JPH09286870A - Production of biodegradable resin foam - Google Patents

Production of biodegradable resin foam

Info

Publication number
JPH09286870A
JPH09286870A JP8122697A JP12269796A JPH09286870A JP H09286870 A JPH09286870 A JP H09286870A JP 8122697 A JP8122697 A JP 8122697A JP 12269796 A JP12269796 A JP 12269796A JP H09286870 A JPH09286870 A JP H09286870A
Authority
JP
Japan
Prior art keywords
resin
biodegradable
biodegradable resin
starch
softening point
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
JP8122697A
Other languages
Japanese (ja)
Inventor
Jun Furuhashi
潤 古橋
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.)
Kyocera Chemical Corp
Original Assignee
Toshiba Chemical Corp
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 Toshiba Chemical Corp filed Critical Toshiba Chemical Corp
Priority to JP8122697A priority Critical patent/JPH09286870A/en
Publication of JPH09286870A publication Critical patent/JPH09286870A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a process whereby a biodegradable resin foam which does not shrink just after molding and is excellent in mechanical strengths can be produced whole using a generally used molding machine. SOLUTION: A biodegradable resin compsn, essentially comprising a starch- based biodegradable resin, a biodegradable polyester resin having an m.p. or softening point higher then that of the foregoing resin, and a foaming agent is molded and foamed at a temp, somewhat higher than the m.p. or softening point.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、一般の成形機で成
形でき、強度の優れた生分解性樹脂発泡体の製造方法に
関する。
TECHNICAL FIELD The present invention relates to a method for producing a biodegradable resin foam which can be molded by a general molding machine and has excellent strength.

【0002】[0002]

【従来の技術】近年、環境問題の高まりから合成樹脂成
形品の廃棄対策が求められている。特に包装材は、使用
後すぐに廃棄されることが多く、中でも緩衝材として用
いられている発泡成形品は重量の割にかさばるため、従
来の熱可塑性樹脂発泡体から、廃棄時に微生物によって
分解する生分解性発泡体へ置き替える動きが出始めてい
る。
2. Description of the Related Art In recent years, due to increasing environmental problems, measures for discarding synthetic resin molded products are required. In particular, packaging materials are often discarded immediately after use. Among them, foamed moldings used as cushioning materials are bulky for their weight, so they are decomposed from conventional thermoplastic resin foams by microorganisms at the time of disposal. There is a movement to replace biodegradable foam.

【0003】[0003]

【発明が解決しようとする課題】生分解性樹脂は、澱粉
系、化学合成系、微生物合成系の3 種に大別されるが、
そりいずれに関しても、現在熱可塑性樹脂発泡体とし
て、発泡スチレン等で確立されているような、樹脂中に
揮発性ガスを混練したペレットを予備発泡させて後、型
内にて加熱発泡させるといった製造方法をそのまま用い
ることは、樹脂の性質から困難な状況にある。
The biodegradable resins are roughly classified into three types, starch type, chemical synthetic type and microbial synthetic type.
With regard to both sleds, as the thermoplastic resin foam is currently established as foamed styrene, etc., pellets prepared by kneading a volatile gas in resin are pre-expanded and then heat-foamed in a mold. It is difficult to use the method as it is because of the nature of the resin.

【0004】そこで、押出し機や射出成形機のシリンダ
の中で、発泡成分を含んだ樹脂を加圧状態下で加熱溶融
させた後、ノズルから出して発泡させる方法が行われて
いる。この方法では樹脂を発泡させた後、大気中で冷却
した時に発泡セル中の発泡成分が収縮し、負圧となるこ
とから、その時点で樹脂が固化していないと、折角でき
たセルが収縮してしまうために、成形温度を樹脂の融点
又は軟化点より若干高く設定し樹脂がノズルから出た後
にすぐに固化するようにしなければならない。ところ
が、現在市販されている生分解性樹脂の多くは融点又は
軟化点が低く、特に澱粉系樹脂は、100 〜150 ℃と比較
的低温のものが多いことに加え、澱粉系生分解性樹脂は
混練によって生じる剪断発熱が大きく、シリンダ温度が
直ぐに上昇してしまうため、発泡後のセルの収縮を生じ
ない樹脂の融点又は軟化点より若干高いという、発泡に
最適な成形温度で一定に保つためには、混練速度を落と
さなければならないという製造条件の制限を受けたり、
混練・成形装置に水冷等の冷却機能を持たせければなら
ない。しかしながら、ただでさえ困難な発泡成形の条件
を制限することは製品特性に致命的な打撃を与えかね
ず、冷却を行うにしても、通常の射出成形機、押出し機
には冷却機能をもたせたものは少なく、さらにそれを制
御するシステムをもつものはさらにに少ないため、発泡
成形を行うためには特別の装置を製作するか追加する必
要があり、コストの高いものとなってしまう欠点があっ
た。
Therefore, in a cylinder of an extruder or an injection molding machine, a method is used in which a resin containing a foaming component is heated and melted under pressure and then discharged from a nozzle to foam. In this method, after the resin has been foamed, when it is cooled in the atmosphere, the foaming component in the foamed cell contracts, resulting in a negative pressure, so if the resin has not solidified at that point, the cell that could bend will contract. Therefore, the molding temperature must be set slightly higher than the melting point or softening point of the resin so that the resin solidifies immediately after it comes out of the nozzle. However, most of the biodegradable resins currently on the market have a low melting point or softening point, and in particular, many starch-based resins have relatively low temperatures of 100 to 150 ° C. Since the shearing heat generated by kneading is large and the cylinder temperature rises immediately, in order to keep constant at the optimum molding temperature for foaming, which is slightly higher than the melting point or softening point of the resin that does not cause cell shrinkage after foaming. Is limited by the manufacturing conditions that the kneading speed must be reduced,
The kneading / molding equipment must have a cooling function such as water cooling. However, limiting the conditions of foam molding, which is difficult even by itself, could have a fatal impact on the product characteristics, and even if cooling was performed, ordinary injection molding machines and extruders had a cooling function. There are few things, and even less things have a system to control it, so it is necessary to manufacture or add a special device to perform foam molding, which is a disadvantage that the cost becomes high. It was

【0005】本発明は、上記の欠点を解消するためにな
されたもので、一般の成形機を用い発泡成形が可能で、
成形直後の収縮がなく、機械的強度に優れた生分解性樹
脂発泡の製造方法を提供しようとするものである。
The present invention has been made in order to solve the above-mentioned drawbacks, and it is possible to perform foam molding using a general molding machine.
An object of the present invention is to provide a method for producing a biodegradable resin foam which does not shrink immediately after molding and is excellent in mechanical strength.

【0006】[0006]

【課題を解決するための手段】本発明者は、上記の目的
を達成しようと鋭意研究を重ねた結果、澱粉系生分解性
樹脂よりも、融点又は軟化点の高い生分解性ポリエステ
ル樹脂をブレンドすることによって、上記の目的を達成
できることを見いだし、本発明を完成したものである。
Means for Solving the Problems As a result of intensive studies to achieve the above object, the present inventor has blended a biodegradable polyester resin having a higher melting point or softening point than a starch-based biodegradable resin. It was found that the above-mentioned objects can be achieved by doing so, and the present invention has been completed.

【0007】即ち、本発明は、(A)澱粉系生分解性樹
脂、(B)生分解性ポリエステル樹脂および(C)発泡
剤を必須成分とする生分解性樹脂組成物であって、前記
(B)の生分解性ポリエステル樹脂が前記(A)の澱粉
系生分解性樹脂より高い融点又は軟化点を有し、前記融
点または軟化点より若干高い温度で生分解性樹脂組成物
を成形、発泡させることを特徴とする生分解性樹脂発泡
体の製造方法である。
That is, the present invention provides a biodegradable resin composition comprising (A) a starch-based biodegradable resin, (B) a biodegradable polyester resin, and (C) a foaming agent as essential components, wherein The biodegradable polyester resin of B) has a higher melting point or softening point than the starch-based biodegradable resin of (A), and the biodegradable resin composition is molded and foamed at a temperature slightly higher than the melting point or softening point. And a method for producing a biodegradable resin foam, which comprises:

【0008】以下、本発明を詳細に説明する。Hereinafter, the present invention will be described in detail.

【0009】本発明に用いる生分解性樹脂組成物は、
(A)澱粉系生分解性樹脂、(B)生分解性ポリエステ
ル樹脂および(C)発泡剤を必須成分とするものであ
る。次にこれらの各成分について説明する。
The biodegradable resin composition used in the present invention is
(A) Starch-based biodegradable resin, (B) Biodegradable polyester resin, and (C) Foaming agent are essential components. Next, each of these components will be described.

【0010】(A)澱粉系生分解性樹脂としては、トウ
モロコシ、イモ、タピオカ等から精製される澱粉をその
まま或いは変性させたものに、加工性を上げるためにポ
リビニルアルコール、ポリアクリル酸、ポリカプロラク
タン等の生分解性樹脂をブレンドしたもの等が挙げら
れ、これらは単独又は2 種以上混合して使用することが
できる。
As the starch-based biodegradable resin (A), starch refined from corn, potato, tapioca, etc. is used as it is or modified, and polyvinyl alcohol, polyacrylic acid, polycaproic acid are added to improve processability. Examples include blends of biodegradable resins such as lactan, and these can be used alone or in combination of two or more.

【0011】(B)生分解性ポリエステル樹脂として
は、ポリ乳酸、ポリブチレンサクシネート、ポリブチレ
ンジグリコレート、ポリヒドロキシブチラート系共重合
体、エステル型ポリウレタン等の化学合成系、微生物系
のポリエステル樹脂が挙げられ、これらは単独又は2 種
以上混合して使用することができる。この生分解性ポリ
エステル樹脂は、前述した(A)の澱粉系生分解性樹脂
よりも高い融点又は軟化点を有することが必要である。
澱粉系生分解性樹脂よりも低い融点又は軟化点である
と、発泡セルの委縮を防止することができず好ましくな
い。澱粉系生分解性樹脂と生分解性ポリエステル樹脂の
融点又は軟化点の差を大きくし、成形温度が高くできる
ように、澱粉系生分解性樹脂がシリンダ中で変質しない
範囲で、できる限り生分解性ポリエステル樹脂の融点又
は軟化点を高くすることが望ましい。澱粉系生分解性樹
脂に生分解性ポリエステル樹脂をブレンドする方法は、
成形以前に押出し機でブレンドしてペレットとしても、
別々にペレット状に加工したものを成形時にブレンドし
て使用してもよいが、発泡剤に水を用いる場合には、生
分解性ポリエステル樹脂が加水分解されない条件でブレ
ンドする必要がある。 (C)発泡剤としては、重炭酸ナトリウム、炭酸アンモ
ニウム、アジド化合物等の無機系発泡剤や、アゾ化合
物、イソシアネート化合物、セミカルバジド化合物等の
有機系発泡剤等が挙げられ、これらは単独又は2 種以上
混合して使用することができる。これらの発泡剤は、上
述した樹脂の成形温度に合わせて使用することができる
が、廃棄後の汚染を考慮すれば、予め樹脂中に余分な水
分を加えておき、成形時の熱で蒸気化して発泡させる水
発泡を行うことが望ましい。
Examples of the biodegradable polyester resin (B) include polylactic acid, polybutylene succinate, polybutylene diglycolate, polyhydroxybutyrate-based copolymers, chemically synthesized polyesters such as ester-type polyurethane, and microbial polyesters. Examples thereof include resins, and these can be used alone or in combination of two or more. This biodegradable polyester resin needs to have a higher melting point or softening point than the starch-based biodegradable resin (A) described above.
If the melting point or softening point is lower than that of the starch-based biodegradable resin, the shrinkage of the foam cells cannot be prevented, which is not preferable. Biodegradable as much as possible within the range where the starch biodegradable resin does not deteriorate in the cylinder so that the difference in melting point or softening point between the starch biodegradable resin and the biodegradable polyester resin can be increased and the molding temperature can be increased. It is desirable to increase the melting point or softening point of the water-soluble polyester resin. The method of blending the starch-based biodegradable resin with the biodegradable polyester resin is
Even if blended with an extruder before molding into pellets,
Individually processed pellets may be blended at the time of molding and used. However, when water is used as the foaming agent, it is necessary to blend them under the condition that the biodegradable polyester resin is not hydrolyzed. Examples of the foaming agent (C) include inorganic foaming agents such as sodium bicarbonate, ammonium carbonate and azide compounds, and organic foaming agents such as azo compounds, isocyanate compounds and semicarbazide compounds. These may be used alone or in combination of two kinds. The above can be mixed and used. These foaming agents can be used according to the molding temperature of the above-mentioned resin, but in consideration of contamination after disposal, extra water is added to the resin in advance and vaporized by the heat during molding. It is desirable to perform water bubbling for foaming.

【0012】本発明に用いる生分解性樹脂組成物は、
(A)澱粉系生分解性樹脂、(B)生分解性ポリエステ
ル樹脂および(C)発泡剤をブレンドして製造すること
ができる。この生分解性樹脂組成物を生分解性ポリエス
テル樹脂の融点又は軟化点より若干高い温度で成形、発
泡させて生分解性樹脂発泡体を製造することができる。
本発明では、澱粉系生分解性樹脂に、それよりも高い融
点又は軟化点を有する生分解性ポリエステル樹脂をブレ
ンドして、生分解性ポリエステル樹脂の融点又は軟化点
より若干高い温度で発泡、成形を行うものである。こう
することによって、樹脂がノズルより出された際に、澱
粉系生分解性樹脂が発泡セル中の温度低下に伴う収縮か
ら生じる負圧で萎もうとするのに対し、生分解性ポリエ
ステル樹脂はその融点又は軟化点より若干高い温度であ
ることからすぐに固化し、一種の芯材的な役割を果た
し、発泡セルの萎みを防ぐ効果がある。このことによっ
て、従来、澱粉系生分解性樹脂の発泡成形では、成形温
度を低く保ち、萎みを防止しようとしているため、剪断
発熱の影響を受け易く、シリンダ温度が直ぐに上昇して
しまうという欠点があったのに対して、成形温度をもと
から上げられ、剪断発熱の影響が少なくなることから、
スクリューの回転数を落としたり、シリンダに特別に冷
却機能を付け加えることなしに、成形温度を一定に保つ
ことができるようになる。さらに、作られた生分解性ポ
リエステル樹脂の芯材は、フィラー的な役割も担うこと
から、目的に合った性質の生分解性ポリエステル樹脂を
使用することによって、発泡体の圧縮強度の向上や製品
脆さの改善も行うことができた。このような作用を有効
に活用するためには、澱粉系生分解性樹脂と生分解性ポ
リエステル樹脂の組合せにあたって、それらの融点又は
軟化点の差を大きくするとともに、成形温度を高くでき
るように、生分解性ポリエステル樹脂の融点又は軟化点
は、澱粉系生分解性樹脂がシリンダ中で変質しない範囲
でできるだけ高いものとすることが望ましい。
The biodegradable resin composition used in the present invention is
It can be produced by blending (A) starch-based biodegradable resin, (B) biodegradable polyester resin and (C) foaming agent. This biodegradable resin composition can be molded and foamed at a temperature slightly higher than the melting point or softening point of the biodegradable polyester resin to produce a biodegradable resin foam.
In the present invention, a starch-based biodegradable resin is blended with a biodegradable polyester resin having a higher melting point or softening point to foam and mold at a temperature slightly higher than the melting point or softening point of the biodegradable polyester resin. Is to do. By doing so, when the resin is discharged from the nozzle, the starch-based biodegradable resin tries to wither due to the negative pressure generated by the contraction due to the temperature decrease in the foam cell, whereas the biodegradable polyester resin does not Since the temperature is slightly higher than the melting point or softening point, it solidifies immediately, plays a role of a kind of core material, and has an effect of preventing the collapse of the foam cells. As a result, in the conventional foam molding of starch-based biodegradable resin, the molding temperature is kept low to prevent shrinkage, so that it is easily affected by heat generation by shearing, and the cylinder temperature rises immediately. On the other hand, since the molding temperature can be raised from the beginning and the influence of shear heat generation is reduced,
The molding temperature can be kept constant without lowering the screw rotation speed or adding a special cooling function to the cylinder. Furthermore, the core material of the biodegradable polyester resin produced also plays the role of a filler. Therefore, by using a biodegradable polyester resin having a property suitable for the purpose, it is possible to improve the compressive strength of the foam and the product. The brittleness could also be improved. In order to effectively utilize such an action, in combining a starch-based biodegradable resin and a biodegradable polyester resin, it is possible to increase the difference in melting point or softening point between them and increase the molding temperature, It is desirable that the melting point or softening point of the biodegradable polyester resin be as high as possible within the range where the starch-based biodegradable resin does not deteriorate in the cylinder.

【0013】[0013]

【発明の実施の形態】次に本発明を実施例によって具体
的に説明するが、本発明はこの実施例によって限定され
るものではない。以下の実施例および比較例において、
「部」とは「重量部」を意味する。
BEST MODE FOR CARRYING OUT THE INVENTION Next, the present invention will be specifically described by way of examples, but the present invention is not limited to these examples. In the following Examples and Comparative Examples,
"Parts" means "parts by weight".

【0014】実施例 固化澱粉にポリビニルアルコール系水溶性高分子をブレ
ンドしてなる澱粉系生分解性樹脂のNOVON−180
1(チッソ社製、商品名、軟化点110 ℃)100部に、発
泡剤として水18部を吸収させたものに、乳酸系生分解性
ポリエステル樹脂のラクティ(島津製作所社製、商品
名、融点170 ℃)30部を、ともにペレット状態でブレン
ドした生分解性樹脂組成物を、二軸押出機PCM30
(池貝社製、商品名)にてシリンダ温度を180 ℃,回転
数150 rpmに設定し、押出成形を行い、連続して生分
解性樹脂発泡体を製造した。この見掛け比重は0.05、発
泡倍率は25倍であった。
EXAMPLE NOVON-180, a starch-based biodegradable resin prepared by blending solidified starch with a polyvinyl alcohol-based water-soluble polymer.
1 (manufactured by Chisso Co., trade name, softening point 110 ° C.), with 18 parts water absorbed as a foaming agent, Lacty lactic acid-based biodegradable polyester resin (manufactured by Shimadzu Corporation, trade name, melting point) A biodegradable resin composition prepared by blending 30 parts of 170 ° C.) in a pellet state was used as a twin screw extruder PCM30.
Cylinder temperature was set to 180 ° C. and rotation speed was 150 rpm by (Ikegai Co., Ltd.), and extrusion molding was performed to continuously produce a biodegradable resin foam. The apparent specific gravity was 0.05 and the expansion ratio was 25 times.

【0015】比較例 固化澱粉にポリビニルアルコール系水溶性高分子をブレ
ンドしてなる澱粉系生分解性樹脂のNOVON−180
1(チッソ社製、商品名、軟化点110 ℃)130部に、発
泡剤として水18部を吸収させたものを、回転数150 rp
mに設定して押出成形をしたところ、初めは発泡体とな
っていたが、徐々にシリンダ温度が上昇し、130 ℃を超
えてから萎み現象がみられるようになり、安定した成形
ができなかった。そこで回転数75rpmに落として押出
成形したところ、シリンダ温度の上昇は緩やかになった
ものの、発泡状態が悪い生分解性樹脂発泡体が得られ
た。この見掛け比重は0.3 、発泡倍率は4 倍で包装材と
して満足できる緩衝能力はなかった。
Comparative Example NOVON-180, a starch-based biodegradable resin prepared by blending solidified starch with a polyvinyl alcohol-based water-soluble polymer.
1 (manufactured by Chisso Co., trade name, softening point 110 ° C) 130 parts absorbed 18 parts of water as a foaming agent, rotation speed 150 rp
When extrusion molding was performed with the m set to m, it initially became a foam, but the cylinder temperature gradually increased, and after the temperature exceeded 130 ° C, the shrinkage phenomenon began to appear, and stable molding was possible. There wasn't. Then, when the extrusion speed was reduced to 75 rpm, a biodegradable resin foam having a poor foaming state was obtained although the increase in the cylinder temperature was moderate. The apparent specific gravity was 0.3 and the expansion ratio was 4 times, and there was no satisfactory cushioning capacity as a packaging material.

【0016】[0016]

【発明の効果】以上説明したように、本発明の生分解性
樹脂発泡体の製造方法によれば、一般の成形機を用いて
発泡成形でき、成形直後の収縮のない、さらに製品とし
て高強度の生分解性樹脂発泡体を製造することができ
た。
As described above, according to the method for producing a biodegradable resin foam of the present invention, it can be foam-molded using a general molding machine, does not shrink immediately after molding, and has high strength as a product. It was possible to produce a biodegradable resin foam.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 (A)澱粉系生分解性樹脂、(B)生分
解性ポリエステル樹脂および(C)発泡剤を必須成分と
する生分解性樹脂組成物であって、前記(B)の生分解
性ポリエステル樹脂が前記(A)の澱粉系生分解性樹脂
より高い融点又は軟化点を有し、前記融点または軟化点
より若干高い温度で生分解性樹脂組成物を成形、発泡さ
せることを特徴とする生分解性樹脂発泡体の製造方法。
1. A biodegradable resin composition comprising (A) a starch-based biodegradable resin, (B) a biodegradable polyester resin, and (C) a foaming agent, which are essential components. The degradable polyester resin has a higher melting point or softening point than the starch-based biodegradable resin (A), and the biodegradable resin composition is molded and foamed at a temperature slightly higher than the melting point or softening point. And a method for producing a biodegradable resin foam.
JP8122697A 1996-04-19 1996-04-19 Production of biodegradable resin foam Pending JPH09286870A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8122697A JPH09286870A (en) 1996-04-19 1996-04-19 Production of biodegradable resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8122697A JPH09286870A (en) 1996-04-19 1996-04-19 Production of biodegradable resin foam

Publications (1)

Publication Number Publication Date
JPH09286870A true JPH09286870A (en) 1997-11-04

Family

ID=14842381

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8122697A Pending JPH09286870A (en) 1996-04-19 1996-04-19 Production of biodegradable resin foam

Country Status (1)

Country Link
JP (1) JPH09286870A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000009609A1 (en) * 1998-08-11 2000-02-24 Toshinobu Yoshihara Composition for molding biodegradable plastic, biodegradable plastic obtained therefrom, method of molding the same, and use of biodegradable plastic
WO2009078309A1 (en) * 2007-12-19 2009-06-25 Showa Highpolymer Co., Ltd. Foamable resin composition and foam
WO2015137057A1 (en) * 2014-03-11 2015-09-17 東洋製罐グループホールディングス株式会社 Resin molded article to be thrown in water

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000009609A1 (en) * 1998-08-11 2000-02-24 Toshinobu Yoshihara Composition for molding biodegradable plastic, biodegradable plastic obtained therefrom, method of molding the same, and use of biodegradable plastic
US6437022B1 (en) 1998-08-11 2002-08-20 Toshinobu Yoshihara Composition for molding biodegradable plastic, biodegradable plastic obtained therefrom, method of molding the same, and use of biodegradable plastic
WO2009078309A1 (en) * 2007-12-19 2009-06-25 Showa Highpolymer Co., Ltd. Foamable resin composition and foam
WO2015137057A1 (en) * 2014-03-11 2015-09-17 東洋製罐グループホールディングス株式会社 Resin molded article to be thrown in water
JP2015172107A (en) * 2014-03-11 2015-10-01 東洋製罐グループホールディングス株式会社 Resin molded article to be thrown in water

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