JPH0729975B2 - Metal soap and thermoplastic resin composition containing the same - Google Patents
Metal soap and thermoplastic resin composition containing the sameInfo
- Publication number
- JPH0729975B2 JPH0729975B2 JP2335537A JP33553790A JPH0729975B2 JP H0729975 B2 JPH0729975 B2 JP H0729975B2 JP 2335537 A JP2335537 A JP 2335537A JP 33553790 A JP33553790 A JP 33553790A JP H0729975 B2 JPH0729975 B2 JP H0729975B2
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- Prior art keywords
- thermoplastic resin
- metal
- metal soap
- resin composition
- acid
- 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.)
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
本発明は、脂肪族カルボン酸と周期律表第II族金属の酸
化物又は水酸化物とを加熱直接反応させる、いわゆる乾
式直接法により製造される金属石鹸であって、含有する
金属量を理論量より過剰とした金属石鹸に関するもので
あり、更にこの金属成形物を熱可塑性樹脂に添加するこ
とにより、該熱可塑性樹脂の加工成形性、熱安定性を著
しく改善した熱可塑性樹脂組成物に関するものである。The present invention is a metal soap produced by a so-called dry direct method, in which an aliphatic carboxylic acid and an oxide or hydroxide of a Group II metal of the periodic table are directly reacted with heating, and the amount of metal contained is theoretical The present invention relates to a metal soap in excess of the amount thereof, and further relates to a thermoplastic resin composition in which the workability and heat stability of the thermoplastic resin is remarkably improved by adding the metal molded product to the thermoplastic resin. Is.
従来、熱可塑性樹脂の成形加工に際し、熱安定性、加工
性等を向上させるためにフエノール系酸化防止剤、有機
リン酸系酸化防止剤等とともに種々の金属石鹸が使用さ
れている。 現在使用されている代表的な金属石鹸としては、ステア
リン酸カルシウム、ステアリン酸マグネシウム、ステア
リン酸亜鉛、ステアリン酸アルミニウム、ステアリン酸
リチウム等である。 しかし、これらの従来の金属石鹸を使用しても、その成
形加工時に生じる金型での目ヤニ現象、金型壁あるいは
加工機壁へのプレート・アウト現象、スクリーンでの目
詰まり現象、さらには成形製品の表面に発生する添加剤
の吐出(浮き出し)現象等のトラブルに対しては未だ充
分に解決されているとはいえないのが現状である。Conventionally, various metal soaps have been used together with a phenol-based antioxidant, an organic phosphoric acid-based antioxidant and the like in order to improve thermal stability, processability and the like when molding a thermoplastic resin. Typical metal soaps currently used are calcium stearate, magnesium stearate, zinc stearate, aluminum stearate, lithium stearate and the like. However, even if these conventional metal soaps are used, the eye-dip phenomenon in the mold, the plate-out phenomenon to the mold wall or the machine wall, the clogging phenomenon on the screen, At present, it cannot be said that the problems such as the discharge (embossing) phenomenon of the additive generated on the surface of the molded product have been sufficiently solved.
そこで、これら諸トラブルを解決するための手段とし
て、種々の滑剤類の添加が試みられているが、未だ満足
すべき結果は得られていない。 そのため、現状ではこのようなトラブルが発生すると、
成形加工機の運転を一時止め、その箇所をクリーニング
した後、再運転している。このような処置を取るため、
長時間の連続成形加工ができず、作業性が低下するばか
りでなく、場合によっては成形製品の品質低下にもつな
がるので、これを早期に解決すべき対策の確立が要望さ
れていた。Therefore, addition of various lubricants has been attempted as a means for solving these problems, but satisfactory results have not yet been obtained. Therefore, at present, when such trouble occurs,
The molding machine is temporarily stopped, the area is cleaned, and then restarted. To take such measures,
Since continuous molding for a long time cannot be performed, workability is deteriorated, and in some cases, the quality of a molded product is deteriorated. Therefore, it has been demanded to establish a measure to solve this early.
本発明者らは、このような問題点を解決するべく鋭意研
究を進めた結果、乾式直接法で製造した期律表第II族の
金属であって、含有する金属量が反応当量より0.1〜1.0
モル過剰に含有する金属石鹸(1種の塩基性金属石鹸で
以下塩基性金属石鹸という)を開発し、この金属石鹸を
従来の金属石鹸に替えて、熱可塑性樹脂に添加使用する
ことにより、前記した諸トラブルを解消し、加工成形性
を改善するとともに、製品の品質低下を防ぐことに成功
し本発明を完成したものである。As a result of intensive studies to solve such problems, the present inventors have found that it is a Group II metal of the Periodic Table produced by the dry direct method, and the content of the metal is 0.1 to more than the reaction equivalent. 1.0
By developing a metal soap containing a molar excess (a kind of basic metal soap, hereinafter referred to as basic metal soap), and replacing this metal soap with a conventional metal soap and adding it to a thermoplastic resin, The present invention has been completed by eliminating the various problems described above, improving the workability and forming, and preventing the deterioration of product quality.
本発明の塩基性金属石鹸は、脂肪族モノカルボン酸(以
下脂肪酸という)と、周期律表第II族金属の酸化物又は
水酸化物(以下金属無機化合物という)とを、公知の製
造方法の一種である乾式直接法(別名熔融法)により加
熱反応させて得られるものであるが、公知の金属石鹸と
異なる点は、公知の金属石鹸が脂肪酸と反応当量の金属
無機化合物とを反応させるのに対して、本発明の塩基性
金属石鹸は脂肪酸と反応当量以上の過剰に金属無機化合
物を加えて、反応生成物が透明になるように完全反応さ
せて得られたもので、その生成物の金属含有量、融点、
酸価は自ずから異なるものである。 本発明の塩基性金属石鹸の金属含有量の過剰率は、0.1
〜1.0モルで、好ましくは0.1〜0.8である。0.1モル以下
では従来の金属石鹸とその性能にあまり差がなく、又1.
0モル以上では生成物の融液が透明にならず、未反応の
金属無機化合物が残存するので好ましくない。 本発明の塩基性金属石鹸の原料となる脂肪酸は炭素数12
〜30を有する天然又は合成の飽和又は不飽和のモノカル
ボン酸の1種以上で、構造中に側鎖、水酸基、ケトン
基、アルデヒド基、エポシキ基等があってもよい。 その代表例としては、ラウリン酸、ミリスチン酸、パル
ミチン酸、ステアリン酸、アラギン酸、ヘプタデシル
酸、ベヘン酸、オレイン酸、エライジン酸、エリカ酸、
リノール酸、リノレイン酸、リシノール酸、ヒドロキシ
ステアリン酸、モンタン酸、イソステアリン酸、エポキ
システアリン酸等が挙げられる。また、その一部を脂肪
族モノカルボン酸以外のカルボン酸又はジカルボン酸に
置き換えてもよい。 本発明の塩基性金属石鹸を構成する金属は、周期率表第
II族の金属の1種以上で、具体的にはIIaアルカリ土類
金属及びIIb亜鉛族金属を言い、好ましくはMg、Ca、Zn
である。 本発明の熱可塑性樹脂組成物は、熱可塑性樹脂に上記塩
基性金属石鹸を添加してなる組成物で、従来の金属石鹸
を添加した熱可塑性樹脂組成物では得られない成形加工
性を発揮する。 即ち、過剰な金属を含有する本発明の金属石鹸は、後記
実施例に示す如く、その融点が従来の金属石鹸に比し著
しく高くなるので、高温成形の熱可塑性樹脂において、
滑性効果並びに離型効果の向上を期待することができる
ものである。 本発明の乾式直接法の塩基性金属石鹸以外に、湿式沈澱
法によって塩基性金属石鹸を製造することもできるが、
この湿式沈澱法で製造した塩基性金属石鹸は、熱熔解す
ると塩基性部分の金属無機化合物が分離し、沈殿が生じ
る。また、この湿式沈澱法で製造した塩基性金属石鹸を
熱可塑性樹脂に添加して成形加工を行うと、金型での目
ヤニ現象は全く改善できないばかりでなく、逆にスクリ
ーンへの目詰まり現象が強く生じ、トラブルを助長する
欠点があり、本発明の塩基性金属石鹸とは性能的に比較
にならない。 本発明に用いる熱可塑性樹脂とは、熱可塑性を有する樹
脂で、例えば 塩素含有樹脂として、ポリ塩化ビニル、塩素化ポリ塩化
ビニル、塩素化ポリエチレン、塩化ビニル/酢酸ビニル
共重合体及びそれら樹脂と他樹脂との共重合体並びにポ
リマーブレンド、ポリオレフイン樹脂としては、低密度
ポリエチレン、高密度ポリエチレン、直鎖低密度ポリエ
チレン、ポリプロピレン及び樹脂相互、α−オレフイン
又は他樹脂との共重合体並びにポリマーブレンド。 各種のポリアミド樹脂及び他樹脂との共重合体並びにポ
リマーブレンド。 各種のポリエステル樹脂及び他樹脂との共重合体並びに
ポリマーブレンド。 各種のABS樹脂及び他樹脂共重合体並びにポリマーブレ
ンド。 各種のポリアセタール樹脂及び他樹脂との共重合体並び
にポリマーブレンド、その他各種エンジニアリングプラ
スチック類が挙げられる。 本発明組成物における塩基性金属石鹸の使用量は、熱可
塑性樹脂100重量部に対して、0.01〜5重量部で、好ま
しくは0.03〜3.0重量部である。 本発明の熱可塑性樹脂組成物には、上記の塩基性金属石
鹸以外に必要な添加物、例えば可塑剤、充填剤、安定
剤、酸化防止剤(フエノール系、有機リン系等)、紫外
線吸収剤(ベゾトリアゾール系、ベンゾフエノン系、ヒ
ンダードアミン系)、顔料、滑剤、帯電防止剤、防曇
剤、難燃剤、抗菌剤、防黴剤、発泡剤、エポキシ化合
物、加工助剤等を適宜添加してもよい。The basic metal soap of the present invention comprises an aliphatic monocarboxylic acid (hereinafter referred to as a fatty acid) and an oxide or hydroxide of a Group II metal of the periodic table (hereinafter referred to as a metal inorganic compound) according to a known production method. Although it is obtained by heating and reacting by a dry direct method (also known as melting method), which is different from known metal soaps, the difference between known metal soaps is that fatty acid reacts with a reaction equivalent of a metal inorganic compound. On the other hand, the basic metal soap of the present invention is obtained by adding a metal inorganic compound in excess of a reaction equivalent to a fatty acid and completely reacting the reaction product to make it transparent. Metal content, melting point,
The acid number is naturally different. The excess metal content of the basic metal soap of the present invention is 0.1
~ 1.0 mol, preferably 0.1-0.8. Below 0.1 mol, there is not much difference in performance from conventional metal soap, and 1.
When it is 0 mol or more, the melt of the product is not transparent, and unreacted metal-inorganic compound remains, which is not preferable. The fatty acid used as the raw material of the basic metal soap of the present invention has 12 carbon atoms
One or more kinds of natural or synthetic saturated or unsaturated monocarboxylic acid having 30 to 30 may have a side chain, a hydroxyl group, a ketone group, an aldehyde group, an epoxy group or the like in the structure. As typical examples thereof, lauric acid, myristic acid, palmitic acid, stearic acid, araginic acid, heptadecyl acid, behenic acid, oleic acid, elaidic acid, ericic acid,
Examples thereof include linoleic acid, linoleic acid, ricinoleic acid, hydroxystearic acid, montanic acid, isostearic acid, and epoxystearic acid. Further, a part thereof may be replaced with a carboxylic acid or a dicarboxylic acid other than the aliphatic monocarboxylic acid. The metal constituting the basic metal soap of the present invention has a periodic table
One or more Group II metals, specifically IIa alkaline earth metals and IIb zinc group metals, preferably Mg, Ca, Zn
Is. The thermoplastic resin composition of the present invention is a composition obtained by adding the above basic metal soap to a thermoplastic resin, and exhibits molding processability that cannot be obtained by a conventional thermoplastic resin composition to which a metal soap is added. . That is, since the melting point of the metal soap of the present invention containing an excessive amount of metal is remarkably higher than that of the conventional metal soap, as shown in Examples below, in a thermoplastic resin for high-temperature molding,
It is possible to expect an improvement in the sliding effect and the releasing effect. In addition to the dry direct method basic metal soap of the present invention, a basic metal soap can be produced by a wet precipitation method,
When the basic metal soap produced by this wet precipitation method is heated and melted, the metal inorganic compound in the basic portion is separated, and precipitation occurs. In addition, when the basic metal soap produced by this wet precipitation method is added to the thermoplastic resin and molding is performed, not only the phenomenon of eye blemishes in the mold cannot be improved, but conversely, the phenomenon of clogging of the screen occurs. Occurs, which is a problem that promotes troubles, and is not comparable in performance to the basic metal soap of the present invention. The thermoplastic resin used in the present invention is a resin having thermoplasticity, and examples of the chlorine-containing resin include polyvinyl chloride, chlorinated polyvinyl chloride, chlorinated polyethylene, vinyl chloride / vinyl acetate copolymers and other resins. Examples of copolymers and polymer blends with resins and polyolefin resins include low-density polyethylene, high-density polyethylene, linear low-density polyethylene, polypropylene and resins, copolymers with α-olefin or other resins, and polymer blends. Copolymers and polymer blends with various polyamide resins and other resins. Copolymers and polymer blends with various polyester resins and other resins. Various ABS resin and other resin copolymers and polymer blends. Examples include various polyacetal resins, copolymers with other resins, polymer blends, and various engineering plastics. The amount of the basic metal soap used in the composition of the present invention is 0.01 to 5 parts by weight, preferably 0.03 to 3.0 parts by weight, based on 100 parts by weight of the thermoplastic resin. The thermoplastic resin composition of the present invention contains necessary additives other than the above basic metal soaps, such as plasticizers, fillers, stabilizers, antioxidants (phenol-based, organic phosphorus-based, etc.) and ultraviolet absorbers. (Bezotriazole type, benzophenone type, hindered amine type), pigment, lubricant, antistatic agent, antifogging agent, flame retardant, antibacterial agent, antifungal agent, foaming agent, epoxy compound, processing aid, etc. Good.
以下実施例をあげて本発明をさらに具体的に説明する。 実施例 1 ステアリン酸(NV=200)100gを130℃に加熱し、攪拌し
ながら酸化亜鉛16.76gを徐々に加えた後、温度を150℃
に上げ、20分間攪拌を続けて熔解すると、透明な、亜鉛
含有量11.86重量%、融点130℃の、0.15MgO・Mg(C17H
35COO)2で表わされる酸化亜鉛として0.15モル過剰な
塩基性ステアリン酸亜鉛を得た。参考までに、このステ
アリン酸のNVに対応する酸化亜鉛で当量反応させて得た
Mg(C17H35COO)2で表わされる正塩(ノルマル塩)の
ステアリン酸亜鉛の亜鉛含有量は10.47重量%、融点は1
23℃であった。 実施例 2 12−ヒドロキシステアリン酸(NV=179)100gを120℃に
加熱後、攪拌しながら酸化マグネシウム10.06gを徐々に
加え、全量加え終わった後温度を165℃に上げ、20分間
攪拌を続けて反応を完結し、マグネシウム含有量5.8重
量%、融点228℃の、熔解すると透明な、0.4MgO・Mg(C
6H13・CH(OH)・C10H20・COO)2で表わされる酸化マ
グネシウムとして0.44モル過剰な塩基性12−ヒドロキシ
ステアリン酸マグネシウムを得た。 参考までに、この12−ヒドロキシステアリン酸のNVに対
応する酸化マグネシウムで当量反応させて得たMg(C6H
13・CH(OH・C10H20・COO)2で表わされる正塩(ノル
マル塩)の12−ヒドロキシステアリン酸マグネシウムの
マグネシウム含有量は3.7重量%、融点は143℃であっ
た。 実施例 3 ラウリン酸(NV=280)100gを125℃に加熱し、攪拌しな
がら水酸化カルシウム21.10gを徐々に加え、温度を175
℃まで上昇させ、20分間攪拌を続けて反応を完結させ、
カルシウム含有量10.03重量%、融点171℃の、熔解する
と透明な、0.115CaO・Ca(C11H23COO)2で表わされる
酸化カルシウムとして0.115モル過剰な塩基性ラウリン
酸カルシウムを得た。参考までに、このラウリン酸のNV
に対応する水酸化カルシウムで当量反応させて得たCa
(C11H23COO)2で表わされる正塩(ノルマル塩)のラ
ウリン酸カルシウムのカルシウム含有量は9.13重量%、
融点は155℃であった。 実施例 4 ベヘン酸(NV=167.26)100gを130℃に加熱後、攪拌し
ながら酸化マグネシウム11.45gを徐々に加えて反応さ
せ、徐々に温度を上げて175℃とする。熔解液が透明に
なるまで攪拌して反応を完結させ、マグネシウム含有量
6.34重量%、融点210℃の、0.8MgO・Mg(C21H43COO)2
で表わされる酸化マグネシウムとして0.8モル過剰な塩
基性ベヘン酸マグネシウムを得た。参考までに、このベ
ヘン酸のNVに対応する酸化マグネシウムで当量反応させ
て得たMg(C21H43COO)2で表わされる正塩(ノルマル
塩)のベヘン酸マグネシウムのマグネシウム含有量は3.
15重量%、融点は119℃であった。 実施例 5 下記配合物を160℃に調節した6インチの試験ロールで
5分間混練し、0.3mm厚のシートを作成した。このシー
トの一部を170℃に調節したギヤーオーブンに入れ、熱
安定性を比較し、残りのシートを170℃に調節した熱プ
レスで5分間プレスし、1mm厚のシートに成形し、その
シートの透明性及び70℃に調節した恒温水槽中に24時間
浸漬した後の表面の吐出(浮き出し)現象を観察した。
その結果を表−1の評点で評価し、表−2に示した。 <配合> PVC(=1000) 100 重量部 DOP(可塑剤) 40 〃 エポキシ化大豆油 2 〃 有機亜リン酸エステル 0.5 〃 ステアリン酸亜鉛 0.4 〃 金属石鹸(表−2) 0.6 〃 実施例 6 下記配合物を180℃に調節した試験ロールで7分間混練
し、0.5mm厚のシートを作成した。このシートを240℃に
調節した熱プレスで表−3に示す各温度で熱プレスして
1mm厚のシートに成形し、そのシートの着色度を東洋精
機製ホトボルト反射率測定器を用いて測定し、白度とし
て表−3に記載した。この数値は大きい程熱安定性が良
い) <配合> ポリプロピレン(MFR=0.3) 100 重量部 微粉末タルク 43 〃 酸化チタン 2 〃 イルガノックス1010 0.05 〃 金属石鹸(表−3) 0.2 〃 実施例 7 下記配合物を26φmm、L/D=16.5の単軸押出機(シリン
ダー温度:C1=150℃、C2=210℃、ダイス温度:230℃、
回転数:40rpm、スクリーン:200メッシュ、金型サイズ:3
0mm×1mm)で12時間連続押出しを行い、金型への目ヤニ
の付着量及びスクリーンへの目詰まり量を目測するとと
もに、押出機のモーター負荷を記録した。その結果を表
−4に示す。 <配合> ポリプロピレン(MFR=0.3) 100 重量部 微粉末タルク 43 〃 酸化チタン 2 〃 イルガノックス1010 0.1 〃 ウルトラノックス626 0.05 〃 金属石鹸(表−4) 0.3 〃 実施例 8 下記配合物を160℃に調節した6インチの試験ロールで
8分間混練し、1.2mm厚のシートを作成した。この時の
試験ロールからの剥離性を観察し、表−5に示した。こ
のシートを240℃に調節した熱プレスで2分間、5分
間、10分間の各時間で熱プレスし、それぞれ1mm厚のシ
ートに調製し、この熱変色したシートの白色度を東洋精
機製ホトボルト反射率測定機で測定し、その結果を表−
5に示す。 <配合> ABS樹脂(ダイヤペット3001MH) 100 重量部 ブロム系難燃剤(DB−101) 12 〃 三酸化アンチモン 5 〃 金属石鹸(表−5) 0.5 〃 Hereinafter, the present invention will be described more specifically with reference to examples. Example 1 100 g of stearic acid (NV = 200) was heated to 130 ° C., 16.76 g of zinc oxide was gradually added with stirring, and then the temperature was changed to 150 ° C.
When the solution is heated for 20 minutes and is melted by stirring, it is transparent and has a zinc content of 11.86% by weight, a melting point of 130 ° C., 0.15 MgO · Mg (C 17 H
As a zinc oxide represented by 35 COO) 2 , a 0.15 molar excess of basic zinc stearate was obtained. For reference, it was obtained by carrying out an equivalent reaction with zinc oxide corresponding to the NV of this stearic acid.
The zinc content of the normal salt (normal salt) zinc stearate represented by Mg (C 17 H 35 COO) 2 is 10.47% by weight and the melting point is 1.
It was 23 ° C. Example 2 After heating 100 g of 12-hydroxystearic acid (NV = 179) to 120 ° C., 10.06 g of magnesium oxide was gradually added to the mixture while stirring, and after the total amount was added, the temperature was raised to 165 ° C. and stirring was continued for 20 minutes. To complete the reaction, magnesium content 5.8% by weight, melting point 228 ° C, transparent when melted, 0.4MgO ・ Mg (C
As a magnesium oxide represented by 6 H 13 .CH (OH) .C 10 H 20 .COO) 2 , 0.44 mol excess of basic 12-hydroxystearate was obtained. For reference, Mg (C 6 H 6) obtained by reacting an equivalent amount of magnesium oxide corresponding to the NV of 12-hydroxystearic acid was used.
The magnesium salt of magnesium 12-hydroxystearate as a normal salt (normal salt) represented by 13 · CH (OH · C 10 H 20 · COO) 2 was 3.7% by weight, and the melting point was 143 ° C. Example 3 100 g of lauric acid (NV = 280) was heated to 125 ° C., 21.10 g of calcium hydroxide was gradually added with stirring, and the temperature was changed to 175.
Up to ℃ and continue stirring for 20 minutes to complete the reaction,
As a calcium oxide represented by 0.115CaO · Ca (C 11 H 23 COO) 2 , which had a calcium content of 10.03% by weight and a melting point of 171 ° C. and was transparent, 0.115 mol excess of basic calcium calcium laurate was obtained. For reference, this lauric acid NV
Ca obtained by the equivalent reaction with calcium hydroxide corresponding to
The normal salt (normal salt) represented by (C 11 H 23 COO) 2 has a calcium content of 9.13% by weight of calcium laurate.
The melting point was 155 ° C. Example 4 After heating 100 g of behenic acid (NV = 167.26) to 130 ° C., 11.45 g of magnesium oxide was gradually added thereto with stirring to cause reaction, and the temperature was gradually raised to 175 ° C. Stir until the melt becomes transparent to complete the reaction and
6.34% by weight, melting point 210 ℃, 0.8MgO ・ Mg (C 21 H 43 COO) 2
As a magnesium oxide represented by the formula, 0.8 molar excess of basic magnesium behenate was obtained. For reference, the magnesium content of magnesium behenate of the normal salt (normal salt) represented by Mg (C 21 H 43 COO) 2 obtained by reacting with an equivalent amount of magnesium oxide corresponding to the NV of behenic acid is 3.
The content was 15% by weight and the melting point was 119 ° C. Example 5 The following composition was kneaded with a 6-inch test roll adjusted to 160 ° C. for 5 minutes to prepare a 0.3 mm-thick sheet. A part of this sheet was placed in a gear oven adjusted to 170 ° C, the thermal stability was compared, and the remaining sheet was pressed with a hot press adjusted to 170 ° C for 5 minutes to form a 1 mm thick sheet. And the phenomenon of ejection (embossing) on the surface after immersion in a constant temperature water bath adjusted to 70 ° C for 24 hours.
The results were evaluated by the scores shown in Table-1 and shown in Table-2. <Compound> PVC (= 1000) 100 parts by weight DOP (plasticizer) 40〃 Epoxidized soybean oil 2〃 Organic phosphite 0.5〃 Zinc stearate 0.4〃 Metal soap (Table-2) 0.6〃 Example 6 The following composition was kneaded with a test roll adjusted to 180 ° C. for 7 minutes to prepare a 0.5 mm-thick sheet. This sheet was hot-pressed at 240 ° C and hot-pressed at each temperature shown in Table-3.
The sheet was formed into a sheet having a thickness of 1 mm, and the degree of coloring of the sheet was measured using a photovolt reflectance meter manufactured by Toyo Seiki, and the whiteness is shown in Table-3. The larger this value, the better the thermal stability.) <Compound> Polypropylene (MFR = 0.3) 100 parts by weight Fine powder talc 43 〃 Titanium oxide 2 〃 Irganox 1010 0.05 〃 Metal soap (Table-3) 0.2 〃 Example 7 A single screw extruder having the following composition of 26φ mm and L / D = 16.5 (cylinder temperature: C 1 = 150 ° C., C 2 = 210 ° C., die temperature: 230 ° C.,
Rotation speed: 40 rpm, screen: 200 mesh, mold size: 3
(0 mm x 1 mm) was continuously extruded for 12 hours, and the amount of adhesion of the resin to the mold and the amount of clogging to the screen were measured, and the motor load of the extruder was recorded. The results are shown in Table-4. <Compound> Polypropylene (MFR = 0.3) 100 parts by weight Fine powder talc 43 〃 Titanium oxide 2 〃 Irganox 1010 0.1 〃 Ultranox 626 0.05 〃 Metal soap (Table-4) 0.3 〃 Example 8 The following composition was kneaded with a 6-inch test roll adjusted to 160 ° C. for 8 minutes to prepare a 1.2 mm-thick sheet. The peelability from the test roll at this time was observed and shown in Table-5. This sheet was heat-pressed for 2 minutes, 5 minutes, and 10 minutes with a heat press adjusted to 240 ° C to prepare each sheet with a thickness of 1 mm, and the whiteness of this heat-discolored sheet was measured by Toyo Seiki Photobolt reflection. Measure with a rate measuring machine and display the results.
5 shows. <Compound> ABS resin (Diapet 3001MH) 100 parts by weight Brominated flame retardant (DB-101) 12〃 Antimony trioxide 5〃 Metal soap (Table-5) 0.5〃
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C07F 3/02 Z 7457−4H 3/04 7457−4H 3/06 7457−4H C08K 5/09 KAR (72)発明者 平松 恒之助 東京都中央区日本橋室町1―6―3 株式 会社耕正内 (56)参考文献 特開 昭55−136244(JP,A) 特開 平1−71836(JP,A)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display area C07F 3/02 Z 7457-4H 3/04 7457-4H 3/06 7457-4H C08K 5/09 KAR (72) Tsunenosuke Hiramatsu 1-6-3 Nihombashi Muromachi, Chuo-ku, Tokyo (56) References JP-A-55-136244 (JP, A) JP-A-1-71836 (JP, A)
Claims (6)
種または2種以上と周期律表第II族金属の酸化物または
水酸化物とを乾式直接法により加熱反応させて得られる
金属石鹸であって、その金属含有量が対応する当量より
0.1〜1.0モル過剰に含有する示性式〔1〕で表わされ、
熱熔解時に透明な粘稠体であることを特徴とする金属石
鹸。 示性式〔1〕 αMO・M(OOCR)2 〔式中、αは、0.1〜1.0の整数であり、Mは、周期律表
第II族の2価の金属であり、Rは、炭素数11〜29の飽和
または不飽和のアルキル基を表わす。〕1. An aliphatic monocarboxylic acid having 12 to 30 carbon atoms.
A metal soap obtained by heating and reacting one or more of them with an oxide or hydroxide of a Group II metal of the periodic table by a dry direct method, the metal content of which is higher than the corresponding equivalent weight.
Represented by the rational formula [1] containing 0.1 to 1.0 molar excess,
A metal soap characterized by being a viscous material which is transparent when melted by heat. Rational Formula [1] αMO · M (OOCR) 2 [wherein α is an integer of 0.1 to 1.0, M is a divalent metal of Group II of the periodic table, and R is the number of carbon atoms. It represents 11 to 29 saturated or unsaturated alkyl groups. ]
た金属の1種または2種以上のものである特許請求の範
囲第1項記載の金属石鹸。2. The metal soap according to claim 1, wherein the metal is one or more metals selected from Mg, Ca, Sr or Zn.
の範囲第1項および第2項のいずれかに記載された金属
石鹸の1種または2種以上を0.01〜5重量部添加してな
る熱可塑性樹脂組成物。3. To 100 parts by weight of a thermoplastic resin, 0.01 to 5 parts by weight of one or more kinds of the metal soaps described in any one of claims 1 and 2 are added. Thermoplastic resin composition.
許請求の範囲第3項記載の熱可塑性樹脂組成物。4. The thermoplastic resin composition according to claim 3, wherein the thermoplastic resin is a chlorine-containing resin.
ある特許請求の範囲第3項記載の熱可塑性樹脂組成物。5. The thermoplastic resin composition according to claim 3, wherein the thermoplastic resin is a polyolefin resin.
求の範囲第3項記載の熱可塑性樹脂組成物。6. The thermoplastic resin composition according to claim 3, wherein the thermoplastic resin is an ABS resin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2335537A JPH0729975B2 (en) | 1990-11-30 | 1990-11-30 | Metal soap and thermoplastic resin composition containing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2335537A JPH0729975B2 (en) | 1990-11-30 | 1990-11-30 | Metal soap and thermoplastic resin composition containing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04208246A JPH04208246A (en) | 1992-07-29 |
JPH0729975B2 true JPH0729975B2 (en) | 1995-04-05 |
Family
ID=18289685
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2335537A Expired - Lifetime JPH0729975B2 (en) | 1990-11-30 | 1990-11-30 | Metal soap and thermoplastic resin composition containing the same |
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JP (1) | JPH0729975B2 (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04331311A (en) * | 1991-01-24 | 1992-11-19 | Mitsubishi Electric Corp | Detecting apparatus of inter-vehicle distance |
JP4642169B2 (en) * | 1999-04-06 | 2011-03-02 | 日本合成化学工業株式会社 | Resin composition and laminate |
JP2000290457A (en) * | 1999-04-06 | 2000-10-17 | Nippon Synthetic Chem Ind Co Ltd:The | Resin composition and laminate |
JP4642170B2 (en) * | 1999-04-06 | 2011-03-02 | 日本合成化学工業株式会社 | Resin composition and laminate |
JP4728302B2 (en) * | 2007-08-31 | 2011-07-20 | 日本合成化学工業株式会社 | Resin composition and laminate |
JP5709362B2 (en) * | 2009-06-26 | 2015-04-30 | 日本合成化学工業株式会社 | Purging agent and purging method |
JP5875369B2 (en) * | 2011-12-28 | 2016-03-02 | ダンロップスポーツ株式会社 | Multi-piece golf ball |
JP5916380B2 (en) * | 2011-12-28 | 2016-05-11 | ダンロップスポーツ株式会社 | Golf ball resin composition and golf ball |
JP5916382B2 (en) | 2011-12-28 | 2016-05-11 | ダンロップスポーツ株式会社 | Golf ball resin composition and golf ball |
JP5875370B2 (en) | 2011-12-28 | 2016-03-02 | ダンロップスポーツ株式会社 | Multi-piece golf ball |
JP5916381B2 (en) * | 2011-12-28 | 2016-05-11 | ダンロップスポーツ株式会社 | Golf ball resin composition and golf ball |
JP6153295B2 (en) * | 2012-05-17 | 2017-06-28 | ダンロップスポーツ株式会社 | Golf ball |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2913592C2 (en) * | 1979-04-04 | 1988-11-10 | Chemische Werke München Otto Bärlocher GmbH, 8000 München | Process for producing metal soaps |
DE3728811A1 (en) * | 1987-08-28 | 1989-03-09 | Henkel Kgaa | METHOD FOR THE CONTINUOUS PRODUCTION OF FATTY ACID SOAPS |
-
1990
- 1990-11-30 JP JP2335537A patent/JPH0729975B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
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JPH04208246A (en) | 1992-07-29 |
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