JPH08302058A - Production of cellulose acetate-based foam - Google Patents

Production of cellulose acetate-based foam

Info

Publication number
JPH08302058A
JPH08302058A JP11451695A JP11451695A JPH08302058A JP H08302058 A JPH08302058 A JP H08302058A JP 11451695 A JP11451695 A JP 11451695A JP 11451695 A JP11451695 A JP 11451695A JP H08302058 A JPH08302058 A JP H08302058A
Authority
JP
Japan
Prior art keywords
cellulose acetate
composition
polyoxyalkylene glycol
foam
foaming
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
JP11451695A
Other languages
Japanese (ja)
Other versions
JP2965887B2 (en
Inventor
Kenkichi Nose
健吉 能勢
Hiroyuki Mori
裕之 森
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP11451695A priority Critical patent/JP2965887B2/en
Publication of JPH08302058A publication Critical patent/JPH08302058A/en
Application granted granted Critical
Publication of JP2965887B2 publication Critical patent/JP2965887B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE: To extremely readily obtain a cellulose acetate-based foam having sufficient uniformity and a high expansion ratio and suitable as a packing material by hydrating a polyoxyalkylene glycol-containing cellulose acetate composition, melting, foaming and extruding. CONSTITUTION: A hydrated cellulose acetate composition containing a polyoxyalkylene glycol (preferably one having 200-1,000 molecular weight) is melted, foamed and extruded by preferably a single screw extruder or a twin- screw extruder. The content of the polyoxyalkylene glycol in the composition is preferably 20-40 pts.wt. based on 100 pts.wt. of the cellulose acetate and the water content of the composition is preferably 10-30wt.%. The melt extrusion temperature and the melting temperature are 160-190 deg.C for 2-7 minutes in the case of the blend of 30 pts.wt. of the polyoxyalkylene glycol having 400 molecular weight. When the melting composition is extruded to an atmosphere controlled in the vicinity of the glass transition temperature once, a highly foamed molding is preferably obtained.

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、酢酸セルロース系発泡
体の製造法に関する。さらに詳しくは、本発明は、均一
かつ高度に発泡させることができ、特にパッキング材と
して好適な特性(例えば、優れた軽量性、緩衝性、断熱
性等)を付与し得る酢酸セルロース系発泡体の製造法に
関する。
FIELD OF THE INVENTION The present invention relates to a method for producing a cellulose acetate type foam. More specifically, the present invention relates to a cellulose acetate-based foam that can be uniformly and highly foamed and can impart properties particularly suitable as a packing material (for example, excellent lightness, cushioning property, heat insulating property, etc.). Regarding manufacturing method.

【0002】[0002]

【従来の技術】従来、合成樹脂発泡体は、梱包用緩衝
材、断熱材などの幅広い分野で利用されている。しか
し、これら合成樹脂発泡体には、焼却処理する際に高熱
を発して炉壁を損傷したり有毒な燃焼ガスを発生すると
いう問題、また一方、野ざらしにすると、長期間にわた
って分解され難いために地球環境を悪化させると言う問
題などがあり、廃棄処理の容易な発泡体の開発が望まれ
ている。
2. Description of the Related Art Conventionally, synthetic resin foams have been used in a wide range of fields such as packing cushioning materials and heat insulating materials. However, these synthetic resin foams have a problem that they generate high heat during incineration to damage the furnace wall or generate toxic combustion gas, and on the other hand, if they are exposed, they are difficult to decompose for a long period of time. There is a problem of deteriorating the global environment, and it is desired to develop a foam that can be easily disposed of.

【0003】このような要求に対して、例えば特開平5
−269875号公報、特開平5−306349号公報
などには、含水した、セルロースのエステル化物のよう
な生分解性樹脂を、水の沸点以上に加熱した油に接触さ
せて発泡させる方法が提案されている。しかし、この方
法により得られる発泡体は油で汚れているため取扱いが
面倒であるという問題、さらには、この含水樹脂が酢酸
セルロースの場合には発泡倍率が小さいため、そのまま
ではパッキング材としては不適当であるといった問題が
あった。一方、この含水樹脂をそのまま溶融押出発泡成
形しても、その発泡倍率は小さくかつ発泡も不均一なも
のになって満足し得る発泡体は得られない。
In response to such a request, for example, Japanese Patent Laid-Open No.
JP-A-269875 and JP-A-5-306349 propose a method of foaming a biodegradable resin such as a hydrolyzed esterified product of cellulose, which is brought into contact with oil heated above the boiling point of water. ing. However, since the foam obtained by this method is soiled with oil, it is troublesome to handle. Furthermore, when the water-containing resin is cellulose acetate, the expansion ratio is small, so that it is not suitable as a packing material as it is. There was a problem of being appropriate. On the other hand, even if the water-containing resin is melt-extruded and foam-molded as it is, the expansion ratio is small and the expansion is not uniform, so that a satisfactory foam cannot be obtained.

【0004】また、特公昭63−65367号公報、特
開平6−32928号公報などには、酢酸セルロース、
可塑剤および発泡剤を含有する溶融混合物を発泡押出し
して発泡体を製造する方法が提案されている。しかし、
これらの方法では、溶融された酢酸セルロースと可塑剤
の混合物中にペンタン、アセトン、フレオン等の有機溶
剤を発泡剤として押出機のシリンダー中間から圧入混合
するため、溶融混合物中の発泡剤の分散状態が不均一な
ものとなりやすく均一な発泡体を得ることが困難であ
り、また有機溶剤ガスによる作業環境悪化の問題もあ
る。
Further, in Japanese Patent Publication No. 63-65367 and Japanese Patent Laid-Open No. 6-32928, cellulose acetate,
It has been proposed to produce a foam by foam extruding a molten mixture containing a plasticizer and a foaming agent. But,
In these methods, an organic solvent such as pentane, acetone, or Freon is press-mixed as a foaming agent from the middle of the cylinder of an extruder into a mixture of melted cellulose acetate and a plasticizer, so that the dispersion state of the foaming agent in the melted mixture is Is likely to be non-uniform, and it is difficult to obtain a uniform foam, and there is a problem that the working environment is deteriorated by the organic solvent gas.

【0005】[0005]

【発明が解決しようとする課題】本発明は、上記従来技
術を背景になされたもので、その目的は、均一且つ高発
泡率の酢酸セルロース系発泡体を容易に製造することの
できる方法を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made against the background of the above-mentioned prior art, and an object thereof is to provide a method capable of easily producing a uniform and high foaming rate cellulose acetate foam. To do.

【0006】[0006]

【課題を解決するための手段】本発明者らは、上記目的
を達成するために鋭意検討した結果、ポリオキシアルキ
レングリコールを配合した酢酸セルロースは、あらかじ
め吸水させた後に溶融押出成形することにより、極めて
容易に均一且つ高度に発泡させ得ることを見いだし、本
発明に到達した。
Means for Solving the Problems As a result of intensive studies to achieve the above-mentioned object, the present inventors have found that cellulose acetate containing polyoxyalkylene glycol is melt-extruded after water-absorption in advance. The present invention has been reached by finding that foaming can be performed uniformly and highly highly easily.

【0007】かくして本発明によれば、含水した、ポリ
オキシアルキレングリコールを含有する酢酸セルロース
組成物を、溶融発泡押出することを特徴とする酢酸セル
ロース系発泡体の製造法が提供される。
Thus, according to the present invention, there is provided a method for producing a cellulose acetate-based foam which comprises melt-foaming and extruding a water-containing cellulose acetate composition containing polyoxyalkylene glycol.

【0008】本発明で用いられる酢酸セルロースとは、
セルロースの酢酸エステル化度が結合酢酸として表され
る酢化度が45%以上であるようなものをいい、特に酢
化度が47〜60%(セルロース1単位当たりの結合ア
セチル基の数は1.9〜2.8)のものが好ましい。セ
ルロース酢化度が45%未満の場合には、溶融温度が高
くなりすぎて安定に溶融成形することは困難となる。
The cellulose acetate used in the present invention is
The degree of acetylation of cellulose represented by bound acetic acid is 45% or more. Particularly, the degree of acetylation is 47 to 60% (the number of bound acetyl groups per unit of cellulose is 1). .9 to 2.8) are preferable. When the degree of cellulose acetylation is less than 45%, the melting temperature becomes too high and stable melt molding becomes difficult.

【0009】また、上記酢酸セルロース中に含有せしめ
るポリオキシアルキレングリコールは、エチレンオキサ
イド及び/又はプロピレンオキサイドからなる重合体、
あるいはこれらの混合物を用いることができ、具体的に
は、ポリオキシエチレングリコール、ポリオキシプロピ
レングリコール、エチレンオキサイド/プロピレンオキ
サイドランダム共重合体などを例示できる。かかるポリ
オキシアルキレングリコールの分子量は、特に限定する
必要はないが、酢酸セルロースとの相溶性の観点から2
0000程度以下、特に200〜1000が好ましい。
分子量が20000を越える場合には酢酸セルロースと
の相溶性が低下して均一発泡し難くなる傾向がある。
The polyoxyalkylene glycol contained in the cellulose acetate is a polymer composed of ethylene oxide and / or propylene oxide,
Alternatively, a mixture thereof can be used, and specific examples thereof include polyoxyethylene glycol, polyoxypropylene glycol, and an ethylene oxide / propylene oxide random copolymer. The molecular weight of the polyoxyalkylene glycol is not particularly limited, but it is 2 from the viewpoint of compatibility with cellulose acetate.
It is preferably about 0000 or less, particularly preferably 200 to 1000.
If the molecular weight exceeds 20,000, the compatibility with cellulose acetate decreases and uniform foaming tends to be difficult.

【0010】酢酸セルロース組成物中におけるポリオキ
シアルキレングリコールの含有割合は、用いる酢酸セル
ロースの発泡適性、ポリオキシアルキレングリコールの
分子量さらには該組成物中の含水割合をどの程度にする
かによっても変ってくるが、好ましくは酢酸セルロース
100重量部に対して10〜60重量部、特に20〜4
0重量部の範囲とする。ポリオキシアルキレングリコー
ルの割合が10重量部未満では成形し難くなるだけでな
く得られる発泡体の発泡倍率が低下する傾向にあり、一
方60重量部を越える場合には酢酸セルロース組成物の
ガラス転移温度が低下しすぎて、成形時に充分発泡して
も冷却時に収縮しやすく、高度に発泡した発泡体は得難
くなる。
The polyoxyalkylene glycol content in the cellulose acetate composition varies depending on the foamability of the cellulose acetate used, the molecular weight of the polyoxyalkylene glycol, and the water content of the composition. However, it is preferably 10 to 60 parts by weight, particularly 20 to 4 parts by weight based on 100 parts by weight of cellulose acetate.
The range is 0 parts by weight. If the proportion of polyoxyalkylene glycol is less than 10 parts by weight, not only molding becomes difficult, but also the expansion ratio of the resulting foam tends to decrease, while if it exceeds 60 parts by weight, the glass transition temperature of the cellulose acetate composition is increased. Is too low, and even if it is sufficiently foamed at the time of molding, it tends to shrink when cooled, making it difficult to obtain a highly foamed foam.

【0011】また、上記した組成物中には、本発明の目
的を損なわない範囲で他の物質を配合しても良く、例え
ば酢酸セルロースとの相溶性が良好な熱可塑性樹脂、可
塑剤、熱安定剤、発泡調整剤等が挙げられる。なかで
も、タルク、酸化チタン、ケイ酸カルシウム、シリカ、
炭酸カルシウム、ステアリン酸金属塩などの発泡調整
剤、特にタルクは、該組成物により好適な発泡性を付与
することができ、均一で且つ高度に発泡した発泡体を容
易に得ることができるようになるので好ましい。
Further, the above composition may contain other substances within the range not impairing the object of the present invention. For example, a thermoplastic resin having good compatibility with cellulose acetate, a plasticizer, and a thermosetting resin. Examples include stabilizers and foaming regulators. Among them, talc, titanium oxide, calcium silicate, silica,
Foaming regulators such as calcium carbonate and metal stearates, especially talc, can impart a more suitable foaming property to the composition, so that a uniform and highly foamed foam can be easily obtained. Therefore, it is preferable.

【0012】次ぎに上記酢酸セルロースをポリオキシア
ルキレングリコール及び発泡調整剤等の添加剤とを混合
して組成物となすには、常法に従ってこれらを加熱溶融
混練すればよく、その際の加熱温度、溶融混練時間、溶
融混練手段等の条件は、酢酸セルロースやポリオキシア
ルキレングリコールの熱分解が起こらない範囲内であれ
ば特に限定する必要はない。例えば、加熱温度は混合物
が溶融する温度以上であればよく、用いる酢酸セルロー
スの種類及びポリオキシアルキレングリコールの種類や
混合量等によって混合物の溶融温度は変わってくるの
で、組成に応じて適宜設定すればよい。また溶融混練時
間は、酢酸セルロース及びポリオキシアルキレングリコ
ールの種類やこれらの混合割合だけでなく、用いる溶融
混練手段によっても異なってくるので一概に決定するこ
とはできないが、得られる混合物が均一に分散されるに
必要な時間が採られる。なお、溶融混練手段としては、
通常一軸または二軸のスクリュータイプの押出機が採用
される。
Next, in order to form the composition by mixing the above-mentioned cellulose acetate with polyoxyalkylene glycol and an additive such as a foaming regulator, these may be melted and kneaded by heating according to a conventional method, and the heating temperature at that time. The conditions such as the melt-kneading time and the melt-kneading means are not particularly limited as long as they do not cause thermal decomposition of cellulose acetate or polyoxyalkylene glycol. For example, the heating temperature may be equal to or higher than the temperature at which the mixture melts, and the melting temperature of the mixture varies depending on the type of cellulose acetate and the type and mixing amount of polyoxyalkylene glycol used. Good. The melt-kneading time cannot be unconditionally determined because it depends not only on the types of cellulose acetate and polyoxyalkylene glycol and the mixing ratios thereof, but also on the melt-kneading means used, but the obtained mixture is uniformly dispersed. The time required to be taken is taken. As the melt-kneading means,
Usually, a single-screw or twin-screw type extruder is adopted.

【0013】本発明においては、上記のごとくして得ら
れた酢酸セルロース組成物に、あらかじめ水を積極的に
含水させ、含水した状態のものを溶融押出する必要があ
る。ここで含水させる方法は、特に限定する必要はな
く、任意の方法を採用することができる。例えば、ペレ
ット状の酢酸セルロース組成物を水中に充分な時間浸漬
した後、チップ表面に付着した水滴を取り除いて次の溶
融押出発泡工程に供給する方法、高湿度雰囲気下に長時
間放置して吸湿させる方法等があげられる。この際、適
度に加温してもよく、かくすることによって吸水させる
時間が短くなるし、得られるチップの平衡含水量も大き
くなって高度に発泡した発泡体が容易に得られるので好
ましい。もちろん、大気下における平衡水分量が、求め
られる発泡倍率に充分であれば、あえて含水させる工程
を設ける必要はなく、大気下に放置された平衡水分を含
有する組成物をそのまま用いてもよい。
In the present invention, the cellulose acetate composition obtained as described above is required to be positively hydrated with water in advance, and the hydrated state must be melt-extruded. The method of making water hydrate is not particularly limited, and any method can be adopted. For example, after immersing the pelletized cellulose acetate composition in water for a sufficient time, a method of removing water droplets adhering to the chip surface and supplying it to the next melt extrusion foaming step, and leaving it in a high humidity atmosphere for a long time to absorb moisture There is a method of making it. At this time, it may be heated appropriately, and by doing so, the time for absorbing water is shortened, and the equilibrium water content of the obtained chips is increased, so that a highly foamed foam is easily obtained, which is preferable. Of course, if the equilibrium water content in the air is sufficient for the required expansion ratio, it is not necessary to purposely provide a step of hydrating, and the composition containing the equilibrium water left in the air may be used as it is.

【0014】上記方法等により含水させた組成物中の含
水量は、少なすぎると発泡倍率が不充分となって得られ
る発泡体の特性、特に軽量性、緩衝性、断熱性といった
特性が不充分なものになりやすく、一方多すぎると溶融
押出時の成形安定性が低下して発泡倍率が低下しやす
く、またエネルギーコストも高くなるので5〜40重量
%、特に10〜30重量%の範囲とすることが好まし
い。
If the water content of the composition hydrated by the above-mentioned method is too small, the expansion ratio will be insufficient, and the properties of the resulting foam, especially the properties such as light weight, cushioning property, and heat insulating property will be insufficient. On the other hand, if it is too large, the molding stability during melt extrusion decreases, the expansion ratio tends to decrease, and the energy cost also increases, so it is in the range of 5 to 40% by weight, particularly 10 to 30% by weight. Preferably.

【0015】次に含水した酢酸セルロース組成物を溶融
押出発泡成形するには、従来ポリスチレン等の発泡成形
体を製造するに採用されている公知の溶融押出発泡成形
法を採用すればよいが、特に発泡ガスが逃げない構造の
押出機を採用することが大切で、一軸又は二軸のスクリ
ュー押出機が好ましく用いられる。この際、溶融押出温
度及び溶融時間は、酢酸セルローズの種類、ポリオキシ
アルキレングリコールの種類・量、さらにはスクリュー
押出機の能力によって決定されるが、通常は混合物が分
解されること無く均一に溶融される条件、例えば分子量
が400のポリオキシエチレングリコールを30重量部
配合した場合では溶融温度は160〜190℃、溶融混
練時間は2〜7分が選択される。
Next, in order to perform melt extrusion foam molding of the hydrated cellulose acetate composition, a known melt extrusion foam molding method which has been conventionally used for producing a foam molded article such as polystyrene may be adopted, but particularly, It is important to use an extruder having a structure in which the foaming gas does not escape, and a single-screw or twin-screw extruder is preferably used. At this time, the melt extrusion temperature and the melting time are determined by the type of cellulose acetate, the type and amount of polyoxyalkylene glycol, and the capacity of the screw extruder, but normally the mixture is melted uniformly without decomposition. Under the conditions, for example, when 30 parts by weight of polyoxyethylene glycol having a molecular weight of 400 is blended, a melting temperature of 160 to 190 ° C. and a melt kneading time of 2 to 7 minutes are selected.

【0016】溶融混練された酢酸セルロース組成物は、
円形又は楕円形の吐出孔を有するダイから例えばロッド
状に押出し、次いで所望の長さに切断して発泡体チップ
(ペレット)となす。この時、発泡した水蒸気が逃げな
いように、溶融された組成物を一旦ガラス転移温度付近
にコントロールされた雰囲気中に押出すと、より高度に
発泡した成形物が得られるので好ましい。
The melt-kneaded cellulose acetate composition is
For example, it is extruded into a rod shape from a die having circular or elliptical discharge holes, and then cut into a desired length to obtain foam chips (pellets). At this time, it is preferable to extrude the melted composition into an atmosphere controlled at a temperature near the glass transition temperature so that foamed water vapor does not escape, because a highly foamed molded product can be obtained.

【0017】本発明の製造法によって得られる発泡体の
特性は、例えば発泡倍率(発泡前のペレット比重/発泡
体の比重)で表され、10〜50倍、特に20〜40倍
程度であることが望ましい。かかる発泡倍率が前記範囲
を越える場合には安定に成形することができなくなり、
また機械的強度も悪くなる傾向があり、一方前記範囲未
満では発泡体としての特性を発揮することができない。
The characteristics of the foam obtained by the production method of the present invention are represented by, for example, the expansion ratio (pellet specific gravity before foaming / specific gravity of the foam), and are about 10 to 50 times, especially about 20 to 40 times. Is desirable. When the expansion ratio exceeds the above range, stable molding cannot be achieved,
Further, the mechanical strength tends to be poor, and on the other hand, if it is less than the above range, the properties as a foam cannot be exhibited.

【0018】なお、得られた発泡体の発泡倍率が不十分
な場合には、発泡体に適度に吸水させた後再加熱するこ
とにより発泡倍率を向上させることができる。また、本
発明の製造法においては、得られる発泡体の形状をチッ
プ状(発泡ペレット)にするとともに発泡倍率を小さめ
にし、この発泡ペレットを適当な金型に詰めて加熱する
ことにより、賦形と同時に追発泡させることもできる。
かかる方法によれば、酢酸セルロース組成物中に残存す
る水分が加熱されることにより沸騰気化するとともに、
酢酸セルロース樹脂が軟化ないし溶融するのでその水蒸
気圧によりさらに膨化・発泡し、発泡した塊状体同志が
互いに融着するため、容易に任意の形状を有し且つ高度
な発泡倍率を有する成形体を作成することができる。
When the expansion ratio of the obtained foam is insufficient, the expansion ratio can be improved by allowing the foam to absorb water appropriately and then reheating. Further, in the production method of the present invention, the obtained foam is shaped into chips (foamed pellets), the expansion ratio is made small, and the foamed pellets are packed in an appropriate mold and heated to form a shape. At the same time, additional foaming can be performed.
According to such a method, the water remaining in the cellulose acetate composition is heated to boil and vaporize, and
Since the cellulose acetate resin softens or melts, it further expands and foams due to its water vapor pressure, and the foamed lumps fuse together to create a molded product with any shape and a high expansion ratio. can do.

【0019】[0019]

【実施例】以下実施例により本発明をさらに詳しく説明
するが、本発明はこれらに限定されるものではない。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto.

【0020】平均酢化度が54.7%のセルロースアセ
テートフレークスを粉砕した後、ポリオキシエチレング
リコール(日本油脂製PEG−400)とタルク(富士
タルク製LMR−200)を表1記載の割合で混合し、
これを日本製鋼製押出成形機P90−28Vにて径2m
mの円形孔を20個有するダイから溶融押出し、ペレッ
トに成形した。得られたペレットを水中に20℃下で浸
漬して表1記載の割合となるよう吸水させた後、Ishina
ka Iron Works Co.Lid. 製単軸押出成形機にて径3.5
mmの円形孔を7個有するダイから表1記載の温度で溶
融押出し発泡チップを得た。結果は表1に示す。
After crushing cellulose acetate flakes having an average degree of acetylation of 54.7%, polyoxyethylene glycol (PEG-400 manufactured by NOF CORPORATION) and talc (LMR-200 manufactured by Fuji Talc) in the proportions shown in Table 1. Mix and
This is 2m in diameter with a Japanese steel extrusion machine P90-28V.
It was melt extruded from a die having 20 circular holes of m and formed into pellets. The pellets thus obtained were immersed in water at 20 ° C. to absorb water at the ratios shown in Table 1, and then Ishina
Diameter of 3.5 with a single-screw extruder manufactured by ka Iron Works Co.Lid.
Melt extrusion was performed at a temperature shown in Table 1 to obtain foam chips from a die having 7 mm circular holes. The results are shown in Table 1.

【0021】[0021]

【表1】 [Table 1]

【0022】[0022]

【発明の効果】以上、本発明の方法によれば、格別な発
泡剤を用いることなく、極めて容易に均一かつ高度に発
泡した酢酸セルロース系発泡体を得ることができ、従来
の酢酸セルロース系発泡体に比して、特にパッキング材
として好適な発泡体を提供することができる。また、併
用するポリオキシアルキレングリコールも生分解性に優
れているため、廃棄処理も容易で地球環境を悪化させる
ことはない。
As described above, according to the method of the present invention, a uniform and highly foamed cellulose acetate-based foam can be obtained very easily without using a special foaming agent. It is possible to provide a foam that is particularly suitable as a packing material as compared with the body. Further, the polyoxyalkylene glycol used in combination is also excellent in biodegradability, so that it can be easily disposed of and does not deteriorate the global environment.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 含水した、ポリオキシアルキレングリコ
ールを含有する酢酸セルロース組成物を、溶融発泡押出
することを特徴とする酢酸セルロース系発泡体の製造
法。
1. A method for producing a cellulose acetate-based foam, which comprises melt-foaming and extruding a water-containing cellulose acetate composition containing polyoxyalkylene glycol.
【請求項2】 組成物中の含水量が5〜40重量%であ
る請求項1記載の酢酸セルロース系発泡体の製造法。
2. The method for producing a cellulose acetate-based foam according to claim 1, wherein the water content of the composition is 5 to 40% by weight.
【請求項3】 ポリオキシアルキレングリコールが、平
均分子量が20000以下のポリオキシエチレングリコ
ールである請求項2記載の酢酸セルロース系発泡体の製
造法。
3. The method for producing a cellulose acetate-based foam according to claim 2, wherein the polyoxyalkylene glycol is polyoxyethylene glycol having an average molecular weight of 20,000 or less.
【請求項4】 組成物中のポリオキシエチレングリコー
ルの含有割合が、酢酸セルロース100重量部に対して
10〜60重量部である請求項3記載の酢酸セルロース
系発泡体の製造法。
4. The method for producing a cellulose acetate-based foam according to claim 3, wherein the content ratio of polyoxyethylene glycol in the composition is 10 to 60 parts by weight based on 100 parts by weight of cellulose acetate.
JP11451695A 1995-05-12 1995-05-12 Method for producing cellulose acetate foam Expired - Fee Related JP2965887B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11451695A JP2965887B2 (en) 1995-05-12 1995-05-12 Method for producing cellulose acetate foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11451695A JP2965887B2 (en) 1995-05-12 1995-05-12 Method for producing cellulose acetate foam

Publications (2)

Publication Number Publication Date
JPH08302058A true JPH08302058A (en) 1996-11-19
JP2965887B2 JP2965887B2 (en) 1999-10-18

Family

ID=14639717

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11451695A Expired - Fee Related JP2965887B2 (en) 1995-05-12 1995-05-12 Method for producing cellulose acetate foam

Country Status (1)

Country Link
JP (1) JP2965887B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0940243A4 (en) * 1997-09-05 2000-04-05 Teijin Ltd Biodegradable cellulose acetate foams and process for producing the same
JP2002069437A (en) * 2000-08-28 2002-03-08 Plusto:Kk Antibacterial cold-reserving material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0940243A4 (en) * 1997-09-05 2000-04-05 Teijin Ltd Biodegradable cellulose acetate foams and process for producing the same
JP2002069437A (en) * 2000-08-28 2002-03-08 Plusto:Kk Antibacterial cold-reserving material

Also Published As

Publication number Publication date
JP2965887B2 (en) 1999-10-18

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