JPH04220458A - Resin composition for blow molding - Google Patents

Resin composition for blow molding

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Publication number
JPH04220458A
JPH04220458A JP40439090A JP40439090A JPH04220458A JP H04220458 A JPH04220458 A JP H04220458A JP 40439090 A JP40439090 A JP 40439090A JP 40439090 A JP40439090 A JP 40439090A JP H04220458 A JPH04220458 A JP H04220458A
Authority
JP
Japan
Prior art keywords
blow molding
weight
nylon
copper
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.)
Granted
Application number
JP40439090A
Other languages
Japanese (ja)
Other versions
JP3140471B2 (en
Inventor
Itaru Natori
名取 至
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 JP02404390A priority Critical patent/JP3140471B2/en
Publication of JPH04220458A publication Critical patent/JPH04220458A/en
Application granted granted Critical
Publication of JP3140471B2 publication Critical patent/JP3140471B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To provide a resin composition for blow molding excellent in melt tension and a good blow molding produced therefrom. CONSTITUTION:A polyamide resin is mixed with an adduct of a copolymer comprising an aromatic vinyl compound (X) and a hydrogenated conjugated diene compound (Y) with an alpha,beta-unsaturated carboxylic acid or its derivative, another thermoplastic resin, and a glass fiber, wherein 38<X<80, 20<Y<62, and X+Y=100 [wherein X (wt.%) and Y (wt.%) are the amounts of components (X) and (Y), respectively].

Description

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

【0001】0001

【産業上の利用分野】本発明はポリアミド樹脂組成物に
関するものである。詳しくは、ブロー成形用のポリアミ
ド樹脂組成物に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to polyamide resin compositions. Specifically, the present invention relates to a polyamide resin composition for blow molding.

【0002】0002

【従来の技術】ポリアミド樹脂は、機械的特性,耐薬品
性,加工性等にすぐれた樹脂であり、幅広い用途に使用
されてはいるが、溶融粘度のせん断速度依存性が小さく
、滞留時の粘度低下が大きく、溶融張力が小さいなどと
いう、ブロー成形用材料として用いようとした場合に、
均一な肉厚をもった製品を、安定して生産することがで
きないという、きわめて重大な欠点を有している。
[Prior Art] Polyamide resin is a resin with excellent mechanical properties, chemical resistance, processability, etc., and is used in a wide range of applications, but the dependence of melt viscosity on shear rate is small and When trying to use it as a material for blow molding, it has a large viscosity drop and low melt tension.
This method has a very serious drawback in that it is not possible to stably produce products with uniform wall thickness.

【0003】すなわち、ブロー成形用材料として要求さ
れる性能しては、溶融粘度が高いことのみならず、生産
性という意味からは、成形機内では溶融粘度がなるべく
低く、パリソンを形成する時点では溶融粘度が高いこと
が必要であり、また、ドロータウンを防ぐという意味か
らは、滞留時の粘度低下が小さいことが必要であり、パ
リソンにガスを吹き込み、均一な肉厚をもった製品とす
るためには溶融張力が必要であるが、ポリアミド樹脂は
いずれの性能も不十分である。
In other words, the performance required for a material for blow molding is not only high melt viscosity, but also from the perspective of productivity, the melt viscosity should be as low as possible in the molding machine, and the melt viscosity should be as low as possible at the time of forming the parison. It is necessary to have high viscosity, and in order to prevent draw town, it is necessary that the decrease in viscosity during retention is small. Melt tension is required for this purpose, but polyamide resins are insufficient in both properties.

【0004】この欠点を改良するために、従来より数多
くの検討がなされてきた(特開昭53−101048号
公報、特開昭55−12082号公報、特開昭60−1
70664号公報、特開昭60−171133号公報、
特開昭62−290725号公報など)。しかしながら
、これらの組成物においても、いくらかの改良は見られ
るものの、いまだ溶融粘度のせん断速度依存性が小さく
、滞留時の分解ガス、ゲル化などの好ましからざる現象
が見られるなど、数多くの解決すべき問題点を有してい
る。
[0004] In order to improve this drawback, many studies have been made in the past (Japanese Unexamined Patent Publications No. 101048/1982, No. 12082/1982, Japanese Unexamined Patent Publications No. 60/1982).
Publication No. 70664, Japanese Unexamined Patent Publication No. 171133/1983,
(Japanese Patent Application Laid-Open No. 62-290725, etc.). However, although some improvements have been made in these compositions, there are still many unresolved problems, such as the small dependence of melt viscosity on shear rate and unfavorable phenomena such as decomposition gas and gelation during retention. There are some issues that need to be addressed.

【0005】[0005]

【発明が解決しようとする課題】本発明は、ポリアミド
樹脂をブロー成形用材料として使用しようとする場合の
上記問題点のうち、溶融張力の高いすぐれたブロー成形
用材料を提供し、さらにこれらから製造された良好なブ
ロー中空成形品を提供するという課題を解決するもので
ある。
SUMMARY OF THE INVENTION The present invention provides an excellent blow molding material with high melt tension, which solves the above-mentioned problems when polyamide resin is used as a blow molding material, and also solves the above problems. This solves the problem of providing a well-produced blow hollow molded product.

【0006】[0006]

【課題を解決するための手段】本発明者は、上記課題を
解決するために研究を重ねた結果、ポリアミド樹脂に、
特定の熱可塑性樹脂を、特定の比率にて配合した場合に
のみ上記課題を解決できることを見い出し本発明を完成
した。すなわち本発明は、 (A)ポリアミド樹脂 (B)芳香族ビニル化合物(X)と共役ジエン化合物の
水素化物(Y)からなる共重合体のα,β−不飽和カル
ボン酸又はその誘導体の付加物 (C)他の熱可塑性樹脂 (D)ガラス繊維 (ただし、(A)、(B)、(C)、(D)各成分の配
合量をそれぞれ、A、B、C、D重量%とするとき、6
0≦A≦97,3≦B+C≦40,0.01≦B/C≦
99,0.05≦D/(A+B+C)≦1,A+B+C
+D=100;(X),(Y)各成分の共重合量をそれ
ぞれ、X,Y重量%とするとき、38<X<80,20
<Y<62,X+Y=100)であることを特徴とする
ブロー成形用樹脂組成物である。
[Means for Solving the Problems] As a result of repeated research in order to solve the above problems, the present inventor has discovered that polyamide resin has the following properties:
The present invention has been completed by discovering that the above problem can be solved only when a specific thermoplastic resin is blended in a specific ratio. That is, the present invention provides an adduct of an α,β-unsaturated carboxylic acid or a derivative thereof of a copolymer consisting of (A) a polyamide resin (B) an aromatic vinyl compound (X) and a hydride of a conjugated diene compound (Y). (C) Other thermoplastic resin (D) Glass fiber (however, the blending amounts of each component (A), (B), (C), and (D) are A, B, C, and D weight percent, respectively) Time, 6
0≦A≦97, 3≦B+C≦40, 0.01≦B/C≦
99, 0.05≦D/(A+B+C)≦1, A+B+C
+D=100; When the copolymerization amounts of each component (X) and (Y) are X and Y weight%, respectively, 38<X<80, 20
<Y<62, X+Y=100).

【0007】本発明において、成分(A)であるポリア
ミド樹脂とは、ナイロン4,ナイロン6,ナイロン8,
ナイロン9,ナイロン10,ナイロン11,ナイロン1
2,ナイロン46,ナイロン66,ナイロン610,ナ
イロン612,ナイロン636,ナイロン1212など
の脂肪族ポリアミド樹脂や、ナイロン4T(T:テレフ
タル酸),ナイロン4I(I:イソフタル酸),ナイロ
ン6T,ナイロン6I,ナイロン12T,ナイロン12
Iなどの芳香族ポリアミド樹脂や、これらの共重合体、
ブレンドなどを例示することができる。
In the present invention, the polyamide resin as component (A) includes nylon 4, nylon 6, nylon 8,
Nylon 9, Nylon 10, Nylon 11, Nylon 1
2. Aliphatic polyamide resins such as nylon 46, nylon 66, nylon 610, nylon 612, nylon 636, nylon 1212, nylon 4T (T: terephthalic acid), nylon 4I (I: isophthalic acid), nylon 6T, nylon 6I , nylon 12T, nylon 12
Aromatic polyamide resins such as I and copolymers thereof,
Examples include blends.

【0008】これらのポリアミド樹脂は、数平均分子量
5,000〜100,000のものが好ましく、8,0
00〜50,000のものがより好ましく、10,00
0〜30,000のものが最も好ましい。数平均分子量
が5,000以下であると、組成物とした場合に十分な
溶融粘度が得られない。数平均分子量が100,000
以上であると、初期の溶融粘度は高いものの、滞留時の
粘度低下が大きく好ましくない。
These polyamide resins preferably have a number average molecular weight of 5,000 to 100,000, with a number average molecular weight of 8.0 to 100,000.
00 to 50,000 is more preferable, and 10,00
0 to 30,000 is most preferred. When the number average molecular weight is 5,000 or less, sufficient melt viscosity cannot be obtained when used as a composition. Number average molecular weight is 100,000
If it is above, although the initial melt viscosity is high, the viscosity decreases greatly during residence, which is not preferable.

【0009】本発明において、成分(B)である、芳香
族ビニル化合物(X)と共役ジエン化合物の水素化物(
Y)からなる共重合体の、α,β−不飽和カルボン酸又
はその誘導体の付加物とは、芳香族ビニル化合物、例え
ばスチレン,α−メチルスチレン,ビニルトルエンなど
の化合物と、共役ジエン化合物、例えばブタジエン,イ
ソプレン,1,3−ペンタジエンなどの化合物の水素化
物からなる共重合体、好ましくはスチレンとブタジエン
の水素化物からなる共重合体に、α,β−不飽和カルボ
ン酸又はその誘導体が付加した共重合体を示す。
In the present invention, component (B), a hydride of an aromatic vinyl compound (X) and a conjugated diene compound (
The adduct of α,β-unsaturated carboxylic acid or its derivative of the copolymer consisting of Y) is an aromatic vinyl compound, such as a compound such as styrene, α-methylstyrene, or vinyltoluene, and a conjugated diene compound, For example, an α,β-unsaturated carboxylic acid or a derivative thereof is added to a copolymer of a hydride of a compound such as butadiene, isoprene, or 1,3-pentadiene, preferably a copolymer of a hydride of styrene and butadiene. This shows the copolymer.

【0010】ここで用いられるα,β−不飽和カルボン
酸又はその誘導体としては、マレイン酸,無水マレイン
酸,マレイン酸モノメチルエステル,マレイン酸モノメ
チルエステルの金属塩,フマル酸,フマル酸モノメチル
エステル,コハク酸,無水コハク酸,イタコン酸,アク
リル酸,メタクリル酸,ハイミック酸,無水ハイミック
酸,クロトン酸,フタル酸,無水フタル酸,メタクリル
酸の金属塩,アクリル酸の金属塩,マレイミド,フタル
イミド,グリシジルメタクリレート,グリシジルアクリ
レート,アリルグリシジルエーテル,ビニルグリシジル
エーテル,グリシジルイタコネートなどを例示すること
ができる。
The α,β-unsaturated carboxylic acids or derivatives thereof used here include maleic acid, maleic anhydride, maleic acid monomethyl ester, metal salts of maleic acid monomethyl ester, fumaric acid, fumaric acid monomethyl ester, and succinic acid. Acid, succinic anhydride, itaconic acid, acrylic acid, methacrylic acid, himic acid, himic anhydride, crotonic acid, phthalic acid, phthalic anhydride, metal salts of methacrylic acid, metal salts of acrylic acid, maleimide, phthalimide, glycidyl methacrylate , glycidyl acrylate, allyl glycidyl ether, vinyl glycidyl ether, glycidyl itaconate, and the like.

【0011】特に好ましいのは無水マレイン酸である。 α,β−不飽和カルボン酸又はその誘導体の上記共重合
体への付加量は、0.01〜20mol%の範囲が好ま
しく、特に0.05〜10mol%の範囲が好ましい。 付加量が0.01mol%以下であると、ポリアミドに
対する混和性が見られず、成形品に相ハクリが見られる
などの好ましからざる結果を与える。
Particularly preferred is maleic anhydride. The amount of α,β-unsaturated carboxylic acid or its derivative added to the copolymer is preferably in the range of 0.01 to 20 mol%, particularly preferably in the range of 0.05 to 10 mol%. If the amount added is less than 0.01 mol %, miscibility with polyamide is not observed and unfavorable results such as phase peeling are observed in the molded product are produced.

【0012】付加量が20mol%以上であると、ポリ
アミドの着色、ゲル化などが起こり好ましくない。本発
明において、成分(B)の、芳香族ビニル化合物(X)
と共役ジエンの水素化物(Y)の共重合量をそれぞれX
,Y重量%とするとき、38<X<80,20<Y<6
2(X+Y=100)の範囲が好ましく、38<X<7
0,30<Y<62(X+Y=100)の範囲が特に好
ましく、38<X<60,40<Y<62(X+Y=1
00)の範囲が最も好ましい。
[0012] If the amount added is 20 mol % or more, coloring and gelation of the polyamide occur, which is undesirable. In the present invention, the aromatic vinyl compound (X) of component (B)
The amount of copolymerization of hydride (Y) of conjugated diene and
, Y weight%, 38<X<80, 20<Y<6
The range of 2(X+Y=100) is preferable, and 38<X<7
The range of 0,30<Y<62 (X+Y=100) is particularly preferable, and the range of 38<X<60,40<Y<62 (X+Y=1
00) is most preferred.

【0013】芳香族ビニル化合物(X)の共重合量がX
≦38もしくはX≧80(Y≦20もしくはY≧62)
となると、組成物とした場合に十分な溶融粘度が得られ
ず好ましくない。本発明において、成分(C)である他
の熱可塑性樹脂とは、成分(B)以外のオレフィン系ポ
リマー、ポリフェニレンエーテルから選択される少くな
とも1種の熱可塑性樹脂である。
[0013] The amount of copolymerization of the aromatic vinyl compound (X) is
≦38 or X≧80 (Y≦20 or Y≧62)
In this case, a sufficient melt viscosity cannot be obtained when the composition is prepared, which is not preferable. In the present invention, the other thermoplastic resin as component (C) is at least one thermoplastic resin selected from olefin polymers and polyphenylene ether other than component (B).

【0014】上記成分(B)以外のオレフィン系ポリマ
ーとしては、結晶性ポリオレフィン(例えば、ポリエチ
レン、ポリプロピレンなど)、熱可塑性エラストマー(
例えば、スチレン−ブタジエン共重合体、スチレン−イ
ソプレン共重合体あるいはこれらの水素化物、1,2−
ポリブタジエンなど)、末端にのみ酸無水基を有するオ
レフィン系ポリマー(例えば本発明者が、WO89−0
8120にて提案した重合体)などが挙げられる。
Olefinic polymers other than the above component (B) include crystalline polyolefins (eg, polyethylene, polypropylene, etc.), thermoplastic elastomers (
For example, styrene-butadiene copolymer, styrene-isoprene copolymer or their hydrides, 1,2-
polybutadiene, etc.), olefinic polymers having acid anhydride groups only at the terminals (for example, the present inventor has
8120) and the like.

【0015】本発明に用いられる結晶性ポリオレフィン
,熱可塑性エラストマー,ポリフェニレンエーテルには
、前記のα,β−不飽和カルボン酸又はその誘導体が付
加していてもよい。ここで、成分(A),(B),(C
)の配合量をそれぞれA,B,C重量%とすると、60
≦A≦97,3≦B+C≦40,0.01≦B/C≦9
9である。
The above-mentioned α,β-unsaturated carboxylic acid or derivative thereof may be added to the crystalline polyolefin, thermoplastic elastomer, and polyphenylene ether used in the present invention. Here, components (A), (B), (C
) is 60% by weight of A, B, and C, respectively.
≦A≦97, 3≦B+C≦40, 0.01≦B/C≦9
It is 9.

【0016】A<60(B+C>40)であると、溶融
粘度は高くなるものの、溶融張力が低くなり良好な製品
を得ることができない。また耐熱性、剛性も著しく低下
してしまう。A>97(B+C<3)であると、十分な
溶融粘度が得られず、また、滞留時の粘度低下も大きい
。B/C<0.01であると、十分な溶融粘度が得られ
ない。B/C>99であると、溶融粘度は高いものの、
溶融張力が低く、良好な製品を得ることができない。
If A<60 (B+C>40), although the melt viscosity will be high, the melt tension will be low, making it impossible to obtain a good product. Moreover, heat resistance and rigidity are also significantly reduced. When A>97 (B+C<3), sufficient melt viscosity cannot be obtained and the viscosity decreases greatly during retention. When B/C<0.01, sufficient melt viscosity cannot be obtained. When B/C>99, although the melt viscosity is high,
The melt tension is low and it is not possible to obtain a good product.

【0017】本発明において、成分(D)であるガラス
繊維とは、通常の熱可塑性樹脂に配合されるものであれ
ば特にその種類は限定されないが、シラン系,チタン系
,アルミニウム系などのカップリング剤で処理されてい
るものが特に好ましい。ガラス繊維(D)の配合量をD
重量%とすると、0.05≦D/(A+B+C)≦1(
A+B+C+D=100)の範囲が好ましい。D/(A
+B+C)<0.05であると、ガラス繊維による補強
効果が見られない。D/(A+B+C)>1であると、
溶融張力が低くなり、良好な製品を得ることができない
[0017] In the present invention, the glass fiber as component (D) is not particularly limited in type as long as it can be blended with ordinary thermoplastic resins, but glass fibers such as silane-based, titanium-based, aluminum-based, etc. Particularly preferred are those treated with a ring agent. The blending amount of glass fiber (D) is D
In weight%, 0.05≦D/(A+B+C)≦1(
A+B+C+D=100) is preferred. D/(A
+B+C)<0.05, no reinforcing effect by glass fibers is observed. If D/(A+B+C)>1,
Melt tension becomes low, making it impossible to obtain a good product.

【0018】本発明に用いることのできる銅化合物また
は銅化合物とヨウ素化合物の混合物としては、ヨウ化第
一銅,塩化第一銅,塩化第二銅,臭化第一銅,臭化第二
銅,ギ酸銅,酢酸銅,プロピオン酸銅,ステアリン酸銅
,シュウ酸銅,セバシン酸銅,乳酸銅,安息香酸銅,サ
リチル酸銅,硫酸銅,硝酸銅,リン酸銅,亜リン酸銅,
あるいは銅キレート化合物などのような銅化合物または
、これらの銅化合物とヨウ化リチウム,ヨウ化カリウム
,ヨウ化ナトリウム,ヨウ化カルシウム,ヨウ化亜鉛,
ヨウ化銀などのようなヨウ素化合物の混合物を例示する
ことができる。特に好ましいのは、酢酸銅とヨウ化カリ
ウムの混合物,ヨウ化銅とヨウ化カリウムの混合物であ
る。
Examples of the copper compound or the mixture of a copper compound and an iodine compound that can be used in the present invention include cuprous iodide, cuprous chloride, cupric chloride, cuprous bromide, and cupric bromide. , copper formate, copper acetate, copper propionate, copper stearate, copper oxalate, copper sebacate, copper lactate, copper benzoate, copper salicylate, copper sulfate, copper nitrate, copper phosphate, copper phosphite,
Or copper compounds such as copper chelate compounds, or combinations of these copper compounds with lithium iodide, potassium iodide, sodium iodide, calcium iodide, zinc iodide,
Mixtures of iodine compounds such as silver iodide can be exemplified. Particularly preferred are mixtures of copper acetate and potassium iodide, and mixtures of copper iodide and potassium iodide.

【0019】銅化合物または銅化合物とヨウ素化合物の
混合物の、本発明の組成物100重量部への配合量は、
0.001〜5重量部の範囲が好ましく、0.005〜
4重量部の範囲が特に好ましい。配合量が0.001重
量部以下であると、配合する目的である耐熱性の向上が
見られない。5重量部以上であると組成物の機械的強度
に好ましからざる影響を与える。
The amount of the copper compound or the mixture of the copper compound and the iodine compound added to 100 parts by weight of the composition of the present invention is as follows:
The range is preferably from 0.001 to 5 parts by weight, and from 0.005 to 5 parts by weight.
A range of 4 parts by weight is particularly preferred. If the blending amount is 0.001 part by weight or less, the improvement in heat resistance, which is the purpose of blending, will not be observed. If the amount is 5 parts by weight or more, the mechanical strength of the composition will be adversely affected.

【0020】本発明の組成物に必要に応じて、通常の熱
可塑性樹脂に添加される添加剤、例えば安定剤,紫外線
吸収剤,滑剤,核剤,染料,顔料,離型剤,可塑剤,難
燃剤,無機充填剤などを配合することも特に制限される
ものではない。本発明の組成物の調整は、ブラベンダー
,ニーダー,バンバリーミキサー,押出機等の従来公知
の技術によって達成される。
If necessary, the composition of the present invention may contain additives that are added to ordinary thermoplastic resins, such as stabilizers, ultraviolet absorbers, lubricants, nucleating agents, dyes, pigments, mold release agents, plasticizers, There are no particular restrictions on the addition of flame retardants, inorganic fillers, etc. Preparation of the compositions of the present invention is accomplished by conventionally known techniques such as Brabenders, kneaders, Banbury mixers, extruders, and the like.

【0021】[0021]

【実施例】以下に本発明の実施例を示すが、本発明はそ
の要旨を超えない限り以下の実施例に限定されるもので
はない。本発明に用いた原料及び試験方法を以下に示す
。 〔1〕  原  料 (1)   Ny66(A)ナイロン66;硫酸相対粘
度(JIS  K6810,98%  H2 SO4 
)2.63(アミノ末端基濃度46mgeq/Kg) (2)   Ny66(B)ナイロン66;硫酸相対粘
度(JIS  K6810,98%  H2 SO4 
)2.60(アミノ末端基濃度80mgeq/Kg) (3)   Ny6ナイロン6;硫酸相対粘度(JIS
  K6810,98%H2 SO4 )2.90(4
)   MHTR(A)水素添加した変性スチレン−ブ
タジエン共重合体;旭化成工業(株)製  タフテック
  M1953(登録商標),酸価10(mgCH3 
ONa/g,滴定法)、スチレン成分約40重量%、引
張モジュラス2,300Kg/cm2  (5)   MHTR(B)水素添加した変性スチレン
−ブタジエン共重合体;旭化成工業(株)製  タフテ
ック  M1943(登録商標),酸価10(mgCH
3 ONa/g,滴定法)、スチレン成分約20重量%
(6)   HTR(A)水素添加したスチレン−ブタ
ジエン共重合体;旭化成工業(株)製  タフテック 
 H1051(登録商標),スチレン成分約40重量%
(7)   HTR(B)水素添加したスチレン−ブタ
ジエン共重合体;旭化成工業(株)製  タフテック 
 H1052(登録商標),スチレン成分約20重量%
(8)   MEPエチレン−プロピレン共重合体の無
水マレイン酸付加物;エクソン化学(株)製  EXX
ELOR  VA1803(登録商標),無水マレイン
酸付加量0.7重量% (9)   EP エチレン−プロピレン共重合体;三井石油化学工業(株
)製,タフマー  P0180(登録商標)(10) 
 HD−PE高密度ポリエチレン;旭化成工業(株)製
  サンテック  J320(登録商標)(11)  
THPB製造例1に示した、両末端に酸無水基を有する
水素化ポリブタジエン (12)  MPPE製造例2に示した、数平均分子量
約20,000のポリ(2,6−ジメチル−1,4−フ
ェニレンエーテル)に無水マレイン酸を0.7mol%
付加したもの (13)  GFガラス繊維;旭ファイバーグラス(株
)製  03JA  FT−2A(10μmφ,3mm
  チョップドストランド) (14)  HS−1酢酸銅;和光純薬工業(株)製(
15)  HS−2ヨウ化カリウム;和光純薬工業(株
)製(16)  HS−3ビス(2,6−ジ−t−ブチ
ル−4−メチルフェニル)ペンタエリトール−ジ−ホス
ファイト:アデカアーガス化学(株)製  MARKP
EP−36(17)  HS−4テトラキス(2,2,
6,6−テトラメチル−4−ピペリジル)−1,2,3
,4−ブタンテトラカルボキシレート;アデカアーガス
(株)製  MARK  LA−57 (18)  HS−54,4′−ブチリデン−ビス−(
3−メチル−6−t−ブチルフェノール);吉富製薬(
株)  ヨシノックスBB 〔2〕  試験方法 (1)   溶融張力 図1に示す(株)東洋精機製作所製  メルトテンショ
ンテスターにて、押出速度20mm/minにて測定を
行なった。なお、図中1は圧力ゲージ、2は押出棒、3
は加熱炉、4は測定ゲージ、5は引取ロール、6は樹脂
を示す。
[Examples] Examples of the present invention are shown below, but the present invention is not limited to the following examples unless it exceeds the gist thereof. The raw materials and test methods used in the present invention are shown below. [1] Raw material (1) Ny66 (A) Nylon 66; Sulfuric acid relative viscosity (JIS K6810, 98% H2 SO4
) 2.63 (amino end group concentration 46 mgeq/Kg) (2) Ny66 (B) Nylon 66; Sulfuric acid relative viscosity (JIS K6810, 98% H2 SO4
) 2.60 (amino end group concentration 80 mgeq/Kg) (3) Ny6 nylon 6; sulfuric acid relative viscosity (JIS
K6810, 98%H2SO4)2.90(4
) MHTR (A) Hydrogenated modified styrene-butadiene copolymer; Tuftec M1953 (registered trademark) manufactured by Asahi Kasei Industries, Ltd., acid value 10 (mg CH3
ONa/g, titration method), styrene component approximately 40% by weight, tensile modulus 2,300 Kg/cm2 (5) MHTR (B) Hydrogenated modified styrene-butadiene copolymer; Tuftec M1943 (registered) manufactured by Asahi Kasei Industries, Ltd. Trademark), acid value 10 (mgCH
3 ONa/g, titration method), styrene component approximately 20% by weight
(6) HTR (A) Hydrogenated styrene-butadiene copolymer; Tuftec manufactured by Asahi Kasei Industries, Ltd.
H1051 (registered trademark), styrene component approximately 40% by weight
(7) HTR (B) Hydrogenated styrene-butadiene copolymer; Tuftec manufactured by Asahi Kasei Industries, Ltd.
H1052 (registered trademark), styrene component approximately 20% by weight
(8) Maleic anhydride adduct of MEP ethylene-propylene copolymer; EXX manufactured by Exxon Chemical Co., Ltd.
ELOR VA1803 (registered trademark), maleic anhydride addition amount 0.7% by weight (9) EP ethylene-propylene copolymer; manufactured by Mitsui Petrochemical Industries, Ltd., Tafmer P0180 (registered trademark) (10)
HD-PE high-density polyethylene; Suntec J320 (registered trademark) (11) manufactured by Asahi Kasei Industries, Ltd.
Hydrogenated polybutadiene (12) having acid anhydride groups at both ends, shown in THPB Production Example 1. Poly(2,6-dimethyl-1,4- 0.7 mol% maleic anhydride in (phenylene ether)
Added item (13) GF glass fiber; manufactured by Asahi Fiberglass Co., Ltd. 03JA FT-2A (10μmφ, 3mm
(chopped strand) (14) HS-1 copper acetate; manufactured by Wako Pure Chemical Industries, Ltd. (
15) HS-2 potassium iodide; manufactured by Wako Pure Chemical Industries, Ltd. (16) HS-3 bis(2,6-di-t-butyl-4-methylphenyl)pentaerytol-di-phosphite: ADEKA MARKP manufactured by Argus Chemical Co., Ltd.
EP-36 (17) HS-4 Tetrakis (2,2,
6,6-tetramethyl-4-piperidyl)-1,2,3
,4-butanetetracarboxylate; manufactured by Adeka Argus Co., Ltd. MARK LA-57 (18) HS-54,4'-butylidene-bis-(
3-methyl-6-t-butylphenol); Yoshitomi Pharmaceutical (
Yoshinox BB Co., Ltd. [2] Test method (1) Melt tension Measurement was performed at an extrusion speed of 20 mm/min using a melt tension tester manufactured by Toyo Seiki Seisakusho Co., Ltd. shown in Figure 1. In the figure, 1 is a pressure gauge, 2 is an extrusion rod, and 3 is a pressure gauge.
4 is a heating furnace, 4 is a measuring gauge, 5 is a take-up roll, and 6 is a resin.

【0022】[0022]

【製造例1】(THPBの合成)両末端に酸無水基を有
する水素添加ポリブタジエン(NISSO−PB,GI
−3000  日本曹達(株)製)300g、ピリジン
15.8gを酢酸エチルエステルに溶解する。この混合
液を氷冷した後、乾燥窒素雰囲気下、無水トリメリット
酸クロライド42.1gを酢酸エチルエステル200m
lに溶解した溶液を1時間かけて滴下した。滴下終了後
室温まで昇温し、さらに8時間攪拌した。沈澱してくる
不溶物を濾別し、濾液をロータリーエバポレーターにて
濃縮した。残渣をクロロホルム500mlに溶解し、不
溶物を濾別後、濾液をシリカゲルカラムに通し、精製を
行なった。溶媒をロータリーエバポレーターにて留去す
ると295gの微黄色粘調な液状ポリマーが得られた。
[Production Example 1] (Synthesis of THPB) Hydrogenated polybutadiene having acid anhydride groups at both ends (NISSO-PB, GI
-3000 (manufactured by Nippon Soda Co., Ltd.) and 15.8 g of pyridine were dissolved in ethyl acetate. After cooling this mixture on ice, 42.1 g of trimellitic anhydride chloride was added to 200 m of ethyl acetate under a dry nitrogen atmosphere.
A solution dissolved in 1 ml was added dropwise over 1 hour. After the dropwise addition was completed, the temperature was raised to room temperature, and the mixture was further stirred for 8 hours. The precipitated insoluble matter was filtered off, and the filtrate was concentrated using a rotary evaporator. The residue was dissolved in 500 ml of chloroform, and after filtering off insoluble matter, the filtrate was passed through a silica gel column for purification. When the solvent was distilled off using a rotary evaporator, 295 g of a slightly yellow viscous liquid polymer was obtained.

【0023】赤外吸収スペクトル、 1H−NMRによ
り、末端に無水トリメリット酸基が結合していることを
確認した。末端基定量から求めた数平均分子量は4,8
60であった。
It was confirmed by infrared absorption spectrum and 1H-NMR that a trimellitic anhydride group was bonded to the terminal. The number average molecular weight determined from the terminal group amount is 4.8
It was 60.

【0024】[0024]

【製造例2】(MPPEの合成)数平均分子量約20,
000のポリ(2,6−ジメチル−1,4−フェニレン
エーテル)100重量部、無水マレイン酸3重量部、2
,5−ジメチル−ジ(t−ブチルパーオキシ)ヘキサン
(日本油脂(株)製  パーヘキサ25B)1重量部を
、30mmφ2軸押出機(PCM30  池貝鉄工(株
)製  L/D=17)中で、300〜320℃の温度
で混合し、更にペレット化し目的物を得た。得られたポ
リマーをトルエン−メタノールにて再沈澱をくり返し、
真空乾燥を行った後、ナトリウムメチラートにて無水マ
レイン酸の付加量を滴定により求めた所、0.7mol
%の無水マレイン酸が付加していた。
[Production Example 2] (Synthesis of MPPE) Number average molecular weight approximately 20,
000 poly(2,6-dimethyl-1,4-phenylene ether) 100 parts by weight, maleic anhydride 3 parts by weight, 2
, 1 part by weight of 5-dimethyl-di(t-butylperoxy)hexane (Perhexa 25B manufactured by Nippon Oil & Fats Co., Ltd.) in a 30 mmφ twin screw extruder (PCM30 manufactured by Ikegai Iron Works Co., Ltd. L/D = 17). The mixture was mixed at a temperature of 300 to 320°C and further pelletized to obtain the desired product. The obtained polymer was repeatedly reprecipitated with toluene-methanol,
After vacuum drying, the amount of maleic anhydride added was determined by titration with sodium methylate, and it was found to be 0.7 mol.
% maleic anhydride was added.

【0025】[0025]

【実施例1〜13,比較例1〜10】Ny66(A),
Ny66(B),Ny6,MHTR(A),MHTR(
B),HTR(A),HTR(B),MEP,EP,H
D−PE,THPB,MPPE,GF,HS−1〜5を
表1〜4に示す組成で、池貝鉄工(株)製  PCM4
5(L/D=33.5)2軸押出機中で、275〜29
5℃のシリンダー設定温度で溶融混合し、更にペレット
化して組成物を得た。この組成物の評価結果を表5,表
6に示す。
[Examples 1 to 13, Comparative Examples 1 to 10] Ny66(A),
Ny66 (B), Ny6, MHTR (A), MHTR (
B), HTR (A), HTR (B), MEP, EP, H
D-PE, THPB, MPPE, GF, HS-1 to 5 with the composition shown in Tables 1 to 4, PCM4 manufactured by Ikegai Iron Works Co., Ltd.
5 (L/D=33.5) in a twin-screw extruder, 275-29
The mixture was melt-mixed at a cylinder temperature of 5° C. and further pelletized to obtain a composition. The evaluation results of this composition are shown in Tables 5 and 6.

【0026】[0026]

【実施例14〜26,比較例11〜20】実施例1〜1
3の組成物を(株)日本製鋼所製ブロー成形機(JSW
−JB105CP,ダイス外/内=90mmφ/70m
mφ)により230〜250℃で約90mmφの直径を
有し、肉厚2〜3mmのパリソンを作成し、さらに縦1
50mm、横85mm、高さ220mmの容器を成形し
た。
[Examples 14-26, Comparative Examples 11-20] Examples 1-1
The composition of No. 3 was molded using a blow molding machine manufactured by Japan Steel Works, Ltd. (JSW).
-JB105CP, die outside/inside = 90mmφ/70m
A parison with a diameter of about 90 mmφ and a wall thickness of 2 to 3 mm was prepared at 230 to 250°C using
A container measuring 50 mm, width 85 mm, and height 220 mm was molded.

【0027】実施例1〜13の組成物より得られた成形
品(実施例14〜26)はピンホールもなく、良好な成
形品であった。一方、比較例1〜10の組成物を同一の
成形条件により成形した成形品(比較例11〜20)は
、いずれも破れが見られ、全く商品価値のないものであ
った。
The molded articles obtained from the compositions of Examples 1 to 13 (Examples 14 to 26) had no pinholes and were good molded articles. On the other hand, the molded products (Comparative Examples 11 to 20) obtained by molding the compositions of Comparative Examples 1 to 10 under the same molding conditions were all found to be torn and had no commercial value.

【0028】[0028]

【表1】[Table 1]

【0029】[0029]

【表2】[Table 2]

【0030】[0030]

【表3】[Table 3]

【0031】[0031]

【表4】[Table 4]

【0032】[0032]

【表5】[Table 5]

【0033】[0033]

【表6】[Table 6]

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

【図1】本発明の実施例に供するメルトテンションテス
ターの略図である。
FIG. 1 is a schematic diagram of a melt tension tester used in an embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  (A)ポリアミド樹脂(B)芳香族ビ
ニル化合物(X)と共役ジエン化合物の水素化物(Y)
からなる共重合体のα,β−不飽和カルボン酸又はその
誘導体の付加物 (C)他の熱可塑性樹脂 (D)ガラス繊維 (ただし、(A)、(B)、(C)、(D)各成分の配
合量をそれぞれ、A、B、C、D重量%とするとき、6
0≦A≦97,3≦B+C≦40,0.01≦B/C≦
99,0.05≦D/(A+B+C)≦1,A+B+C
+D=100;(X),(Y)各成分の共重合量をそれ
ぞれ、X,Y重量%とするとき、38<X<80,20
<Y<62,X+Y=100)であることを特徴とする
ブロー成形用樹脂組成物。
Claim 1: (A) polyamide resin (B) hydride of aromatic vinyl compound (X) and conjugated diene compound (Y)
(C) Other thermoplastic resins (D) Glass fibers (provided that (A), (B), (C), (D ) When the amount of each component is A, B, C, D weight%, 6
0≦A≦97, 3≦B+C≦40, 0.01≦B/C≦
99, 0.05≦D/(A+B+C)≦1, A+B+C
+D=100; When the copolymerization amounts of each component (X) and (Y) are X and Y weight%, respectively, 38<X<80, 20
<Y<62, X+Y=100) A resin composition for blow molding.
JP02404390A 1990-12-20 1990-12-20 Resin composition for blow molding Expired - Fee Related JP3140471B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02404390A JP3140471B2 (en) 1990-12-20 1990-12-20 Resin composition for blow molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02404390A JP3140471B2 (en) 1990-12-20 1990-12-20 Resin composition for blow molding

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Publication Number Publication Date
JPH04220458A true JPH04220458A (en) 1992-08-11
JP3140471B2 JP3140471B2 (en) 2001-03-05

Family

ID=18514068

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101464782B1 (en) * 2006-08-23 2014-11-26 바스프 에스이 Polyamide molding materials with improved thermal aging and hydrolysis stability
JP2019172759A (en) * 2018-03-27 2019-10-10 テクノUmg株式会社 Thermoplastic resin composition and molded article
CN112424288A (en) * 2018-07-31 2021-02-26 东丽株式会社 Polyamide resin composition for blow-molded article in contact with high-pressure hydrogen, and blow-molded article using same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101464782B1 (en) * 2006-08-23 2014-11-26 바스프 에스이 Polyamide molding materials with improved thermal aging and hydrolysis stability
US9505912B2 (en) 2006-08-23 2016-11-29 Basf Se Polyamide molding materials with improved thermal aging and hydrolysis stability
JP2019172759A (en) * 2018-03-27 2019-10-10 テクノUmg株式会社 Thermoplastic resin composition and molded article
CN112424288A (en) * 2018-07-31 2021-02-26 东丽株式会社 Polyamide resin composition for blow-molded article in contact with high-pressure hydrogen, and blow-molded article using same
CN112424288B (en) * 2018-07-31 2023-06-02 东丽株式会社 Polyamide resin composition for blow-molded article in contact with high-pressure hydrogen and blow-molded article thereof

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