JPH05139435A - Foaming container - Google Patents

Foaming container

Info

Publication number
JPH05139435A
JPH05139435A JP30058691A JP30058691A JPH05139435A JP H05139435 A JPH05139435 A JP H05139435A JP 30058691 A JP30058691 A JP 30058691A JP 30058691 A JP30058691 A JP 30058691A JP H05139435 A JPH05139435 A JP H05139435A
Authority
JP
Japan
Prior art keywords
acid
lactic acid
foaming
container
copolymer
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
JP30058691A
Other languages
Japanese (ja)
Inventor
Kazuhiko Suzuki
和彦 鈴木
Takayuki Watanabe
孝行 渡辺
Yasuhiro Kitahara
泰広 北原
Masanobu Ajioka
正伸 味岡
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP30058691A priority Critical patent/JPH05139435A/en
Priority to CA002064410A priority patent/CA2064410A1/en
Priority to DE69214183T priority patent/DE69214183T2/en
Priority to EP92302840A priority patent/EP0507554B1/en
Publication of JPH05139435A publication Critical patent/JPH05139435A/en
Priority to US08/186,920 priority patent/US5447962A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D65/00Wrappers or flexible covers; Packaging materials of special type or form
    • B65D65/38Packaging materials of special type or form
    • B65D65/44Applications of resilient shock-absorbing materials, e.g. foamed plastics material, honeycomb material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/14Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
    • C08J9/143Halogen containing compounds
    • C08J9/147Halogen containing compounds containing carbon and halogen atoms only
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/04Polyesters derived from hydroxy carboxylic acids, e.g. lactones
    • 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

Abstract

PURPOSE:To provide foaming containers such as tray and lunch box which are made from a thermoplastic polymer composition consisting mainly of the copolymer of polylactic acid or lactic acid and hydroxycarboxylic acid so as to be made decomposable in a relatively short period of time in a natural environment. CONSTITUTION:Polystyrene or polyolefin foaming containers are widely used in the tray or lunch box. In this case, the foaming container is made from a thermoplastic polymer composition consisting mainly of the copolymer of polylactic acid or lactic acid and hydroxycarboxylic acid. Levo or dextro-lactic acid alone or the mixture thereof is used in the aforesaid lactic acid. Glycolic acid is used in the aforesaid hydroxycarboxylic acid. When the foaming container is disposed of by being buried under the ground or discarded into the sea or river, as in the case of paper or wood, the foaming container is decomposed into harmless water and carbon dioxide in a relatively short period of time in a natural environment.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は発泡容器に関する。さら
に詳しくは、乳酸ポリマーを主体とする熱可塑性ポリマ
ー組成物からなる、自然環境下での分解性を持った発泡
容器に関するものである。
FIELD OF THE INVENTION The present invention relates to a foam container. More specifically, the present invention relates to a foam container having a degradability in a natural environment, which is made of a thermoplastic polymer composition mainly containing lactic acid polymer.

【0002】[0002]

【従来の技術】従来、ポリスチレン系、ポリオレフィン
系の発泡容器は、例えばトレーや弁当箱等に広く用いて
いる。特にこれら発泡容器は、少量の樹脂で成形されて
おり、使い捨ての容器、食品容器として用いられてい
る。しかし、このような樹脂から成形した発泡容器は、
廃棄する際、かさばり、ゴミの量を増すうえに、従来の
物は自然環境下での分解速度がきわめて遅いため、埋設
処理された場合、半永久的に地中に残留する。また投棄
されたプラスチック類により、景観が損なわれ海洋生物
の生活環境が破壊されるなどの問題も起こっている。然
しながら、これまで、自然環境下で容易に分解してしま
う発泡容器は知られていない。
2. Description of the Related Art Conventionally, polystyrene-based or polyolefin-based foam containers have been widely used for trays, lunch boxes and the like. In particular, these foam containers are molded with a small amount of resin and are used as disposable containers and food containers. However, the foam container molded from such a resin,
In addition to being bulky and increasing the amount of garbage at the time of disposal, conventional materials have a very slow decomposition rate in the natural environment, so when they are buried, they remain in the ground semipermanently. In addition, the discarded plastics have caused problems such as damage to the landscape and the living environment of marine life. However, up to now, no foam container that is easily decomposed in a natural environment has been known.

【0003】一方、分解性のある熱可塑性ポリマーとし
て、ポリ乳酸または乳酸のコポリマーが知られている。
この乳酸系ポリマーは、自然環境下で分解性があり、土
壌や海水中に置かれた場合、数週間で分解を始め、約一
年で消滅する。また分解生成物は乳酸と二酸価炭素と水
であり、すべて無害である。また原料となる乳酸は、コ
ーンスターチやコーンシロップのような安価の発酵から
得られ、また、エチレンのような石油化学原料からも容
易に製造される。ポリ乳酸または乳酸のコポリマーの製
造に関しては、米国特許1,995,970に開示され
ており、通常ラクタイドと呼ばれる乳酸の環状2量体か
ら合成されている。この乳酸系ポリマーは、その生体適
合と分解性から手術用の縫合糸や、医学用の除放性材料
として用いられているが、緩衝材として用いることはい
まだ知られていない。
On the other hand, polylactic acid or a copolymer of lactic acid is known as a degradable thermoplastic polymer.
This lactic acid-based polymer is degradable in a natural environment, and when placed in soil or seawater, it begins to decompose in a few weeks and disappears in about a year. The decomposition products are lactic acid, carbon dioxide and water, all of which are harmless. Lactic acid as a raw material is obtained from inexpensive fermentation such as corn starch and corn syrup, and is easily produced from petrochemical raw materials such as ethylene. The production of polylactic acid or a copolymer of lactic acid is disclosed in US Pat. No. 1,995,970 and is synthesized from a cyclic dimer of lactic acid commonly referred to as lactide. Because of its biocompatibility and degradability, this lactic acid-based polymer is used as a surgical suture and a medical sustained-release material, but its use as a cushioning material has not yet been known.

【0004】[0004]

【発明が解決しようとする課題】本発明は自然環境下で
分解可能な発泡容器を提供することである。
The present invention is to provide a foam container that can be decomposed in a natural environment.

【0005】[0005]

【課題を解決するための手段】本発明者らは、自然環境
下で分解可能な発泡容器を得る目的で、乳酸系ポリマー
に着目し、乳酸ポリマーを主体とする樹脂から発泡シー
トを得、更にポリマーの持っている分解性を損なうこと
のない容器を得ることに成功し、本発明を完成したもの
である。即ち、本発明は、ポリ乳酸または乳酸とヒドロ
キシカルボン酸のコポリマーを主成分とする熱可塑性ポ
リマー組成物からなる発泡容器である。本発明に用いら
れるポリ乳酸または乳酸とヒドロキシカルボン酸のコポ
リマーは、原料として乳酸または乳酸の環状2量体であ
るラクタイド、さらにヒドロキシカルボン酸を用いる
か、場合によってこの他のモノマーを適宜使用できる。
乳酸を用いる場合には脱水縮合によるが、高分子量の物
を得るにはラクタイドの開環重合によるのが好ましい。
開環重合に用いるラクタイドは、L−ラクタイド、D−
ラクタイド、mesoラクタイド、あるいはそれらの混
合物が用いられるが、DまたはL−ラクタイドに、反対
の光学活性が混ざった物が好ましい。その混合割合は、
DまたはL−ラクタイド/光学対掌体=95/5〜50
/50が好ましい。
Means for Solving the Problems The present inventors have focused on lactic acid-based polymers for the purpose of obtaining a foamable container that can be decomposed in a natural environment, and obtained a foamed sheet from a resin mainly containing lactic acid polymer. The present invention has been completed by succeeding in obtaining a container that does not impair the degradability of the polymer. That is, the present invention is a foam container made of a thermoplastic polymer composition containing polylactic acid or a copolymer of lactic acid and hydroxycarboxylic acid as a main component. In the polylactic acid or the copolymer of lactic acid and hydroxycarboxylic acid used in the present invention, lactic acid or a lactide which is a cyclic dimer of lactic acid and further hydroxycarboxylic acid may be used as a raw material, or other monomer may be appropriately used depending on the case.
When lactic acid is used, dehydration condensation is used, but to obtain a high molecular weight product, ring-opening polymerization of lactide is preferable.
Lactide used for ring-opening polymerization is L-lactide or D-lactide.
Lactide, meso lactide, or a mixture thereof is used, but a mixture of D or L-lactide with the opposite optical activity is preferable. The mixing ratio is
D or L-lactide / optical antipode = 95/5 to 50
/ 50 is preferable.

【0006】乳酸系ポリマーの重合度は、150から2
0,000である。これより低い重合度ではフィルム等
の成形品にしたときの強度が小さく実用に適さない。ま
た、重合度が高過ぎると、熱時溶融した状態での粘度が
高く、成形加工性が劣る。
The degree of polymerization of the lactic acid type polymer is 150 to 2
It is 10,000. If the degree of polymerization is lower than this, the strength of a molded product such as a film is small and it is not suitable for practical use. On the other hand, if the degree of polymerization is too high, the viscosity in the molten state during heating is high and the moldability is poor.

【0007】重合方法は、溶媒を用いる方法でも、溶媒
を用いない方法でも良いが、溶媒の回収の問題から、工
業的には溶媒を用いない塊状重合がよい。開環重合の触
媒は、一般に亜鉛、錫の塩化物またはカルボン酸塩等が
用いられるが、特に限定されない。生体適合性材料や食
品関係に用いる場合は毒性を考慮する必要がある。ま
た、本発明による乳酸系ポリマーには可塑剤、改質剤等
を含んでいてもよい。
The polymerization method may be a method using a solvent or a method not using a solvent, but in view of the problem of recovery of the solvent, industrially bulk polymerization without a solvent is preferable. As the ring-opening polymerization catalyst, zinc, tin chloride, carboxylate or the like is generally used, but the catalyst is not particularly limited. Toxicities should be considered when used in biocompatible materials and food products. The lactic acid-based polymer according to the present invention may contain a plasticizer, a modifier and the like.

【0008】本発明による発泡容器は乳酸系ポリマーを
主成分とする熱可塑性ポリマー組成物から製造される
が、通常、上記熱可塑性ポリマーを用いて発泡シートを
製造し、これを用いて任意の形状の発泡容器として用い
られる。発泡シートの製造は通常の方法を用いて実施す
ることが出来る。通常は、発泡剤を用いた押出機から押
し出すと同時に発泡させるいわゆる押出発泡法を用いる
ことが好ましい。発泡剤としては、蒸発により発泡させ
る蒸発発泡剤、例えばエタン、ブタン、ペンタン、ヘキ
サン、ヘプタン、エチレン、プロピレン、石油エーテル
等の炭化水素、塩化メチル、モノクロルトリフルオロメ
タン、ジクロルジフルオロメタン、ジクロルテトラフル
オロエタン等のハロゲン化炭化水素や炭酸ガス、窒素ガ
ス、水等が挙げられる。これらの発泡剤の添加量は、熱
可塑性ポリマー組成物に対して0.1〜30重量%、特
に0.5〜10重量%が好ましい。
The foam container according to the present invention is manufactured from a thermoplastic polymer composition containing a lactic acid-based polymer as a main component. Usually, a foamed sheet is manufactured using the above-mentioned thermoplastic polymer, and the foamed sheet is used in an arbitrary shape. Used as a foam container. The production of the foamed sheet can be carried out using a usual method. Usually, it is preferable to use a so-called extrusion foaming method in which foaming is carried out simultaneously with extrusion from an extruder using a foaming agent. Examples of the foaming agent include evaporative foaming agents that are foamed by evaporation, such as hydrocarbons such as ethane, butane, pentane, hexane, heptane, ethylene, propylene, petroleum ether, methyl chloride, monochlorotrifluoromethane, dichlorodifluoromethane, dichlorotetramethane. Examples thereof include halogenated hydrocarbons such as fluoroethane, carbon dioxide gas, nitrogen gas, and water. The amount of these foaming agents added is preferably 0.1 to 30% by weight, and particularly preferably 0.5 to 10% by weight, based on the thermoplastic polymer composition.

【0009】また必要に応じて、加熱すると分解してガ
スを発生する分解型発泡剤、例えば重炭酸ソーダ等の無
機発泡剤、アゾジカルボンアミド、N,N’−ジニトロ
ペタメチレンテトラミン、p,p’−オキシビス(ベン
ゼンスルホニルカルバジド)、アゾビスイソブチロニト
リル、ベンゼンスルホニルヒドラジド等の有機発泡剤や
発泡助剤あるいは核剤、例えばステアリン酸、シュウ
酸、サリチル酸、フタル酸、安息香酸、クエン酸、酒石
酸等の無機酸、前記有機酸または無機酸の塩、炭酸ソー
ダ等の炭酸塩、酸化亜鉛、酸化カルシュウム、酸化チタ
ン、シリカ、アルミナ、クレイ、カオリン、ケイソウ土
等を適当量加えてもよい。発泡成形品の着色その他の変
成のために、顔料、難燃剤、充填剤等を適当量加えるこ
とも何ら差し支えない。
If necessary, a decomposition type foaming agent which decomposes to generate gas when heated, for example, an inorganic foaming agent such as sodium bicarbonate, azodicarbonamide, N, N'-dinitropetamethylenetetramine, p, p'- Organic foaming agents such as oxybis (benzenesulfonylcarbazide), azobisisobutyronitrile, benzenesulfonylhydrazide, foaming aids or nucleating agents such as stearic acid, oxalic acid, salicylic acid, phthalic acid, benzoic acid, citric acid, tartaric acid An appropriate amount of an inorganic acid such as the above, a salt of the organic acid or the inorganic acid, a carbonate such as sodium carbonate, zinc oxide, calcium oxide, titanium oxide, silica, alumina, clay, kaolin, diatomaceous earth and the like may be added. For coloring or other modification of the foamed molded product, it is also possible to add an appropriate amount of pigment, flame retardant, filler or the like.

【0010】発泡シートの押出温度は、ポリマーの組成
によって異なるが、通常溶融粘度が10,000〜10
0,000ポイズになる温度で行う。これより低いと溶
融したポリマーの粘度が高く気泡の生成が遅く発泡倍率
が上がらない。逆にこれより高い温度でポリマーの粘度
が小さすぎると、気泡を保持できなくなり、均一な品質
の発泡シートが得られない。発泡倍率は成形する容器に
よって異なるが、1.5倍から15倍が好ましい。発泡
容器は、上記のシートを再加熱して軟化させた後、真空
あるいは圧空成形等の熱成形によって所望の形状にされ
る。発泡容器は、好ましくは外表面のスキン層が部分的
に除かれているものである。発泡容器の外表面のスキン
層を部分的に除くには、例えば熱成形する前に発泡シー
トの表層に切れ目を入れておき、容器を成形する前にオ
ーブン中に加熱することにより切れ目を拡大させたり、
あるいは容器を成形した後、小孔をあける方法が用いら
れる。
The extrusion temperature of the foamed sheet depends on the composition of the polymer, but the melt viscosity is usually 10,000 to 10
Perform at a temperature of 50,000 poise. If it is lower than this, the viscosity of the melted polymer is high, the formation of bubbles is slow, and the expansion ratio does not increase. On the other hand, if the viscosity of the polymer is too low at a temperature higher than this, bubbles cannot be retained, and a foamed sheet of uniform quality cannot be obtained. Although the expansion ratio depends on the container to be molded, it is preferably 1.5 to 15 times. The foamed container is reheated to soften the sheet, and then formed into a desired shape by thermoforming such as vacuum or pressure forming. The foam container is preferably one in which the skin layer on the outer surface is partially removed. To partially remove the skin layer on the outer surface of the foam container, for example, make a cut in the surface layer of the foam sheet before thermoforming and expand the cut by heating in an oven before molding the container. Or
Alternatively, a method of forming small holes after molding the container is used.

【0011】[0011]

【実施例】以下、実施例により本発明を詳細に説明す
る。 実施例1〜3 表−Iに示す分子量約10万のポリD,L−ラクタイド
とポリL−ラクタイド混合物に気泡調整剤としてタルク
0.5重量%を添加し、50mmΦの押出機で200℃
の温度で溶融混練した後、ブタンを樹脂100gに対し
0.065molの割合で圧入した。圧入後の押出機の
シリンダー温度を140にして樹脂混合物を冷却し、ス
リットより大気中に放出して650mm巾の発泡シート
を得た。得られた発泡シートの厚み、見掛け密度をそれ
ぞれ表−Iに示した。 これらの発泡シートから真空成
形機で200×100mm、深さ15mmのトレイを成
形した。発泡シートは成形機のオーブンに入る前、容器
の外表面側に5mmの十字の切れ目が入るロールを通
す。切れ目は150℃のオーブンを通過すると約2mm
に広がった。引きつづき金型の上に挿入され賦形され
る。得られたトレイは外側が格子状にスキン層が除かれ
ており、しかもトレイとして使用上の問題はなかった。
このトレイを温度35℃、水分30%の土壌中に埋設し
て分解試験を行った。分解性の評価は、重量の減少率で
判定した。結果を表−Iに併記した。
The present invention will be described in detail below with reference to examples. Examples 1 to 3 0.5% by weight of talc was added as a cell regulator to a mixture of poly D, L-lactide and poly L-lactide having a molecular weight of about 100,000 shown in Table-I, and the temperature was 200 ° C. in an extruder of 50 mmΦ.
After melt-kneading at the temperature of, butane was injected under pressure at a ratio of 0.065 mol to 100 g of the resin. After the press-fitting, the cylinder temperature of the extruder was set to 140 to cool the resin mixture, and the resin mixture was discharged into the atmosphere through the slit to obtain a foamed sheet having a width of 650 mm. The thickness and apparent density of the obtained foamed sheet are shown in Table-I. A tray having a size of 200 × 100 mm and a depth of 15 mm was formed from these foamed sheets by a vacuum forming machine. Before entering the oven of the molding machine, the foamed sheet is passed through a roll having a 5 mm cross cut on the outer surface side of the container. The break is about 2 mm when passing through an oven at 150 ° C
Spread to. Then, it is inserted into the mold and shaped. The outer side of the obtained tray had a lattice-like skin layer removed, and there was no problem in using the tray.
This tray was embedded in soil having a temperature of 35 ° C. and a water content of 30% to carry out a decomposition test. The degradability was evaluated by the weight reduction rate. The results are also shown in Table-I.

【0012】実施例4〜6 表−IIに示したL−ラクタイドとオキシカルボン酸のコ
ポリマーに変えた以外は実施例1と同様にして、発泡シ
ート更にトレイを成形した。得られた発泡シートの厚
み、見かけ密度及び分解試験の結果を表−IIに示した。
Examples 4 to 6 A foamed sheet and a tray were formed in the same manner as in Example 1 except that the copolymer of L-lactide and oxycarboxylic acid shown in Table II was used. The thickness, apparent density and result of the decomposition test of the obtained foamed sheet are shown in Table-II.

【0013】[0013]

【表1】 [Table 1]

【0014】[0014]

【表2】 [Table 2]

【0015】[0015]

【発明の効果】本発明の乳酸の主成分とするポリマーを
主体とする発泡容器は、廃棄物として地中に埋設された
り海や川に投棄された場合、紙や木等の天然物と同じよ
うに自然環境中で比較的短い期間の内に無害な水と炭酸
ガスに分解する。
INDUSTRIAL APPLICABILITY The foam container mainly composed of the polymer containing lactic acid as a main component of the present invention is the same as a natural product such as paper or wood when it is buried in the ground as waste or dumped in the sea or river. It decomposes into harmless water and carbon dioxide within a relatively short period of time in the natural environment.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C08J 9/14 CFD 8927−4F C08L 67/04 LPM 8933−4J // B29B 17/00 8824−4F B29C 51/00 7421−4F B29K 105:04 C08L 67:00 (72)発明者 味岡 正伸 神奈川県横浜市栄区笠間町1190番地 三井 東圧化学株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI Technical display location C08J 9/14 CFD 8927-4F C08L 67/04 LPM 8933-4J // B29B 17/00 8824-4F B29C 51/00 7421-4F B29K 105: 04 C08L 67:00 (72) Inventor Masanobu Amioka 1190 Kasama-cho, Sakae-ku, Yokohama-shi, Kanagawa Mitsui Toatsu Chemical Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ポリ乳酸または乳酸とヒドロキシカルボ
ン酸のコポリマーを主成分とする熱可塑性ポリマー組成
物からなる発泡容器。
1. A foam container made of a thermoplastic polymer composition containing polylactic acid or a copolymer of lactic acid and hydroxycarboxylic acid as a main component.
【請求項2】 乳酸がL−乳酸、D−乳酸またはそれら
の混合物であることを特徴とする請求項1記載の発泡容
器。
2. The foam container according to claim 1, wherein the lactic acid is L-lactic acid, D-lactic acid or a mixture thereof.
【請求項3】 ヒドロキシカルボン酸がグリコール酸で
あることを特徴とする請求項1記載の発泡容器。
3. The foam container according to claim 1, wherein the hydroxycarboxylic acid is glycolic acid.
JP30058691A 1991-04-01 1991-11-15 Foaming container Pending JPH05139435A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP30058691A JPH05139435A (en) 1991-11-15 1991-11-15 Foaming container
CA002064410A CA2064410A1 (en) 1991-04-01 1992-03-30 Degradable foam and use of same
DE69214183T DE69214183T2 (en) 1991-04-01 1992-03-31 Degradable foam, process for its production and its use
EP92302840A EP0507554B1 (en) 1991-04-01 1992-03-31 Degradable foam, process for its preparation and use of same
US08/186,920 US5447962A (en) 1991-04-01 1994-01-27 Degradable foam and use of same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30058691A JPH05139435A (en) 1991-11-15 1991-11-15 Foaming container

Publications (1)

Publication Number Publication Date
JPH05139435A true JPH05139435A (en) 1993-06-08

Family

ID=17886627

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30058691A Pending JPH05139435A (en) 1991-04-01 1991-11-15 Foaming container

Country Status (1)

Country Link
JP (1) JPH05139435A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007052543A1 (en) 2005-11-04 2007-05-10 Unitika Ltd. Biodegradable resin foam sheet, biodegradable resin foam article and biodegradable resin molded container
JP2010280921A (en) * 2010-09-24 2010-12-16 Toray Ind Inc White polylactic acid film
KR101396528B1 (en) * 2012-08-21 2014-05-21 케이비에프(주) Biodegradable foamed pots and manufacturing method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007052543A1 (en) 2005-11-04 2007-05-10 Unitika Ltd. Biodegradable resin foam sheet, biodegradable resin foam article and biodegradable resin molded container
JP2010280921A (en) * 2010-09-24 2010-12-16 Toray Ind Inc White polylactic acid film
KR101396528B1 (en) * 2012-08-21 2014-05-21 케이비에프(주) Biodegradable foamed pots and manufacturing method thereof

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