JPH0321643A - Foamable resin composition - Google Patents

Foamable resin composition

Info

Publication number
JPH0321643A
JPH0321643A JP1155813A JP15581389A JPH0321643A JP H0321643 A JPH0321643 A JP H0321643A JP 1155813 A JP1155813 A JP 1155813A JP 15581389 A JP15581389 A JP 15581389A JP H0321643 A JPH0321643 A JP H0321643A
Authority
JP
Japan
Prior art keywords
foaming
resin
blowing agent
weight
resin composition
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
JP1155813A
Other languages
Japanese (ja)
Inventor
Maki Horikoshi
堀越 真木
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP1155813A priority Critical patent/JPH0321643A/en
Publication of JPH0321643A publication Critical patent/JPH0321643A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/08Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/10Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
    • C08J9/102Azo-compounds
    • C08J9/103Azodicarbonamide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2201/00Foams characterised by the foaming process
    • C08J2201/02Foams characterised by the foaming process characterised by mechanical pre- or post-treatments
    • C08J2201/024Preparation or use of a blowing agent concentrate, i.e. masterbatch in a foamable composition
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2325/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Derivatives of such polymers
    • C08J2325/02Homopolymers or copolymers of hydrocarbons
    • C08J2325/04Homopolymers or copolymers of styrene
    • C08J2325/06Polystyrene

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、ヒケ防止用の微発泡を伴なう射出戊形に適し
た発泡性樹脂組成物に関するもので、特に発泡状態を改
良したスチレン系の発泡性樹脂組成物に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention relates to a foamable resin composition suitable for injection molding with fine foaming to prevent sink marks, and in particular to a styrene resin composition with improved foaming state. The present invention relates to a foamable resin composition of the type.

[従来の技術] 例えばOA機器のハウジング及びシャーシー等の構造部
材の射出成形においては、冷却時に金型内の樹脂が熱収
縮し、成形品にヒケと称される窪みや、収縮量のムラに
よるそり等が生じてしまうのを防止するため、発泡剤を
含む発泡性樹脂を射出成形し、成形時にわずかに内部発
泡させる、所謂低発泡射出戒形法や、予めガス体により
加圧された閉鎖形の型キャビティに射出し、射出後型キ
ャビティの圧力を開放することによって、未発泡の外殻
で包まれた発泡成形体を得る、所謂ガスカウンター成形
法等が用いられている。これらの主目的は、わずかでは
あるが発泡によって樹脂が膨張することを利用してヒケ
の発生を防止するものである。
[Prior Art] For example, in injection molding of structural members such as housings and chassis of OA equipment, the resin in the mold heat-shrinks during cooling, causing depressions called sink marks and uneven shrinkage in the molded product. In order to prevent warping, etc., we use the so-called low-foaming injection molding method, in which foamable resin containing a foaming agent is injection-molded and slightly foamed internally during molding, and closed molding that is pressurized with a gas in advance. A so-called gas counter molding method or the like is used, in which a foamed molded article surrounded by an unfoamed outer shell is obtained by injecting foam into a mold cavity of a shape and releasing the pressure in the mold cavity after injection. The main purpose of these is to prevent the occurrence of sink marks by utilizing the expansion of the resin due to foaming, albeit slightly.

ところで、上記射出戒形においては、大きく発泡させる
と、気泡が成形品の表面に露出して成形品の外観が損な
われるだけでなく、成形品の機械的強度も低下してしま
うことになる。特にガスカウンター成形法では、表面が
平滑な未発泡層を得ることが主目的であるため、気泡に
より外観が損われることは致命的欠陥となる。このため
、微発泡を伴なう射出成形に用いる発泡性樹脂組成物は
、発泡が比較的緩やかに行われるよう、調整されている
のが通常である。
By the way, in the above-mentioned injection molding, if the bubbles are expanded to a large extent, the air bubbles will be exposed on the surface of the molded product, which will not only impair the appearance of the molded product, but also reduce the mechanical strength of the molded product. In particular, in the gas counter molding method, the main purpose is to obtain an unfoamed layer with a smooth surface, so spoiling the appearance due to air bubbles is a fatal defect. For this reason, a foamable resin composition used for injection molding that involves microfoaming is usually adjusted so that foaming is performed relatively slowly.

従来、微発泡を伴なう射出成形に用いられる発泡性樹脂
組成物としては、クエン酸ソーダと重炭酸ソーダを混合
した発泡剤をスチレン系樹脂に配合したものが知られて
いる(特開昭62−89743号)。これは、発泡剤を
一時に急激に発泡させることなく、いわば二段に発泡さ
せることで、微細かつ均一な内部発泡状態を得ようとす
るものである。
Conventionally, as a foamable resin composition used for injection molding accompanied by micro-foaming, one in which a foaming agent mixed with sodium citrate and sodium bicarbonate is blended with a styrene resin is known (Japanese Patent Application Laid-Open No. 1983-1999). No. 89743). This is intended to achieve a fine and uniform internal foaming state by foaming the foaming agent in two stages, so to speak, without foaming the foaming agent rapidly at once.

また、特に微発泡を伴なう射出成形用に開発されたもの
ではないが、一般的な発泡剤として、アゾジカルボンア
ミド(以下rADcAJと記す)が知られている(特開
昭47−26406号)。
Additionally, azodicarbonamide (hereinafter referred to as rADcAJ) is known as a general foaming agent, although it has not been specifically developed for injection molding that involves microfoaming (Japanese Patent Laid-Open No. 47-26406). ).

[発明が解決しようとする課題] しかしながら、クエン酸ソーダと重炭酸ソーダとからな
る発泡剤を配合した従来のスチレン系の発泡性樹脂組成
物は、微発泡を伴なう射出成形によって、表面に気泡が
露出していない内部発泡の成形品は得られるが、比較的
多量の発泡剤を加えないと発泡させられず、発泡剤の消
費量が大きくなる問題がある。また、得られる発泡状態
もまだ満足できるほど微細であるとはいえないものであ
る。気泡が十分微細でないと、気泡の分布に偏りを生じ
やすく、特に成形品の肉厚が偏肉している場合、薄肉部
分が十分に発泡せず、ヒケ防止効果に確実性が得にくく
なるばかりか、成形品の強度にも偏りを生じやすくなる
問題を生じる。
[Problems to be Solved by the Invention] However, conventional styrene-based foamable resin compositions containing a blowing agent consisting of sodium citrate and sodium bicarbonate do not produce air bubbles on the surface due to injection molding accompanied by microfoaming. Although it is possible to obtain a molded article with internal foaming that is not exposed, foaming cannot be achieved unless a relatively large amount of blowing agent is added, and there is a problem that the amount of blowing agent consumed is large. Furthermore, the foamed state obtained cannot be said to be sufficiently fine. If the bubbles are not fine enough, the distribution of the bubbles tends to be uneven, and especially if the wall thickness of the molded product is uneven, the thin-walled areas will not foam sufficiently, making it difficult to achieve a reliable sink prevention effect. Otherwise, the problem arises that the strength of the molded product tends to be uneven.

一方、ADCAは、確かにポリオレフィンには適した発
泡剤ではあるが、断熱材等のように大きく発泡させる場
合にはよいが、微発泡を伴なうスチレン系樹脂の射出成
形に用いた場合、発泡が急激過ぎて、微細かつ均一な内
部発泡や薄肉での発泡はとても得られないものである。
On the other hand, ADCA is certainly a suitable blowing agent for polyolefins, and is good for large foams such as insulation materials, but when used in injection molding of styrenic resins, which involves fine foaming, The foaming is too rapid and it is difficult to achieve fine and uniform internal foaming or foaming in thin walls.

[課題を解決するための手段] 上記課題を解決するために本発明において講じられた手
段を説明すると、本発明では、アゾジカルボンアミド1
0重量部に対してクエン酸ソーダと重炭酸ソーダを各々
2〜8重量部加えた発泡剤をスチレン系樹脂に配合する
という手段を講じているものである。
[Means for Solving the Problems] To explain the means taken in the present invention to solve the above problems, in the present invention, azodicarbonamide 1
A method is taken in which a blowing agent in which 2 to 8 parts by weight of sodium citrate and sodium bicarbonate are each added to 0 parts by weight is blended into the styrene resin.

更に本発明を説明する。The present invention will be further explained.

本発明で用いるADCAとは、次の構造式を有するもの
をいう。
ADCA used in the present invention has the following structural formula.

00 本発明で用いる発泡剤は、上記ADCAにクエン酸ソー
ダと重炭酸ソーダを加えたものである。
00 The blowing agent used in the present invention is the above-mentioned ADCA plus sodium citrate and sodium bicarbonate.

その配合比率は、ADCA 1 0重量部に対して各々
2〜8重量部で、好ましくはADCA1 0重量部に対
して各々4〜6重量部である。
The mixing ratio thereof is 2 to 8 parts by weight per 10 parts by weight of ADCA, preferably 4 to 6 parts by weight per 10 parts by weight of ADCA.

ADCAの比率が少な過ぎると発泡が不足しがちとなり
、逆に多すぎると急激な発泡になりやすくなる。
If the ratio of ADCA is too low, foaming tends to be insufficient, whereas if it is too high, rapid foaming tends to occur.

クエン酸ソーダは、クエン酸モノソーダでもクエン酸ト
リソーダでもよいが、より微細な発泡状態が得やすいこ
とと、クエン酸モノソーダの場合に生じやすい黄褐色の
着色を生じないことから、クエン酸トリソーダが好まし
い。
Sodium citrate may be monosodium citrate or trisodium citrate, but trisodium citrate is preferred because it is easier to obtain a finer foamed state and does not cause the yellow-brown coloring that tends to occur when using monosodium citrate. .

本発明に係る発泡性樹脂組成物は、上記ADCAとクエ
ン酸ソーダと重炭酸ソーダの三成分からなる発泡剤をス
チレン系樹脂に配合したものである。
The foamable resin composition according to the present invention is a composition in which a blowing agent consisting of the above-mentioned ADCA, sodium citrate, and sodium bicarbonate is blended with a styrene resin.

本発明における発泡剤とスチレン系樹脂の配合割合は、
スチレン系樹脂100重量部に対して発泡剤0.1〜5
重量部、特に0.1〜1.0重量部であることが好まし
い。発泡剤の添加量が少な過ぎると発泡させにくく、逆
に多すぎると発泡過剰となって外観を損ないやすくなる
The blending ratio of the blowing agent and styrene resin in the present invention is as follows:
Foaming agent 0.1 to 5 per 100 parts by weight of styrene resin
It is preferably 0.1 to 1.0 parts by weight, particularly 0.1 to 1.0 parts by weight. If the amount of foaming agent added is too small, it will be difficult to foam, whereas if it is too large, excessive foaming will occur and the appearance will be easily impaired.

本発明で用いるスチレン系樹脂としては、ジエネラルバ
ーパスボリスチレンの他、射出成形可能なものであれば
、例えばハイインパクトボリスチレン、アクリロニトリ
ルースチレン共重合体、ABS樹脂等のようなスチレン
を含む共重合体であってもよい。
The styrene-based resin used in the present invention includes not only general bar-pass polystyrene but also polymers containing styrene such as high-impact polystyrene, acrylonitrile-styrene copolymers, ABS resins, etc., as long as they can be injection molded. It may also be a polymer.

本発明の樹脂組成物には上記発泡剤とスチレン系樹脂の
他、CaO等の発泡助剤、脂肪酸エステル等の発泡抑制
剤、滑剤、軟化剤、顔料等を加えることができる。
In addition to the above-mentioned foaming agent and styrene resin, the resin composition of the present invention may contain a foaming aid such as CaO, a foaming inhibitor such as a fatty acid ester, a lubricant, a softener, a pigment, and the like.

本発明におけるスチレン系樹脂と発泡剤の配合は、マス
ターバッチ方式によって行うことが好ましい。このマス
ターバッチの製造は、本発明の樹脂組成物を構成ずろス
ヂ1,/ン系樹脂と同種のスチ1ノン系樹脂を担休ポリ
マーとし、5−2 5重量%程度の高濃度と47:るよ
う、前述の発泡剤を添加混合することによって製造でき
る。
In the present invention, the styrenic resin and the blowing agent are preferably blended by a masterbatch method. This masterbatch is manufactured by using a stylinone resin, which is the same type as the stylinone resin that constitutes the resin composition of the present invention, as a supported polymer, and at a high concentration of about 5-25% by weight and 47% by weight. : It can be produced by adding and mixing the above-mentioned blowing agent.

本発明の樹脂組成物を用いで、微発泡を伴なう射出成形
を行うときの条件は、従来とほぼ同様である。即ち、射
出温度は180”−250゜C、射出LL力1丈4 0
 ”− 8 0 kg/cm2、背圧は10−3 0 
kl4/c:lll’稈L0である。
The conditions for performing injection molding with fine foaming using the resin composition of the present invention are almost the same as conventional ones. That is, the injection temperature is 180''-250°C, the injection LL force 1 length 40
”-80 kg/cm2, back pressure is 10-30
kl4/c:lll'culm L0.

1作 用] 第1図?J、、発泡剤の分解挙動を示すグラフで、図中
、(1)の曲線が八i’) C A 2重量部に対j,
,でクゴン酸−0ノソーダど@DI酸ソーダを各々1重
漬部添加した本発明(″′用いる発泡剤、(2)の曲線
がA D C: A 2重藏部(!対してク,エン酸1
・リソー・−ダと勇炭酸ソーダな名々1束風部添加した
本発明で・用いる発泡剤、(3)の曲綿がADCA甲、
独の発泡剤、(4)の曲線がクーLン酸モノソーダL本
炭酸ソーダを等以ずつ合せ”た発泡剤て−ある。測定は
、名究泡剤(1゛一流動バラフィン10mlを加え、温
序士昇2℃/分で行った。また、発泡剤は各々1gどし
た。
1 action] Figure 1? J., is a graph showing the decomposition behavior of a blowing agent. In the figure, the curve (1) is 8 i')
In the present invention, in which one part of each of sodium succinic acid and sodium DI acid was added (the foaming agent used, the curve (2) is A D C: A double part (!) enoic acid 1
・The foaming agent used in the present invention, in which one bundle of Lyso-da and Soda Carbonate is added, the bent cotton of (3) is ADCA A,
A German blowing agent, curve (4), is a blowing agent made by combining 100ml of monosodic acid and 300ml of sodium carbonate.Measurements were made using a famous foaming agent (10ml of monoliquid paraffin), The temperature was increased at 2°C/min.The blowing agent was added in an amount of 1g each.

第1図から明らかなように、本発明で用い′(′いる発
泡剤は、(3)の発泡剤に比し,て、低温側でのガス発
生量が多くか一つ低温側て・(4)の弁泡剤よりも緩や
かなガス発生をなすものとなっている。また、(4)の
発11タ剤に比して全ガス発生量ばか7ll−り多くな
ー)でいる4, ど1二ろで、本発明にお6づる発泡剤は、いわl:tr
(3)と(4)の発泡剤を名ぜたものであるにく)拘ら
ず、この両省のガス発9−゛特性をU1j純(こ合わセ
/、:ガス発生特性とは、なっていない。この,(1う
ir分I′ll1′半動を示す理南は必ずしく)明らか
で(ユないが、何らかのかたちで両者がガス発生を抑制
し合ってい、うたぬと推測きれる。−で.一シて、この
ような低温測{3″移行した緩やかな分解2¥−動が、
特j1Jスチ1・ン系樹脂に適したものとなっ“Cいる
と考λられる。
As is clear from Fig. 1, the blowing agent used in the present invention generates more gas on the low temperature side than the blowing agent (3). It generates gas more slowly than the valve foaming agent (4).In addition, the total amount of gas generated is 7 liters more than the foaming agent (4). The blowing agent according to the present invention is called l:tr.
Regardless of the names of the blowing agents in (3) and (4), the gas generation characteristics of these two sources are not defined as the pure gas generation characteristics. No. It is clear (not necessarily) that the two sides are suppressing each other's gas generation in some way, and it can be inferred that the two are suppressing each other's gas generation. Then, such a slow decomposition movement that transitioned to {3'' in temperature measurement is
It is considered to be particularly suitable for steel-based resins.

[実施例] 実施例1 3種類のハイ,インバク1・・ボリスヂ1/ンを成形対
?樹脂2・1,(“、微ウ?:泡な{′1′な)射出成
JT■な!行い、各々5f!@類0)厚さの板状成形品
を成形した。
[Example] Example 1 Three types of high, inbaku1, borisdine1/n were molded. Resin 2.1 (slightly foamy) injection molding was carried out to form plate-shaped molded products each having a thickness of 5 f!@class 0).

ハイイ゛7バク1・ボリスグ)ノンとしては、ボリスチ
!2・ンどボリブクジエンを95、2;4.8(単量体
の重量比二以下同じ)の割合で共重名させたもの(樹脂
A)、ボリスチレンとポリプタジエンを92:8の割合
で共重合させたもの(問脂B)  ボリスチレンとポリ
ブタジエンを94、5 : 5,5の割合で共屯音させ
たもの(樹脂C)の3 f!頬と1,たaまた、板状成
形品厚みは、7、5、3、2.5、2mmの5 f!類
とした。
Hii゛7 Baku1 Borisug) As a non-Boristi! Copolymerization of 2-nd polybutadiene at a ratio of 95:2:4.8 (monomer weight ratio of 2 or less) (resin A), and copolymerization of polystyrene and polyptadiene at a ratio of 92:8. (Resin B) Polystyrene and polybutadiene were combined in a ratio of 94.5:5.5 (Resin C). The thickness of the plate-shaped molded product is 7, 5, 3, 2.5, and 2mm. It was classified as a kind.

発泡剤は、ADCA2重風部に対して、クエン酸モノソ
ーダと重炭酸ソーダを各々j本量部加えたちの(発泡剤
I)とした。
The blowing agent was (Blowing Agent I) obtained by adding J parts of monosodium citrate and sodium bicarbonate to the ADCA double air section.

上記発泡剤は、ボリスチレンを担体ボリマーとして、2
0%のマスターバッチとし、発泡剤の添加量が0.24
重量%となるよう、このマスタ−バッヂを成形対象樹脂
と共に射出成形機に供給して成形を行った。
The above blowing agent contains polystyrene as a carrier polymer, and 2
The masterbatch is 0%, and the amount of blowing agent added is 0.24.
This master badge was supplied to an injection molding machine together with the resin to be molded, and molding was performed so as to achieve the same weight percentage.

得られた板状成形品につい″C′、発泡侶〒、平均セル
径、トル径分布、{ごル密摩,E 8、ノ/測:iEl
,た。
Regarding the obtained plate-shaped molded product, "C', foam size, average cell diameter, diameter distribution,
,Ta.

結果を第エ表〜第3表に示ず。* i:二、樹脂Cて・
成形した厚さ3mmの板状成形品の定泡状態をΔ2図に
示す。
The results are not shown in Tables E to Table 3. *i: 2. Resin C
Figure Δ2 shows the constant foam state of the plate-shaped molded product with a thickness of 3 mm.

尚、成形は、射出温度220℃、射出圧60kg/cn
+”、背圧20kg/cLl12で17 つた。
The molding was performed at an injection temperature of 220°C and an injection pressure of 60kg/cn.
17 at a back pressure of 20 kg/cL12.

実施例2 発泡剤を、ADCA2重量部にH L−C、ご7工ン酸
1・リソーダヒ重炭酸ソーダを各々1重量部加λ,たち
の(発泡剤II )とした以外ぱナ施例l):同様にし
て、発泡倍率、平均セル径、セル径分布、セル密度を各
々測定した。
Example 2 The blowing agent was 2 parts by weight of ADCA, 1 part by weight each of HLC and 1-lysodium bicarbonate added to 2 parts by weight of (foaming agent II): In the same manner, the foaming ratio, average cell diameter, cell diameter distribution, and cell density were each measured.

結果を第1〜3表に示す。また、樹脂C″r−成形し2
た厚さ3mmの板状成形品の発泡状態を第3図1こ示す
The results are shown in Tables 1-3. In addition, resin C″r-molded 2
Figure 3 shows the foamed state of a plate-shaped molded product with a thickness of 3 mm.

比較例1 樹脂八を成形列象樹脂どし7、クエン酸モノソーダと重
炭酸ソーダを等重量部ずつ白ぜた発泡削(発泡剤n+ 
)を用い、射出温度を220゜Cど230℃として成形
した以外は実施例1と同様にして、厚さ3及び2mmの
板状成形品の成形を行った。  得られた板状成形品に
ついて、発泡倍率、平均セル径、セル径分布、セル密度
を各々測定しようとしたが、実施例1及び2と同量の発
泡剤■を加えているにも拘らず発泡しておらず、これら
の測定はできなかった。
Comparative Example 1 Resin 8 was molded with resin 7, foamed shavings made by whitening equal parts by weight of monosodium citric acid and sodium bicarbonate (foaming agent n+
) and the injection temperature was 220° C. to 230° C. The same procedure as in Example 1 was used to mold plate-shaped molded products with thicknesses of 3 and 2 mm. We attempted to measure the expansion ratio, average cell diameter, cell diameter distribution, and cell density of the obtained plate-shaped molded product, but despite adding the same amount of foaming agent (■) as in Examples 1 and 2, There was no foaming, so these measurements were not possible.

結果を第1表に示す。The results are shown in Table 1.

比較例2 ADCA単独の発泡剤(発泡剤IV)を使用し、成形対
象樹脂への発泡剤配合割合を0.18%とした以外は実
施例lと同様にして、樹脂Aについては厚さ7、5及び
3 am,樹脂B及びCについては厚さ7、5、3、2
、5及び2mmの板状成形品を成形した。
Comparative Example 2 Resin A was made in the same manner as in Example 1, except that ADCA alone as a blowing agent (Blowing Agent IV) was used and the proportion of the blowing agent in the resin to be molded was 0.18%. , 5 and 3 am, thicknesses 7, 5, 3, 2 for resins B and C.
, 5 and 2 mm plate-shaped molded products were molded.

得られた板状成形品について、発泡倍率、平均セル径、
セル径分布、セル密度を各々測定した。
Regarding the obtained plate-shaped molded product, the expansion ratio, average cell diameter,
Cell diameter distribution and cell density were each measured.

結果を第1表〜第3表に示す。また、樹脂Cで成形した
厚さ3au++の板状成形品の発泡状態を第4図に示す
The results are shown in Tables 1 to 3. Further, the foamed state of a plate-shaped molded product molded from resin C and having a thickness of 3 au++ is shown in FIG.

[発明の効果] 本発明は、以−1二説明した通りのものであり、微発泡
を伴なう躬出成形において、十分に微小な気泡を形成で
きるので、発泡によるヒケ防止効果が確実で、また成形
品の機械的強度の偏りも生じにくいものである。
[Effects of the Invention] The present invention is as explained below, and since sufficiently small bubbles can be formed in extrusion molding accompanied by microfoaming, the effect of preventing sinkage due to foaming is reliable. Also, the mechanical strength of the molded product is less likely to be uneven.

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

第1図は発泡剤の分解特性を示すグラフ、第2図(,j
実施例1にお4Jる樹脂Cで成形した厚さ3mmの板状
成形品の気1(1状態を示す図、第3図は実施例21・
ごお61 4州剤脂Cで成形した厚さ3111+11の
板状成形品の気泡状態を示す図、第4図は比較例2にお
ける樹脂Cで成形した厚さ3開の板状成形品の気泡状態
を示す図である。
Figure 1 is a graph showing the decomposition characteristics of blowing agents, Figure 2 (,j
Figure 3 is a diagram showing a 3 mm thick plate-shaped molded product molded with 4J resin C in Example 1 (1 state, and FIG. 3 is a diagram showing Example 21.
Figure 4 shows the air bubbles in a plate-shaped molded product with a thickness of 3111+11 molded with Resin C in Comparative Example 2. It is a figure showing a state.

Claims (1)

【特許請求の範囲】[Claims] 1)アゾジカルボンアミド10重量部に対してクエン酸
ソーダと重炭酸ソーダを各々2〜8重量部加えた発泡剤
がスチレン系樹脂に配合されていることを特徴とする発
泡性樹脂組成物。
1) A foamable resin composition characterized in that a foaming agent containing 2 to 8 parts by weight of sodium citrate and sodium bicarbonate each added to 10 parts by weight of azodicarbonamide is blended into a styrene resin.
JP1155813A 1989-06-20 1989-06-20 Foamable resin composition Pending JPH0321643A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1155813A JPH0321643A (en) 1989-06-20 1989-06-20 Foamable resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1155813A JPH0321643A (en) 1989-06-20 1989-06-20 Foamable resin composition

Publications (1)

Publication Number Publication Date
JPH0321643A true JPH0321643A (en) 1991-01-30

Family

ID=15614035

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1155813A Pending JPH0321643A (en) 1989-06-20 1989-06-20 Foamable resin composition

Country Status (1)

Country Link
JP (1) JPH0321643A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003080549A (en) * 2001-09-11 2003-03-19 Kanegafuchi Chem Ind Co Ltd Manufacturing method of thermoplastic resin molded product
JP2005324423A (en) * 2004-05-13 2005-11-24 Toyoda Gosei Co Ltd Manufacturing method of foam molded article
WO2007129925A1 (en) * 2006-05-09 2007-11-15 Termo Organika Sp. Z.O.O. Modified foamable and foamed materials and the method of obtaining such materials
JP2015054935A (en) * 2013-09-12 2015-03-23 ソマール株式会社 Adhesive composition and adhesive sheet
CN105131501A (en) * 2015-09-06 2015-12-09 贵州省材料产业技术研究院 Foaming master batch for ABS microcellular foaming material and preparation method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003080549A (en) * 2001-09-11 2003-03-19 Kanegafuchi Chem Ind Co Ltd Manufacturing method of thermoplastic resin molded product
JP2005324423A (en) * 2004-05-13 2005-11-24 Toyoda Gosei Co Ltd Manufacturing method of foam molded article
WO2007129925A1 (en) * 2006-05-09 2007-11-15 Termo Organika Sp. Z.O.O. Modified foamable and foamed materials and the method of obtaining such materials
JP2015054935A (en) * 2013-09-12 2015-03-23 ソマール株式会社 Adhesive composition and adhesive sheet
CN105131501A (en) * 2015-09-06 2015-12-09 贵州省材料产业技术研究院 Foaming master batch for ABS microcellular foaming material and preparation method thereof

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