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JPS6331365B2 - - Google Patents
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JPS6331365B2 - - Google Patents

Info

Publication number
JPS6331365B2
JPS6331365B2 JP55136315A JP13631580A JPS6331365B2 JP S6331365 B2 JPS6331365 B2 JP S6331365B2 JP 55136315 A JP55136315 A JP 55136315A JP 13631580 A JP13631580 A JP 13631580A JP S6331365 B2 JPS6331365 B2 JP S6331365B2
Authority
JP
Japan
Prior art keywords
mixing
rubber
time
plasticity
ram
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.)
Expired
Application number
JP55136315A
Other languages
Japanese (ja)
Other versions
JPS5759740A (en
Inventor
Haruyuki Takagi
Yoshioku Takahashi
Kazuaki Kamata
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.)
Yokohama Rubber Co Ltd
Original Assignee
Yokohama Rubber 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 Yokohama Rubber Co Ltd filed Critical Yokohama Rubber Co Ltd
Priority to JP55136315A priority Critical patent/JPS5759740A/en
Publication of JPS5759740A publication Critical patent/JPS5759740A/en
Publication of JPS6331365B2 publication Critical patent/JPS6331365B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/18Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/183Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7495Systems, i.e. flow charts or diagrams; Plants for mixing rubber

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Accessories For Mixers (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Description

【発明の詳細な説明】 本発明は混練中におけるラムが特定位置になつ
た時期より混合終了までの混合時間を一定にして
ゴム混合を終了させるゴム混合法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a rubber mixing method in which rubber mixing is completed by keeping the mixing time constant from the time when a ram reaches a specific position during kneading until the end of mixing.

従来、混合中の混合機内で発生する剪断力の程
度が混合バツチ毎に変動することによる混合物の
可塑度のバラツキを無くするために、混合開始よ
り混合終了までの消費電気エネルギーを一定とす
る混合法が適用されて来たが、同種のゴム混合
で、混合に要した消費電力量を一定とした場合、
投入する原料ゴムの可塑度バラツキが得られる混
合物の可塑度バラツキをもたらすことが良く知ら
れている。即ち、混合に要した消費電力量を一定
とした場合原料ゴム可塑度の高いものは、原料ゴ
ム投入直後、原料ゴムを機械的に粉砕するための
電気エネルギーが高いレベルにあり、ゴム混合物
が所定の可塑度に低下しないうちに、消費電力量
が所定の値に達してしまい、混合が終了してしま
うためである。従来、この種のゴム混合法で混合
初期に原料ゴムの可塑度を検出し、それによつ
て、基準消費電力値を混合中に修正する方法が試
みられて来た、たとえば原料ゴム投入直後の電力
のピーク値を検出使用する方法があるが、原料ゴ
ム投入直後のピーク電力レベルは、原料ゴムの形
状や原料ゴム投入のタイミングによつて変化す
る。
Conventionally, in order to eliminate variations in the plasticity of the mixture due to variations in the degree of shear force generated in the mixer during mixing from batch to batch, mixing methods have been used in which the electrical energy consumed from the start of mixing to the end of mixing is constant. However, if the same type of rubber is mixed and the amount of power required for mixing is constant,
It is well known that variations in the plasticity of the raw material rubber introduced lead to variations in the plasticity of the resulting mixture. In other words, assuming that the amount of power consumed for mixing is constant, if the raw rubber has a high plasticity, the electric energy required to mechanically crush the raw rubber is at a high level immediately after the raw rubber is added, and the rubber mixture will not reach the specified level. This is because the amount of power consumption reaches a predetermined value and the mixing ends before the plasticity level decreases to . Conventionally, attempts have been made to use this type of rubber mixing method to detect the plasticity of the raw rubber at the initial stage of mixing and use it to correct the standard power consumption value during mixing. There is a method of detecting and using the peak value of raw rubber, but the peak power level immediately after raw rubber is introduced changes depending on the shape of raw rubber and the timing of raw rubber input.

周知の如く、一般のゴム混合機の2本のロータ
は練効率を高めるためにある一定の比率で回転し
ているために、両ロータの回転位相が一致した時
に原料ゴムを投入する場合とそうでない時とでは
原料ゴムのくい込みが異り、ピーク電力値に大き
な変化があらわれる。通常のゴム混合機(バンバ
リーミキサー)では、この回転位相が一致する時
間間隔は約10秒であり、このピーク電力値を用い
て原料ゴムの可塑度の程度を混合中に検出する方
法は現実的ではない。又混合中に混合機よりもた
らされる電気信号を応用して原料ゴム可塑度の程
度を検出するためには、比較的多くのテスト混合
によつて両者の実験式を求める必要があり、原料
ゴム種、量の異る他のゴム混合では、その実験式
がそのまゝ使用出来ないのが一般的である。更
に、基準消費電力値を混合中に修正するに当つて
その修正量は、配合の異るゴム種毎に決定しなけ
ればならないのが一般的である。
As is well known, the two rotors of a general rubber mixing machine rotate at a certain ratio to increase the kneading efficiency, so raw rubber may be introduced when the rotational phase of both rotors matches. The penetration of the raw material rubber differs from when it is not used, and a large change appears in the peak power value. In a normal rubber mixer (Banbury mixer), the time interval during which the rotational phases match is approximately 10 seconds, and it is practical to use this peak power value to detect the degree of plasticity of raw rubber during mixing. isn't it. In addition, in order to detect the degree of plasticity of raw rubber by applying the electric signal provided by the mixer during mixing, it is necessary to obtain the empirical formula for both by performing a relatively large number of test mixtures. When mixing other rubbers with different amounts, the empirical formula cannot generally be used as is. Furthermore, when modifying the reference power consumption value during mixing, the amount of modification must generally be determined for each type of rubber with a different composition.

本発明は原料ゴムの可塑度の差異による混合物
の可塑度のバラツキを減少させたゴム混合法を提
供することを目的とする。
An object of the present invention is to provide a rubber mixing method that reduces variations in the plasticity of a mixture due to differences in the plasticity of raw rubbers.

以下本発明の実施例を図面に基いて説明する。 Embodiments of the present invention will be described below based on the drawings.

第1図は本発明方法に使用されるゴム混合機
(バンバリーミキサー)を示しており、1はチヤ
ンバー、2は冷却ジヤケツト、3は該チヤンバー
1内に設けられたローターである。該チヤンバー
1の下部に混合物を放出するドアー4が設けられ
てある。6は原料ゴム投入口、7はカーボンブラ
ツク投入口、8は前記チヤンバー1内にオイルを
注入するノズルである。9は前記チヤンバー1内
にある材料に圧力を加えるためのラムで、上部に
配置されているシリンダー10内のピストン(図
示せず)とピストンロツド11を介して連結され
ている。12は前記シリンダー10の外側に延び
るテルテルロツトで、前記ラム9(ピストンロツ
ド11でも良い)に連結されている。テルテルロ
ツト12には永久磁石13が取付けられている。
この永久磁石13と対向する位置にラムモーシヨ
ンセンサー14が設けられている。ラムモーシヨ
ンセンサー14は、永久磁石13の上下動に対し
て、その高さに応じた電気信号が取出せる構造の
もので、例えば永久磁石13の移動線上に対向し
て並設された多数のリードスイツチからなつてい
る。
FIG. 1 shows a rubber mixer (Banbury mixer) used in the method of the present invention, in which 1 is a chamber, 2 is a cooling jacket, and 3 is a rotor provided within the chamber 1. A door 4 is provided at the bottom of the chamber 1 for releasing the mixture. 6 is a raw rubber inlet, 7 is a carbon black inlet, and 8 is a nozzle for injecting oil into the chamber 1. Reference numeral 9 denotes a ram for applying pressure to the material in the chamber 1, and is connected via a piston rod 11 to a piston (not shown) in a cylinder 10 located above. Reference numeral 12 denotes a stopper rod extending outside the cylinder 10 and connected to the ram 9 (which may also be the piston rod 11). A permanent magnet 13 is attached to the rotor rod 12.
A ram motion sensor 14 is provided at a position facing this permanent magnet 13. The ram motion sensor 14 has a structure that can extract an electric signal according to the height of the vertical movement of the permanent magnet 13. It is connected to the reed switch.

第2図はゴム混合中に観測されるチヤートの一
例であつて混合機において消費されるAは電力の
時間的変化、Bはラム9の動き(ラムモーシヨ
ン)の時間的変化で、前記ラムモーシヨンセンサ
ー14の出力信号として取出される。
Figure 2 is an example of a chart observed during rubber mixing, where A represents the temporal change in electric power consumed in the mixer, and B represents the temporal change in the movement of the ram 9 (ram motion). It is taken out as an output signal of the sensor 14.

一般的なゴム混合動作は次のように行なわれ
る。ラム9を上死点まで上昇させた状態で、所定
の重量だけ、原料ゴム、カーボンブラツクを各々
原料ゴム投入口6及びカーボンブラツク投入口7
より投入し、投入時期T1、各々の投入口6,7
を閉じた後シリンダー10によつてラム9を下降
させ、所定の圧力で原料ゴムを加圧する。ロータ
3の回転によつて原料ゴムは砕かれチヤンバー1
内で原料ゴムがカーボンでまぶされた状態であ
り、この期間ではいわゆる機械的混合が進行す
る。原料ゴムが細かく砕かれることによつてゴム
混合物の見かけ上の体積が膨張し、所定の圧力で
加圧しているにもかゝわらずラム9は徐々に上方
に押し上げられていく。そして、ゴム混合物の体
積膨張に伴う反撥力とシリンダー10による圧力
とが均衡した状態に達する。この状態がラムモー
シヨンの最高値Pであり、この時期をT2で表し
ている。更に混合が進行するにつれて、機械的混
合が化学的混合に移行し、カーボンブラツクの分
散、混合物の可塑度低下が成され、それに伴つて
混合物全体の反撥力が低下するためラムは下降し
ていきラムモーシヨンBは山形をなす。その後
種々の条件から決まる時期T3で、オイル等の他
の添加剤が投入され、混合終了時期T4に至る。
A typical rubber mixing operation is performed as follows. With the ram 9 raised to the top dead center, a predetermined weight of raw rubber and carbon black are loaded into the raw rubber inlet 6 and the carbon black inlet 7, respectively.
Input time T 1 , each input port 6, 7
After closing, the ram 9 is lowered by the cylinder 10, and the raw rubber is pressurized at a predetermined pressure. The raw rubber is crushed by the rotation of the rotor 3 and the chamber 1
The raw rubber is coated with carbon within the chamber, and so-called mechanical mixing progresses during this period. As the raw rubber is crushed into pieces, the apparent volume of the rubber mixture expands, and the ram 9 is gradually pushed upward despite being pressurized with a predetermined pressure. Then, a state is reached where the repulsive force due to the volumetric expansion of the rubber mixture and the pressure exerted by the cylinder 10 are balanced. This state is the maximum value P of the ram motion, and this period is represented by T2 . As the mixing further progresses, mechanical mixing shifts to chemical mixing, dispersing carbon black and reducing the plasticity of the mixture.As the repulsive force of the entire mixture decreases, the ram descends. Ram motion B forms a chevron. Thereafter, at time T3 determined from various conditions, other additives such as oil are added, and the mixing ends at time T4 .

第3図はある種のゴム混合において、ラムモー
シヨン最大時期T2より混合終了時期T4までの混
合時間によつてゴム混合物の可塑度がどの様に変
化するかをプロツトしたものである。グラフ中の
四角印、三角印および丸印は、その混合に使用し
た原料ゴム可塑度の水準を示している。この図よ
り、得られたゴム混合物の可塑度は、ラムモーシ
ヨン最大時期T2より混合終了時期T4までの混合
時間によつて決定することができ、原料ゴム可塑
度には依存しないことが明らかである。したがつ
て、本発明方法においては、原料ゴムの可塑度に
よつて大きくバラツキのある機械的混合に要した
電気エネルギー(時期T1より時期T2までの消費
電力量)を無視して、化学的混合に要する時間
(時期T2より、時期T4までの時間)を同種のゴム
混合において、常に一定とするように混合終了時
期T4と制御するようにしたものである。
FIG. 3 is a plot of how the plasticity of a rubber mixture changes depending on the mixing time from the maximum ram motion time T2 to the end of mixing time T4 in a certain type of rubber mixing. The square, triangle, and circle marks in the graph indicate the level of plasticity of the raw material rubber used for mixing. From this figure, it is clear that the plasticity of the obtained rubber mixture can be determined by the mixing time from the maximum ram motion time T 2 to the mixing end time T 4 , and does not depend on the plasticity of the raw rubber. be. Therefore, in the method of the present invention, the chemical The mixing end time T 4 is controlled so that the time required for the target mixing (time from time T 2 to time T 4 ) is always constant when mixing the same type of rubber.

第4図は本発明の実施において使用される電気
回路の一例であつて、ラムモーシヨンセンサー1
4の出力はフイルター15に加えられ、該フイル
ター15によつて不要な周波数帯域の信号が除去
され、第2図のBのような電圧波形の信号として
出力される。該フイルター15の出力はピーク検
出部17に入力される。ピーク検出部17は原料
ゴム投入時期T1よりタイマー16で定められた
時間経過後のラムモーシヨンBの最大値Pを検出
した時期T2で信号を発生する。タイマー16を
使用する理由は、時期T2以前のラムモーシヨン
のピーク値を検出しないようにするためである。
ピーク検出部17の信号は、混合時間カウンタ1
8を作動させる。該時間カウンタ18のカウント
値がゴム混合物の種類に応じてあらかじめ設定部
19に設定されてある値に達した時点で該時間カ
ウンタ18から混合終了指令が出力される。
FIG. 4 is an example of an electric circuit used in carrying out the present invention, and shows the ram motion sensor 1.
The output of No. 4 is applied to a filter 15, which removes signals in unnecessary frequency bands and outputs it as a signal with a voltage waveform as shown in FIG. 2B. The output of the filter 15 is input to a peak detection section 17. The peak detection unit 17 generates a signal at a time T2 when the maximum value P of the ram motion B is detected after a time period determined by the timer 16 has elapsed from the raw rubber input time T1 . The reason for using the timer 16 is to avoid detecting the peak value of the ram motion before time T2 .
The signal from the peak detector 17 is sent to the mixing time counter 1.
Activate 8. When the count value of the time counter 18 reaches a certain value preset in the setting section 19 according to the type of rubber mixture, the time counter 18 outputs a mixing end command.

本実施例では、ラムモーシヨンをアナログ信号
として取出し、この信号の最大点Pを混合終了ま
での時間カウントを決める基準点としているが、
これに限定されず、例えばラム9が最大点に達し
た位置を検知し得る個所にリードスイツチ、リミ
ツトスイツチ等の検知器を設けておけば、この検
知器の信号がすなわち時期T2の信号となるので、
この信号を前記時間カウンタ18に入力させれば
全く同一の効果が得られる。又原理的に、ゴム混
合機内で機械的にゴムの切断が生ずる時にいつで
もラムモーシヨンBの形は上昇して下降するか
ら、混合途中で添加剤を投入しないゴム混合、原
料ゴムのみ、又はそれに類するゴム混合物のみを
練る(素練)場合であつても本発明での混合法が
適用できる。
In this embodiment, the ram motion is extracted as an analog signal, and the maximum point P of this signal is used as the reference point for determining the time count until the end of mixing.
The invention is not limited to this, but for example, if a detector such as a reed switch or a limit switch is provided at a location where the position where the ram 9 reaches its maximum point can be detected, the signal from this detector becomes the signal at time T2 . So,
If this signal is input to the time counter 18, exactly the same effect can be obtained. Also, in principle, the shape of ram motion B rises and falls whenever rubber is mechanically cut in the rubber mixing machine, so it is possible to mix rubber without adding additives during mixing, only raw rubber, or similar rubbers. Even when only the mixture is kneaded (massured), the mixing method of the present invention can be applied.

以上説明したように、ラムモーシヨン最大時期
よりの混合時間を一定とするように混合終了時期
を決定することによつて、次のような効果が得ら
れる。
As explained above, by determining the mixing end time so that the mixing time from the maximum ram motion time is constant, the following effects can be obtained.

(1) 原料ゴムの可塑度のバラツキがあつても混合
物の可塑度のバラツキがほとんどなく、均一な
ゴム混合物が得られる。
(1) Even if there is variation in the plasticity of the raw rubber, there is almost no variation in the plasticity of the mixture, and a uniform rubber mixture can be obtained.

(2) 所定の可塑度のゴム混合物を得るためのゴム
混合機の混合時間の決定を、原料ゴムの可塑度
の程度と無関係に行えるために、原料ゴムの可
塑度と混合中の電力チヤートとの関係式が決つ
てなくても良い。
(2) In order to determine the mixing time of the rubber mixer to obtain a rubber mixture with a predetermined plasticity, regardless of the degree of plasticity of the raw rubber, the plasticity of the raw rubber and the electric power chart during mixing can be determined. It is not necessary that the relational expression for

(3) ゴム混合物の可塑度のバラツキを無くすため
に、上記関係式によつて、全体の混合時間基準
値を修正制御する時、修正量決定のためのテス
ト混合、データ解析等が不要であり、修正演算
する等の制御回路が不要である。
(3) When correcting and controlling the overall mixing time reference value using the above relational expression in order to eliminate variations in the plasticity of the rubber mixture, there is no need for test mixing, data analysis, etc. to determine the amount of correction. , a control circuit for performing correction calculations, etc. is not required.

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

第1図は本発明方法に使用されるゴム混合機の
断面図、第2図はゴム混合中の電力チヤートとラ
ムモーシヨンチヤート、第3図は混合によつて得
られたゴム混合物の可塑度とラムモーシヨン最大
点より混合終了までの、混合時間とのプロツト
図、第4図は本発明方法の実施に使用される電気
回路図である。 14:ラムモーシヨンセンサ、17:ピーク検
出部、18:時間カウンタ、19:設定部。
Figure 1 is a sectional view of the rubber mixer used in the method of the present invention, Figure 2 is a power chart and ram motion chart during rubber mixing, and Figure 3 is the plasticity of the rubber mixture obtained by mixing. FIG. 4 is an electrical circuit diagram used to carry out the method of the present invention. 14: Ram motion sensor, 17: Peak detection section, 18: Time counter, 19: Setting section.

Claims (1)

【特許請求の範囲】[Claims] 1 ゴム混合機を用いて原料ゴムを練る方法にお
いて、混練中におけるラムモーシヨンの最高値を
検出し、この最高値になつた時期より混合終了ま
での混合時間を一定とすることを特徴とするゴム
混合法。
1. A method of kneading raw rubber using a rubber mixer, which is characterized by detecting the highest value of ram motion during kneading and keeping the mixing time constant from the time when this highest value is reached until the end of mixing. Law.
JP55136315A 1980-09-30 1980-09-30 Mixing method for rubber Granted JPS5759740A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55136315A JPS5759740A (en) 1980-09-30 1980-09-30 Mixing method for rubber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55136315A JPS5759740A (en) 1980-09-30 1980-09-30 Mixing method for rubber

Publications (2)

Publication Number Publication Date
JPS5759740A JPS5759740A (en) 1982-04-10
JPS6331365B2 true JPS6331365B2 (en) 1988-06-23

Family

ID=15172328

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55136315A Granted JPS5759740A (en) 1980-09-30 1980-09-30 Mixing method for rubber

Country Status (1)

Country Link
JP (1) JPS5759740A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4667967B2 (en) * 2005-06-09 2011-04-13 神鋼テクノ株式会社 Pressurized kneader

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JPS5759740A (en) 1982-04-10

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