JPH054208B2 - - Google Patents
Info
- Publication number
- JPH054208B2 JPH054208B2 JP58090748A JP9074883A JPH054208B2 JP H054208 B2 JPH054208 B2 JP H054208B2 JP 58090748 A JP58090748 A JP 58090748A JP 9074883 A JP9074883 A JP 9074883A JP H054208 B2 JPH054208 B2 JP H054208B2
- Authority
- JP
- Japan
- Prior art keywords
- hopper
- service
- output
- resin
- load cell
- 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
- 239000011347 resin Substances 0.000 claims description 37
- 229920005989 resin Polymers 0.000 claims description 37
- 239000008188 pellet Substances 0.000 claims description 23
- 230000001186 cumulative effect Effects 0.000 claims description 12
- 238000001125 extrusion Methods 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 238000005259 measurement Methods 0.000 claims 1
- 238000004898 kneading Methods 0.000 description 3
- 239000004020 conductor Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007765 extrusion coating Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/29—Feeding the extrusion material to the extruder in liquid form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/9218—Weight
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92333—Raw material handling or dosing, e.g. active hopper or feeding device
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
- B29C2948/926—Flow or feed rate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92828—Raw material handling or dosing, e.g. active hopper or feeding device
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92866—Inlet shaft or slot, e.g. passive hopper; Injector, e.g. injector nozzle on barrel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/9298—Start-up, shut-down or parameter setting phase; Emergency shut-down; Material change; Test or laboratory equipment or studies
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/05—Filamentary, e.g. strands
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processes Specially Adapted For Manufacturing Cables (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】 〔発明の技術分野〕 本発明は押出機における樹脂供給装置に係る。[Detailed description of the invention] [Technical field of invention] The present invention relates to a resin supply device for an extruder.
電線の絶縁層、シース等を被覆する押出機の樹
脂供給装置は第1図に示すように構成されてい
る。すなわち、押出機ハウジング1の導体入口側
にはメインホツパ2の下端が連通させてあり、メ
インホツパ2の上面板2aにはサービスホツパ3
が取付けられている。なお、サービスホツパ3は
メインホツパ内に延入し、先端を斜めに切落され
た弁ストツパ3aを有する。また、サービスホツ
パ3の上部に連通したパイプ4の他端は樹脂パレ
ツト5内の樹脂ペレツト6中に埋没している。さ
らに、サービスホツパ3はパイプ7により吸気フ
アン8に連通されている。
A resin supply device for an extruder for coating an insulating layer, sheath, etc. of an electric wire is constructed as shown in FIG. That is, the lower end of the main hopper 2 is connected to the conductor inlet side of the extruder housing 1, and the service hopper 3 is connected to the upper surface plate 2a of the main hopper 2.
is installed. The service hopper 3 extends into the main hopper and has a valve stopper 3a whose tip is cut off diagonally. The other end of the pipe 4 communicating with the upper part of the service hopper 3 is buried in the resin pellet 6 in the resin pallet 5. Further, the service hopper 3 is connected to an intake fan 8 through a pipe 7.
また、メインホツパ2には、第2のサービスホ
ツパ9が取付けてあり、このホツパには粉砕機1
0からのパイプ11が連通されている。図中、1
2,13はレベル計を示す。 Further, a second service hopper 9 is attached to the main hopper 2, and a crusher 1 is attached to this hopper.
A pipe 11 from 0 is connected. In the figure, 1
2 and 13 indicate level meters.
上記の構成において、樹脂の供給は次のように
して行われる。まず、作業開始指令によつて吸気
フアン8が起動される。これにより、サービスホ
ツパ3内が負圧になると、樹脂パレツト5内の樹
脂ペレツト6は、パイプ4を通つてサービスホツ
パ3内に吸引される。吸引フアン8はタイマによ
つて制御され、サービスホツパ3内に適量の樹脂
ペレツトが吸引されるのに必要な時間運転され
る。フアン8が停止されると、大気中からサービ
スホツパ3内に空気が入込み、サービスホツパ3
とメインホツパ2内の圧力がバランスしたところ
で両者間の弁(図略)が開き、サービスホツパ3
内のペレツトはメインホツパ2内に落下する。次
に、弁は閉じられフアン8は再起動され、前記と
同様にしてサービスホツパ3を経由して、メイン
ホツパ2内にぺレツトを充填する。而して、この
操作はメインホツパ2内に堆積したペレツトの山
14が、ストツパ3aに当り弁が閉鎖できなくな
るまで自動的に繰返される。 In the above configuration, the resin is supplied as follows. First, the intake fan 8 is activated in response to a work start command. As a result, when the inside of the service hopper 3 becomes negative pressure, the resin pellets 6 in the resin pallet 5 are sucked into the service hopper 3 through the pipe 4. The suction fan 8 is controlled by a timer and is operated for a period of time necessary to suck an appropriate amount of resin pellets into the service hopper 3. When the fan 8 is stopped, air enters the service hopper 3 from the atmosphere, and the service hopper 3
When the pressure in the main hopper 2 and the main hopper 2 are balanced, a valve (not shown) between the two opens, and the service hopper 3
The pellets inside fall into the main hopper 2. Next, the valve is closed and the fan 8 is restarted to fill the main hopper 2 with pellets via the service hopper 3 in the same manner as described above. This operation is automatically repeated until the pile of pellets 14 accumulated in the main hopper 2 hits the stopper 3a and the valve cannot be closed.
押出機が稼働してメインホツパ2内のペレツト
が減り、上部のレベル計12の位置までペレツト
の山の表面が低下すると、上記と同様にしてメイ
ンホツパ2にペレツトが補充される。何らかの理
由でサービスホツパ3にペレツトが吸引されなか
つた場合には、サービスホツパにはそれを検知す
る能力はないので、ペレツトの山の表面が下部の
レベル計13の位置まで低下した時、警報が発せ
られるようにしてあり、作業者がこの警報により
適当な処置をとる。 When the extruder is operated and the number of pellets in the main hopper 2 decreases, and the surface of the pile of pellets falls to the level gauge 12 at the top, the main hopper 2 is replenished with pellets in the same manner as described above. If pellets are not sucked into the service hopper 3 for some reason, the service hopper does not have the ability to detect this, so an alarm is issued when the surface of the pellet pile drops to the level indicated by the level meter 13 at the bottom. The operator takes appropriate action based on this alarm.
なお、粉砕機10は運転開始時にねりが良好に
なるまで行う空ねりによつて発生したねり屑を粉
砕してホツパ9に送込み、最終的にはメインホツ
パ2に回収するためのものである。 The pulverizer 10 is used to crush the dough waste generated by dry kneading that is performed at the start of operation until the dough becomes good, send it to the hopper 9, and finally collect it in the main hopper 2.
上記構成の樹脂供給装置にあつては、樹脂の供
給量を正確に知ることはできない。コスト管理
上、作業管理上、供給した樹脂量を正確に知るこ
とが重要であるのに対し、不都合である。
In the resin supply device having the above configuration, it is not possible to accurately know the amount of resin supplied. This is inconvenient, since it is important to accurately know the amount of resin supplied for cost control and work management purposes.
本発明は上記の事情に基きなされたもので、樹
脂供給量を正確に知ることができる樹脂供給装置
を得ることを目的としている。
The present invention was made based on the above-mentioned circumstances, and an object of the present invention is to obtain a resin supply device that can accurately determine the amount of resin supplied.
〔発明の概要〕
本発明の樹脂供給装置は、押出機ハウジングに
連通するメインホツパと、このメインホツパに連
通する第1、第2のサービスホツパと、前記第1
のサービスホツパに吸気口を連通させた吸気フア
ンと、前記第1のサービスホツパに連通し樹脂ペ
レツトを収容する樹脂パレツトと、空ねり時の空
出の樹脂を粉砕して前記第2のサービスホツパに
供給する粉砕機と、前記吸気フアンの起動、停止
を自動的に繰返して前記第1のサービスホツパ内
の負圧と大気圧との交番によつて前記メインホツ
パに所定量の樹脂ペレツトを落下、貯蔵させるよ
うにした樹脂供給装置において、前記第1、第2
のサービスホツパを前記メインホツパとは機械的
に切り離して設置するとともに前記メインホツパ
を前記押出機ハウジングとは機械的に切り離して
設置し、前記メインホツパ、前記第1のサービス
ホツパの重量を測定する第1、第2のロードセル
を設け、さらに前記粉砕機に供給される空出の樹
脂を計量する台スケールを設け、前記第1、第2
のロードセルおよび前記台スケールの測定出力を
デジタル化する変換手段を設け、製品取り開始時
の前記第2のロードセル出力の累積値をW1、押
出停止時の前記第2のロードセル出力の累積値を
W2、前記第1のロードセルの製品取り開始時の
出力をW3、押出停止時の前記第1のロードセル
の出力をW4、前記台スケールの出力の累計量を
WB、W1−W3すなわち空出量をWAとして、CPU
により次式
WD=(W2−W4)−WA+WB
によつてケーブル等への付着量WDを求めること
を特徴とする。[Summary of the Invention] The resin supply device of the present invention includes a main hopper communicating with an extruder housing, first and second service hoppers communicating with the main hopper, and the first service hopper communicating with the main hopper.
an intake fan whose intake port communicates with the service hopper; a resin pallet that communicates with the first service hopper and accommodates resin pellets; and a resin pallet that is blown out when the resin is idle and is pulverized and supplied to the second service hopper. Starting and stopping of the crusher and the intake fan are automatically repeated to cause a predetermined amount of resin pellets to fall and be stored in the main hopper by alternating the negative pressure in the first service hopper and the atmospheric pressure. In the resin supply device, the first and second
a service hopper is installed mechanically separated from the main hopper, and the main hopper is installed mechanically separated from the extruder housing, and first and second A load cell is provided, and a table scale is provided for measuring the discharged resin to be supplied to the crusher, and the first and second
A conversion means is provided to digitize the measured output of the load cell and the table scale, and the cumulative value of the second load cell output at the time of starting product picking is W1 , and the cumulative value of the second load cell output at the time of stopping extrusion is determined.
W 2 is the output of the first load cell at the time of starting product picking, W 3 is the output of the first load cell at the time of stopping extrusion, W 4 is the cumulative output of the platform scale.
W B , W 1 − W 3 , that is, the idle amount is W A , and the CPU
It is characterized in that the amount of adhesion W D to the cable etc. is determined by the following formula W D = (W 2 - W 4 ) - W A + W B.
第1図と同一部分には同一符号を附した第2図
は本発明の一実施例を示す。本発明においては、
サービスホツパ3および9とメインホツパ2とは
機械的に切りはなされており、メインホツパ2と
ハウジング1も同様である。すなわち、それら二
者間はフレキシブルジヨイント等で連通されてい
る。さらに、メインホツパ2、サービスホツパ3
は、それぞれロードセル14,15を介して固定
部材上に支持されている。ロードセル14,1
5、粉砕機10の近傍に設置した台スケール16
の出力は、変換器17においてデジタル信号に変
換され、CPU18に送込まれる。
FIG. 2, in which the same parts as in FIG. 1 are given the same reference numerals, shows an embodiment of the present invention. In the present invention,
The service hoppers 3 and 9 and the main hopper 2 are mechanically separated, and the same applies to the main hopper 2 and the housing 1. That is, the two are communicated by a flexible joint or the like. In addition, main hopper 2, service hopper 3
are supported on a fixed member via load cells 14 and 15, respectively. Load cell 14,1
5. Platform scale 16 installed near the crusher 10
The output is converted into a digital signal by the converter 17 and sent to the CPU 18.
上記構成の本発明装置においては、樹脂ペレツ
トのメインホツパ2に対する供給は、第1図に示
した従来例と同様にして行われる。ただし、フア
ン8の起動時に、CPU18に作業開始指令Aが
入る。フアン8のタイマによる停止時に、ロード
セル15の出力すなわちサービスホツパ3内の樹
脂ペレツトの重量は、変換器17においてデジタ
ル信号に変換され、CPU18に送られる。サー
ビスホツパ3への吸引とメインホツパ2への落下
とが、自動的に繰返されることは前記と同様であ
るが、サービスタンク3内の樹脂ペレツト重量は
その都度CPU18に送られ、累計されて総供給
量が求められる。一方、メインホツパ2内のペレ
ツト重量、すなわちロードセル14の出力もデジ
タル化されて、CPU18に送られる。CPU18
はロードセル14の出力が設定値となつた時、樹
脂の供給を停止させる。 In the apparatus of the present invention having the above structure, resin pellets are supplied to the main hopper 2 in the same manner as in the conventional example shown in FIG. However, when the fan 8 is started, a work start command A is input to the CPU 18. When the fan 8 is stopped by the timer, the output of the load cell 15, that is, the weight of the resin pellets in the service hopper 3, is converted into a digital signal by the converter 17 and sent to the CPU 18. As mentioned above, the suction into the service hopper 3 and the dropping into the main hopper 2 are automatically repeated, but the weight of the resin pellets in the service tank 3 is sent to the CPU 18 each time, and the weight of the resin pellets is added up and totaled. is required. On the other hand, the pellet weight in the main hopper 2, ie, the output of the load cell 14, is also digitized and sent to the CPU 18. CPU18
stops the supply of resin when the output of the load cell 14 reaches the set value.
押出機が起動され樹脂ペレツトが減少し、その
山の表面が上部のレベル計12まで低下すると、
フアン8が起動されるのは、従来と同様である。
また、ペレツトの山の表面が下部のレベル計13
まで低下すると、警報が発せられることも同様で
ある。なお、念のため附言すれば、これらは
CPUとは別の他のシーケンスによつて行われる。 When the extruder is started and the resin pellets decrease and the surface of the pile drops to the level gauge 12 at the top,
The fan 8 is activated in the same way as in the conventional case.
Also, the surface of the pellet pile is at the bottom of the level meter 13.
Similarly, an alarm will be issued if the temperature drops to a certain level. By the way, just to be sure, these are
This is done by another sequence separate from the CPU.
なお、空ねり時に発生した屑は台スケール16
で計量され、その出力もデジタル化されて、台ス
ケール読込指令BによつてCPU18に送られ、
累積される。台スケールによる計量後、粉砕して
メインホツパ2に投入される。 In addition, the waste generated during dry kneading is on the platform scale 16.
The output is also digitized and sent to the CPU 18 by the platform scale reading command B.
Accumulated. After being weighed using a table scale, it is crushed and put into the main hopper 2.
空ねりが終了して、製品取り、すなわち導体等
への押出被覆を開始する時計尺を開始するが、こ
の時計尺器のカウンタはリセツトされる。このリ
セツト時のリセツト指令、すなわち計尺開始信号
CをCPUに取込み、その時点におけるロードセ
ル14の出力およびロードセル15の出力の累計
量を、CPUに記憶させる。 After the empty kneading process is completed, a clock measure is started to take out the product, that is, to start extrusion coating onto conductors, etc., but the counter of this clock measure is reset. The reset command at the time of this reset, that is, the measuring start signal C, is taken into the CPU, and the cumulative amount of the output of the load cell 14 and the output of the load cell 15 at that time is stored in the CPU.
押出機が停止すると、その停止信号DをCPU
18に取込み、その時点におけるロードセル14
の出力およびロードセル15の出力の累計量を求
める。 When the extruder stops, the stop signal D is sent to the CPU
Load cell 14 at that point
The cumulative output of the output of the load cell 15 and the output of the load cell 15 are determined.
前記の製品取り開始時のロードセル15の出力
の累計量をW1、押出停止時のそれをW2、製品取
り開始時のロードセル14の出力をW3、押出停
止時のそれをW4とすれば、
W1−W3=WA ただし、WAは空出量
WA−WB=WC ただし、WBは台スケール累計量
WCは屑量
(W2−W4)−WA+WB=WD
ただし、WDはケーブル附着量
のようにして、被覆された樹脂量を求めることが
できる。 Let W 1 be the cumulative output of the load cell 15 at the time of starting the product taking, W 2 be the cumulative output of the load cell 15 when the extrusion is stopped, W 3 be the output of the load cell 14 at the time of starting the product taking, and W 4 be the output when the extrusion is stopped. For example, W 1 − W 3 = W A However, W A is the empty amount W A − W B = W C However, W B is the cumulative amount on the platform scale W C is the amount of scrap (W 2 − W 4 ) − W A +W B = W D However, W D can be used as the cable adhesion amount to determine the coated resin amount.
上記から明らかなように、本発明によれば樹脂
ペレツトの供給量を正確に知ることができ、それ
からケーブル等への附着量をも求めることができ
るので、コスト管理、作業管理上有利である。
As is clear from the above, according to the present invention, the amount of resin pellets supplied can be accurately determined, and the amount attached to cables, etc. can also be determined from this, which is advantageous in terms of cost control and work management.
第1図は従来の供給装置の一例の模式図、第2
図は本発明一実施例の模式図である。
1……押出機ハウジング、2……メインホツ
パ、3……サービスホツパ、5……樹脂パレツ
ト、8……吸気フアン、9……サービスホツパ、
10……粉砕機、12,13……レベル計、1
4,15……ロードセル、16……台スケール、
17……変換器、18……CPU。
Figure 1 is a schematic diagram of an example of a conventional supply device;
The figure is a schematic diagram of one embodiment of the present invention. 1... Extruder housing, 2... Main hopper, 3... Service hopper, 5... Resin pallet, 8... Intake fan, 9... Service hopper,
10...Crusher, 12,13...Level meter, 1
4, 15...load cell, 16...scale,
17...Converter, 18...CPU.
Claims (1)
このメインホツパに連通する第1、第2のサービ
スホツパと、前記第1のサービスホツパに吸気口
を連通させた吸気フアンと、前記第1のサービス
ホツパに連通し樹脂ペレツトを収容する樹脂パレ
ツトと、空ねり時の空出の樹脂を粉砕して前記第
2のサービスホツパに供給する粉砕機と、前記吸
気フアンの起動、停止を自動的に繰返して前記第
1のサービスホツパ内の負圧と大気圧との交番に
よつて前記メインホツパに所定量の樹脂ペレツト
を落下、貯蔵させるようにした樹脂供給装置にお
いて、前記第1、第2のサービスホツパを前記メ
インホツパとは機械的に切り離して設置するとと
もに前記メインホツパを前記押出機ハウジングと
は機械的に切り離して設置し、前記メインホツ
パ、前記第1のサービスホツパの重量を測定する
第1、第2のロードセルを設け、さらに前記粉砕
機に供給される空出の樹脂を計量する台スケール
を設け、前記第1、第2のロードセルおよび前記
台スケールの測定出力をデジタル化する変換手段
を設け、製品取り開始時の前記第2のロードセル
出力の累積値をW1、押出停止時の前記第2のロ
ードセル出力の累積値をW2、前記第1のロード
セルの製品取り開始時の出力をW3、押出停止時
の前記第1のロードセル出力をW4、前記台スケ
ールの出力の累計量をWB、W1−W3すなわち空
出量をWAとして、CPUにより次式 WD=(W2−W4)−WA+WB によつてケーブル等への付着量WDを求めること
を特徴とする樹脂供給装置。[Claims] A main hopper communicating with the extruder housing;
A first and second service hopper communicating with the main hopper, an intake fan having an intake port communicating with the first service hopper, a resin pallet communicating with the first service hopper containing resin pellets, a pulverizer that pulverizes the discharged resin and supplies it to the second service hopper; and a pulverizer that automatically repeats starting and stopping of the intake fan to alternate between negative pressure and atmospheric pressure in the first service hopper. Accordingly, in the resin supply device which allows a predetermined amount of resin pellets to fall and be stored in the main hopper, the first and second service hoppers are installed mechanically separated from the main hopper, and the main hopper is connected to the extruder. A stand that is installed mechanically separate from the housing and that is provided with first and second load cells that measure the weight of the main hopper and the first service hopper, and further that weighs the empty resin to be supplied to the crusher. A scale is provided, and a conversion means is provided to digitize the measurement outputs of the first and second load cells and the platform scale, and the cumulative value of the output of the second load cell at the time of starting product taking is W 1 and the cumulative value of the output of the second load cell at the time of stopping extrusion. The cumulative value of the output of the second load cell is W 2 , the output of the first load cell at the time of starting product picking is W 3 , the output of the first load cell at the time of stopping extrusion is W 4 , and the cumulative value of the output of the platform scale Assuming that the amount is W B and W 1 − W 3 , that is, the empty amount is W A , the CPU calculates the adhesion amount W D to the cable etc. using the following formula W D = (W 2 − W 4 ) − W A + W B. A resin supply device characterized by the following.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58090748A JPS59215844A (en) | 1983-05-25 | 1983-05-25 | Resin feeder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58090748A JPS59215844A (en) | 1983-05-25 | 1983-05-25 | Resin feeder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59215844A JPS59215844A (en) | 1984-12-05 |
| JPH054208B2 true JPH054208B2 (en) | 1993-01-19 |
Family
ID=14007212
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58090748A Granted JPS59215844A (en) | 1983-05-25 | 1983-05-25 | Resin feeder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59215844A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61228926A (en) * | 1985-04-04 | 1986-10-13 | Yazaki Corp | Feeding device for material to extruder |
| JPH01118409A (en) * | 1987-11-02 | 1989-05-10 | Matsuji Nakagome | Continuously drying and feeding device of resin material |
| JPH02107426A (en) * | 1988-10-17 | 1990-04-19 | Shikoku Maruyasu Kk | Method and apparatus for supply of material to molding machine |
| JP2502429B2 (en) * | 1992-02-14 | 1996-05-29 | 株式会社カワタ | Measuring device for powder and granular material |
-
1983
- 1983-05-25 JP JP58090748A patent/JPS59215844A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59215844A (en) | 1984-12-05 |
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