JPS58111837A - Non-crosslinked high-density polyethylene pre-expanded particle and preparation of same - Google Patents

Non-crosslinked high-density polyethylene pre-expanded particle and preparation of same

Info

Publication number
JPS58111837A
JPS58111837A JP56215166A JP21516681A JPS58111837A JP S58111837 A JPS58111837 A JP S58111837A JP 56215166 A JP56215166 A JP 56215166A JP 21516681 A JP21516681 A JP 21516681A JP S58111837 A JPS58111837 A JP S58111837A
Authority
JP
Japan
Prior art keywords
softening point
vicat softening
particles
crosslinked high
component
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
JP56215166A
Other languages
Japanese (ja)
Other versions
JPS6010048B2 (en
Inventor
Shohei Yoshimura
吉村 正平
Hideki Kuwabara
英樹 桑原
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.)
JSP Corp
Original Assignee
JSP 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 JSP Corp filed Critical JSP Corp
Priority to JP56215166A priority Critical patent/JPS6010048B2/en
Publication of JPS58111837A publication Critical patent/JPS58111837A/en
Publication of JPS6010048B2 publication Critical patent/JPS6010048B2/en
Expired legal-status Critical Current

Links

Abstract

PURPOSE:To prepare the titled pre-expanded particle with excellent weatherability, thermal resistance, tensile strength, etc., by dispersing in a dispersing medium a specified non-crosslinked high-density PE particle impregnated with a volatile foaming agent, and releasing the dispersion from a high-temp. high- press. atmosphere to a low-press. atomsphere. CONSTITUTION:100pts.wt. non-crosslinked high-density PE particle (A), Vicat softening point >=115 deg.C and density of 0.950-0.968g/cm<2>, 5-40pts.wt. volatile foaming agent (B) (e.g., dichlorodifluoromethane), 0.01-10pts.wt. dispersant (C) (e.g., particulate Al2O3), and dispersing medium (D) (e.g., water) are charged in a closed vessel, which is heated at temp. in a range from 10 deg.C lower than the Vicat softening point of component A to 10 deg.C higher than the m.p. of component A, and component A is impregnated with component B while components A, B and C are dispersed in component D. Then the mixt. is released into a low- press. atmosphere by opening one end of the vessel, yielding a non-crosslinked high-density PE pre-poamed particle, bulk density of 0.01-0.3g/cm<3>, average cell diameter of 20-500mu and closed cell content >=65%.

Description

【発明の詳細な説明】 本発明紘無架橋高1!度ポリエチレン予備−fIIA′
IIj1子およびその製法に関する。
[Detailed description of the invention] The present invention has no crosslinking height 1! degree polyethylene reserve-fIIA'
This invention relates to IIj1 child and its manufacturing method.

従来よシポリエチレン樹脂発泡威渥体を得る方法として
予備発泡粒子を用いる所剛ビーズ成lI法が行なわれて
いる。しかしながら、そC−に用いる予備発泡粒子が架
橋していない場合に妹、高発電の威瀝体が得られ難く、
またj!履体O収all著しく大きい丸め実用に至って
いない。そ〇九めii*架橋し丸予備発泡粒子を用いて
発池成■体を得ているのであるが、架橋工程が必要でh
り、i丸それに用いる薬品、エネルギーも消費し、さも
に紘再刹用し難いことから無架橋の予備尭M111子を
用いる威m法OII俺が待望されている。
Conventionally, a rigid bead forming method using pre-expanded particles has been used as a method for obtaining a foamed polyethylene resin body. However, if the pre-expanded particles used in SoC are not cross-linked, it is difficult to obtain a powerful body with high power generation.
Again j! The shoe body has a significantly large rounding capacity and has not yet been put to practical use. Soni II * Bridge bridge and circle preliminary foam particles.
However, since it consumes chemicals and energy and is difficult to reuse, a method using uncrosslinked preliminary M111 has been eagerly awaited.

本発明は無架橋高蜜度ポリエチレン予備発池曽子および
その製法を提供する仁とを目的とするものでありて1本
発明考らは上記の点について鋭意研究し九結果、耐候性
、耐熱性、引裂強度、耐履自疲労性、耐圧縮性、瀝内威
麿性等が優れえ無架橋高書度ポリエチレン予備発泡粒子
およびその製法の一発に成功し本発明を完成するに至−
)大。
The purpose of the present invention is to provide a non-crosslinked high-density polyethylene pre-fired foam and a method for producing the same. We succeeded in developing non-crosslinked high-strength polyethylene pre-foamed particles with excellent properties such as durability, tear strength, self-fatigue resistance, compression resistance, and internal strength properties, as well as a process for producing the same, leading to the completion of the present invention.
)Big.

すなわち1本発*a、ビカット軟化点115℃以上=0
.9SOj/−を超える豐°度の無架橋高密度ポリエチ
レンよ)11嵩11度0.01−0.31/al。
That is, one shot *a, Vicat softening point 115℃ or higher = 0
.. Non-crosslinked high-density polyethylene with a temperature exceeding 9 SOj/-) 11 bulk 11 degrees 0.01-0.31/al.

平均気111@20 s 〜S OOμ+ lk立気泡
率65優以上であることを畳黴とする無架橋高蜜度ポリ
エチレン予備発―粒子を要旨とする。本発努のいま一つ
O畳旨紘ビカット軟化点115℃以上、0.950II
/−を超える*度O無架橋高書度ポリエチレン軸子に揮
発性発泡剤を含有させる工II、 1111器内で前1
6g子を分散mに分散させる工程、および冑W1411
器内01111!を粒子のビカット軟化点よシ10℃低
い温度から融点よ〉10℃高い温度の範■に保持しなが
ら容器の一端を開放し、前記粒子と分tm、=t″l″
IIIKmFIIn ! DffiBl)$111!L
TKlttlする工程よnすることを特徴とする無架橋
高書度ポリエチレン予備発池糠子の製法に&る。
The gist is non-crosslinked, high-density polyethylene preformed particles having an average air density of 111 @ 20 s to S OOμ+ lk and a bubble rate of 65 or more. Honsha Tsutomu's one-of-a-kind Otatami Uhiro Vicat Softening point 115℃ or higher, 0.950II
Incorporating a volatile blowing agent into a non-crosslinked high-texture polyethylene shaft with a degree of O exceeding /- II, in a 1111 vessel
A process of dispersing 6 g particles into dispersion m, and a helmet W1411
Vessel 01111! One end of the container is opened while maintaining the temperature between 10°C below the Vicat softening point of the particles and 10°C above the melting point, and the particles are separated by tm,=t″l″.
IIIKmFIIn! DffiBl) $111! L
The present invention relates to a method for producing pre-fired bran bran of non-crosslinked high-texture polyethylene, which is characterized by a step of TKlttl.

本発−に用いられる基質樹脂嬬ビカット軟化点115℃
以上、0.950j/atを超える冑度の無架橋高書度
ポリエチレン(以下、無架橋HDP璽という)である。
Substrate resin used in this invention Vicat softening point 115℃
The above is a non-crosslinked high-texture polyethylene (hereinafter referred to as non-crosslinked HDP) with a strength exceeding 0.950 j/at.

ビカット軟化点が1115’c未濃て紘渥内成型性が愚
<、lIられる威朦品の物性が劣悪と1に多好ましくな
い。を九書度がo、* s o I/d以下で紘、予備
発泡が困難と康る。ビカット軟化点04Iに好ましい範
i!141118℃以上であ〉9m度の41KtFft
 Lい範囲はO,il 50−0.96 II I /
 dである。
The Vicat softening point is 1115'c, the internal moldability is poor, and the physical properties of the prestigious product are poor. If the degree is less than 0, *s o I/d, pre-foaming will be difficult. Preferred range i for Vicat softening point 04I! 41KtFft of 〉9m degree above 141118℃
L range is O,il 50-0.96 II I/
It is d.

本発明の無架橋HDPKは1例えば過電の低圧銖によp
得ることができ、ペレット化球状粒子化0過穆で酸化防
止剤、紫外lII歌収剤等の添加剤を含有させ九屯ので
あってもよい。
The non-crosslinked HDPK of the present invention is
It can be made into pelletized spherical particles with 0% filtration and may contain additives such as antioxidants and ultraviolet 1I absorbers.

本発IjlIに用いられる揮発111iIlll剤とし
て紘1例エバフロパン、ブタン、ペンタン、ヘキナン、
ヘプタン等で例示される脂肪族炭化水奏鎖、シクロブタ
ン、V/I2ペンタン等で例示される票式脂肺族炭化水
素類お□よびトリクロロ7μロメタン、ジタロロジ70
ロメタン、ジタνロテトツ7−ロエタン、メチルクロラ
イド、エチルク四ライド、メチレンフレライド等で例示
されるハロゲン化炭化水嵩類が使用1れる。この!i池
泡剤添加量は皺発泡剤0m1llおよび断値する発泡の
1度によって異なるが通常5〜40重量部である。
Examples of volatile 111iIll agents used in the present invention include evafuropane, butane, pentane, hequinane,
Aliphatic hydrocarbon groups such as heptane, cyclobutane, V/I2 pentane, etc., and trichloro7μlomethane, Ditarology 70
Halogenated hydrocarbons exemplified by lomethane, di-7-loethane, methyl chloride, ethyl tetralide, methylene fulleride and the like are used. this! The amount of foaming agent added varies depending on the amount of wrinkle foaming agent (0 ml, 1 liter) and the degree of foaming, but is usually 5 to 40 parts by weight.

本発#0無架橋HDPE予備発泡粒子の製法において、
無架橋HDPI@子Klf発性発泡剤を含有させるが、
この時期は41IIIIciIN定されず、tJ6HD
PK誼子に発泡剤を含有させておき、この発泡剤を含有
したHDI’l*子を書間容器内に入れて該一閉容器内
で分散flaK分散させてもよく、或いはHDPE翰子
と発泡剤を冑閉春器内に入れて鋏書間春器内でそれらを
分散1/I&に分散させつつHDPΣ粒子に発、泡剤を
含有させてもよい。を丸管閉容器内で前記粒子を所定温
度に:al11mlする過l!において発泡剤を1閉容
器内に入れて前記粒子と発泡剤を分散させつつ前記粒子
に発泡剤を含有させてもよい。肯。
In the method for producing #0 non-crosslinked HDPE pre-expanded particles of the present invention,
Contains non-crosslinked HDPI @ child Klf foaming agent,
At this time, 41IIIciIN was not determined, and tJ6HD
A foaming agent may be contained in the PK yoshi, and the HDI'l* child containing this foaming agent may be placed in a container and dispersed in the closed container, or alternatively, the HDPE yoshi and the foaming agent may be dispersed in the closed container. The foaming agent may be added to the HDPΣ particles while dispersing the agent in the scissor spring container at a dispersion ratio of 1/I& in the scissor spring container. The particles were brought to a predetermined temperature in a closed round tube container with 11 ml of aliquot. The foaming agent may be contained in the particles while the foaming agent is placed in a closed container and the particles and the foaming agent are dispersed. Yes.

前記粒子に発泡剤を含有させるときの温度も任意で&)
、41に議定されない。
The temperature at which the foaming agent is contained in the particles is also optional.
, 41.

本発明方法では、HDPI誼子と揮発性発泡剤を別々に
或いは揮発性発泡剤をHDPK粒子に含有させた後分散
厳に分散させるが、このとき畳すれば分散剤2例えば黴
較状の酸化アルミニウム訃よび酸化チタ・ン、塩基性脚
酸iダネシウム、塩基性炭酸亜鉛、炭酸カルシウム等を
用いることかで1する。
In the method of the present invention, HDPI particles and a volatile blowing agent are mixed separately or after the volatile blowing agent is incorporated into HDPK particles and then thoroughly dispersed. This can be achieved by using oxidized titanium oxide, basic danesium legate, basic zinc carbonate, calcium carbonate, etc.

この分散剤の添加量は通常HDPK粒子1粒子1貴0 粒子を分散するに轟って,融点21C以上,HLI値1
〜100有機化合物1例えばステアリン酸アミド等を5
重量部以下添加することもできる。重九分散媒はHDP
I粒子を溶解させない11媒であればよく1例えば、水
,エチレングリコール、グリセリン、メタノール、エタ
ノール等のうちの1種又はそれらの2種以上の梶金物が
例示されるが。
The amount of this dispersant added is usually enough to disperse 1 HDPK particle, 1 particle, 10 particles, a melting point of 21C or higher, and an HLI value of 1.
~100 organic compound 1 such as stearic acid amide etc. 5
It can also be added in an amount of less than part by weight. Heavy nine dispersion medium is HDP
Any medium may be used as long as it does not dissolve the particles.For example, one or more of water, ethylene glycol, glycerin, methanol, ethanol, etc. may be used.

通常は水が好ましい。Water is usually preferred.

本発明の予備発泡方法で嬬,容器〇一端を1款してHD
PKf11子と分散媒とを同時に容器内よ)も低圧の1
1As気下に放出するが,このときO11度紘HDPΣ
粒子のビカット軟化点よ311G℃低い温度からビカッ
ト軟化点よ)10℃高い温度011−である。ビカット
軟化点よJlloを低い温度未満で紘ハとんど発電せず
、ビカット軟化点よJ)10℃高い温度を′超える場合
IIc紘独立気泡率が著しく減少し、連泡と′1k〉機
械的強度が低下する。こO発泡温度の特に好ましい範−
はビカット軟化点よシ5℃低い温度からビカット軟化点
よ〉8℃高い温度である。を九このと會O圧力は揮発性
発泡剤の蒸気圧以上を丸状以下のいずれでもよく、放出
す−る雰園気轄通當常圧の雰囲気が選ばれる。
Using the pre-foaming method of the present invention, one end of the container is heated and hardened.
PKf11 and the dispersion medium are placed in the container at the same time) at low pressure.
1As is released into the atmosphere, but at this time O11 degree HiroHDPΣ
The temperature ranges from 311 G°C lower than the Vicat softening point of the particles to 011-10°C higher than the Vicat softening point. When the temperature is lower than the Vicat softening point Jllo, HIRO hardly generates electricity, and when the temperature exceeds the VICAT softening point J) 10℃ higher, the closed cell ratio decreases markedly, and the open cell and '1k> machines target strength decreases. Particularly preferred range of foaming temperature
The temperature ranges from 5°C lower than the Vicat softening point to 8°C higher than the Vicat softening point. In this case, the pressure may be greater than or equal to the vapor pressure of the volatile blowing agent and less than or equal to the vapor pressure of the volatile blowing agent, and the atmosphere in which the blowing agent is discharged is selected to be at normal pressure.

上記の如き方法によ多得られる本発明の予備発泡粒子は
、貴書* 0.01−0.311/al、独立気泡率6
s憾以上、平均気泡径20〜500μである。
The pre-expanded particles of the present invention obtained by the above-described method have a ratio of 0.01 to 0.311/al and a closed cell ratio of 6.
The average bubble diameter is 20 to 500μ.

嵩冑度が0.01j/−未満で紘予備発#lI粒子の形
状が歪に1G易<、1九O,3,9/−を超える場冶に
は粒子の形状が歪にte易いはか)でなく、a池状簡が
不均一になる。嵩一度のIl/IK好ましい範m線GG
15−0.15j/jである。独立気泡率が45596
未濃の鳩舎に社1発泡、―・・子が歪Keel易<、1
え圧縮弾性が低下する。独立気泡率041に好ましい範
−は75饅以上である。平均気msが20声未満の場舎
に紘発池較子の形状が歪11゜機械的強度が低下し、を
九sOOμを超える鳩舎には、11内威瀝性に劣J)j
llL好な成層体が得られ難く、仮に成層体が得られ友
としてもIN両が硬く目凸の暮しいものとなる。平均気
泡11041に好ましい範囲は50〜400μである。
When the bulkiness is less than 0.01J/-, the shape of the particle is easily distorted by 1G<, and when the bulkiness exceeds 19O,3,9/-, the shape of the particle is easily distorted. (a), but the shape of the strips becomes uneven. Bulk Il/IK preferred range m line GG
15-0.15j/j. Closed cell ratio is 45596
The company 1 foam in the pigeon house of Mino, -... the child is distorted Keel easy <, 1
The compressive elasticity decreases. A preferable range for the closed cell ratio of 041 is 75 or more. If the average air ms is less than 20 voices, the shape of the pigeon house will be distorted by 11 degrees, and the mechanical strength will be reduced, and if the average air ms is more than 9 secondsOOμ, the internal strength will be poor.
It is difficult to obtain a good laminated body, and even if a laminated body is obtained, the IN and IN sides are hard and convex and dull. The preferred range for the average bubble size 11041 is 50 to 400μ.

tえ予備発泡粒子の粒径は特に限定されないが流動性の
点から&5〜20mmが好ましい。
The particle size of the pre-expanded particles is not particularly limited, but is preferably from 5 to 20 mm from the viewpoint of fluidity.

上記の如き本発明の予備発泡粒子は2通常、常温常圧下
所定時間熟成され1次いで必要に応じて無機ガスまえは
無機ガスと揮発性発泡剤との議会ガスによ)所定圧力、
所定時間加圧熟成される。
The pre-expanded particles of the present invention as described above are usually aged for a predetermined period of time at room temperature and normal pressure.(1) Then, if necessary, an inorganic gas (prepared with an inorganic gas and a volatile blowing agent) is used at a predetermined pressure.
Matured under pressure for a predetermined period of time.

上記の如く内圧を付与され九予備発m粒子は金層に充填
され1通常水蒸気圧1.2〜L S Ill/aj(G
)で加熱発泡されて蓋過〉O発池威蓋体が得られる。
The nine pre-generated particles are filled into the gold layer with the internal pressure applied as described above, and the normal water vapor pressure is 1.2 to L S Ill/aj (G
) to obtain a foamed lid body.

上記の如く得られる発池威履体は例えば包lI材。The Hatsuikei shoe body obtained as described above is, for example, a Bao II material.

緩衝質、断熱賛11食品容器、浮111N等に用いるこ
とができる。
Can be used for buffer materials, heat-insulating food containers, floating 111N, etc.

以上説明したように1本発−の予備li池輸子紘耐候性
、耐熱性、引裂強度、耐層−痕労性、Im圧縮弾性、I
l内成瀾性等が優れて&J)、この予備発泡粒子を用い
て得られる発池威濡体紘上記O如き優れ良性質を有する
良好表ものである。を九本発@によれば、無架橋HDP
I @子から優れ良性質を有する予備発泡粒子を得るこ
とができ、架橋工程が不要となることによ)工IiO簡
略化を図ることができると共にそれKfFなうエネルギ
ー、薬品等を消費しなくて済むためコストも安くできる
ものであり、さらには無架橋な丸め再利用も可能である
等種々011点を有するものである。
As explained above, the preliminary lithium-ion weather resistance, heat resistance, tear strength, layer-imprint resistance, Im compressive elasticity, I
The foamed particles obtained using these pre-expanded particles have excellent properties such as the above-mentioned properties. According to Kuhonshu@, non-crosslinked HDP
It is possible to obtain pre-expanded particles with excellent properties from I@, and by eliminating the need for a cross-linking process, it is possible to simplify the process (IiO), and it does not consume energy, chemicals, etc. It has various advantages, such as being able to reduce costs because it requires only a few steps, and furthermore, it can be rolled up and reused without crosslinking.

以下、II施例および比較例を掃けて本発明をさらに詳
Stに説明する。
Hereinafter, the present invention will be explained in more detail by referring to Example II and Comparative Examples.

実施例1〜!sI−よび比較例1〜9 all真に示され丸管度、ビカット軟化点および融点を
有する無架橋HDPE@子100重置部、ジダーロ′シ
フ0ロメタン25重量部、微粒状酸化アル建ニウムO9
s重量部、水300重量部をオートタレーブ内に入れ、
攪拌下昇議して容器内の温度を会O〜l110℃、圧力
を20〜s 6kf/j(G) K保持し&がも審II
〇一端な−放し一大気下に放出して発亀させて第1貴に
示す穏々O予備発泡粒子を得え。を友比較例として低書
度ポリエチレン(以下LDPKという)、架橋LDPK
 、本発明範囲外O無架橋HDPEを用いて実施例と同
様に行なって第1表に併せて示す予備発泡粒子をlIえ
Example 1~! sI- and Comparative Examples 1 to 9 All true roundness, Vicat softening point and melting point 100 parts of non-crosslinked HDPE, 25 parts by weight of Gidaro' Schiffromethane, fine granular aluminum oxide O9
Put s parts by weight and 300 parts by weight of water into the autotaleve,
While stirring, raise the temperature in the container to 110°C, and keep the pressure at 20 to 6 kf/j (G) K.
〇 Firstly, release it under the atmosphere and cause it to foam to obtain the gently O pre-expanded particles shown in the first example. As a comparative example, low density polyethylene (hereinafter referred to as LDPK), cross-linked LDPK
Pre-expanded particles shown in Table 1 were prepared in the same manner as in the examples using non-crosslinked HDPE which is outside the scope of the present invention.

得られ良予備発泡粒子を常温、常圧下41時開放置した
後、 ll1Fl嚇器内に充填しz s k#/−(G
)−35℃の空気にて48時間加圧熟熟成え。次いで予
備発泡粒子を金mに充填し、各貴重のビカット軟化点以
上OSmで1. z 〜s、 s k#/ai (Q)
0水蒸気で加熱威濡し1発池威濡体を得え。予備発泡粒
子および得られ九a池成層体について種々の物性試験を
行なりえ。結果を第!IIIK示す。肯、平均気泡価O
掬定は切断−を電子顕微鏡にてI!察することによル行
なりえ。
The obtained pre-expanded particles were left open for 41 hours at room temperature and pressure, and then filled into a ll1Fl intimidator and zs k#/-(G
) Matured under pressure for 48 hours in air at -35°C. The pre-expanded particles are then filled into the gold m and each precious metal has an OSm above the Vicat softening point of 1. z ~s, s k#/ai (Q)
Heating it with 0 water vapor will give you a powerful body in one shot. Various physical property tests were conducted on the pre-expanded particles and the resulting Kuaike stratified body. Results first! IIIK shown. Yes, average bubble value O
Scooping is cutting using an electron microscope! Act by observing.

第 2 表 @1−−−− ’l工f*)−fi−f2 G 04間
処理し、111子O着色、変形1弾力!10変化で判定
しえ。
Table 2 @1 ---- 'l engineering f *) - fi - f2 G Processed for 04, 111 coloring, deformation 1 elasticity! Judge by 10 changes.

◎−着色、変形殆んどなく弾力性あシ 0−−−−−着色、変形が若干■められるが弾力性あり 八−一着色、変形が認められ1弾力性低下×−−−着色
、変形が着しく認められ2弾力性低下大 ※2−ギヤーオーブン中、ioo℃、1000時間畿の
着色、変形2弾力性の変化で判定しえ。
◎ - Almost no coloring or deformation, elasticity 0 ---- Coloring, some deformation ■ - Elasticity 8-1 Coloring, deformation observed, 1 elasticity decrease x---- Coloring, Severe deformation was observed and 2. Significant decrease in elasticity *2 - In a gear oven at 1000 hrs.

Q7−−−着色、変形1弾力性の変化殆んどなし O・−着色、変形が若干認められるが弾力性あシ Δ−−−着色、変形が認められ弾力性も低下×−−着色
、変形が著しく認められ弾力性低下大 秦3− JIB 811sK準じテall定シエ。
Q7 --- Coloring, deformation 1 Almost no change in elasticity O - Coloring, some deformation is observed, but elasticity Δ --- Coloring, deformation is observed, and elasticity decreases × --- Coloring, Significant deformation was observed and the elasticity decreased.

0−11 Oal1以上破漸破断い o −s o o −s o o 6未満で破断Δ−−
100〜SOO回未満で破断 X−100g未満で破断 ※4−− JIB K@7@7に準じて判定した。
0-11 Oal 1 or more fractures o -s o o -s o o Fractures at less than 6 Δ--
Fractured at less than 100 to SOO times

Q−7kl/10■幅を超えるもの Q−−3に#/10■−を超える7kIi/16■躯Δ
−−−1に5P/10−一を超える31I#/10■幅
X−−1ゆ/10■@以下 豪5−−−テンシロンを用いて10m/−の適度で最大
応力4klI/−まて圧縮し応力除去後の員貿歪からの
弾性闘復皐で楯定した。
Q-7kl/10■ Width exceeding Q--3 #/10■- 7kIi/16■ Body Δ
---1 to 5P/10-31I#/10 ■Width X--1 Yu/10■@ less than Australia 5---Using Tensilon, the maximum stress is 4klI/- at a moderate distance of 10m/-. After compression and stress removal, elastic recovery from strain was established.

Q −−−−−−955に以上目量 ○−−−85〜95憾未満−復 △−75〜85s未濃回復 X −−75慢未満 秦6−−−下記O規卑で判定しえ。Q ------Graduation of 955 or more ○---85 to less than 95 - recovery △-75~85s unconcentrated recovery X -- less than 75 arrogant Qin 6 --- Judge according to the following O criteria.

〇−成m*好 0−・−威騰畳通 Δ−−−− *蓋不JIILtK千発生×−一成墓不嵐〇-Narm*Good 0-・-Weiten Tatami Street Δ−−−− *Full of cover JIILtK thousand occurrences

Claims (2)

【特許請求の範囲】[Claims] (1)  ビカット軟化点115℃以上、O59601
1/dを超える1度の無架橋高!Ifポリエチレンより
tb、嵩*度o)ox〜0.311/aJ、平均気泡径
20μ〜500711.lII立気泡率6516以上で
あることを4111とする無架橋高11&ポリエチレン
予備俺池粒子。
(1) Vicat softening point 115℃ or higher, O59601
Unbridged height exceeding 1/d! If tb from polyethylene, bulk * degree o) ox ~ 0.311/aJ, average cell diameter 20μ ~ 500711. lII Non-crosslinked high 11 & polyethylene preliminary Oreike particles with 4111 having a bubble rate of 6516 or more.
(2)  ビカット軟化点115℃以上、 o、e s
 o g7aiを超える書度の無架橋高冑度ポリエチレ
ン粒子に揮発性発泡剤を含有させる工程、密閉容器内で
前記粒子を分散mに分散させる1婁、および一閉春器内
の温度を粒子のビカット軟化点より10℃低いi**か
らビカット軟化点より10℃高い**0範−内に保持し
ながら容器〇一端を−放し、曽起粒子と分散謀とを同時
に容器内よ)低圧Ot−気下に放出する工程よpなる仁
とをll1Ikとする無架橋高IItポリエチレン予備
弛泡粒子OII法。
(2) Vicat softening point 115℃ or higher, o, e s
A step of incorporating a volatile blowing agent into non-crosslinked high-strength polyethylene particles with a size exceeding 7.o g. While maintaining the temperature within the range from i** 10°C lower than the Vicat softening point to 10°C higher than the Vicat softening point, one end of the container is released and the originating particles and dispersion plot are simultaneously placed inside the container) at low pressure. Ot- Non-crosslinked high IIt polyethylene pre-expanded particle OII method in which the step of releasing into the atmosphere and the p layer are ll1Ik.
JP56215166A 1981-12-25 1981-12-25 Non-crosslinked high-density polyethylene pre-expanded particles and method for producing the same Expired JPS6010048B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56215166A JPS6010048B2 (en) 1981-12-25 1981-12-25 Non-crosslinked high-density polyethylene pre-expanded particles and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56215166A JPS6010048B2 (en) 1981-12-25 1981-12-25 Non-crosslinked high-density polyethylene pre-expanded particles and method for producing the same

Publications (2)

Publication Number Publication Date
JPS58111837A true JPS58111837A (en) 1983-07-04
JPS6010048B2 JPS6010048B2 (en) 1985-03-14

Family

ID=16667743

Family Applications (1)

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

Country Link
JP (1) JPS6010048B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6215239A (en) * 1985-07-12 1987-01-23 Kanegafuchi Chem Ind Co Ltd Uncrosslinked straight chain low-density polyethylene preexpanded partifle and molding thereof
US4644013A (en) * 1983-04-08 1987-02-17 Asahi Kasei Kogyo Kabushiki Kaisha Preparation of foam particles of ethylenic resin and foam moldings prepared therefrom

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4644013A (en) * 1983-04-08 1987-02-17 Asahi Kasei Kogyo Kabushiki Kaisha Preparation of foam particles of ethylenic resin and foam moldings prepared therefrom
JPS6215239A (en) * 1985-07-12 1987-01-23 Kanegafuchi Chem Ind Co Ltd Uncrosslinked straight chain low-density polyethylene preexpanded partifle and molding thereof

Also Published As

Publication number Publication date
JPS6010048B2 (en) 1985-03-14

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