JPH01110549A - Fomable plastisol composition - Google Patents

Fomable plastisol composition

Info

Publication number
JPH01110549A
JPH01110549A JP26905787A JP26905787A JPH01110549A JP H01110549 A JPH01110549 A JP H01110549A JP 26905787 A JP26905787 A JP 26905787A JP 26905787 A JP26905787 A JP 26905787A JP H01110549 A JPH01110549 A JP H01110549A
Authority
JP
Japan
Prior art keywords
vinyl chloride
parts
weight
injection molding
foam
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
JP26905787A
Other languages
Japanese (ja)
Inventor
Toshiro Igarashi
敏郎 五十嵐
Tsuguo Mitani
三谷 嗣雄
Shukuyu Nakatsuji
中辻 淑裕
Makoto Shimada
誠 島田
Eiji Makita
牧田 栄司
Osamu Endo
修 遠藤
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.)
Kobayashi KK
Sumitomo Chemical Co Ltd
Original Assignee
Kobayashi KK
Sumitomo 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 Kobayashi KK, Sumitomo Chemical Co Ltd filed Critical Kobayashi KK
Priority to JP26905787A priority Critical patent/JPH01110549A/en
Publication of JPH01110549A publication Critical patent/JPH01110549A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain the above composition suitable for interior automative trim materials and building materials, having high melt fluidity and excellent low-pressure injection molding properties, by blending a resin consisting of a vinyl chloride-based polymer with a vinyl chloride-ethylene copolymer. CONSTITUTION:(A) 100pts.wt. vinyl chloride-based resin consisting of A1: 60-95 pts.wt. vinyl chloride-based polymer having 0.1-20mum average particle diameter useful for paste obtained by emulsion polymerization or micro-suspension polymerization and A2: 40-5pts.wt. vinyl chloride-ethylene copolymer having 400-2,000 average polymerization degree and 0.5-20wt.% ethylene content is blended with (B) 50-150pts.wt. plasticizer (e.g., dioctyl phthalate), (C) 0.5-15 pts.wt. stabilizer, (D) 0.5-10pts.wt. blowing agent and (E) 2-40pts.wt., preferably 5-30pts.wt. hollow glass beads having 10-200mum diameter, 0.8-0.9g/cc specific gravity and >=1,000kg/cm<2> compression strength.

Description

【発明の詳細な説明】 〈産業との利用分野〉 本発明は塩化ビニル重合体からなる発泡体を成形するた
めの射出成形用とくに低圧射出成形性に優れたポリ塩化
ビニル系発泡性プラスチゾル組成物に関する。
[Detailed description of the invention] <Field of industrial application> The present invention provides a polyvinyl chloride-based foamable plastisol composition that is particularly excellent in low-pressure injection moldability for injection molding to mold a foam made of a vinyl chloride polymer. Regarding.

〈従来の技術〉 可塑剤を含む軟質ポリ塩化ビニル樹脂にアゾジカルボン
アミド等の化学発泡剤を混合し射出成形して得た可塑化
ポリ塩化ビニル発泡体は、風合、耐薬品性、耐候性、難
燃性等の点でオレフィン系熱可塑性樹脂発泡体よりも優
れており、近年これらの特徴を生かして自動車内装材、
家具、雑貨用品等の分野で多用されているうこれまで可
塑化ポリ塩化ビニル系発泡体は懸濁重合またはバルク重
合により得られた平均粒子径が150uml後の一般の
ポリ塩化ビニル樹脂と可塑剤、安定剤、発泡剤等を混合
し、ス−パーミキサー等を用いてポリ塩化ビニル樹脂に
可塑剤を吸収さしてドライアップして得た粉末状のコン
パウンドや、これをさらに押出機で押出して得たペレッ
ト状のコンパウンドを射出成形して製造されてきた。
<Prior art> Plasticized polyvinyl chloride foam obtained by injection molding a mixture of a soft polyvinyl chloride resin containing a plasticizer and a chemical blowing agent such as azodicarbonamide has excellent texture, chemical resistance, and weather resistance. , is superior to olefin thermoplastic resin foam in terms of flame retardancy, etc., and in recent years, these characteristics have been utilized to develop automobile interior materials,
Up until now, plasticized polyvinyl chloride foams, which have been widely used in the fields of furniture, miscellaneous goods, etc., have been produced by suspension polymerization or bulk polymerization, with an average particle size of 150 um, and are made from general polyvinyl chloride resin and plasticizer. , stabilizers, foaming agents, etc. are mixed, the plasticizer is absorbed into polyvinyl chloride resin using a super mixer, etc., and the resulting powder is dried up. It has been manufactured by injection molding a pellet-shaped compound.

しかし、上記の方法で得た可塑化塩化ビニル樹脂の粉末
状コンパウンドやペレット状コンパウンドは溶融粘度が
高く、溶融流動性が低いために射出成形時に高い射出圧
力と大きな型締力が必要であり、このためにウレタンフ
オーム等射出時の圧力により形状が損なわれやすい部材
をインサートしたりアウトサートすることが出来ないと
か、良好な表面状態と均一なスキン層を持ったセルの均
一な発泡体が得られないとか、複雑な形状の成形体が得
にくい等櫨々の問題点があった。
However, the powdered and pelleted compounds of plasticized vinyl chloride resin obtained by the above method have high melt viscosity and low melt fluidity, so high injection pressure and large mold clamping force are required during injection molding. For this reason, it is not possible to insert or outsert parts such as urethane foam whose shape is easily damaged by the pressure during injection, and it is not possible to obtain a foam with uniform cells with a good surface condition and a uniform skin layer. There have been many problems, such as the inability to produce molded products and the difficulty in obtaining molded products with complex shapes.

特開昭59−215880号公譲には、ポリ塩化ビニル
゛樹脂に発泡剤を添加した配合物に平均粒径10〜20
0μmの中空ガラスビーズを充填した発泡ぼり塩化ビニ
ル系樹脂組成物が良好な成形加工性を示し、軽量で表面
状態の良好な成形品が得られると記載されているうこの
方法では添加する中空ガラスビーズの作用により軽量な
成形品は得られるが、比較例に示されているように配合
物をスーパーミキサーで混合してドライアップし、押出
機で作成したペレットを用いて射出成形する方法では溶
融流動性が低く、射出圧が高いために均一なスキン層を
持った発泡体が得られず、また、インサートやアウトサ
ートする部材に制限を受けるなど不十分である。
JP-A No. 59-215880 discloses that a compound containing a polyvinyl chloride resin and a blowing agent has an average particle size of 10 to 20.
It is stated that a foamed vinyl chloride resin composition filled with 0 μm hollow glass beads exhibits good molding processability, and that a molded product that is lightweight and has a good surface condition can be obtained. Lightweight molded products can be obtained due to the action of beads, but as shown in the comparative example, the method of mixing the compound in a super mixer, drying it up, and injection molding using pellets made with an extruder does not melt the product. Since the fluidity is low and the injection pressure is high, a foam with a uniform skin layer cannot be obtained, and there are restrictions on the parts that can be inserted or outsert, making it unsatisfactory.

又、均一なスキン層を持った発泡体を得る目的で、特開
昭55−75488号公報には非発泡性可塑化塩化ビニ
ル系Ji[組成物からなるペレットとアクリル系樹脂お
よび/またはエチレン−酢酸ビニル共重合体を含む発泡
性可塑化塩化ビニル系樹脂組成物からなるペレットを混
合した射出成形用樹脂組成物が記載されている。
In addition, for the purpose of obtaining a foam having a uniform skin layer, JP-A-55-75488 discloses that a non-expandable plasticized vinyl chloride-based Ji [composition consisting of pellets, an acrylic resin and/or an ethylene-based A resin composition for injection molding is described in which pellets of a foamable plasticized vinyl chloride resin composition containing a vinyl acetate copolymer are mixed.

しかし、この方法では溶融流動性が低く、射出圧が高い
ために複雑な形状の成形体が得にくいとか、インサート
やアウトサートする部材に制限を受けるなどと記問題点
をすべて解決する方法では)い。
However, this method does not solve all of the problems mentioned above, such as low melt flowability and high injection pressure, making it difficult to obtain molded bodies with complex shapes, and restrictions on the parts that can be inserted and outsert. stomach.

〈発明が解決しようとする問題点〉 本発明は前記のような従来技術のもつ問題点を解決し、
溶融流動性が耳く、小さな型締カ!低い射出圧力によっ
て射出成形が可能で、良好な表面状態と均一なスキン層
を持った発泡体が通常の射出成形機で成形できる発泡性
プラスチゾル組成物を得ることにある。
<Problems to be solved by the invention> The present invention solves the problems of the prior art as described above,
A small mold clamping force with excellent melt fluidity! To obtain a foamable plastisol composition which can be injection molded at low injection pressure and which can be molded into a foam having a good surface condition and a uniform skin layer using an ordinary injection molding machine.

〈問題点を解決するための手段〉 本発明者らは溶融流動性が高く、低い射出圧力によって
射出成形が可能な発泡剤を含む軟質ポリ塩化ビニル系樹
脂組成物について種々研究を重ね、本発明の完成に散っ
た。
<Means for Solving the Problems> The present inventors have conducted various studies on flexible polyvinyl chloride resin compositions containing a foaming agent that have high melt fluidity and can be injection molded with low injection pressure, and have developed the present invention. Scattered to completion.

すなわち、本発明は平均粒径が0.1〜20μmの塩化
ビニル系重合体60〜95]!量部と塩化ビニル−エチ
レン共重合体40〜5重量部からなる塩化ビニル系aw
iooiit量部に可塑剤50〜150itffi部と
、安定剤、発泡剤及び中空ガラスビーズを配合すること
を特徴とする発泡性プラスチゾル組成物に関するつ本発
明の平均粒径が0.1〜20μ情の塩化ビニル系重合体
は塩化ビニル単独あるいは塩化ビニルと塩化ビニルに対
し共重合性を有する他の単量体との混合物を乳化重合法
またはミクロ懸濁重合法により製造することができ、一
般にペースト用塩化ビニル系重合体窃貨として知られて
いるう 平均粒子径が0.1μmより小さいと発泡性プラスチゾ
ル組成物の粘度が高くなり不都合であろつ又、平均粒子
径が20μmより大きいと溶融流動性を高くする効果が
損なわれ好ましくないつ塩化ビニルと共重合しうる単量
体としては脂肪酸ビニルエステル、アルキルビニルエー
テル、アクリル酸アルキルエステル、メタクリル酸アル
キルエステル、アクリロニトリル、エチプラスチゾル組
成物の粘度安定性や製品物性の点で10!1%以下が好
ましい。
That is, the present invention uses vinyl chloride polymers with an average particle size of 0.1 to 20 μm 60 to 95]! vinyl chloride-based aw consisting of 40 to 5 parts by weight of vinyl chloride-ethylene copolymer
The present invention relates to an expandable plastisol composition characterized in that 50 to 150 parts of a plasticizer, a stabilizer, a blowing agent, and hollow glass beads are blended to 1 part of IOOIIT, and the average particle size of the present invention is 0.1 to 20μ. Vinyl chloride polymers can be produced by emulsion polymerization or microsuspension polymerization using vinyl chloride alone or a mixture of vinyl chloride and other monomers that are copolymerizable with vinyl chloride, and are generally used for pastes. If the average particle diameter is smaller than 0.1 μm, the viscosity of the expandable plastisol composition will increase, which is disadvantageous, and if the average particle diameter is larger than 20 μm, the melt flowability will decrease. Examples of monomers that can undesirably copolymerize with vinyl chloride, such as impairing the effect of increasing the From the viewpoint of product physical properties, it is preferably 10!1% or less.

本発明にて用いる塩化ビニル−エチレン共重合体は、一
般公知の方法で製造し得るものでよく、平均重合度が4
00〜2000で、エチレン含有故が0.5〜20重短
チ、好ましくは0.5〜10重量%の範囲のものが使用
される。エチレン含有駄が0.5瓜Skπより少ないと
溶融流動性の改良効果がなく、逆にエチレン含冑スが2
゜Xi 11%より多くなるとプラスチゾルの粘度が高
くなり不都合であろう 平均粒径が0.1〜20μmの塩化ビニル系重合体と塩
化ビニル−エチレン共重合体の配合割合は、塩化ビニル
系重合体60〜96重ユ部に対し、塩化ビニル−エチレ
ン共重合体40〜5重量部の範囲で用いらn;1、塩化
ビニル−エチレン共重合体が5ffift部より少ない
と溶融流動性の改良効果が不十分であり、逆に40tf
J部より多いとプラスチゾルの粘度が高くなり不都合で
あり、また得られる発泡体の風合いも損なわれ好ましく
ないつ 本発明で用いる可塑剤としてはジオクチルフタレート→
で示されるフタル酸エステル可塑剤、トリクレジルホス
フェート等で示されるリン酸エステル可塑剤、ジオクチ
ルアジペート等で示塑剤、ジー2−エチルへキシルアゼ
レート等で示されるアゼライン酸エステル可塑剤、クエ
ン酸トリブチル等で示されるクエン酸エステル可塑剤、
ブチルフタリル”if zlJ/リコレート等で示され
るグリコール酸エステル可塑剤、トリー2−エチルへキ
シルトリメリテート等で示されるトリメリット酸エステ
ル可塑剤、ジー2−エチルへキシルテレフタレート等で
示されるフタル酸異性体エステル可塑剤、ポリプロピレ
ンアジペート等で示されるぼりエステル系可塑剤、エボ
キレ化大豆油等で示されるエポキシ系可塑剤等公知の可
塑剤を使用することができる。可塑剤の配合量は、塩化
ビニル系樹脂100重量部に対し50〜150重量部の
範囲で使用される。可塑剤の使用量が50[を部以下だ
と溶融流動性が低下し、また製品の風合いが硬くなり好
ましくない。逆に可塑剤の使用量が150Wf1部以と
になると製品が軟らか(なりすぎ、また可塑剤のブリー
ドによる製品表面のべたつきが生じ好ましくない。
The vinyl chloride-ethylene copolymer used in the present invention may be produced by a generally known method, and has an average degree of polymerization of 4.
00 to 2000, and the ethylene content is 0.5 to 20% by weight, preferably 0.5 to 10% by weight. If the ethylene content is less than 0.5 Skπ, there will be no improvement in melt fluidity; on the other hand, if the ethylene content is less than 2
゜Xi If it exceeds 11%, the viscosity of the plastisol will increase, which would be disadvantageous. The vinyl chloride-ethylene copolymer is used in a range of 40-5 parts by weight per 60-96 parts by weight.If the amount of the vinyl chloride-ethylene copolymer is less than 5 parts by weight, the effect of improving melt fluidity is Not enough, on the contrary, 40tf
If the amount exceeds the J part, the viscosity of the plastisol increases, which is disadvantageous, and the texture of the resulting foam is also impaired, which is undesirable.As the plasticizer used in the present invention, dioctyl phthalate→
phthalate ester plasticizers represented by , phosphate ester plasticizers represented by tricresyl phosphate, plasticizers such as dioctyl adipate, azelaic ester plasticizers represented by di-2-ethylhexyl azelate, etc. Citrate ester plasticizers represented by tributyl acid, etc.
Glycolic acid ester plasticizers such as butylphthalyl"if zlJ/licorate, trimellitic acid ester plasticizers such as tri-2-ethylhexyl trimellitate, and phthalic acid isomers such as di-2-ethylhexyl terephthalate. Known plasticizers such as polyester plasticizers, polyester plasticizers such as polypropylene adipate, and epoxy plasticizers such as evaporated soybean oil can be used.The blending amount of the plasticizer is as follows: It is used in the range of 50 to 150 parts by weight per 100 parts by weight of the plasticizer.If the amount of plasticizer used is less than 50 parts, the melt fluidity will decrease and the texture of the product will become hard, which is undesirable. If the amount of plasticizer used is less than 1 part of 150 Wf, the product will become too soft (too much) and the surface of the product will become sticky due to bleeding of the plasticizer, which is undesirable.

本発明に用いられる安定剤は変色を防止するために添加
され、その使用にはペースト用塩化ビニル樹脂と塩化ビ
ニル−エチレン共重合樹脂の合計100ffiffi部
に対し、約157it量部以下0.5mSi部以とであ
るうこのような安定剤としては脂肪酸のバリウム、匪鉛
、カドミウム、鉛、錫及びカルシウムの塩の錯化合物等
が挙げられる。
The stabilizer used in the present invention is added to prevent discoloration, and its use includes 0.5 mSi part of up to about 157 it parts to a total of 100 ffiffiffi parts of the vinyl chloride resin for paste and the vinyl chloride-ethylene copolymer resin. Examples of such stabilizers include complex compounds of barium, lead, cadmium, lead, tin and calcium salts of fatty acids.

ために添加され、その使用量は塩化ビニル系樹8110
0ii部に対し、0.5重量部以上10if量部以下で
ある。0.6N量部以下だと製品の風合いやソフト感の
改良効果が不十分でありat化効果も不十分である。1
0を置部以上だと発泡倍率が高くなりすぎて発泡体のセ
ル状態が悪くなりすぎ、またこのため均一なスキン層の
形成が防げられろう使用される発泡剤としてはアゾジカ
ルボンアミドやアゾビスイソブチロニトン リル等で示されるアゾ系発泡剤、ジニトロ)tぺ′ソ 等で示されるヒドラジド系発泡剤、トリヒドラジノトリ
アジン、重炭酸ナトリウム等で示されとを併用するとア
ゾジカルボンアミドの分解残置による着色や臭いのない
発泡体が得られる。
The amount used is PVC 8110
The amount is 0.5 parts by weight or more and 10 parts by weight or less with respect to 0 parts by weight. If the amount is less than 0.6 parts by weight, the effect of improving the texture and soft feel of the product will be insufficient, and the effect of attenuating the product will also be insufficient. 1
If the value of 0 is higher than 0, the foaming ratio will be too high and the cell condition of the foam will be too poor, and this will prevent the formation of a uniform skin layer.The foaming agent used is azodicarbonamide or azobis. When used in combination with an azo blowing agent represented by isobutyronitonol, etc., a hydrazide blowing agent represented by dinitro)tpe'so, trihydrazinotriazine, sodium bicarbonate, etc., azodicarbonamide decomposes and remains. A foam that is free from coloration and odor can be obtained.

本発明において用いられる中空ガラスビーズは製品を軽
1化し、発泡剤の分解時に造核剤的な働きをして発泡セ
ルの均一化を行ない、また溶1流動性を高めるなど多く
の効果を合わせ持つ重要な添加剤で島り、比重が0,3
〜0.9 t/ccで直径が10〜200μmで圧縮強
度が100Kg/ a4以上の欠陥のない真球に近いも
のである。
The hollow glass beads used in the present invention have many effects, such as making the product lighter, acting as a nucleating agent when the blowing agent decomposes, making the foam cells uniform, and increasing the fluidity of the melt. Due to the important additives that it has, the specific gravity is 0.3
~0.9 t/cc, a diameter of 10 to 200 μm, and a compressive strength of 100 Kg/a4 or more, which is close to a perfect sphere without defects.

比重が0.8 f/cc以下だと成形時に破損し好まし
くな(、逆に0.9g/ccを超えると軽量化効果が不
十分となる。直径が1011m以下だと溶融流動性を高
める効果が不十分であり逆に200μmを超えると製品
の表面がざらつき外観が損なわれ好ましくない、圧縮強
度が100Kt/a4以下だと成形時β破損し好ましく
ない。中空ガラスピースの使用量は塩化ビニル系樹11
1100逗澁部に対し、2i1!j1部以上40重ff
i部以下である。、2Wi部以下だと上記の添加効果が
不十分であり、逆に40’gg量部より多いと製品表面
がざらつき外鍋が損なわれ、引裂き強度や引張強度が低
下するなど製品物性が低下し好ましくない。
If the specific gravity is less than 0.8 f/cc, it will break during molding, which is undesirable (on the contrary, if it exceeds 0.9 g/cc, the weight reduction effect will be insufficient. If the diameter is less than 1011 m, it will be effective in increasing melt fluidity. On the other hand, if it exceeds 200 μm, the surface of the product will be rough and the appearance will be impaired, which is undesirable. If the compressive strength is less than 100 Kt/a4, β breakage will occur during molding, which is undesirable. The amount of hollow glass pieces used is vinyl chloride type. Tree 11
2i1 against 1100 Zubu! J 1 copy or more 40 folds FF
I part or less. If it is less than 2 Wi parts, the above-mentioned effect of addition will be insufficient, and conversely, if it is more than 40'g parts, the product surface will be rough, the outer pot will be damaged, and the physical properties of the product will deteriorate, such as tear strength and tensile strength. Undesirable.

本発明の発泡性プラスチゾル組成物には上記の添加剤以
外に必要に応じて希釈用塩化ビニル樹脂、増粘剤、希釈
剤、セル調整剤、抗菌化剤、紫外線吸収剤、麺燃剤、充
填剤、着色剤、帯電防止剤、架橋剤、滑剤等が用いられ
る。なかでも滑剤の使用は成形性の改良に大きな役割を
果す。この目的のために用いられる滑剤としてはマグネ
シウムやアルミニウムなどの金属石けんが挙げられ、そ
の使用量は塩化ビニル系樹脂100重量部に対し、5重
量部以下で用いられる。5iltfii部以上用いると
発泡性が損なわれるなどの不都合が生じ好ましくないつ 本発明の発泡性プラスチゾル組成物は常温で流動性のあ
るペースト状であり、ライカイ機、ニーダ−、ホバート
疋キサ−、デイスパー、インクロール等の通常のプラス
チゾル混練装はを用いて配合混練される。
In addition to the above-mentioned additives, the foamable plastisol composition of the present invention may optionally contain a vinyl chloride resin for dilution, a thickener, a diluent, a cell conditioner, an antibacterial agent, an ultraviolet absorber, a noodle retardant, and a filler. , colorants, antistatic agents, crosslinking agents, lubricants, etc. are used. Among these, the use of lubricants plays a major role in improving moldability. Examples of the lubricant used for this purpose include metal soaps such as magnesium and aluminum, and the amount used is 5 parts by weight or less per 100 parts by weight of the vinyl chloride resin. If more than 5 parts of plastisol is used, problems such as loss of foaming properties may occur, which is undesirable. Ordinary plastisol kneading equipment such as ink rolls are used for blending and kneading.

本発明の発泡性プラスチゾル組成物は、常温で流動性の
あるペースト状態のまま通常の射出成形機で成形が可能
である。
The expandable plastisol composition of the present invention can be molded in a paste state that is fluid at room temperature using a conventional injection molding machine.

状態にし、これを粉砕したものを通常の射出成形機で成
形してもよい。
This may be crushed and molded using a normal injection molding machine.

本発明の発泡性プラスチゾル組成物は腐い流′動性を有
し、低い射出圧力で成形できるため、良好な表面状態と
均一なスキン層を持ち風合いに優れた発泡体が1回の射
出成形で得られる。
The foamable plastisol composition of the present invention has good fluidity and can be molded at low injection pressure, so a foam with good surface condition, a uniform skin layer, and excellent texture can be produced in a single injection molding process. It can be obtained with

また、発泡ウレタンなど形状の損なわれやすい材質をも
った部材でもアウトサートやインサートが可能であるな
ど工iaJ:大きな利点を持っており、自動車内装材や
建材、雑貨など幅広い工業分野で使用される。
In addition, it has great advantages such as being able to outsert and insert parts made of materials that easily lose their shape, such as urethane foam, and is used in a wide range of industrial fields such as automobile interior materials, building materials, and miscellaneous goods. .

以下に実施例により、本発明の詳細な説明するが、本発
明はこれらは実施例により制限されるものではないつ 実施例1 ミクロ懸濁重合法によって得た平均粒子径が1.2μm
で平均重合度が1700のペースト用塩化ビニル樹脂(
注文化学工業(株)スミリット@)l”XQHA)80
重量部と懸濁重合法によって得たエチレン含96重t%
、平均重合度800、平均粒子径180μmの塩化ビニ
ル−エチレン共重合m1li201tffi部に可塑剤
としてジウンデシルフタレートを95重量部、錫系安定
剤を5重量部、発泡剤としてアゾジカルボンアミド2に
!2部と一1yyt滑剤2重量部を配合し、ニーダ−で
混練後真空説泡してプラスチゾルを得た。このプラスチ
ゾルに平均粒径60μm、比重0.6で圧縮強度が70
0Kt15Mの中空ガラスビーズを20X!量部添加混
合して射出成形原料となる発泡性プラスチゾル組成物を
得た。
The present invention will be described in detail with reference to Examples below, but the present invention is not limited to these Examples.
Vinyl chloride resin for paste with an average degree of polymerization of 1700 (
Order Kagaku Kogyo Co., Ltd. Sumirit@)l”XQHA)80
Part by weight and 96% by weight of ethylene obtained by suspension polymerization method
, 95 parts by weight of diundecyl phthalate as a plasticizer, 5 parts by weight of a tin-based stabilizer, and 2 parts of azodicarbonamide as a blowing agent! 2 parts by weight of lubricant and 2 parts by weight of lubricant were mixed in a kneader and foamed under vacuum to obtain plastisol. This plastisol has an average particle size of 60 μm, a specific gravity of 0.6, and a compressive strength of 70.
0Kt15M hollow glass beads 20X! A foamable plastisol composition to be used as a raw material for injection molding was obtained by adding and mixing a certain amount.

この発泡性プラスチゾル組成物はBL型粘度計轟40−
ター6rpm(測定温度25°C)の条件で測定した粘
度が作成直後で2500cp(センチポイズ)、25℃
55にRHの条件で1週間放置したあとで、290GC
I)であも、取り扱いやすく、しかも保存安定性の良い
原料であった。
This foamable plastisol composition was tested using a BL type viscometer, Todoroki 40-
The viscosity measured at 6 rpm (measurement temperature 25°C) was 2500 cp (centipoise) immediately after preparation at 25°C.
After leaving it for a week under RH condition of 55, 290GC
However, it was a raw material that was easy to handle and had good storage stability.

この発泡性プラスチゾル組成物を使用し、新潟鉄工新製
$1’1J−1518射出成形機を用表に示す。
This foamable plastisol composition was used in a $1'1J-1518 injection molding machine manufactured by Niigata Iron Works as shown in the table below.

(射出成形条件) Cs   l B 0°C C2100℃ Cm   160℃ ノズル195℃ 保圧(ゲージ圧’)   100Ktt/cd射出時間
    16秒 金型温度   80℃ い最低の圧力で操作したところ20に#/jの非常に低
い射出圧力で成形できた。PJられな成形体は、均一な
厚さのスキン層を持ったセル状態の良好な発泡体であり
、表面状態も良好で風合いも優れたものであった。
(Injection molding conditions) Cs l B 0°C C2100°C Cm 160°C Nozzle 195°C Holding pressure (gauge pressure') 100Ktt/cd Injection time 16 seconds Mold temperature 80°C When operated at the lowest pressure, it reached 20#/ Molding was possible at a very low injection pressure. The PJ resin molded product was a foam with a good cell condition and a skin layer of uniform thickness, and had a good surface condition and an excellent texture.

実施例2〜4 発泡性プラスチゾル組成物の配合を第1表に示すように
変更した以外は実施例1と全(同様の方法で発泡性プラ
スチゾル組成物を作成し、実施例1と射出圧力を除いて
他は全く同一の方法で射出成形を行ない、平板状の試験
片を得た。結果を第1表に示した。
Examples 2 to 4 Same as Example 1 except that the formulation of the expandable plastisol composition was changed as shown in Table 1 (expandable plastisol compositions were prepared in the same manner as in Example 1, and the injection pressure was Injection molding was carried out in exactly the same manner except for the following: A flat test piece was obtained.The results are shown in Table 1.

イスレの発泡性プラスチゾル組成物も粘度が低く、粘度
安定性が良く、低圧でシーートシ■ッ卜することなしに
射出成形が出来、得られた成形体は均一な厚さのスキン
r−を持ったセル状態の良好な発泡体であり、表面状態
も良好で風合いも優れたものであった。
Isure's foamable plastisol composition also has a low viscosity and good viscosity stability, and can be injection molded at low pressure without sheet sealing, and the resulting molded product has a skin of uniform thickness. The foam had a good cell condition, a good surface condition, and an excellent texture.

比較例1〜6 発泡性プラスチゾル組成物の配合を第1表に示すように
変更した以外は実施例1と全く同様の方法で発泡性プラ
スチゾル組成物を作成し、実施例1と射出圧力を除いて
他は全く同一の方法で射出成形を行ない平板状の成形体
を得たう但し、比較例8は射出成形出来ず成形体を得ら
れなかった。
Comparative Examples 1 to 6 Expandable plastisol compositions were prepared in exactly the same manner as in Example 1, except that the formulation of the expandable plastisol composition was changed as shown in Table 1, and the compositions were prepared in the same manner as in Example 1 except for the injection pressure. Except for this, injection molding was carried out in the same manner as above to obtain a plate-shaped molded product. However, in Comparative Example 8, injection molding could not be performed and no molded product could be obtained.

結果を@1表に示した。The results are shown in Table @1.

比較例1は射出圧力が高く成形体のスキン層の均一性が
悪く、発泡セルの状態や表面状態も不満足なものであっ
た。比較例2はプラスチゾルの粘度変化が大きく作業性
が不良であり、また、発泡体のセル状態、表面状態も不
十分であり、風合いも悪かった。
In Comparative Example 1, the injection pressure was high, the uniformity of the skin layer of the molded article was poor, and the condition of the foamed cells and the surface condition were also unsatisfactory. In Comparative Example 2, the plastisol had a large viscosity change, resulting in poor workability, and the foam had insufficient cell and surface conditions, as well as poor texture.

比較例8はプラスチゾルの粘度が高く作業性が悪い上、
射出圧力に高圧を要し、実施例1と同一条件では射出成
形できなかった。
Comparative Example 8 had high plastisol viscosity and poor workability.
High injection pressure was required, and injection molding could not be performed under the same conditions as in Example 1.

比蒙例4は、発泡体の表面がべとつき、また風合いが軟
らか過ぎて問題であったつ比較例5は射出圧力が高く、
発泡体のスキン層の均一性が悪く、発泡セル、表面状態
も不十分であったつ比較例6は発泡体の表面がざらつい
て悪く風合い不良であった。
In Comparative Example 4, the surface of the foam was sticky and the texture was too soft, and in Comparative Example 5, the injection pressure was high.
The skin layer of the foam had poor uniformity, and the foam cells and surface condition were also insufficient. In Comparative Example 6, the surface of the foam was rough and had poor texture.

比較例7 ペースト用塩化ビニル樹udを、懸鵡重合法によって得
た平均粒子径が120μmで平均重合度が1700のポ
リ塩化ビニル樹宙(任友化学工業(株)スミリット05
X−17)に置き換えたほかは実施例1と全く同一の配
合物をスーパーミキサーで混合し、単軸押出機で押出し
てペレットを得た。これを実施例1と射出圧力を除いて
他は全く同一の方法で射出成形を行なったが、射出圧力
が高くなりすぎて成形体が得られなかった。
Comparative Example 7 A polyvinyl chloride resin UD for paste having an average particle diameter of 120 μm and an average degree of polymerization of 1700 obtained by a hanging parrot polymerization method (Sumirit 05, manufactured by Ninyu Chemical Industry Co., Ltd.) was used.
The same formulation as in Example 1 except that X-17) was used was mixed in a super mixer and extruded in a single screw extruder to obtain pellets. This was injection molded in exactly the same manner as in Example 1 except for the injection pressure, but the injection pressure was too high and no molded product could be obtained.

比較例8 比較例7で得たペレットを用い、新潟鉄工新製5N−1
518射出成形機を用い、下記平板状の成形体を得た。
Comparative Example 8 Using the pellets obtained in Comparative Example 7, Niigata Tekko Shinsei 5N-1
Using a 518 injection molding machine, the following plate-shaped molded product was obtained.

結果を@1表に示すな。Do not show the results in @1 table.

(射出成形条件) C+    180°C保圧(ゲージ圧) 150Kq
/adC214G’C射出時間   15秒 Cs    160°C金型温度   ao’″Cノズ
ル  195°C型締圧    15 Q TON表面
状態も不満足なものであった。
(Injection molding conditions) C+ 180°C holding pressure (gauge pressure) 150Kq
/adC214G'C Injection time 15 seconds Cs 160°C Mold temperature ao'''C Nozzle 195°C Mold clamping pressure 15 Q TON surface condition was also unsatisfactory.

Claims (3)

【特許請求の範囲】[Claims] (1)平均粒径が0.1〜20μmの塩化ビニル系重合
体60〜95重量部と塩化ビニル−エチレン共重合体4
0〜5重量部からなる塩化ビニル系樹脂100重量部に
可塑剤50〜150重量部と、安定剤、発泡剤及び中空
ガラスビーズを配合することを特徴とする発泡性プラス
チゾル組成物。
(1) 60 to 95 parts by weight of vinyl chloride polymer with an average particle size of 0.1 to 20 μm and 4 parts by weight of vinyl chloride-ethylene copolymer
1. A foamable plastisol composition comprising 50 to 150 parts by weight of a plasticizer, a stabilizer, a foaming agent, and hollow glass beads to 100 parts by weight of a vinyl chloride resin consisting of 0 to 5 parts by weight.
(2)前記塩化ビニル系重合体が乳化重合法またはミク
ロ懸濁重合法で製造されたペースト用塩化ビニル系重合
体である特許請求の範囲第1項記載の発泡性プラスチゾ
ル組成物。
(2) The expandable plastisol composition according to claim 1, wherein the vinyl chloride polymer is a paste vinyl chloride polymer produced by an emulsion polymerization method or a microsuspension polymerization method.
(3)前記中空ガラスビーズが、直径10〜200μm
、比重が0.8〜0.9g/ccかつ圧縮強度が100
kg/cm^2以上であり、その配合量が前記塩化ビニ
ル系樹脂100重量部に対し2〜40重量部、好ましく
は5〜30重量部配合した特許請求の範囲第1項記載の
発泡性プラスチゾル組成物。
(3) The hollow glass beads have a diameter of 10 to 200 μm
, specific gravity of 0.8 to 0.9 g/cc and compressive strength of 100
kg/cm^2 or more, and the foamable plastisol according to claim 1, wherein the amount is 2 to 40 parts by weight, preferably 5 to 30 parts by weight, based on 100 parts by weight of the vinyl chloride resin. Composition.
JP26905787A 1987-10-23 1987-10-23 Fomable plastisol composition Pending JPH01110549A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26905787A JPH01110549A (en) 1987-10-23 1987-10-23 Fomable plastisol composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26905787A JPH01110549A (en) 1987-10-23 1987-10-23 Fomable plastisol composition

Publications (1)

Publication Number Publication Date
JPH01110549A true JPH01110549A (en) 1989-04-27

Family

ID=17467063

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26905787A Pending JPH01110549A (en) 1987-10-23 1987-10-23 Fomable plastisol composition

Country Status (1)

Country Link
JP (1) JPH01110549A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001342316A (en) * 2000-06-02 2001-12-14 Kanegafuchi Chem Ind Co Ltd Vinyl chloride paste resin composition and disposable glove
JP2018131594A (en) * 2017-02-17 2018-08-23 タキロンシーアイ株式会社 Foamable vinyl chloride-based resin paste and vinyl chloride-based resin foamed sheet using the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001342316A (en) * 2000-06-02 2001-12-14 Kanegafuchi Chem Ind Co Ltd Vinyl chloride paste resin composition and disposable glove
JP2018131594A (en) * 2017-02-17 2018-08-23 タキロンシーアイ株式会社 Foamable vinyl chloride-based resin paste and vinyl chloride-based resin foamed sheet using the same

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