argon and air. , At least one selected from these groups can be used. Among them, a hydrocarbon foaming agent having 3 to 6 carbon atoms is preferable from the viewpoint that the gas dissipation with respect to the polylactic acid resin is small, the foamable particles can be transported, and the desired foamability can be obtained.

前記基材樹脂中には、例えば、黒、灰色、茶色、青色、緑色等の着色顔料又は染料を添加してもよい。着色した基材樹脂を用いれば着色された発泡粒子及び発泡成形体を得ることができる。着色剤としては、有機系、無機系の顔料、染料などが挙げられる。このような顔料及び染料としては、従来公知の各種のものを用いることができる。また、気泡調整剤として、例えばタルク、炭酸カルシウム、ホウ砂、ほう酸亜鉛、水酸化アルミニウム、ステアリン酸カルシウム等の無機物を予め添加することができる。基材樹脂に着色顔料、染料又は無機物等の添加剤を添加する場合は、添加剤をそのまま基材樹脂であるポリ乳酸系樹脂に練り込むこともできるが、通常は分散性等を考慮して添加剤のマスターバッチを作り、それと基材樹脂とを混練することが好ましい。ここでマスターバッチとは、所望の添加剤をポリ乳酸系樹脂と混合して作製したものである。着色顔料又は染料の添加量は着色の色によっても異なるが、通常、ポリ乳酸系樹脂100重量部に対して0.001重量部〜5重量部が好ましく、0.02重量部〜3重量部がより好ましい。前記ポリ乳酸系樹脂中には、本発明の効果を損なわない程度であれば、その他、難燃剤、帯電防止剤、耐候剤、末端封鎖剤などの添加剤を添加しても良い。   For example, a coloring pigment or dye such as black, gray, brown, blue, or green may be added to the base resin. If the colored base resin is used, colored foamed particles and foamed molded products can be obtained. Examples of the colorant include organic and inorganic pigments and dyes. As such pigments and dyes, various conventionally known pigments can be used. Moreover, as a bubble regulator, inorganic substances, such as talc, calcium carbonate, borax, zinc borate, aluminum hydroxide, calcium stearate, can be added in advance. When additives such as color pigments, dyes or inorganic substances are added to the base resin, the additives can be kneaded as they are into the polylactic acid resin as the base resin, but usually in consideration of dispersibility, etc. It is preferable to make a master batch of the additive and knead it with the base resin. Here, the master batch is prepared by mixing a desired additive with a polylactic acid resin. The addition amount of the color pigment or dye varies depending on the color of the color, but is usually preferably 0.001 to 5 parts by weight, and 0.02 to 3 parts by weight with respect to 100 parts by weight of the polylactic acid resin. More preferred. Other additives such as flame retardants, antistatic agents, weathering agents, and end-capping agents may be added to the polylactic acid resin as long as the effects of the present invention are not impaired.

本発明の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法では、特に限定はないが、例えば以下のように、まずポリ乳酸系発泡性粒子を作製し、次いで該発泡性粒子を発泡させポリ乳酸系発泡粒子を得た後、型内成形してポリ乳酸系発泡成形体を得る。その後、該発泡成形体に二酸化炭素処理を行い、揮発分含有量が低減されたポリ乳酸系発泡成形体を得る。   The method for producing a polylactic acid-based foamed molded article having a reduced volatile content of the present invention is not particularly limited. For example, first, polylactic acid-based foamable particles are prepared, and then the foamable particles are produced as follows. Is expanded to obtain polylactic acid-based expanded particles, and then molded in-mold to obtain a polylactic acid-based expanded molded body. Thereafter, the foamed molded product is treated with carbon dioxide to obtain a polylactic acid-based foamed molded product having a reduced volatile content.

<ポリ乳酸系発泡成形体製造工程>
本発明で用いるポリ乳酸系発泡成形体を製造する方法としては、従来公知の方法が採用できる(例えば、国際公開第99/021915号パンフレット)。
<Process for producing polylactic acid-based foamed molded products>
As a method for producing the polylactic acid-based foam molded article used in the present invention, a conventionally known method can be employed (for example, International Publication No. WO 99/021915).

(ポリ乳酸系樹脂粒子作製)
本発明において、ポリ乳酸系発泡成形体を好ましく製造するには、まずポリ乳酸系樹脂粒子を作製する。このポリ乳酸系樹脂粒子は従来公知の方法で作ることができ、例えば、ポリ乳酸系樹脂と架橋剤、必要に応じてその他添加剤を押出機で溶融混練した後、水中カッターやストランドカッター等で押出カットすることで得ることができる。ポリ乳酸系樹脂粒子の1個当りの重量は、0.05〜10mgが好ましく、より好ましくは0.1〜4mgである。粒子重量が前記範囲であれば、樹脂粒子の生産性が良好であり、型内成形時の充填性が良好になる傾向である。
(Preparation of polylactic acid resin particles)
In the present invention, in order to preferably produce a polylactic acid-based foamed molded article, first, polylactic acid-based resin particles are prepared. These polylactic acid-based resin particles can be produced by a conventionally known method. For example, after polylactic acid-based resin and a crosslinking agent, and if necessary, other additives are melt-kneaded with an extruder, an underwater cutter or a strand cutter is used. It can be obtained by extrusion cutting. The weight per polylactic acid resin particle is preferably 0.05 to 10 mg, more preferably 0.1 to 4 mg. When the particle weight is in the above range, the productivity of the resin particles is good, and the filling property during in-mold molding tends to be good.

(ポリ乳酸系樹脂粒子への発泡剤含浸)
次に前記ポリ乳酸系樹脂粒子に発泡剤を含浸させ、ポリ乳酸系発泡性粒子を得る。ポリ乳酸系樹脂粒子に発泡剤を含浸する方法としては、所望の発泡性が得られる発泡剤の存在下で、十分な圧力がかかる条件さえそろっていれば特に限定されるものではない。例えば、密閉容器内に水性媒体または非水性媒体を入れて、これに樹脂粒子と発泡剤を添加して、適度な温度、時間で攪拌することにより樹脂粒子に発泡剤を含浸させることが可能である。水性媒体で含浸を行う場合には、加水分解反応を受けやすいポリエステル系樹脂組成物であることを考慮し、加水分解を抑制する工夫や短時間で含浸を終了させることが好ましい。
(Polylactic acid resin particles impregnated with foaming agent)
Next, the polylactic acid resin particles are impregnated with a foaming agent to obtain polylactic acid foamable particles. The method for impregnating the polylactic acid resin particles with the foaming agent is not particularly limited as long as sufficient pressure is applied in the presence of the foaming agent that provides the desired foamability. For example, it is possible to impregnate a resin particle with a foaming agent by placing an aqueous medium or a non-aqueous medium in an airtight container, adding resin particles and a foaming agent thereto, and stirring at an appropriate temperature and time. is there. In the case of impregnation with an aqueous medium, it is preferable to end the impregnation in a short time or a device that suppresses hydrolysis in consideration of the polyester resin composition that is susceptible to hydrolysis reaction.

発泡剤の含浸量としては、発泡剤の種類や所望の発泡倍率により調整すれば良いが、例えば、発泡倍率30倍以上の発泡粒子を得るためには、発泡性粒子を構成する基材樹脂100重量部に対して、4重量部以上が好ましい。   The impregnation amount of the foaming agent may be adjusted depending on the type of foaming agent and the desired foaming ratio. For example, in order to obtain foamed particles having a foaming ratio of 30 times or more, the base resin 100 constituting the foamable particles 4 parts by weight or more is preferable with respect to parts by weight.

なお、発泡剤の含浸では、安定した含浸性、発泡性を得るために含浸助剤、分散剤などを使用しても良い。含浸助剤としては、メタノール、エタノール、プロパノールなどのアルコール類に代表されるプロトン系溶剤,アセトン、メチルエチルケトンなどのケトン類,酢酸エチル、酢酸ブチル、ノルマルプロピルアセテートなどのエステル類,トルエン、キシレン等の芳香族炭化水素類、などに代表される非プロトン系溶剤、などが挙げられるが、水性媒体で含浸する場合はポリ乳酸系樹脂の加水分解を助長しない、非プロトン系溶剤を用いることが好ましい。   In the impregnation of the foaming agent, an impregnation aid, a dispersing agent or the like may be used in order to obtain stable impregnation properties and foamability. As impregnation aids, proton solvents represented by alcohols such as methanol, ethanol and propanol, ketones such as acetone and methyl ethyl ketone, esters such as ethyl acetate, butyl acetate and normal propyl acetate, toluene, xylene and the like Examples include aprotic solvents such as aromatic hydrocarbons. When impregnated with an aqueous medium, it is preferable to use an aprotic solvent that does not promote hydrolysis of the polylactic acid resin.

前記分散剤としては、カチオン系界面活性剤、アニオン系界面活性剤、非イオン系界面活性剤等が挙げられる。   Examples of the dispersant include a cationic surfactant, an anionic surfactant, and a nonionic surfactant.

また、水性媒体で含浸する場合は、樹脂中への水の浸透を抑制する目的で、塩化ナトリウム、硫酸ナトリウム、炭酸ナトリウム、塩化カリウム、硫酸カリウム、炭酸カリウムなどの1価の金属塩、塩化マグネシウム、硫酸マグネシウムなどの2価の金属塩、硫酸アルミニウムなどの3価の金属塩、などの水溶性塩類などを添加することが好ましい。前記樹脂中への水の浸透を抑制する目的で添加する水溶性塩類などの添加量は、水100重量部に対して5重量部以上、さらに好ましくは7.5重量部以上が好ましい。   When impregnated with an aqueous medium, monovalent metal salts such as sodium chloride, sodium sulfate, sodium carbonate, potassium chloride, potassium sulfate, and potassium carbonate, magnesium chloride for the purpose of suppressing water penetration into the resin Water-soluble salts such as divalent metal salts such as magnesium sulfate and trivalent metal salts such as aluminum sulfate are preferably added. The amount of water-soluble salts added for the purpose of suppressing the penetration of water into the resin is 5 parts by weight or more, more preferably 7.5 parts by weight or more with respect to 100 parts by weight of water.

上記において、ポリ乳酸系発泡性粒子を得る際に、押出機を用いることができ、その場合、ポリ乳酸系樹脂と架橋剤、必要に応じてその他添加剤を押出機へ投入し、その後発泡剤を加え溶融混練した後、混練物を押出し、押出された混練物をカットして発泡性粒子を得ることができる。   In the above, when obtaining polylactic acid-based expandable particles, an extruder can be used. In that case, a polylactic acid-based resin and a crosslinking agent, and if necessary, other additives are added to the extruder, and then the foaming agent. After kneading and melt-kneading, the kneaded product can be extruded, and the extruded kneaded product can be cut to obtain expandable particles.

(ポリ乳酸系発泡性粒子の発泡)
次に、前記のようにして得られるポリ乳酸系発泡性粒子を発泡させてポリ乳酸系発泡粒子を得る。このような方法としは、例えば、発泡ポリスチレン用の予備発泡機を用いて、ポリ乳酸系発泡性粒子を蒸気や熱風、高周波等によって予備発泡する方法(A)が挙げられ、最も簡便である。また、他の方法として、樹脂粒子を密閉容器内において発泡剤の存在下で分散媒に分散させるとともに、その内容物を加熱して樹脂粒子を軟化させてその粒子内に発泡剤を含浸させ、次いで容器の一端を開放し、容器内圧力を発泡剤の蒸気圧以上の圧力に保持しながら粒子と分散媒とを同時に容器内よりも低圧の雰囲気(通常は大気圧下)に放出して発泡させる発泡方法(B)、基材樹脂と架橋剤、その他添加剤を押出機で溶融させると共に、発泡剤と混練して発泡性溶融混練物とし、次いでストランド状に押出して発泡させると共に、冷却後適当な長さに切断するか又はストランドを適当な長さに切断後冷却することによって発泡粒子を製造する方法(C)が挙げられるが、発泡性粒子輸送が可能であるという点から方法(A)が好ましい。
(Foaming of polylactic acid-based expandable particles)
Next, the polylactic acid-based expandable particles obtained as described above are expanded to obtain polylactic acid-based expanded particles. As such a method, for example, a method (A) in which polylactic acid-based expandable particles are pre-foamed with steam, hot air, high frequency or the like using a pre-foaming machine for foamed polystyrene is the simplest method. As another method, the resin particles are dispersed in a dispersion medium in the presence of a foaming agent in a sealed container, and the contents are heated to soften the resin particles and impregnate the foaming agent in the particles. Next, one end of the container is opened, and while maintaining the internal pressure of the container at a pressure equal to or higher than the vapor pressure of the foaming agent, the particles and the dispersion medium are simultaneously released into an atmosphere at a lower pressure (usually under atmospheric pressure) than in the container to foam Foaming method (B), base resin, crosslinking agent, and other additives are melted with an extruder, kneaded with a foaming agent to form a foamable melt-kneaded product, and then extruded into a strand to foam, and after cooling There is a method (C) for producing expanded particles by cutting to an appropriate length or by cooling the strands to an appropriate length and then cooling. The method (A) is possible because the expandable particles can be transported. Is preferred

(型内成形)
上記で得られたポリ乳酸系発泡粒子を所望の型内に所定量充填し、蒸気などで適当な条件で加熱して2次発泡させ、型内で発泡粒子同士を融着させてポリ乳酸系発泡成形体を得る。この型内成形では、従来の発泡ポリスチレンや発泡ポリオレフィン等の成形機を用いることができる。
(In-mold molding)
A predetermined amount of the polylactic acid-based foamed particles obtained above is filled into a desired mold, heated under appropriate conditions with steam or the like to be secondarily foamed, and the foamed particles are fused together in the mold to form a polylactic acid-based A foamed molded product is obtained. In this in-mold molding, a conventional molding machine such as foamed polystyrene or foamed polyolefin can be used.

<揮発分含有量が低減されたポリ乳酸系発泡成形体製造工程>
上記で得られたポリ乳酸系発泡成形体に、以下の二酸化炭素処理を行うことで揮発分を減らして、所望の揮発分含有量が低減されたポリ乳酸系発泡成形体を得た。
<Production process of polylactic acid-based foamed molded product with reduced volatile content>
The polylactic acid-based foamed molded product obtained above was subjected to the following carbon dioxide treatment to reduce the volatile content, thereby obtaining a polylactic acid-based foamed molded product having a desired volatile content reduced.

<二酸化炭素処理>
本工程では、上記で得られたポリ乳酸系発泡成形体を二酸化炭素雰囲気下で特定の圧力下、一定時間維持することで揮発分含有量が低減されたポリ乳酸系発泡成形体を得ることができる。二酸化炭素処理を行うことで、ポリ乳酸系発泡成形体中の炭化水素系発泡剤の含有量が減少し、結果として高温高湿条件下での体積膨張を抑制することができる。
<CO2 treatment>
In this step, it is possible to obtain a polylactic acid-based foam molded article having a reduced volatile content by maintaining the polylactic acid-based foam molded article obtained above in a carbon dioxide atmosphere under a specific pressure for a certain period of time. it can. By performing the carbon dioxide treatment, the content of the hydrocarbon-based foaming agent in the polylactic acid-based foamed molded product is reduced, and as a result, volume expansion under high-temperature and high-humidity conditions can be suppressed.

二酸化炭素処理をポリ乳酸系発泡成形体に行う条件としては、必要な加圧条件下で短時間実施することが好ましい。具体的に二酸化炭素による加圧条件は、0.1≦圧力(MPa)<2.0が好ましく、より好ましくは0.2≦圧力(MPa)≦1.0、さらに好ましくは0.3≦圧力(MPa)≦1.0である。また、発泡成形体に所定圧力で二酸化炭素を付与する処理時間は、処理する温度又は二酸化炭素が保有する湿度等によるが、0.5≦処理時間(min)<10が好ましく、より好ましくは1≦処理時間(min)<10、さらに好ましくは3≦処理時間(min)<10、特に好ましくは3≦処理時間(min)<5である。なお、二酸化炭素による加圧条件は、2.0MPa以上になると設備面を含めたコストが上がるために、2.0MPa未満が好ましい。また二酸化炭素付与処理時間は、短時間で十分であり、生産性の利点を考慮すると、10分間未満が好ましい。   As a condition for performing the carbon dioxide treatment on the polylactic acid-based foamed molded article, it is preferable to carry out for a short time under the necessary pressure condition. Specifically, the pressurizing condition with carbon dioxide is preferably 0.1 ≦ pressure (MPa) <2.0, more preferably 0.2 ≦ pressure (MPa) ≦ 1.0, and further preferably 0.3 ≦ pressure. (MPa) ≦ 1.0. The treatment time for applying carbon dioxide to the foamed molded article at a predetermined pressure depends on the temperature to be treated or the humidity held by the carbon dioxide, but preferably 0.5 ≦ treatment time (min) <10, more preferably 1. ≦ Processing time (min) <10, more preferably 3 ≦ Processing time (min) <10, and particularly preferably 3 ≦ Processing time (min) <5. The pressurizing condition with carbon dioxide is preferably less than 2.0 MPa because the cost including the equipment is increased when the pressure is 2.0 MPa or more. Further, the carbon dioxide application treatment time is sufficient in a short time, and considering the productivity advantage, it is preferably less than 10 minutes.

二酸化炭素を付与する設備は、耐圧性が保証される容器であれば形状、大きさ問わず使用することができる。ポリ乳酸系発泡成形体を金型より取り出してから、別の耐圧容器に該成形体を投入して二酸化炭素処理を行っても良いし、型内成型において耐圧性の金型を用い、成型終了後に金型内に二酸化炭素を封入して二酸化炭素処理を行っても良い。生産性の観点からは、後者の方が好ましい。   The equipment for imparting carbon dioxide can be used regardless of its shape and size as long as the pressure resistance is guaranteed. After taking out the polylactic acid-based foamed molded product from the mold, the molded product may be put into another pressure-resistant container and subjected to carbon dioxide treatment, or the molding is completed using a pressure-resistant mold in in-mold molding. Later, carbon dioxide may be treated by enclosing carbon dioxide in a mold. The latter is preferable from the viewpoint of productivity.

以上のようにして得られた揮発分含有量が低減されたポリ乳酸系発泡成形体は、高温高湿条件下での寸法安定性に優れたものである。本発明において、低揮発分ポリ乳酸系発泡成形体中の残留揮発分量は、以下のようにして測定する。上記で得られた二酸化炭素処理済み発泡成形体を充分乾燥し、その後150℃の雰囲気下に30分放置してから、発泡成形体の元重量に対する放置前後の重量変化を測定し、その差分を発泡成形体の元重量で除した値を揮発分含有量(%)とする。前記揮発分は、殆どが発泡剤であるが、少量の水分が含まれている。   The polylactic acid-based foam molded article having a reduced volatile content obtained as described above is excellent in dimensional stability under high temperature and high humidity conditions. In the present invention, the residual volatile content in the low volatile polylactic acid-based foamed molded article is measured as follows. The carbon dioxide-treated foam molded product obtained above is sufficiently dried, and then left in an atmosphere at 150 ° C. for 30 minutes, and then the change in weight before and after standing is measured with respect to the original weight of the foam molded product. The value divided by the original weight of the foamed molded product is defined as the volatile content (%). The volatile matter is mostly a foaming agent, but contains a small amount of moisture.

本発明の揮発分含有量が低減されたポリ乳酸系発泡成形体は種々の用途に使用することができる。例えば、精密機器、電化製品、電子機器、電子部品などの緩衝材、食品類、酒類、薬品類などの包装材、展示パネル、マネキン、デコレーション等の美粧材、食品、機械部品、電子部品などの通い箱、断熱材、建築材、玩具、アイスクリーム、冷凍食品等の保温材などに使用することができる。   The polylactic acid-based foamed molded article having a reduced volatile content of the present invention can be used for various applications. For example, cushioning materials such as precision equipment, electrical appliances, electronic equipment, electronic parts, packaging materials such as foods, alcoholic beverages, chemicals, cosmetics such as display panels, mannequins, decorations, foods, mechanical parts, electronic parts, etc. It can be used for heat retaining materials such as returnable boxes, heat insulating materials, building materials, toys, ice cream, frozen foods, and the like.

以下、実施例によって本発明を詳細に説明するが、本発明は、これらの実施例に何ら限定されるものではない。尚、評価は下記の方法で行った。なお、実施例において「部」や「%」は重量基準である。   EXAMPLES Hereinafter, although an Example demonstrates this invention in detail, this invention is not limited to these Examples at all. The evaluation was performed by the following method. In the examples, “parts” and “%” are based on weight.

<評価方法>
(1)発泡性粒子の発泡剤含浸率:
含浸率は含浸前後の樹脂粒子重量から以下の式で求めた。
含浸率(%)=100×(含浸後重量−含浸前重量)/含浸前重量
(2)発泡粒子の発泡倍率の測定方法:
内容積2000cmのポリエチレン製カップに発泡粒子を擦切り一杯量り取り、重量を測定し、カップ重量を差引いて発泡粒子の重量を求める。発泡粒子の重量と見かけ体積(2000cm)から下記の式により求めた。
発泡倍率=見かけ体積(2000cm)/発泡粒子の重量
(3)発泡成形体の揮発分含有量:
十分乾燥した発泡成形体を、150℃の雰囲気下に30分放置し、発泡成形体の元重量に対する放置前後の重量変化を測定し、揮発分含有量とした。
(4)耐熱性(高温高湿条件下での体積変化率):
発泡成形体を150×150×20mmに切り出し、60℃×80%RHの条件にて24時間処理し、処理前後の縦、横、厚みの測定値からそれぞれの体積を算出し、処理前の成形体に対する体積変化の割合を算出した。
<Evaluation method>
(1) Foaming agent impregnation rate of expandable particles:
The impregnation rate was obtained from the weight of resin particles before and after impregnation by the following formula.
Impregnation rate (%) = 100 × (weight after impregnation−weight before impregnation) / weight before impregnation (2) Method for measuring expansion ratio of expanded particles:
The foamed particles are scraped off into a polyethylene cup having an internal volume of 2000 cm 3 , and the weight is measured. The weight of the foamed particles is determined by subtracting the weight of the cup. It calculated | required by the following formula from the weight and the apparent volume (2000 cm < 3 >) of the expanded particle.
Foaming ratio = apparent volume (2000 cm 3 ) / weight of foamed particles (3) volatile content of foam molded article:
The sufficiently dried foamed molded product was allowed to stand for 30 minutes in an atmosphere of 150 ° C., and the change in weight before and after the standing with respect to the original weight of the foamed molded product was measured to obtain the volatile content.
(4) Heat resistance (volume change rate under high temperature and high humidity conditions):
The foamed molded product is cut into 150 × 150 × 20 mm, treated under conditions of 60 ° C. × 80% RH for 24 hours, and the respective volumes are calculated from the measured values of length, width, and thickness before and after the processing, and molding before processing. The ratio of volume change to the body was calculated.

(実施例1)
まず、D体比率10%、JIS K 7210(荷重2.16kg)に準拠したMI値3.7g/10分のポリ乳酸100重量部とポリイソシアネート化合物(日本ポリウレタン(株)製、MR−200)3.0重量部を、二軸押出機(東芝機械製、TEM35B)を用いて、シリンダー温度185℃で溶融混練し、水中カッターを用いて約1mmφ(約1.5mg)のビーズ状のポリ乳酸系樹脂粒子を得た。
Example 1
First, 100 parts by weight of polylactic acid and a polyisocyanate compound (MR-200, manufactured by Nippon Polyurethane Co., Ltd.) having a D-form ratio of 10% and an MI value of 3.7 g / 10 min based on JIS K 7210 (load 2.16 kg) 3.0 parts by weight is melt-kneaded at a cylinder temperature of 185 ° C. using a twin screw extruder (Toshiba Machine, TEM35B), and about 1 mmφ (about 1.5 mg) bead-shaped polylactic acid using an underwater cutter System resin particles were obtained.

得られたポリ乳酸系樹脂粒子100重量部に対して、水100重量部、発泡剤として脱臭ブタン(ノルマルブタン/イソブタン重量比=7/3)12重量部、含浸助剤として食塩10重量部、分散剤としてポリオキシエチレンオレイルエーテル0.3重量部を耐圧容器に仕込み、90℃で90分間保持した。十分に冷却後取出し、乾燥して、ポリ乳酸系発泡性粒子を得た。得られたポリ乳酸系発泡性粒子の含浸率は5.7%であった。   With respect to 100 parts by weight of the obtained polylactic acid-based resin particles, 100 parts by weight of water, 12 parts by weight of deodorized butane (normal butane / isobutane weight ratio = 7/3) as a foaming agent, 10 parts by weight of sodium chloride as an impregnation aid, As a dispersant, 0.3 part by weight of polyoxyethylene oleyl ether was charged in a pressure vessel and held at 90 ° C. for 90 minutes. After sufficiently cooling, it was taken out and dried to obtain polylactic acid-based expandable particles. The impregnation rate of the obtained polylactic acid-based expandable particles was 5.7%.

該ポリ乳酸系発泡性粒子を予備発泡機(ダイセン工業製、BHP−300)に約1.5kg投入し、90℃の蒸気下に40〜60秒間保持してポリ乳酸系発泡粒子を得た。得られたポリ乳酸系発泡粒子を風乾した後、篩を使用し融着粒子を分別した。分取されたポリ乳酸系発泡粒子の発泡倍率は35倍であった。   About 1.5 kg of the polylactic acid-based expandable particles were put into a pre-foaming machine (manufactured by Daisen Kogyo Co., Ltd., BHP-300) and held under steam at 90 ° C. for 40 to 60 seconds to obtain polylactic acid-based expanded particles. The obtained polylactic acid-based foamed particles were air-dried, and then the fused particles were separated using a sieve. The expansion ratio of the fractionated polylactic acid-based expanded particles was 35 times.

分取されたポリ乳酸系発泡粒子を24時間以上熟成した後、発泡成形機(ダイセン工業製、KR−57)に300×450×20mmの金型を設置し、発泡粒子を圧縮率0%で充填し、スチーム圧0.1MPaで10〜20秒処理し型内成形を実施し、発泡成形体を得た。   After the separated polylactic acid-based foamed particles are aged for 24 hours or more, a 300 × 450 × 20 mm mold is placed on a foam molding machine (made by Daisen Kogyo, KR-57), and the foamed particles are compressed at 0%. Filled and treated with a steam pressure of 0.1 MPa for 10 to 20 seconds to perform in-mold molding to obtain a foam molded article.

得られた発泡成形体を密閉容器内に投入し、表1に従って、二酸化炭素を封入して密閉容器内圧力を0.3MPaで3分間保持することで二酸化炭素処理を行った。その後、容器内の圧力を開放し、揮発分含有量が低減されたポリ乳酸系発泡成形体を得た。得られた揮発分含有量が低減されたポリ乳酸系発泡成形体の揮発分含有量と耐熱性を評価した。評価結果は表1の通りであった。   The obtained foamed molded article was put into a sealed container, and carbon dioxide treatment was performed by enclosing carbon dioxide in accordance with Table 1 and maintaining the pressure in the sealed container at 0.3 MPa for 3 minutes. Thereafter, the pressure in the container was released to obtain a polylactic acid-based foamed molded article having a reduced volatile content. The polylactic acid-based foamed molded article having a reduced volatile content was evaluated for the volatile content and heat resistance. The evaluation results are shown in Table 1.

Figure 2008239728
Figure 2008239728

(比較例1)
二酸化炭素処理を行わない以外は、実施例1と同様にして発泡成形体を得た。その際、発泡成形体の揮発分含有量と耐熱性を評価した結果は表1の通りであった。
(Comparative Example 1)
A foamed molded article was obtained in the same manner as in Example 1 except that the carbon dioxide treatment was not performed. At that time, the results of evaluating the volatile content and heat resistance of the foamed molded product are shown in Table 1.

(比較例2)
二酸炭素処理の変わりにメタノール処理を行った以外は、実施例1と同様にして発泡成形体を得た。メタノール処理は、発泡成形体をメタノール中に10秒間浸し、常温で風乾した。
(Comparative Example 2)
A foam molded article was obtained in the same manner as in Example 1 except that methanol treatment was performed instead of carbon dioxide treatment. In the methanol treatment, the foamed molded product was immersed in methanol for 10 seconds and air-dried at room temperature.

実施例1、比較例1より、ポリ乳酸系発泡成形体に二酸化炭素処理を行うことで、発泡剤含有量が減少し、60℃×80%RHでの膨張が抑制されることがわかった。また、特開2005−105097号公報に準拠した比較例2でも、メタノール処理により発泡剤含有量が減少し、60℃×80%RHでの膨張が抑制することがわかったが、二酸化炭素処理の方が揮発分含有量が少ない上に耐熱性も良く、取扱上も容易であるため有利であることがわかった。   From Example 1 and Comparative Example 1, it was found that by performing carbon dioxide treatment on the polylactic acid-based foamed molded article, the foaming agent content was reduced and the expansion at 60 ° C. × 80% RH was suppressed. Moreover, even in Comparative Example 2 based on JP-A-2005-105097, it was found that the foaming agent content was reduced by the methanol treatment and the expansion at 60 ° C. × 80% RH was suppressed. It was found that this method is advantageous because it has a low volatile content, good heat resistance, and is easy to handle.

(実施例2)
低揮発分ポリ乳酸系発泡成形体を作製する際に、発泡成形体を投入してから二酸化炭素を封入した後の密閉容器内圧力を0.1MPaに変えた以外は、実施例1と同様にして揮発分含有量が低減されたポリ乳酸系発泡成形体を得た。その際、揮発分含有量が低減されたポリ乳酸系発泡成形体の揮発分含有量と耐熱性を評価した結果は表2の通りであった。
(Example 2)
When producing a low volatile polylactic acid-based foam molded article, the same procedure as in Example 1 was performed except that the pressure in the sealed container after the carbon dioxide was sealed after the foam molded article was charged was changed to 0.1 MPa. Thus, a polylactic acid-based foamed molded article having a reduced volatile content was obtained. At that time, the results of evaluating the volatile content and heat resistance of the polylactic acid-based foamed molded product having a reduced volatile content are shown in Table 2.

Figure 2008239728
Figure 2008239728

(実施例3)
揮発分含有量が低減されたポリ乳酸系発泡成形体を作製する際に、発泡成形体を投入してから二酸化炭素を封入した後の密閉容器内圧力を0.5MPaに変えた以外は、実施例1と同様にして揮発分含有量が低減されたポリ乳酸系発泡成形体を得た。その際、揮発分含有量が低減されたポリ乳酸系発泡成形体の発泡剤含有量と耐熱性を評価した結果は表2の通りであった。
(Example 3)
When producing a polylactic acid-based foamed molded product with a reduced volatile content, it was carried out except that the pressure inside the sealed container after enclosing the carbon dioxide after the foamed molded product was charged was changed to 0.5 MPa. A polylactic acid-based foamed molded article having a reduced volatile content was obtained in the same manner as in Example 1. At that time, the results of evaluating the foaming agent content and the heat resistance of the polylactic acid-based foamed molded article having a reduced volatile content are shown in Table 2.

(実施例4)
揮発分含有量が低減されたポリ乳酸系発泡成形体を作製する際に、発泡成形体を投入してから二酸化炭素を封入した後の密閉容器内圧力を1.0MPaに変えた以外は、実施例1と同様にして揮発分含有量が低減されたポリ乳酸系発泡成形体を得た。その際、揮発分含有量が低減されたポリ乳酸系発泡成形体の発泡剤含有量と耐熱性を評価した結果は表2の通りであった。
Example 4
When producing a polylactic acid-based foamed molded product with a reduced volatile content, it was carried out except that the pressure inside the sealed container after the carbon dioxide was sealed after the foamed molded product was charged was changed to 1.0 MPa. A polylactic acid-based foamed molded article having a reduced volatile content was obtained in the same manner as in Example 1. At that time, the results of evaluating the foaming agent content and the heat resistance of the polylactic acid-based foamed molded article having a reduced volatile content are shown in Table 2.

実施例1〜4および比較例1より、二酸化炭素処理を行う際、密閉容器保持時間が3分間の場合、容器内圧力が0.1MPaでも、揮発分含有量が減少し、60℃×80%RHでの膨張が抑制されることがわかった。   From Examples 1 to 4 and Comparative Example 1, when the carbon dioxide treatment was performed, when the closed container holding time was 3 minutes, the volatile content decreased even when the pressure in the container was 0.1 MPa, and 60 ° C. × 80% It was found that expansion at RH was suppressed.

(実施例5)
揮発分含有量が低減されたポリ乳酸系発泡成形体を作製する際に、発泡成形体を投入してから二酸化炭素を封入した後の密閉容器内圧力を0.3MPaに保持する時間を1分間に変えた以外は、実施例1と同様にして発泡成形体を得た。その際、発泡成形体の発泡剤含有量と耐熱性を評価した結果は表3の通りであった。
(Example 5)
When producing a polylactic acid-based foamed molded product with a reduced volatile content, the time during which the pressure inside the sealed container is maintained at 0.3 MPa after the carbon dioxide is sealed after the foamed molded product is charged is 1 minute. A foamed molded article was obtained in the same manner as in Example 1 except that the above was changed. The results of evaluating the foaming agent content and heat resistance of the foamed molded product were as shown in Table 3.

Figure 2008239728
Figure 2008239728

(実施例6)
低揮発分ポリ乳酸系発泡成形体を作製する際に、発泡成形体を投入してから二酸化炭素を封入した後の密閉容器内圧力を0.3MPaに保持する時間を5分間に変えた以外は、実施例1と同様にして揮発分含有量が低減されたポリ乳酸系発泡成形体を得た。その際、揮発分含有量が低減されたポリ乳酸系発泡成形体の揮発分含有量と耐熱性を評価した結果は表3の通りであった。
(Example 6)
When producing a low volatile polylactic acid-based foamed molded article, except that the time for maintaining the pressure inside the sealed container at 0.3 MPa after charging the carbon dioxide after charging the foamed molded article was changed to 5 minutes. In the same manner as in Example 1, a polylactic acid-based foamed molded article having a reduced volatile content was obtained. At that time, the results of evaluating the volatile content and the heat resistance of the polylactic acid-based foamed molded product having a reduced volatile content are shown in Table 3.

(実施例7)
低揮発分ポリ乳酸系発泡成形体を作製する際に、発泡成形体を投入してから二酸化炭素を封入した後の密閉容器内圧力を0.3MPaに保持する時間を10分間に変えた以外は、実施例1と同様にして揮発分含有量が低減されたポリ乳酸系発泡成形体を得た。その際、揮発分含有量が低減されたポリ乳酸系発泡成形体の揮発分含有量と耐熱性を評価した結果は表3の通りであった。
(Example 7)
When producing a low volatile polylactic acid-based foamed molded article, except that the time for maintaining the pressure in the sealed container at 0.3 MPa after charging the carbon dioxide after the foamed molded article was charged was changed to 10 minutes. In the same manner as in Example 1, a polylactic acid-based foamed molded article having a reduced volatile content was obtained. At that time, the results of evaluating the volatile content and the heat resistance of the polylactic acid-based foamed molded product having a reduced volatile content are shown in Table 3.

実施例1、5〜7と比較例1より、二酸化炭素処理を行う際、密閉容器内圧力が0.3MPaの場合、保持時間が1分間でも、揮発分含有量が減少し、60℃×80%RHでの膨張が抑制されることがわかった。   From Examples 1, 5 to 7 and Comparative Example 1, when the carbon dioxide treatment was performed, when the pressure in the sealed container was 0.3 MPa, the volatile content decreased even at a holding time of 1 minute, and 60 ° C. × 80 It was found that the expansion at% RH was suppressed.

Claims (5)

炭化水素系発泡剤を含有するポリ乳酸系発泡成形体に対し、二酸化炭素処理を行うことを特徴とする揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法。   A method for producing a polylactic acid-based foamed molded article having a reduced volatile content, characterized by subjecting a polylactic acid-based foamed molded article containing a hydrocarbon-based foaming agent to carbon dioxide treatment. 二酸化炭素処理が、ポリ乳酸系発泡成形体を0.1MPa以上、2.0MPa未満の圧力の二酸化炭素雰囲気下に曝すことを特徴とする請求項1記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法。   The lactic acid content-reduced polylactic acid according to claim 1, wherein the carbon dioxide treatment exposes the polylactic acid-based foamed molded article to a carbon dioxide atmosphere having a pressure of 0.1 MPa or more and less than 2.0 MPa. Method for manufacturing a foamed molded article. 二酸化炭素処理が、ポリ乳酸系発泡成形体を0.5分間以上、10分間未満の時間で二酸化炭素雰囲気下に曝すことを特徴とする請求項1又は2に記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法。   The volatile matter content according to claim 1 or 2, wherein the carbon dioxide treatment exposes the polylactic acid-based foamed molded article to a carbon dioxide atmosphere for a time of 0.5 minutes or more and less than 10 minutes. A method for producing a polylactic acid-based foamed molded article. 炭化水素系発泡剤が炭素数3−6の脂肪族炭化水素である請求項1〜3の何れかに記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法。   The method for producing a polylactic acid-based foamed molded article having a reduced volatile content according to any one of claims 1 to 3, wherein the hydrocarbon-based foaming agent is an aliphatic hydrocarbon having 3 to 6 carbon atoms. ポリ乳酸系発泡成形体が、ポリ乳酸系樹脂を主成分としており、該ポリ乳酸系樹脂をゲル化処理したものである請求項1〜4の何れかに記載の揮発分含有量が低減されたポリ乳酸系発泡成形体の製造方法。   The polylactic acid-based foamed molded article is composed of a polylactic acid-based resin as a main component, and the polylactic acid-based resin is obtained by gelation treatment. The volatile content in any one of claims 1 to 4 is reduced. A method for producing a polylactic acid-based foamed molded article.
JP2007080700A 2007-03-27 2007-03-27 Method for producing polylactic acid foamed molding Pending JP2008239728A (en)

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JP2012025041A (en) * 2010-07-23 2012-02-09 Asahi Kasei Construction Materials Co Ltd Phenolic resin foam plate, method of manufacturing the phenolic resin foam plate, composite board and heat insulating structure
JPWO2011118793A1 (en) * 2010-03-26 2013-07-04 旭化成建材株式会社 Phenol resin foam laminate and method for producing the same
CN114920976A (en) * 2022-06-13 2022-08-19 安徽瑞鸿新材料科技有限公司 Preparation method of degradable polylactic acid foaming particles

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2011118793A1 (en) * 2010-03-26 2013-07-04 旭化成建材株式会社 Phenol resin foam laminate and method for producing the same
US9975311B2 (en) 2010-03-26 2018-05-22 Asahi Kasei Construction Materials Corporation Phenolic resin foam laminated sheet and method for manufacturing the same
JP2012006225A (en) * 2010-06-24 2012-01-12 Asahi Kasei Construction Materials Co Ltd Laminated plate of phenol resin foamed body, method for manufacturing the same, composite plate, and heat insulating structure
JP2012025041A (en) * 2010-07-23 2012-02-09 Asahi Kasei Construction Materials Co Ltd Phenolic resin foam plate, method of manufacturing the phenolic resin foam plate, composite board and heat insulating structure
CN114920976A (en) * 2022-06-13 2022-08-19 安徽瑞鸿新材料科技有限公司 Preparation method of degradable polylactic acid foaming particles

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