JP2000319457A - Starch-filled crosslinked polyolefin open-cell foam and its production - Google Patents

Starch-filled crosslinked polyolefin open-cell foam and its production

Info

Publication number
JP2000319457A
JP2000319457A JP11171447A JP17144799A JP2000319457A JP 2000319457 A JP2000319457 A JP 2000319457A JP 11171447 A JP11171447 A JP 11171447A JP 17144799 A JP17144799 A JP 17144799A JP 2000319457 A JP2000319457 A JP 2000319457A
Authority
JP
Japan
Prior art keywords
starch
polyolefin
open
foam
cell
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
JP11171447A
Other languages
Japanese (ja)
Inventor
Choji Obara
長二 小原
Tadahiro Yonezawa
忠弘 米沢
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.)
Sanwa Kako Co Ltd
Original Assignee
Sanwa 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 Sanwa Kako Co Ltd filed Critical Sanwa Kako Co Ltd
Priority to JP11171447A priority Critical patent/JP2000319457A/en
Publication of JP2000319457A publication Critical patent/JP2000319457A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a crosslinked polyolefin open-cell foam desirable for a medium for bacterial proliferation and excellent in water permeability by introducing starch into cell membranes and/or a skeleton. SOLUTION: There is provided a process for producing a starch-filled crosslinked polyolefin open-cell foam, comprising foaming under heating in a non-sealed mold a foamable crosslinkable composition prepared by adding a blowing agent and a crosslinking agent to a polyolefin to form a foam and converting the cells of the foam into open cells by the action of mechanical deformation, which process comprises adding starch to the polyolefin and foaming the mixture under kneading. It is desirable that 10-100 pts.wt. starch is added to 100 pts.wt. polyolefin. The polyolefin is exemplified by a polyethylene or an ethylene/propylene copolymer. The starch used may be one of various starches. The crosslinking agent used is an organic peroxide having a decomposition temperature not lower than the flow initiation temperature of the polyethylene resin. In this case, a chemical blowing agent having a decomposition temperature not lower than the melting temperature of the polyethylene resin is used.

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、澱粉入り架橋ポリ
オレフィン連続気泡体及びその製造方法に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a starch-containing crosslinked polyolefin open cell and a method for producing the same.

【0002】[0002]

【従来の技術】架橋ポリオレフィン連続気泡体は、耐候
性、断熱性、吸音性等に優れているので、エアコン内の
断熱材、自動車のドアミラー内の吸音材、浄化槽内のバ
クテリアの担体、塗布材等の各種用途に広く利用されて
いる。架橋ポリオレフィン連続気泡体の製造方法として
は、 (1)密閉金型中で発泡性架橋性組成物中の発泡剤と架
橋剤を部分的に分解させ、常圧下で残存する発泡剤と架
橋剤を分解させて独立気泡体を得、次いで得られた独立
気泡体を圧縮して独立気泡を破壊する方法が提案されて
いた(特公昭59−23545号及び特開昭56−14
6732号公報参照)。 (2)本出願人は、発泡性架橋性組成物を所望の形状に
加熱整形した後、常圧下にて加熱して架橋剤及び発泡剤
を同時進行的に分解させて気泡体を生成させ、次いで機
械的変形を加えて気泡を連通化させる方法を開発してい
る(特公昭62−19294号公報、特公平1−444
99号公報)。 (3)無架橋のポリオレフィン系樹脂連続気泡体の製造
方法としては、ポリオレフィン系樹脂に、エチレン−メ
タクリル酸共重合体及び核形成剤、収縮防止剤等からな
るポリオレフィン系樹脂組成物を加熱して軟化、または
溶融発泡させた後、揮発性発泡剤を供給混合して得られ
る組成物を低圧域に開放する方法(特開平10−279
724号公報参照)が提案されている。 しかしながら、上記(2)及び(3)の方法により得ら
れる連続気泡体は、連続気泡率が低く、上記(1)の方
法によれば、連続気泡率100%又は100%に近い連
続気泡体が得られるが、気泡体内部の通水性に劣ると共
に、バクテリアを増殖させる培地としての効果が十分と
は言えなかった。
2. Description of the Related Art Cross-linked polyolefin open-cell foams are excellent in weather resistance, heat insulating properties, sound absorbing properties, etc., and are therefore heat insulating materials in air conditioners, sound absorbing materials in door mirrors of automobiles, bacteria carriers in septic tanks, and coating materials. Widely used for various applications such as. The method for producing a cross-linked polyolefin open cell is as follows: (1) The foaming agent and the cross-linking agent in the foamable cross-linkable composition are partially decomposed in a closed mold, and the foaming agent and the cross-linking agent remaining under normal pressure are mixed. A method has been proposed in which closed cells are obtained by disintegration, and then the obtained closed cells are compressed to break closed cells (Japanese Patent Publication No. 59-23545 and Japanese Patent Application Laid-Open No. 56-14 / 1981).
No. 6732). (2) The present applicant heat-shapes the expandable crosslinkable composition into a desired shape, and then heats it under normal pressure to simultaneously and progressively decompose the crosslinker and the foaming agent to form a foam, Subsequently, a method of making the bubbles open by applying mechanical deformation has been developed (Japanese Patent Publication No. 62-19294, Japanese Patent Publication No. 1-444).
No. 99). (3) As a method for producing a non-crosslinked polyolefin resin open cell, a polyolefin resin is heated by heating a polyolefin resin composition comprising an ethylene-methacrylic acid copolymer, a nucleating agent, a shrinkage inhibitor and the like. A method in which a composition obtained by softening or melt-foaming and then supplying and mixing a volatile foaming agent is opened to a low pressure region (JP-A-10-279).
724) has been proposed. However, the open-cell foam obtained by the methods (2) and (3) has a low open-cell rate, and according to the method (1), the open-cell rate is 100% or close to 100%. Although it was obtained, it was inferior in water permeability inside the foam and was not sufficiently effective as a medium for growing bacteria.

【0003】[0003]

【発明が解決しようとする課題】従って、本発明の目的
は、前記従来技術の欠点を解消し、バクテリア増殖の培
地として好適で、通水性に優れた架橋ポリオレフイン連
続気泡体及びその製造方法を提供することにある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a crosslinked polyolefin open-cell foam which overcomes the above-mentioned drawbacks of the prior art, is suitable as a culture medium for bacterial growth, and has excellent water permeability. Is to do.

【0004】[0004]

【課題を解決するための手段】前記目的を達成するた
め、本発明の澱粉入り架橋ポリオレフィン連続気泡体
は、気泡の膜及び/又は骨格に澱粉粒子を含有すること
を特徴とする。本発明の澱粉入り架橋ポリオレフィン発
泡体において、ポリオレフィン100重量部に対し、澱
粉10〜100重量部を含有することが好ましい。本発
明の澱粉入り架橋ポリオレフィン連続気泡体の製造方法
は、ポリオレフィンに発泡剤及び架橋剤を添加した発泡
性架橋性組成物を気密でない金型中で加熱発泡させて気
泡体を生成させ、次いで機械的変形を加えて気泡を連通
化させる連続気泡体の製造方法において、ポリオレフィ
ンに澱粉を添加、混練りして発泡させることを特徴とす
るものである。本発明の製造方法において、ポリオレフ
ィン100重量部中に澱粉10〜100重量部を添加す
ることが好ましい。
Means for Solving the Problems In order to achieve the above object, a starch-containing crosslinked polyolefin open cell according to the present invention is characterized in that the cell membrane and / or skeleton contains starch particles. The starch-containing crosslinked polyolefin foam of the present invention preferably contains 10 to 100 parts by weight of starch based on 100 parts by weight of polyolefin. The method for producing a starch-containing crosslinked polyolefin open cell of the present invention comprises producing a foam by heating and foaming a foamable crosslinkable composition obtained by adding a foaming agent and a crosslinking agent to a polyolefin in an airtight mold. A method for producing an open-cell body in which bubbles are communicated by subjecting the polyolefin to continuous deformation, characterized in that starch is added to a polyolefin, kneaded and foamed. In the production method of the present invention, it is preferable to add 10 to 100 parts by weight of starch to 100 parts by weight of polyolefin.

【0005】[0005]

【発明の実施の形態】本発明は、澱粉のバクテリア菌増
殖効果に着目し、架橋ポリオレフィン連続気泡体の製造
工程において、ポリオレフィンに澱粉を添加し、澱粉を
気泡の膜及び/又は骨格に含有させることにより、培地
としてバクテリアの増殖作用を促進すると共に、水中で
の使用時に澱粉の消失による気泡膜の連通化を促進する
ものである。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention focuses on the effect of starch on the growth of bacteria, and in the process of producing a crosslinked polyolefin open cell, starch is added to the polyolefin so that the starch is contained in the film and / or skeleton of the cell. This not only promotes the growth of bacteria as a medium, but also promotes the communication of the cell membrane due to the disappearance of starch when used in water.

【0006】以下、本発明に係る連続気泡体の製造方法
についてその好適な態様を具体的に説明する。まず、ポ
リオレフィン100重量部に澱粉を好ましくは10重量
部〜100重量部、特に好ましくは20重量部〜50重
量部、発泡剤、架橋剤、及び必要に応じて発泡助剤、充
填剤、顔料等を添加し、これを加熱したミキシングロー
ル、加圧式ニーダー、押出機等によって練和する。上記
において澱粉が10重量部未満の場合、バクテリアの増
殖作用が不足すると共に、気泡の連通化効果が不足し、
100重量部を超えると満足な気泡体が形成できない。
本発明でいうポリオレフィンとは、例えば通常市販の
高、中、低圧法により製造されたポリエチレン、ポリ−
1・2−ブタジエン、エチレン−プロピレン共重合体、
エチレン−ブテン共重合体、エチレン−酢酸ビニル共重
合体、エチレンと含有量45%までのメチル−、エチル
−、プロピル−、ブチル−の各アクリレートもしくはメ
タクリレートとの共重合体、またはこれらをそれぞれ塩
素化したもの(塩素含有率60重量%まで)、あるい
は、これらの2種以上の混合物またはこれらとアタクチ
ックもしくはアイソタクチック構造を有するポリプロピ
レンとの混合物などである。
Hereinafter, a preferred embodiment of the method for producing an open-cell body according to the present invention will be specifically described. First, starch is preferably 10 to 100 parts by weight, particularly preferably 20 to 50 parts by weight, based on 100 parts by weight of polyolefin, a foaming agent, a crosslinking agent, and, if necessary, a foaming aid, a filler, a pigment, and the like. And kneaded with a heated mixing roll, pressure kneader, extruder or the like. In the case where the amount of starch is less than 10 parts by weight, the effect of growing bacteria is insufficient, and the effect of communicating air bubbles is insufficient,
If it exceeds 100 parts by weight, a satisfactory foam cannot be formed.
The polyolefin referred to in the present invention includes, for example, polyethylene, poly-polyethylene produced by high-, medium-, and low-pressure methods which are usually commercially available.
1,2-butadiene, ethylene-propylene copolymer,
Ethylene-butene copolymer, ethylene-vinyl acetate copolymer, copolymer of ethylene with each acrylate or methacrylate of methyl-, ethyl-, propyl-, butyl- up to 45% content, or chlorine (A chlorine content of up to 60% by weight), a mixture of two or more of these, or a mixture of these with a polypropylene having an atactic or isotactic structure.

【0007】本発明でいう澱粉とは、種々のものが使用
でき、たとえば、トウモロコシ澱粉、馬鈴薯デンプン、
甘藷デンプン、小麦デンプン、キッサバデンプン、サゴ
デンプン、タビオデンプン、モロコシデンプン、コメデ
ンプン、マメデンプン、クズデンプン、ワラビデンプ
ン、ハスデンプン、ヒシデンプン等;物理的変性デンプ
(α−デンプン、分別アミロース、湿熱処理デンプン
等);酵素変性デンプン(加水分解デキストリン、酵素
分解デキストリン、アミロース等);化学分解変性デン
プン(酸処理デンプン、次亜塩素酸化デンプン、ジアル
デヒドデンプン等);化学変性デンプン誘導体(エステ
ル化デンプン、エーテル化デンプン、カチオン化デンプ
ン、架橋デンプン等)等が例示できる。本発明でいう架
橋剤とは、ポリエチレン系樹脂中において少なくともポ
リエチレン系樹脂の流動開始温度以上の分解温度を有す
るものであって、加熱により分解され、遊離ラジカルを
発生してその分子間もしくは分子内に架橋結合を生じせ
しめるラジカル発生剤であるところの有機過酸化物、例
えばジクミルパーオキサイド、1,1−ジターシャリー
ブチルパーオキシ−3,3,5−トリメチルシクロヘキ
サン、2,5−ジメチル−2,5−ジターシャリーブチ
ルパーオキシヘキサン、2,5−ジメチル−2,5−ジ
ターシャリーブチルパーオキシヘキシン、α,α−ジタ
ーシャリーブチルパーオキシイソプロピルベンゼン、タ
ーシャリーブチルパーオキシケトン、ターシャリーブチ
ルパーオキシベンゾエートなどがあるが、その時に使用
される樹脂によって最適な有機過酸化物を選ばなければ
ならない。
As the starch used in the present invention, various types can be used. For example, corn starch, potato starch,
Sweet potato starch, wheat starch, kissava starch, sago starch, tabio starch, sorghum starch, rice starch, bean starch, kudzu starch, bracken starch, hasto starch, hisshi starch, etc .; physically modified starch (α-starch, fractionated amylose, etc.) ); Enzyme-modified starch (hydrolyzed dextrin, enzymatically-degraded dextrin, amylose, etc.); Chemically-modified starch (acid-treated starch, hypochlorinated starch, dialdehyde starch, etc.); Chemically-modified starch derivative (esterified starch, etherified) Starch, cationized starch, cross-linked starch, etc.). The cross-linking agent referred to in the present invention has a decomposition temperature in the polyethylene resin at least equal to or higher than the flow start temperature of the polyethylene resin, and is decomposed by heating to generate free radicals to generate intermolecular or intramolecular molecules. Organic peroxides that are radical generators that cause cross-linking to be formed, such as dicumyl peroxide, 1,1-ditert-butylperoxy-3,3,5-trimethylcyclohexane, 2,5-dimethyl-2 , 5-Di-tert-butyl peroxyhexane, 2,5-dimethyl-2,5-di-tert-butyl peroxyhexyne, α, α-di-tert-butyl peroxyisopropylbenzene, tert-butyl peroxy ketone, tert-butyl There is peroxybenzoate, etc., but it is used at that time The optimum organic peroxide must be selected depending on the resin used.

【0008】本発明で使用し得る発泡剤は、ポリエチレ
ン系樹脂の溶融温度以上の分解温度を有する化学発泡剤
であり、例えばアゾ系化合物のアゾジカルボンアミド、
バリウムアゾジカルボキシレート等:ニトロソ系化合物
のジニトロソペンタメチレンテトラミン、トリニトロト
リメチルトリアミン等;ヒドラジッド系化合物のp,
p’−オキシビスベンゼンスルホニルヒドラジッド等;
スルホニルセミカルバジッド系化合物のp,p’−オキ
シビスベンゼンスルホニルセミカルバジッド、トルエン
スルホニルセミカルバジッド等、がある。
The blowing agent which can be used in the present invention is a chemical blowing agent having a decomposition temperature higher than the melting temperature of the polyethylene resin, such as azodicarbonamide, an azo compound,
Barium azodicarboxylate and the like: nitroso compounds such as dinitrosopentamethylenetetramine and trinitrotrimethyltriamine; hydrazide compounds such as p,
p'-oxybisbenzenesulfonyl hydrazide and the like;
There are sulfonyl semicarbazide compounds such as p, p'-oxybisbenzenesulfonyl semicarbazide and toluenesulfonyl semicarbazide.

【0009】本発明においては、発泡助剤を発泡剤の種
類に応じて添加することができる。発泡助剤としては尿
素を主成分とした化合物、酸化亜鉛、酸化鉛等の金属酸
化物、サリチル酸、ステアリン酸等を主成分とする化合
物、即ち高級脂肪酸あるいは高級脂肪酸の金属化合物な
どがある。本発明においては、使用する組成物の物性の
改良あるいは価格の低下を目的として、架橋結合に著し
い悪影響を与えない配合剤(充填剤)、例えば酸化亜
鉛、酸化チタン、酸化カルシウム、酸化マグネシウム、
酸化ケイ素等の金属酸化物、炭酸マグネシウム、炭酸カ
ルシウム等の炭酸塩、あるいはパルプ等の繊維物質、ま
たは各種染料、顔料並びに蛍光物質、その他常用のゴム
配合剤等を必要に応じて添加することができる。
In the present invention, a foaming aid can be added according to the type of the foaming agent. Examples of the foaming aid include compounds mainly containing urea, metal oxides such as zinc oxide and lead oxide, compounds mainly containing salicylic acid, stearic acid and the like, that is, higher fatty acids and metal compounds of higher fatty acids. In the present invention, for the purpose of improving the physical properties or reducing the price of the composition to be used, a compounding agent (filler) that does not significantly affect cross-linking, for example, zinc oxide, titanium oxide, calcium oxide, magnesium oxide,
Metal oxides such as silicon oxide, carbonates such as magnesium carbonate and calcium carbonate, or fibrous materials such as pulp, or various dyes, pigments and fluorescent materials, and other conventional rubber compounding agents may be added as necessary. it can.

【0010】上記のように練和して得られた発泡性架橋
性組成物を金型に仕込み、プレスにて加圧下で樹脂及び
架橋剤の種類に応じて115〜155℃、好ましくは1
20〜140℃において加熱整形する。この加熱整形工
程において、発泡性架橋性組成物を好ましくはゲル分率
ゼロの状態に維持して整形することが、連続気泡率10
0%又は100%に近い連続気泡体を得る条件である。
なお、この加熱整形工程において、非常に微量の発泡剤
が初期分解を生じ、整形品を金型から取り出した場合に
2倍程度まで膨張しうるが、これは発泡という概念から
は程遠く、本発明にとって何ら差し支えない。
[0010] The foamable crosslinkable composition obtained by kneading as described above is charged into a mold, and is pressurized with a press at 115 to 155 ° C, preferably 1 to 150 ° C, depending on the type of the resin and the crosslinking agent.
Heat shaping at 20-140 ° C. In this heating shaping step, shaping while maintaining the foamable crosslinkable composition preferably in a state where the gel fraction is zero can be achieved by an open cell rate of 10%.
This is a condition for obtaining an open cell close to 0% or 100%.
In this heating shaping step, a very small amount of the foaming agent undergoes initial decomposition, and when the shaped article is taken out of the mold, it can expand to about twice, but this is far from the concept of foaming, and the present invention It doesn't hurt anything.

【0011】上記のようにして整形された発泡性架橋性
組成物は、次いで、常圧下にて加熱することによって、
架橋剤及び発泡剤の分解を同時進行的に行なわしめられ
る。この発泡・架橋工程は、例えば整形されたポリオレ
フィン組成物を所望の断面形状、寸法を有する気密でな
い、即ち密閉されていない金型中に入れ、該金型の金属
板を外部から加熱することによって上記組成物を間接的
に加熱せしめる。間接的に加熱せしめる方法としては、
例えば金属板外表面にヒーターを密着させて加熱する
か、あるいは金属板に熱媒の流路を設け、ジャケット方
式で蒸気、加熱オイル等によって加熱する方法がある。
あるいは、整形されたポリオレフィン組成物を気密でな
い開閉式の金型に入れ、ローゼ合金、ウッド合金等を用
いるメタルバスやオイルバス中、硝酸ナトリウム、硝酸
カリウム、亜硝酸カリウム等の1種又は2種以上の溶融
塩を用いる塩浴中、もしくは窒素気流中で、あるいは伸
張(ないし拡張)可能な鉄板等により覆われた状態で直
接加熱せしめる。所定時間加熱した後、冷却して気泡体
を得る。加熱温度は、使用する樹脂の種類に応じて14
0〜210℃、好ましくは160〜190℃の範囲に設
定する。加熱時間は、好ましくは30〜200分、さら
に好ましくは50〜180分である。このようにして、
機械的変形を与えることによって容易に破壊しうる気泡
膜を有し、かつ従来の気泡体と同程度の架橋度(ゲル分
率95%程度まで)を有する気泡体が得られる。
The foamable crosslinkable composition shaped as described above is then heated under normal pressure to obtain
The decomposition of the crosslinking agent and the blowing agent can be performed simultaneously. This foaming / crosslinking step is performed, for example, by placing the shaped polyolefin composition in a non-hermetic, that is, unsealed mold having a desired cross-sectional shape and dimensions, and heating the metal plate of the mold from outside. The composition is heated indirectly. As a method of indirectly heating,
For example, there is a method in which a heater is brought into close contact with the outer surface of a metal plate and heating is performed, or a flow path of a heat medium is provided in the metal plate and heating is performed by steam, heating oil, or the like in a jacket system.
Alternatively, the shaped polyolefin composition is placed in a mold that is not airtight and can be opened and closed. It is directly heated in a salt bath using a molten salt, in a nitrogen stream, or in a state covered with an extensible (or expandable) iron plate or the like. After heating for a predetermined time, it is cooled to obtain a foam. The heating temperature depends on the type of resin used.
The temperature is set in the range of 0 to 210 ° C, preferably 160 to 190 ° C. The heating time is preferably 30 to 200 minutes, more preferably 50 to 180 minutes. In this way,
A foam having a foam film that can be easily broken by mechanical deformation and having a degree of crosslinking (up to a gel fraction of about 95%) similar to that of a conventional foam can be obtained.

【0012】以上のようにして得られた気泡体(いわゆ
る独立気泡体)は、次いで例えば等速二本ロール等によ
り圧縮変形を加えることによって気泡膜は破壊され、気
泡が連通化されて連続気泡体が得られる。等速二本ロー
ルの表面に無数の小さい針を設けるか、又は等速二本ロ
ールの前及び/又は後に無数の小さい針を設けたロール
を配置して、該気泡体の表面に無数の小孔を開けること
によって、気泡の連通化を促進させることができる。こ
の方法によって得られる連続気泡体は、ASTM−D2
856に準拠した空気比較式比重計1000型(東京サ
イエンス(株)製)を用いて測定した連続気泡率が10
0%又は100%に近いものである。本発明の方法によ
って得られる連続気泡体は、電子線を照射して連続気泡
体表面の架橋度を高くし、耐熱性を5〜10℃向上させ
ることができる。電子線照射の条件は、例えば、室温で
変圧器整流型電子線加速器により、800Kev、6m
A、2.1x10rad/秒の電子線を10Mrad
照射する。
The foam (so-called closed cell) obtained as described above is then subjected to compressive deformation by, for example, a constant-speed double roll or the like, so that the bubble film is broken, and the bubbles are made open to open cells. The body is obtained. Countless small needles are provided on the surface of the constant velocity double roll, or rolls provided with countless small needles are arranged before and / or after the constant velocity double roll, and countless small needles are provided on the surface of the foam. By forming the holes, the communication of bubbles can be promoted. The open cell obtained by this method is ASTM-D2
The open cell ratio measured using an air comparison specific gravity meter 1000 (manufactured by Tokyo Science Co., Ltd.) conforming to 856 is 10
It is close to 0% or 100%. The open-cell body obtained by the method of the present invention can be irradiated with an electron beam to increase the degree of cross-linking on the surface of the open-cell body and improve heat resistance by 5 to 10 ° C. The conditions of the electron beam irradiation are, for example, 800 Kev, 6 m at room temperature by a transformer rectifier type electron beam accelerator.
A, an electron beam of 2.1 × 10 6 rad / sec.
Irradiate.

【0013】[0013]

【実施例】以下、実施例を示して本発明を更に具体的に
説明するが、本発明は下記実施例により何等限定される
ものではない。 実施例1 エチレン酢酸ビニル共重合体(商品名「ノバテックEV
A LV540」、酢酸ビニル含有量20%、MFR
2.5g/10分、密度0.942g/cm、日本ポ
リケム株式会社製)100重量部、アゾジカルボンアミ
ド10重量部、小麦粉30重量部、ステアリン酸亜鉛
0.03重量部、尿素系発泡助剤0.01重量部、活性
亜鉛華0.03重量部、ジクミルパーオキサイド1.0
重量部からなる組成物を85℃のミキシングロールにて
練和し、130℃に加熱されたプレス内の金型(400
x200x40mm)に上記練和物を充填し、80分間
加圧下で加熱し、発泡性架橋性シートを整形した。該発
泡性架橋性シートはゲル分率0であった。次いで、得ら
れた発泡性架橋性シートを既に170℃に加熱されてい
る気密でない開閉式の金型(1000x500x100
mm)に入れ、ジャケット方式により170℃の蒸気で
180分間加熱し、冷却後取り出し、発泡体を得た。得
られた発泡体をロール間隔20mmに設定した等速二本
ロールの間を5回通化させて気泡膜を破壊させ、気泡の
連通化を行なった。得られた連続気泡体は、見掛け密度
0.05g/cm、連続気泡率100%、気泡径約1
mmであった。得られた連続気泡体は、通水性に優れ、
10mm程度の矩形に裁断し、浄化槽内のバクテリアの
担体として使用した結果、培地としてバクテリア菌を増
殖させる効果が顕著であった。
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to Examples, but the present invention is not limited to the following Examples. Example 1 Ethylene vinyl acetate copolymer (trade name: Novatec EV
A LV540 ", vinyl acetate content 20%, MFR
2.5 g / 10 min, density 0.942 g / cm 3 , manufactured by Nippon Polychem Co., Ltd.) 100 parts by weight, azodicarbonamide 10 parts by weight, flour 30 parts by weight, zinc stearate 0.03 parts by weight, urea foaming aid 0.01 parts by weight, active zinc white 0.03 parts by weight, dicumyl peroxide 1.0
The composition consisting of parts by weight was kneaded with a mixing roll at 85 ° C., and a mold (400
(× 200 × 40 mm), and the mixture was heated under pressure for 80 minutes to form a foamable crosslinkable sheet. The foamable crosslinkable sheet had a gel fraction of 0. Then, the obtained foamable crosslinkable sheet is sealed with a non-hermetic open / close mold (1000 × 500 × 100) already heated to 170 ° C.
mm), heated with steam at 170 ° C. for 180 minutes by a jacket method, taken out after cooling, and obtained a foam. The obtained foam was passed five times between two constant-velocity rolls set at a roll interval of 20 mm to break the cell membrane, thereby allowing the cells to communicate. The obtained open cell had an apparent density of 0.05 g / cm 3 , an open cell ratio of 100%, and a cell diameter of about 1
mm. The obtained open-celled body has excellent water permeability,
After cutting into a rectangle of about 10 mm and using it as a carrier for bacteria in the septic tank, the effect of growing bacterial bacteria as a medium was remarkable.

【0014】比較例1 実施例1において、澱粉を添加しない以外は、実施例1
と同じ配合及び同じ条件で、連続気泡体を得た。得られ
た連続気泡体は、見掛け密度0.05g/cm、連続
気泡率100%であったが、通水性に劣り、バクテリア
の増殖作用が不十分であった。 実施例2 実施例1において、澱粉を20重量部に変えた以外は、
実施例1と同じ配合及び同じ条件で連続気泡体を得た。
得られた連続気泡体は、見掛け密度0.05g/c
、連続気泡率100%で通水性に優れ、実施例1と
同様、バクテリア菌を増殖させる培地として好適であっ
た。 実施例3 実施例1において、澱粉を50重量部に変えた以外は、
実施例1と同じ配合及び同じ条件で連続気泡体を得た。
得られた連続気泡体は、見掛け密度0.05g/c
、連続気泡率100%で通水性に優れ、実施例1と
同様、バクテリア菌を増殖させる培地として好適であっ
た。 比較例2 実施例1において、澱粉を120部に変えた以外は、実
施例1と同じ配合及び同じ条件で発泡させた結果、収縮
し、満足な気泡体を得ることができなかった。 実施例4 実施例1において、小麦粉30重量部を馬鈴薯澱粉30
重量部に変えた以外は、実施例1と同じ配合及び発泡条
件で連続気泡体を得た。得られた連続気泡体は、見掛け
密度0.05g/cm、連続気泡率100%で通水性
に優れ、実施例1と同様、バクテリア菌を増殖させる培
地として好適であった。 実施例5 実施例1において、小麦粉30重量部を甘藷澱粉30重
量部に変えた以外は、実施例1と同じ配合及び発泡条件
で連続気泡体を得た。得られた連続気泡体は、見掛け密
度0.05g/cm、連続気泡率100%で通水性に
優れ、実施例1と同様、バクテリア菌を増殖させる培地
として好適であった。
Comparative Example 1 Example 1 was repeated except that no starch was added.
Under the same composition and under the same conditions as in Example 1, an open-cell foam was obtained. The obtained open-cell foam had an apparent density of 0.05 g / cm 3 and an open-cell ratio of 100%, but had poor water permeability and insufficient bacterial growth. Example 2 In Example 1, except that the starch was changed to 20 parts by weight.
An open cell was obtained under the same composition and under the same conditions as in Example 1.
The obtained open-cell foam has an apparent density of 0.05 g / c.
m 3 , 100% open cell rate and excellent water permeability, and was suitable as a medium for growing bacterial bacteria as in Example 1. Example 3 In Example 1, except that starch was changed to 50 parts by weight.
An open cell was obtained under the same composition and under the same conditions as in Example 1.
The obtained open-cell foam has an apparent density of 0.05 g / c.
m 3 , 100% open cell rate and excellent water permeability, and was suitable as a medium for growing bacterial bacteria as in Example 1. Comparative Example 2 In Example 1, except that the amount of starch was changed to 120 parts, foaming was performed under the same composition and under the same conditions as in Example 1. As a result, the foam shrank and a satisfactory foam could not be obtained. Example 4 In Example 1, 30 parts by weight of flour was replaced with potato starch 30.
An open-cell body was obtained under the same blending and foaming conditions as in Example 1 except that the amount was changed to parts by weight. The obtained open-cell foam was excellent in water permeability with an apparent density of 0.05 g / cm 3 and an open-cell ratio of 100%, and was suitable as a medium for growing bacterial bacteria as in Example 1. Example 5 An open-cell foam was obtained in the same manner as in Example 1 except that 30 parts by weight of wheat flour was changed to 30 parts by weight of sweet potato starch. The obtained open-cell foam was excellent in water permeability with an apparent density of 0.05 g / cm 3 and an open-cell ratio of 100%, and was suitable as a medium for growing bacterial bacteria as in Example 1.

【0015】[0015]

【表1】 [Table 1]

【0016】[0016]

【発明の効果】上述の様に、本発明によれば、架橋ポリ
オレフィン連続気泡体の製造工程において、基材に澱粉
を練り込み、発泡させ、気泡膜及び/又は骨格に澱粉の
粒子を混合させることにより、培地としてバクテリア菌
を増殖させると共に通水性に優れ、例えば、浄化槽の担
体として使用する場合、浄化作用を促進し、バクテリア
の担体として好適である。
As described above, according to the present invention, in the process of producing a crosslinked polyolefin open cell, starch is kneaded into a substrate, foamed, and starch particles are mixed into a cell membrane and / or skeleton. Thereby, bacteria can be propagated as a medium and excellent in water permeability. For example, when used as a carrier for a septic tank, the purification action is promoted, and the medium is suitable as a carrier for bacteria.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C08L 3:00) Fターム(参考) 4D003 EA14 EA19 EA21 EA30 EA38 FA02 4F074 AA03 AA10 AA16 AA17 AA18 AA19 AA20 AA22 AA23 AA25 BA13 BA15 BA16 BA17 BA18 BA19 BB02 CA30 CC06Y CC32X CC32Y CC34X CC42 CD01 CD11 DA13 DA32 DA57 DA59 4J002 AB04X AC04W BB03W BB05W BB06W BB07W BB15W BB24W EK036 EK066 EN047 EQ017 EQ027 ES007 EV267 EV287 FA09W FD146 FD327 GT00──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C08L 3:00) F-term (Reference) 4D003 EA14 EA19 EA21 EA30 EA38 FA02 4F074 AA03 AA10 AA16 AA17 AA18 AA19 AA20 AA22 AA23 AA25 BA13 BA15 BA16 BA17 BA18 BA19 BB02 CA30 CC06Y CC32X CC32Y CC34X CC42 CD01 CD11 DA13 DA32.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 気泡の膜及び/又は骨格に澱粉粒子を含
有することを特徴とする澱粉入り架橋ポリオレフィン連
続気泡体。
1. A starch-containing cross-linked polyolefin open cell comprising starch particles in a cell membrane and / or skeleton.
【請求項2】 ポリオレフィン100重量部に対し、澱
粉10〜100重量部を含有する請求項1記載の架橋ポ
リオレフィン連続気泡体。
2. The crosslinked polyolefin open cell according to claim 1, which contains 10 to 100 parts by weight of starch based on 100 parts by weight of polyolefin.
【請求項3】 ポリオレフィンに発泡剤及び架橋剤を添
加した発泡性架橋性組成物を気密でない金型中で加熱発
泡させて気泡体を生成させ、次いで機械的変形を加えて
気泡を連通化させる連続気泡体の製造方法において、ポ
リオレフィンに澱粉を添加、混練りして発泡させること
を特徴とする澱粉入り架橋ポリオレフィン連続気泡体の
製造方法。
3. A foamable crosslinkable composition obtained by adding a foaming agent and a crosslinking agent to polyolefin is heated and foamed in a non-hermetic mold to form a foam, and then mechanically deforms the foam to make it open. A method for producing an open-cell, crosslinked polyolefin containing starch, comprising adding starch to a polyolefin, kneading the mixture, and foaming.
【請求項4】 ポリオレフィン100重量部中に澱粉1
0〜100重量部を添加することを特徴とする請求項1
記載の製造方法。
4. Starch per 100 parts by weight of polyolefin
2. The composition according to claim 1, wherein 0 to 100 parts by weight are added.
The manufacturing method as described.
JP11171447A 1999-05-13 1999-05-13 Starch-filled crosslinked polyolefin open-cell foam and its production Pending JP2000319457A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11171447A JP2000319457A (en) 1999-05-13 1999-05-13 Starch-filled crosslinked polyolefin open-cell foam and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11171447A JP2000319457A (en) 1999-05-13 1999-05-13 Starch-filled crosslinked polyolefin open-cell foam and its production

Publications (1)

Publication Number Publication Date
JP2000319457A true JP2000319457A (en) 2000-11-21

Family

ID=15923288

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2000319457A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009066592A (en) * 2007-08-23 2009-04-02 Nisshinbo Ind Inc Carrier for treating fluid and method for manufacturing the same
US7604745B2 (en) 2004-02-06 2009-10-20 Takachiho Corp. Water-purifying solid material made of a natural raw material containing polysaccharides as principal components, and water-purifying method using the same
JP2013202512A (en) * 2012-03-28 2013-10-07 Cci Corp Method of treating oil-and-fat- or fatty acid-containing waste water
CN110563128A (en) * 2019-09-03 2019-12-13 江西夏氏春秋环境股份有限公司 MBBR (moving bed biofilm reactor) sewage treatment filler and using method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7604745B2 (en) 2004-02-06 2009-10-20 Takachiho Corp. Water-purifying solid material made of a natural raw material containing polysaccharides as principal components, and water-purifying method using the same
JP2009066592A (en) * 2007-08-23 2009-04-02 Nisshinbo Ind Inc Carrier for treating fluid and method for manufacturing the same
JP2015016473A (en) * 2007-08-23 2015-01-29 日清紡ホールディングス株式会社 Carrier for treating fluid
JP2013202512A (en) * 2012-03-28 2013-10-07 Cci Corp Method of treating oil-and-fat- or fatty acid-containing waste water
CN110563128A (en) * 2019-09-03 2019-12-13 江西夏氏春秋环境股份有限公司 MBBR (moving bed biofilm reactor) sewage treatment filler and using method thereof

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