JPS6226283B2 - - Google Patents
Info
- Publication number
- JPS6226283B2 JPS6226283B2 JP54145249A JP14524979A JPS6226283B2 JP S6226283 B2 JPS6226283 B2 JP S6226283B2 JP 54145249 A JP54145249 A JP 54145249A JP 14524979 A JP14524979 A JP 14524979A JP S6226283 B2 JPS6226283 B2 JP S6226283B2
- Authority
- JP
- Japan
- Prior art keywords
- ram
- output
- rubber
- level
- mixing
- 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
Links
- 229920001971 elastomer Polymers 0.000 claims description 38
- 239000005060 rubber Substances 0.000 claims description 38
- 238000002156 mixing Methods 0.000 claims description 14
- 230000007423 decrease Effects 0.000 claims description 11
- 238000010074 rubber mixing Methods 0.000 claims description 9
- 239000006229 carbon black Substances 0.000 claims description 8
- 238000001514 detection method Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 241000872198 Serjania polyphylla Species 0.000 claims 1
- 239000000203 mixture Substances 0.000 description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 229910052799 carbon Inorganic materials 0.000 description 8
- 239000006185 dispersion Substances 0.000 description 8
- 235000014676 Phragmites communis Nutrition 0.000 description 6
- 238000010008 shearing Methods 0.000 description 3
- 230000002123 temporal effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000010077 mastication Methods 0.000 description 1
- 230000018984 mastication Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
- B29B7/06—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
- B29B7/10—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
- B29B7/18—Mixing; 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
- B29B7/183—Mixing; 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
- B29B7/22—Component parts, details or accessories; Auxiliary operations
- B29B7/24—Component parts, details or accessories; Auxiliary operations for feeding
- B29B7/246—Component parts, details or accessories; Auxiliary operations for feeding in mixers having more than one rotor and a casing closely surrounding the rotors, e.g. with feeding plungers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
- B29B7/22—Component parts, details or accessories; Auxiliary operations
- B29B7/28—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control
- B29B7/283—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control measuring data of the driving system, e.g. torque, speed, power
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
- B29B7/22—Component parts, details or accessories; Auxiliary operations
- B29B7/28—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control
- B29B7/286—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control measuring properties of the mixture, e.g. temperature, density
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
- B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/82—Heating or cooling
- B29B7/823—Temperature control
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
本発明はカーボン分散度のすぐれたゴム混合物
を得るためのゴム混合方法及びその装置に関する
ものである。
カーボンブラツクをゴム混合物内に均一に分散
させるためには、できるだけ高い剪断力を混合機
内で発生させることが必要である。しかるに混合
機内のゴム混合物は、ローターよりうける変形に
よる粘度低下、及び補強、加工性向上のために添
加されるオイルによつて、ゴム混合物に加えられ
る剪断力には限界があり、又、その剪断力は、特
に粘度低下に伴つて、混合中に変化する。従来、
この種の混合法では規定の時間、混合に消費され
た電気エネルギー及び温度レベル、又はこれらの
組合せによつてオイル投入時間が決定されてい
た。これらの方法は原料ゴムの可塑度、温度、混
合機の温度等のバラツキにより混合機内でのゴム
の喰い込み、ゴムブロツクの粉砕エネルギーが混
合バツチ毎に変化し混合トルクに大きな変化をも
たらし、混合後のゴム混合物中のカーボン分散を
高いレベルで安定させることができなかつた。
又これらの混合条件のバラツキをなくするため
に、混合機の温度調節設備や、原料ゴムの素練、
保温設備が必要であり、装置が複雑化する欠点が
あつた。
本発明はゴム混合中にラムの動きを検出してこ
のラム位置の特定レベルでオイル投入又はラム圧
力を切換えるようにし、もつてゴム混合物中のカ
ーボンブラツクの分散度を高め、混合バツチ間の
バラツキをなくして均一なゴム混合物が得られる
ようにしたゴム混合方法及び装置を提供すること
を目的とする。
以下、本発明の実施例を図面に基いて説明す
る。
第1図は本発明に使用されるゴム混合機(バン
バリーミキサ)の一例を示しており、1はチヤン
バ、2はジヤケツト、3は該チヤンバ1内に設け
られたロータである。該チヤンバ1の下部には混
合物放出ドア4の一部を構成するうね5が設けら
れている。6は原料ゴムの投入口、7はカーボン
ブラツク投入口、8は前記チヤンバ1に臨ませた
オイル投入ノズルである。9は前記チヤンバ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10の外側に延びるテ
ルテルロツドで、前記ラム9(ピストンロツド1
1でもよい)に連結されている。該テルテルロツ
ド12には永久磁石13が取付けられている。該
永久磁石13と対向する位置にラムモーシヨンセ
ンサ14(以下センサと称す)が設けられてい
る。該センサ14の一例を第2図に示している。
第2図において、15は電源端子、16は整流
器、17は定電流発生回路、18は電圧分割回
路、19はリミツトスイツチ、20はリードリレ
ー、21は出力端子である。前記電圧分割回路1
8は前記永久磁石13の移動方向に沿つて配列さ
れたリードスイツチ22………と各リードスイツ
チ22……間に接続された抵抗器23とからな
る。電源端子15に交流電源を供給すると、定電
流発生回路17により整流され、直流の安定した
電流が電圧分割回路18に供給される。リミツト
スイツチ19は常時はオフの状態にある。この状
態で永久磁石13が上下に移動すると、該永久磁
石13に対向した位置のリードスイツチ22がオ
ンになり、抵抗器23の分割比に比例した出力が
出力端子21に生ずる。永久磁石13がリードス
イツチ22の領域から外れるとリミツトスイツチ
19が永久磁石13(テルテルロツド12に別に
キツカーを設けてもよい)によつてオンに切換え
られ、これによつてリードリレー20がオンにな
り出力端子21一定の電圧が出力される。上記し
たラムモーシヨンセンサ14は単なる一例であつ
て、周知のリニアセンサや角度センサを用いても
よい。
第3図は前記センサ13からの信号を処理して
オイル投入時期を制御するための電気回路であつ
て、24はフイルタ、25は電圧減少検出部、2
6はレベル設定部、27は比較部を示す。
次にゴム混合の動作を第4図を参照しながら説
明する。第4図におけるAはゴム混合中における
ラム9の動き(ラムモーシヨン)、Bはロータ3
のトルクの時間的変化を示したものである。ラム
9を上死点まで上昇させた状態で原料ゴム及びカ
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、各々の投入口
6,7を閉じた後シリンダ10によつてラム9を
下降させ、適当な圧力で原料ゴムを加圧する。ロ
ーラ3の回転によつて原料ゴムは砕かれカーボン
ブラツクと混合される。原料ゴムが砕かれること
によつてゴム混合物の見かけ上の体積が膨張し、
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併う反撥力とシリンダ
10による圧力とが均衡した状態に達する(第4
図P)。さらに混合が進むにつれて混合物の反撥
弾性が低下していくため、ラム9が徐々に下降し
下死点(第4図Q)に達する。このラム9の動き
はテルテルロツド12を介して永久磁石13の上
下の動きとなつて表われ、これによつて前述した
ようにセンサ14の出力端子21から電気信号が
出力される。
第3図においてセンサ13の出力はフイルタ2
4に加えられ、該フイルタ24によつて不要な周
波数帯域の信号が除去され第4図のCのような電
圧波形の信号として出力される。該フイルタ24
の出力は電圧減少検出部25と比較部27に加え
られる。電圧減少検出部25は電圧が最大レベル
P′に達して減少し始めると出力を出す回路であ
る。このような回路は周知であるが、一例を上げ
ると、OPアンプの端子にフイルタ24から出
力を加え、端子にフイルタ24からの出力を遅
延回路を介して加えることにより、端子の電圧
の方が側の電圧より高い場合、すなわち電圧減
少時にOPアンプから出力が出される。あるいは
OPアンプに代えて比較器を用い、同様に二つの
入力の端子の一方にフイルタ24の出力を、他方
にフイルタ24の出力を遅延回路を介して加え、
他方の電圧が一方の電圧より高い場合のみ比較器
から出力を出すような回路でもよい。
電圧減少検出部25の出力は比較部25に与え
られ、これにより比較部27は作動状態となり、
フイルタ24の出力とレベル設定部26の出力と
が比較される。該レベル設定部26にはオイル投
入時期を決定するラムの位置H(ラムレベル)が
電気的に設定されており、このレベル設定部26
の出力とフイルタ24からの出力とが一致する
(第4図T)と比較部27よりレベル判定、信号
が出力される。この信号に基いてオイル投入ノズ
ル8からオイルが投入される。その後一定時間経
過後又は一定の電気エネルギー消費後ドア4を開
いてゴム混合物を取出す。
オイル投入時期は混合するゴムの種類、重量等
により異なるため、ラムレベルHはゴムの種類、
重量に応じて最適の値が選ばれる。一例として
NR:SBR:IR=2:1:1.5の混合比を有する総
重量187Kgのゴムを混合した場合のラムレベルと
カーボン分散度(ノンプロ混合)の関係を試験し
た結果を下表に示す。
The present invention relates to a rubber mixing method and apparatus for obtaining a rubber mixture with excellent carbon dispersion. In order to uniformly distribute the carbon black within the rubber mixture, it is necessary to generate as high a shear force as possible in the mixer. However, there is a limit to the shearing force that can be applied to the rubber mixture in the mixer due to viscosity reduction due to deformation from the rotor and oil added to strengthen and improve workability. The force changes during mixing, especially as the viscosity decreases. Conventionally,
In this type of mixing method, the oil input time was determined by a specified time, the electrical energy consumed in mixing, the temperature level, or a combination thereof. In these methods, the rubber bite in the mixer and the crushing energy of the rubber blocks change for each mixing batch due to variations in the plasticity of the raw rubber, the temperature, the temperature of the mixer, etc., which causes a large change in the mixing torque. It was not possible to stabilize the carbon dispersion in the rubber mixture at a high level. In addition, in order to eliminate variations in these mixing conditions, temperature control equipment for the mixer, mastication of raw rubber,
This had the disadvantage of requiring heat insulation equipment and complicating the equipment. The present invention detects the movement of the ram during rubber mixing and switches the oil input or ram pressure at a specific level of this ram position, thereby increasing the degree of dispersion of carbon black in the rubber mixture and reducing the variation between mixed batches. It is an object of the present invention to provide a rubber mixing method and apparatus that eliminates this problem and allows a uniform rubber mixture to be obtained. Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an example of a rubber mixer (Banbury mixer) used in the present invention, in which 1 is a chamber, 2 is a jacket, and 3 is a rotor provided in the chamber 1. The lower part of the chamber 1 is provided with a ridge 5 forming part of a mixture discharge door 4. Reference numeral 6 designates a raw rubber inlet, 7 a carbon black inlet, and 8 an oil inlet nozzle facing 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 disposed above. Reference numeral 12 denotes a stopper rod extending outside the cylinder 10, which connects the ram 9 (piston rod 1) to the outside of the cylinder 10.
1). A permanent magnet 13 is attached to the telltale rod 12. A ram motion sensor 14 (hereinafter referred to as a sensor) is provided at a position facing the permanent magnet 13. An example of the sensor 14 is shown in FIG. In FIG. 2, 15 is a power supply terminal, 16 is a rectifier, 17 is a constant current generating circuit, 18 is a voltage dividing circuit, 19 is a limit switch, 20 is a reed relay, and 21 is an output terminal. The voltage dividing circuit 1
8 consists of reed switches 22 arranged along the moving direction of the permanent magnet 13 and resistors 23 connected between each reed switch 22 . When AC power is supplied to the power supply terminal 15, it is rectified by the constant current generating circuit 17, and a stable DC current is supplied to the voltage dividing circuit 18. The limit switch 19 is normally in an off state. When the permanent magnet 13 moves up and down in this state, the reed switch 22 at the position facing the permanent magnet 13 is turned on, and an output proportional to the division ratio of the resistor 23 is generated at the output terminal 21. When the permanent magnet 13 comes out of the area of the reed switch 22, the limit switch 19 is turned on by the permanent magnet 13 (a separate kicker may be provided on the telltale rod 12), thereby turning on the reed relay 20 and outputting. A constant voltage is output from the terminal 21. The above-mentioned ram motion sensor 14 is merely an example, and a well-known linear sensor or angle sensor may be used. FIG. 3 shows an electric circuit for processing the signal from the sensor 13 to control the oil supply timing, in which 24 is a filter, 25 is a voltage reduction detection section, 2
Reference numeral 6 indicates a level setting section, and 27 indicates a comparison section. Next, the rubber mixing operation will be explained with reference to FIG. In Fig. 4, A is the movement of the ram 9 during rubber mixing (ram motion), and B is the rotor 3.
This figure shows the temporal change in torque. With the ram 9 raised to the top dead center, raw rubber and carbon black are charged from the raw rubber input port 6 and carbon black input port 7, respectively, and after closing each of the input ports 6 and 7, the cylinder 10 The ram 9 is lowered and the raw rubber is pressurized with an appropriate pressure. As the roller 3 rotates, the raw rubber is crushed and mixed with carbon black. As the raw rubber is crushed, the apparent volume of the rubber mixture expands,
Ram 9 is gradually pushed upward. Then, a state is reached where the repulsive force accompanying the volumetric expansion of the rubber mixture and the pressure exerted by the cylinder 10 are balanced (fourth
Figure P). As the mixing further progresses, the rebound elasticity of the mixture decreases, so the ram 9 gradually descends and reaches the bottom dead center (Q in FIG. 4). This movement of the ram 9 is expressed as a vertical movement of the permanent magnet 13 via the telltale rod 12, thereby causing an electrical signal to be output from the output terminal 21 of the sensor 14 as described above. In Fig. 3, the output of sensor 13 is
4, unnecessary frequency band signals are removed by the filter 24, and the signal is output as a voltage waveform signal as shown in FIG. 4C. The filter 24
The output is applied to the voltage decrease detection section 25 and the comparison section 27. The voltage decrease detection unit 25 detects that the voltage is at the maximum level.
This circuit outputs an output when it reaches P' and begins to decrease. Such a circuit is well known, but to give an example, by adding the output from the filter 24 to the terminal of the OP amplifier and applying the output from the filter 24 to the terminal via a delay circuit, the voltage at the terminal can be lowered. When the voltage is higher than the voltage on the side, that is, when the voltage decreases, the OP amp outputs an output. or
Using a comparator instead of the OP amplifier, similarly adding the output of the filter 24 to one of the two input terminals and the output of the filter 24 to the other via a delay circuit,
A circuit may also be used in which the comparator outputs an output only when the other voltage is higher than the one voltage. The output of the voltage decrease detection section 25 is given to the comparison section 25, which causes the comparison section 27 to be in an operating state.
The output of the filter 24 and the output of the level setting section 26 are compared. The level setting unit 26 is electrically set with a ram position H (ram level) that determines the timing of oil injection.
When the output from the filter 24 matches the output from the filter 24 (T in FIG. 4), the comparison section 27 makes a level determination and outputs a signal. Based on this signal, oil is supplied from the oil supply nozzle 8. Thereafter, after a certain period of time has elapsed or after a certain amount of electrical energy has been consumed, the door 4 is opened and the rubber mixture is taken out. The timing of adding oil varies depending on the type of rubber to be mixed, weight, etc., so ram level H depends on the type of rubber, weight, etc.
The optimal value is selected depending on the weight. As an example
The table below shows the results of testing the relationship between ram level and carbon dispersion (non-pro mixture) when rubber with a total weight of 187 kg having a mixing ratio of NR:SBR:IR=2:1:1.5 was mixed.
【表】
上述の混合物ではラムレベルを1.5〜2.0cmの範
囲に設定すると高いカーボン分散度が得られる。
上述の実施例では比較部27の出力信号により
オイル投入を行なう例を示したが、オイル投入を
行なわず、ラム圧力の切換のみを行なうこともで
きる。すなわち、前述したようにゴム混合物の体
積膨張に併つてラム9が最上昇点Pまで達した
後、混合が進むにつれて混合物の粘度が低下して
反撥弾性が徐々に衰退していき、これに併つてラ
ム9が下降を始める。このラム下降時の特定レベ
ルでラム圧力を減圧し、又はラム上昇を短時間行
なうことにより、衰退していく反撥弾性の回復が
なされ、再びラムで加圧した際ゴム混合物の受け
る剪断力をラムの最上昇点Pのときと同程度に回
復できる。このラム圧力の減圧又はラム上昇の切
換え時期は、オイル投入を行なう場合のオイル投
入時期と一致する。したがつて前記比較部27の
出力信号を利用してラム圧力を減圧又はラム上昇
を行なうことにより同様にカーボン分散度を高め
ることができる。ゴム混合機内の温度や、原料ゴ
ムの可塑度、温度等は季節的に変化し、又ある原
料ゴムは混合バツチ毎に変化する。それは原料ゴ
ムを粉砕し、カーボンブラツクをゴム内に分散さ
せる混合プロセスに大きな変化をもたらす。ラム
モーシヨンの出力波形は、その形状と時間的ずれ
によつてこれらの混合条件の変化を表わすから、
同種のゴムの場合はその特定レベル、すなわちオ
イル投入又はラム切換時間を決定するレベルは常
に一定である。したがつて本発明によれば、
(1) ラムモーシヨンの特定のレベルでオイル投入
を実施することにより混合条件の変化にもかか
わらずカーボン分散を高い水準に安定させるこ
とができる。
(2) ラムモーシヨンの一定のレベルでは、ゴムと
カーボンの混合物がある一定の見かけ上の体積
を有するから、この時期にオイル投入した場
合、その後の電気エネルギーをゴム混合物に安
定して加えることができる。
(3) ラムモーシヨンの一定レベルでラム圧力を減
圧したり、ラムをもち上げる時、ゴム混合物の
粘度低下とともに、衰退していく反撥弾性の回
復が同程度に行なわれ、再びラムで加圧した
時、ゴム混合物の受ける剪断力を同程度に回復
することができ、オイル投入しない場合もカー
ボン分散度を高い水準に安定することができ
る。
(4) 混合機に温度調節設備や原料ゴムの素練保温
設備等の特殊な設備を要しないため装置が簡略
化される。
という効果がある。[Table] In the above mixture, a high degree of carbon dispersion can be obtained by setting the ram level in the range of 1.5 to 2.0 cm. In the above-mentioned embodiment, an example was shown in which oil is supplied based on the output signal of the comparison section 27, but it is also possible to perform only switching of the ram pressure without supplying oil. That is, as described above, after the ram 9 reaches the highest point P as the rubber mixture expands in volume, as mixing progresses, the viscosity of the mixture decreases and the rebound properties gradually decline. Ram 9 then begins to descend. By reducing the ram pressure at a certain level when the ram is lowering, or by raising the ram for a short period of time, the declining rebound resilience can be recovered, and when the ram is pressurized again, the shearing force applied to the rubber mixture can be reduced by the ram. You can recover to the same extent as at the highest point P. The switching timing for reducing the ram pressure or increasing the ram pressure coincides with the timing for adding oil when adding oil. Therefore, by reducing the ram pressure or increasing the ram pressure using the output signal of the comparison section 27, the degree of carbon dispersion can be similarly increased. The temperature inside the rubber mixing machine, the plasticity of the raw rubber, the temperature, etc. change seasonally, and some raw rubbers change from batch to batch. It brings about a major change in the mixing process that grinds the raw rubber and disperses the carbon black into the rubber. The output waveform of the ram motion represents changes in these mixing conditions depending on its shape and time lag, so
For homogeneous rubbers, the specific level, which determines the oil input or ram switching time, is always constant. Therefore, according to the present invention, (1) By performing oil injection at a specific level of ram motion, carbon dispersion can be stabilized at a high level despite changes in mixing conditions. (2) At a certain level of ram motion, the rubber and carbon mixture has a certain apparent volume, so if oil is introduced at this time, subsequent electrical energy can be stably added to the rubber mixture. . (3) When the ram pressure is reduced or the ram is lifted at a certain level of ram motion, as the viscosity of the rubber mixture decreases, the rebound resilience, which has been declining, recovers to the same extent, and when the ram is pressurized again. , the shearing force applied to the rubber mixture can be recovered to the same extent, and the degree of carbon dispersion can be stabilized at a high level even when no oil is added. (4) The equipment is simplified because the mixer does not require special equipment such as temperature control equipment or equipment for masticating and insulating raw rubber. There is an effect.
第1図は本発明に使用されるゴム混合機の縦断
側面図、第2図はラムモーシヨンセンサの一例を
示す回路、第3図は本発明を実施するための信号
処理回路図、第4図はラム位置、トルク、フイル
タ出力の時間的変化を示すグラフである。
3:ロータ、9:ラム、14:ラムモーシヨン
センサ、24:フイルタ、25:電圧減少検出
部、26:レベル設定部、27:比較器。
Fig. 1 is a vertical side view of a rubber mixer used in the present invention, Fig. 2 is a circuit showing an example of a ram motion sensor, Fig. 3 is a signal processing circuit diagram for carrying out the present invention, and Fig. 4 The figure is a graph showing temporal changes in ram position, torque, and filter output. 3: rotor, 9: ram, 14: ram motion sensor, 24: filter, 25: voltage reduction detection section, 26: level setting section, 27: comparator.
Claims (1)
ツクを混合する方法において、混合中におけるラ
ムの位置を連続的に検出し、ラムが最上昇点から
最下降点に至る間の特定レベルになつたときレベ
ル判定信号を出力し、この信号に基いてオイル投
入又はラム圧力の切換えを行なうことを特徴とす
るゴム混合方法。 2 ゴム混合機に取付けられたラムモーシヨンセ
ンサと、該ラムモーシヨンセンサの出力が最大レ
ベルに達して減少しはじめると出力を出す電圧減
少検出部と、ラムの特定レベルがあらかじめ設定
されたレベル設定部と、該レベル設定部の出力と
前記ラムモーシヨンセンサの出力とを比較し両者
が一致しかつ前記電圧減少検出部の出力が出てい
る条件で、レベル判定信号を出力する比較器とを
備えたことを特徴とするゴム混合装置。[Claims] 1. In a method of mixing carbon black with raw rubber using a rubber mixer, the position of the ram during mixing is continuously detected, and the position of the ram is continuously detected while the ram moves from the highest point to the lowest point. A rubber mixing method characterized in that a level determination signal is output when a specific level is reached, and oil injection or ram pressure switching is performed based on this signal. 2. A ram motion sensor attached to the rubber mixing machine, a voltage reduction detection section that outputs an output when the output of the ram motion sensor reaches a maximum level and begins to decrease, and a level at which a specific level of the ram is set in advance. a setting section; a comparator that compares the output of the level setting section and the output of the ram motion sensor and outputs a level determination signal under the condition that the two match and the output of the voltage reduction detection section is output; A rubber mixing device characterized by comprising:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14524979A JPS5670039A (en) | 1979-11-09 | 1979-11-09 | Rubber mixing and device therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14524979A JPS5670039A (en) | 1979-11-09 | 1979-11-09 | Rubber mixing and device therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5670039A JPS5670039A (en) | 1981-06-11 |
| JPS6226283B2 true JPS6226283B2 (en) | 1987-06-08 |
Family
ID=15380758
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14524979A Granted JPS5670039A (en) | 1979-11-09 | 1979-11-09 | Rubber mixing and device therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5670039A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57183867U (en) * | 1981-05-15 | 1982-11-22 | ||
| JPS6012973U (en) * | 1984-05-18 | 1985-01-29 | ダイワ精工株式会社 | Bale attachment device for spinning reel |
-
1979
- 1979-11-09 JP JP14524979A patent/JPS5670039A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5670039A (en) | 1981-06-11 |
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