JPH02292015A - Manufacture of foam rubber molding - Google Patents

Manufacture of foam rubber molding

Info

Publication number
JPH02292015A
JPH02292015A JP1111270A JP11127089A JPH02292015A JP H02292015 A JPH02292015 A JP H02292015A JP 1111270 A JP1111270 A JP 1111270A JP 11127089 A JP11127089 A JP 11127089A JP H02292015 A JPH02292015 A JP H02292015A
Authority
JP
Japan
Prior art keywords
extruder
extruded
molding
screw
dimensions
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
JP1111270A
Other languages
Japanese (ja)
Inventor
Seiji Murakawa
村川 聖二
Masami Yamada
山田 正巳
Tetsuya Bando
坂東 徹也
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.)
Toyoda Gosei Co Ltd
Original Assignee
Toyoda Gosei 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 Toyoda Gosei Co Ltd filed Critical Toyoda Gosei Co Ltd
Priority to JP1111270A priority Critical patent/JPH02292015A/en
Publication of JPH02292015A publication Critical patent/JPH02292015A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92009Measured parameter
    • B29C2948/92114Dimensions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92428Calibration, after-treatment, or cooling zone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/9259Angular velocity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92885Screw or gear

Abstract

PURPOSE:To manufacture a foam rubber molding capable of setting excellent dimensional accuracy of a molding and having less control loss by measuring the dimension of an extrusion molding extruded from an extruder, and increasing or decreasing the speed of a screw of the extruder on the basis of the increase of decrease of the dimension. CONSTITUTION:The tape base material 2 of a rubber material is held in a accommodation container 3, and then supplied into a hopper 4 on the upper part of an extruder 1. In the extruder 1, a cylinder 6 having a screw 5 inside is disposed, which extrudes a rubber material from the hopper 4. In the tip end of the extruder 1, a die 7 is attached thereon, which forms an extruded molding P extruded by the screw 5. Ahead of the extruder 1, an optical dimension measuring unit 8 is arranged for irradiating light on the extruded molding P and measuring successively the dimension thereof. And, ahead of the measuring unit 8, a microwave heating unit 10 having a conveyer 9 inside is placed, and the extruded molding P is heated, and thus cured, while moving on the conveyor 9. Furthermore, a hot air furnace 12 having a conveyor 11 is arranged thereon, and the extruded molding P is cured while moving thereon, thereby obtaining a cured molding Q.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は押出成形法により押出した後、加熱加硫するこ
とからなるウェザーストリップ等の自動車ノシール部品
等として利用される発泡ゴム成形品の製造方法に関する
ものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is directed to the manufacture of foamed rubber molded products used as automobile seal parts such as weather strips, which are extruded by an extrusion method and then heated and vulcanized. It is about the method.

〔従来の技術〕[Conventional technology]

従来、発泡ゴムとしてのスポンジゴムの長尺状の成形品
は、押出機により所定の形状で押出し、それをベルト搬
送しながらマイクロ波(UHF)や熱風により、加熱、
保温することによって加硫成形されている。この場合、
加硫成形品の寸法の調整は、同加硫成形品の寸法を測定
し、その寸法が所定の寸法から外れるとき、押出機のス
クリューの回転数をそれに対応させて調整することによ
って行われている。
Conventionally, elongated molded products of sponge rubber as foamed rubber have been extruded into a predetermined shape using an extruder, and then heated and heated using microwaves (UHF) or hot air while being conveyed by a belt.
It is vulcanized and molded by keeping it warm. in this case,
The dimensions of the vulcanized product are adjusted by measuring the dimensions of the vulcanized product, and when the dimensions deviate from the predetermined dimensions, the extruder screw rotation speed is adjusted accordingly. There is.

[発明が解決しようとする課題] ところが、押出機に供給されるゴム材料(練生地)は、
バッチで生産して押出機へ供給しているため、バッチが
変わるごとにゴム材料の組成がわずかに変化し、押出機
から押出される押出成形品の寸法、ひいては加硫成形品
の寸法が変動し、しかも押出成形品を加熱加硫する工程
が長いため、加硫成形品の寸法の変動に基づいて押出機
のスクリューの回転数を調整する方法では、ゴム材料の
バッチによる変動に対応して加硫成形品の寸法を精度良
く設定することができず、制御ロスも発生するという問
題点があった。
[Problem to be solved by the invention] However, the rubber material (kneaded dough) supplied to the extruder is
Because it is produced in batches and supplied to the extruder, the composition of the rubber material changes slightly each time the batch changes, resulting in variations in the dimensions of the extruded product extruded from the extruder and, by extension, the dimensions of the vulcanized product. However, since the process of heating and vulcanizing the extruded product is long, the method of adjusting the rotation speed of the extruder screw based on the variation in the dimensions of the vulcanized product cannot accommodate the variation due to batches of rubber materials. There was a problem in that the dimensions of the vulcanized product could not be set with high accuracy and control loss occurred.

本発明の目的は、ゴム材料がバッチによって変化しても
加硫成形品の寸法を精度良く設定することができるとと
もに、制御ロスの少ない発泡ゴム成形品の製造方法を提
供することにある。
An object of the present invention is to provide a method for manufacturing a foamed rubber molded product that allows the dimensions of a vulcanized molded product to be set with high precision even if the rubber material changes from batch to batch, and that reduces control loss.

[課題を解決するための手段] 上記目的を達成するために、本発明ではゴム材料を押出
機からスクリューの回転により所定の形状で押出成形し
た後、加熱して加硫成形する発泡ゴム成形品の製造方法
において、前記押出機から所定の形状で押出した押出成
形品の寸法を測定し、その寸法の増加又は減少に基づい
て前記押出機のスクリューの回転数を同様に対応させて
増加又は減少させるという手段を採用している。
[Means for Solving the Problem] In order to achieve the above object, the present invention provides a foamed rubber molded product in which a rubber material is extruded from an extruder into a predetermined shape by rotating a screw, and then heated and vulcanized. In the manufacturing method, the dimensions of the extruded product extruded in a predetermined shape from the extruder are measured, and based on the increase or decrease in the dimensions, the rotation speed of the screw of the extruder is similarly increased or decreased. We have adopted the method of letting

[作用] 上記手段を採用したことにより、押出機に供給されるゴ
ム材料の粘度が低いと押出機から押出された押出成形品
の寸法が小さくなり、逆にゴム材料の粘度が高いと押出
成形品の寸法が大きくなることから、ゴム材料の粘度と
押出成形品の寸法との間には正の相関関係がある。また
、ゴム材料の粘度が低いと発泡しやすく加硫成形品の寸
法が大きくなり、逆にゴム材料の粘度が高いと発泡しに
くく加硫成形品の寸法が小さくなることから、ゴム材料
の粘度と加硫成形品との間には負の相関関係がある。
[Function] By adopting the above means, when the viscosity of the rubber material supplied to the extruder is low, the dimensions of the extruded product extruded from the extruder become small, and conversely, when the viscosity of the rubber material is high, the extrusion molding becomes smaller. As the dimensions of the product increase, there is a positive correlation between the viscosity of the rubber material and the dimensions of the extruded product. In addition, if the viscosity of the rubber material is low, it will easily foam and the dimensions of the vulcanized molded product will increase, whereas if the viscosity of the rubber material is high, it will be difficult to foam and the dimensions of the vulcanized molded product will become small. There is a negative correlation between and vulcanized molded products.

一方、スクリューの回転数を上げると加硫成形品の寸法
も太き《なり、逆にスクリューの回転数を下げると、加
硫成形品の寸法も小さくなることからスクリューの回転
数と加硫成形品の寸法との間には正の相関関係がある。
On the other hand, when the screw rotation speed is increased, the dimensions of the vulcanized molded product become thicker, and conversely, when the screw rotation speed is decreased, the dimensions of the vulcanized molded product become smaller. There is a positive correlation with the dimensions of the product.

このように、押出成形品の寸法、ゴム材料の粘度スクリ
ューの回転数及び加硫成形品の寸法の間には、一定の相
関関係があるので、押出成形品の寸法の平均値を測定し
、その変化量に基づいて、スクリューの回転数を変化さ
せることにより、ゴム材料がバッチによって変動しても
すぐにそれに対応させて加硫成形品の寸法を精度良く設
定でき、しかも制御ロスを少なくすることができる。
In this way, there is a certain correlation between the dimensions of the extruded product, the viscosity of the rubber material, the rotation speed of the screw, and the dimensions of the vulcanized product, so the average value of the dimensions of the extruded product is measured, By changing the rotational speed of the screw based on the amount of change, even if the rubber material changes from batch to batch, the dimensions of the vulcanized product can be set with high precision by immediately responding to it, while reducing control loss. be able to.

〔実施例〕〔Example〕

以下に本発明を具体化したー実施例を第1図及び第2図
に基づいて説明する。
Embodiments embodying the present invention will be described below with reference to FIGS. 1 and 2.

第1図に示すように、押出機1の後方(第1図左方)に
は、ゴム材料としてのエチレンープロピレンージエン共
重合ゴム(EPDM)製のテーブ基材2が収納容器3内
に収納され、その上部から押出機1上部のホンパー4へ
供給されるようになっている。押出機1内には、内部に
スクリュー5を有するシリンダ6が配設され、ホッパ−
4からのゴム材料を押出すようになっている。同押出機
1の先端部には、金型7が取付けられ、スクリュー5で
押出された押出成形品Pを第2図に示すような形状に賦
形するようになっている。
As shown in FIG. 1, at the rear of the extruder 1 (left side in FIG. 1), a tape base material 2 made of ethylene-propylene-diene copolymer rubber (EPDM) as a rubber material is placed in a storage container 3. It is stored and supplied from the upper part to the omper 4 above the extruder 1. Inside the extruder 1, a cylinder 6 having a screw 5 inside is disposed, and a hopper
The rubber material from 4 is extruded. A mold 7 is attached to the tip of the extruder 1, and is configured to shape the extruded product P extruded by the screw 5 into the shape shown in FIG. 2.

同押出機1の前方(第1図右方)には、光学式寸法測定
器8が配置され、押出成形品Pに光を照射してその寸法
(幅)を連続的に測定するようになっている。同光学式
寸法測定器8の前方には、内部にコンベア9を有するマ
イクロ波加熱装置10が配設され、押出成形品Pは同コ
ンベア9上を移動しながら加熱され、加硫されるように
なっている。同マイクロ波加熱装置1oの前方には、同
じくコンベア1lを有する熱風炉12が配設され、押出
成形品Pがコンベアll上を移動しながら一定温度に加
熱保持され、加硫が継続されるようになっている。
An optical dimension measuring device 8 is placed in front of the extruder 1 (on the right side in Figure 1) and continuously measures the dimensions (width) of the extruded product P by irradiating it with light. ing. A microwave heating device 10 having a conveyor 9 inside is disposed in front of the optical dimension measuring device 8, and the extruded product P is heated and vulcanized while moving on the conveyor 9. It has become. In front of the microwave heating device 1o, a hot blast furnace 12 having a conveyor 1l is disposed so that the extruded product P is heated and maintained at a constant temperature while moving on the conveyor 1l, and vulcanization is continued. It has become.

上記熱風炉12内のコンベア11がら搬送されて出て来
る加硫成形品Qは、第2図に示すような形状を有し、自
動車の窓枠ゴムとしてのウェザーストリップとして使用
される。
The vulcanized molded product Q conveyed through the conveyor 11 in the hot-blast stove 12 has a shape as shown in FIG. 2, and is used as a weather strip for window frame rubber of automobiles.

さて、原料であるゴムのテープ状基材2は、収納容器3
から押出機1のホッパー4内へ供給され、さらに押出機
lのシリンダ6内のスクリュー5により前方へ押出され
る。そして、金型7を通ることにより略第2図に示すよ
うな形状に成形されて押出される。同押出成形品Pはマ
イクロ波加熱装置10内のコンベア9上を加熱されなが
ら搬送されることにより加硫され、続いて熱風炉12内
のコンベアll上を加熱されながら搬送されることによ
り加硫が継続され、加硫成形品Qである製品となって取
出される。
Now, the rubber tape-like base material 2, which is the raw material, is stored in the storage container 3.
It is fed into the hopper 4 of the extruder 1, and further extruded forward by the screw 5 in the cylinder 6 of the extruder 1. Then, by passing through a mold 7, it is formed into a shape approximately as shown in FIG. 2 and extruded. The extruded product P is vulcanized by being conveyed while being heated on the conveyor 9 in the microwave heating device 10, and then vulcanized by being conveyed while being heated on the conveyor 11 in the hot air stove 12. The process continues, and a product, which is a vulcanized molded product Q, is taken out.

前記押出成形品Pの寸法の平均値Xと押出機に供給する
ゴム材料のムーニー粘度Mとの間には、ゴム材料のムー
ニー粘度Mが小さくなると軟らかくなって押出成形品P
の寸法が小さくなり、逆にゴム材料のムーニー粘度Mが
大きくなると硬くなって押出成形品Pの寸法が大きくな
ることから、正の相関関係があり、次の式が成立する。
There is a difference between the average dimension value X of the extrusion molded product P and the Mooney viscosity M of the rubber material supplied to the extruder, and as the Mooney viscosity M of the rubber material becomes smaller, the extrusion molded product P becomes softer.
If the Mooney viscosity M of the rubber material becomes smaller, and conversely the Mooney viscosity M of the rubber material increases, it will become harder and the dimensions of the extruded product P will increase, so there is a positive correlation and the following equation holds true.

X=0.3 2 8 6M+9.4 5・・・・・・■
但し、Mは45〜49である。
X=0.3 2 8 6M+9.4 5・・・・・・■
However, M is 45-49.

また、押出機1内のスクリュー5の回転数の変化量ΔR
と加硫成形品Qの寸法の平均値の変化遣ΔYとの間には
、スクリエー5の回転数を下げると加硫成形品Qの寸法
も小さくなり、逆にスクリュー5の回転数を上げると加
硫成形品Qの寸法も大きくなることから、正の相関関係
があり、次の式が成立する。
In addition, the amount of change ΔR in the rotation speed of the screw 5 in the extruder 1
The difference between ΔY and the change in the average dimension of the vulcanized product Q is that when the rotation speed of the screw 5 is decreased, the dimensions of the vulcanized product Q are also reduced, and conversely, when the rotation speed of the screw 5 is increased, the size of the vulcanized product Q is decreased. Since the dimensions of the vulcanized product Q also increase, there is a positive correlation, and the following equation holds true.

ΔY = 0. 2 xΔR・・・・・・■さらに、加
硫成形品Qの寸法の平均値Yとゴム材料のムーニー粘度
Mとの間には、ゴム材料のムーニー粘度Mが小さいと軟
らかくなって押出成形品Pの寸法は小さくなるが、発泡
しやすくなって加硫成形晶Qの寸法は大きくなり、逆に
ゴム材料のムーニー粘度Mが大きくなると硬くなって押
出成形品Pの寸法は大きくなるが、発泡しにくくなって
加硫成形品Qの寸法は小さくなることから、負の相関関
係があり、次の式が成立する。
ΔY = 0. 2 Although the size of P becomes smaller, it becomes easier to foam and the size of the vulcanized crystal Q becomes larger.On the other hand, when the Mooney viscosity M of the rubber material increases, it becomes harder and the size of the extruded product P becomes larger, but foaming becomes easier. Since the dimensions of the vulcanized product Q become smaller as a result, there is a negative correlation, and the following equation holds true.

Y=−0.257M+37.8・・・・・・■ここで、
具体的に加硫成形品Qの寸法を26.01に設定する場
合、押出成形品Pの寸法の平均値Xが24.53+am
から25.55mmに変化した場合、上記■式よりムー
ニー粘度Mは45.9から49,0に変化していると考
えられる。このムーニー粘度Mの変化に対し、■弐から
加硫成形品Qの寸法の平均値Yが26.OOmmから2
5.21mmに下がると予測され、その変化量ΔYは0
.79mmとなる。従って、■式からΔRは3. 9 
5 r p mとなり、これだけスクリュー5の回転数
を上げればよいこととなる。
Y=-0.257M+37.8...■Here,
Specifically, when the dimensions of the vulcanized product Q are set to 26.01, the average value X of the dimensions of the extruded product P is 24.53+am
When the diameter changes from 25.55 mm to 25.55 mm, it is considered that the Mooney viscosity M changes from 45.9 to 49.0 from the above equation (2). With respect to this change in Mooney viscosity M, the average value Y of the dimensions of the vulcanized molded product Q is 26. OOmm to 2
It is predicted that it will decrease to 5.21mm, and the amount of change ΔY is 0.
.. It will be 79mm. Therefore, from equation (2), ΔR is 3. 9
5 rpm, and it is sufficient to increase the rotational speed of the screw 5 by this amount.

このように、押出成形品Pの寸法平均値X、スクリュー
5の回転数の変化量ΔR及び加硫成形品Qの寸法の平均
値Yの間には、一定の相関関係があるので、押出成形品
Pの寸法の平均値Xを測定し、その変化量に基づいて、
スクリエ−5の回転数を制御しているため、ゴム材料の
組成(物性)がバッチによって変化してもその変化に速
やかに対応して制御できるので、加硫成形品Qの寸法を
精度良く設定できる。
In this way, there is a certain correlation between the dimensional average value X of the extruded product P, the amount of change ΔR in the rotation speed of the screw 5, and the average dimension value Y of the vulcanized product Q. Measure the average value X of the dimensions of product P, and based on the amount of change,
Since the rotational speed of Scrier 5 is controlled, even if the composition (physical properties) of the rubber material changes from batch to batch, it can quickly respond to the change and set the dimensions of the vulcanized product Q with high precision. can.

また、従来のように、マイクロ波加熱装置10と熱風炉
l2の長い工程を経た加硫成形品Qの寸法の変化量に基
づいてスクリエ−5の回転数を制御する方法を保用して
いないので、加硫に要するマイクロ波加熱装置10と熱
風炉l2の長い工程の間の制御ロスを少なくすることが
できる。
Furthermore, unlike the conventional method, there is no method of controlling the rotational speed of the scratcher 5 based on the amount of change in the dimensions of the vulcanized product Q that has gone through the long process of the microwave heating device 10 and the hot air stove 12. Therefore, control loss during the long process of using the microwave heating device 10 and the hot air stove 12 required for vulcanization can be reduced.

上記のように、本実施例の発泡ゴム成形品の製造方法に
よれば、ゴム材料がバッチによって変化しても加硫成形
品Qの寸法を精度良く設定することができ、かつ制御ロ
スの発生が少久い。
As described above, according to the method for manufacturing a foamed rubber molded product of this embodiment, even if the rubber material changes from batch to batch, the dimensions of the vulcanized molded product Q can be set with high accuracy, and control loss can be avoided. It's been a while.

本発明は上記実施例に限定されるものではなく、発明の
趣旨を逸脱しない範囲で任意に変更することができ、例
えば次のように構成することもできる。
The present invention is not limited to the above-mentioned embodiments, and can be modified as desired without departing from the spirit of the invention. For example, it can be configured as follows.

即ち、発泡ゴム材料としては、発泡ゴム成形品にできる
ものであればよく、EP[)M以外にエチレンーブロビ
レン共重合ゴム(EPM)等を使用することもできる。
That is, the foamed rubber material may be any material that can be made into a foamed rubber molded article, and in addition to EP[)M, ethylene-propylene copolymer rubber (EPM) or the like may also be used.

[発明の効果] 本発明の発泡ゴムの製造方法によれば、ゴム材料がバッ
チによって変化しても加硫成形品の寸法を精度良く設定
することができるとともに、制御ロスの発生が少ないと
いう効果を奏する。
[Effects of the Invention] According to the method for producing foamed rubber of the present invention, the dimensions of the vulcanized product can be set with high accuracy even if the rubber material changes from batch to batch, and there is an effect that control loss is less likely to occur. play.

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

第1図及び第2図は本発明の実施例を示す図であって、
第1図は発泡ゴム成形品の製造装直を示す概略正面図、
第2図は加硫成形品としての発泡ゴム成形品の斜視図で
ある。 1・・・押出機、2・・・ゴム材料としてのテープ基材
、5・・・スクリュー、P・・・押出成形品、X・・・
押出成形品の寸法の平均値
FIG. 1 and FIG. 2 are diagrams showing embodiments of the present invention,
Figure 1 is a schematic front view showing the manufacturing setup for foam rubber molded products;
FIG. 2 is a perspective view of a foamed rubber molded product as a vulcanized molded product. DESCRIPTION OF SYMBOLS 1... Extruder, 2... Tape base material as a rubber material, 5... Screw, P... Extrusion molded product, X...
Average dimensions of extruded products

Claims (1)

【特許請求の範囲】[Claims] 1、ゴム材料(2)を押出機(1)からスクリュー(5
)の回転により所定の形状で押出成形した後、加熱して
加硫成形する発泡ゴム成形品の製造方法において、前記
押出機(1)から所定の形状で押出した押出成形品(P
)の寸法(X)を測定し、その寸法(X)の増加又は減
少に基づいて前記押出機(1)のスクリュー(5)の回
転数を同様に対応させて増加又は減少させることを特徴
とする発泡ゴム成形品の製造方法。
1. Rubber material (2) is transferred from the extruder (1) to the screw (5
), the extrusion molded product (P
), and based on the increase or decrease in the dimension (X), the rotation speed of the screw (5) of the extruder (1) is similarly increased or decreased. A method for manufacturing foam rubber molded products.
JP1111270A 1989-04-28 1989-04-28 Manufacture of foam rubber molding Pending JPH02292015A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1111270A JPH02292015A (en) 1989-04-28 1989-04-28 Manufacture of foam rubber molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1111270A JPH02292015A (en) 1989-04-28 1989-04-28 Manufacture of foam rubber molding

Publications (1)

Publication Number Publication Date
JPH02292015A true JPH02292015A (en) 1990-12-03

Family

ID=14556956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1111270A Pending JPH02292015A (en) 1989-04-28 1989-04-28 Manufacture of foam rubber molding

Country Status (1)

Country Link
JP (1) JPH02292015A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04301427A (en) * 1991-03-29 1992-10-26 Kinugawa Rubber Ind Co Ltd Controller for continuous extrusion vulcanizing line
JPH05305648A (en) * 1992-04-30 1993-11-19 Kinugawa Rubber Ind Co Ltd Automatic shape controlling device of rubber extruded article

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04301427A (en) * 1991-03-29 1992-10-26 Kinugawa Rubber Ind Co Ltd Controller for continuous extrusion vulcanizing line
US5328348A (en) * 1991-03-29 1994-07-12 Kinugawa Rubber Ind. Co., Ltd. Control system for continuous vulcanization line for manufacturing sponge rubber product
US5385463A (en) * 1991-03-29 1995-01-31 Kinugawa Rubber Ind. Co., Ltd. Control system for continuous vulcanization line for manufacturing sponge rubber product
JPH05305648A (en) * 1992-04-30 1993-11-19 Kinugawa Rubber Ind Co Ltd Automatic shape controlling device of rubber extruded article

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