JPH05269875A - Method for molding biodegradable resin - Google Patents

Method for molding biodegradable resin

Info

Publication number
JPH05269875A
JPH05269875A JP11949392A JP11949392A JPH05269875A JP H05269875 A JPH05269875 A JP H05269875A JP 11949392 A JP11949392 A JP 11949392A JP 11949392 A JP11949392 A JP 11949392A JP H05269875 A JPH05269875 A JP H05269875A
Authority
JP
Japan
Prior art keywords
biodegradable resin
water
oil
moisture
resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP11949392A
Other languages
Japanese (ja)
Other versions
JP3241088B2 (en
Inventor
Motoyasu Nakanishi
幹育 中西
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.)
Suzuki Sogyo Co Ltd
Original Assignee
Suzuki Sogyo Co Ltd
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 Suzuki Sogyo Co Ltd filed Critical Suzuki Sogyo Co Ltd
Priority to JP11949392A priority Critical patent/JP3241088B2/en
Publication of JPH05269875A publication Critical patent/JPH05269875A/en
Application granted granted Critical
Publication of JP3241088B2 publication Critical patent/JP3241088B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Biological Depolymerization Polymers (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:To provide molding technique highly foaming biodegradable resin without requiring a special chemical foaming agent. CONSTITUTION:A process bringing particles 1 of a moisture-containing biodegradable resin into contact with oil 5 heated to the b.p. of water or higher to boil and evaporate the moisture in the biodegradable resin and a process gathering the obtained foamed particles of the biodegradable resin and heating and/or pressing the whole of the particles to integrate the same are provided. The moisture in the biodegradable resin receives the heat of the peripheral oil to be boiled and evaporated while the biodegradable resin itself is softened or melted by the peripheral oil to be foamed by the steam pressure obtained by the boiling and evaporation of the moisture in the resin. A large number of these foamed particles are gathered to be pressed under heating and fused or bonded each other or mechanically entangled and confined in the outermost solidified and shaped skin to obtain an integrated specific whole shape.

Description

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

【0001】[0001]

【発明の目的】[Object of the Invention]

【産業上の利用分野】本発明は、地球に優しい、環境に
優しいとして、最近一段と脚光を浴びてきた生分解性樹
脂に関するものであり、詳しくはそれらの発泡及び賦形
技術に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biodegradable resin that has recently been in the spotlight as being environmentally friendly and environmentally friendly, and more particularly to a foaming and shaping technique for them.

【0002】[0002]

【発明の背景】合成樹脂は量産性、成形性、耐久性の何
れにも優れるため、今世紀驚異的な速度で技術的発展と
それに伴う消費拡大を遂げてきた。ところが、ここにき
て、これら合成樹脂が廃棄される量も莫大なものとなっ
てきたため、海上に漂ったり海岸線に打ち寄せるゴミの
中にも多くの合成樹脂製品が存在するようになり、ま
た、ゴミ焼却処理場においても、合成樹脂廃棄物が原因
で様々な問題が提起されている。すなわち、合成樹脂は
分子間結合力が非常に強いため、焼却時には高熱を発し
て炉壁を損傷し、燃焼ガスは有害ガスを大量に含む。ま
た、野ざらしにしても錆びたり、光やオゾンで分解する
こともなく、只々風雨や波動等の機械的エネルギーによ
り擦り削られてゆくのを待つしかない。特に、梱包用緩
衝材、断熱材、包装トレイ等として高発泡で成形された
ものにあっては、これが体積ばかりを要しており分別回
収もコストに見合わず、海上及び海岸線等にあってはそ
れが白色であることもあって目立つばかりの厄介な存在
であった。
BACKGROUND OF THE INVENTION Since synthetic resins are excellent in mass productivity, moldability and durability, they have achieved technological development and accompanying consumption expansion at a remarkable rate in this century. However, since the amount of these synthetic resins discarded has become enormous, many synthetic resin products are also present in the dust that floats on the sea and rushes to the coastline. Various problems have also been raised in waste incineration plants due to synthetic resin waste. That is, since the synthetic resin has a very strong intermolecular bonding force, it emits high heat during incineration to damage the furnace wall, and the combustion gas contains a large amount of harmful gas. In addition, it does not rust even if it is exposed, and it does not decompose with light or ozone, and there is no choice but to wait for it to be abraded by mechanical energy such as wind and rain and waves. In particular, as for the cushioning material for packing, the heat insulating material, the packaging tray, etc., which are molded with high foaming, it requires only a large volume and the separate collection does not justify the cost. Was an embarrassing entity, as it was white in color.

【0003】このような状況下、リサイクル運動が行わ
れるようになったり、分解性の樹脂も上市されるように
なり、分解性の樹脂にあっては技術開発が著しく、消費
も徐々に拡大の傾向にある。しかし、分解性樹脂、特に
生分解性樹脂は、その軟化ないし融点と発泡剤の発泡化
温度との関係からか、従来の化学発泡剤では高発泡させ
ることがなかなか困難であり、今、特に生分解性樹脂の
高発泡、賦形技術が求められている。
Under such circumstances, a recycling movement has been carried out, and degradable resins have been put on the market. With respect to degradable resins, technological development is remarkable and consumption is gradually expanding. There is a tendency. However, degradable resins, especially biodegradable resins, are difficult to be highly foamed by conventional chemical foaming agents because of the relationship between their softening or melting points and the foaming temperature of the foaming agents, and now, especially High foaming and shaping technology of degradable resin is required.

【0004】[0004]

【開発を試みた技術的事項】そこで、本発明は、生分解
性樹脂を格別な化学発泡剤を要することなく、高発泡に
も対処し得る成形技術を提供しようとするものである。
[Technical Items Attempted to Develop] Therefore, the present invention intends to provide a molding technique capable of coping with high foaming of a biodegradable resin without requiring a special chemical foaming agent.

【0005】[0005]

【発明の構成】[Constitution of the invention]

【目的達成の手段】すなわち、本出願に係る第一の発明
たる生分解性樹脂の成形方法は、含水した生分解性樹脂
の粒体を水の沸点以上に加熱した油と接触させ、含水水
分を生分解性樹脂中で沸騰気化させる工程と、これによ
り得た生分解性樹脂の発泡粒体を多数集合させた上で、
この全体を加熱及び/又は加圧して一体化せしめる工程
とを有することを特徴とする。また、本出願に係る第二
の発明たる生分解性樹脂の成形方法は、含水した生分解
性樹脂の粒体を水の沸点以上に加熱した油と接触させ、
含水水分を生分解性樹脂中で沸騰気化させる工程と、こ
れにより得た生分解性樹脂の発泡粒体を接着成分ととも
に多数集合させた上で、この全体を加熱及び/又は加圧
して一体化せしめる工程とを有することを特徴とする。
これら発明によって前記目的を達成しようとするもので
ある。
[Means for Achieving the Object] That is, the method for molding a biodegradable resin, which is the first invention of the present application, comprises contacting hydrous granules of biodegradable resin with oil heated above the boiling point of water, After boil vaporizing in a biodegradable resin, and after collecting a large number of foam particles of the biodegradable resin obtained by this,
A step of heating and / or pressurizing the whole to integrate them. Further, the method of molding the biodegradable resin according to the second invention of the present application, the granules of hydrous biodegradable resin is contacted with oil heated above the boiling point of water,
A step of boiling and evaporating water-containing water in a biodegradable resin, and a large number of biodegradable resin foam granules thus obtained are collected together with an adhesive component, and the whole is heated and / or pressurized to be integrated. And a step of setting.
These inventions are intended to achieve the above object.

【0006】[0006]

【発明の作用】本発明では、生分解性樹脂中の含水水分
は、周囲の油の熱を受領して沸騰気化する。一方、生分
解性樹脂自身は周囲の油で軟化ないし溶融するため、内
部で沸騰気化した水蒸気圧で膨化つまり発泡する。そし
て、これにより得た発泡粒体が必要により接着成分とと
もに多数集合され、全体が加熱及び/又は加圧されれ
ば、その相互の接触部位が融着し合ったり、接着された
り、機械的に絡み合ったり、最外郭が形状固化して閉じ
こめられたりして、一体化した特定の全体形状を呈する
ようになる。
In the present invention, the water-containing water in the biodegradable resin receives the heat of the surrounding oil and evaporates by boiling. On the other hand, since the biodegradable resin itself is softened or melted by the surrounding oil, it expands or foams due to the vapor pressure of the vaporized inside. Then, a large number of the foamed granules thus obtained are aggregated together with an adhesive component if necessary, and if the whole is heated and / or pressurized, their mutual contact portions are fused or bonded, or mechanically. It becomes entangled, or the outermost contour is solidified and enclosed, so that it has an integrated specific overall shape.

【0007】[0007]

【実施例】次に本発明をその構成要素たる生分解性樹脂
について説明した後、図示の実施例に基づいて具体的に
説明する。本発明における生分解性樹脂とは生物学的作
用に基づき物性を低下する樹脂材料を意味し、これには
樹脂自体が完全に分解するタイプと、分解し難い樹脂と
ブレンドし崩壊性を付与したタイプとがある。そして、
前者のタイプには微生物による生産物、天然高分子の利
用品、石油系原料からの生成品等があり、また、後者の
タイプにはでん粉とのブレンド体、脂肪族ポリエステル
とのブレンド体等がある。これらの生分解機構として
は、リパーゼ、アミラーゼ、セルラーゼ、プロテアーゼ
等の酵素による分解、活性汚泥中等の微生物による分
解、森林、耕作地等の自然環境における土壌による分解
等、種々の態様がある。更に具体的には、ポリヒドロキ
シン酪酸及びその誘導体、プルラン、セルロース−キト
サン混合体、セルロースやアミロースや木粉のエステル
化物、ポリエステル−ナイロン共重合体、ポリエステル
共重合体、澱粉とポリエチレンとのブレンド体をはじ
め、ポリビニルアルコール、ポリエーテル、ポリウレタ
ン、ポリアミド等が挙げられる。これらはおしなべて低
融点を有し、水の存在下に分解促進されるものである。
また、水の沸点以上に加熱される油とは、動物油、植物
油、鉱物油、化学合成油等、種々のものであってよい
が、安全性が高く、粘性が低くて、後の分離回収が容易
なものが適する。
EXAMPLES The present invention will be described below with reference to biodegradable resins as its constituent elements, and then concretely based on the illustrated examples. The biodegradable resin in the present invention means a resin material whose physical properties are deteriorated based on a biological action, and a type in which the resin itself is completely decomposed and a resin which is difficult to decompose are blended to impart disintegration property. There is a type. And
The former type includes products produced by microorganisms, products using natural polymers, products produced from petroleum-based raw materials, and the latter type includes blends with starch and blends with aliphatic polyesters. is there. As the biodegradation mechanism, there are various modes such as degradation by enzymes such as lipase, amylase, cellulase and protease, degradation by microorganisms such as activated sludge, and degradation by soil in natural environments such as forests and cultivated land. More specifically, polyhydroxybutyric acid and its derivatives, pullulan, cellulose-chitosan mixture, esterification products of cellulose, amylose and wood flour, polyester-nylon copolymer, polyester copolymer, blend of starch and polyethylene In addition to the body, polyvinyl alcohol, polyether, polyurethane, polyamide and the like can be mentioned. These generally have a low melting point and are accelerated in the presence of water.
Further, the oil heated above the boiling point of water may be various ones such as animal oil, vegetable oil, mineral oil, chemically synthesized oil, etc., but it has high safety and low viscosity, and is separated and recovered later. Easy ones are suitable.

【0008】本実施例では、生分解性樹脂に日本合成化
学工業株式会社販売のMater−Bi「マタービー」
(登録商標)のペレット状のものを用い、また油として
は市販食用のサラダオイルを用いた。ここで、生分解性
樹脂としてのMater−Biは、イタリアのモンテジ
ソングループに属するNOVAMONT社の開発に係
り、植物からの精製物質と合成高分子とが分子レベルで
相互に相手分子中に潜り込み、水素結合により結ばれて
なる、熱可塑性の生分解性ポリマーとされているもので
ある。また、その融点は140℃前後とされており、水
を吸収して膨潤することにより生分解促進され、微生物
生存の環境下で紙と同等の生分解性を示すとされている
ものである。
In this example, the biodegradable resin was used as Mater-Bi "Matterby" sold by Nippon Synthetic Chemical Industry Co., Ltd.
(Registered trademark) pellets were used, and the commercially available edible salad oil was used as the oil. Here, Mater-Bi as a biodegradable resin is involved in the development of NOVAMONT, which belongs to the Montedison Group of Italy, and a purified substance from a plant and a synthetic polymer dip into each other at the molecular level, It is a thermoplastic biodegradable polymer formed by hydrogen bonds. Further, its melting point is around 140 ° C., and it is said that biodegradation is promoted by absorbing water and swelling, and exhibits biodegradability equivalent to that of paper under the environment of microbial survival.

【0009】本実施例では、前処理工程として、この生
分解性樹脂に水を積極的に含水させる含水工程を設け
た。具体的には、図1のごとく、容器2に十分な水3を
注ぎ、水没させた状態でペレット状の生分解性樹脂1を
10時間漬けた。図示しないが、この後、含水させた生
分解性樹脂を取り出して吸水紙上に広げ、表面に付着す
る水滴を取り除き、次に述べる工程の前処理とした。な
お、この含水工程は、この他、適度に加温ないし沸騰し
た湯中に浸漬してもよいし、高湿度雰囲気下に長時間放
置してもよい。このような含水工程を設けることによ
り、大気下における平衡水分よりも多く含水させること
ができるから、より高発泡化させることが可能となる。
また、十分に計算管理された含水工程によれば、生分解
性樹脂の表皮層と芯部とにおける含水程度を均一にして
一様に発泡したものが得られやすい。勿論、平衡水分が
求められる発泡倍率にとって必要十分であれば、敢えて
含水工程を設けるまでもなく、大気下に放置され平衡水
分を含む生分解性樹脂をそのまま用いてもよい。
In this embodiment, a water-containing step of positively containing water in this biodegradable resin was provided as a pretreatment step. Specifically, as shown in FIG. 1, sufficient water 3 was poured into the container 2, and the pelletized biodegradable resin 1 was immersed in the water for 10 hours. Although not shown, after this, the hydrolyzed biodegradable resin was taken out and spread on a water-absorbent paper to remove water droplets adhering to the surface, which was the pretreatment for the next step. In addition to this, the water-containing step may be immersed in hot water that is appropriately heated or boiled, or may be left for a long time in a high humidity atmosphere. By providing such a water-containing step, more water can be contained than the equilibrium water content in the atmosphere, so that the foaming can be further increased.
Further, according to the water-containing step which is sufficiently calculated and controlled, it is easy to obtain the one in which the biodegradable resin has a uniform water content in the skin layer and the core portion and is uniformly foamed. Of course, if the equilibrium water content is necessary and sufficient for the required expansion ratio, the biodegradable resin containing the equilibrium water content that is left in the atmosphere may be used as it is without needing to provide a water-containing step.

【0010】続く、本発明の特徴たる水の沸点以上に加
熱した油と接触させる工程は、本実施例ではごく普通の
気温、湿度の大気圧下において、図2のごとく、鍋4に
満たしたサラダオイル5をガスレンジ6で130℃〜1
80℃程度に加熱し、このサラダオイル5中に前記含水
工程を経て得られた含水した生分解性樹脂1をペレット
状のままで分散落下させて行なった。
In the subsequent step of contacting with oil heated above the boiling point of water, which is a feature of the present invention, the pot 4 is filled under atmospheric pressure of ordinary temperature and humidity in this embodiment as shown in FIG. Salad oil 5 with a gas stove 6 at 130 ℃ -1
It was heated to about 80 ° C., and the water-containing biodegradable resin 1 obtained through the water-containing step was dispersed and dropped in this salad oil 5 in the form of pellets.

【0011】含水した生分解性樹脂1が加熱された油5
中に没入すると、生分解性樹脂には油の大量の熱量がそ
の表面から伝達され、生分解性樹脂自体とともにその含
水水分がほぼ同時的に加熱されて急速に温度上昇する。
この温度上昇は水の沸点以上に至るため、含水水分は生
分解性樹脂中で沸騰気化する。生分解性樹脂も同時的に
軟化温度ないし融点に至っているため、内部で沸騰気化
した水蒸気圧により、生分解性樹脂自身が膨化、発泡し
た状態となる。この作用は、その表皮層から順次行なわ
れ、小粒のものにあっては全体がほぼ同時的に瞬時に近
く行なわれるが、比較的大粒のものにあっては表皮層か
ら芯部に向かって順次同作用が連続的して行なわれ、間
もなく全体がほぼ一様に膨化、発泡した状態となる。な
お、この油没入の初期に隣接し合った生分解性樹脂同士
は、互いが融着し合って発泡した群塊状のものとして得
られることもある。
Oil 5 obtained by heating biodegradable resin 1 containing water
When immersed, a large amount of heat of oil is transferred from the surface to the biodegradable resin, and the water content of water is heated almost simultaneously with the biodegradable resin itself, and the temperature rises rapidly.
Since this temperature increase reaches the boiling point of water or higher, the water content of water is vaporized in the biodegradable resin. Since the biodegradable resin has also reached the softening temperature or melting point at the same time, the biodegradable resin itself is expanded and foamed due to the vapor pressure of the water vaporized inside. This action is performed sequentially from the skin layer, and in the case of small grains, the whole is almost instantaneously performed almost instantaneously, but in the case of relatively large grains, it is sequentially performed from the skin layer to the core. The same action is continuously performed, and soon the whole becomes almost uniformly inflated and foamed. The biodegradable resins that are adjacent to each other in the initial stage of oil immersion may be obtained in the form of a lump that is fused and foamed with each other.

【0012】この実施例では、油の温度を160℃〜1
80℃としたときに、約8〜10倍程度の発泡倍率をも
って発泡させることができ、市販の化学発泡剤を数%添
加して得られた2倍程度の発泡倍率に比べ、遥かに高発
泡化させることができた。このようにして得られた生分
解性樹脂の発泡粒体は、その後、遠心分離や洗浄、乾燥
等を行うことにより、付着油が分離回収されるのが望ま
しく、分離回収した油は、次回の工程用の油として用い
ればよい。また、この工程における油の温度が低いと、
生分解性樹脂の軟化ないし融点にゆっくりと至り沸騰気
化による水蒸気圧が一気に利用されないため比較的低発
泡のものが、また、油の温度が高いと、沸騰気化した水
蒸気が一気に開放されるので比較的高発泡のものが得る
ことができる。
In this embodiment, the oil temperature is from 160 ° C to 1 ° C.
When the temperature is set to 80 ° C., foaming can be performed with an expansion ratio of about 8 to 10 times, which is much higher than the expansion ratio of about 2 times obtained by adding a few% of a commercially available chemical foaming agent. I was able to make it. The foamed granules of the biodegradable resin thus obtained are then subjected to centrifugation, washing, drying, etc., so that the adhered oil is desirably separated and recovered. It may be used as an oil for the process. Also, if the oil temperature in this step is low,
A comparatively low foaming type because the steam pressure due to boiling vaporization is not utilized at once because the biodegradable resin softens or melts slowly, and when the oil temperature is high, boiling vaporized steam is released all at once. A highly foamed product can be obtained.

【0013】このようにして得られた生分解性樹脂の発
泡粒体10は、本実施例では次工程として図3に示すご
とくの成形型7内に集合され、加熱及び加圧される。す
なわち、図3において前記工程を経て得られた生分解性
樹脂の発泡粒体10は、予定の充填率を考慮して定めら
れた適当量が、成形型7のキャビティー内に置かれる。
この成形型7は、上型7aと下型7bとがガイドピン7
1、71に案内されて上下動自在となっており、二点鎖
線Aで示すように上型7aと下型7bとが閉じられて内
部に断面肉厚アングル状のキャビティーを形成するよう
になっている。また、上型7aと下型7bには加熱手
段、図示実施例ではヒーター8が設けてあり、成形型7
を通してキャビティー内に置かれる発泡粒体10を加熱
できるようになっている。また、成形型7全体は図示し
ないプレス機における基盤と加圧盤との間に設置され
る。なお、この実施例では成形型7内に加熱手段8を配
したが、プレス機として加硫プレス機を用いるときには
それ自体が加熱手段を設けているので、成形型に熱伝導
性の良いものを用いさえすればよい。
The foamed granules 10 of the biodegradable resin thus obtained are assembled in a molding die 7 as shown in FIG. 3 and heated and pressed in the next step in this embodiment. That is, in FIG. 3, the expanded granules 10 of biodegradable resin obtained through the above steps are placed in the cavity of the molding die 7 in an appropriate amount determined in consideration of the expected filling rate.
In this molding die 7, the upper die 7a and the lower die 7b are guide pins 7
The upper mold 7a and the lower mold 7b are closed as shown by the two-dot chain line A so as to form a cavity having a thick-walled cross section inside. Is becoming Further, the upper die 7a and the lower die 7b are provided with heating means, in the illustrated embodiment, a heater 8,
The expanded granules 10 placed in the cavity can be heated. Further, the entire molding die 7 is installed between a base and a pressure plate in a press machine (not shown). In this embodiment, the heating means 8 is arranged in the molding die 7, but when a vulcanizing press is used as the pressing machine, the heating means itself is provided, so that the molding die having good thermal conductivity should be used. All you have to do is use it.

【0014】そこで、予め成形型7のヒーター8に通電
しておき、あるいは発泡粒体10をキャビティー内に配
した上で通電し、成形型7が温度上昇して発泡粒体10
がその軟化ないし融点付近に加熱昇温されたタイミング
を見計らい、プレス機にて成形型7を押圧し、上型7a
と下型7bとを閉じるようにすれば、内部の発泡粒体1
0は一部押し潰されつつ互いに入り組み合い、一部は互
いが融着し合い、特に成形型の内壁と接触する部分では
それに沿って比較的堅固に隣接発泡粒体同士が融着し合
い、外郭がキャビティー形状に賦形された一個の成形物
となる。さらに、加熱及び加圧の状態を暫く保持して内
部での融着等の確実化を図った上で、プレス機による押
圧を停止して、上型7aと下型7bとを解放し、キャビ
ティー内の成形物を取り出せば、発泡粒体10の集合は
肉厚アングル状の棒体として得ることができる。なお、
このとき内部での融着等の確実化を図る上で、加圧中に
加熱を中断したり、あるいは積極的に冷却する等は適宜
行ない得るものである。
Therefore, the heater 8 of the molding die 7 is energized in advance, or the expanded granules 10 are placed in the cavity and then energized so that the temperature of the molding die 7 rises and the expanded granules 10 are heated.
The softening or heating point near the melting point, the molding die 7 is pressed by the press machine and the upper die 7a is pressed.
If the lower mold 7b and the lower mold 7b are closed, the foamed granules 1 inside
0 is partially crushed and intermingled with each other, and some of them are fused to each other, and particularly, in the portion that comes into contact with the inner wall of the molding die, the adjacent foamed granules are relatively firmly fused to each other, The outer shell becomes a single molded product shaped into a cavity. Furthermore, after maintaining the heating and pressurizing state for a while to ensure internal fusion and the like, the pressing by the pressing machine is stopped, and the upper mold 7a and the lower mold 7b are released, and If the molded product in the tee is taken out, the aggregate of the expanded granules 10 can be obtained as a thick angled rod. In addition,
At this time, in order to ensure internal fusion and the like, it is possible to appropriately suspend heating during pressurization, actively cool, or the like.

【0015】このようにして得られた生分解性樹脂の発
泡粒体10の集合成形物たる肉厚アングル状の棒体は、
梱包用段ボール箱における梱包物のコーナー支持材とし
て用いることができる。これは万一、不法投棄された場
合であっても生分解するため、海上に漂ったり海岸線に
打ち寄せていても、暫くすれば分解してしまい、また地
上に放っておいても風雨や地中の湿気を吸って分解して
ゆくため、敢えてゴミ焼却処理場にて処分する必要もな
い。しかも、これは比較的高発泡品として得られ、ま
た、格別な化学発泡剤を要せず得られる。
An angled rod having a thick wall, which is an aggregate molded product of the expanded beads 10 of the biodegradable resin thus obtained, is
It can be used as a corner support material for a package in a packaging cardboard box. Even if it is illegally dumped, it will biodegrade, so even if it floats on the sea or hits the coastline, it will be decomposed after a while, and even if it is left on the ground it will wind and rain and underground. Since it absorbs the moisture of the product and decomposes it, there is no need to dispose of it at a refuse incineration plant. Moreover, it can be obtained as a comparatively high foaming product and does not require a special chemical foaming agent.

【0016】なお、上記工程において、成形型7への加
熱程度が生分解性樹脂の融点を遥かに越えてしまうと、
その前工程で比較的高発泡させて発泡粒体10として得
た意味が失われてしまう。このためには、発泡粒体とし
て、融点の低い生分解性樹脂による発泡粒体を別途加え
たり、融点の低い分解性樹脂の粉体、熱可塑性樹脂、さ
らには糊等の接着機能を有する成分を添加してもよい。
この他本願にいう接着成分としては、デンプン糊、ふの
り、アラビアガム、ニカワ、カゼイン、アマニ油、酢酸
デンプン・カルボキシメチルスターチ等のデンプン誘導
体、メチルセルロース・エチルセルロース等の繊維素誘
導体、アルギン酸ソーダ、ローカストビーンガム、ポリ
ビニルアルコール等のビニル系合成糊、酢酸ビニルアク
リル酸共重合物等のビニル系共重合物合成糊、ポリアク
リル酸ソーダ等のアクリル系合成糊、スチロールマレイ
ン酸共重合物等のスチロール系合成糊等、天然、半合
成、合成糊をはじめ、接着剤は勿論、各種樹脂を適宜溶
剤に溶かした溶液、さらには生分解性樹脂を軟化膨潤さ
せる溶剤等であってもよい。これら接着成分とともに発
泡粒体を集合させた上で加熱加圧すれば、前記実施例と
同様に発泡粒体が融着し合い機械的に絡み合う他、接着
成分により融着し合ったり、接着されたりして、全体が
特定形状に賦形されることになる。
In the above process, if the heating degree of the mold 7 far exceeds the melting point of the biodegradable resin,
The meaning obtained as the expanded granules 10 by relatively high-foaming in the previous step is lost. To this end, as the foamed granules, foamed granules made of a biodegradable resin having a low melting point are added separately, or a powder of a degradable resin having a low melting point, a thermoplastic resin, and a component having an adhesive function such as glue. May be added.
In addition to this, as the adhesive component referred to in the present application, starch paste, furi, gum arabic, glue, casein, linseed oil, starch derivatives such as starch acetate / carboxymethyl starch, fibrin derivatives such as methyl cellulose / ethyl cellulose, sodium alginate, locust bean. Gum, vinyl synthetic adhesives such as polyvinyl alcohol, vinyl acetate synthetic adhesives such as vinyl acetate acrylic acid copolymers, acrylic synthetic adhesives such as sodium polyacrylate, styrene synthetic adhesives such as styrene-maleic acid copolymers In addition to adhesives such as glue, natural, semi-synthetic, and synthetic glues, adhesives may be used, as well as solutions in which various resins are appropriately dissolved in solvents, and solvents that soften and swell biodegradable resins may be used. By heating and pressurizing the expanded granules together with these adhesive components, the expanded granules are fused and mechanically entangled in the same manner as in the above-described example, and are also fused and bonded by the adhesive component. As a result, the whole is shaped into a specific shape.

【0017】さらに、後処理工程として、重荷重にも耐
え寿命を持たせようとするのであれば、その後、耐水性
塗料等で塗装してもよい。本発明では、この他、平板状
の成形型間にてシート状のものを得たり、トレイ状に賦
形したり、瀬戸物、ガラス製品、精密機器、高級果物等
の緩衝材として各種形状に賦形したりして、従来の発泡
スチロール等の発泡体が用いられていたと同様に使用す
ることができる。なお、以上の実施例では生分解性樹脂
にMater−Bi「マタービー」(登録商標)のペレ
ット状のものを用い、また油としてはサラダオイルを用
いたが、本発明はこれらに限定されるものではなく、そ
の他の生分解性樹脂が、また各種の大きさ形状の生分解
性樹脂が、さらに、その他の油が適用できるものであ
る。場合によっては、加熱された油が液状として生分解
性樹脂に接触するのではなく、これがガス状となって充
満している雰囲気下において接触する場合であっても施
用可能なものであり、また、含水工程や遠心分離、洗
浄、乾燥、塗装等の前処理工程及び後処理工程は必ずし
も必要ではなく適宜付加できる工程である。また、油が
乾燥性油脂であるときは、これが接着成分として使用で
きる場合もあるため、発泡粒体に付着している油を回収
することなく、これをそのまま接着成分として使用して
もよい。さらに、上記実施例ではバッチ式に成形型にて
1回毎賦形していたが、所定断面の連続棒状の集合成形
物を必要とするときは、いわゆる押出成形的に筒状成形
型で徐々に加熱及び/又は加圧して連続的に賦形するよ
うにしてもよい。また、上記実施例では、加熱及び加圧
するようにしたが、この何れか一方を作用させる場合で
あっても、発泡粒体の相互が融着し合ったり、接着され
たり、機械的に絡み合ったり、最外郭が形状固化して閉
じこめられたりして、一体化した特定の全体形状を呈せ
ばよい。
Further, as a post-treatment step, if it is intended to endure a heavy load and have a life, a water-resistant paint or the like may be applied thereafter. In addition to the above, in the present invention, a sheet-like material is obtained between flat plate-shaped molding dies, or it is shaped into a tray, or is applied to various shapes as a cushioning material for crockery, glass products, precision instruments, high-grade fruits and the like. It can be shaped and used in the same manner as in the case where conventional foams such as Styrofoam were used. In the above examples, Mater-Bi "Matterby" (registered trademark) pellets were used as the biodegradable resin, and salad oil was used as the oil, but the present invention is not limited to these. Instead, other biodegradable resins, biodegradable resins of various sizes and shapes, and other oils can be applied. In some cases, the heated oil does not come into contact with the biodegradable resin as a liquid, but it can be applied even when the heated oil comes into contact with the biodegradable resin under a filled atmosphere. The water-containing step, the pretreatment step and the posttreatment step such as centrifugation, washing, drying, and painting are not necessarily required and can be appropriately added. In addition, when the oil is a drying fat or oil, it may be used as an adhesive component in some cases, and therefore, the oil adhering to the foam granules may be used as it is as an adhesive component without being recovered. Further, in the above-mentioned embodiment, the molding was performed batchwise by the molding die once, but when a continuous rod-shaped aggregate molding having a predetermined cross section is required, it is gradually extruded by a so-called extrusion molding in a cylindrical molding die. Alternatively, heating and / or pressure may be applied to continuously shape. Further, in the above-mentioned embodiment, the heating and the pressing are performed, but even when either one of them is made to act, the foamed granules are fused to each other, adhered, or mechanically entangled with each other. The outermost contour may be solidified and confined to present an integrated specific overall shape.

【0018】[0018]

【発明の効果】以上、本発明によれば、生分解性樹脂を
格別な化学発泡剤を要することなく、高発泡にも対処し
得て、発泡及び適宜形状に賦形することができ、従来の
発泡体の代替品として提供し得て、今や重要課題のゴミ
公害の軽減に寄与することができる。
As described above, according to the present invention, the biodegradable resin can cope with high foaming without requiring a special chemical foaming agent, and can be foamed and shaped into an appropriate shape. It can be provided as a substitute for the foam of the present invention and can contribute to the reduction of garbage pollution, which is now an important issue.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明生分解性樹脂の成形方法の一実施例にお
ける前処理工程たる含水工程の状態を示す斜視図であ
る。
FIG. 1 is a perspective view showing a state of a water-containing step as a pretreatment step in an example of the method for molding a biodegradable resin of the present invention.

【図2】本発明生分解性樹脂の成形方法の一実施例にお
ける発泡化工程の状態を示す斜視図である。
FIG. 2 is a perspective view showing a state of a foaming step in one example of the method for molding a biodegradable resin of the present invention.

【図3】本発明生分解性樹脂の成形方法の一実施例にお
ける賦形工程の状態を示す成形型の一部断面図である。
FIG. 3 is a partial cross-sectional view of a molding die showing a state of a shaping step in one example of the method for molding a biodegradable resin of the present invention.

【符号の説明】[Explanation of symbols]

1 生分解性樹脂 2 容器 3 水 4 鍋 5 油 6 ガスレンジ 7 成形型 7a 上型 7b 下型 71 ガイドピン 8 ヒーター(加熱手段) 10 生分解性樹脂の発泡粒体 1 biodegradable resin 2 container 3 water 4 pan 5 oil 6 gas range 7 molding die 7a upper die 7b lower die 71 guide pin 8 heater (heating means) 10 foam granules of biodegradable resin

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】含水した生分解性樹脂の粒体を水の沸点以
上に加熱した油と接触させ、含水水分を生分解性樹脂中
で沸騰気化させる工程と、これにより得た生分解性樹脂
の発泡粒体を多数集合させた上で、この全体を加熱及び
/又は加圧して一体化せしめる工程とを有することを特
徴とする生分解性樹脂の成形方法。
1. A step of bringing water-containing biodegradable resin granules into contact with oil heated to a boiling point of water or higher to evaporate water-containing water in the biodegradable resin by boiling, and a biodegradable resin obtained thereby. A method of molding a biodegradable resin, which comprises a step of collecting a large number of the expanded granules and then heating and / or pressurizing the whole to integrate them.
【請求項2】含水した生分解性樹脂の粒体を水の沸点以
上に加熱した油と接触させ、含水水分を生分解性樹脂中
で沸騰気化させる工程と、これにより得た生分解性樹脂
の発泡粒体を接着成分とともに多数集合させた上で、こ
の全体を加熱及び/又は加圧して一体化せしめる工程と
を有することを特徴とする生分解性樹脂の成形方法。
2. A step of bringing hydrous biodegradable resin granules into contact with oil heated to a boiling point of water or higher to evaporate hydrous water in the biodegradable resin, and a biodegradable resin obtained thereby. And a step of assembling a large number of the foamed granules together with the adhesive component, and heating and / or pressurizing the whole to integrate them.
JP11949392A 1992-03-27 1992-03-27 Molding method of biodegradable resin Expired - Fee Related JP3241088B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11949392A JP3241088B2 (en) 1992-03-27 1992-03-27 Molding method of biodegradable resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11949392A JP3241088B2 (en) 1992-03-27 1992-03-27 Molding method of biodegradable resin

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP8274799A Division JPH11314277A (en) 1999-03-26 1999-03-26 Biodegradable resin composition and molding method thereof

Publications (2)

Publication Number Publication Date
JPH05269875A true JPH05269875A (en) 1993-10-19
JP3241088B2 JP3241088B2 (en) 2001-12-25

Family

ID=14762636

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11949392A Expired - Fee Related JP3241088B2 (en) 1992-03-27 1992-03-27 Molding method of biodegradable resin

Country Status (1)

Country Link
JP (1) JP3241088B2 (en)

Also Published As

Publication number Publication date
JP3241088B2 (en) 2001-12-25

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