JPH035209B2 - - Google Patents
Info
- Publication number
- JPH035209B2 JPH035209B2 JP59203360A JP20336084A JPH035209B2 JP H035209 B2 JPH035209 B2 JP H035209B2 JP 59203360 A JP59203360 A JP 59203360A JP 20336084 A JP20336084 A JP 20336084A JP H035209 B2 JPH035209 B2 JP H035209B2
- Authority
- JP
- Japan
- Prior art keywords
- kneading
- door top
- door
- height
- chambers
- 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 - Lifetime
Links
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
- B29B7/22—Component parts, details or accessories; Auxiliary operations
- B29B7/26—Component parts, details or accessories; Auxiliary operations for discharging, e.g. doors
- B29B7/263—Component parts, details or accessories; Auxiliary operations for discharging, e.g. doors from the underside in mixers having more than one rotor and a a casing closely surrounding the rotors
-
- 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
- B29B7/06—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
- B29B7/186—Rotors therefor
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Description
【発明の詳細な説明】
(産業上の利用用分野)
本発明は、ゴム、プラスチツク等を添加剤とと
もに混練するに当つて用いバツチ式バンバリミキ
サー等の密閉式混練機において、混練行程の各過
程に対応して最適の混練内容が得られるようにし
た新しい混練技術の提供に関する。Detailed Description of the Invention (Field of Industrial Application) The present invention is applicable to each step of the kneading process in an internal kneading machine such as a batch-type Banbury mixer used for kneading rubber, plastic, etc. with additives. The present invention relates to the provision of a new kneading technology that allows optimum kneading contents to be obtained in response to the above.
(従来技術)
ゴム、プラスチツク等の可塑性材料を必要な添
加剤とともに混練する場合に用いられるバツチ式
バンバリミキサー等の密閉式混練機は、例示する
までもなく周知のものであるが、その機構と内容
は次の通りである。第1図および第6図におい
て、ロータ1aを備えた混練室1およびロータ2
aを備えた混練室2は、軸方向に平行に並設され
るとともに軸方向に沿う連通部3によつて相互連
通状とされた密閉式のものであり、前記連通部3
の上部には材料投入口4が押込部材である押込ラ
ム5とともに形成され、また下部には開閉自在の
排出ドア6を備えた材料排出口7が形成される。
このさいロータ1a,2aには非噛合式と噛合式
の両タイプが存在する。また排出ドア6には左右
の混練室1,2を分割するドアトツプ8が、連通
部3内に突出状に形成され、このドアトツプ8の
突出高さは経験的に決定されるが、従来は第3図
に示すように排出ドア6と一体的に形成され、決
定された高さは一定不変である。このような密閉
式混練機による混練材料は、以下のようにしてそ
の混練が行なわれる。即ち目的の混練材料(例え
ばゴムカーボンブラツク等)を一括して材料投入
口4より投入し、押込ラム5を下降させて材料を
混練室1,2側へ押込み、ロータ1a,2aを相
反方向に回転させてその混練を開始するのである
が、その混練初期は、混練室1,2内で投入材料
の破砕、分砕が行なわれる。このさい投入材料が
ゴム、プラスチツク等の場合、投入材料は当初は
室温状態で高弾性体あるいは高粘性体であるため
に、過大な混練トルクを発生し、この高いピーク
トルクに耐えるようにロータ1a,2aの回転駆
動源として高馬力のモータを必要とし、また混練
機の本体強度もこれに応じて高める必要がある。
更にこの混練初期には、ゴム、プラスチツク等の
主材料の他に、低いカサ密度の各種添加剤も一緒
に投入しているため、見掛けの材料体積が大き
く、押込ラム5によつて材料を混練室1,2へ押
込むのに時間が掛るとともに、混練初期における
材料の破砕、分砕状態並びに発熱状態および添加
剤の主材料に対する混入は一般的に不安定であ
る。良好な混練を迅速に達成するためには、この
混練初期における主材料と添加剤の充分な混合
(マクロ的分散)の早期完了が必要で、このため
には材料全体を左右の混練室1,2間で活発に移
動させることが望ましい。更に混練が進行する
と、添加剤は主材料中に完全に混入するため、材
料体積は当然に減少する。この段階では材料の温
度は高まつて材料は流動状態となり、添加剤は流
動せん断下でその分散(ミクロ的分散)が行なわ
れるが、材料体積が減少しているために、材料は
左右混練室1,2の中間の連通部3における排出
ドア6のドアトツプ8上に滞溜気味となる。混練
を促進させるためには、この滞溜を抑制し、左右
の混練室1,2での有効な混練がされるように、
材料充填体積を増加させる必要がある。このよう
な混練行程は一定の混練エネルギーあるいは材料
温度となつた時点でストツプし、混練済み材料は
排出ドア6の開放によつて材料排出口7から排出
されることになる。(Prior Art) Internal kneading machines such as batch-type Banbury mixers used for kneading plastic materials such as rubber and plastics with necessary additives are well-known, needless to be exemplified, but their mechanism and The contents are as follows. In FIG. 1 and FIG. 6, a kneading chamber 1 equipped with a rotor 1a and a rotor 2 are shown.
The kneading chambers 2 equipped with the kneading chambers a are of a closed type and are arranged parallel to each other in the axial direction and communicated with each other by a communication section 3 along the axial direction.
A material input port 4 is formed together with a pushing ram 5 as a pushing member in the upper part of the machine, and a material discharge port 7 with a discharge door 6 that can be opened and closed is formed in the lower part.
At this time, the rotors 1a and 2a are of both non-meshing type and meshing type. Further, the discharge door 6 has a door top 8 formed in a protruding manner within the communication portion 3 to divide the left and right kneading chambers 1 and 2. Although the protrusion height of the door top 8 is determined empirically, conventionally As shown in FIG. 3, it is formed integrally with the discharge door 6, and the determined height remains constant. The materials kneaded by such an internal kneader are kneaded in the following manner. That is, the target kneading material (for example, rubber carbon black, etc.) is introduced all at once from the material input port 4, the pushing ram 5 is lowered to push the material into the kneading chambers 1 and 2, and the rotors 1a and 2a are moved in opposite directions. The kneading is started by rotating the kneading chamber, and at the beginning of the kneading, the input materials are crushed and divided in the kneading chambers 1 and 2. At this time, when the input material is rubber, plastic, etc., the input material is initially a highly elastic or highly viscous body at room temperature, so an excessive kneading torque is generated, and the rotor 1a is moved to withstand this high peak torque. , 2a are required to have a high horsepower motor as a rotational drive source, and the strength of the kneading machine body must be correspondingly increased.
Furthermore, at the beginning of this kneading, in addition to the main materials such as rubber and plastic, various additives with low bulk density are also added, so the apparent volume of the material is large, and the material is kneaded by the pushing ram 5. It takes time to push the material into the chambers 1 and 2, and the crushing, crushing and exothermic state of the material at the initial stage of kneading and the mixing of additives into the main material are generally unstable. In order to quickly achieve good kneading, it is necessary to complete sufficient mixing (macroscopic dispersion) of the main material and additives at the early stage of kneading. It is desirable to actively move between the two. As the kneading further progresses, the additive is completely mixed into the main material, so the material volume naturally decreases. At this stage, the temperature of the material increases and the material becomes fluid, and the additives are dispersed (microdispersion) under fluid shear. There appears to be some accumulation on the door top 8 of the discharge door 6 in the communication section 3 between the discharge doors 1 and 2. In order to promote kneading, this stagnation is suppressed and effective kneading is performed in the left and right kneading chambers 1 and 2.
It is necessary to increase the material filling volume. Such a kneading process is stopped when a certain kneading energy or material temperature is reached, and the kneaded material is discharged from the material discharge port 7 by opening the discharge door 6.
(発明が解決しようとする問題点)
上記したような密閉式混練機における問題点
は、既に述べた混練過程において見られるよう
に、混練初期における過大なピークトルクの発
生、材料の破砕、分砕状態や発熱状態および添加
剤の主材に対する混入等にムラを生じ易いこと、
更には混練進行に伴つて生じる材料の滞溜による
混練のエネルギー効率の低下、添加剤のミクロ分
散のムラ等であり、従来型式のものでは、混練室
形状が一定不変であるために、上記の問題点を解
決することは著しく困難である。(Problems to be Solved by the Invention) Problems with the internal kneading machine as described above, as seen in the kneading process already mentioned, include generation of excessive peak torque at the initial stage of kneading, crushing of materials, and crushing of materials. It is easy to cause unevenness in the state, heat generation state, and mixing of additives into the main material, etc.
Furthermore, the energy efficiency of kneading decreases due to the accumulation of materials that occurs as kneading progresses, and the microdispersion of additives becomes uneven.In the conventional type, the shape of the kneading chamber remains constant, so the above-mentioned problems occur. Solving the problems is extremely difficult.
(問題点を解決するための手段)
本発明は、上記した従来の密閉式混練機による
問題点を解決するために、左右の混練室形状を混
練中に可変とすることによつて、混練初期から終
期に亘る混練行程に対し、その混練過程に対応し
た適切な混練内容が得られるようにしたものであ
り、具体的には、それぞれロータを備えた混練室
の一対が軸方向に平行かつ連通状に設けられ、該
連通部の上部に材料投入口が押込部材とともに設
けられるとともに下部に材料排出口が排出ドアと
ともに設けられる密閉式混練機によつて目的材料
の混練を行なうに当り、前記排出ドアにおける連
通部内に突出するドアトツプの高さを、混練過程
に応じて変更しつつその混練を行なうことにあ
る。(Means for Solving the Problems) In order to solve the problems with the conventional closed-type kneading machine described above, the present invention makes it possible to change the shape of the left and right kneading chambers during the kneading process. This system is designed to obtain appropriate kneading contents corresponding to the kneading process from the beginning to the final stage, and specifically, a pair of kneading chambers, each equipped with a rotor, are parallel to each other in the axial direction and communicate with each other. When kneading target materials using a closed-type kneading machine, which has a material inlet in the upper part of the communication part together with the pushing member and a material outlet in the lower part together with the discharge door, the target material is kneaded. To perform kneading while changing the height of a door top projecting into a communicating part of a door according to the kneading process.
(作用)
本発明の技術的手段によれば、第1図および第
2図に示すように、左右の混練室1,2の連通部
3における排出ドア6において、その中央部分に
位置しかつ連通部3内に突出しているドアトツプ
8を、排出ドア6と別体に形成し、例えば油圧シ
リンダ9ピストン10等の昇降手段によつて、ド
アトツプ8を垂直昇降自在に排出ドア6に設け、
該ドアトツプ8の連通部3内に突出する高さを可
変とすることにより、連通部3を含めて混練室形
状を可変とすることができ、これにより混練室内
における混練内容を、混練過程に応じて適切に変
化させることが容易に可能である。即ちドアトツ
プ8の高さを変更することによつて、ピークトル
クの調整や混練の迅速化、更には効率的混練を行
なうことができるのである。(Function) According to the technical means of the present invention, as shown in FIG. 1 and FIG. A door top 8 protruding into the portion 3 is formed separately from the discharge door 6, and the door top 8 is provided on the discharge door 6 so that it can be vertically raised and lowered, for example, by a lifting means such as a hydraulic cylinder 9 and a piston 10.
By making the height of the door top 8 that protrudes into the communication section 3 variable, the shape of the kneading chamber including the communication section 3 can be made variable, thereby changing the kneading content in the kneading chamber depending on the kneading process. It is easily possible to change it appropriately. That is, by changing the height of the door top 8, it is possible to adjust the peak torque, speed up the kneading process, and moreover, achieve efficient kneading.
第4図および第5図は、ドアトツプ高さを低く
することによつて、ピークトルクを低下させるこ
とが可能であることを示した実験グラフ図であ
り、第1,2図で示したドアトツプ高さ可変の実
験用小型混練機による結果を示し、第4図は投入
材料形態としてブロツク状のものを用い、第5図
は投入材料形態として小片状のものを用いた場合
で、両図において縦軸はピークトルク値、横軸は
ドアトツプ8の高さ値をそれぞれ示しており、ま
たマークはドアトツプ8の上端形状が丸型のも
の、マークは上端形状が平型のもの、またマー
クは上端形状が角型のものをそれぞれ示したい
るが、図で明らかなように、何れもドアトツプ8
の高さを低くすることによつて、ピークトルクを
下げることが可能である。またこの他に、ドアト
ツプ8の高さを変えることによつて、押込ラム5
を最下限まで下降させる所要時間や、混練初期に
おける混練用主材料の粉砕状態、添加剤の混入状
態、また練り上がり材料粘度の1バツチ内のバラ
ツキ等が変化することも、同様の実験結果によつ
てそれぞれ変化することが確認されたのである。
従つてドアトツプ8の高さを可変とし、その混練
過程に応じてドアトツプ8の高さを随時変えるこ
とによつて、より短時間で効率の高い混練内容を
与えることが可能となるのである。例えば主材料
であるゴムに添加剤としてカーボンブラツク等を
混練する場合、通常第6図に示すような動力の経
時変化を示す。図において縦軸は動力、横軸は時
間を示すが、材料投入に始まつて、ゴム粉砕過程
が行なわれるとともにこれと並進して添加剤混入
過程が始まり、更に添加剤分散過程が続行して、
一連の混練行程が完成するのであり、動力の変化
過程は前記混練行程における各過程に対応してい
る。 Figures 4 and 5 are experimental graphs showing that it is possible to reduce peak torque by lowering the door top height. The results are shown using a small experimental kneading machine with variable height. Figure 4 shows the case where a block-shaped material is used as the input material, and Figure 5 shows the result when a small piece-shaped material is used as the input material. The vertical axis shows the peak torque value, and the horizontal axis shows the height value of the door top 8. Also, the mark indicates the door top 8 whose upper end is round, the mark indicates the upper end of which is flat, and the mark indicates the height of the door top 8. The square shape is shown, but as is clear from the figure, all of them have a door top of 8.
It is possible to lower the peak torque by lowering the height of. In addition, by changing the height of the door top 8, the pushing ram 5 can be
Similar experimental results also show that the time required to lower the kneaded material to the lowest limit, the pulverized state of the main material for kneading at the initial stage of kneading, the state of additives mixed in, and the variation in the viscosity of the kneaded material within one batch, etc. Therefore, it was confirmed that each of them changes.
Therefore, by making the height of the door top 8 variable and changing the height of the door top 8 as needed according to the kneading process, it is possible to provide more efficient kneading in a shorter time. For example, when adding carbon black or the like as an additive to rubber, which is the main material, the power normally changes over time as shown in FIG. In the figure, the vertical axis shows power and the horizontal axis shows time. Starting from the input of materials, the rubber crushing process is carried out, and parallel to this, the additive mixing process begins, and then the additive dispersion process continues. ,
A series of kneading processes is completed, and the power change process corresponds to each process in the kneading process.
従つて、先ずドアトツプ8の高さを最下限に設
定し、ゴム、添加剤を材料投入口4を投入し、押
込ラム5を下降させて材料を混練室1,2内に押
込むのである。このさいドアトツプ高さが低いた
めに、低動力ピークで混練が開始される。また同
時に混練室空間がより広いため、押込ラム5の降
下はドアトツプ高さが高い時に比べより速いとと
もに、左右混練室1,2間でゴム粉砕や添加剤の
活発な移動が良好に促進されるのである。かくし
てゴムの粉砕化並びに材料温度の昇温が進行し、
動力がある程度低下してくれば、ドアトツプ8の
高さを高め、この直上の連通部3の空間をせばめ
て、左右混練室1,2内での添加剤の混入作用を
強力に高めることができるのである。また適度な
時間を経過して後、再びドアトツプ8を下げ、連
通部3の空間を広めて、左右混練室内の各材料の
移動を高めることにより、全体の混合を良好に促
進させることができる。これに続いて再びドアト
ツプ8を上げ、左右混練室1,2内での混入した
添加剤の分散作用をより高めることができるよう
に、経時変化、動力変化に即応して、混練の各過
程に応じ、そのドアトツプ8の高さを適切に変化
させて、目的材料の混練、混合の能率向上とその
内容の改善を図ることができ、従来技術において
生じる混練上の問題点を解消させることができる
のである。 Therefore, first, the height of the door top 8 is set to the lowest limit, rubber and additives are introduced into the material input port 4, and the pushing ram 5 is lowered to push the materials into the kneading chambers 1 and 2. At this time, since the door top height is low, kneading is started at a low power peak. At the same time, since the kneading chamber space is wider, the push-in ram 5 descends more quickly than when the door top height is high, and the active movement of rubber crushing and additives between the left and right kneading chambers 1 and 2 is promoted well. It is. In this way, the rubber becomes pulverized and the material temperature increases,
When the power decreases to a certain extent, the height of the door top 8 can be increased and the space of the communication section 3 directly above it can be narrowed to strongly increase the effect of mixing additives in the left and right kneading chambers 1 and 2. It is. Furthermore, after a suitable period of time has elapsed, the door top 8 is lowered again to widen the space in the communication section 3, thereby increasing the movement of each material in the left and right kneading chambers, thereby promoting overall mixing. Following this, the door top 8 is raised again, and in order to further enhance the dispersion effect of the mixed additives in the left and right kneading chambers 1 and 2, each kneading process is adjusted in response to changes over time and power changes. Accordingly, the height of the door top 8 can be changed appropriately to improve the efficiency and content of kneading and mixing of the target materials, and the problems in kneading that occur in the conventional technology can be solved. It is.
(実施例)
本発明の具体的実施例について説示する。第
1,2図において、ロータ1a,2aを具備した
左右の混練室1,2、材料投入口4押込ラム5
は、従来の密閉式混練機のそれと同一であるので
説明は省略し、ドアトツプ8の必要構造について
のみ述べる。この図例では排出ドア6内に油圧シ
リンダ9を設置し、該シリンダ9のピストン10
に排出ドア6と別体に設けたドアトツプ8の下部
を一体に形成または連結し、ドアトツプ8を排出
ドア6の中央頂部に設けたガイド孔6aにより、
垂直昇降自在に設けてある。図例ではドアトツプ
8の上端は円弧面あるいは半球面等の丸型をして
あるが、これは平坦な直線面による平型でも、あ
るいは3角山形の角型としても同効である。また
ドアトツプ8の軸方向長さは排出ドア6の長さ
(混練室奥行)と略同一の長さとすることが好ま
しい。即ち本発明による可変ドアトツプ8は、ド
アトツプ全長に対し部分的に設けることによつて
もそれなりの効果はあるが、全長に亘るのが更に
効果的である。その理由は、ドアトツプ8の高さ
を変更して、ドアトツプ8上の連通部3における
材料滞留を抑制し、あるいは左右混練室1,2間
に亘る材料移動を促進したりするように、混練中
の材料移動に対するコントロール効果は、ドアト
ツプ8の上下方向移動長さおよび巾が大きい程増
大するのであり、従つてその軸方向長さは可及的
全長に亘ることが最良だからである。但し第7図
に例示するように、左右の混練室1,2における
各ロータ1a,2aが長翼11短翼12を対称に
有し、投入材料を中央部へ集める作用を行ない、
ロータ1a,2a上における翼長さにおいて、長
翼11の長さl1と短翼12の長さl2とが、l1/L
0.6〜0.7=2/3、l2/L0.3〜0.4=1/3の関係と
なつている時、中央部へ集められる材料の動きを
コントロールすることも、本発明における可変ド
アトツプ8の効果でもあるので、このような場
合、中央部にL1/L=1/3以上の長さで可変ドア
トツプ8を設ければ、長短両翼11,12による
中央部へ材料を集める機能が阻外あるいは促進さ
れ、本発明による混練内容のコントロール効果を
同様に期待できるものである。尚同図において矢
印は材料の動きを示したものである。(Example) Specific examples of the present invention will be described. In Figures 1 and 2, left and right kneading chambers 1 and 2 equipped with rotors 1a and 2a, a material input port 4 and a pushing ram 5 are shown.
Since this is the same as that of a conventional internal kneading machine, the explanation will be omitted and only the necessary structure of the door top 8 will be described. In this example, a hydraulic cylinder 9 is installed inside the discharge door 6, and a piston 10 of the cylinder 9 is installed.
The lower part of the door top 8 provided separately with the discharge door 6 is integrally formed or connected to the discharge door 6, and the guide hole 6a provided in the center top of the discharge door 6 allows the door top 8 to
It is installed so that it can be raised and lowered vertically. In the illustrated example, the upper end of the door top 8 has a round shape such as an arcuate surface or a hemispherical surface, but it can be equally effective as a flat shape with a flat straight surface or a square shape with a triangular chevron shape. Further, it is preferable that the axial length of the door top 8 is approximately the same as the length of the discharge door 6 (depth of the kneading chamber). That is, the variable door top 8 according to the present invention can have some effect even if it is provided partially over the entire length of the door top, but it is even more effective when it is provided over the entire length of the door top. The reason for this is that the height of the door top 8 is changed to suppress material retention in the communication section 3 above the door top 8 or to promote material movement between the left and right kneading chambers 1 and 2 during kneading. The control effect on the material movement increases as the length and width of the vertical movement of the door top 8 increases, and therefore, it is best for the axial length to cover the entire length as much as possible. However, as illustrated in FIG. 7, each of the rotors 1a and 2a in the left and right kneading chambers 1 and 2 has long blades 11 and short blades 12 symmetrically, and serves to collect the input material to the center,
Regarding the blade length on the rotors 1a and 2a, the length l 1 of the long blade 11 and the length l 2 of the short blade 12 are l 1 /L.
When the relationship is 0.6~0.7=2/3 and l2 /L0.3~0.4=1/3, the effect of the variable door top 8 in the present invention is to control the movement of the material collected to the center. Therefore, in such a case, if the variable door top 8 is provided in the center with a length of L 1 /L = 1/3 or more, the function of collecting material to the center by the long and short wings 11 and 12 will be hindered or Therefore, the effect of controlling the kneading content according to the present invention can be similarly expected. In the figure, arrows indicate the movement of the material.
また本発明における可変ドアトツプ8の構成
は、既知の連続混練機において用いるインサート
とは全く別異のものであることを付言する。即ち
FCMタイプの連続混練機においては、第8図に
例示するように、一対のロータ13a,14aに
よる左右のチヤンバ13,14間において、その
混練部の中間上下にインサート15,15を挿入
して、混練効果を高めているが、両インサート1
5,15の主たる作用効果は、左右のチヤンバ1
3,14間の連通部を、何等せん断作用を受ける
ことなく軸方向へ移動する材料(所謂シヨートパ
ス材料を阻止するためのものであつて、両インサ
ートは運転中は全く固定不動のものであり、本発
明のように左右混練室1,2間の材料移動を、混
練中にコントロールするものとは全く相違する。
尚同図において13b,14bはロータ13a,
14aに続く材料フイード用スクリユで、材料投
入口はこの上部にあり、また16は左右チヤンバ
13,14前端の排出口を示している。 It should also be noted that the configuration of the variable door top 8 in the present invention is completely different from the inserts used in known continuous kneading machines. That is,
In the FCM type continuous kneading machine, as illustrated in FIG. 8, inserts 15, 15 are inserted between the left and right chambers 13, 14 between the left and right chambers 13, 14 formed by a pair of rotors 13a, 14a, in the upper and lower middle of the kneading section. Although the kneading effect is enhanced, both inserts 1
The main effect of 5 and 15 is that the left and right chambers 1
This is to prevent material (so-called short pass material) from moving in the axial direction through the communication portion between 3 and 14 without being subjected to any shearing action, and both inserts are completely fixed and immovable during operation. This is completely different from the present invention in which the movement of materials between the left and right kneading chambers 1 and 2 is controlled during kneading.
In the figure, 13b and 14b are rotors 13a,
A material feed screw follows 14a, and the material input port is located at the top thereof, and 16 indicates the discharge ports at the front ends of the left and right chambers 13, 14.
第1図において可変ドアトツプ8の高さを変化
させるに当り、油圧シリンダ方式を示したが、こ
の昇降機構としては、第9図Aおよび第9図Bに
例示するような機械式手段を用いることもでき
る。即ち両図に示すように、排出ドア6の中央頂
部に開設したガイド孔6aに続いてドア内部にス
ライドガイド室17を設け、前記ガイド孔6aに
昇降自在に挿設したドアトツプ8の基部8aを前
記スライドガイド室17内に昇降自在兼回動不可
能に内嵌し、この基部8aに形成したネジ孔18
を、スライドガイド室17内に排出ドア6外から
モータ19軸受20を介して可回動に装設したネ
ジ軸21を螺合させたものである。これによれば
ネジ21の正逆回動により、ドアトツプ8の基部
8aがスライドガイド室17内において上下する
ことにより、ドアトツプ8はそのガイド孔6aか
ら連通部3内に突出する高さLを自在に変更でき
るものであり、ドアトツプ8の昇降手段は自由に
設計可能である。 Although a hydraulic cylinder method is shown in FIG. 1 to change the height of the variable door top 8, mechanical means such as those illustrated in FIGS. 9A and 9B may be used as the elevating mechanism. You can also do it. That is, as shown in both figures, a slide guide chamber 17 is provided inside the door following a guide hole 6a opened at the center top of the discharge door 6, and a base 8a of the door top 8 is inserted into the guide hole 6a so as to be able to rise and fall. A screw hole 18 is fitted into the slide guide chamber 17 so as to be able to move up and down and not rotate, and is formed in the base portion 8a.
A screw shaft 21 is screwed into the slide guide chamber 17 so as to be rotatable from the outside of the discharge door 6 via a motor 19 and a bearing 20. According to this, the base portion 8a of the door top 8 moves up and down within the slide guide chamber 17 by forward and reverse rotation of the screw 21, so that the door top 8 can freely adjust the height L of protruding into the communication portion 3 from the guide hole 6a. The means for raising and lowering the door top 8 can be freely designed.
このドアトツプ8を混練過程に対応して、その
高さを変更するに当つては、遠隔操作によつて自
動制御することになるが、その制御方式について
は各種のプログラムが実施例として上げられる
が、基本的には先に第6図において説示した縦軸
に動力変化をとり、横軸に混練時間経過をとる動
力一時間チヤートにおいて示される1バツチの混
練行程を示す曲線図において、ある設定混練時間
ti以後において、設定動力PがPiになるとドアト
ツプ8の高さL(第9図A参照)をLicmに設定す
るようにするのである。但しiはi=1〜nまで
のn回、ドアトツプ8を上下する意味のものであ
る。即ち具体的には、材料投入時にはL=0に設
定(最下限位置)して置き、動力PがP2となり、
混練時間がt2となつた時、L=0のドアトツプを
図示のようにL1位置から所定のL2位置まで上昇
させ、この状態で混練行程が動力P3、時間t3の位
置となれば、L2の状態でL3までその状態を保持
しているドアトツプ8をL3からL4のように下降
させ、このL4の状態を保持して混練行程が動力
P4、時間t4となれば、ドアトツプ8をL5からL6の
ように上昇させるように、動力変化と時間経過に
よつてその混練過程に対応したドアトツプ8の上
下が自動的に得られることは明らかである。勿論
プログラム設定条件としては、動力のみでなく、
例えば1バツチの必要混練時間tのみでもよく、
あるいは混練材料温度Tによつてもよく、更には
ロータ回転動力としてモータを用いる場合、動力
消費に伴なう積算電力ΣP等を用いることも可能
であり、第11図は混練時間tのみを設定条件と
して用い、時間tの経時変化に応じてドアトツプ
8の高さLをL1〜L8のように自動的に上下変化
させる場合を示し、第12図は混練時間tに伴な
う材料温度Tの経時変化に対応して、ドアトツプ
8の高さLをL1〜L8のように自動的に上下変化
させる場合を示している。また上記例示した各設
定条件を組合せてドアトツプ8の高さLを変化さ
せるようにしても同効である。 Changing the height of the door top 8 in response to the kneading process is automatically controlled by remote control, and various programs can be cited as examples of the control method. Basically, in the curve diagram showing the kneading process of one batch shown in the power one hour chart where the vertical axis shows the power change and the horizontal axis shows the kneading time elapsed, as explained in FIG. time
After ti, when the set power P becomes Pi, the height L of the door top 8 (see FIG. 9A) is set to Licm. However, i means that the door top 8 is raised and lowered n times from i=1 to n. That is, specifically, when loading the material, set L = 0 (lowest limit position), power P becomes P 2 ,
When the kneading time reaches t2 , the door top with L=0 is raised from the L1 position to the predetermined L2 position as shown in the figure, and in this state, the kneading process reaches the position of power P3 and time t3 . For example, the door top 8 is held at L 2 until L 3 , and then the door top 8 is lowered from L 3 to L 4 , and while the L 4 is maintained, the kneading process is powered.
When P 4 and time t 4 come, the door top 8 is automatically moved up and down corresponding to the kneading process by changing the power and elapsed time so that the door top 8 is raised from L 5 to L 6 . That is clear. Of course, the program setting conditions include not only power but also
For example, the required kneading time t for one batch may be sufficient.
Alternatively, it may be based on the kneading material temperature T, or furthermore, when a motor is used as rotor rotational power, it is also possible to use the integrated power ΣP associated with power consumption, etc. In Fig. 11, only the kneading time t is set. A case is shown in which the height L of the door top 8 is automatically changed up and down from L 1 to L 8 according to the change in time t as a condition, and FIG. 12 shows the material temperature as the kneading time t changes. A case is shown in which the height L of the door top 8 is automatically changed up and down from L1 to L8 in response to changes in T over time. The same effect can also be achieved by changing the height L of the door top 8 by combining the setting conditions exemplified above.
第13,14図は前記した遠隔操作を実際的に
行なうためのシステム例を示したものであり、第
13図に示すように演算ユニツト22に対し、例
えば動力Pは、混練ロータの回転動力源としての
モータ23より電力計24を介し、また混練時間
tはタイマー25を介し、また材料温度Tは混練
室内に設けた温度センサ26を介し、何れもパル
ス信号等として入力させ、ドアトツプ8側には変
位計27を配設してその上下変位を同様にユニツ
ト22に入力させ、各条件下における温度センサ
22による演算結果はドアトツプ上下用の出力と
してサーボバルブ28側に送られ、ドアトツプ上
下用の油圧ユニツト29を作動させ、プログラム
に応じたドアトツプ8の上下変化をコントロール
することができ、また第14図に示したものは、
油圧システム回路の1例を示しており、設定条件
30の組込まれた動力/変位演算回路31に動力
信号P′、時間信号t′、あるいは温度信号T′を入力
させ、変位計27によるドアトツプ8の位置検索
と相まつて、サーボアンプ32を経由してサーボ
バルブ28を介し油圧ユニツト29を作動させる
ものであり、何れにもせよドアトツプ8の遠隔操
作による自動上下コントロール(混練過程に応じ
ての)は、既知の各種自動制御システムを容易に
採用できる。 13 and 14 show an example of a system for practically performing the above-mentioned remote control. As shown in FIG. The kneading time t is input from the motor 23 via the wattmeter 24, the kneading time t is input via the timer 25, and the material temperature T is input via the temperature sensor 26 installed in the kneading chamber as pulse signals etc. A displacement meter 27 is installed and its vertical displacement is similarly input to the unit 22, and the calculation results from the temperature sensor 22 under each condition are sent to the servo valve 28 side as an output for the door top up and down. By operating the hydraulic unit 29, the vertical movement of the door top 8 can be controlled according to the program.
An example of a hydraulic system circuit is shown in which a power signal P', a time signal t', or a temperature signal T' is inputted to a power/displacement calculation circuit 31 in which a setting condition 30 is incorporated, and a door top 8 is detected by a displacement meter 27. In conjunction with the position search, the hydraulic unit 29 is actuated via the servo valve 28 via the servo amplifier 32, and in any case, the door top 8 is automatically controlled up and down by remote control (depending on the kneading process). can easily employ various known automatic control systems.
以上に例示した各実施例によれば、既に作用の
項において原則的に説示したように、密閉式混練
機を用いて、各種可塑材料の混練を行なうに当
り、連通部3内に突出するドアトツプ8の高さL
を、1バツチの混練行程において、その各混練過
程において必要とされる適切な混練内容が得られ
るように上下調整し、これによつて混練初期にお
けるピークトルクの低下、低動力による混練起動
を容易とし、また混練の進行に伴なう主材料や添
加剤の活発な移動、あるいは抑制を、その混練過
程に対応して正確容易に規制し、混練、混合の内
容と効率の向上が期待できることになる。 According to each of the embodiments exemplified above, as already explained in principle in the operation section, when kneading various plastic materials using a closed kneader, the door top protruding into the communication portion 3 is used. 8 height L
is adjusted up and down to obtain the appropriate kneading content required in each kneading process in one batch of kneading process, thereby reducing the peak torque at the initial stage of kneading and making it easier to start kneading with low power. In addition, the active movement or suppression of main materials and additives as kneading progresses can be accurately and easily controlled in accordance with the kneading process, and it is expected that the content and efficiency of kneading and mixing will be improved. Become.
(発明の効果)
本発明によれば、バツチ式バンバリミキサー等
の密閉式混練機において各種材料と添加剤との混
練作業を行なうに当り、ドアトツプを混練中に上
下変化させてその混練を行なうことにより、従来
技術における問題点、即ち混練初期における過大
な混練トルクの要求、高いピークトルクに耐え得
るための高馬力モータや混練機本体強度の増強を
回避でき、更には左右混練室間での主材料や添加
剤の活発な移動による混練初期における材料の破
砕、分砕状態や発熱状態、添加剤混入のムラをな
くし、安定均一な初期混練が得られる。このこと
は同時に初期混練における材料と添加剤の充分な
混合の早期完了により、良好な混練を迅速に達成
できることになるのである。更には混練の進行に
伴ない、材料が連通部やドアトツプ上に滞留する
現象も抑制することができ、滞留によつて生じる
混練のエネルギ効率の低下、添加剤分散ムラをな
くすことができるのであり、しかもこれはドアト
ツプ8の高さを変化させ、混練室形状を可変とす
ることにより、何れも確実容易に得られる点でき
わめて有利であり、しかもこのドアトツプ8の高
さの変化は、混練主材料の粉砕過程、添加剤の混
入過程、混入された添加剤の分散過程のそれぞれ
に対応して、その過程において必要なドアトツプ
8の高さを変化させることができ、適切な混練内
容を混練全行程に亘つて与えることにより、混練
の質的向上が確保できるのである。(Effects of the Invention) According to the present invention, when kneading various materials and additives in an internal kneading machine such as a batch-type Banbury mixer, the door top can be moved up and down during kneading to perform the kneading. This makes it possible to avoid problems with conventional technology, such as the requirement for excessive kneading torque at the initial stage of kneading, and the need to increase the strength of a high-horsepower motor or the kneader main body in order to withstand high peak torque. Stable and uniform initial kneading can be achieved by eliminating material crushing, fragmentation, heat generation, and uneven mixing of additives during the initial stage of kneading due to the active movement of materials and additives. At the same time, by early completion of sufficient mixing of materials and additives during initial kneading, good kneading can be quickly achieved. Furthermore, as the kneading progresses, it is possible to suppress the phenomenon in which materials accumulate in the communicating parts and on the door top, and it is possible to eliminate the decrease in energy efficiency of kneading and uneven dispersion of additives caused by the accumulation. Moreover, this is extremely advantageous in that both can be achieved reliably and easily by changing the height of the door top 8 and by making the shape of the kneading chamber variable. The height of the door top 8 can be changed depending on the material crushing process, additive mixing process, and dispersion process of the mixed additives, so that the appropriate kneading content can be adjusted throughout the kneading process. By applying it over the course of the process, it is possible to ensure a qualitative improvement in kneading.
第1図は本発明実施例としての混練機縦断面
図、第2図は同ドアトツプの斜面図、第3図は従
来のドアトツプ斜面図、第4,5図は本発明によ
る可変ドアトツプとピークトルクの関係グラフ
図、第6図は混練行程の動力一時間チヤート図、
第7図は本発明による可変ドアトツプ変形実施例
の説明図、第8図は連続混練機におけるインサー
ト説明図、第9図A、第9図Bは本発明可変ドア
トツプの昇降機構実施例の全体図および要部断面
図、第10,11,12図は本発明によるドアト
ツプ上下作動プログラム実施例の各フローシート
図、第13,14図は同遠隔操作システム各実施
例のフローシート図である。
1a,2a……ロータ、1,2……混練室、3
……連通部、4……材料投入口、5……押込ラ
ム、6……排出ドア、7……材料排出口、8……
ドアトツプ、9……油圧シリンダ、10……ピス
トン、18……ネジ孔、21……ネジ軸。
Fig. 1 is a vertical sectional view of a kneading machine as an embodiment of the present invention, Fig. 2 is a slope view of the same door top, Fig. 3 is a slope view of a conventional door top, and Figs. 4 and 5 are a variable door top and peak torque according to the present invention. Figure 6 is a power hour chart of the kneading process.
Fig. 7 is an explanatory diagram of a modified embodiment of the variable door top according to the present invention, Fig. 8 is an explanatory diagram of an insert in a continuous kneading machine, and Figs. 9A and 9B are general views of an embodiment of the lifting mechanism of the variable door top of the present invention. FIGS. 10, 11, and 12 are flow sheet diagrams of an embodiment of the door top up/down operation program according to the present invention, and FIGS. 13 and 14 are flow sheet diagrams of each embodiment of the remote control system. 1a, 2a...rotor, 1, 2...kneading chamber, 3
...Communication section, 4...Material input port, 5...Pushing ram, 6...Discharge door, 7...Material discharge port, 8...
Door top, 9...hydraulic cylinder, 10...piston, 18...screw hole, 21...screw shaft.
Claims (1)
向に平行かつ連通状に設けられ、該連通部の上部
に材料投入口が押込部材とともに設けられるとと
もに下部に材料排出口が排出ドアとともに設けら
れる密閉式混練機によつて目的材料の混練を行な
うに当り、前記排出ドアにおける連通部内に突出
するドアトツプの高さを、混練過程に応じて変更
しつつその混練を行なうことを特徴とする密閉式
混練機の混練方法。1 A pair of kneading chambers, each equipped with a rotor, are provided in parallel and in communication with each other in the axial direction, a material input port is provided together with a pushing member in the upper part of the communication part, and a material discharge port is provided in the lower part with a discharge door. A closed kneading method characterized in that when kneading target materials using a kneading machine, the kneading is carried out while changing the height of a door top protruding into the communication portion of the discharge door according to the kneading process. Machine kneading method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59203360A JPS6182829A (en) | 1984-09-27 | 1984-09-27 | Kneading method of tightly closed kneader |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59203360A JPS6182829A (en) | 1984-09-27 | 1984-09-27 | Kneading method of tightly closed kneader |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6182829A JPS6182829A (en) | 1986-04-26 |
| JPH035209B2 true JPH035209B2 (en) | 1991-01-25 |
Family
ID=16472737
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59203360A Granted JPS6182829A (en) | 1984-09-27 | 1984-09-27 | Kneading method of tightly closed kneader |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6182829A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19649493C1 (en) * | 1996-11-29 | 1998-11-12 | Continental Ag | Internal mixer for processing rubber or rubber-like plastic mixtures |
| JP5320271B2 (en) * | 2009-11-26 | 2013-10-23 | 日立マクセル株式会社 | Kneading equipment |
| KR102756829B1 (en) * | 2023-12-28 | 2025-01-22 | 한국바이오플랜트 주식회사 | Melt extrusion module for recycling PET flakes |
-
1984
- 1984-09-27 JP JP59203360A patent/JPS6182829A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6182829A (en) | 1986-04-26 |
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