JPH09151269A - Foamable vinyl chloride resin composition for injection molding - Google Patents

Foamable vinyl chloride resin composition for injection molding

Info

Publication number
JPH09151269A
JPH09151269A JP7311324A JP31132495A JPH09151269A JP H09151269 A JPH09151269 A JP H09151269A JP 7311324 A JP7311324 A JP 7311324A JP 31132495 A JP31132495 A JP 31132495A JP H09151269 A JPH09151269 A JP H09151269A
Authority
JP
Japan
Prior art keywords
vinyl chloride
chloride resin
injection molding
resin
weight
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
JP7311324A
Other languages
Japanese (ja)
Inventor
Shingo Nakamura
伸吾 中村
Yori Hanakawa
因 花川
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP7311324A priority Critical patent/JPH09151269A/en
Publication of JPH09151269A publication Critical patent/JPH09151269A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a foamable vinyl chloride resin compsn. for injection molding which can give a foam expanded twice or higher even with an ordinary injection molding machine by compounding a vinyl chloride resin with a specific polymethyl methacrylate resin and a thermally decomposable blowing agent. SOLUTION: This compsn. is prepd. by compounding 100 pts.wt. vinyl chloride resin having an average degree of polymn. of 400-1,000 with 2-30 pts.wt. polymethyl methacrylate resin having a wt. average mol.wt. of 4,500,000-7,000,000 and 0.5-10 pts.wt. thermally decomposable blowing agent. Since the latter resin disperses homogeneously in the former, the melt viscosity of the compsn. is maintained properly without causing excessive heat build-up, enabling a foam with uniform cells to be obtd.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、汎用されている通
常の射出成形機の、成形材料として使用可能な射出成形
用発泡塩化ビニル系樹脂組成物に関する。
TECHNICAL FIELD The present invention relates to a foamed vinyl chloride resin composition for injection molding, which can be used as a molding material for a general-purpose ordinary injection molding machine.

【0002】[0002]

【従来の技術】塩化ビニル系樹脂製の成形体は、耐衝撃
性、耐熱性等の物理的性質や、耐溶剤性、耐酸性、耐ア
ルカリ性等の化学的性質が優れていることから、建材そ
の他の用途に広く用いられてきたが、発泡体の成形が可
能となってから、その特性を利用して軽量性、断熱性、
遮音性等を必要とする用途にも採用されるようになり、
さらに広い用途に使用されている。
2. Description of the Related Art Molded articles made of vinyl chloride resin are excellent in physical properties such as impact resistance and heat resistance and chemical properties such as solvent resistance, acid resistance and alkali resistance. It has been widely used for other purposes, but since it became possible to mold foam, its characteristics were utilized to make it lightweight, heat insulating,
It has come to be used in applications that require sound insulation,
It is used for a wider range of purposes.

【0003】このような塩化ビニル系樹脂製の発泡成形
体は、熱分解型無機発泡剤や熱分解型有機発泡剤等を使
用し 主として押出成形法により製造されてきた。例え
ば、特公昭63−9540号公報には、低重合度の塩化
ビニル系樹脂を主材とし、発泡剤として、アゾジカルボ
ンアミド等の熱分解型有機発泡剤と、重炭酸ナトリウム
等の熱分解型無機発泡剤とを併用し、更に分子量が20
万〜300万のメタクリル酸エステル系樹脂並びに炭酸
カルシウム、タルク、クレイ、アスベスト、シリカから
なる群より選ばれる1種以上の充填剤を配合してなる高
発泡性塩化ビニル系樹脂組成物が記載されている。
Such a foamed molded product made of a vinyl chloride resin has been manufactured mainly by an extrusion molding method using a pyrolytic inorganic foaming agent, a pyrolytic organic foaming agent or the like. For example, in Japanese Examined Patent Publication No. 63-9540, a vinyl chloride resin having a low degree of polymerization is used as a main material, and as a foaming agent, a thermally decomposable organic foaming agent such as azodicarbonamide and a thermally decomposable type such as sodium bicarbonate. Combined with an inorganic foaming agent, the molecular weight is 20
A highly foamable vinyl chloride resin composition containing 1 to 3 million methacrylic acid ester-based resins and one or more fillers selected from the group consisting of calcium carbonate, talc, clay, asbestos and silica is described. ing.

【0004】この樹脂組成物を用いて成形した場合、均
一微細なセル構造を有し且つ表面光沢に優れると共に高
い表面硬度のスキン層を有する発泡成形体が得られるこ
とが開示されている。ところが、この樹脂組成物を用い
て射出成形法により成形した場合、射出成形法自体の特
性に基づく溶融樹脂の滞留や高剪断力その他の理由によ
り溶融樹脂が過熱されて熱分解を起こし易く、2倍を超
える発泡倍率を持つ成形体を得ることが困難であった。
It has been disclosed that when molded using this resin composition, a foamed molded product having a uniform and fine cell structure, an excellent surface gloss and a skin layer having a high surface hardness can be obtained. However, when the resin composition is molded by an injection molding method, the molten resin is likely to be overheated and thermally decomposed due to retention of the molten resin based on the characteristics of the injection molding method itself, high shearing force, and other reasons. It was difficult to obtain a molded product having a foaming ratio of more than double.

【0005】そこで、射出成形に適した発泡塩化ビニル
系樹脂組成物についての開発がなされた。その一つとし
て、特開平3−146534号公報には、同じく低重合
度の塩化ビニル系樹脂を主材とし、更に可塑剤と耐衝撃
剤と特定の発泡剤とを、それぞれ特定の割合で配合して
なる組成物が開示されており、併せてこの組成物を材料
として得た硬質塩化ビニル系樹脂発泡成形体と、その製
造方法についての提案がなされている。
Therefore, a foamed vinyl chloride resin composition suitable for injection molding has been developed. As one of them, JP-A-3-146534 discloses that a vinyl chloride resin having a low degree of polymerization is also used as a main material, and a plasticizer, an impact-resistant agent, and a specific foaming agent are mixed in specific proportions. The following composition is disclosed, and at the same time, a proposal has been made on a rigid vinyl chloride resin foam molded article obtained by using this composition as a material and a method for producing the same.

【0006】しかしながら、この技術を用いて硬質塩化
ビニル系樹脂発泡成形体を得るには、上記公報に記載さ
れている通り、特別の射出成形機を使用し、特定の成形
条件の下で成形する必要があり、汎用されている通常の
射出成形機を用いたのでは、尚樹脂分解が発生したり、
発泡セルの分散が不均一であったり、ヒケが生ずる等、
良好な品質のものが得られず、更に発泡倍率の低下をも
引き起こすという問題点があった。
However, in order to obtain a rigid vinyl chloride resin foam molded article using this technique, as described in the above publication, a special injection molding machine is used and molding is performed under specific molding conditions. It is necessary to use a general-purpose injection molding machine that is widely used.
Dispersion of foam cells is uneven, sink marks occur, etc.
There was a problem in that good quality could not be obtained and the expansion ratio was also lowered.

【0007】[0007]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解消し、汎用されている通常の射出成形機
でも、発泡倍率が2倍を超える高発泡倍率の発泡体の成
形が可能であり、且つ外観形状等の品質にも優れた成形
体が得られる、射出成形用発泡塩化ビニル系樹脂組成物
を提供することを課題とする。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and even a general-purpose ordinary injection molding machine can form a foam having a high expansion ratio of more than 2 times. It is an object of the present invention to provide a foamed vinyl chloride resin composition for injection molding, which is capable of obtaining a molded product which is excellent in quality such as appearance.

【0008】[0008]

【課題を解決するための手段】本発明の射出成形用発泡
塩化ビニル系樹脂組成物は「塩化ビニル系樹脂100重
量部に、分子量が450万〜700万のポリメチルメタ
クリレート系樹脂2〜30重量部及び熱分解型発泡剤
0.5〜10重量部を配合してなること」を特徴とする
ものであり、このことにより上記課題が解決される。
The foamed vinyl chloride resin composition for injection molding according to the present invention is "2 to 30 parts by weight of polymethylmethacrylate resin having a molecular weight of 4.5 million to 7 million per 100 parts by weight of vinyl chloride resin. Parts and a pyrolytic foaming agent in an amount of 0.5 to 10 parts by weight. "

【0009】本発明に於いて使用する塩化ビニル系樹脂
としては、発泡成形体の素材として従来から使用されて
いるものであれば採用可能であり、例えば、塩化ビニル
単量体の単独重合体;塩化ビニル単量体と塩化ビニル単
量体以外の重合性単量体との共重合体;塩化ビニル系樹
脂以外の重合体に塩化ビニル単量体をグラフトさせたグ
ラフト共重合体;或いは、これらを乾式法や湿式法等の
従来公知の方法を用いて、後塩素化して得られる塩素化
塩化ビニル系重合体等が挙げられ、更にこれらの重合体
や共重合体の混合物も含まれる。
The vinyl chloride resin used in the present invention may be any one that has been conventionally used as a material for foamed molded articles, for example, a homopolymer of vinyl chloride monomer; Copolymer of vinyl chloride monomer and polymerizable monomer other than vinyl chloride monomer; Graft copolymer obtained by grafting vinyl chloride monomer on polymer other than vinyl chloride resin; or these Examples thereof include a chlorinated vinyl chloride polymer obtained by post-chlorination using a conventionally known method such as a dry method or a wet method. Further, a mixture of these polymers and copolymers is also included.

【0010】上記塩化ビニル系樹脂の平均重合度は、小
さ過ぎると成形体の機械的強度、特に耐衝撃性が低下す
る。又、逆に大き過ぎると成形時の溶融粘度が高くな
り、成形温度が高くなると共に剪断発熱が激しくなって
射出成形し難くなる上に発泡不良を引き起こすことがあ
る。従って、400〜1000が好ましく、より好まし
くは500〜800の範囲である。
If the average degree of polymerization of the above vinyl chloride resin is too small, the mechanical strength of the molded product, especially the impact resistance, will decrease. On the contrary, if it is too large, the melt viscosity at the time of molding becomes high, the molding temperature becomes high, the shear heat generation becomes intense, the injection molding becomes difficult, and the foaming failure may occur. Therefore, it is preferably 400 to 1000, and more preferably 500 to 800.

【0011】上記塩化ビニル単量体以外の重合性単量体
としては、反応性二重結合を有し、塩化ビニル単量体と
共重合可能なものであれば特に限定されず、例えば、エ
チレン、プロピレン、ブテン−1等のα−オレフィン
類;酢酸ビニル、プロピオン酸ビニル等のビニルエステ
ル類;ブチルビニルエーテル、セチルビニルエーテル等
のビニルエーテル類;メチルアクリレート、エチルアク
リレート等のアクリル酸エステル類;メチルメタクリレ
ート、エチルメタクリレート、フェニルメタクリレート
等のメタクリル酸エステル類;スチレン、α−メチルス
チレン等の芳香族ビニル類;塩化ビニリデン、ふっ化ビ
ニル等のハロゲン化ビニル類;N−フェニルマレイミ
ド、N−シクロヘキシルマレイミド等のN−置換マレイ
ミド類等が挙げられ、これらは単独で用いられて2種以
上が併用されてもよい。
The polymerizable monomer other than the vinyl chloride monomer is not particularly limited as long as it has a reactive double bond and can be copolymerized with the vinyl chloride monomer. , Α-olefins such as propylene and butene-1; vinyl esters such as vinyl acetate and vinyl propionate; vinyl ethers such as butyl vinyl ether and cetyl vinyl ether; acrylic acid esters such as methyl acrylate and ethyl acrylate; methyl methacrylate, Methacrylic acid esters such as ethyl methacrylate and phenyl methacrylate; aromatic vinyls such as styrene and α-methylstyrene; vinyl halides such as vinylidene chloride and vinyl fluoride; N such as N-phenylmaleimide and N-cyclohexylmaleimide -Substituted maleimides and the like, These may be used alone and two or more kinds may be used in combination.

【0012】上記グラフト共重合体に使用される塩化ビ
ニル系樹脂以外の重合体としては特に限定されず、例え
ば、エチレン−酢酸ビニル共重合体、エチレン−酢酸ビ
ニル−一酸化炭素共重合体、エチレン−エチルアクリレ
ート共重合体、エチレン−エチルアクリレート−一酸化
炭素共重合体、エチレン−メチルメタクリレート共重合
体、エチレン−プロピレン共重合体、アクリロニトリル
−ブタジエン共重合体、ポリウレタン、塩素化ポリエチ
レン、塩素化ポリプロピレン等が挙げられ、これらは単
独で用いられて2種以上が併用されてもよい。
The polymer other than the vinyl chloride resin used in the above graft copolymer is not particularly limited, and examples thereof include ethylene-vinyl acetate copolymer, ethylene-vinyl acetate-carbon monoxide copolymer, ethylene. -Ethyl acrylate copolymer, ethylene-ethyl acrylate-carbon monoxide copolymer, ethylene-methyl methacrylate copolymer, ethylene-propylene copolymer, acrylonitrile-butadiene copolymer, polyurethane, chlorinated polyethylene, chlorinated polypropylene And the like, and these may be used alone or in combination of two or more kinds.

【0013】本発明で使用されるポリメチルメタクリレ
ート系樹脂としては、ポリメチルメタクリレート、或い
はメチルメタクリレートを主体とし、これとエチルアク
リレート、アクリロニトリル、スチレン等との共重合体
等が挙げられる。また、上記ポリメチルメタクリレート
系樹脂の重量平均分子量は450万〜700万に制限さ
れ、且つその使用割合は塩化ビニル系樹脂100重量部
に対して2〜30重量部に限定され、好ましくは5〜2
0重量部である。
Examples of the polymethylmethacrylate resin used in the present invention include polymethylmethacrylate or methylmethacrylate as a main component, and a copolymer of this with ethylacrylate, acrylonitrile, styrene and the like. The weight average molecular weight of the polymethylmethacrylate resin is limited to 4.5 to 7,000,000, and the use ratio thereof is limited to 2 to 30 parts by weight, preferably 5 to 100 parts by weight of the vinyl chloride resin. Two
0 parts by weight.

【0014】上記ポリメチルメタクリレート系樹脂の重
量平均分子量が、450万に満たない場合は、有効な発
泡倍率のものが得られず、逆に700万を超えると、ポ
リメチルメタクリレート系樹脂の、成形時に於ける塩化
ビニル系樹脂中への分散が悪くなり、発泡性を向上させ
る効果が低下するだけでなく、溶融粘度が高くなって成
形性が悪化するばかりでなく、工業的に生産することが
次第に困難となる。
If the weight average molecular weight of the polymethylmethacrylate resin is less than 4.5 million, an effective expansion ratio cannot be obtained. Conversely, if it exceeds 7 million, molding of the polymethylmethacrylate resin will occur. At times, not only the dispersion in the vinyl chloride resin becomes poor and the effect of improving the foamability decreases, but not only the melt viscosity becomes high and the moldability deteriorates, but it can be produced industrially. It becomes difficult gradually.

【0015】又、上記分子量範囲のポリメチルメタクリ
レート系樹脂の使用量が、2重量部に満たない場合は、
有効な発泡倍率の成形体が得られず、逆に30重量部を
超えると、成形時の溶融粘度が高くなり成形し難くな
る。
When the amount of the polymethylmethacrylate resin in the above molecular weight range is less than 2 parts by weight,
If a molded product having an effective expansion ratio cannot be obtained and conversely exceeds 30 parts by weight, the melt viscosity at the time of molding becomes high and molding becomes difficult.

【0016】通常、押出成形では発泡性の安定化を図る
ために、分子量400万以下のポリメチルメタクリレー
ト系樹脂が使用されるが、分子量が450万以上のもの
を採用すると、溶融粘度上昇による成形性の悪化、熱分
解の発生に伴い、発泡性も悪化するので殆ど用いられる
ことがなかった。
Usually, in extrusion molding, a polymethylmethacrylate resin having a molecular weight of 4,000,000 or less is used in order to stabilize the foamability. However, when a resin having a molecular weight of 4.5,000,000 or more is used, molding due to an increase in melt viscosity occurs. Since the foamability deteriorates with the deterioration of the properties and the occurrence of thermal decomposition, it was hardly used.

【0017】本発明者等はこの点に関し種々研究した結
果、射出成形機の成形時に於いて、樹脂が受ける剪断速
度が速いので、分子量450万〜700万のポリメチル
メタクリレート系樹脂の採用が可能であることを見出し
た。即ち、この範囲のものを使用すると、溶融粘度が上
昇しても成形性にそれほど影響することがなく、しかも
所期の発泡倍率のものが安定して得られるようになった
のである。
As a result of various studies conducted by the present inventors on this point, the resin undergoes a high shear rate at the time of molding by an injection molding machine, so that a polymethylmethacrylate resin having a molecular weight of 4.5 to 7 million can be adopted. I found that. That is, by using those in this range, even if the melt viscosity is increased, the moldability is not affected so much, and the desired foaming ratio can be stably obtained.

【0018】本発明で使用される熱分解型発泡剤として
は、重炭酸ナトリウム、重炭酸アンモニウム、炭酸アン
モニウム等の熱分解型無機発泡剤;N,N′−ジニトロ
ソペンタメチレンテトラミン、N,N′−ジメチル−
N,N′−ジニトロソテレフタルアミド等のニトロソ化
合物;アゾジカルボンアミド、アゾビスイソブチロニト
リル等のアゾ化合物;ベンゼンスルホニルヒドラジド、
トルエンスルホニルヒドラジド等のスルホニルヒドラジ
ド化合物等の熱分解型有機発泡剤が挙げられる。これら
の熱分解型発泡剤は、単独で使用してもよく、2種以上
を併用してもよい。
Examples of the thermal decomposition type foaming agent used in the present invention include thermal decomposition type inorganic foaming agents such as sodium bicarbonate, ammonium bicarbonate and ammonium carbonate; N, N'-dinitrosopentamethylenetetramine, N, N. ′ -Dimethyl-
Nitroso compounds such as N, N'-dinitrosoterephthalamide; azo compounds such as azodicarbonamide and azobisisobutyronitrile; benzenesulfonylhydrazide,
Pyrolysis type organic foaming agents such as sulfonyl hydrazide compounds such as toluene sulfonyl hydrazide can be mentioned. These thermal decomposition type foaming agents may be used alone or in combination of two or more kinds.

【0019】上記熱分解型発泡剤の添加量は、所期の発
泡成形体の発泡倍率や品質特性等により種々設定すれば
よいが、塩化ビニル系樹脂100重量部に対して、0.
5〜10重量部である。もし添加量が0.5重量部に満
たない場合は有効な発泡倍率を得ることが困難であり、
10重量部を超える量を添加しても、それだけの効果が
得られず、発泡効率が悪くなって不経済である。
The amount of the heat-decomposable foaming agent added may be variously set according to the expansion ratio and quality characteristics of the desired foamed molded product, but is 0.
It is 5 to 10 parts by weight. If the added amount is less than 0.5 parts by weight, it is difficult to obtain an effective expansion ratio,
Even if the amount is more than 10 parts by weight, such an effect is not obtained and the foaming efficiency is deteriorated, which is uneconomical.

【0020】本発明の塩化ビニル系樹脂組成物には、必
要に応じて成形性、熱安定性、耐候性等を向上させるた
めに、熱安定剤、酸化防止剤、帯電防止剤、紫外線吸収
剤、滑剤、充填剤、難燃剤、可塑剤、顔料、塗料等を適
宜添加することができる。
The vinyl chloride resin composition of the present invention contains a heat stabilizer, an antioxidant, an antistatic agent, an ultraviolet absorber in order to improve moldability, heat stability, weather resistance and the like, if necessary. Lubricants, fillers, flame retardants, plasticizers, pigments, paints and the like can be added as appropriate.

【0021】上記熱安定剤としては、例えばジブチル錫
マレート、ジブチル錫メルカプト等の錫系;ステアリン
酸カルシウム、ステアリン酸バリウム、ステアリン酸亜
鉛等の有機金属石鹸系;ステアリン酸鉛等の鉛化合物系
等の熱安定剤が挙げられる。
Examples of the heat stabilizer include tin-based compounds such as dibutyltin malate and dibutyltin mercapto; organometallic soaps such as calcium stearate, barium stearate and zinc stearate; and lead compound systems such as lead stearate. A heat stabilizer is mentioned.

【0022】又、滑剤としては、例えばポリエチレンワ
ックス、パラフィンワックス等の脂肪族炭化水素系;ス
テアリルアルコール等の高級脂肪族アルコール系;ステ
アリン酸、ヒドロキシステアリン酸等の高級脂肪酸系;
ブチルステアレート等のモノアルコール脂肪酸エステル
系;グリセリンモノステアレート、グリセリントリステ
アレート等の多価アルコール脂肪酸エステル系等が挙げ
られる。
Examples of lubricants include aliphatic hydrocarbons such as polyethylene wax and paraffin wax; higher aliphatic alcohols such as stearyl alcohol; higher fatty acid such as stearic acid and hydroxystearic acid.
Examples include monoalcohol fatty acid ester such as butyl stearate; polyhydric alcohol fatty acid ester such as glycerin monostearate and glycerin tristearate.

【0023】又、難燃剤としては、例えばハロゲン系難
燃剤、リン系難燃剤、三酸化アンチモン等の金属酸化物
系難燃剤等が挙げられる。
Examples of the flame retardant include halogen flame retardants, phosphorus flame retardants, and metal oxide flame retardants such as antimony trioxide.

【0024】上述の各成分を配合するには、通常の塩化
ビニル系樹脂組成物の配合に採用される方法がそのまま
採用出来る。即ち、例えば各配合成分をヘンシェルミキ
サー等のミキサーに投入してミキシングを行い、均一に
混合すればよい。
In order to mix the above-mentioned respective components, the method adopted in the usual compounding of vinyl chloride resin composition can be directly adopted. That is, for example, the respective components may be added to a mixer such as a Henschel mixer and mixed to uniformly mix them.

【0025】本発明の発泡塩化ビニル系樹脂組成物を用
いて、射出成形する場合の成形条件としては、射出成形
機の成形温度を適正に管理する必要があり、樹脂や発泡
剤等の種類や添加量等により多少異なるので、一概には
いえないが、シリンダー温度としては、供給側温度(以
下C1 という)が80〜160℃、中央部温度(以下C
2 という)が100〜180℃、排出側温度(以下C3
という)が130〜200℃、ノズルヘッドの温度とし
ては、130〜200℃、金型温度としては20〜80
℃とするのが好ましい。
[0025] As molding conditions for injection molding using the expanded vinyl chloride resin composition of the present invention, it is necessary to properly control the molding temperature of the injection molding machine, the type of resin and foaming agent, and the like. since somewhat with an amount added, can not be said sweepingly, the cylinder temperature, supply temperature (hereinafter referred to as C 1) is 80 to 160 ° C., central temperature (hereinafter C
2 ) is 100-180 ℃, discharge side temperature (hereinafter C 3
Is 130 to 200 ° C, the temperature of the nozzle head is 130 to 200 ° C, and the mold temperature is 20 to 80 ° C.
C. is preferred.

【0026】(作用)本発明の射出成形用発泡塩化ビニ
ル系樹脂組成物は、塩化ビニル系樹脂とポリメチルメタ
クリレートと熱分解型発泡剤とを使用し、特にポリメチ
ルメタクリレートは、分子量が450万〜700万とい
う特定の範囲内にあるものを特定量使用するので、通常
の射出成形機による発泡成形が可能であり、ポリメチル
メタクリレートが塩化ビニル系樹脂中に均一に分散し、
成形材料の溶融粘度が適正に維持されて過度に発熱する
ことなく発泡セルの均一化を図ることができ、且つ有効
な高発泡倍率のものが得られる。
(Function) The foamed vinyl chloride resin composition for injection molding of the present invention uses a vinyl chloride resin, polymethylmethacrylate, and a thermal decomposition type foaming agent. Particularly, polymethylmethacrylate has a molecular weight of 4.5 million. Since a specific amount of ~ 7 million is used in a specific amount, foam molding by a normal injection molding machine is possible, and polymethylmethacrylate is uniformly dispersed in the vinyl chloride resin,
The melt viscosity of the molding material is appropriately maintained, the foam cells can be made uniform without excessive heat generation, and an effective high expansion ratio can be obtained.

【0027】[0027]

【発明の実施の形態】以下、本発明の実施の形態につい
て詳細に説明する。
Embodiments of the present invention will be described below in detail.

【0028】(実施例1〜4および比較例1〜7)表1
に示した各種材料配合の組合せからなるものを、ヘンシ
ェルミキサーに供給して均一に混合し、射出成形用発泡
塩化ビニル系樹脂組成物を得た。次に、これを射出成形
機(日本製鋼所社製、型式:JSWJ100E−C5)
に供給し、内径32mm、外径40mm、長さ80mm
の筒状成形体成形用の金型内に、下記成形条件にて射出
成形し、塩化ビニル系樹脂発泡成形体を得た。得られた
成形体に関する各種物性を下記評価方法で評価し、その
結果を表1に示す。
(Examples 1 to 4 and Comparative Examples 1 to 7) Table 1
A mixture of the various material formulations shown in 1 above was supplied to a Henschel mixer and uniformly mixed to obtain a foamed vinyl chloride resin composition for injection molding. Next, an injection molding machine (manufactured by Japan Steel Works, model: JSWJ100E-C5) was used.
, Inner diameter 32mm, outer diameter 40mm, length 80mm
Into a mold for molding a cylindrical molded body of No. 1 was injection-molded under the following molding conditions to obtain a vinyl chloride resin foam molded body. Various physical properties of the obtained molded product were evaluated by the following evaluation methods, and the results are shown in Table 1.

【0029】表1において、塩化ビニル樹脂(I)は平
均重合度600のもの、塩化ビニル樹脂(II)は平均重
合度800のもの、ポリメチルメタクリレート系樹脂
(I)は分子量470万のもの(三菱レーヨン社製、商
品名:メタブレンP−531)、ポリメチルメタクリレ
ート系樹脂(II)は分子量310万のもの(三菱レーヨ
ン社製、商品名:メタブレンP−530A)、ポリメチ
ルメタクリレート系樹脂(III)は分子量145万のもの
(三菱レーヨン社製、商品名:メタブレンP−551
A)をそれぞれ指す。
In Table 1, vinyl chloride resin (I) has an average degree of polymerization of 600, vinyl chloride resin (II) has an average degree of polymerization of 800, and polymethylmethacrylate resin (I) has a molecular weight of 4.7 million ( Mitsubishi Rayon Co., Ltd., trade name: Metabrene P-531), polymethylmethacrylate resin (II) having a molecular weight of 3.1 million (Mitsubishi Rayon Co., Ltd., trade name: Metabrene P-530A), polymethylmethacrylate resin (III ) Has a molecular weight of 1.45 million (trade name: METABLEN P-551 manufactured by Mitsubishi Rayon Co., Ltd.).
A) respectively.

【0030】又、表1に示した各種配合材料には、上記
塩化ビニル樹脂とポリメチルメタクリレート系樹脂の他
に、熱分解型無機発泡剤(永和化成工業社製、商品名:
セルボンSC−D)4重量部、充填剤(白石工業社製、
商品名:CCR)5重量部、錫系安定剤(三共有機社
製、商品名:ONZ−142F)2重量部、ポリエチレ
ンワックス(三井石油化学社製、商品名:Hiwax4
202E)1重量部、グリセリンモノステアレート(理
研ビタミン社製、商品名:リケマールS─100)1重
量部、エステル系滑剤(理研ビタミン社製、商品名:S
L−02)0.5重量部をそれぞれ配合した。
In addition to the vinyl chloride resin and the polymethylmethacrylate resin, the various compounding materials shown in Table 1 also include a thermal decomposition type inorganic foaming agent (trade name: manufactured by Eiwa Chemical Industry Co., Ltd .:
Cerbon SC-D) 4 parts by weight, filler (manufactured by Shiraishi Industry Co., Ltd.,
Trade name: CCR) 5 parts by weight, tin stabilizer (manufactured by Sansha Machine Co., Ltd., trade name: ONZ-142F) 2 parts by weight, polyethylene wax (manufactured by Mitsui Petrochemical Co., Ltd., trade name: Hiwax4)
202E) 1 part by weight, glycerin monostearate (manufactured by Riken Vitamin Co., trade name: RIKEMAL S-100) 1 part by weight, ester lubricant (manufactured by Riken Vitamin Co., trade name: S)
L-02) 0.5 part by weight was blended.

【0031】又、成形条件は次のように設定した。 ・成形温度 C1 =170℃、C2 =175℃、C3 =180℃、ノ
ズルヘッド=185℃ ・スクリュー回転速度=15%、・射出速度=70%、
・射出圧力=70% ・保圧=0%、・背圧=5%、・金型温度=40℃ ・射出時間=10秒、・冷却時間=60秒 ・計量=樹脂が完全に充満する量(発泡倍率等により変
更)とした。
The molding conditions were set as follows.・ Molding temperature C 1 = 170 ° C., C 2 = 175 ° C., C 3 = 180 ° C., nozzle head = 185 ° C. ・ Screw rotation speed = 15%, ・ Injection speed = 70%,
・ Injection pressure = 70% ・ Holding pressure = 0%, ・ Back pressure = 5%, ・ Mold temperature = 40 ° C ・ Injection time = 10 seconds, ・ Cooling time = 60 seconds ・ Measurement = Amount completely filled with resin (Changed depending on the expansion ratio, etc.).

【0032】又、評価方法は次の通りである。 発泡倍率 得られた発泡成形体の見掛け密度をASTM−D−15
65に準拠して測定し、その測定値をもとに次式により
算出した。 発泡倍率=樹脂組成物の非発泡見掛け密度/発泡成形体
の見掛け密度 発泡セル状態 得られた発泡成形体の断面を光学顕微鏡で観察し、次の
判定基準により評価した。 ○=セルが均一に分散、△
=セルの分散状態がやや不均一 ×=セルの分散状態が不均一 外観形状 得られた発泡成形体の外観形状を目視により観察し、次
の判定基準により評価した。 ○=ヒケがない、△=ヒケが少しある、×=ヒケが大き
The evaluation method is as follows. Foaming ratio The apparent density of the foamed molded product obtained was determined according to ASTM-D-15.
It measured based on 65 and calculated by the following formula based on the measured value. Foaming ratio = Apparent density of non-foaming resin composition / Apparent density of foamed molded product Foamed cell state The cross section of the foamed molded product was observed with an optical microscope and evaluated according to the following criteria. ○ = cells are evenly distributed, △
= Slightly non-uniform cell distribution state == Non-uniform cell dispersion state Appearance The appearance of the foamed molded product obtained was visually observed and evaluated according to the following criteria. ○ = No sink mark, △ = Slight sink mark, × = Large sink mark

【0033】[0033]

【表1】 [Table 1]

【0034】表1の結果から明らかなように、塩化ビニ
ル樹脂に対して、特定範囲の分子量を持つポリメチルメ
タクリレート系樹脂を適量に配合した各実施例の場合
は、所期の品質のものが得られたのに対し、特定範囲の
分子量を持たないポリメチルメタクリレート系樹脂を使
用した比較例1〜3および5の場合は、何れも発泡倍率
が2倍に満たないものであり、更に比較例5の場合は、
発泡セル分散状態の悪いものが得られた。
As is clear from the results shown in Table 1, in the case of each example in which a suitable amount of polymethylmethacrylate resin having a molecular weight in a specific range was blended with vinyl chloride resin, the desired quality was obtained. On the other hand, in the cases of Comparative Examples 1 to 3 and 5 in which the polymethylmethacrylate resin having no specific range of molecular weight was used, the expansion ratio was less than 2 times, In case of 5,
A foamed cell with a poor dispersion state was obtained.

【0035】又、実施例と同じポリメチルメタクリレー
ト系樹脂を使用したが、使用量の少ない比較例4の場合
は、所期の発泡倍率が得られず、発泡セルの分散状態も
好ましいものではなく、同じく使用量の少ない比較例6
の場合は、発泡倍率が極端に低く、しかも発泡セル分散
状態が悪く、外観形状も好ましいものではなかった。
又、実施例と同じポリメチルメタクリレートを、特定範
囲を越えて多量に使用した比較例7の場合は、発泡倍
率、発泡セル状態及び外観形状全てに劣るものであっ
た。
Although the same polymethylmethacrylate resin as in Example was used, but in the case of Comparative Example 4 in which the amount used was small, the desired expansion ratio could not be obtained, and the dispersed state of the foam cells was not preferable either. , Comparative Example 6 which also uses a small amount
In the case of No. 2, the expansion ratio was extremely low, the dispersed state of the foam cells was poor, and the appearance shape was not preferable.
Further, in the case of Comparative Example 7 in which the same polymethylmethacrylate as that used in Example was used in a large amount exceeding the specific range, the foaming ratio, foamed cell state and appearance shape were all inferior.

【0036】[0036]

【発明の効果】本発明の射出成形用発泡塩化ビニル系樹
脂組成物は、塩化ビニル系樹脂とポリメチルメタクリレ
ート系樹脂と熱分解型発泡剤とを使用し、特にポリメチ
ルメタクリレート系樹脂は、分子量が450万〜700
万という特定の範囲内にあるものを特定量使用したの
で、通常の射出成形機でも発泡倍率が2倍を超えるもの
が得られ、且つ外観形状等の品質にも優れた発泡成形体
が得られる。従って、既存の射出成形機の使用による製
造コストの低減が可能であり、且つ用途範囲が拡大され
る。
The foamed vinyl chloride resin composition for injection molding of the present invention uses a vinyl chloride resin, a polymethylmethacrylate resin, and a thermal decomposition type foaming agent, and in particular, the polymethylmethacrylate resin has a molecular weight of Is 4.5 million to 700
Since a specific amount within the specific range of 10,000 is used, a foaming ratio of more than 2 can be obtained even with an ordinary injection molding machine, and a foamed product excellent in quality such as appearance shape can be obtained. . Therefore, the manufacturing cost can be reduced by using the existing injection molding machine, and the range of applications can be expanded.

───────────────────────────────────────────────────── 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 B29K 27:06 105:04 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location B29K 27:06 105: 04

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 塩化ビニル系樹脂100重量部に、重量
平均分子量が450万〜700万のポリメチルメタクリ
レート系樹脂2〜30重量部及び熱分解型発泡剤0.5
〜10重量部を配合してなることを特徴とする射出成形
用発泡塩化ビニル系樹脂組成物。
1. 100 parts by weight of a vinyl chloride resin, 2 to 30 parts by weight of a polymethylmethacrylate resin having a weight average molecular weight of 4.5 to 7 million, and 0.5 parts of a thermal decomposition type foaming agent.
A foamed vinyl chloride resin composition for injection molding, which is characterized by containing 10 to 10 parts by weight.
JP7311324A 1995-11-29 1995-11-29 Foamable vinyl chloride resin composition for injection molding Pending JPH09151269A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7311324A JPH09151269A (en) 1995-11-29 1995-11-29 Foamable vinyl chloride resin composition for injection molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7311324A JPH09151269A (en) 1995-11-29 1995-11-29 Foamable vinyl chloride resin composition for injection molding

Publications (1)

Publication Number Publication Date
JPH09151269A true JPH09151269A (en) 1997-06-10

Family

ID=18015772

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7311324A Pending JPH09151269A (en) 1995-11-29 1995-11-29 Foamable vinyl chloride resin composition for injection molding

Country Status (1)

Country Link
JP (1) JPH09151269A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000212355A (en) * 1999-01-26 2000-08-02 Asahi Chem Ind Co Ltd Styrene-based resin composition
WO2001070862A1 (en) * 2000-03-21 2001-09-27 Kaneka Corporation Foamable vinyl chloride resin composition
WO2002012378A1 (en) * 2000-08-08 2002-02-14 Kaneka Corporation Expandable vinyl chloride resin composition
US6723762B1 (en) 1999-09-22 2004-04-20 Kaneka Corporation Foamable vinyl chloride-base resin compositions
US6765033B1 (en) 1999-01-18 2004-07-20 Kaneka Corporation Expandable vinyl chloride resin composition

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6765033B1 (en) 1999-01-18 2004-07-20 Kaneka Corporation Expandable vinyl chloride resin composition
JP2000212355A (en) * 1999-01-26 2000-08-02 Asahi Chem Ind Co Ltd Styrene-based resin composition
US6723762B1 (en) 1999-09-22 2004-04-20 Kaneka Corporation Foamable vinyl chloride-base resin compositions
WO2001070862A1 (en) * 2000-03-21 2001-09-27 Kaneka Corporation Foamable vinyl chloride resin composition
US6610757B2 (en) 2000-03-21 2003-08-26 Kaneka Corporation Foamable vinyl chloride resin composition
WO2002012378A1 (en) * 2000-08-08 2002-02-14 Kaneka Corporation Expandable vinyl chloride resin composition
US6635687B2 (en) * 2000-08-08 2003-10-21 Kaneka Corporation Expandable vinyl chloride resin composition

Similar Documents

Publication Publication Date Title
US4394460A (en) Ethylene-chlorotrifluoroethylene copolymer foam
US4331619A (en) Ethylene-chlorotrifluoroethylene copolymer foam
US4632942A (en) Resin composition for masterbatch of foaming agent
EP1310519B1 (en) Expandable vinyl chloride resin composition
JP3374356B2 (en) Method for producing foam molded article and foam molded article
JPH09151269A (en) Foamable vinyl chloride resin composition for injection molding
JP4612266B2 (en) Thermoplastic resin molded article excellent in wood texture and method for producing the same
US20050137341A1 (en) Foamable polyvinyl chloride compound tolerant of high heat conditions
JPH1160868A (en) Vinyl chloride resin composition for foam extrusion
JPH0873641A (en) Resin molding composition for high-density plastic foam
JPS6140707B2 (en)
JPH04239046A (en) Foamable vinyl chloride composition
JPH07157587A (en) Vinyl chloride-based resin composition
JPH09143298A (en) Vinyl chloride-based resin composition
JPS5840986B2 (en) Method for producing polyvinyl chloride resin foam moldings
JP3555636B2 (en) Vinyl chloride resin composition for foam molding
JPH09124825A (en) Foamed vinylchloride-based resin composition for injection molding
JPH0859874A (en) Vinyl chloride resin composition
JPH07228742A (en) Vinyl chloride resin composition
JP3514551B2 (en) Low foam molding resin composition
JPS6132338B2 (en)
JPH0449863B2 (en)
JPH1025384A (en) Highly packed foamable resin composition having hydrogen chloride scavenging ability and its molding
JPS60135440A (en) Foamed molding of vinyl chloride resin and its manufacture
JPH09124826A (en) Hard-type foamed material of vinylchloride-based resin