JPS6042433A - Expanded synthetic resin in-mold molding and its production - Google Patents

Expanded synthetic resin in-mold molding and its production

Info

Publication number
JPS6042433A
JPS6042433A JP58149299A JP14929983A JPS6042433A JP S6042433 A JPS6042433 A JP S6042433A JP 58149299 A JP58149299 A JP 58149299A JP 14929983 A JP14929983 A JP 14929983A JP S6042433 A JPS6042433 A JP S6042433A
Authority
JP
Japan
Prior art keywords
expanded particles
particles
molding
expansion force
synthetic resin
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
JP58149299A
Other languages
Japanese (ja)
Other versions
JPH0414058B2 (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 JP58149299A priority Critical patent/JPS6042433A/en
Publication of JPS6042433A publication Critical patent/JPS6042433A/en
Publication of JPH0414058B2 publication Critical patent/JPH0414058B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Molding Of Porous Articles (AREA)

Abstract

PURPOSE:To produce the titled molding in which expanded particles constituting the surface layer have a specified flattened shape, by filling surface layer portions with pre- expanded particles having a heat expansion force smaller than that of the pre-expanded particles in the inner layer portion and heat-molding the whole. CONSTITUTION:A molding die 7 is protioned into three compartments by diaphragms 6, 6, and molding chambers 9, 9 are filled with pre-expanded particles 13, 13 having a heat expansion force Ps (kg/cm<2>.abs) satisfying the relationship: Pi/Ps>1.5 (wherein Pi (kg/cm<2>.abs) is the heat expansion force of the pre-expanded particles with which molding chamber 10 is filled). After removing the diaphragms 6, 6, the whole system is heated. By the expansion of the pre-expanded particles of the pre-expanded particles 12 in the inner portion, the pre-expanded particles 13, 13 having a smaller heat expansion force in the surface layre portion are pressed and expand flatly to form a molding in which the ratio, Lf/Ld, is larger than 3.5, wherein Lf(mm.) is the average diameter along the face and Ld(mm.) is the average diameter along the thickness. This molding has a smooth surface, so that when used as a core material, it shows excellent adhesion to a covering material and forms a product of good appearance particularly in the case of a thin covering material.

Description

【発明の詳細な説明】 本発明は合成樹脂予備発泡粒子を成型用型に充填し加熱
成型して得られる合成樹脂発泡粒子屋内成型体およびそ
の製造方法に関し、更に詳しくは。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an indoor molded article of foamed synthetic resin particles obtained by filling a mold with pre-expanded synthetic resin particles and heating and molding the same, and a method for producing the same.

成型体の表面層を構成する発泡粒子が特定の偏平形状を
有する合成樹脂発泡粒子屋内成型体およびその製造方法
に関する。
The present invention relates to an indoor molded product of synthetic resin foam particles in which the foamed particles constituting the surface layer of the molded product have a specific flat shape, and a method for producing the same.

近年、テーブル、コタツ板等の家具類の芯材。In recent years, it has been used as core material for furniture such as tables and kotatsu boards.

畳用芯材、風呂釜用断熱材、すのこ板、痣築用内装材等
の構築部材、あるいは自動車用部材等として合成樹脂発
泡体が広く用いられており、これら発泡体の製造方法と
しては予備発泡粒子を成型用型に充填して加熱成型する
。いわゆるビーズ成型法が知られている。しかしながら
従来のビーズ成型法によシ得られる発泡成型体は、該成
型体を構成する発泡粒子が、成型体表面層に位置する発
泡粒子および内面層に位置する発泡粒子ともに、全て球
形に近いほぼ同一形状を有するため、成型体全体として
の衝撃吸収性は有するものの表面層の剛性に劣る欠点が
あった。しかも成型体表面層の発泡粒子が球形に近い形
状を有するため、成型体表面の平滑性に乏しく、該成型
体を芯材として用いた場合に成核材との接合性が低下し
、特に壁紙等の如く薄い成核材を成型体表面に設けた場
合には、該成核材表面に成型体表面の凹凸が顕著に現わ
れ、著るしい外観低下をきたす等の欠点があった。
Synthetic resin foams are widely used as construction materials such as core materials for tatami mats, insulation materials for bathtubs, slatted boards, interior materials for scar removal, and automobile parts, and there are no preliminary methods for manufacturing these foams. The expanded particles are filled into a mold and heated and molded. A so-called bead molding method is known. However, in the foamed molded product obtained by the conventional bead molding method, the foamed particles constituting the molded product are all approximately spherical, including the foamed particles located in the surface layer of the molded product and the foamed particles located in the inner layer. Since they have the same shape, although the molded body as a whole has shock absorbing properties, the surface layer has a disadvantage of poor rigidity. Moreover, since the foamed particles in the surface layer of the molded product have a nearly spherical shape, the surface of the molded product has poor smoothness, and when the molded product is used as a core material, the bondability with the nucleating material decreases, especially for wallpaper. When a thin nucleating material such as nucleating material is provided on the surface of a molded product, there are drawbacks such as noticeable irregularities on the surface of the molded product, resulting in a significant deterioration in appearance.

本発明者らは上記欠点を解消すべく鋭意研究した結果、
成型体表面部を構成する発泡粒子を特定の割合で偏平せ
しめた成型体が全体としての衝撃吸収性を有するととも
に表面剛性1表面平滑性に優れることを見い出すととも
にその製造方法を見い出し本発明を完成するに至った。
As a result of intensive research by the present inventors to eliminate the above drawbacks,
It was discovered that a molded product in which the foamed particles constituting the surface of the molded product were flattened at a specific ratio had overall shock absorbing properties and excellent surface rigidity and surface smoothness. They also discovered a method for producing the same and completed the present invention. I ended up doing it.

即ち本発明の要旨とするところの−っは9合成樹脂予備
発泡粒子を成型用型内で発泡成型して得られる合成樹脂
発泡粒子型内成型体において、該成型体の表面層を構成
する発泡粒子の、平面方向゛ の平均径Lf(mQと厚
さ方向の平均径Ld(*りとの比が、 Lf /Ld>
 3.5であることを特徴とする合成樹脂発泡粒子屋内
成型体にある。
That is, the gist of the present invention is to provide a synthetic resin foam particle in-mold molded product obtained by foam-molding 9 synthetic resin pre-expanded particles in a mold, in which the foam constituting the surface layer of the molded product is The ratio of the average diameter Lf (mQ) of the particles in the plane direction and the average diameter Ld (*) in the thickness direction is Lf /Ld>
There is an indoor molded article of foamed synthetic resin particles characterized in that the particle size is 3.5.

本発明の要旨とするところの他の一つは、成型用型の壁
面と接する表層部に、加熱膨張力Ps(kg/lri・
絶対圧)が、該表層部より内側の内層部に充填された予
備発泡粒子の加熱膨張力p+ (kg/−・絶対圧)に
対してPi / Ps > 1.’ 5なる関係を有す
る予備発泡粒子を充填し、加熱成型して表面層を構成す
る発泡粒子の平面方向の平均径Lf (mりと厚さ方向
の平均径Ld (mm)との比がLf /Ld > 3
.5である成型体を得ることを特徴とする合成樹脂発泡
粒子型内成型体の製造方法にある。
Another aspect of the present invention is that the heating expansion force Ps (kg/lri・
(absolute pressure) is Pi / Ps > 1. The average diameter Lf in the planar direction of the foamed particles that are filled with pre-expanded particles having a relationship of /Ld > 3
.. 5. A method for producing an in-mold molded article of foamed synthetic resin particles is provided.

本発明の合成樹脂発泡粒子型内成型体は、予備発泡粒子
を成型用型内で加熱成型するビーズ成型法によシ得られ
る。上記予備発泡粒子の基材樹脂としては、ポリエチレ
ン、ポリプロピレン、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、ポリスチレン、ポリエステルエラストマー、ポリ
アミドエラストマー、ポリウレタンエラストマー等が例
示されこれらは架橋、無架橋のいずれでもよいが。
The in-mold molded synthetic resin foam particles of the present invention are obtained by a bead molding method in which pre-expanded beads are heated and molded in a mold. The base resin of the pre-expanded particles includes polyethylene, polypropylene, ethylene-propylene copolymer,
Examples include ethylene-butene copolymer, ethylene-vinyl acetate copolymer, polystyrene, polyester elastomer, polyamide elastomer, polyurethane elastomer, etc., and these may be either crosslinked or non-crosslinked.

特に無架橋のエチレン−プロピレンランダム共重合体が
好ましい。
Particularly preferred is a non-crosslinked ethylene-propylene random copolymer.

上記予備発泡粒子は2例えば密閉容器内で樹脂粒子を発
泡剤とともに分散媒に分散させ、所定温度に加熱した後
、容器の一端を開放し、樹脂粒子と分散媒とを容器内よ
シ低王の雰囲気下(通常は大気圧雰囲気下)に放出して
樹脂粒子を発泡せしめる等の方法によシ得られる。上記
発泡剤としては、二酸化炭素等の無機発泡剤、プロパン
、ブタン、ペンタン、ヘキサン、ヘプタン等で例示され
クロロフロロメタン、シクロロジフロロメターン。
The above-mentioned pre-expanded particles can be prepared by dispersing the resin particles in a dispersion medium together with a blowing agent in a closed container, for example, and heating it to a predetermined temperature, then opening one end of the container, and dispersing the resin particles and dispersion medium inside the container. The resin particles can be obtained by a method such as foaming the resin particles by discharging the resin particles into an atmosphere (usually an atmospheric pressure atmosphere). Examples of the blowing agent include inorganic blowing agents such as carbon dioxide, propane, butane, pentane, hexane, heptane, etc., and chlorofluoromethane and cyclodifluoromethane.

ジクロロテトラフロロエタン、メチルクロンイド。Dichlorotetrafluoroethane, methylchloride.

エチルクロライド、メチレンクロライド等で例示される
ハロゲン化炭化水素類等の揮発性発泡剤等が用いられる
。これらの発泡剤は通常樹脂粒子100重量部に対して
5〜40重量部重量部−られる。また分散媒は樹脂粒子
を溶解させない溶媒であればよく1例えば水、エチレン
グリコール。
Volatile blowing agents such as halogenated hydrocarbons such as ethyl chloride and methylene chloride are used. These blowing agents are usually used in an amount of 5 to 40 parts by weight per 100 parts by weight of the resin particles. The dispersion medium may be any solvent that does not dissolve the resin particles, such as water or ethylene glycol.

グリセリン、メタノール、エタノール等のうちの1f1
またはそれらの2種以上の混合物が例示されるが通常は
水が好ましい・。
1f1 of glycerin, methanol, ethanol, etc.
Or a mixture of two or more thereof is exemplified, but water is usually preferred.

本発明において上記予備発泡粒子の加熱膨張力とは、予
備発泡粒子を@300I+l!×長さ300闘X厚さ3
0闘の金型に充填して加熱した際に予備発泡粒子の膨張
によシ金型面に作用する最大面圧であり、該加熱膨張力
は、予備発泡粒子製造時の基材樹脂の種類の選定9発泡
剤添加量1発泡温度。
In the present invention, the heating expansion force of the pre-expanded particles is defined as @300I+l! x Length 300mm x Thickness 3
This is the maximum surface pressure that acts on the mold surface due to the expansion of the pre-expanded particles when they are filled into a mold with zero pressure and heated, and the heating expansion force depends on the type of base resin at the time of producing the pre-expanded particles. Selection 9 Foaming agent addition amount 1 Foaming temperature.

発泡時の圧力9発泡後の予備発泡粒子の養生条件。Pressure during foaming 9Curing conditions for pre-expanded particles after foaming.

予備発泡粒子の加圧処理条件等の調節によシ所定の値と
することができる。
It can be set to a predetermined value by adjusting the conditions for pressurizing the pre-expanded particles.

次に本発明の一実施例を図面に基き説明する。Next, one embodiment of the present invention will be described based on the drawings.

第1図に示すように本発明の合成樹脂発泡粒子型内成型
体1は、該成型体1の表面Wi2を構成する発泡粒子3
が、偏平した円盤形状を有し、内面M4’li:構成す
る発泡粒子5は球形に近い形状を有する。表面層2の発
泡粒子3は平面方向の平均径Lf(闘)と厚さ方向の平
均径Ld (1111)との間にLf/Ld〉3.5好
ましくはLf/Ld>5なる関係を有する。
As shown in FIG. 1, the synthetic resin foam particle in-mold molded body 1 of the present invention has foamed particles 3 constituting the surface Wi2 of the molded body 1.
However, it has a flattened disk shape, and the foamed particles 5 forming the inner surface M4'li have a shape close to a spherical shape. The foamed particles 3 of the surface layer 2 have a relationship between the average diameter Lf in the planar direction and the average diameter Ld in the thickness direction (1111) such that Lf/Ld>3.5, preferably Lf/Ld>5. .

Lf / Ldが3.5以下となると表面平滑性1表面
剛性が低下する。上記Lfは同図に示すように発泡粒子
3の平面方向の粒子径ノfの平均値であシ、 Ldは厚
さ方向の粒子径ノdの平均値である。Ldは通常0.0
1〜2mm、Lfは1〜10朋であることが好ましい。
When Lf/Ld is 3.5 or less, surface smoothness 1 surface rigidity decreases. As shown in the figure, Lf is the average value of the particle diameter f in the planar direction of the expanded particles 3, and Ld is the average value of the particle diameter d in the thickness direction. Ld is usually 0.0
It is preferable that the length is 1 to 2 mm, and Lf is 1 to 10 mm.

また上記表面層2の厚さdは成型体1の15撃吸収性を
維持しかつ表面剛性の向上を図るためには通常成壓体1
の厚さDの2%〜10%であることが好ましい。上記構
成含有する表面層2は成型体1の表裏両面に設けられた
場合に限らず9片面にのみ設けられたものでもよい。
In addition, the thickness d of the surface layer 2 is normally set to 15 in order to maintain the impact absorption properties of the molded body 1 and to improve the surface rigidity.
It is preferable that it is 2% to 10% of the thickness D of . The surface layer 2 containing the above structure is not limited to the case where it is provided on both the front and back surfaces of the molded body 1, but may be provided only on one side.

上記本発明の成型体1は次のようにして製造することが
できる。即ち例えば第2図に示す如き仕切板6.6によ
シ成呈室を3分割した成型用型7鵞用い、成型用m7の
壁面8.8と接する表層部側の成屋室9,9には、該成
壓室9,9よシ内側に位置する成屋室10に供給口11
よシ供給されて充填された予備発泡粒子12の加熱膨張
力Pi(kg/d・絶対圧)に対してPi/Ps> 1
.5 、好ましくはPi/Ps)2となる加熱膨張力P
s (kl / crl ・絶対圧)を有する予備発泡
粒子13を供給口14゜14よシ供給して充填する。し
かる後仕切板6゜6′?:取り除き、1.0kl? /
 cJ(G) 〜5. Okg / cJ(G)の水蒸
気等により加熱する。加熱によシ成型室9゜9内に充填
された表層部の予備発泡粒子13および成型室10内に
充填された内層部の予備発泡粒子12はともに膨張する
が2表層部の予備発泡粒子13社内層部の予備発泡粒子
12よシも加熱膨張力が小さいため、内層部の予備発泡
粒子12の膨張によって該予備発泡粒子12と成型用型
7の壁面8とで挟圧される結果偏平して膨張し、以って
第1図に示す構造の成型体1が得られる。
The molded article 1 of the present invention described above can be manufactured as follows. That is, for example, a forming chamber 7 is divided into three parts by a partition plate 6.6 as shown in FIG. In this case, a supply port 11 is provided in the finishing chamber 10 located inside the finishing chambers 9, 9.
Pi/Ps>1 with respect to the heating expansion force Pi (kg/d・absolute pressure) of the pre-expanded particles 12 supplied and filled.
.. 5, preferably Pi/Ps)2 heating expansion force P
Pre-expanded particles 13 having a pressure of s (kl/crl/absolute pressure) are supplied through the supply port 14 and filled. The rear partition plate 6゜6'? : Removed, 1.0kl? /
cJ(G) ~5. Heating with water vapor, etc. of Okg/cJ (G). When heated, both the surface pre-foamed particles 13 filled in the molding chamber 9°9 and the inner layer pre-foamed particles 12 filled in the molding chamber 10 expand; Since the heating expansion force is smaller than that of the pre-expanded particles 12 in the in-house layer section, the expansion of the pre-expanded particles 12 in the inner layer section causes the pre-expanded particles 12 to be pressed between the pre-expanded particles 12 and the wall surface 8 of the mold 7, resulting in flattening. The molded body 1 having the structure shown in FIG. 1 is obtained.

上記の方法に用いられる予備発泡粒子は発泡倍率10〜
80倍9粒子の平均径0.8〜101111のものが好
ましく9表層部の予備発泡粒子13は加熱膨張力P8が
2 kg / cyd (絶対圧)未満、内層部の予備
発泡粒子12は加熱膨張力ptが2 kg/ tri 
(絶対圧)以上であるとともに前述の如(Pi /Ps
 > 1.5好ましくはPi/Ps>2となるものを用
いる。
The pre-expanded particles used in the above method have an expansion ratio of 10 to
Pre-expanded particles 13 in the surface layer have a thermal expansion force P8 of less than 2 kg/cyd (absolute pressure), and the pre-expanded particles 12 in the inner layer have a thermal expansion force of less than 2 kg/cyd (absolute pressure). Force pt is 2 kg/tri
(absolute pressure) or more and as mentioned above (Pi /Ps
>1.5, preferably Pi/Ps>2.

また上記した如き仕切板を有す′る成型用型を用いる場
合に限られず、成型室内容積を拡大できるように構成さ
れた成型用型にまず加熱膨張力Piを有する予備発泡粒
子を充填した後、成型用型を拡大しつつ表層部側に上記
加熱膨張力Piに対してPl/ps>t、sとなる加熱
膨張力Pt+を有する予備発泡粒子を充填して加熱する
方法によってもよい。
In addition, it is not limited to the case where a mold having a partition plate as described above is used, but after filling a mold configured to expand the internal volume of the molding chamber with pre-expanded particles having a thermal expansion force Pi, Alternatively, while enlarging the mold, the surface layer side may be filled with pre-expanded particles having a thermal expansion force Pt+ such that Pl/ps>t,s with respect to the thermal expansion force Pi, and then heated.

以上説明したように本発明の成型体は1表面層を構成す
る発泡粒子が、内面層を構成する発泡粒子に比べ、平面
方向の平均径Lfと厚さ方向の平均径LdがLf/Ld
 > 3.5となるよう偏平した形状を有するため、成
型体表面が従来の成型体に比して極めて滑らかであると
ともに、成型体全体としての衝撃吸収性を維持したまま
表面層の剛性向上を図ることができる効果を有する。
As explained above, in the molded article of the present invention, the foamed particles constituting one surface layer have an average diameter Lf in the plane direction and an average diameter Ld in the thickness direction Lf/Ld compared to the foamed particles constituting the inner surface layer.
> 3.5, the surface of the molded body is extremely smooth compared to conventional molded bodies, and the rigidity of the surface layer can be improved while maintaining the impact absorption properties of the molded body as a whole. It has the effect that can be achieved.

また本発明方法によれば、加熱膨張力の異なる予備発泡
粒子を層別に充填し加熱発泡せしめるという簡単な作業
によシ上記の成型体を確定かつ容易に製造することがで
きる。
Further, according to the method of the present invention, the above-mentioned molded body can be manufactured reliably and easily by a simple operation of filling pre-expanded particles having different heating expansion powers in layers and heating and foaming them.

以下、具体的実施例を挙げて本発明を更に詳細に説明す
る。
Hereinafter, the present invention will be explained in more detail by giving specific examples.

実施例1〜3.比較例1〜4 実施例、比較例において用いた予備発泡粒子1〜5は以
下のようにして製造した。
Examples 1-3. Comparative Examples 1 to 4 Pre-expanded particles 1 to 5 used in Examples and Comparative Examples were manufactured as follows.

く予備発泡粒子1〉 エチレン成分含有量3.0重量係、メルトインデックス
7.8J9/10分のエチレン−プロピレンランダム共
重合体よシなる平均粒径1.5闘の樹脂粒子100重量
部、ジクロロシフ0口メタン18重員部、微粒状酸化ア
ルミニウム0.5重量部、水250重量部をオートクレ
ーブに入れ、143℃\J に外淵した。このときのオートクレーブ内圧は24 k
g/ d(G)であった。次いで窒素ガスによシオート
クレープ内圧’t−30kg/6A(G)に維持しつつ
オートクレーブの一端を開放し、樹脂粒子と水とを大気
圧下に放出して樹脂粒子を発泡せしめた。
Pre-expanded particles 1> 100 parts by weight of resin particles with an average particle size of 1.5 mm made of ethylene-propylene random copolymer with an ethylene content of 3.0 weight and a melt index of 7.8 J9/10, dichlorosif 18 parts by weight of methane, 0.5 parts by weight of finely divided aluminum oxide, and 250 parts by weight of water were placed in an autoclave, and the autoclave was heated to 143°C\J. The internal pressure of the autoclave at this time was 24 k.
g/d(G). Next, one end of the autoclave was opened while maintaining the internal pressure of the autoclave at -30 kg/6A (G) using nitrogen gas, and the resin particles and water were discharged to atmospheric pressure to foam the resin particles.

この予備発泡粒子を常温、常圧下で48時間放置し1粒
子内のジクロロジフロロメタンを空気置換したものを予
備発泡粒子1とした。
These pre-expanded particles were allowed to stand at room temperature and under normal pressure for 48 hours, and the dichlorodifluoromethane in each particle was replaced with air, thus forming pre-expanded particles 1.

く予備発泡粒子2〉 上記予備発泡粒子1を加圧タンクに入れ空気によl) 
0.05 kl / cd / hrの昇圧速′度で2
.6 kg #J(G)まで昇圧して加圧処理し粒子内
圧3. s kg / tri (絶対圧)1i−付与
せしめ予備発泡粒子2とした。
Pre-expanded particles 2〉 Put the above-mentioned pre-expanded particles 1 into a pressurized tank and blow air into it.
2 at a boost rate of 0.05 kl/cd/hr
.. The pressure is increased to 6 kg #J (G) and the internal pressure of the particles is 3. s kg/tri (absolute pressure) 1i- was applied to obtain pre-expanded particles 2.

〈予備発泡粒子3〉 予備発泡粒子1と同一の原料を同一の配合でオートクレ
ーブに仕込み、一旦155℃まで昇温した後、140℃
まで降温し該温度においてオートクレーブ内圧を5ok
1?/cr/1(G)に維持しつつ、樹脂粒子と水とを
大気圧下に放出して樹脂粒千金発泡せしめた。この予備
発泡粒子を常温、常圧下で48時間放置して予備発泡粒
子3とした。
<Pre-expanded particles 3> The same raw materials as those for pre-expanded particles 1 were charged into an autoclave with the same composition, and the temperature was once raised to 155°C, then 140°C.
At that temperature, the autoclave internal pressure was increased to 5ok.
1? /cr/1 (G), the resin particles and water were released under atmospheric pressure to cause the resin particles to foam. The pre-expanded particles were left at room temperature and under normal pressure for 48 hours to obtain pre-expanded particles 3.

く予1111発泡粒子4〉 予備発泡粒子1′Ii−予備発泡粒子2と同様の方法に
よ!+0.7kg/d(G)まで昇圧して加圧処理し。
1111 Expanded particles 4> Pre-expanded particles 1'Ii - Same method as pre-expanded particles 2! The pressure was increased to +0.7 kg/d (G) and the pressure was applied.

粒子内圧1.5 kl / crli (絶対圧)を付
与せしめて予備発泡粒子4とした。
Pre-expanded particles 4 were obtained by applying a particle internal pressure of 1.5 kl/crli (absolute pressure).

(予備発泡粒子5〉 予備発泡粒子3t−予備発泡粒子2と同様の方法により
1.2 ky / ca (G)まで昇圧して加圧処理
し。
(Pre-expanded particles 5) Pre-expanded particles 3t - Pressurized by increasing the pressure to 1.2 ky/ca (G) in the same manner as for pre-expanded particles 2.

粒子内圧2.0 kg/ ca (絶対圧)を付与せし
めて予備発泡粒子5とした。
A particle internal pressure of 2.0 kg/ca (absolute pressure) was applied to obtain pre-expanded particles 5.

する厚さ50闘Xlt9i300mx長さ300闘(内
寸法)の成型用型に充填し仕切板を取シ除いた後。
After filling a mold with a thickness of 50cm x 300m x length of 300cm (inner dimensions) and removing the partition plate.

3.4ky/c+J(G)の水蒸気により加熱して予備
発泡粒子を発泡PI#彊せしめ成型体t−得た。得られ
た各成瀧体の物性t−測測定た結果′を第2表に示す。
The pre-expanded particles were heated with steam of 3.4 ky/c+J (G) to form foamed PI# to obtain a molded article. Table 2 shows the results of the t-measurement of the physical properties of each of the obtained grown bodies.

また成型体の宍面から2IIIItでの表面層t−構成
する発泡粒子の平面方向の平均径Lfと厚さ方向の平均
径Ldを測定した結果を第2表に示す。
Further, Table 2 shows the results of measuring the average diameter Lf in the plane direction and the average diameter Ld in the thickness direction of the foamed particles constituting the surface layer t at 2IIIt from the bottom of the molded body.

岡、成型用型の、相対向する壁面と各々接する表層部お
よび該表層部よシ内偶の内層部に充填した予備発泡粒子
の種類を第2表にあわせて示した。
Table 2 also shows the types of pre-expanded particles that were filled in the surface layer portions of the molds that were in contact with the opposing wall surfaces, and the inner layer portions between the surface layer portions and the inner layer portions.

※l Lf、Ldは成型体縦断面の上面よシ3龍以内に
ある発泡粒子よシランダムに50個を選び顕微鏡(フッ
−株式会社製デジタル顕微鏡 MS−224)により測
定した値の平均値である。
*Lf and Ld are the average values of the values measured using a microscope (Digital Microscope MS-224 manufactured by Fu-Co., Ltd.) selected from 50 foamed particles within 3 degrees of the top surface of the vertical section of the molded product. be.

※2 成型体の成型性り。*2 Molding properties of the molded object.

成型体の、成型用型面方向に対する 収縮率が2%未満で型iJ1シの成型体が得られる・−
−−−一−−・−・−=0収縮率が2〜3%未満であシ
はぼ型通シの成型体が得られるが冷却に長時間を要する
一−−−−−−−−−−−−−−−△収縮率が3%以上
の成型体となる・−・−−−−−−−・−・−・−×と
して判定した。
A molded body of type iJ1 can be obtained with a shrinkage rate of the molded body in the direction of the mold surface of less than 2%.
−−−1−−・−・−=0 If the shrinkage rate is less than 2 to 3%, a round-shaped molded product can be obtained, but it takes a long time to cool down.−−−−−−−− -----------------------------------------------------------------------------------------------------------------------------------------

※3 曲げ強さは1J25闘、長さ300nの試験片を
長さ150鯖が試験台より突出するように試験台に固定
し、突出した試験片の先端に500gの荷重をのせた時
に生ずるたわみ1(jIII)で表示した。
*3 The bending strength is 1J25, and the deflection that occurs when a 300n long test piece is fixed on a test stand with a length of 150 nm protruding from the test stand and a 500g load is placed on the tip of the protruding test piece. 1 (jIII).

※41rlj撃吸収性は水平状態の成形体表面に、直径
65朋の円形底面を有する2kllの分銅を1mの高さ
から自然落下させ(このとき。
*41rlj Shock absorption was measured by dropping a 2kll weight with a circular base of 65 mm in diameter naturally onto the surface of the molded product in a horizontal state from a height of 1 m (at this time).

分銅の円形底面を水平にして落下させる)。(Drop the weight with its circular bottom horizontally).

落下後の成形体の表面状態により判定した。Judgment was made based on the surface condition of the molded product after it was dropped.

表面が破れず変形も殆んどなし−−−−−−−−−−−
・−−−−0表面に変形が残るー・−−−−−−−−−
〜−−−−・−−一一−−−−・Δ表面に裂傷が生ずる
−・−−−−−−−−・−−一−−−−・−−−−x※
5 表面状態は 表面平滑で凹凸、しわがきわめて 小さい・−・−−−−−−−−−−0 表面凹凸、しわがやや大きい −・−・・−−−−−−
−−−6表面平滑性に劣シ、凹凸、しわが 大きい・−・−−−−−−−x として判定した。
The surface is not torn and there is almost no deformation.
・-----Deformation remains on the surface-----------
〜−−−−・−−1−−−−・Δ Tears occur on the surface−・−−−−−−−−・−−1−−−−・−−−−x※
5 The surface condition is smooth with very small irregularities and wrinkles ---------0 Surface irregularities and wrinkles are somewhat large ---------
---6 Poor surface smoothness, large unevenness, and wrinkles -------x

【図面の簡単な説明】[Brief explanation of the drawing]

図面拡本発明の一実施例を示すもので、第1図は本発明
成型体の要部縦断面図、第2図は本発明の成狙体の製造
方法において用いられる成型用型の一例を示す縦断面略
図である。 1−一一一合成樹脂発泡粒子型内成型体8・−・−表面
層の発泡粒子 8−−−−一壁面1.2−−・−内層部
の予備発泡粒子 + 8−−−−−−一表層部の予備発
泡粒子 第1図
The drawings are enlarged to show one embodiment of the present invention. Fig. 1 is a longitudinal cross-sectional view of a main part of a molded body of the present invention, and Fig. 2 is an example of a mold used in the method for manufacturing a target body of the present invention. FIG. 1-11 Synthetic resin foamed particle in-mold molded body 8 --- Foamed particles in the surface layer 8 --- One wall surface 1.2 --- Pre-expanded particles in the inner layer + 8 --- - Figure 1 of pre-expanded particles in one surface layer

Claims (2)

【特許請求の範囲】[Claims] (1) 合成樹脂予備発泡粒子を成型用屋内で発泡成型
して得られる合成樹脂発泡粒子屋内成型体において、該
成型体の表面層を構成する発泡粒子の、平面方向の平均
径Lf (闘) と厚さ方向の平均径Ld(闘)との比
が、Lf/Ld>3.5であることを特徴とする合成樹
脂発泡粒子型内成型体。
(1) In an indoor molded synthetic resin foamed particle obtained by foam-molding synthetic resin pre-expanded particles indoors for molding, the average diameter Lf in the planar direction of the foamed particles constituting the surface layer of the molded object. An in-mold molded article of foamed synthetic resin particles, characterized in that the ratio of Lf/Ld to the average diameter Ld in the thickness direction is Lf/Ld>3.5.
(2) 成型用型の壁面と接する表層部に、加熱膨張力
Ps(kg / cd・絶対圧)が、該表層部よ)内側
の内層部に充填された予備発泡粒子の加熱膨張力Pi(
kf / d ・絶対圧)に対してPi / Ps >
1.5なる関係を有する予備発泡粒子を充填し一加熱成
型して表面層を構成する発泡粒子の平面方向の平均径L
f(m)と厚さ方向の平均径Ld (mm)との比がL
f /Ld > 3.5である成型体を得ることを特徴
とする合成樹脂発泡粒子型内成型体の製造方法。
(2) The heating expansion force Ps (kg/cd・absolute pressure) is applied to the surface layer in contact with the wall surface of the mold, and the heating expansion force Pi (
kf/d・absolute pressure) vs. Pi/Ps>
Average diameter L in the planar direction of foamed particles that are filled with pre-expanded particles having a relationship of 1.5 and then heat-molded to form a surface layer.
The ratio of f (m) to the average diameter Ld (mm) in the thickness direction is L
A method for producing an in-mold molded article of foamed synthetic resin particles, characterized by obtaining a molded article in which f /Ld > 3.5.
JP58149299A 1983-08-16 1983-08-16 Expanded synthetic resin in-mold molding and its production Granted JPS6042433A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58149299A JPS6042433A (en) 1983-08-16 1983-08-16 Expanded synthetic resin in-mold molding and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58149299A JPS6042433A (en) 1983-08-16 1983-08-16 Expanded synthetic resin in-mold molding and its production

Publications (2)

Publication Number Publication Date
JPS6042433A true JPS6042433A (en) 1985-03-06
JPH0414058B2 JPH0414058B2 (en) 1992-03-11

Family

ID=15472125

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58149299A Granted JPS6042433A (en) 1983-08-16 1983-08-16 Expanded synthetic resin in-mold molding and its production

Country Status (1)

Country Link
JP (1) JPS6042433A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63108727U (en) * 1986-12-30 1988-07-13
US4777000A (en) * 1985-11-29 1988-10-11 Japan Styrene Paper Corporation Production method of expansion-molded article of polypropylene resin
JP2006240285A (en) * 2005-02-01 2006-09-14 Kaneka Corp Thermoplastic resin in-mold foamed molded product and its manufacturing method
JP2011068776A (en) * 2009-09-25 2011-04-07 Sekisui Plastics Co Ltd Foam-molded article
JP2012176686A (en) * 2011-02-25 2012-09-13 Sekisui Plastics Co Ltd Railway vehicular interior material
WO2019198642A1 (en) * 2018-04-09 2019-10-17 旭化成株式会社 Foam molding and method for producing same
WO2024042810A1 (en) * 2022-08-22 2024-02-29 パナソニックIpマネジメント株式会社 Heat insulating wall and heat insulating container

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS493639U (en) * 1972-04-13 1974-01-12
JPS54174682U (en) * 1978-05-30 1979-12-10

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS493639U (en) * 1972-04-13 1974-01-12
JPS54174682U (en) * 1978-05-30 1979-12-10

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4777000A (en) * 1985-11-29 1988-10-11 Japan Styrene Paper Corporation Production method of expansion-molded article of polypropylene resin
JPS63108727U (en) * 1986-12-30 1988-07-13
JPH051380Y2 (en) * 1986-12-30 1993-01-14
JP2006240285A (en) * 2005-02-01 2006-09-14 Kaneka Corp Thermoplastic resin in-mold foamed molded product and its manufacturing method
JP2011068776A (en) * 2009-09-25 2011-04-07 Sekisui Plastics Co Ltd Foam-molded article
JP2012176686A (en) * 2011-02-25 2012-09-13 Sekisui Plastics Co Ltd Railway vehicular interior material
WO2019198642A1 (en) * 2018-04-09 2019-10-17 旭化成株式会社 Foam molding and method for producing same
JPWO2019198642A1 (en) * 2018-04-09 2020-12-03 旭化成株式会社 Foam molded product and its manufacturing method
US11235553B2 (en) 2018-04-09 2022-02-01 Asahi Kasei Kabushiki Kaisha Foam molded product and method of producing same
WO2024042810A1 (en) * 2022-08-22 2024-02-29 パナソニックIpマネジメント株式会社 Heat insulating wall and heat insulating container

Also Published As

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