JPS5945331A - Manufacture of foam-molded article - Google Patents

Manufacture of foam-molded article

Info

Publication number
JPS5945331A
JPS5945331A JP57157339A JP15733982A JPS5945331A JP S5945331 A JPS5945331 A JP S5945331A JP 57157339 A JP57157339 A JP 57157339A JP 15733982 A JP15733982 A JP 15733982A JP S5945331 A JPS5945331 A JP S5945331A
Authority
JP
Japan
Prior art keywords
foam
molded article
foaming agent
temperature
injection molding
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
JP57157339A
Other languages
Japanese (ja)
Other versions
JPH0231737B2 (en
Inventor
Kenjiro Hashimoto
健次郎 橋本
Seiji Saka
坂 聖二
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.)
Mitsuboshi Belting Ltd
Original Assignee
Mitsuboshi Belting 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 Mitsuboshi Belting Ltd filed Critical Mitsuboshi Belting Ltd
Priority to JP57157339A priority Critical patent/JPS5945331A/en
Publication of JPS5945331A publication Critical patent/JPS5945331A/en
Publication of JPH0231737B2 publication Critical patent/JPH0231737B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To manufacture a high-quality practical foam-molded article without causing the rusting and corrosion of the mold, by adding a foaming agent composed of a specific compound and sodium bicarbonate to a thermoplastic resin, and injection molding the composition at a temperature above the decomposition initiation temperature of the foaming agent. CONSTITUTION:A foaming agent obtained by mixing 1mol of a monoamine salt of citric acid, itaconic acid or tartaric acid with 1-0.2mol of sodium bicarbonate, is added to a thermoplastic resin (e.g. polyamide), and the composition is injection-molded by a particular injection molding machine for structural foam at a temperature above the decomposition initiation temperature of the foaming agent (about 200 deg.C) to obtain the objective foam-molded article. EFFECT:The venting time of the foam-molded article can be shortened.

Description

【発明の詳細な説明】 てスキン層と発泡層のサンドインチ構造となるストラク
テヤルフォームの如き熱F+1塑性樹脂発泡成形品の製
造方法に開するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention discloses a method for producing a thermal F+1 plastic resin foam molded product such as a structural foam having a sandwich structure of a skin layer and a foam layer.

ホリアミド,ホリエステル.改質ボリフェニレンオキサ
イド,ABS,ボリスチレンの如き特ニ高融点重会体を
発泡射出成形する場合、従来発泡剤としてアソ糸,ニト
ロソ系.ヒドラジン系等ノ発泡剤が使用され、なかでも
アゾ・ジ・カーボン7ミl’は最も一般的に良く用いら
れている。しかしこれ等の発泡剤は優れた発泡性能を示
す反面、発泡剤の残査がボス,リブ,穴等につ1り数シ
ョットごとに取り除く作業を必要とし、J]つ残査によ
るモールドの錆や腐蝕を発生させる等大@な欠点分有し
ている。さらに、これ等の発泡剤企使用した成形物は該
成形物内のガス拡散速度が遅く、成形後すぐに塗装する
と成形物内部のガスが塗膜にビンポール状の穴を発生せ
しめるという基本的な欠点があり、ガス抜は期間、成形
物をストックしなければならない難点を右下る。
Pholamide, hollyester. In the case of foam injection molding of special polymers with high melting points such as modified polyphenylene oxide, ABS, and polystyrene, conventionally, aso yarn, nitroso type, etc. are used as blowing agents. Foaming agents such as hydrazine are used, and among them, azo dicarbon 7 mil' is most commonly used. However, while these foaming agents exhibit excellent foaming performance, they require work to remove foaming agent residue from bosses, ribs, holes, etc. every few shots, and the mold rust due to the residue. It has major drawbacks such as corrosion and corrosion. Furthermore, molded products using these blowing agents have a slow gas diffusion rate within the molded product, and if painted immediately after molding, the gas inside the molded product will cause holes in the paint film. There are disadvantages, such as the difficulty of having to stock molded products for a long time to vent the gas.

これを更に具体的に実験にもとづいて詳述すると、一般
に重炭酸ナトリウム又はこれとクエン酸あるいは酒石酸
との組合せによる発泡方法は古くから行なわれており、
周知である。
To explain this in more detail based on experiments, foaming methods using sodium bicarbonate or its combination with citric acid or tartaric acid have generally been used for a long time.
It is well known.

ところで、重炭酸ナトリウムだけの発泡について温度上
昇中のガス発生状況をみると、上昇速度29気で流動バ
ラフィン1 0 0 ac  中・試別1。
By the way, looking at the gas generation during temperature rise for foaming with only sodium bicarbonate, the rate of rise was 29 atmospheres, and the liquid paraffin was 100 ac.

o07について考察すると、第1図の如くであり、14
0℃〜160℃lcおけるガス発生量の増加が著しく成
形物の表面に分解残査を生じて塗装π対する悪影響が懸
念される。
Considering o07, it is as shown in Figure 1, and 14
The increase in the amount of gas generated at 0°C to 160°C 1C causes decomposition residue on the surface of the molded product, and there is concern that it will have an adverse effect on the coating π.

これに対し上昇速度2℃廓、流動パラフィン1OCC中
、試料]、、 OOO¥といつ同条件で前記発泡剤π等
モルのクエン酸を加え、重炭酸ナトリウム0.2857
V、クエン酸0.7143Pの混合物を用いて実験した
ところ温度上昇中のガス発生状況は第2図の如くなり、
前記のような事態汀クエン酸で中和されることによりな
くなるが、反面、分解温度が低くなり、高融点重合体に
は分解が急激すぎて気泡荒れやガスの逃げによる発泡倍
率不足及び金型腐蝕の問題が発生する。
To this, at a rising rate of 2°C, in 1 OCC of liquid paraffin, under the same conditions as the sample], OOO\, add citric acid equivalent to π of the blowing agent, and add 0.2857 ml of sodium bicarbonate.
In an experiment using a mixture of V and citric acid 0.7143P, the gas generation situation during temperature rise was as shown in Figure 2.
The above-mentioned situation can be eliminated by neutralization with citric acid, but on the other hand, the decomposition temperature becomes low, and the decomposition is too rapid for high melting point polymers, resulting in rough bubbles, insufficient foaming ratio due to gas escape, and mold failure. Corrosion problems occur.

かくして本発明は、斜上の如き問題に着目し、その欠点
を排除し高融点重合体の発泡成形といえどもモールドの
錆や腐蝕の発生の懸念がなく・かつ成形抜の発泡成形品
のガス抜き時間を短かくした発泡成形品?製造する方法
?提供するものである。
Thus, the present invention focuses on problems such as tilting, eliminates the drawbacks, eliminates the concern of mold rust and corrosion even when foam molding is performed using a high melting point polymer, and eliminates the risk of mold rust and corrosion. Foam molded products with shortened punching time? How to manufacture? This is what we provide.

即ち、本発明は従来の発泡剤に代る発泡剤を見出し、所
要温度で発泡成形することを目的とし、熱可塑性樹脂に
発泡剤ひ添加して発泡射出成形するに際し、該発泡剤と
してクエン醗、イタコン酸又は酒石酸の1アミン塩のコ
一つに重炭酸すトリウム(重そう〕を組合せたものを使
用し、該発泡剤の分解温度以上の湿度で射出成形下べ)
ことを特徴とする。
That is, the present invention aims to find a blowing agent to replace conventional blowing agents and to perform foam molding at a required temperature. Injection molding using a combination of one amine salt of itaconic acid or tartaric acid and thorium bicarbonate at a humidity above the decomposition temperature of the blowing agent.
It is characterized by

ここで、前記重炭酸ナト17ウムに紹合わされるクエ’
#1.イタコン酸又は酒石酸の]アミン塩とは、酒石酸
、クエン酸又はイタコン酸のカルボン酸からなる群より
選ばれた1つにシクロヘギシルアミン、イソプロピルア
ミン、ブチルアミン、オクチルアミン、ドアシリアミン
。オレイルアミン。
Here, que' introduced to the 17 um of sodium bicarbonate.
#1. The amine salt of itaconic acid or tartaric acid is one selected from the group consisting of tartaric acid, citric acid, or the carboxylic acid of itaconic acid, such as cyclohegycylamine, isopropylamine, butylamine, octylamine, and doasilyamine. Oleylamine.

ステアリルアミン等の有機アミン塩としたものであり、
重炭酸ナトリウムとの組合せに際してはそれら1アミン
塩と重炭酸すl・リウムとのモル比は1:1〜0.2の
組合せが好lしい。
It is an organic amine salt such as stearylamine,
When used in combination with sodium bicarbonate, the molar ratio of the amine salt and sulfur/lium bicarbonate is preferably 1:1 to 0.2.

そして、この組@せによる発泡剤は発泡にあたり分解開
始温度が重炭酸す) IJウム単独よジ上がV成形物か
らのブレードもなく1発泡が特π高融点重合体に適する
と共に・これらのアミン塩が金型腐蝕を防止し、かつ、
アゾ型と異なって炭酸ガス系は成形物中のガスの拡散が
良いことからガス抜き期間が短かくて済み、理想的な発
泡剤である。
The blowing agent created by this combination has a decomposition starting temperature of bicarbonate during foaming. Amine salt prevents mold corrosion, and
Unlike the azo type, carbon dioxide type foams have good gas diffusion within the molded product, requiring a short degassing period, making them ideal blowing agents.

第3図はこの発泡剤の温度上昇中のガス発生状態を前記
第1図、第2図同様上昇速度2°Chin 、流動ハラ
フィン10 cc  中試刺10oOVで、かつ重炭酸
ナトリウム0.4000!/、クエン酸1シクロヘキシ
ルアミン塩0.6000 f/の発泡剤πツfi実験し
た結果である。
Figure 3 shows the state of gas generation during temperature rise of this blowing agent, as in Figures 1 and 2 above, with a rising rate of 2° Chin, 10 cc of liquid halafine, 10 oOV, and 0.4000 sodium bicarbonate! This is the result of an experiment using a blowing agent of 0.6000 f/, cyclohexylamine citric acid salt, and 0.6000 f/.

しかして、本発明において発泡剤の前記分解開始湿度と
汀、炭酸ガスの発生量が急激に発生し始める温度であり
、その1例は前記第3図を参照すれば200℃程度であ
る。
Therefore, in the present invention, the decomposition start humidity of the blowing agent and the temperature at which the amount of stagnation and carbon dioxide gas generation start to occur suddenly are about 200° C., as shown in FIG. 3 above.

なかでも、本発明では炭酸ガスによって均一微細気泡の
発泡成形品を得るため 炭酸ガスの発生量′とその温度
の関係は重要であり、成形温度は重要な要件になる。
In particular, in the present invention, the relationship between the amount of carbon dioxide gas generated and its temperature is important in order to obtain a foam molded product with uniform fine cells using carbon dioxide gas, and the molding temperature is an important requirement.

本発明では、この点についてiII記分解開始温度以上
で射出成形することも特徴としている。
Regarding this point, the present invention is also characterized by injection molding at a temperature higher than the decomposition start temperature described in III.

若し、成形が前Be分解開始濁度以下で行なわれるとき
は炭酸ガスの発生が少なく、充分な7%期の発泡を得る
ことはできない。
If molding is carried out at a turbidity below the start of Be decomposition, less carbon dioxide gas is generated and sufficient foaming at the 7% stage cannot be obtained.

なお・この場合の成形温度とは熱n1塑性樹脂と発泡剤
とが溶融混練されるシリンダ一部の温度である。
Note that the molding temperature in this case is the temperature of a part of the cylinder where the hot n1 plastic resin and the foaming agent are melt-kneaded.

そして本発明では発泡剤の分解湿度が上記第3図の如く
、200”C以上と高いため、この分解湿度に適合した
熱可塑性柿脂としてポリアミド、ポリエステル、改質ホ
リフエニレンオキサイド、A適用される。
In the present invention, since the decomposition humidity of the blowing agent is as high as 200"C or more as shown in Figure 3 above, polyamide, polyester, modified polyphenylene oxide, and A are used as thermoplastic persimmon fats suitable for this decomposition humidity. Ru.

又、射出成形については、通常の射出成形機が使用され
、射出成形機に種々の成形機でよいが、主にストラクナ
ヤルフォーム用の専用成形機が使用される。
Further, for injection molding, a normal injection molding machine is used, and although various molding machines may be used as the injection molding machine, a special molding machine for Struknayal foam is mainly used.

以下引続き、実施例を挙げて更に具体的に説明する。The present invention will be described in more detail below with reference to Examples.

実施例1 比i1.1の改質ポリフェニレンオキサイド1O07に
重炭酸ナトリウム0.87とクエン酷lシク口・\キシ
ルアミン塩1.o2の比率でタンブラ−で混合し、それ
を低圧のS Tiw用マシマシンOX−CelF’  
社M 400 トン〕 を用いンリンダー、マニホール
ドとも260℃の温度て成形した。得られlζ製品は均
一微細気泡を有L、発泡倍率611.3倍であった。
Example 1 Modified polyphenylene oxide 1007 with a ratio of 1.1, 0.87 sodium bicarbonate, and xylamine salt 1. Mix in a tumbler at a ratio of
Both the cylinder and the manifold were molded at a temperature of 260° C. using a molding machine manufactured by Matsumoto Co., Ltd. (400 tons). The obtained lζ product had uniform fine bubbles and a foaming ratio of 611.3 times.

且つ、モールドの錆発生汀なく、成形2時間後塗装して
も、塗膜に異常は認められなかった。
In addition, there was no rust formation on the mold, and no abnormality was observed in the coating film even when it was painted 2 hours after molding.

実施例2 比重1.1の改質ポリフェニレンオキサイド100フπ
重炭酸ナトリウム0.8yと酒石酸1シクロヘギシルア
ミン塩0.82の比率でタンブラ−で混介し、それ?低
圧のSF専用マシン(Ex−Oe 11−0社製400
 +、ン)を用いシリンダー、マニホールドとも260
℃の温度で成形した。
Example 2 Modified polyphenylene oxide 100 π with specific gravity 1.1
Mix 0.8 y of sodium bicarbonate and 0.82 y of tartaric acid cyclohegycylamine salt in a tumbler. Low-pressure SF machine (400 manufactured by Ex-Oe 11-0)
+, n) for both cylinder and manifold.
Molded at a temperature of ℃.

得られた製品は均一微細気泡を有し、発泡倍率は1.3
倍であった。且つ、モールドの錆発生はなく、成形2時
間後塗装しても、塗膜に異常は認められなかつlこ。
The obtained product has uniform fine cells, and the foaming ratio is 1.3.
It was double that. In addition, there was no rust on the mold, and no abnormalities were observed in the coating film even when it was painted 2 hours after molding.

実施例3 比重1,06のA E S樹脂ぺL・シト100フπ車
炭酸すトリウム0.8ンとイタコン酸lイソプロピルア
ミン塩o、79の比率でタンブラ−で混付し、それを低
圧のSF専用マシン(Ex C!θ11−0礼製400
!・ン)を用いシリンダー、マニホールドとも210°
Cの温度で成形した。得られた製品は均一微細気泡を有
し、発泡倍率は]5倍であった。
Example 3 AES resin with a specific gravity of 1.06 was mixed in a tumbler at a ratio of 0.8% thorium carbonate and 79% isopropylamine salt of itaconate, and then heated under low pressure. SF dedicated machine (Ex C! θ11-0 made 400
!・Both cylinder and manifold are 210°.
It was molded at a temperature of C. The obtained product had uniform fine cells, and the expansion ratio was 5 times.

且つ、モールドの錆発生汀なく、成形3晶間後で塗装し
ても、塗膜に異常は認められなかった。
In addition, there was no rust formation on the mold, and no abnormality was observed in the coating film even if it was painted after three molding cycles.

以上の各実施例より明らかな如く本発明方法によれば高
融点重合体の発泡成形といえども均一微細気泡の良質な
製品で発泡倍率も充分であるストラクチャルフオームを
容易に製造することができ、しかも金型腐蝕の問題もな
く、塗装に対する悪影響も生ぜず、誠VC実用的である
As is clear from the above examples, according to the method of the present invention, it is possible to easily produce a structural foam that is a high-quality product with uniform fine cells and has a sufficient expansion ratio, even in the case of foam molding of a high melting point polymer. Moreover, there is no problem of mold corrosion, and there is no adverse effect on the coating, making it a practical VC.

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

第1図乃至第3図は温度上昇中のガス発生状況を示す図
表で、第1図及び第2図は比較例であり、第3図Qゴ木
発明の実施例の場会である。 竿1回 ’5T&11(’C) 94Z図 温度(・C)
FIGS. 1 to 3 are charts showing the state of gas generation during temperature rise, FIGS. 1 and 2 are comparative examples, and FIG. 3 is a diagram showing an embodiment of the invention. Rod once '5T & 11 ('C) 94Z chart temperature (・C)

Claims (1)

【特許請求の範囲】[Claims] / 熱可塑性樹脂に発泡剤を添加して発泡射出成形する
に際し、発泡剤としてクエン酸の1アミン塩、イタコン
酸の1アミン酸あ句いは酒石酸の1アミン塩からなる群
から選ばれた少くとも]つと重炭酸ナトリウムとを組合
せたものを使用し、該発泡剤の分解開始温度以上で射出
成形することを特徴とする発泡成形品の製造方法。
/ When foaming injection molding is performed by adding a blowing agent to a thermoplastic resin, a small amount selected from the group consisting of a monoamine salt of citric acid, a monoamine salt of itaconic acid, or a monoamine salt of tartaric acid is used as the blowing agent. 1. A method for producing a foamed molded article, which uses a combination of foam and sodium bicarbonate, and performs injection molding at a temperature equal to or higher than the decomposition temperature of the foaming agent.
JP57157339A 1982-09-08 1982-09-08 Manufacture of foam-molded article Granted JPS5945331A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57157339A JPS5945331A (en) 1982-09-08 1982-09-08 Manufacture of foam-molded article

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57157339A JPS5945331A (en) 1982-09-08 1982-09-08 Manufacture of foam-molded article

Publications (2)

Publication Number Publication Date
JPS5945331A true JPS5945331A (en) 1984-03-14
JPH0231737B2 JPH0231737B2 (en) 1990-07-16

Family

ID=15647522

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57157339A Granted JPS5945331A (en) 1982-09-08 1982-09-08 Manufacture of foam-molded article

Country Status (1)

Country Link
JP (1) JPS5945331A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61101537A (en) * 1984-10-23 1986-05-20 Mitsubishi Petrochem Co Ltd Method for producing painted thermoplastic resin foam moldings

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61101537A (en) * 1984-10-23 1986-05-20 Mitsubishi Petrochem Co Ltd Method for producing painted thermoplastic resin foam moldings

Also Published As

Publication number Publication date
JPH0231737B2 (en) 1990-07-16

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