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JPH0952901A - Composition for biodegradable molding and production of biodegradable molding - Google Patents

Composition for biodegradable molding and production of biodegradable molding

Info

Publication number
JPH0952901A
JPH0952901A JP20348995A JP20348995A JPH0952901A JP H0952901 A JPH0952901 A JP H0952901A JP 20348995 A JP20348995 A JP 20348995A JP 20348995 A JP20348995 A JP 20348995A JP H0952901 A JPH0952901 A JP H0952901A
Authority
JP
Japan
Prior art keywords
starch
weight
parts
oxidizing agent
plasticizer
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
JP20348995A
Other languages
Japanese (ja)
Other versions
JP3078478B2 (en
Inventor
Tetsuya Shimooozono
哲哉 下大薗
Akira Muramatsu
明 村松
Jiro Hino
治郎 日野
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.)
Japan Maize Products Co Ltd
Nihon Shokuhin Kako Co Ltd
Original Assignee
Japan Maize Products Co Ltd
Nihon Shokuhin Kako 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 Japan Maize Products Co Ltd, Nihon Shokuhin Kako Co Ltd filed Critical Japan Maize Products Co Ltd
Priority to JP07203489A priority Critical patent/JP3078478B2/en
Publication of JPH0952901A publication Critical patent/JPH0952901A/en
Application granted granted Critical
Publication of JP3078478B2 publication Critical patent/JP3078478B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Biological Depolymerization Polymers (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain the subject composition containing a gelatinized material of starch which is subjected to oxidation treatment, capable of improving fluidity when heat melting, enabling injection molding and useful for disposable dishes, etc. SOLUTION: This composition comprises (A) only a gelatinized material of starch which is subjected to oxidation treatment or contains the component A and (B) a biodegradable resin. Furthermore, the component A is obtained by heating and mixing (i) starch with (ii) water and (iii) an oxidizing agent (preferably persulfuric acid salt selected from potassium persulfate, ammonium persulfate and sodium persulfate or hydrogen peroxide) or component (ii), (iv)a plasticizer and the component (ii) or the component (iv) and the component (iii), preferably so that 0.01-50 pts.wt. component (iii) or 10-50 pts.wt. component (ii) or 0.1-40pts wt. component (ii) and 1-100 pts.wt. component (iv) or 1-100 pts.wt. component (iv) based on 100 pts.wt. component (i) are used, respectively.

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、澱粉糊化物を含有
する生分解性生成品用組成物および生分解性生成品の製
造方法に関する。さらに詳しくは澱粉に酸化剤を配合す
ることにより澱粉糊化時に低粘度化させ、成形時の流動
性が改善させれた生分解性成形品用の組成物、および成
形時の流動性を改善して良好な形成加工性を有する生分
解性成形品の製造方法に関する。
TECHNICAL FIELD The present invention relates to a composition for a biodegradable product containing a starch gelatinization product and a method for producing the biodegradable product. More specifically, by adding an oxidizing agent to starch, the viscosity of the starch is reduced during gelatinization, the composition for biodegradable molded articles having improved fluidity during molding, and the fluidity during molding are improved. The present invention relates to a method for producing a biodegradable molded article having excellent forming processability.

【0002】[0002]

【従来の技術】澱粉糊化物を生分解性成分として利用す
ることが提案されている。例えば、特開平1−2170
02号(先行技術1という)には、澱粉糊化物を主成分
とする生分解性組成物が開示されている。また、例え
ば、特開平2−14228号(先行技術2という)に
は、澱粉糊化物と生分解性樹脂の複合体である生分解性
組成物が開示されている。
It has been proposed to utilize a gelatinized starch as a biodegradable component. For example, JP-A 1-2170
No. 02 (referred to as Prior Art 1) discloses a biodegradable composition containing a starch gelatinized material as a main component. Further, for example, Japanese Patent Application Laid-Open No. 2-14228 (referred to as Prior Art 2) discloses a biodegradable composition which is a complex of a starch gelatinization product and a biodegradable resin.

【0003】また、澱粉として種々の加工澱粉を用いた
生分解性樹脂組成物も知られている。例えば、特開平3
−56543号(先行技術3という)には澱粉グラフト
コポリマーを含む生分解性組成物が開示されている。特
開平3−70752号(先行技術4という)には、アニ
オン性修飾澱粉を含む生分解性組成物が開示されてい
る。特開平3−74445号(先行技術5という)には
カチオン性修飾澱粉を含む生分解性組成物が開示されて
いる。特開平3−74446号(先行技術6という)に
は、ヒドロキシアルキル基、アルキルエーテル基及びエ
ステル基の少なくとも1つを含む様に化学的に改質され
た澱粉を澱粉成分として含む生分解性組成物が開示され
ている。
Biodegradable resin compositions using various modified starches as starch are also known. For example, JP-A-3
-56543 (referred to as Prior Art 3) discloses a biodegradable composition containing a starch graft copolymer. JP-A-3-70752 (referred to as Prior Art 4) discloses a biodegradable composition containing an anionically modified starch. Japanese Patent Application Laid-Open No. 3-74445 (referred to as Prior Art 5) discloses a biodegradable composition containing a cationic modified starch. Japanese Patent Application Laid-Open No. 3-74446 (referred to as Prior Art 6) discloses a biodegradable composition containing as a starch component a starch chemically modified to contain at least one of a hydroxyalkyl group, an alkyl ether group and an ester group. The thing is disclosed.

【0004】[0004]

【発明が解決しようとする課題】生分解性組成物におい
て、重要な物性は生分解性、強度、伸び等である。しか
し、これらの物性に加えて、成形品に加工する場合の加
熱溶融時の流動性が良好であることも実用上重要であ
る。生分解性組成物を実用するに当たり、従来から成形
品に加工されている合成樹脂、例えば、ポリスチレン等
と同程度の流動性を有することが好ましい。ところが、
これまでは、澱粉系生分解性組成物の開発に当たり、流
動性についてあまり注目されていなかった。
In the biodegradable composition, important physical properties are biodegradability, strength, elongation and the like. However, in addition to these physical properties, it is also practically important that the fluidity at the time of heating and melting in processing into a molded product is good. In putting the biodegradable composition into practical use, it is preferable that it has fluidity comparable to that of synthetic resins conventionally processed into molded articles, such as polystyrene. However,
Until now, much attention has been paid to fluidity in the development of starch-based biodegradable compositions.

【0005】先行技術1および2に開示された澱粉糊化
物、さらには、先行技術3〜6に記載された加工澱粉に
おいては、加熱溶融時の流動性が不十分であった。その
ため、押し出し成形により、簡単な形状の成形物、例え
ば、シート等を得ることはある程度可能であったが、射
出成形により複雑な形状の物品を成形しようとする場
合、流動性不良により、所望の形状の成形物を得ること
は困難であった。
In the starch gelatinization products disclosed in the prior arts 1 and 2, and further in the processed starches described in the prior arts 3 to 6, the fluidity during heating and melting was insufficient. Therefore, it was possible to obtain a molded article having a simple shape, for example, a sheet, by extrusion molding to some extent, but when attempting to mold an article having a complicated shape by injection molding, a desired fluidity was not obtained due to poor fluidity. It was difficult to obtain a shaped molded product.

【0006】そこで本発明の第1の目的は、澱粉糊化物
を用いる生分解性組成物であって、加熱溶融時の流動性
が改善され、成形が容易である生分解性成形品用の組成
物を提供することにある。さらに本発明の第2の目的
は、加熱溶融時の流動性が改善され、成形加工を容易に
行える澱粉糊化物を含む生分解性成形品の製造方法を提
供することにある。
Therefore, a first object of the present invention is a biodegradable composition using a starch gelatinization product, which has improved fluidity when heated and melted and is easy to mold, and is therefore a composition for biodegradable molded articles. To provide things. A second object of the present invention is to provide a method for producing a biodegradable molded product containing a starch gelatinized product, which has improved fluidity during heating and melting and can be easily molded.

【0007】[0007]

【課題を解決するための手段】本発明は、酸化処理した
澱粉糊化物を含有することを特徴とする生分解性成形品
用組成物に関する。本発明の生分解性成形品用組成物
は、酸化処理した澱粉糊化物からなる態様および酸化処
理した澱粉糊化物と生分解性樹脂とを含む態様を含むも
のである。
The present invention relates to a composition for biodegradable molded articles, which comprises an oxidized starch gelatinized product. The biodegradable composition for molded articles of the present invention includes an embodiment comprising an oxidized starch gelatinization product and an embodiment including an oxidation-treated starch gelatinization product and a biodegradable resin.

【0008】さらに本発明は、澱粉を水および酸化剤、
又は水、可塑剤および酸化剤、又は可塑剤および酸化剤
と加熱混合し、得られた混合物を所望の形状に成形する
ことを特徴とする生分解性成形品の製造方法に関する。
さらに本発明は、澱粉を水、酸化剤および生分解性樹
脂、又は水、可塑剤、酸化剤および生分解性樹脂、又は
可塑剤、酸化剤および生分解性樹脂と加熱混合し、得ら
れた混合物を所望の形状に成形することを特徴とする生
分解性成形品の製造方法に関する。
The present invention further provides that starch is added to water and an oxidizing agent,
Alternatively, the present invention relates to a method for producing a biodegradable molded article, which comprises heating and mixing with water, a plasticizer and an oxidizing agent, or a plasticizer and an oxidizing agent, and molding the obtained mixture into a desired shape.
Further, the present invention was obtained by heating and mixing starch with water, an oxidizing agent and a biodegradable resin, or water, a plasticizer, an oxidizing agent and a biodegradable resin, or a plasticizer, an oxidizing agent and a biodegradable resin. The present invention relates to a method for producing a biodegradable molded article, which comprises molding the mixture into a desired shape.

【0009】生分解性成形品用組成物 本発明の生分解性成形品用組成物は酸化処理した澱粉糊
化物を含有するものである。酸化処理した澱粉糊化物
は、澱粉の酸化処理と糊化とを並行して行うことにより
得ることができる。上記酸化処理と糊化の原料として用
いる澱粉は、特に制限なくいずれの澱粉も用いることが
できる。例えば、馬鈴薯澱粉、コーンスターチ、甘薯澱
粉、タピオカ澱粉、サゴヤシ澱粉、米澱粉、小麦澱粉な
どの未加工澱粉、さらには、各種エステル化澱粉、エー
テル化澱粉等の加工澱粉等を挙げることができる。
Biodegradable Molded Article Composition The biodegradable molded article composition of the present invention contains an oxidized starch gelatinization product. The gelatinized starch subjected to the oxidation treatment can be obtained by performing the oxidation treatment and the gelatinization of the starch in parallel. The starch used as a raw material for the above-mentioned oxidation treatment and gelatinization is not particularly limited, and any starch can be used. Examples thereof include unprocessed starch such as potato starch, corn starch, sweet potato starch, tapioca starch, sago palm starch, rice starch, wheat starch, and modified starch such as various esterified starches and etherified starches.

【0010】澱粉の酸化処理と糊化とは、例えば、澱粉
を水および酸化剤、又は水、可塑剤および酸化剤と加熱
混合することにより行うことができる。酸化剤を共存さ
せることで酸化処理を澱粉糊化と同時に行うことがで
き、得られる組成物の加熱溶融時の流動性を改善するこ
とができる。上記酸化剤としては、例えば、過酸化物を
用いることができる。過酸化物としては、例えば、過硫
酸カリウム、過硫酸アンモニウム、過硫酸ナトリウムか
らなる群から選ばれる過硫酸塩又は過酸化水素を用いる
ことができる。酸化剤の使用量は、澱粉(乾物基準)1
00重量部当たり0.01〜0.50重量部の範囲とす
ることが適当である。好ましくは、0.02〜0.10
重量部の範囲である。尚、酸化剤の種類および量は、得
られる組成物の流動性を考慮して適宜変化させることが
できる。
The oxidation treatment and gelatinization of starch can be carried out, for example, by heating and mixing the starch with water and an oxidizing agent, or water, a plasticizer and an oxidizing agent. By allowing an oxidizing agent to coexist, the oxidizing treatment can be performed simultaneously with gelatinization of starch, and the fluidity of the resulting composition at the time of heating and melting can be improved. As the oxidizing agent, for example, a peroxide can be used. As the peroxide, for example, a persulfate salt selected from the group consisting of potassium persulfate, ammonium persulfate, and sodium persulfate, or hydrogen peroxide can be used. The amount of oxidizing agent used is starch (dry matter basis) 1
It is suitable to set it in the range of 0.01 to 0.50 parts by weight per 00 parts by weight. Preferably 0.02-0.10
The range is parts by weight. The type and amount of the oxidizing agent can be appropriately changed in consideration of the fluidity of the obtained composition.

【0011】上記のように、澱粉を、酸化剤に加えて、
水、可塑剤、又は水および可塑剤の共存下で加熱混合す
ることにより澱粉糊化物が得られる。澱粉の糊化は水単
独又は可塑剤単独の存在下で行うことが出来る。また、
水と可塑剤との存在下でも澱粉を糊化することができ、
この場合水の使用量も低減でき、成形時の発泡防止に有
効である。さらに、糊化物に可塑剤を含有させることに
より澱粉糊化物と生分解性樹脂との混合及び成形を容易
に出来ると言う利点もある。
As mentioned above, starch is added to the oxidant,
A starch gelatinized product is obtained by heating and mixing in the presence of water, a plasticizer, or water and a plasticizer. The gelatinization of starch can be carried out in the presence of water alone or a plasticizer alone. Also,
Starch can be gelatinized even in the presence of water and plasticizer,
In this case, the amount of water used can be reduced, which is effective in preventing foaming during molding. Furthermore, there is an advantage that the starch gelatinized product and the biodegradable resin can be easily mixed and molded by adding a plasticizer to the gelatinized product.

【0012】糊化に用いられる可塑剤は澱粉を糊化出
来、かつ糊化物に可塑性を付与できるものであれば特に
制限はなく、例えば生分解性を有する高沸点可塑剤を挙
げることが出来る。そのような可塑剤の例としては、エ
チレングリコール、プロピレングリコール、グリセリ
ン、ソルビトール、ポリエチレングリコール、ポリプロ
ピレングリコール等を挙げることができる。
The plasticizer used for gelatinization is not particularly limited as long as it can gelatinize starch and can impart plasticity to the gelatinized product, and examples thereof include biodegradable high boiling point plasticizers. Examples of such plasticizers include ethylene glycol, propylene glycol, glycerin, sorbitol, polyethylene glycol, polypropylene glycol and the like.

【0013】糊化に水を用いる場合には、澱粉(乾物基
準)100重量部当たり10〜50重量部の水を用いる
ことが、澱粉を充分に糊化させるという観点から適当で
ある。さらに好ましくは澱粉(乾物基準)100重量部
当たり10〜20重量部の水を用いることが、澱粉を充
分糊化させるとともに生分解性組成物に添加して成形す
る際の発泡を防止できる観点から適当である。
When water is used for gelatinization, it is appropriate to use 10 to 50 parts by weight of water per 100 parts by weight of starch (dry matter basis) from the viewpoint of sufficiently gelatinizing the starch. It is more preferable to use 10 to 20 parts by weight of water per 100 parts by weight of starch (on a dry matter basis) from the viewpoint of sufficiently gelatinizing the starch and preventing foaming when the starch is added to the biodegradable composition and molded. Appropriate.

【0014】また、糊化に水と可塑剤を用いる場合に
は、澱粉(乾物基準)100重量部当たり0.1〜40
重量部の水及び1〜100重量部の可塑剤を用いること
が、澱粉を充分に糊化させ、かつ糊化物に充分な可塑性
を付与できるという観点から適当である。さらに、好ま
しくは、澱粉(乾物基準)100重量部当たり0.1〜
20重量部の水及び5〜40重量部の可塑剤を用いるこ
とが、澱粉を充分に糊化させるとともに、生分解性組成
物に添加して成形する際の発泡を防止でき、かつ糊化物
に適度な可塑性を付与できるという観点から適当であ
る。
When water and a plasticizer are used for gelatinization, 0.1 to 40 per 100 parts by weight of starch (dry matter basis) is used.
The use of parts by weight of water and 1 to 100 parts by weight of a plasticizer is suitable from the viewpoint that the starch can be sufficiently gelatinized and the gelatinized product can have sufficient plasticity. Further, it is preferably 0.1 to 100 parts by weight of starch (dry matter basis).
The use of 20 parts by weight of water and 5 to 40 parts by weight of a plasticizer can sufficiently gelatinize the starch, prevent foaming when added to the biodegradable composition and mold it, and form a gelatinized product. It is suitable from the viewpoint that appropriate plasticity can be imparted.

【0015】また、糊化に可塑剤のみを用いる場合に
は、澱粉(乾物基準)100重量部当たり1〜100重
量部の可塑剤を用いることが、澱粉を充分に糊化させ、
かつ糊化物に充分な可塑性を付与できるという観点から
適当である。さらに、好ましくは、澱粉(乾物基準)1
00重量部当たり5〜40重量部の可塑剤を用いること
が、澱粉を充分に糊化させるとともに、糊化物に適度な
可塑性を付与できるという観点から適当である。
When only the plasticizer is used for gelatinization, 1 to 100 parts by weight of the plasticizer is used per 100 parts by weight of the starch (on a dry matter basis) so that the starch is sufficiently gelatinized.
It is also suitable from the viewpoint that it can impart sufficient plasticity to the gelatinized product. Further, preferably, starch (dry matter basis) 1
It is suitable to use 5 to 40 parts by weight of the plasticizer per 00 parts by weight from the viewpoint of sufficiently gelatinizing the starch and imparting appropriate plasticity to the gelatinized product.

【0016】澱粉の糊化とは、一般に水等の存在下で加
熱すると澱粉粒が不可逆的に膨潤又は溶解し、結晶性及
び複屈折性を失い、粘度が上昇した状態をいう。本発明
における澱粉糊化物は結晶性及び複屈折性を実質的に示
さないものをいう。尚、結晶性及び複屈折性の喪失は澱
粉粒を偏光顕微鏡で観察し、未糊化澱粉では見られた形
成中心で交差した偏光十字が見られなくなることで判定
することができる。
The gelatinization of starch generally refers to a state in which starch particles irreversibly swell or dissolve when heated in the presence of water or the like, lose crystallinity and birefringence, and increase in viscosity. The starch gelatinization product in the present invention refers to a substance which exhibits substantially no crystallinity or birefringence. The loss of crystallinity and birefringence can be determined by observing the starch granules with a polarization microscope and eliminating the crossed polarization cross at the forming center, which was observed in the ungelatinized starch.

【0017】澱粉の酸化処理および糊化のための加熱混
合は、澱粉の種類や、可塑剤を用いる場合には可塑剤の
種類、さらには水や可塑剤の添加量により適宜決定でき
る。例えば、60〜220℃で10〜60分間行うこと
が適当である。加熱混合は、例えば、加圧ニーダーや押
出し機を用いて行うことができる。加熱混合により、酸
化処理した澱粉糊化物からなる、本発明の生分解性成形
品用組成物を得ることができる。得られる組成物は、例
えばペレット化しておき、生分解性成形品の製造の際に
このペレットを使用することができる。
The heating and mixing for the oxidation treatment and gelatinization of starch can be appropriately determined depending on the type of starch, the type of plasticizer when a plasticizer is used, and the addition amount of water or plasticizer. For example, it is suitable to carry out at 60 to 220 ° C. for 10 to 60 minutes. The heat mixing can be performed using, for example, a pressure kneader or an extruder. By heat-mixing, the composition for biodegradable molded articles of the present invention, which comprises an oxidized starch gelatinized product, can be obtained. The obtained composition can be pelletized, for example, and the pellets can be used in the production of a biodegradable molded article.

【0018】また、酸化処理した澱粉糊化物と生分解性
樹脂とを含む本発明の生分解性成形品用組成物は、例え
ば、ペレット状の上記酸化処理した澱粉糊化物と生分解
性樹脂と混合することにより得ることが出来る。本発明
において用いられる生分解性樹脂には特に制限はない。
それ自身生分解性を有する樹脂であれば良く、成形性を
考慮すると熱可塑性であることが適当である。化学合成
系樹脂、微生物系樹脂、天然物利用系樹脂等のいずれに
属する樹脂でも良い。例えば、脂肪族ポリエステル(例
えば、ポリカプロラクトン、ポリ乳酸、ポリヒドロキシ
ブチレート・バリレート共重合体など)、ポリビニルア
ルコール、アセチルセルロース等を挙げることができ
る。
The composition for biodegradable molded articles of the present invention containing an oxidized starch gelatinized product and a biodegradable resin is, for example, a pellet-shaped above-mentioned oxidized starch gelatinized product and a biodegradable resin. It can be obtained by mixing. The biodegradable resin used in the present invention is not particularly limited.
Any resin that has biodegradability itself may be used, and thermoplastic resin is suitable in consideration of moldability. Resins belonging to any of chemically synthesized resins, microbial resins, resins utilizing natural products, etc. may be used. For example, aliphatic polyester (for example, polycaprolactone, polylactic acid, polyhydroxybutyrate / vallate copolymer, etc.), polyvinyl alcohol, acetyl cellulose and the like can be mentioned.

【0019】本発明の生分解性成形品用組成物には、上
記成分に加えて必要により添加剤を適宜加えることもで
きる。添加剤としては、例えば、植物性タンパク質、パ
ルプ、紫外線安定剤、殺菌剤、除草剤、肥料、酸化防止
剤、界面活性剤、顔料等を挙げることが出来る。
The composition for biodegradable molded articles of the present invention may optionally contain additives in addition to the above components. Examples of the additive include vegetable protein, pulp, ultraviolet stabilizer, bactericide, herbicide, fertilizer, antioxidant, surfactant, pigment and the like.

【0020】生分解性成形品の製造方法 本発明の生分解性成形品の製造方法は、生分解性成形品
が酸化処理した澱粉糊化物のみからなる場合は、上記生
分解性成形品用組成物の場合と同様に、澱粉を水および
酸化剤、又は水、可塑剤および酸化剤、又は可塑剤およ
び酸化剤と加熱混合した後、得られる混合物を所望の形
状に成形することにより行うことができる。成形品への
成形は、例えば、射出成形や押出成形等を用いて行うこ
とができる。また、酸化処理した澱粉糊化物と生分解性
樹脂を含む生分解性成形品の製造は、澱粉を水、酸化剤
および生分解性樹脂、又は水、可塑剤、酸化剤および生
分解性樹脂、又は可塑剤、酸化剤および生分解性樹脂と
加熱混合し、得られた混合物を所望の形状に成形するこ
とにより行うことができる。成形品への成形は、上記と
同様に、例えば、射出成形や押出成形等を用いて行うこ
とができる。
Method for Producing Biodegradable Molded Article In the method for producing a biodegradable molded article of the present invention, when the biodegradable molded article is composed only of an oxidized starch gelatinized product, the above composition for biodegradable molded article is used. As in the case of the product, it can be carried out by heating and mixing the starch with water and an oxidizing agent, or water, a plasticizer and an oxidizing agent, or a plasticizer and an oxidizing agent, and then shaping the resulting mixture into a desired shape. it can. Molding into a molded product can be performed by using, for example, injection molding or extrusion molding. In addition, the production of a biodegradable molded article containing an oxidized starch gelatinization product and a biodegradable resin, starch is water, an oxidizing agent and a biodegradable resin, or water, a plasticizer, an oxidizing agent and a biodegradable resin, Alternatively, it can be carried out by heating and mixing with a plasticizer, an oxidizing agent and a biodegradable resin, and molding the resulting mixture into a desired shape. Molding into a molded article can be performed by using, for example, injection molding, extrusion molding, or the like, as in the above.

【0021】いずれの場合も、澱粉、酸化剤、可塑剤、
生分解性樹脂としては、生分解性成形品用組成物の場合
と同様のものを用いることができる。また、澱粉に対す
る酸化剤、可塑剤および水の使用量についても、生分解
性成形品用組成物の場合と同様にすることができる。成
形品の形状には特に制限はなく、生分解性を利用できる
いずれの用途の成形品、例えば、洗剤等の容器、使い捨
て食器等を挙げることができる。
In any case, starch, oxidizer, plasticizer,
As the biodegradable resin, the same one as in the case of the composition for biodegradable molded articles can be used. The amounts of oxidizing agent, plasticizer and water used for starch can be the same as in the case of the composition for biodegradable molded articles. The shape of the molded article is not particularly limited, and examples thereof include molded articles for any purpose in which biodegradability can be utilized, such as containers for detergents, disposable tableware, and the like.

【0022】[0022]

【発明の効果】本発明によれば、澱粉糊化物を用いる生
分解性組成物であって、加熱溶融時の流動性が改善さ
れ、成形が容易である生分解性成形品用の組成物を提供
することができる。特に、本発明の生分解性成形品用組
成物は射出成形によっても成形することができる。さら
に本発明によれば、加熱溶融時の流動性が改善され、成
形加工を容易に行える澱粉糊化物を含む生分解性成形品
の製造方法を提供することができる。本発明の製造方法
では、射出成形によっても成形することができる。
According to the present invention, there is provided a composition for a biodegradable molded article, which is a biodegradable composition using a starch gelatinization product, which has improved fluidity during heating and melting and is easy to mold. Can be provided. In particular, the composition for biodegradable molded articles of the present invention can also be molded by injection molding. Further, according to the present invention, it is possible to provide a method for producing a biodegradable molded article containing a starch gelatinized product, which has improved fluidity during heating and melting and can be easily molded. In the manufacturing method of the present invention, injection molding can also be used.

【0023】本発明による流動性の改善は、少量の酸化
剤を用い、糊化と並行して行える(追加の工程が不要で
ある)ことから、安いコストで行うことができる。澱粉
や澱粉糊化物に比べて高価である生分解性樹脂に複合化
させる場合、流動性が改善されることから、澱粉糊化物
(酸化処理した)の配合率を増加させることができ、そ
の結果、生分解性樹脂成形品の価格を低減することがで
きる。本発明の酸化処理した澱粉糊化物は流動性が改善
され、その結果、種々の複合組成物に対して高率で配合
することができる。その結果、複合組成物の生分解性を
促進でき(澱粉糊化物の有する生分解性は生分解性樹脂
より高いから)、生分解性複合組成物の応用範囲を汎用
樹脂並みに拡大させることが可能となる。
The improvement of fluidity according to the present invention can be carried out at a low cost because it can be carried out in parallel with gelatinization by using a small amount of an oxidizing agent (no additional step is required). When compounded with a biodegradable resin, which is more expensive than starch and starch gelatinized products, the fluidity is improved, so the blending ratio of starch gelatinized products (oxidized) can be increased. The cost of the biodegradable resin molded product can be reduced. The oxidised starch gelatinization product of the present invention has improved fluidity and, as a result, can be incorporated at a high rate in various composite compositions. As a result, the biodegradability of the composite composition can be accelerated (because the starch gelatinized product has a higher biodegradability than the biodegradable resin), and the application range of the biodegradable composite composition can be expanded to the level of general-purpose resins. It will be possible.

【0024】[0024]

【実施例】以下本発明を実施例によりさらに説明する。 実施例1〜3 コーンスターチ(乾物基準)100重量部当、水15重
量部、グリセリン20重量部に、過硫酸アンモニウム
0.02重量部、0.06重量部、または0.10重量
部を加えた。これら混合物を堅型ミキサー(関東混合機
工業製関東ミキサー)にて低速、中速、高速にて各1分
間ずつ混合した。上記混合物を一軸押し出し機(プラス
トグラフ)を用いて下記条件にて直径約4mmの棒状に
押し出し加工した。その後ハサミで長さ約0.5〜1c
mのペレット状にカットした。
EXAMPLES The present invention will be further described below with reference to examples. Examples 1 to 3 To 100 parts by weight of corn starch (dry matter basis), 15 parts by weight of water, and 20 parts by weight of glycerin, 0.02 part by weight, 0.06 part by weight, or 0.10 part by weight of ammonium persulfate was added. These mixtures were mixed for 1 minute at low speed, medium speed, and high speed with a tight mixer (Kanto mixer manufactured by Kanto mixer Co., Ltd.). The above mixture was extruded into a rod having a diameter of about 4 mm under the following conditions using a uniaxial extruder (Plastograph). After that, with scissors, the length is about 0.5-1c
m into pellets.

【0025】 スクリュー L/D25(一軸) 回転数 60r.p.m ダイ 6φ 温度 ZONE1:ZONE2:ZONE3=50℃:13
0℃:50℃
Screw L / D25 (uniaxial) Rotational speed 60r.pm Die 6φ Temperature ZONE1: ZONE2: ZONE3 = 50 ° C.:13
0 ℃: 50 ℃

【0026】比較例1 過硫酸カリウムを添加しなかった以外は、実施例1と同
様にしてペレット状組成物を得た。 比較例2 市販のポリスチレンレット(旭化成(株)製スタイロン
600)を用いた。
Comparative Example 1 A pelletized composition was obtained in the same manner as in Example 1 except that potassium persulfate was not added. Comparative Example 2 A commercially available polystyrene let (Styron 600 manufactured by Asahi Kasei Corporation) was used.

【0027】[0027]

【表1】 [Table 1]

【0028】実施例1〜3および比較例1〜2で調製し
たペレットの熱流動性をフローテスター(島津製作所製
CFT500C)を用いて昇温法により調べた。測定方
法としては、長さ2cm、直径1mmのダイを用い、荷
重を50kgfにし、5℃/minの昇温速度にて50
℃〜200℃の範囲で測定した。各温度における溶融粘
度の結果を図1に、フローレート(剪断速度)の結果を
図2に示す。即ち、ごく少量の酸化剤を添加した実施例
1〜3は、酸化剤を添加していない比較例1に比べて溶
融粘度が低下して、流動性が改善され、それらは比較例
2のごとき汎用ポリスチレンと同等であることが認めら
れた。
The heat fluidity of the pellets prepared in Examples 1 to 3 and Comparative Examples 1 and 2 was examined by a temperature rising method using a flow tester (CFT500C manufactured by Shimadzu Corporation). As a measuring method, a die having a length of 2 cm and a diameter of 1 mm was used, the load was 50 kgf, and the temperature was 50 ° C./min.
It measured in the range of ℃ -200 ℃. The result of melt viscosity at each temperature is shown in FIG. 1, and the result of flow rate (shear rate) is shown in FIG. That is, in Examples 1 to 3 to which a very small amount of the oxidizing agent was added, the melt viscosity was lowered and the fluidity was improved as compared with Comparative Example 1 to which the oxidizing agent was not added. It was found to be equivalent to general-purpose polystyrene.

【0029】実施例4 コーンスターチ(乾物基準)100重量部当、水20重
量部、ポリエチレングリコール15重量部、過硫酸カリ
ウム0.04重量部をヘンシェルミキサー(三井三池化
工機製)にとり、600r.p.m 5分間攪拌し混合した。
これを下記押出機、条件にてペレット化した。 押出機名 東洋精機(株)製ラボプラストミル 型式 2軸押出機2D25S スクリュー L/D=25(2軸) 温度 ZONE 1:ZONE 2:ZONE 3:ZONE 4 =50℃:60
℃: 120℃: 100℃ ダイ 3φ ペレッタイザー 東洋精機(株)製コールドカットペレ
ッタイザーPETEC 型
Example 4 100 parts by weight of corn starch (on a dry matter basis), 20 parts by weight of water, 15 parts by weight of polyethylene glycol and 0.04 part by weight of potassium persulfate were placed in a Henschel mixer (Mitsui Miike Kakoki Co., Ltd.) at 600 rpm. The mixture was stirred for 1 minute and mixed.
This was pelletized under the following extruder and conditions. Extruder name Labo Plastomill model manufactured by Toyo Seiki Co., Ltd. 2 screw extruder 2D25S screw L / D = 25 (2 screw) Temperature ZONE 1: ZONE 2: ZONE 3: ZONE 4 = 50 ° C: 60
℃: 120 ℃: 100 ℃ Die 3φ pelletizer Toyo Seiki Co., Ltd. cold cut pelletizer PETEC type

【0030】上記条件で得た澱粉ペレットを日精樹脂工
学(株)製射出成形機、植木鉢成形金型を用いて下記条
件にて射出成形し、成形品を得た。 加熱筒設定温度 ノズル 150℃ 前部 155℃ 中間部
145℃ 後部 120℃ 金型表面温度 20℃ 射出時間 3秒
The starch pellets obtained under the above conditions were injection-molded under the following conditions using an injection molding machine and a flowerpot molding die manufactured by Nissei Plastic Engineering Co., Ltd. to obtain molded products. Heating cylinder set temperature Nozzle 150 ℃ Front 155 ℃ Middle
145 ℃ Rear 120 ℃ Mold surface temperature 20 ℃ Injection time 3 seconds

【0031】比較例3 過硫酸カリウム添加を添加しなかった以外は実施例4と
同様にしてペレットおよび成形品を得た。
Comparative Example 3 Pellets and molded articles were obtained in the same manner as in Example 4 except that potassium persulfate was not added.

【0032】[0032]

【表2】 [Table 2]

【0033】実施例5 実施例4で得たペレット50重量部と、ダイセル化学工
業株式会社製ポリカプロラクトン(プラクセルH7)5
0重量部とを混合し、日精樹脂工学(株)製射出成形
機、植木鉢成形金型を用いて下記条件にて射出成形試験
を行い成形品を得た。 加熱筒設定温度 ノズル 150℃、前部 155℃、中間部
145℃、後部 120℃ 金型表面温度 20℃ 射出時間 3秒
Example 5 50 parts by weight of the pellet obtained in Example 4 and polycaprolactone (Placcel H7) 5 manufactured by Daicel Chemical Industries, Ltd.
0 parts by weight was mixed, and an injection molding test was performed under the following conditions using an injection molding machine and a flowerpot molding die manufactured by Nissei Plastic Engineering Co., Ltd. to obtain a molded product. Heating cylinder set temperature Nozzle 150 ℃, front 155 ℃, middle part
145 ℃, rear 120 ℃ Mold surface temperature 20 ℃ Injection time 3 seconds

【0034】比較例4 過硫酸カリウム添加を添加しなかった以外は実施例5と
同様にして成形品を得た。
Comparative Example 4 A molded product was obtained in the same manner as in Example 5 except that potassium persulfate was not added.

【0035】[0035]

【表3】 [Table 3]

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

【図1】 実施例1〜3および比較例1および2の各組
成物の各温度における溶融粘度を示す。
1 shows the melt viscosity of each composition of Examples 1 to 3 and Comparative Examples 1 and 2 at each temperature.

【図2】 実施例1〜3および比較例1および2の各組
成物の各温度におけるフローレート(剪断速度)を示
す。
FIG. 2 shows the flow rate (shear rate) of each composition of Examples 1 to 3 and Comparative Examples 1 and 2 at each temperature.

Claims (14)

【特許請求の範囲】[Claims] 【請求項1】 酸化処理した澱粉糊化物を含有すること
を特徴とする生分解性成形品用組成物。
1. A composition for a biodegradable molded article, which comprises an oxidized starch gelatinized product.
【請求項2】 酸化処理した澱粉糊化物のみからなる
か、または酸化処理した澱粉糊化物と生分解性樹脂とを
含む請求項1記載の組成物。
2. The composition according to claim 1, which consists only of an oxidized starch gelatinization product or comprises an oxidized starch gelatinization product and a biodegradable resin.
【請求項3】 酸化処理した澱粉糊化物が、澱粉の酸化
処理と糊化とを並行して行って得たものである請求項1
または2記載の組成物。
3. The starch gelatinization product subjected to oxidation treatment is obtained by subjecting starch to oxidation treatment and gelatinization in parallel.
Or the composition according to 2.
【請求項4】 澱粉の酸化処理と糊化を、澱粉を水およ
び酸化剤、又は水、可塑剤および酸化剤、又は可塑剤お
よび酸化剤と加熱混合することにより行う請求項5記載
の組成物。
4. The composition according to claim 5, wherein the starch is oxidized and gelatinized by heating and mixing the starch with water and an oxidizing agent, or water, a plasticizer and an oxidizing agent, or a plasticizer and an oxidizing agent. .
【請求項5】 酸化剤が過酸化物である請求項4記載の
組成物。
5. The composition according to claim 4, wherein the oxidizing agent is a peroxide.
【請求項6】 過酸化物が過硫酸カリウム、過硫酸アン
モニウム、過硫酸ナトリウムからなる群から選ばれる過
硫酸塩又は過酸化水素である請求項5記載の組成物。
6. The composition according to claim 5, wherein the peroxide is a persulfate selected from the group consisting of potassium persulfate, ammonium persulfate and sodium persulfate, or hydrogen peroxide.
【請求項7】 澱粉(乾物基準)100重量部当たり
0.01〜0.50重量部の酸化剤を用いる請求項4〜
6のいずれか1項に記載の組成物。
7. An oxidizing agent is used in an amount of 0.01 to 0.50 parts by weight per 100 parts by weight of starch (dry matter basis).
7. The composition according to any one of the above items 6.
【請求項8】 澱粉(乾物基準)100重量部当たり1
0〜50重量部の水、又は澱粉(乾物基準)100重量
部当たり0.1〜40重量部の水及び1〜100重量部
の可塑剤、又と澱粉(乾物基準)100重量部当たり1
〜100重量部の可塑剤を用いる請求項4〜7のいずれ
か1項に記載の組成物。
8. 1 per 100 parts by weight of starch (dry matter basis)
0 to 50 parts by weight of water, or 0.1 to 40 parts by weight of water and 1 to 100 parts by weight of plasticizer per 100 parts by weight of starch (dry matter), and 1 per 100 parts by weight of starch (dry matter).
The composition according to any one of claims 4 to 7, which uses -100 parts by weight of a plasticizer.
【請求項9】 澱粉を水および酸化剤、又は水、可塑剤
および酸化剤、又は可塑剤および酸化剤と加熱混合し、
得られた混合物を所望の形状に成形することを特徴とす
る生分解性成形品の製造方法。
9. Starch is heated and mixed with water and an oxidizing agent, or water, a plasticizer and an oxidizing agent, or a plasticizer and an oxidizing agent,
A method for producing a biodegradable molded article, which comprises molding the obtained mixture into a desired shape.
【請求項10】 澱粉を水、酸化剤および生分解性樹
脂、又は水、可塑剤、酸化剤および生分解性樹脂、又は
可塑剤、酸化剤および生分解性樹脂、と加熱混合し、得
られた混合物を所望の形状に成形することを特徴とする
生分解性成形品の製造方法。
10. A starch obtained by heating and mixing starch with water, an oxidizing agent and a biodegradable resin, or water, a plasticizer, an oxidizing agent and a biodegradable resin, or a plasticizer, an oxidizing agent and a biodegradable resin. A method for producing a biodegradable molded article, which comprises molding the above mixture into a desired shape.
【請求項11】 酸化剤が過酸化物である請求項9また
は10記載の製造方法。
11. The method according to claim 9, wherein the oxidizing agent is a peroxide.
【請求項12】 過酸化物が過硫酸カリウム、過硫酸ア
ンモニウム、過硫酸ナトリウムからなる群から選ばれる
過硫酸塩又は過酸化水素である請求項11記載の製造方
法。
12. The method according to claim 11, wherein the peroxide is a persulfate selected from the group consisting of potassium persulfate, ammonium persulfate and sodium persulfate, or hydrogen peroxide.
【請求項13】 澱粉(乾物基準)100重量部当たり
0.01〜0.50重量部の酸化剤を用いる請求項9〜
12のいずれか1項に記載の製造方法。
13. The use of 0.01 to 0.50 part by weight of an oxidizing agent per 100 parts by weight of starch (dry matter basis).
13. The manufacturing method according to any one of 12.
【請求項14】 澱粉(乾物基準)100重量部当たり
10〜50重量部の水、又は澱粉(乾物基準)100重
量部当たり0.1〜40重量部の水及び1〜100重量
部の可塑剤、又は澱粉(乾物基準)100重量部当たり
1〜100重量部の可塑剤を用いる請求項9〜13のい
ずれか1項に記載の製造方法。
14. 10 to 50 parts by weight of water per 100 parts by weight of starch (dry matter), or 0.1 to 40 parts by weight of water and 1 to 100 parts by weight of plasticizer per 100 parts by weight of starch (dry matter). Or the plasticizer of 1 to 100 parts by weight per 100 parts by weight of starch (dry matter basis) is used.
JP07203489A 1995-08-09 1995-08-09 Composition for biodegradable molded article and method for producing biodegradable molded article Expired - Fee Related JP3078478B2 (en)

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* Cited by examiner, † Cited by third party
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JP2008296482A (en) * 2007-05-31 2008-12-11 Showa Highpolymer Co Ltd Multilayer film
US9376648B2 (en) 2008-04-07 2016-06-28 The Procter & Gamble Company Foam manipulation compositions containing fine particles

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103906809B (en) 2011-11-15 2016-06-29 昭和电工株式会社 Biodegradable resin composition and biological degradability film
US9441105B2 (en) 2011-11-15 2016-09-13 Showa Denko K.K. Biodegradable resin composition, and biodegradable film
JP2016196536A (en) 2015-04-02 2016-11-24 昭和電工株式会社 Resin composition and film thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008296482A (en) * 2007-05-31 2008-12-11 Showa Highpolymer Co Ltd Multilayer film
US9376648B2 (en) 2008-04-07 2016-06-28 The Procter & Gamble Company Foam manipulation compositions containing fine particles

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Publication number Publication date
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