JPH0464541B2 - - Google Patents

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Publication number
JPH0464541B2
JPH0464541B2 JP59110074A JP11007484A JPH0464541B2 JP H0464541 B2 JPH0464541 B2 JP H0464541B2 JP 59110074 A JP59110074 A JP 59110074A JP 11007484 A JP11007484 A JP 11007484A JP H0464541 B2 JPH0464541 B2 JP H0464541B2
Authority
JP
Japan
Prior art keywords
resin particles
container
blowing agent
particles
decomposable blowing
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.)
Expired - Lifetime
Application number
JP59110074A
Other languages
Japanese (ja)
Other versions
JPS60252637A (en
Inventor
Hiroyuki Akyama
Takashi Kubota
Shigeru Okabe
Koji Iizuka
Toshio Tokoro
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 JP11007484A priority Critical patent/JPS60252637A/en
Publication of JPS60252637A publication Critical patent/JPS60252637A/en
Publication of JPH0464541B2 publication Critical patent/JPH0464541B2/ja
Granted legal-status Critical Current

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

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は予備発泡粒子の製造方法に関する。 予備発泡粒子を成型用型内に充填して加熱発泡
せしめて得られる型内発泡成型体は、近年、断熱
材、緩衝材、梱包材、建築資材、浮揚材等広汎な
用途に使用されている。 本発明者らは上記型内発泡成型体の成型に用い
られる予備発泡粒子について長年に亘つて研究を
行なつた結果、気泡の均一な優れた予備発泡粒子
を容易かつ確実に製造し得る新規な製造方法の開
発に成功し本発明を完成するに至つた。 即ち本発明は実質的に未分解の分解型発泡剤を
含有する樹脂粒子を密閉容器内で分散媒に分散さ
せ、分解型発泡剤の分解温度以上の温度で所定時
間加熱、保持するとともに無機ガスにより容器内
を加圧しつつ容器の一端を開放し樹脂粒子を容器
内より低圧の雰囲気下に放出して発泡せしめるこ
とを特徴とする予備発泡粒子の製造方法を要旨と
する。 本発明において用いれる樹脂粒子の基材として
は、スチレン単独重合体、スチレン−無水マレイ
ン酸共重合体、スチレン−アクリロニトリル共重
合体、スチレン−アクリロニトリル−ブタジエン
共重合体等のスチレン系樹脂、エチレン単独重合
体、プロピレン単独重合体、エチレン−プロピレ
ンブロツク共重合体、エチレン−プロピレンラン
ダム共重合体等のポリオレフインが挙げられるが
中でもポリオレフインが好ましく、特に低密度ポ
リエチレン及びエチレン−プロピレンランダム共
重合体が好ましい。これらは架橋、無架橋のいず
れでも良いが、無架橋のものが好ましい。 本発明において用いられる分解型発泡剤として
は、アゾジカーボンアミド、ジニトロソペンタメ
チレンテトラミン、ジアゾアミノベンゼン、アゾ
ビスイソブチロニトリル、P,P′−オキシビスベ
ンゼンスルホニルヒドラジド、重炭酸ナトリウム
等が挙げられ、これら分解型発泡剤は1種または
2種以上を適宜選択して用いることができるが、
樹脂粒子の基材の融点に対し、分解温度が5℃以
上、好ましくは10〜100℃高いものを選択して用
いることが好ましい。 本発明における分解媒としては樹脂を溶解させ
ない溶媒であればよく、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1種または2以上の混合物が挙げられるが、
通常は水が用いられる。また樹脂粒子を分散媒に
分散せしめる際に必要に応じて微粒状酸化アルミ
ニウム、酸化チタン、塩基性炭酸マグネシウム、
塩基性炭酸亜鉛、炭酸カルシウム等の分散剤を添
加することができ、通常分散剤は樹脂粒子100重
量部当り0.1〜10重量部である。また上記樹脂粒
子の加熱温度は分解型発泡剤の分解温度以上の温
度であれば特に制限はないが通常は分解型発泡剤
の分解温度をT(℃)としたときT+10℃〜T+
100℃が好ましく、加熱保持時間は通常5〜120分
程度である。上記実質的に未分解の分解型発泡剤
を含有する樹脂粒子は、例えば押出機内で樹脂と
分解型発泡剤を分解型発泡剤の分解温度以下の温
度で溶融混練した後、押出機より押出し適宜の大
きさに切断する方法や液状の分解型発泡剤を密閉
容器内で分散媒の存在下樹脂粒子中に含浸させる
方法等により得られる。 本発明においては上記樹脂粒子を密閉容器内で
分解型発泡剤の分解温度以上の温度で所定時間加
熱保持するとともに、無機ガスにより容器内を加
圧しつつ容器の一端を開放して容器内より低圧の
雰囲気下に放出するが、このときの無機ガスとし
ては酸素、窒素、ヘリウム、ネオン、二酸化炭
素、空気等が挙げられこれらは混合して用いるこ
とができる。また無機ガスによる加圧圧力は通常
10Kg/cm2(G)以上好ましくは25〜40Kg/cm2(G)であ
り、所定時間(通常5分以上)保持した後同圧力
を保持しつつ(即ち無機ガスを補充しつつ)容器
の一端を開放して粒子を発泡させる。 以上のようにして樹脂粒子を容器内より低圧の
雰囲気下(通常は大気圧下)に放出することによ
り樹脂粒子が発泡せしめられ、通常2〜40倍の発
泡倍率の予備発泡粒子が得られる。 以上説明したように本発明によれば容易かつ確
実に予備発泡粒子を製造し得るとともに実質的に
未分解の分解型発泡剤を含有する樹脂粒子を用い
るため発泡剤が樹脂粒子中に均一に分散されてお
りその結果本発明により製造される予備発泡粒子
は気泡が均一で気泡のきめが細かい優れた物性を
有し、型内発泡成型体の成型用として好適な予備
発泡粒子である。 また、本発明製造方法によれば、実質的に未分
解の分解型発泡剤を含有する樹脂粒子を使用して
いるため、発泡剤の分解温度以上の温度に加熱保
持され、樹脂粒子の形状が真球に近い球状に形成
され、成型性の良好な発泡粒子が得られる効果が
ある。 更に本発明は分解型発泡剤を使用しているの
で、発泡剤が分解した場合窒素ガスや炭酸ガスや
水蒸気等が発生するが、これらのガスは揮発性発
泡剤に見られる可燃性ガスのような危険性やフロ
ンガス等のような大気汚染等の問題がなく、安全
で環境を汚染しない予備発泡粒子の製造方法を提
供することができる。 以下、実施例を挙げて本発明を更に詳細に説明
する。 実施例 1〜3 第1表に示す樹脂100重量部に対し、同表に示
す分解型発泡剤を添加して、押出機内で溶融混練
した後押出機より押出し、切断すると共に急冷し
実質的に未分解の分解型発泡剤を含有する樹脂粒
子を得た。この樹脂粒子100重量部を水300重量
部、微粒状酸化アルミニウム1重量部とともにオ
ートクレーブ内に供給し、第1表に示す温度で同
表に示す時間加熱及び空気で加圧しそれを保持し
た後、発泡温度を調節し容器内圧力を空気により
加圧し、同表に示す時間保持した後同表に示す圧
力を維持しつつ容器の一端を開放して樹脂粒子を
大気圧下に放出して発泡せしめ予備発泡粒子を得
た。得られた予備発泡粒子の性状を第1表にあわ
せて示す。
The present invention relates to a method for producing pre-expanded particles. In-mold foam molded products obtained by filling pre-expanded particles into a mold and heating and foaming them have recently been used in a wide range of applications such as insulation, cushioning, packaging, construction materials, flotation materials, etc. . The present inventors have conducted research for many years on the pre-expanded particles used in the molding of the above-mentioned in-mold foamed product, and as a result, we have developed a novel method that can easily and reliably produce excellent pre-expanded particles with uniform bubbles. They succeeded in developing a manufacturing method and completed the present invention. That is, in the present invention, resin particles containing a substantially undecomposed decomposable blowing agent are dispersed in a dispersion medium in a closed container, heated and held at a temperature equal to or higher than the decomposition temperature of the decomposable blowing agent for a predetermined period of time, and an inorganic gas is The gist of the present invention is a method for producing pre-expanded particles, which is characterized by pressurizing the inside of the container while opening one end of the container and releasing the resin particles from the inside of the container into a lower pressure atmosphere to cause foaming. The base material of the resin particles used in the present invention includes styrene homopolymer, styrene-based resin such as styrene-maleic anhydride copolymer, styrene-acrylonitrile copolymer, styrene-acrylonitrile-butadiene copolymer, and ethylene monopolymer. Examples include polyolefins such as polymers, propylene homopolymers, ethylene-propylene block copolymers, and ethylene-propylene random copolymers, among which polyolefins are preferred, with low-density polyethylene and ethylene-propylene random copolymers being particularly preferred. These may be either crosslinked or non-crosslinked, but non-crosslinked ones are preferred. Examples of decomposable blowing agents used in the present invention include azodicarbonamide, dinitrosopentamethylenetetramine, diazoaminobenzene, azobisisobutyronitrile, P,P'-oxybisbenzenesulfonyl hydrazide, and sodium bicarbonate. These decomposable blowing agents can be used alone or in combination of two or more.
It is preferable to select and use a resin particle whose decomposition temperature is 5° C. or higher, preferably 10 to 100° C. higher than the melting point of the base material of the resin particles. The decomposition medium in the present invention may be any solvent that does not dissolve the resin, and examples include one or a mixture of two or more of water, ethylene glycol, glycerin, methanol, ethanol, etc.
Usually water is used. In addition, when dispersing resin particles in a dispersion medium, fine particles of aluminum oxide, titanium oxide, basic magnesium carbonate,
A dispersant such as basic zinc carbonate or calcium carbonate can be added, and the amount of the dispersant is usually 0.1 to 10 parts by weight per 100 parts by weight of the resin particles. The heating temperature of the resin particles is not particularly limited as long as it is higher than the decomposition temperature of the decomposable blowing agent, but usually T+10°C to T+, where the decomposition temperature of the decomposable blowing agent is T (°C).
The temperature is preferably 100°C, and the heating holding time is usually about 5 to 120 minutes. The resin particles containing the substantially undecomposed decomposable blowing agent can be obtained by, for example, melting and kneading the resin and the decomposable blowing agent in an extruder at a temperature below the decomposition temperature of the decomposable blowing agent, and then extruding the resin particles from the extruder as appropriate. It can be obtained by cutting into pieces of size, or by impregnating a liquid decomposable foaming agent into resin particles in the presence of a dispersion medium in a closed container. In the present invention, the resin particles are heated and held in a closed container at a temperature higher than the decomposition temperature of the decomposable blowing agent for a predetermined period of time, and one end of the container is opened while the inside of the container is pressurized with an inorganic gas to lower the pressure from the inside of the container. The inorganic gas at this time includes oxygen, nitrogen, helium, neon, carbon dioxide, air, etc., and these can be used in combination. In addition, pressurization pressure using inorganic gas is usually
The pressure is 10Kg/cm 2 (G) or more, preferably 25 to 40Kg/cm 2 (G), and after maintaining the pressure for a predetermined period of time (usually 5 minutes or more), the pressure is maintained (that is, while replenishing the inorganic gas) in the container. One end is opened to allow the particles to foam. As described above, the resin particles are foamed by discharging the resin particles from the inside of the container into a lower pressure atmosphere (usually under atmospheric pressure), and pre-expanded particles having an expansion ratio of 2 to 40 times are usually obtained. As explained above, according to the present invention, it is possible to easily and reliably produce pre-expanded particles, and since resin particles containing a substantially undecomposed decomposable blowing agent are used, the blowing agent is uniformly dispersed in the resin particles. As a result, the pre-expanded particles produced according to the present invention have excellent physical properties such as uniform cells and fine cell texture, and are suitable for molding in-mold foamed products. Further, according to the manufacturing method of the present invention, since resin particles containing a substantially undecomposed decomposable blowing agent are used, the resin particles are heated and maintained at a temperature higher than the decomposition temperature of the blowing agent, and the shape of the resin particles is changed. This has the effect of obtaining foamed particles that are formed into a spherical shape close to a true sphere and have good moldability. Furthermore, since the present invention uses a decomposable blowing agent, when the blowing agent decomposes, nitrogen gas, carbon dioxide gas, water vapor, etc. are generated, but these gases are not combustible gases such as those found in volatile blowing agents. It is possible to provide a method for producing pre-expanded particles that is safe and does not pollute the environment, without problems such as air pollution caused by fluorocarbon gas or other dangers. Hereinafter, the present invention will be explained in more detail with reference to Examples. Examples 1 to 3 To 100 parts by weight of the resin shown in Table 1, the decomposable foaming agent shown in the same table was added, melted and kneaded in an extruder, extruded from the extruder, cut, and rapidly cooled to substantially Resin particles containing an undecomposed decomposable blowing agent were obtained. 100 parts by weight of these resin particles were supplied into an autoclave together with 300 parts by weight of water and 1 part by weight of finely divided aluminum oxide, heated at the temperature shown in Table 1 for the time shown in the same table, and then pressurized with air and held there. Adjust the foaming temperature, increase the pressure inside the container with air, hold it for the time shown in the same table, then open one end of the container while maintaining the pressure shown in the same table to release the resin particles under atmospheric pressure and foam. Pre-expanded particles were obtained. The properties of the obtained pre-expanded particles are also shown in Table 1.

【表】 *1 予備発泡粒子を切断して切断面の気泡状態を顕
微鏡で観察した。
[Table] *1 Pre-expanded particles were cut and the state of bubbles on the cut surface was observed using a microscope.

Claims (1)

【特許請求の範囲】[Claims] 1 実質的に未分解の分解型発泡剤を含有する樹
脂粒子を密閉容器内で分散媒に分散させ、分解型
発泡剤の分解温度以上の温度で所定時間加熱、保
持するとともに無機ガスにより容器内を加圧しつ
つ容器の一端を開放し樹脂粒子を容器内より低圧
の雰囲気下に放出して発泡せしめることを特徴と
する予備発泡粒子の製造方法。
1. Resin particles containing a substantially undecomposed decomposable blowing agent are dispersed in a dispersion medium in a closed container, heated and held at a temperature higher than the decomposition temperature of the decomposable blowing agent for a predetermined period of time, and the inside of the container is heated with an inorganic gas. 1. A method for producing pre-expanded particles, which comprises: opening one end of the container while pressurizing the resin particles, and releasing the resin particles from inside the container into a low-pressure atmosphere to cause foaming.
JP11007484A 1984-05-30 1984-05-30 Preparation of preexpanded particle Granted JPS60252637A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11007484A JPS60252637A (en) 1984-05-30 1984-05-30 Preparation of preexpanded particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11007484A JPS60252637A (en) 1984-05-30 1984-05-30 Preparation of preexpanded particle

Publications (2)

Publication Number Publication Date
JPS60252637A JPS60252637A (en) 1985-12-13
JPH0464541B2 true JPH0464541B2 (en) 1992-10-15

Family

ID=14526377

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11007484A Granted JPS60252637A (en) 1984-05-30 1984-05-30 Preparation of preexpanded particle

Country Status (1)

Country Link
JP (1) JPS60252637A (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49129759A (en) * 1973-04-16 1974-12-12
JPS5876230A (en) * 1981-10-31 1983-05-09 Kanegafuchi Chem Ind Co Ltd Manufacture of polypropylene resin foamed particle
JPS5930836A (en) * 1982-08-13 1984-02-18 Kanegafuchi Chem Ind Co Ltd Method for preliminarily expanding polyolefin type resin particle

Also Published As

Publication number Publication date
JPS60252637A (en) 1985-12-13

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