JPS6136533B2 - - Google Patents

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Publication number
JPS6136533B2
JPS6136533B2 JP5550778A JP5550778A JPS6136533B2 JP S6136533 B2 JPS6136533 B2 JP S6136533B2 JP 5550778 A JP5550778 A JP 5550778A JP 5550778 A JP5550778 A JP 5550778A JP S6136533 B2 JPS6136533 B2 JP S6136533B2
Authority
JP
Japan
Prior art keywords
weight
salts
parts
fatty acid
foaming
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
Application number
JP5550778A
Other languages
Japanese (ja)
Other versions
JPS54148061A (en
Inventor
Hirohisa Oowada
Yasuhisa Okazaki
Tetsuya Sato
Nobuyuki Watabe
Koji Onoda
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.)
Myoshi Oil and Fat Co Ltd
Original Assignee
Myoshi Oil and Fat 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 Myoshi Oil and Fat Co Ltd filed Critical Myoshi Oil and Fat Co Ltd
Priority to JP5550778A priority Critical patent/JPS54148061A/en
Publication of JPS54148061A publication Critical patent/JPS54148061A/en
Publication of JPS6136533B2 publication Critical patent/JPS6136533B2/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、樹脂発泡剤の分解温度を適度に、確
実に、且つ迅速に調整、制御できる化学発泡助剤
に関するものである。 従来、各種樹脂、特に熱可塑性樹脂の発泡体製
造に於て作業上重要なポイントは、加熱時の低溶
融粘度化による発泡剤の分解ガスの逃散防止であ
り、この対策として例えばポリ塩化ビニル樹脂
(以下PVCと略す)の場合には可塑剤を配合して
ゲル化せしめ、又ポリオレフインの場合には、架
橋剤を添加したり、電子線による架橋を行なうと
いつた方法を用いているが、このような樹脂の粘
度調節とともに発泡剤の分解温度を適度に、確実
に、且つ迅速に調整・制御し、有効に分解ガスを
発生させることを重要となつてきている。かかる
目的のため従来、発泡助剤として尿素、尿素誘導
体等の尿素系、サリチル酸、ステアリン酸、ラウ
リン酸、フタル酸等の有機酸系、前述有機酸の亜
鉛塩、カルシウム塩、鉛塩、バリウム塩等の金属
塩系、亜鉛華、リサージ等の金属酸化物系及び、
グリセリン、エタノールアミン、エチレングリコ
ール等を用いている。しかしながらこれ等は発泡
剤の分解を助けはするが、他の欠点が多く、例え
ば尿素系発泡助剤は、ニトソロ系発泡剤であるジ
ニトロソペンタメチレンテトラミン(以下DPT
と略す)、アゾ系発泡剤であるアゾジカルボンア
ミド(以下ADCと略す)等と併用されるが、吸
湿性が高い。樹脂との相溶性が悪い、ブルーミン
グを起こしやすい等の大きな欠点があり実用商品
に用いるには、問題がある。また亜鉛華を用いる
と熱安定性の低下をきたし、有機酸のカルシウム
塩、バリウム塩は、プレートアウトに問題があ
り、エタノールアミンを用いると気泡が粗大とな
る。サリチル酸は、ゴム用でDPTと併用される
が異臭が激しく、ステアリン酸は製品表面にブリ
ードしやすい等の欠点がある。そこで本発明者ら
は、 (イ) 一般式() (式中R1、R2はそれぞれ5〜19、1〜10のアル
キル基)で示される総炭素数8〜22の分岐鎖脂
肪酸又は、該分岐鎖脂肪酸と一般式() R3−CH2−COOH ……() (式中R3は6〜20のアルキル基)で示されるる
総炭素数8〜22の直鎖脂肪酸との混合物で前者
を10重量%以上含有する混合脂肪酸。 (ロ) (イ)の脂肪酸と、マグネシウム、カルシウム、
バリウム、亜鉛、錫、鉛又はアルキル錫との
塩。 上記(イ)、(ロ)より選ばれたる一種又は二種以上を
発泡剤と併用することにより従来の発泡助剤の欠
点であつた吸湿性が高い、樹脂との相溶性が悪
い、ブルーミング、ブリードしやすい、熱安定性
の低下をきたす、異臭がある等の点を改良すると
ともに移行性、抽出性が小さい等の優れた性能を
有することを見い出した。 本発明に用いられる脂肪酸としては、α−オレ
フイン又はn−オレフインを原料とし、一酸化炭
素と水素とを副原料として、オキソ法によりアル
デヒド化した後、酸化して得られたものである。
また上記脂肪酸の塩を構成する金属としてはマグ
ネシウム、カルシウム、バリウム、亜鉛、錫、鉛
が挙げられ、又アルキル基としてはモノメチル
錫、モノブチル錫、モノオクチル錫、モノシクロ
ヘキシル錫、モノフエニル錫、モノベンジル錫、
ジメチル錫、ジブチル錫、ジオクチル錫、ジシク
ロヘキシル錫、ジフエニル錫、ジベンジル錫、ト
リメチル錫、トリブチル錫、トリオクチル錫、等
が挙げられる。 本発明発泡助剤と併用される発泡剤としては、
例えばDPT、ADC、P・P′−オキシビス(ベン
ゼンスルホニルヒドラジド)、N・N′−ジメチル
−N・N′−ジニトロソテレフタルイミド、ベン
ゼンスルホニルヒドラジド、P−トルエンスルホ
ニルヒドラジド、アゾビスイソブチロニトリル、
ニトロウレア、アセトン−P−トルエンスルホニ
ルヒラゾン、P−トルエンスルホニルアジド、
2・4−トルエンジスルホニルヒドラジド、P−
メチルウレタンベンゼンスルホニルヒドラジド、
トリニトロソトリメチレントリアミン、P−トル
エンスルホニルセミカルバジド、オキザリルヒド
ラジド、ニトログアニジン、ヒドラゾカルボニア
ミド、トリヒドラジノトリアジン等が挙げられ
る。 本発明発泡助剤は他の発泡助剤、発泡剤、顔
料、染料、螢光増白剤、充填剤、補強剤、整泡
剤、帯電防止剤、防曇剤、滑剤、可塑剤、酸化防
止剤、紫外線吸収剤、キレート剤、防炎剤、防燃
剤、電気絶縁性向上剤、安定剤、殺菌剤、着色
剤、架橋剤、香料、石油系軟化剤、老化防止剤等
の各種添加剤を目的、用途に応じて使用しても、
何ら本発明の効果は、損なわれない。 該発泡助剤は以下の方法によつて製造される。
即ち、マグネシウム、カルシウム、バリウム、亜
鉛等と脂肪酸との塩はオレフインのオキソ法によ
り得られる脂肪酸又はそのエステルと、金属水酸
化物、酸化物、弱酸塩との沈殿法(複分解法)、
溶融法、脂肪酸と金属粉末とを反応させる直接法
等により得られる。 また、錫、塩等と脂肪酸との塩は、無水有機溶
剤中で金属のアルコラート又は、塩化物と脂肪酸
を反応させて得られる。脂肪酸とアルキル錫との
反応物は、アルキル錫オキサイド又は、アルキル
錫低級脂肪酸エステルと脂肪酸との脱水反応又
は、交換反応等で得られる。以上の製法は単なる
一例であり、他の方法によつても製造が可能であ
るが、本発明はこれ等の製法によつて何等制限を
受けるものではない。 次に本発明を実施例により更に詳細に説明する
が、これ等実施例によつて本発明は何等制限され
るものではない。 実施例 1〜8 塩化ビニル樹脂(以下PVCと略す)を用い以
下に示す組成で配合した後、ヘンシルミキサーで
充分に混合し、更に5mm/Hgの減圧下で1時間脱
泡した。次いで脱泡調整したゾルをフエロ板上に
塗布し、150℃オーブン中で5分間ゲル化せしめ
た。このゲル化したシートを190℃で一定時間毎
に発泡せしめ、発泡体の一定時間毎の発泡倍率を
測定した結果を第一表に示した。 樹脂配合組成 PVC(日本ゼオン#25) 100 重量部 ジオクチルフタレート(DOP) 80 重量部 安定剤(エンビライザーT−508) 3 重量部 安定剤(エンビライザーSB−24) 0.5重量部 ADC 3 重量部 発泡助剤(第一表) 第一表に記載
The present invention relates to a chemical foaming aid that can appropriately, reliably, and quickly adjust and control the decomposition temperature of a resin foaming agent. Conventionally, an important point in the production of foams of various resins, especially thermoplastic resins, is to prevent the decomposed gas of the blowing agent from escaping by lowering the melt viscosity during heating. In the case of PVC (hereinafter abbreviated as PVC), a plasticizer is added to make it gel, and in the case of polyolefin, methods such as adding a crosslinking agent or crosslinking with electron beams are used. It has become important to adjust and control the decomposition temperature of the blowing agent appropriately, reliably, and quickly in addition to adjusting the viscosity of the resin to effectively generate decomposed gas. For this purpose, conventional foaming aids include urea-based agents such as urea and urea derivatives, organic acid-based agents such as salicylic acid, stearic acid, lauric acid, and phthalic acid, and zinc salts, calcium salts, lead salts, and barium salts of the aforementioned organic acids. metal salts such as zinc white, metal oxides such as litharge, and
Glycerin, ethanolamine, ethylene glycol, etc. are used. However, although these aid in the decomposition of the blowing agent, they have many other drawbacks; for example, urea-based blowing aids are nitrosopentamethylenetetramine (hereinafter referred to as DPT), which is a nitroso-based blowing agent.
It is used in combination with the azo foaming agent azodicarbonamide (hereinafter referred to as ADC), but it has high hygroscopicity. It has major drawbacks such as poor compatibility with resins and a tendency to cause blooming, which poses problems for use in practical products. Further, when zinc white is used, thermal stability decreases, when calcium salts and barium salts of organic acids are used, there is a problem with plate-out, and when ethanolamine is used, bubbles become coarse. Salicylic acid is used in conjunction with DPT for rubber, but it has a strong odor, and stearic acid has drawbacks such as the tendency to bleed onto the product surface. Therefore, the present inventors (a) General formula () (In the formula, R 1 and R 2 are alkyl groups of 5 to 19 and 1 to 10, respectively) or a branched chain fatty acid with a total of 8 to 22 carbon atoms and the general formula () R 3 -CH 2 A mixed fatty acid containing 10% by weight or more of the former in a mixture with a straight chain fatty acid having a total carbon number of 8 to 22 represented by -COOH () (in the formula, R 3 is an alkyl group of 6 to 20). (b) The fatty acids in (b), magnesium, calcium,
Salts with barium, zinc, tin, lead or alkyltin. By using one or more selected from (a) and (b) above in combination with a foaming agent, the drawbacks of conventional foaming aids such as high hygroscopicity, poor compatibility with resins, and blooming can be avoided. It has been found that it has improved the problems of easy bleeding, decreased thermal stability, and unpleasant odor, and has excellent performance such as low migration and extractability. The fatty acid used in the present invention is obtained by using α-olefin or n-olefin as a raw material, converting it into an aldehyde by the oxo method using carbon monoxide and hydrogen as auxiliary raw materials, and then oxidizing it.
Metals constituting the above fatty acid salts include magnesium, calcium, barium, zinc, tin, and lead, and alkyl groups include monomethyltin, monobutyltin, monooctyltin, monocyclohexyltin, monophenyltin, and monobenzyltin. tin,
Examples include dimethyltin, dibutyltin, dioctyltin, dicyclohexyltin, diphenyltin, dibenzyltin, trimethyltin, tributyltin, trioctyltin, and the like. As blowing agents used in combination with the blowing aid of the present invention,
For example, DPT, ADC, P・P′-oxybis(benzenesulfonylhydrazide), N・N′-dimethyl-N・N′-dinitrosoterephthalimide, benzenesulfonylhydrazide, P-toluenesulfonylhydrazide, azobisisobutyronitrile,
Nitrourea, acetone-P-toluenesulfonylhylazone, P-toluenesulfonyl azide,
2,4-Toluene disulfonyl hydrazide, P-
Methyl urethane benzenesulfonyl hydrazide,
Examples include trinitrosotrimethylenetriamine, P-toluenesulfonyl semicarbazide, oxalylhydrazide, nitroguanidine, hydrazocarboniamide, trihydrazinotriazine, and the like. The foaming aid of the present invention may include other foaming aids, blowing agents, pigments, dyes, fluorescent whitening agents, fillers, reinforcing agents, foam stabilizers, antistatic agents, antifogging agents, lubricants, plasticizers, and antioxidants. various additives such as UV absorbers, chelating agents, flame retardants, flame retardants, electrical insulation improvers, stabilizers, bactericidal agents, colorants, crosslinking agents, fragrances, petroleum softeners, and anti-aging agents. Even if you use it depending on the purpose and use,
The effects of the present invention are not impaired in any way. The foaming aid is produced by the following method.
That is, salts of magnesium, calcium, barium, zinc, etc. and fatty acids are obtained by precipitation of fatty acids or their esters obtained by the olefin oxo method and metal hydroxides, oxides, and weak acid salts (metathesis method);
It can be obtained by a melting method, a direct method of reacting a fatty acid with a metal powder, or the like. Salts of tin, salts, etc. and fatty acids can be obtained by reacting metal alcoholates or chlorides with fatty acids in an anhydrous organic solvent. The reaction product of a fatty acid and an alkyltin can be obtained by a dehydration reaction or an exchange reaction between an alkyltin oxide or an alkyltin lower fatty acid ester and a fatty acid. The above manufacturing method is merely an example, and manufacturing is possible by other methods, but the present invention is not limited in any way by these manufacturing methods. Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to these Examples in any way. Examples 1 to 8 Vinyl chloride resin (hereinafter abbreviated as PVC) was blended with the composition shown below, thoroughly mixed using a Henshil mixer, and further defoamed for 1 hour under reduced pressure of 5 mm/Hg. Next, the defoamed sol was applied onto a ferro plate and allowed to gel in an oven at 150°C for 5 minutes. This gelled sheet was foamed at 190°C at regular intervals, and the foaming ratio of the foam was measured at regular intervals. The results are shown in Table 1. Resin composition PVC (Nippon Zeon #25) 100 parts by weight Dioctyl phthalate (DOP) 80 parts by weight Stabilizer (Envirizer T-508) 3 Parts by weight Stabilizer (Envirizer SB-24) 0.5 parts by weight ADC 3 Parts by weight Foaming Auxiliary agent (Table 1) Listed in Table 1

【表】 実施例 9〜14 PVC100重量部、DOP80重量部、ADC3重量
部、バリウム〜亜鉛系液状安定剤3重量部、及び
発泡助剤(組成及び添加量は第二表に示した)と
からなる配合物を実施例1〜8と同様にして加工
した後、220℃で3分間発泡させた。得られた発
泡体を薄くスライスし、気泡の大きさを顕微鏡で
観察し、その結果を第二表に示した。
[Table] Examples 9 to 14 From 100 parts by weight of PVC, 80 parts by weight of DOP, 3 parts by weight of ADC, 3 parts by weight of barium-zinc liquid stabilizer, and foaming aid (composition and amount added are shown in Table 2). The formulation was processed in the same manner as in Examples 1 to 8 and then foamed at 220°C for 3 minutes. The obtained foam was sliced thinly and the size of the bubbles was observed under a microscope, and the results are shown in Table 2.

【表】【table】

【表】 実施例 15〜22 ABS樹脂を用いて以下に示す組成で配合した
混合物をヘンシルミキサーにより均一に撹拌した
後、シリンダー温度150℃及び160℃、ヘツド温度
160℃、ダイ温度160℃の30mm径の押出機を使用
し、スクリユーの回転速度50r.p.m.にて押出発泡
を行なつた。得られた発泡成型品の表面及び内部
発泡層の状態を観察し、第三表に結果を示した。 樹脂配合組成 ABS(サイコラツク) 100 重量部 安定剤(エンビライザーP#55) 2 重量部 ADC 0.5重量部 発泡助剤 第三表記載
[Table] Examples 15 to 22 A mixture of ABS resin and the composition shown below was uniformly stirred using a Henschel mixer, and the cylinder temperature was 150°C and 160°C, and the head temperature was
Extrusion foaming was carried out using a 30 mm diameter extruder with a die temperature of 160° C. and a screw rotation speed of 50 rpm. The surface and internal foam layer of the obtained foamed molded product were observed, and the results are shown in Table 3. Resin composition ABS (Cycolac) 100 parts by weight Stabilizer (Enbilizer P#55) 2 parts by weight ADC 0.5 parts by weight Foaming aid Listed in Table 3

【表】【table】

【表】 実施例 23〜30 添加量 PVC(日本ゼオン103EP) 100重量部 DOP 50重量部 安定剤(エンビライザーP#55) 2重量部 DPT 2重量部 発泡助剤 第四表に記載 上記配合物をヘンシルミキサーにてドライブレ
ンドした後160℃の2本カレンダーロールで0.5
m/mのシートを作成し、このシートについて下
記の試験を行なつた結果を第四表に示した。 試験方法 1 ブリード性試験 (i) 紫外線照射;10W殺菌灯×2本、試料片と
の間隔15cmで、30℃恒温中6時間照射 (ii) 高 湿;40℃×98%RH×120時間 ◎;ブリードなし △;ややブリードあり ×;激しいブリードあり の三段階で結果を判定し表示した。 2 耐熱安定性試験 190℃ギヤオーブン中で試料片が黄褐色に変
色するまでの時間(分)
[Table] Examples 23 to 30 Addition amount PVC (Nippon Zeon 103EP) 100 parts by weight DOP 50 parts by weight Stabilizer (Enbilizer P#55) 2 parts by weight DPT 2 parts by weight Foaming aid Listed in Table 4 Above formulation After dry blending with a Henshil mixer, 0.5% with two calendar rolls at 160℃
A m/m sheet was prepared, and the following tests were conducted on this sheet. The results are shown in Table 4. Test method 1 Bleeding test (i) Ultraviolet irradiation: irradiation with 2 x 10W germicidal lamps at 30℃ constant temperature with a distance of 15cm from the sample piece for 6 hours (ii) High humidity: 40℃ x 98% RH x 120 hours◎ The results were judged and displayed in three stages: no bleed △; slight bleed ×; severe bleed. 2 Heat resistance stability test Time (minutes) until sample piece changes color to yellowish brown in 190℃ gear oven

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 1 (イ) 一般式() (式中R1、R2はそれぞれ5〜19、1〜10のアル
キル基)で示される総炭素数8〜22の分岐鎖脂
肪酸又は該分岐鎖脂肪酸と一般式() R3−CH2−COOH ……() (式中R3は6〜20のアルキル基)で示される総
炭素数8〜22の直鎖脂肪酸との混合物で前者を
10重量%以上含有する混合脂肪酸。 (ロ) (イ)の脂肪酸と、マグネシウム、カルシウム、
バリウム、亜鉛、錫、鉛又はアルキル錫との
塩。 上記(イ)、(ロ)より選ばれたる一種又は二種以上を
用いることを特徴とする発泡助剤。
[Claims] 1 (a) General formula () (In the formula, R 1 and R 2 are alkyl groups of 5 to 19 and 1 to 10, respectively) or a branched chain fatty acid with a total carbon number of 8 to 22 and the general formula () R 3 -CH 2 - COOH...() (in the formula, R 3 is an alkyl group of 6 to 20) is a mixture with a straight chain fatty acid having a total of 8 to 22 carbon atoms.
Mixed fatty acids containing 10% or more by weight. (b) The fatty acids in (b), magnesium, calcium,
Salts with barium, zinc, tin, lead or alkyltin. A foaming aid characterized by using one or more selected from (a) and (b) above.
JP5550778A 1978-05-12 1978-05-12 Auxiliary foaming agent Granted JPS54148061A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5550778A JPS54148061A (en) 1978-05-12 1978-05-12 Auxiliary foaming agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5550778A JPS54148061A (en) 1978-05-12 1978-05-12 Auxiliary foaming agent

Publications (2)

Publication Number Publication Date
JPS54148061A JPS54148061A (en) 1979-11-19
JPS6136533B2 true JPS6136533B2 (en) 1986-08-19

Family

ID=13000577

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5550778A Granted JPS54148061A (en) 1978-05-12 1978-05-12 Auxiliary foaming agent

Country Status (1)

Country Link
JP (1) JPS54148061A (en)

Also Published As

Publication number Publication date
JPS54148061A (en) 1979-11-19

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