JPH04255331A - Manufacture of vinyl chloride foam - Google Patents
Manufacture of vinyl chloride foamInfo
- Publication number
- JPH04255331A JPH04255331A JP3038114A JP3811491A JPH04255331A JP H04255331 A JPH04255331 A JP H04255331A JP 3038114 A JP3038114 A JP 3038114A JP 3811491 A JP3811491 A JP 3811491A JP H04255331 A JPH04255331 A JP H04255331A
- Authority
- JP
- Japan
- Prior art keywords
- foam
- foaming
- vinyl chloride
- microwave
- 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
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Molding Of Porous Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は塩化ビニル発泡体、特に
肉厚物を短時間に製造する方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing vinyl chloride foams, particularly thick-walled products, in a short time.
【0002】0002
【従来の技術】従来の塩化ビニル発泡体の製造方法とし
ては特公昭46−2184号公報、特公昭63−757
4号公報、および特公昭53−7944号公報等が知ら
れている。[Prior Art] Conventional methods for producing vinyl chloride foam are disclosed in Japanese Patent Publication No. 46-2184 and Japanese Patent Publication No. 63-757.
4, Japanese Patent Publication No. 53-7944, etc. are known.
【0003】0003
【発明が解決しようとする課題】しかしながら、この種
方法により製造される発泡体の厚さは、熱伝導が悪いの
とスコーチ発生の関係で約10mm位までしか製造でき
ず、その製造時間は10時間位を要し、かつ設備も巨大
であった。[Problems to be Solved by the Invention] However, the thickness of the foam produced by this type of method can only be about 10 mm due to poor heat conduction and scorch generation, and the production time is about 10 mm. It took a long time and the equipment was huge.
【0004】0004
【課題を解決するための手段】本発明はこのような欠点
を除去するため、型内の温度が表面だけでなく発泡体の
中心まで超音波によって短時間に、かつ均一に加温する
ことによって均一セルの厚物、例えば厚さが約20〜5
0mmの発泡体を従前の1/2〜1/5位の短時間で製
造できる方法を提案するものである。[Means for Solving the Problem] In order to eliminate such drawbacks, the present invention uses ultrasonic waves to quickly and uniformly heat the inside of the mold not only on the surface but also on the center of the foam. Thick material with uniform cells, e.g. thickness of about 20-5
We propose a method that can produce foams of 0 mm in a short time, about 1/2 to 1/5 of the time required by conventional methods.
【0005】[0005]
【実施例】以下に、本発明に係る塩化ビニル発泡体の製
造法の一実施例について図面を用いて詳細に説明する。
すなわち、図1はその製造工程を示すブロック図であり
、架橋型のポリ塩化ビニル発泡体を型内でマイクロ波に
より加熱して所定倍率に発泡体を形成する方法である。EXAMPLE Hereinafter, an example of the method for producing a vinyl chloride foam according to the present invention will be described in detail with reference to the drawings. That is, FIG. 1 is a block diagram showing the manufacturing process, which is a method in which a crosslinked polyvinyl chloride foam is heated in a mold using microwaves to form a foam to a predetermined magnification.
【0006】さらに説明すると、本発明におけるポリ塩
化ビニル発泡体は主にポリ塩化ビニル樹脂、架橋剤、可
塑剤、安定剤、発泡剤等からなり、架橋熱処理の際の接
着性で他面材と直接に一体に接着すると共に、10〜6
0倍位の発泡体を形成したものである。さらに説明する
と、ポリ塩化ビニル樹脂としては塩化ビニル単独のポリ
マーおよび、塩化ビニル酢酸ビニル、アクリル酸エステ
ル、ビニルエーテル、ビニルエステル、エチレン等との
共重合体の1種からなるものである。なお、ポリ塩化ビ
ニル樹脂の粘度は分子量を変化させることによって低減
させることができる。To explain further, the polyvinyl chloride foam of the present invention mainly consists of a polyvinyl chloride resin, a crosslinking agent, a plasticizer, a stabilizer, a foaming agent, etc., and has adhesive properties during crosslinking heat treatment to other surface materials. In addition to directly gluing them together, 10 to 6
This is a foam that is approximately 0 times larger. To explain further, the polyvinyl chloride resin is composed of a polymer of vinyl chloride alone and a copolymer of vinyl chloride with vinyl acetate, acrylic ester, vinyl ether, vinyl ester, ethylene, etc. Note that the viscosity of the polyvinyl chloride resin can be reduced by changing the molecular weight.
【0007】上記架橋触媒としては4級アンモニウム塩
等であり、添加量は塩化ビニル系樹脂100重量部に対
し0.01〜5重量部位である。また、架橋触媒として
は4級アンモニウム塩のみ、その他架橋助剤を使用する
ことが好ましく、架橋助剤の一例としては2ケ以上のカ
ルボキシル基を有する多価カルボン酸金属塩、エポキシ
樹脂を用いることが好ましい。The crosslinking catalyst is a quaternary ammonium salt or the like, and the amount added is 0.01 to 5 parts by weight per 100 parts by weight of the vinyl chloride resin. Further, as a crosslinking catalyst, it is preferable to use only a quaternary ammonium salt and other crosslinking aids. Examples of crosslinking aids include metal salts of polycarboxylic acids having two or more carboxyl groups, and epoxy resins. is preferred.
【0008】塩化ビニル発泡体の発泡剤としては100
〜250℃で分解し、ガスを発生させる化合物、例えば
独立気泡組織にはアゾジカルボンアミドが好ましく、そ
の他水酸化アルミニウム(250〜350℃)、ホウ酸
亜鉛(330℃)は連通気泡の発泡組織を形成するのに
用いる。100 as a blowing agent for vinyl chloride foam
Compounds that decompose at ~250°C and generate gas, such as azodicarbonamide, are preferred for closed cell structures, while aluminum hydroxide (250~350°C) and zinc borate (330°C) are preferred for open cell foam structures. used to form
【0009】前記した架橋剤および接着剤として機能す
る多価エポキシ化合物は1分子中に2ケ以上のエポキシ
基を持つ化合物が用いられる。例えばエポキシ化大豆油
、エポキシ化アマニ油、エピクロルヒドリンとビスフェ
ノールAとを縮合させて得られる通称エポキシ樹脂等で
あって、塩化ビニル系樹脂もしくはそれらの可塑剤と或
る程度の相溶性を持つ化合物である。なお、多価エポキ
シ化合物の量は、塩化ビニル系樹脂100重量部に対し
て1から50重量部の範囲である。[0009] As the polyvalent epoxy compound that functions as the crosslinking agent and adhesive described above, a compound having two or more epoxy groups in one molecule is used. For example, epoxidized soybean oil, epoxidized linseed oil, commonly known as epoxy resin obtained by condensing epichlorohydrin and bisphenol A, etc., which are compounds that have a certain degree of compatibility with vinyl chloride resins or their plasticizers. be. The amount of the polyvalent epoxy compound is in the range of 1 to 50 parts by weight based on 100 parts by weight of the vinyl chloride resin.
【0010】前記したエポキシ硬化剤としては通常のエ
ポキシ樹脂硬化剤である。その具体例としては例えばア
ミン化合物、ジアミン化合物、ポリアミン化合物、ポリ
アミド、アミノ酸類、二個以上のカルボキシル基を持つ
多塩基性酸及びその酸無水物等の1種からなるものであ
る。なお、アミン硬化剤とエポキシ化合物との反応は極
めて速いために、一般の塩化ビニル系樹脂の使用条件に
不適な場合が多いが、塗料の場合は有用である。また、
一般反応条件に適当な硬化剤はアミノ酸、例えばε−ア
ミノカプロン酸等、二塩基性酸、例えばアジピン酸等、
酸無水物、例えば無水コハク酸、無水マレイン酸、無水
フタル酸、無水トリメリット酸、無水ピロメリット酸、
メチルヘキサヒドロ無水フタル酸等、及びこれら多塩基
性酸とグライコールとの縮合物等が有用であり、単独も
しくは共用して用いる。なお、エポキシ硬化剤の量は、
塩化ビニル系樹脂100重量部に対して0.2から20
重量部の範囲である。The above-mentioned epoxy curing agent is a common epoxy resin curing agent. Specific examples thereof include one of amine compounds, diamine compounds, polyamine compounds, polyamides, amino acids, polybasic acids having two or more carboxyl groups, and acid anhydrides thereof. Since the reaction between the amine curing agent and the epoxy compound is extremely fast, it is often unsuitable for the usage conditions of general vinyl chloride resins, but it is useful for paints. Also,
Suitable curing agents for the general reaction conditions are amino acids, such as epsilon-aminocaproic acid, dibasic acids, such as adipic acid, etc.
Acid anhydrides, such as succinic anhydride, maleic anhydride, phthalic anhydride, trimellitic anhydride, pyromellitic anhydride,
Methylhexahydrophthalic anhydride and the like, and condensates of these polybasic acids and glycol are useful, and can be used alone or in combination. In addition, the amount of epoxy curing agent is
0.2 to 20 per 100 parts by weight of vinyl chloride resin
Parts by weight range.
【0011】前記した可塑剤としては例えばフタール酸
ジオクチル等は任意に使用できる。従って本発明によっ
て硬質から軟質に及ぶ広範囲の架橋塩化ビニル系樹脂発
泡体となる。[0011] As the above-mentioned plasticizer, for example, dioctyl phthalate can be used as desired. Therefore, the present invention provides a wide range of crosslinked vinyl chloride resin foams ranging from hard to soft.
【0012】前記した安定剤は塩化ビニル系樹脂の架橋
反応に直接的に作用するので、その種類と配合量に注意
を要する。その一例としては二塩基性フタル酸鉛、三塩
基性硫酸鉛、ラウリン酸亜鉛等で添加量は塩化ビニル系
樹脂100重量部に対し0.5〜5重量部位である。Since the above-mentioned stabilizer acts directly on the crosslinking reaction of the vinyl chloride resin, care must be taken regarding its type and amount. For example, dibasic lead phthalate, tribasic lead sulfate, zinc laurate, etc. are added in an amount of 0.5 to 5 parts by weight per 100 parts by weight of the vinyl chloride resin.
【0013】本発明で使用する軽量骨材はパーライト粒
、バーミキュライト、炭酸カルシウム、シラスバルーン
、水酸化アルミニウム、ケイ酸カルシウムの1種からな
り、芯材となる発泡体の機械強度、防火性の向上または
発泡剤としても役立つものである。[0013] The lightweight aggregate used in the present invention is composed of one of pearlite grains, vermiculite, calcium carbonate, shirasu balloons, aluminum hydroxide, and calcium silicate, and improves the mechanical strength and fire retardant properties of the foam core material. Or it can serve as a blowing agent.
【0014】前記した整泡剤はシリコンで発泡組織のセ
ルを均一形状にするのに役立ち、発泡体全体の強度アッ
プ、断熱性能の向上と樹脂量の低減を図りコストダウン
にも寄与するものである。[0014] The above-mentioned foam stabilizer is silicone and helps to make the cells of the foam structure into a uniform shape, which increases the strength of the entire foam, improves the heat insulation performance, and reduces the amount of resin, which also contributes to cost reduction. be.
【0015】本発明では使用するマイクロ波としては塩
化ビニル発泡体の原料が架橋、発泡あるいは発泡の際に
発泡途中の発泡体の中心層を加熱するためである。その
周波数としては2450MHZ、出力0.5〜5KW位
であり、その被加熱空間は1〜5mm位、幅は30〜9
00mm、空間高さは5〜100mm位である。勿論図
示しないカバー内のローラ等で被加熱物が搬送される空
間の際は上記長さ等に制限されないものである。In the present invention, the microwave used is for heating the center layer of the foam in the process of crosslinking, foaming, or foaming the raw material of the vinyl chloride foam. The frequency is 2450MHz, the output is about 0.5~5KW, the space to be heated is about 1~5mm, and the width is 30~9mm.
00 mm, and the spatial height is about 5 to 100 mm. Of course, in the case of a space in which an object to be heated is conveyed by a roller or the like in a cover (not shown), the length is not limited to the above.
【0016】本発明によって製造される塩化ビニル発泡
体Aの片面、あるいは両面には図2に示すように面材B
として紙、アスファルトフェルト、クラフト紙、アスベ
スト紙等を用いる。[0016] On one side or both sides of the vinyl chloride foam A produced according to the present invention, a facing material B is provided as shown in Fig. 2.
Paper, asphalt felt, kraft paper, asbestos paper, etc. are used as materials.
【0017】本発明に係る塩化ビニル発泡体の製造法に
ついて図1を用いて説明すると、塩化ビニル樹脂1、発
泡剤2、溶剤3等の発泡体組成物を密閉ニーダ4に同時
に吹き付け、次にこの組成物を押出機5に供給し、その
後に所定型6に送給して加熱しながら成形する。この際
、型内にはマイクロ波が照射される構造とし、発泡途中
の組成物の外周面、次に発泡途中の組成物の中心部をマ
イクロ波で加熱し、冷却して脱型する。この方法では発
泡時間が従前の1/2以下に短縮され、かつ肉厚20〜
30mmの中心部も表層と同様のセル構造となっていた
。The method for producing a vinyl chloride foam according to the present invention will be explained using FIG. 1. A foam composition including a vinyl chloride resin 1, a blowing agent 2, a solvent 3, etc. is simultaneously sprayed into a closed kneader 4, and then This composition is supplied to an extruder 5, and then fed to a predetermined mold 6 and molded while being heated. At this time, the inside of the mold is structured to be irradiated with microwaves, and the outer circumferential surface of the composition that is being foamed and then the center of the composition that is being foamed are heated by microwaves, cooled, and removed from the mold. With this method, the foaming time is reduced to less than half of the conventional foaming time, and the wall thickness is 20~
The 30 mm center portion also had the same cell structure as the surface layer.
【0018】以上、説明したのは本発明に係る塩化ビニ
ル発泡体の製造法の一実施例にすぎず、図3に示すよう
な方法によっても上記発泡体を製造できる。すなわち混
合機7、混合された発泡体組成物(プラチナゾル)を連
続ベルト上型8に厚さ3mmで吐出し、次に架橋発泡炉
9に送給して50倍の発泡体を得た。この炉9は上、下
型不織布がベルトで上型の上方にマイクロ波照射機と熱
風送風機があり、表面の加温と発泡体の中心層の加熱を
移動中に行うことができるものである。What has been described above is only one embodiment of the method for producing a vinyl chloride foam according to the present invention, and the above foam can also be produced by the method shown in FIG. 3. That is, the mixer 7 discharged the mixed foam composition (platinum sol) onto the continuous belt upper die 8 to a thickness of 3 mm, and then fed it to the crosslinking and foaming furnace 9 to obtain a foam 50 times larger. In this furnace 9, the upper and lower mold nonwoven fabrics are belts, and above the upper mold there is a microwave irradiator and a hot air blower, so that the surface heating and the central layer of the foam can be heated during movement. .
【0019】なお、上記発泡体の配合例としては、配合
割合
ポリ塩化ビニル
100重量部 ジオク
チルアジペート
20重量部 ブチルベンジルフタレ
ート(可塑剤) 20重量部
エポキシ化アマニ油
5重量部 無水トリ
メット(架橋助剤)
2重量部 三塩基性硫酸鉛(安定剤)
10重量
部 シリコーン(整泡剤)
1重量部 アゾジ
カルボンアミド
10重量部 酸化ポリエチレン(滑
剤)
2重量部 酸化亜鉛(発泡助剤)
1重量部
臭化テトラプロピルアンモニウム
1重量部 パーライト粒(増量剤
、骨材) 50重
量部である。[0019] As a blending example of the above foam, the blending ratio: polyvinyl chloride
100 parts by weight dioctyl adipate
20 parts by weight Butylbenzyl phthalate (plasticizer) 20 parts by weight
Epoxidized linseed oil
5 parts by weight Anhydrous Trimet (crosslinking aid)
2 parts by weight tribasic lead sulfate (stabilizer)
10 parts by weight Silicone (foam stabilizer)
1 part by weight azodicarbonamide
10 parts by weight polyethylene oxide (lubricant)
2 parts by weight Zinc oxide (foaming aid)
1 part by weight
Tetrapropylammonium bromide
1 part by weight Perlite grains (filler, aggregate) 50 parts by weight.
【0020】[0020]
【発明の効果】上述したように本発明に係る塩化ビニル
発泡体の製造方法によれば、■塩化ビニル発泡体を従前
の2倍以上の速度で生産できる。■厚肉物、例えば20
〜50mmも容易に、かつ均一セルの発泡組織で製造で
き、しかも歩留まりが向上し、さらに製造時間が大幅に
短縮される。等の特徴がある。As described above, according to the method for producing vinyl chloride foam according to the present invention, (1) vinyl chloride foam can be produced at a rate more than twice that of the conventional method. ■Thick-walled items, e.g. 20
50 mm can be easily manufactured with a foamed structure of uniform cells, the yield is improved, and the manufacturing time is significantly shortened. It has the following characteristics.
【図1】本発明に係る塩化ビニル発泡体の製造法の一例
を示す説明図である。FIG. 1 is an explanatory diagram showing an example of a method for producing a vinyl chloride foam according to the present invention.
【図2】本発明に係る製造法によって得られる塩化ビニ
ル発泡体の断面の一例を示す説明図である。FIG. 2 is an explanatory diagram showing an example of a cross section of a vinyl chloride foam obtained by the manufacturing method according to the present invention.
【図3】本発明に係る塩化ビニル発泡体の製造法のその
他の実施例を示す説明図である。FIG. 3 is an explanatory diagram showing another example of the method for producing a vinyl chloride foam according to the present invention.
A 塩化ビニル発泡体 4 密閉ニーダ 6 型 7 混合機 8 連続ベルト上型 9 架橋発泡炉 A Vinyl chloride foam 4 Closed kneader 6 type 7 Mixer 8 Continuous belt upper mold 9 Crosslinking foaming furnace
Claims (1)
における加熱工程をマイクロ波により行うことを特徴と
する塩化ビニル発泡体の製造法。1. A method for producing a vinyl chloride foam, characterized in that the heating step during foaming in producing the vinyl chloride foam is performed using microwaves.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3038114A JPH04255331A (en) | 1991-02-06 | 1991-02-06 | Manufacture of vinyl chloride foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3038114A JPH04255331A (en) | 1991-02-06 | 1991-02-06 | Manufacture of vinyl chloride foam |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04255331A true JPH04255331A (en) | 1992-09-10 |
Family
ID=12516450
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3038114A Pending JPH04255331A (en) | 1991-02-06 | 1991-02-06 | Manufacture of vinyl chloride foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04255331A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012170334A (en) * | 2011-02-17 | 2012-09-10 | Kizakura Co | Method for producing float for fishing |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58142828A (en) * | 1982-02-17 | 1983-08-25 | Toyoda Gosei Co Ltd | Manufacture of inside foamed molded product |
| WO1990008803A1 (en) * | 1987-05-04 | 1990-08-09 | The Dow Chemical Company | Foamable thermoplastic polymers and a method for foaming |
-
1991
- 1991-02-06 JP JP3038114A patent/JPH04255331A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58142828A (en) * | 1982-02-17 | 1983-08-25 | Toyoda Gosei Co Ltd | Manufacture of inside foamed molded product |
| WO1990008803A1 (en) * | 1987-05-04 | 1990-08-09 | The Dow Chemical Company | Foamable thermoplastic polymers and a method for foaming |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012170334A (en) * | 2011-02-17 | 2012-09-10 | Kizakura Co | Method for producing float for fishing |
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