JPH02300252A - Vinyl chloride resin composition for molding - Google Patents

Vinyl chloride resin composition for molding

Info

Publication number
JPH02300252A
JPH02300252A JP12175989A JP12175989A JPH02300252A JP H02300252 A JPH02300252 A JP H02300252A JP 12175989 A JP12175989 A JP 12175989A JP 12175989 A JP12175989 A JP 12175989A JP H02300252 A JPH02300252 A JP H02300252A
Authority
JP
Japan
Prior art keywords
vinyl chloride
chloride resin
molding
resin composition
parts
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
JP12175989A
Other languages
Japanese (ja)
Inventor
Kazuaki Sanjo
山條 和明
Kiyokazu Shimokawa
下川 清和
Rikuo Watanabe
陸生 渡辺
Shinji Omae
大前 眞治
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP12175989A priority Critical patent/JPH02300252A/en
Publication of JPH02300252A publication Critical patent/JPH02300252A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To improve both tension and elongation in a molten state and to obtain a corrugated pipe for wiring for electric power and telecommunication fields without fluctuation in strength by blow molding, by incorporating a melt tension improver in a vinyl chloride resin with a high degree of polymn. CONSTITUTION:A vinyl chloride resin compsn. for blow molding is provided by compounding 100 pts.wt. vinyl chloride resin with a high degree of polymn. (an average degree of polymn. of 900 or higher, most desirably 900-1,300) with 0.5-3 pts. molt tension improver (e.g. a methyl methacrylate polymer) and if necessary, 1-3 pts. auxiliary for improving impact strength (e.g. phthalates).

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は成形加工用の塩化ビニル系樹脂組成物に関し、
詳細には加熱溶融時における張力および伸び率が高く、
特に溶融状態でコルゲート管の成形等に適した流動特性
を示す高重合度の塩化ビニル系樹脂組成物に関するもの
である。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a vinyl chloride resin composition for molding,
In detail, the tension and elongation rate during heating and melting are high,
In particular, the present invention relates to a vinyl chloride resin composition with a high degree of polymerization that exhibits flow characteristics suitable for molding corrugated pipes in a molten state.

[従来の技術] 塩化ビニル系樹脂は様々の商用びん材料、アルコールや
油類用の容器材料等として広く実用化されており、これ
ら容器の製造にはブロー成形法が採用されている。これ
らの容器材料として使用される最も一般的な塩化ビニル
系樹脂組成物は、重合度が700〜800程度のポリ塩
化ビニルを主体とし、これに?I!!強度向上成分とし
て少量のMBS (メチルメタクリレート−ブタジェン
−スチレン共重合体)を配合するほか、錫系安定剤、溶
融粘度調節剤、滑剤等を少量配合したもので、ブロー成
形性や製品容器の物性においても一応の満足を得ている
[Prior Art] Vinyl chloride resins have been widely put into practical use as materials for various commercial bottles, containers for alcohol and oils, etc., and blow molding is used to manufacture these containers. The most common vinyl chloride resin composition used as material for these containers is mainly polyvinyl chloride with a degree of polymerization of about 700 to 800. I! ! In addition to containing a small amount of MBS (methyl methacrylate-butadiene-styrene copolymer) as a strength-improving component, it also contains small amounts of tin-based stabilizers, melt viscosity modifiers, lubricants, etc., and improves blow moldability and the physical properties of product containers. I am also somewhat satisfied with this.

また最近では、塩化ビニル系樹脂を電力通信用配線用コ
ルゲート管等の成形原着として利用し、押出し技術とブ
ロー成形技術の組合せによってコルゲート管を製造しよ
うとする試みもある。
Recently, there have also been attempts to use vinyl chloride resin as a molding material for corrugated pipes for power communication wiring, etc., and to manufacture corrugated pipes by a combination of extrusion technology and blow molding technology.

ところが塩化ビニル系樹脂を用いてコルゲート管を連続
ブロー成形しようとした場合、以下に示す如く様々の問
題が生じてくる。たとえば電力通信用配線用コルゲート
管には通常の容器以上に高レベルの耐久性と強度が要求
されるので、ポリ塩化ビニルとして高重合度のもの(p
=900程度以上)を使用する必要があり、この様な高
重合度体は溶融粘度が高く、溶融状態での伸び率が低い
のでブロー成形が非常に困難である。そこでブロー成形
性を高める為の手段として、溶融粘度調節剤の配合量を
多くして溶融粘度を下げることも考えられるが、そうす
ると樹脂組成物の筒型化が進んで強度が低下するばかり
でなく、該組成物の溶融張力が低下し、ブロー成形時に
おける材料伸びの均一性が悪くなり、ブロー成形品の厚
みが不均一になって強度むらが生じてくる。即ち塩化ビ
ニル系樹脂組成物溶融物の粘性(即ちブロー成形時の伸
び易さ)と樹脂張力の間には反比例の関係があり、ブロ
ー成形性を悪化させたり成形品に強度むらを生ずる要因
となっている。そして粘性の高い高重合度の塩化ビニル
系樹脂組成物を使用する場合は、上記傾向がブロー成形
の困難性となって顕著に現われてくるのである。
However, when attempting to continuously blow mold corrugated pipes using vinyl chloride resin, various problems arise as shown below. For example, corrugated pipes for power communication wiring require a higher level of durability and strength than ordinary containers, so polyvinyl chloride with a high degree of polymerization (p
= about 900 or more), and such highly polymerized materials have high melt viscosity and low elongation in the molten state, making blow molding very difficult. Therefore, as a means to improve blow moldability, it may be possible to lower the melt viscosity by increasing the blending amount of a melt viscosity modifier, but this would not only cause the resin composition to become cylindrical, but also reduce its strength. , the melt tension of the composition decreases, the uniformity of material elongation during blow molding deteriorates, and the thickness of the blow molded product becomes non-uniform, resulting in uneven strength. In other words, there is an inverse relationship between the viscosity of a molten vinyl chloride resin composition (i.e., the ease of elongation during blow molding) and the resin tension, and this is a factor that deteriorates blow moldability and causes strength unevenness in molded products. It has become. When a vinyl chloride resin composition with a high degree of polymerization and high viscosity is used, the above-mentioned tendency becomes conspicuous in the form of difficulty in blow molding.

[発明が解決しようとする課題] 本発明は上記の様な事情に着目してなされたものであり
て、その目的は、溶融時の張力および伸び率の両方が改
善され、ブロー成形等によって強度むらのない優れた物
性の成形品を得ることのできる高重合度の塩化ビニル系
樹脂組成物を提供しようとするものである。
[Problems to be Solved by the Invention] The present invention has been made focusing on the above-mentioned circumstances, and its purpose is to improve both the tension and elongation during melting, and to increase the strength by blow molding etc. The object of the present invention is to provide a vinyl chloride resin composition with a high degree of polymerization that allows molded articles with uniform and excellent physical properties to be obtained.

[課題を解決するための手段] 上記課題を解決することのできた本発明組成物の構成は
、平均重合度が900以上である塩化ビニル系樹脂を主
成分とする成形加工用樹脂組成物において、塩化ビニル
系樹脂100重量部に対し0.5〜3重量部の溶融張力
向上剤を配合し、あるいはこれと共に1〜3重量部の衝
撃強度向上助剤を配合してなるところに要旨を有するも
のである。
[Means for Solving the Problems] The composition of the present invention that can solve the above problems is a resin composition for molding whose main component is a vinyl chloride resin having an average degree of polymerization of 900 or more. The gist is that 0.5 to 3 parts by weight of a melt tension improver is blended with 100 parts by weight of a vinyl chloride resin, or 1 to 3 parts by weight of an impact strength improving aid is blended together with this. It is.

[作用] 本発明で成形加工用塩化ビニル系樹脂組成物に配合され
る溶融張力向上剤は、可塑剤等の汎用添加剤に比べて特
異な作用効果を有しており、これを塩化ビニル系樹脂に
適量配合すると、当該樹脂の溶融張力を高めると共に伸
び率も高める作用があり、ブロー成形等に極めて適した
ものとなる。
[Function] The melt tension improver blended into the vinyl chloride resin composition for molding in the present invention has a unique action and effect compared to general-purpose additives such as plasticizers. When blended in an appropriate amount with a resin, it has the effect of increasing the melt tension and elongation of the resin, making it extremely suitable for blow molding and the like.

即ち従来の塩化ビニル系樹脂組成物では、前述の如く溶
融時伸び率と溶融時張力は相反比例する関係にあり、両
者を同時に満足することはできなかったが、溶融張力向
上剤を適量配合すると上記2つの要求特性が共に改善さ
れ、溶融樹脂の伸びが良くなってブロー成形金型の成形
面に沿った成形等が容易になるばかりでなく、溶融張力
の向上によって材料伸びの均一性も良くなり、ブロー成
形を極めて円滑に進めることができるのである。
That is, in conventional vinyl chloride resin compositions, as mentioned above, elongation at melting and tension at melting are in a reciprocal proportional relationship, and it was not possible to satisfy both at the same time. However, when an appropriate amount of a melt tension improver is added, Both of the above two required properties have been improved, and the elongation of the molten resin has become better, making it easier to mold along the molding surface of the blow molding mold, as well as improving the uniformity of elongation of the material due to the improved melt tension. This allows blow molding to proceed extremely smoothly.

また上記溶融時伸び率および溶融時張力は、ブロー成形
に限らず押出成形や加圧成形等を行なう場合においても
極めて重要な特梅であるから、本発明はブロー成形以外
の成形加工にも有効に活用することができる。
Furthermore, the elongation at melting and the tension at melting mentioned above are extremely important characteristics not only for blow molding but also for extrusion molding, pressure molding, etc., so the present invention is effective for molding processes other than blow molding. It can be used for

第1.2図は、下記基本組成の塩化ビニル系樹脂組成物
を使用し、これにポリメチルメタクリレート系の溶融張
力向上剤を配合した場合と配合しなかった場合のブロー
成形時における膨張速度と溶融張力の関係(第1図)、
および樹脂温度と伸び率の関係(第2図)を示したもの
であり、溶融張力向上剤を配合することによって、ブロ
ー成形時の膨張速度に対する溶融張力(メルトストレン
グス)は2〜5割程度向上し、またm融時の伸び率も3
〜5割程度向上している。
Figure 1.2 shows the expansion rate during blow molding when a polymethyl methacrylate melt tension improver was added to the vinyl chloride resin composition having the basic composition shown below, and when it was not added. Relationship of melt tension (Figure 1),
Figure 2 shows the relationship between resin temperature and elongation rate.By adding a melt tension improver, the melt tension (melt strength) relative to the expansion rate during blow molding can be improved by about 20 to 50%. Also, the elongation rate at m melting is 3
It has improved by about 50%.

(樹脂組成) ポリ塩化ビニル(r=1000)100重量部MBS 
 ・           4重量部錫系安定剤(ジメ
チル錫メルカプチド)2I!量部 金属石けん(ステアリン酸カルシウム ・マグネシウム) 1.5 IIt量部滑部滑剤リエチ
レンワックス)0.5重量部衝撃強度向上助剤(脂肪酸
エステル) 2.0 !l量奮 起融張力向上剤   0または2.0 !を1部(測定
法) 第3図に示す如く押出機1、ヒーター2、ダイ3等を備
えた溶融押出装置I、荷重検出器4、引取ロール5等か
らなる測定装置を使用し、ダイ3から吐出される樹脂を
強制的に引き取り、その時の張力を荷重検出器4によっ
て測定するもので、引取速度を段階的に増速させ、吐出
樹脂が切断したときの速度と張力を測定する。切断時の
速度が速いほど伸び易い樹脂であり、張力の大きいもの
ほど溶融強度が強く均一な伸びが得られ易い樹脂である
(Resin composition) Polyvinyl chloride (r=1000) 100 parts by weight MBS
- 4 parts by weight tin stabilizer (dimethyltin mercaptide) 2I! Parts by weight Metal soap (calcium/magnesium stearate) 1.5 Parts by weight Lubricant (liethylene wax) 0.5 parts Impact strength improving aid (fatty acid ester) 2.0! Amount of stimulant melt tension improver 0 or 2.0! (Measurement method) As shown in FIG. The resin discharged from the machine is forcibly taken up and the tension at that time is measured by the load detector 4. The taking speed is increased in stages and the speed and tension when the discharged resin is cut are measured. The faster the cutting speed, the easier the resin stretches, and the higher the tension, the stronger the melt strength, and the easier it is to obtain uniform elongation.

裡10に住 押出機:異方向パラレル型二軸押出機 (内径20 m1l) スクリュー:フルフライト型、L/D−27回転数17
〜18rpm ダイ :3ffl諺φX22mL、ストランドダイ 設定温度(℃) (r    C2C3ダイ 吐出量: 1B、1〜16.5g/分 引取条件 2m/分の速度からin/分間隔で段階的に増速し、各
速度で5分間引取り、ストランドが破断するまで繰り返
す。
Extruder: Different direction parallel type twin screw extruder (inner diameter 20ml) Screw: Full flight type, L/D-27 rotation speed 17
~18 rpm Die: 3fflφX22mL, Strand die setting temperature (℃) (r C2C3 die discharge rate: 1B, 1~16.5g/min Take-up condition: Increase the speed step by step at in/min intervals from a speed of 2m/min , take off for 5 minutes at each speed and repeat until the strand breaks.

ノズル−ロードセル間 11t : 222.5a+i
1旦久1ユニ25℃ この様に溶融張力向上剤の添加によって塩化ビニル系樹
脂組成物の溶融張力および溶融時伸び率が向上する理由
は必ずしも明確にされた訳ではないが、溶融張力向上剤
がポリ塩化ビニル分子相互間)絡み度合いを高め、溶融
状態における張力および伸び率を高めたものと考えられ
る。
Between nozzle and load cell 11t: 222.5a+i
The reason why the melt tension and melt elongation of vinyl chloride resin compositions are improved by the addition of a melt tension improver is not necessarily clear, but the melt tension improver It is thought that this increases the degree of entanglement (between polyvinyl chloride molecules) and increases the tension and elongation rate in the molten state.

こうした溶融張力向上剤の効果は、塩化ビニル系樹脂1
00!量部に対して0.5〜3重量部含有させることに
よって有効に発揮される。0.5重量部未満では上記の
改善効果が殆んど発現されず、一方3重量部を超える場
合は、熱変形温度の低下、耐衝撃特性の減少が起こり、
熱に弱く、割れ易い材質になる。尚溶融張力向上剤とし
ては、アクリル酸エステルやメタクリル酸エステルの単
独重合体もしくは共重合体(重合度は20〜数100万
程度)が最も一般的であるが、このほか少量のアクリル
アミド、アクリロニトリル等が共重合されたものであっ
てもよく、更には少量のビニル化合物、スチレン系化合
物等が共重合されたものであってもよい。
The effect of such a melt tension improver is that vinyl chloride resin 1
00! It is effectively exhibited by containing it in an amount of 0.5 to 3 parts by weight. If it is less than 0.5 parts by weight, the above-mentioned improvement effect will hardly be exhibited, while if it exceeds 3 parts by weight, the heat distortion temperature will decrease, the impact resistance properties will decrease,
The material is sensitive to heat and easily breaks. The most common melt tension improver is a homopolymer or copolymer of acrylic ester or methacrylic ester (polymerization degree is about 20 to several million million), but in addition, small amounts of acrylamide, acrylonitrile, etc. may be copolymerized, or further may be copolymerized with a small amount of a vinyl compound, a styrene compound, or the like.

上記の様に本発明は、塩化ビニル系樹脂組成物中に特定
量の溶融張力向上剤を配合したところに1つの特徴があ
るが、この他、衝撃強度向上助剤を適量含有させると、
塩化ビニル系樹脂組成物の可塑化が進み、製品の耐衝撃
性を一段と高めることができる。即ち衝撃強度向上助剤
としては塩化ビニル系樹脂との相溶性に侵れたジブチル
フタレート、ジヘプチルフタレート、ジー2−エチルへ
キシルフタレート、ジ−n−オクチルフタレート、ジ−
イソオクチルフタレート、ジイソデシルフタレート、ブ
チルベンジルフタレート等のフタル酸エステル類ニジー
2−エチルへキシルアジペート、ジー2−エチルへキシ
ルアゼレート。
As mentioned above, one feature of the present invention is that a specific amount of a melt tension improver is blended into the vinyl chloride resin composition, but in addition to this, when an appropriate amount of an impact strength improver is included,
Plasticization of the vinyl chloride resin composition progresses, making it possible to further improve the impact resistance of the product. That is, as impact strength improving aids, dibutyl phthalate, diheptyl phthalate, di-2-ethylhexyl phthalate, di-n-octyl phthalate, di-
Phthalic acid esters such as isooctyl phthalate, diisodecyl phthalate, butylbenzyl phthalate, di-2-ethylhexyl adipate, di-2-ethylhexyl azelate.

ジー2−エチルへキシルセバケート等の脂肪族二塩基酸
エステル類;トリクレジルホスフェート。
Aliphatic dibasic acid esters such as di-2-ethylhexyl sebacate; tricresyl phosphate.

トリキシレニルホスフェート、2−エチルヘキシルジフ
ェニルホスフェート、トリメチルホスフェート、トリフ
ェニルホスフェート等のりん酸エステル類;エポキシ化
植物油;ポリエステル系可塑剤:ニトリル系合成ゴム等
が使用されるが、これらは塩イヒビニル系樹脂の内部に
入り込んで当該樹脂の流動性(円滑性)を高めると共に
可塑化し、更には別途配合されるMBS等の衝撃強度向
上剤の塩化ビニル系樹脂中への分散性も高め、最終成形
品の耐衝撃性を更に高める作用を発揮する。こうした効
果を発揮する衝撃強度向上助剤の好ましい配合量は、塩
化ビニル系樹脂100重量部に対して1〜3重量部の範
囲であり、1重量部未満では衝撃強度改善効果が有効に
発揮されず、一方31i量部を超える場合は樹脂組成物
全体が可塑化し過ぎて強度不足の弊害が表われてくる。
Phosphate esters such as trixylenyl phosphate, 2-ethylhexyldiphenyl phosphate, trimethyl phosphate, triphenyl phosphate; epoxidized vegetable oil; polyester plasticizer: nitrile synthetic rubber, etc. are used, but these are salt hibinyl resins. It penetrates into the inside of the resin and increases the fluidity (smoothness) of the resin and plasticizes it, and also improves the dispersibility of impact strength improvers such as MBS, which are separately blended, into the vinyl chloride resin, improving the final molded product. Demonstrates the effect of further increasing impact resistance. The preferred blending amount of the impact strength improving aid that exhibits these effects is in the range of 1 to 3 parts by weight per 100 parts by weight of the vinyl chloride resin, and if it is less than 1 part by weight, the impact strength improving effect will not be effectively exhibited. On the other hand, if the amount exceeds 31 parts, the entire resin composition becomes too plasticized, resulting in insufficient strength.

このほか本発明においては、組成物の成形性や成形品の
物性向上を目的として様々の配合剤を使用することがで
きるので、以下それらについて簡単に説明する。
In addition, in the present invention, various compounding agents can be used for the purpose of improving the moldability of the composition and the physical properties of the molded article, and these will be briefly explained below.

」1ヒ辻二各 まずベースとなる塩化ビニル系樹脂として代表的なもの
はポリ塩化ビニルであるが、このほか少量の酢酸ビニル
、塩化ビニリデン、アクリル酸エステル、メタクリル酸
エステル、スチレン等の共重合性千ツマ−が共重合され
た塩化ビニル系共重合体も使用できる。これら塩化ビニ
ル系樹脂の好ましい分子量は、成形品に要求される特性
に応じて適宜選定されるが、本発明の効果が最も有効に
発揮されるのは平均重合度CP)が900〜1300の
範囲のものである。
1. Tsuji 2. First of all, polyvinyl chloride is a typical base vinyl chloride resin, but in addition, small amounts of copolymerized vinyl acetate, vinylidene chloride, acrylic esters, methacrylic esters, styrene, etc. A vinyl chloride copolymer copolymerized with a polyvinyl chloride can also be used. The preferred molecular weight of these vinyl chloride resins is appropriately selected depending on the properties required of the molded product, but the effects of the present invention are most effectively exhibited when the average degree of polymerization CP) is in the range of 900 to 1300. belongs to.

MBS  メチルメタクリレート−ブタジェン塩化ビニ
ル系樹脂成形品の耐衝撃性を高める為の成分として有用
なものであり、塩化ビニル系樹脂tooz奮起に対し3
〜10重量部重量部会することによってその作用が有効
に発揮される。
MBS Methyl methacrylate-butadiene is useful as a component for increasing the impact resistance of vinyl chloride resin molded products, and has a resistance of 3.
The effect can be effectively exhibited by adding up to 10 parts by weight.

支足l 塩化ビニル系樹脂を熱や光に長時間さらしたときに起こ
る脱塩酸反応を抑えるために配合されるものであり、鉛
白、三塩基性硫酸鉛、二塩基性亜りん酸鉛、二塩基性フ
タル酸鉛、三塩基性マレイン酸鉛、珪酸鉛およびそのシ
リカゲル共沈物等の鉛塩系安定剤:鉛、カドミウム、バ
リウム、亜鉛、カルシウム等とステアリン酸、リシノー
ル酸、ナフテン酸、2−エチルへキソイン酸等よりなる
金属石けん系安定剤;ジブチル錫ジラウレート、ジブチ
ル錫マレエート、ジブチル錫メルカプチド等の有機錫系
安定剤;トリフェニルホスファイト、ジフェニルイソデ
シルホスファイト、フェニルジイソデシルホスファイト
、トリノニルフェニルホスファイト等の有機安定化助剤
;サリチル酸エステル類、ヒドロキシベンゾフェノン類
、ベンゾトリアゾール類等の紫外線吸収剤などが挙げら
れ、これらは必要により2 f1以上を組合せて使用す
ることができる。好ましい配合量は、塩化ビニル系樹脂
100重量部に対し1〜5重量間外度である。
It is formulated to suppress the dehydrochloric acid reaction that occurs when vinyl chloride resin is exposed to heat or light for a long time, and contains white lead, tribasic lead sulfate, dibasic lead phosphite, Lead salt stabilizers such as dibasic lead phthalate, tribasic lead maleate, lead silicate and their silica gel coprecipitates: lead, cadmium, barium, zinc, calcium, etc. and stearic acid, ricinoleic acid, naphthenic acid, Metal soap stabilizers such as 2-ethylhexoic acid; organotin stabilizers such as dibutyltin dilaurate, dibutyltin maleate, and dibutyltin mercaptide; triphenyl phosphite, diphenylisodecyl phosphite, phenyl diisodecyl phosphite, Examples include organic stabilizing aids such as trinonylphenyl phosphite; ultraviolet absorbers such as salicylic acid esters, hydroxybenzophenones, and benzotriazoles, and these may be used in combination of 2 f1 or more if necessary. The preferred blending amount is between 1 and 5 parts by weight per 100 parts by weight of the vinyl chloride resin.

1見 溶融樹脂の流動性を高めて成形性を改善するほか、成形
金型への粘着を防いで離型性を高めつつ成形体の表面平
滑性を高める作用があり、高級脂肪酸およびその誘導体
、安定剤を兼ねた既述の金属石けん類、天然もしくは合
成のワックス類−等が挙げられ、好ましい配合量は塩化
ビニル系樹脂100重量部に対しO,S〜411量部程
度甲部程度五嵐l 主とし成形体の硬さ、モジュラスおよび曲げ剛性を高め
る作用があり、炭酸カルシウム、カオリン、クレー、シ
リカ、珪藻土、カーボンブラックなどが挙げられる。
In addition to increasing the fluidity of the molten resin and improving its moldability, it also has the effect of increasing the surface smoothness of the molded product while preventing it from sticking to the molding die and improving its releasability.Higher fatty acids and their derivatives, Examples include the aforementioned metal soaps that also serve as stabilizers, natural or synthetic waxes, etc., and the preferred blending amount is about 411 parts of O, S to 100 parts by weight of vinyl chloride resin. l Mainly has the effect of increasing the hardness, modulus, and bending rigidity of the molded body, and examples thereof include calcium carbonate, kaolin, clay, silica, diatomaceous earth, and carbon black.

1Ω別ばど艷1劃 上記以外の配合剤としては、着色剤、難燃剤、帯電防止
剤、発泡剤、防かび剤等が必要に応じて使用される。
As compounding agents other than those mentioned above, colorants, flame retardants, antistatic agents, foaming agents, fungicides, etc. may be used as necessary.

[実施例] 第1表に示す成分組成の成形用塩化ビニル系樹脂組成物
を調製し、夫々について第3図に示した方法に準拠して
溶融張力および破断時引取速度を調べた。結果を第1表
に一括して示す。
[Example] Molding vinyl chloride resin compositions having the component compositions shown in Table 1 were prepared, and the melt tension and take-off speed at break were examined for each according to the method shown in FIG. The results are summarized in Table 1.

第1表より次の様に考えることができる。From Table 1, it can be considered as follows.

実験No、1.2,3,4.8は本発明の規定要件を満
たす実施例であり、溶融張力および破断時引取速度のい
ずれも高い値を示しており、成形性の非常に優ねたもの
であることが分かる。
Experiment Nos. 1.2, 3, and 4.8 are examples that meet the specified requirements of the present invention, and show high values for both melt tension and take-off speed at break, and have very good formability. I can see that it is something.

これに対し実験No、5.6.7は本発明の規定要件を
欠く比較例であり、物性において下記の様な問題がある
On the other hand, Experiment No. 5.6.7 is a comparative example that lacks the specified requirements of the present invention, and has the following problems in physical properties.

実験No、5:溶融張力向上剤が多過ぎる比較例であり
、シャルピー衝撃強度が低 下し、製品の耐衝撃性が不十分で ある。
Experiment No. 5: This is a comparative example in which there is too much melt tension improver, resulting in a decrease in Charpy impact strength and insufficient impact resistance of the product.

実験No、6:溶融張力向上剤が不足する比較例であり
、溶融張力が実施例のもの に比べて乏しく、ブロー成形時の 均−科に問題を生じることが明ら かであるや又破断時伸び率も低 く、ブロー成形時の条件に制約が 生じやすい。
Experiment No. 6: This is a comparative example in which the melt tension improver is insufficient, and the melt tension is poorer than that of the example, and it is clear that there will be a problem in uniformity during blow molding. The molding rate is also low, and there are likely to be restrictions on the conditions during blow molding.

実験No、7:衝撃−電度向1・、N、tl ’+Ij
i M染過ぎる比較例であり、溶融張力が低いばかり でなく成形体の引張強度も低く、 高重合度塩化ビニル樹脂を用いる ことによる特徴が有効に発揮され ない。
Experiment No. 7: Impact-electrical direction 1., N, tl'+Ij
This is a comparative example with too much iM dyeing, and not only the melt tension is low, but also the tensile strength of the molded product is low, and the characteristics of using a high polymerization degree vinyl chloride resin are not effectively exhibited.

[発明の効果] 本発明の成形加工用塩化ビニル系樹脂組成物は以上の様
に構成されており、この組成物は前述の如く適量の溶融
張力向上剤の添加によって溶融時の張力および伸び率が
共に改善されているので、特に成形時における樹脂材料
の伸びが良好で且つその均一性も優れたものであり、厚
みむら等を生じることなく金型内面の隅々まで行き渡り
、均質で物性の優れた成形品を得ることができる。殊に
電力通信用配線翔コルゲート管等の連続ブロー成形に適
用した場合は、上記樹脂組成物の溶融状態における優れ
た流動特性(張力及び伸び率)が遺憾なく発揮され、製
品の物性および均質性の向上並びに生産性の向上を果た
すことができる。また衝撃強度向上助剤の添加によって
耐衝撃性を一段と高めることができるので、使用時の衝
撃破壊を抑えることができ、信頼性の高い成形品を得る
ことができる。
[Effects of the Invention] The vinyl chloride resin composition for molding of the present invention is constructed as described above, and as described above, this composition can be improved in tension and elongation during melting by adding an appropriate amount of a melt tension improver. As both properties have been improved, the elongation of the resin material is particularly good during molding, and its uniformity is also excellent.It spreads to every corner of the inner surface of the mold without causing thickness unevenness, and has uniform physical properties. Excellent molded products can be obtained. In particular, when applied to continuous blow molding of wiring corrugated pipes for electric power communications, etc., the excellent fluidity properties (tension and elongation) of the resin composition in the molten state are fully exhibited, and the physical properties and homogeneity of the product are improved. and productivity. Furthermore, since the impact resistance can be further increased by adding an impact strength improving agent, impact fracture during use can be suppressed, and highly reliable molded products can be obtained.

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

第1図はプロー成形時における膨張速度と樹脂の溶融張
力の関係、第2図は樹脂温度と溶融時伸び率の関係を、
本発明樹脂組成物と比較組成物を対比して示すグラフ、
第3図は物性の測定法を示す説明図である。
Figure 1 shows the relationship between expansion rate and resin melt tension during blow molding, and Figure 2 shows the relationship between resin temperature and elongation during melting.
A graph showing a comparison between the resin composition of the present invention and a comparative composition,
FIG. 3 is an explanatory diagram showing a method for measuring physical properties.

Claims (2)

【特許請求の範囲】[Claims] (1)平均重合度が900以上である高重合度の塩化ビ
ニル系樹脂を主成分とする成形加工用樹脂組成物におい
て、塩化ビニル系樹脂100重量部に対し0.5〜3重
量部の溶融張力向上剤を含有させたものであることを特
徴とする成形加工用塩化ビニル系樹脂組成物。
(1) In a resin composition for molding mainly composed of a high polymerization degree vinyl chloride resin with an average degree of polymerization of 900 or more, 0.5 to 3 parts by weight of the resin is melted per 100 parts by weight of the vinyl chloride resin. A vinyl chloride resin composition for molding processing, characterized in that it contains a tension improver.
(2)平均重合度が900以上である高重合度の塩化ビ
ニル系樹脂を主成分とする成形加工用樹脂組成物におい
て、塩化ビニル系樹脂100重量部に対し0.5〜3重
量部の溶融張力向上剤と、1〜3重量部の衝撃強度向上
助剤を含有させたものであることを特徴とする成形加工
用塩化ビニル系樹脂組成物。
(2) In a resin composition for molding whose main component is a high polymerization degree vinyl chloride resin with an average degree of polymerization of 900 or more, 0.5 to 3 parts by weight of the melted vinyl chloride resin is added to 100 parts by weight of the vinyl chloride resin. A vinyl chloride resin composition for molding, characterized in that it contains a tension improver and 1 to 3 parts by weight of an impact strength improving aid.
JP12175989A 1989-05-15 1989-05-15 Vinyl chloride resin composition for molding Pending JPH02300252A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12175989A JPH02300252A (en) 1989-05-15 1989-05-15 Vinyl chloride resin composition for molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12175989A JPH02300252A (en) 1989-05-15 1989-05-15 Vinyl chloride resin composition for molding

Publications (1)

Publication Number Publication Date
JPH02300252A true JPH02300252A (en) 1990-12-12

Family

ID=14819185

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12175989A Pending JPH02300252A (en) 1989-05-15 1989-05-15 Vinyl chloride resin composition for molding

Country Status (1)

Country Link
JP (1) JPH02300252A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0680814A1 (en) * 1993-11-11 1995-11-08 Tokai Kogyo Kabushiki Kaisha Extrudate and extrusion process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0680814A1 (en) * 1993-11-11 1995-11-08 Tokai Kogyo Kabushiki Kaisha Extrudate and extrusion process
EP0680814A4 (en) * 1993-11-11 1996-03-20 Tokai Kogyo Co Ltd Extrudate and extrusion process.

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