JP2007015384A - Extrusion molding equipment of refuse for manufacturing coke raw material and method for manufacturing molding using the same - Google Patents

Extrusion molding equipment of refuse for manufacturing coke raw material and method for manufacturing molding using the same Download PDF

Info

Publication number
JP2007015384A
JP2007015384A JP2006199785A JP2006199785A JP2007015384A JP 2007015384 A JP2007015384 A JP 2007015384A JP 2006199785 A JP2006199785 A JP 2006199785A JP 2006199785 A JP2006199785 A JP 2006199785A JP 2007015384 A JP2007015384 A JP 2007015384A
Authority
JP
Japan
Prior art keywords
molded product
temperature
heater
molding
extrusion molding
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2006199785A
Other languages
Japanese (ja)
Inventor
Eiji Matsukuma
英治 松隈
Nobuyuki Mikata
信行 三方
Yasuhiko Mori
泰彦 森
Yoshihiro Harada
義弘 原田
Tetsuji Ibaraki
哲治 茨城
Motoki Ikeda
元樹 池田
Tsuneo Koseki
常雄 小関
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.)
Nippon Steel Corp
Nippon Steel Engineering Co Ltd
Nippon Steel Plant Designing Corp
Original Assignee
Nittetsu Plant Designing Corp
Nippon Steel Corp
Nippon Steel Engineering 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 Nittetsu Plant Designing Corp, Nippon Steel Corp, Nippon Steel Engineering Co Ltd filed Critical Nittetsu Plant Designing Corp
Priority to JP2006199785A priority Critical patent/JP2007015384A/en
Publication of JP2007015384A publication Critical patent/JP2007015384A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/80Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
    • B29C48/83Heating or cooling the cylinders
    • B29C48/832Heating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92009Measured parameter
    • B29C2948/92209Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92361Extrusion unit
    • B29C2948/9238Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/924Barrel or housing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Coke Industry (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for manufacturing a molding in an extrusion molding machine in which a molding can secure the quality used as a coke raw material even if the range of fluctuation of such as a composition, moisture or the like of refuse to be molded become large and economical and safe process automation is possible. <P>SOLUTION: The method for manufacturing a massive molding product 13 which can be used as a coke raw material comprises the steps of: feeding the crushed refuse mainly consisting of plastics into an extrusion molding machine 14; extruding from a nozzle 25 of a leading section in the state of heating to make a molding 38; and furthermore cutting the molding 38. The extrusion molding machine 14 is provided with a molding temperature sensor 29 which measures the molding temperature of the molding 38 and a heater which heats the refuse. When a measurement value t by the molding temperature sensor 29 exceeds a setting temperature ta, a specific volume of water is automatically sprayed to the loaded refuse, and further the heater is turned on/off by monitoring the molding temperature sensor 29 to maintain the processing temperature of the molding 38. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、例えば、コークス炉設備の石炭代替原料に利用できるように、分別された家庭ごみ等のプラスチック系一般廃棄物を成形して、コークス原料を製造する廃棄物の押出し成形設備及びこれを用いた成形品の製造方法に関する。 The present invention provides, for example, a waste extrusion molding facility for producing coke raw material by molding plastic general waste such as sorted household waste so that it can be used as a coal substitute raw material for a coke oven facility. The present invention relates to a method for producing a molded product used .

今日大量に生産されているプラスチックは、微生物によっても分解されず、また空気中、水中でも安定しており、さらに燃焼させると発熱量が大きく高熱を出すため、ごみ処理焼却炉を傷める等の問題を有している。そこで、例えば、分別された家庭ごみ等のプラスチック系一般廃棄物の処理として、ごみの減容化が図られており、ごみの減容化のために押出し成形機によってごみをペレット状の成形品に成形している。成形品の製造方法においては、例えば、圧縮梱包体のプラスチックを開梱、破砕、選別及び細破砕してから、細破砕されたプラスチックを定速回転のスクリュー式の押出し成形機に供給し、押出し成形機のスクリューの押出しによる圧縮、摩擦熱、プラスチック間の摩擦熱によって溶解し、ノズルを介して成形品を製造し、成形品を所定の長さに切断して塊状の成形製品を製造している。 Plastics that are produced in large quantities today are not decomposed by microorganisms, are stable in air and water, and generate a high heat when burned, causing problems such as damaging the incinerator. have. Therefore, for example, the volume of waste is reduced as a treatment of plastic waste such as sorted household waste, and the waste is reduced to pellets by an extrusion molding machine to reduce the volume of waste. It is molded into. In the method of manufacturing a molded product, for example, the plastic in a compressed package is unpacked, crushed, sorted, and crushed, and then the crushed plastic is supplied to a screw-type extrusion molding machine that rotates at a constant speed. It is melted by compression by the extrusion of the screw of the molding machine, frictional heat, frictional heat between plastics, manufactures a molded product through a nozzle, and cuts the molded product to a predetermined length to manufacture a massive molded product Yes.

しかしながら、前記従来の押出し成形機における成形品の製造方法においては、ごみの埋立処分容量の削減を目的としているため、成形製品の品質管理(サイズ、嵩比重、塊率等)は行われておらず、また、一定の品質管理をしようとして、廃棄物の含水量に応じて水分量を調整しようとしても、水分量を連続的に測定する手段がなかった。このため、例えば、廃棄物に含まれる水分量が少ないときには、過熱により処理温度が適正な成形可能温度以上に上昇してしまい、熱可塑性樹脂が過剰に溶融した状態でノズルから押出されるため、成形物を切断し難くなり、押出し後に装置の周辺に付着して固化してしまい、このため装置の故障の原因となっていた。一方、廃棄物に含まれる水分量が多いときには、処理温度が適正な成形可能温度まで上昇せず、この結果、成形製品に粉が多く発生して崩壊しやすくなったり、又はサイズ調整のための切断処理時に粉が多く発生するという問題があり、成形製品を埋め立てる場合には、大した問題とはならなかったが、成形製品をコークス原料として有効利用することが困難であった。なお、押出し成形機にはヒータが設けられており、ヒータは立ち上げ時(運転開始時)にプラスチックを溶融するためのみ使用するが、過加熱による発火を防止するために通常運転時には停止させている。 However, in the method of manufacturing a molded product in the conventional extruder, the quality control (size, bulk specific gravity, mass ratio, etc.) of the molded product is not performed because the purpose is to reduce the landfill disposal capacity of waste. In addition, there was no means for continuously measuring the moisture content even if the moisture content was adjusted according to the water content of the waste in order to perform a certain quality control. For this reason, for example, when the amount of water contained in the waste is small, the processing temperature rises to an appropriate moldable temperature or more due to overheating, and the thermoplastic resin is extruded from the nozzle in an excessively melted state. It becomes difficult to cut the molded product, and it adheres to the periphery of the apparatus after extrusion and solidifies, which causes failure of the apparatus. On the other hand, when the amount of water contained in the waste is large, the processing temperature does not rise to an appropriate moldable temperature, and as a result, a lot of powder is generated in the molded product and it tends to collapse, or for size adjustment. There is a problem that a large amount of powder is generated during the cutting treatment, and when the molded product is reclaimed, it has not been a major problem, but it is difficult to effectively use the molded product as a coke raw material. The extruder is equipped with a heater, which is used only to melt the plastic at start-up (at the start of operation), but is stopped during normal operation to prevent overheating. Yes.

特開2002−178388号公報JP 2002-178388 A

上述の課題を解決するために、出願人は特許文献1(特願2000−377825)において、処理温度が適正な成形可能温度を維持でき、これによってコークス原料として有効利用できる成形製品を製造できるようにするため、押出し成形機に投入された廃棄物に所定量の注水を自動的に行うことを特徴とする押出し成形機における成形品の製造方法を提案した。しかしながら、この成形品の製造方法においては、ヒータは立ち上げ時のみ使用しており、成形品の温度を注水のみで制御するので、成形されるプラスチックの組成や、水分量の変動が大きい場合に、制御可能な温度範囲や応答性に限界があり、特に、水分の多いプラスチックを成形する場合には、注水量を0(零)にしても成形品の温度が所定の温度に達せず、コークス原料として満足できる性能の成形製品を製造することが出来ない恐れがあった。また、スクリューの押出しによる圧縮、摩擦熱、プラスチック間の摩擦熱によってのみ成形可能温度を維持する方法であるため、電気エネルギーを機械エネルギー、さらに熱エネルギーに変換して成形する方法であり、より経済的な成形方法が望まれた。
本発明はかかる事情に鑑みてなされたもので、成形する廃棄物の成分、水分等の変動幅が大きくなっても、成形製品がコークス原料として使用可能な品質を確保でき、しかも経済的でかつ安全に、処理の自動化が可能な廃棄物の押出し成形設備及びこれを用いた成形品の製造方法を提供することを目的とする。
In order to solve the above-mentioned problems, the applicant can maintain a molding temperature at an appropriate processing temperature in Patent Document 1 (Japanese Patent Application No. 2000-377825), thereby producing a molded product that can be effectively used as a coke raw material. In order to achieve this, a method for producing a molded product in an extrusion molding machine has been proposed, in which a predetermined amount of water is automatically injected into the waste put into the extrusion molding machine. However, in this method of manufacturing a molded product, the heater is used only at startup, and the temperature of the molded product is controlled only by water injection. , There is a limit to the controllable temperature range and responsiveness, especially when molding plastics with a lot of moisture, even if the amount of water injection is 0 (zero), the temperature of the molded product does not reach the predetermined temperature, coke There was a fear that a molded product with satisfactory performance as a raw material could not be produced. In addition, it is a method that maintains the moldable temperature only by compression by screw extrusion, frictional heat, and frictional heat between plastics. Therefore, it is a method that converts electrical energy into mechanical energy and then heat energy, and is more economical. An ideal molding method was desired.
The present invention has been made in view of such circumstances, and even if the fluctuation range of waste components, moisture, etc. to be molded increases, the quality of the molded product that can be used as a coke raw material can be ensured, and it is economical. An object of the present invention is to provide a waste extrusion molding facility capable of safely processing and a method for producing a molded product using the same.

前記目的に沿う本発明に係るコークス原料として使用可能な塊状の成形製品を製造する廃棄物の押出し成形設備は、破砕されたプラスチック主体の廃棄物投入される開口部を上部に有するケーシングと、
前記ケーシングの下流端部に設けられた加熱プレート及び該加熱プレートの下流側に連接されたダイスプレートと、
前記ケーシングの内部に水平配置され、回転して前記開口部から供給された前記廃棄物中の熱可塑性樹脂を半溶融しながら前記ダイスプレートの孔に押し込むスクリューと、
前記ダイスプレートの下流側に設けられて該ダイスプレートの孔に連通する押出口をそれぞれ有するノズルと、
前記ダイスプレートの下流側に設けられ、前記ノズルから押出された成形品を所定長さごとに切断する回転刃と、
前記開口部に向けて注水可能な噴出ノズル及び該噴出ノズルからの注水量の調整を行う流量調整弁と、
前記ノズルに設けられて前記成形品の温度を測定する成形品温度センサーによる測定値tと、予め入力されている前記成形品の設定温度t a とを比較して所要の注水量を演算し、前記流量調整弁を開閉して前記成形品の成形温度が前記設定温度t a になるように制御する温度指示調節計と、
前記加熱プレートに埋め込まれ前記ダイスプレートを加熱するヒータ及び該加熱プレートの温度を測定する温度センサーを備え、
前記温度センサーの測定値Tが前記加熱プレートの上限温度T H を検知すると前記ヒータの電源が切れ、更に、前記成形品温度センサーの測定値tを前記ヒータの入切の設定温度t b (例えば、成形物の設定温度t a より低い温度である場合、成形物の設定温度t a と同一である場合、又は成形物の設定温度t a より高い温度である場合)と比較し該設定温度t b を境として前記ヒータを入切している。
Extrusion equipment waste producing shaped products available bulk as a coke raw material according to the present invention along the object, a casing having an opening in the upper waste of crushed plastic principal is turned on,
A heating plate provided at the downstream end of the casing and a die plate connected to the downstream side of the heating plate;
A screw that is horizontally disposed inside the casing, rotates and pushes into the hole of the die plate while semi-melting the thermoplastic resin in the waste supplied from the opening,
Nozzles provided on the downstream side of the die plate and each having an extrusion port communicating with a hole of the die plate;
A rotary blade that is provided on the downstream side of the die plate, and that cuts the molded product extruded from the nozzle every predetermined length;
A jet nozzle capable of pouring water toward the opening, and a flow rate adjusting valve for adjusting the amount of water poured from the jet nozzle;
Comparing a measured value t by a molded product temperature sensor that is provided in the nozzle and measures the temperature of the molded product and a preset temperature t a of the molded product that is input in advance, a required water injection amount is calculated, and temperature indicating controllers that control such molding temperature of the molded product becomes the set temperature t a to open and close the flow control valve,
A heater embedded in the heating plate for heating the die plate and a temperature sensor for measuring the temperature of the heating plate;
When the measured value T of the temperature sensor detects the upper limit temperature T H of the heating plate, the heater is turned off, and the measured value t of the molded product temperature sensor is set to the set temperature t b (for example, the heater on / off). If a temperature lower than the set temperature t a of the molding, when it is equal to the set temperature t a of the molding, or molding the set temperature t when the temperature is higher than a) compared with the set temperature t The heater is turned on and off at b .

廃棄物中に含まれる熱可塑性樹脂を溶融、固化させるとき、熱可塑性樹脂の組成は一定ではなく、例えば、ポリエチレン、ポリスチレン等の材料の構成の違いや、プラスチックの厚さの構成の違い等、また、含まれる水分量も一定にならないのが通常である。さらに、例えば、廃棄物中に含まれている水分量が多い場合には、スクリューと廃棄物との摩擦熱が不足し、廃棄物を固めることができず粉状の成形品となる。逆に、廃棄物中に含まれている水分量が少ないときに押出し成形する場合には、スクリューと廃棄物との摩擦熱が過剰となり、適正な成形温度範囲の上限値を超えてしまうことがある。上限値を超えた状態で成形を行ったときには、熱可塑性樹脂が半固形状物又は液状物の状態で押出し成形機から排出されるため、所定の形状を確保することが困難で、また、成形品同士が付着してしまうこともある。このような成形品はコークス原料のように品質を重視する製品として使用することができない。しかしながら、本発明においては、成形品の処理温度が設定値になるように廃棄物に注水制御を行うと共に、成形品の処理温度を監視しながらヒータの入切を行なうようにしているので、成形品の成形温度を維持することができ、適正温度範囲内で成形を行うので、製品の品質を確保することができる。また、温度に応じて自動的に散水を行うと共に、ヒータの入切を自動的に行うので、操作者の勘に頼ることなく、押出し成形機に投入される廃棄物の含有水分等の条件に応じて成形条件を確実且つ容易に制御することができる。 When the thermoplastic resin contained in the waste is melted and solidified, the composition of the thermoplastic resin is not constant, for example, the difference in the composition of materials such as polyethylene and polystyrene, the difference in the thickness of the plastic, etc. Further, the amount of water contained is usually not constant. Furthermore, for example, when the amount of water contained in the waste is large, the frictional heat between the screw and the waste is insufficient, and the waste cannot be hardened, resulting in a powdery molded product. Conversely, when extrusion molding is performed when the amount of water contained in the waste is small, the frictional heat between the screw and the waste becomes excessive, which may exceed the upper limit of the proper molding temperature range. is there. When molding is performed in a state exceeding the upper limit, the thermoplastic resin is discharged from the extrusion molding machine in a semi-solid or liquid state, so that it is difficult to secure a predetermined shape, and molding Products may stick to each other. Such a molded product cannot be used as a product in which quality is important like a coke raw material. However, in the present invention, water injection is controlled so that the processing temperature of the molded product becomes a set value, and the heater is turned on and off while monitoring the processing temperature of the molded product. Since the molding temperature of the product can be maintained and molding is performed within an appropriate temperature range, the quality of the product can be ensured. In addition, water is automatically sprinkled according to the temperature and the heater is automatically turned on and off, so that the moisture content of the waste put into the extruder can be adjusted without depending on the operator's intuition. Accordingly, the molding conditions can be reliably and easily controlled.

本発明において、成形品温度センサーを監視しながらヒータの入切を行う制御は、成形品の設定温度とヒータの入切の温度とに差を持たせて行うこともできる。これによって、ヒータの使用割合を自由に変えることができ、例えば、成形品の設定温度よりヒータの入切の温度を高く設定すると、ヒータの使用割合が高い運転とすることができる。本発明において、ノズルはダイスプレートに設けられ、成形品温度センサーは、成形品と直接又は間接的に接触するように、ノズルに設けられ、成形品の処理温度は、100〜140℃の範囲にあるように構成することもできる。これによって、成形品温度センサーが成形品と直接接触する条件では、より正確な成形品の温度の測定ができる。一方、成形品温度センサーが成形品と間接的に接触する条件では、溶融状態にある熱可塑性樹脂、又は押出し後の成形品が移動して、安定して成形品の温度を測定することができない場合でも、成形品の外形を形成するノズルの温度を測定し、成形品の温度を間接的に測定することができ、また、移動する成形品の代わりに固定されたノズルの温度を測定するので、安定して温度を測定することができる。ここで、成形品の処理温度を100〜140℃の範囲にしている理由は、処理温度が100℃未満であれば成形品の品質が低下するためであり、一方、処理温度が140℃を超えると成形品が形成されず、また発火の恐れがあり、危険性が増すためである。 In the present invention, the control for turning on and off the heater while monitoring the molded product temperature sensor can be performed by making a difference between the set temperature of the molded product and the temperature of turning on and off the heater. Accordingly, the usage rate of the heater can be freely changed. For example, when the heater turning-on / off temperature is set higher than the set temperature of the molded product, an operation with a high heater usage rate can be achieved. In the present invention, the nozzle is provided on the die plate, the molded product temperature sensor is provided on the nozzle so as to be in direct or indirect contact with the molded product, and the processing temperature of the molded product is in the range of 100 to 140 ° C. It can also be configured. Thus, the temperature of the molded product can be measured more accurately under the condition that the molded product temperature sensor is in direct contact with the molded product. On the other hand, when the molded product temperature sensor is in indirect contact with the molded product, the molten thermoplastic resin or the molded product after extrusion cannot move and the temperature of the molded product cannot be measured stably. Even when measuring the temperature of the nozzle that forms the outer shape of the molded product, the temperature of the molded product can be measured indirectly, and the temperature of the fixed nozzle is measured instead of the moving molded product. Can measure temperature stably. Here, the reason why the processing temperature of the molded product is in the range of 100 to 140 ° C. is that if the processing temperature is less than 100 ° C., the quality of the molded product is deteriorated, while the processing temperature exceeds 140 ° C. This is because the molded product is not formed, and there is a risk of fire, increasing the danger.

本発明において、ヒータは、ダイスプレートに連接された加熱プレートに埋め込まれ、加熱プレートには、温度センサーがあって、温度センサーにより測定された加熱プレートの温度が異常温度になるとヒータの電源が切れる。これによって、加熱プレートを介してノズルの付いたダイスプレートを加熱することができ、また、加熱プレートが異常温度になるとヒータの電源を切って加熱プレートの過加熱を防止することができる。本発明において、ヒータの入切は、成形温度(成形物の設定温度)より高い温度で行うこともできる。これによって、ヒータの使用割合が大きくなる。 In the present invention, the heater is embedded in a heating plate connected to the die plate, and the heating plate has a temperature sensor. When the temperature of the heating plate measured by the temperature sensor becomes an abnormal temperature, the heater is turned off. . As a result, the die plate with the nozzle can be heated via the heating plate, and when the heating plate reaches an abnormal temperature, the heater can be turned off to prevent overheating of the heating plate. In the present invention, the heater can be turned on and off at a temperature higher than the molding temperature (set temperature of the molded product) . This increases the usage rate of the heater.

請求項1、2記載のコークス原料として使用可能な塊状の成形製品を製造する廃棄物の押出し成形設備及び請求項3、4に記載の同設備を用いた成形品の製造方法は、成形品の成形温度を注水量による制御と同時に、ヒータの入切による制御によって行うことができるので、成形品の処理温度を維持することができ、適正温度範囲内で成形を行え、製品の品質を確保することができる。また、成形品の温度に応じて自動的に散水を行うと共に、ヒータの入切を自動的に行うので、投入される破砕物の含有水分、成分等の変動に応じて、確実で容易に、且つ応答性の高い制御が行える。さらに、スクリューによる電気エネルギーを、機械品(ギア等)を介して熱エネルギーに変換するというような効率の悪い割合が小さくなると共に、ヒータにより電気エネルギーを直接、熱エネルギーに効率よく変換することができるので、経済的な運転ができる。 The waste extrusion molding equipment for producing a lump-shaped molded product that can be used as a coke raw material according to claims 1 and 2 and the method for producing a molded product using the equipment according to claims 3 and 4 are: Since the molding temperature can be controlled by controlling the amount of water injected and by turning the heater on and off, the processing temperature of the molded product can be maintained, molding can be performed within the appropriate temperature range, and product quality can be ensured. be able to. In addition, watering is automatically performed according to the temperature of the molded product, and the heater is automatically turned on and off, so according to fluctuations in the moisture content, components, etc. of the crushed material to be charged, Moreover, highly responsive control can be performed. Furthermore, the inefficient ratio of converting electrical energy from the screw into thermal energy via a mechanical product (gear, etc.) is reduced, and the electrical energy can be directly and efficiently converted into thermal energy by the heater. Because you can, you can drive economically.

加熱プレートを介してノズルの付いたダイスプレートを加熱することができるので、摩耗して取り替える必要のあるノズルの付いたダイスプレートのみを、ヒータに関係なく交換することができる。
そして、ヒータの使用割合を自由に変えることができ、例えば、成形品の設定温度よりヒータの入切の温度を高く設定すると、ヒータの使用割合が高い運転とすることができるので、さらに経済的な運転ができる。また、加熱プレートが異常温度になるとヒータの電源を切って成形品の処理温度が高過ぎないようにできるので、発火の恐れが無くなる。
請求項3記載の成形品の製造方法においては、成形品の処理温度を100〜140℃の範囲にしているので、成形品の品質が低下することがなく、しかも、発火の危険性も無くなる。
Since the die plate with the nozzle can be heated through the heating plate, only the die plate with the nozzle that needs to be worn and replaced can be replaced regardless of the heater.
The heater usage ratio can be changed freely. For example, if the heater on / off temperature is set higher than the set temperature of the molded product, the heater usage ratio can be set to be higher, so that the operation is more economical. Driving. Further, when the heating plate reaches an abnormal temperature, the heater can be turned off so that the processing temperature of the molded product is not too high, thereby eliminating the risk of ignition.
In the method for manufacturing a molded product according to claim 3, since the processing temperature of the molded product is set in the range of 100 to 140 ° C., the quality of the molded product is not deteriorated and the risk of ignition is eliminated.

請求項記載の成形品の製造方法においては、ヒータの使用割合が大きくなるので、ヒータによる熱エネルギーの変換割合が大きくなり、より経済的となる。 In the method for producing a molded product according to claim 4 , since the heater usage rate is increased, the rate of conversion of heat energy by the heater is increased, which is more economical.

続いて、添付した図面を参照しつつ、本発明を具体化した実施の形態について説明し、本発明の理解に供する。図1は本発明の一実施の形態に係る押出し成形機における成形品の製造方法の概略説明図、図2は同押出し成形機における成形品の製造方法を適用する廃棄物の押出し成形設備の構成図、図3は押出し成形機の押出部の詳細断面図である。
図1及び図2に示すように、本発明の一実施の形態に係る押出し成形機における成形品の製造方法を適用する廃棄物の押出し成形設備10は、破砕されたプラスチック主体の廃棄物を搬送する供給コンベヤ11と、供給コンベヤ11の搬送端部の下方に配置され、ホッパー機能を有する定量供給機12と、定量供給機12から供給される廃棄物を、回転刃37により切断してコークス原料として使用可能な塊状の成形製品13にする前の成形品38に製造するための押出し成形機14とを有している。以下、図を参照しながら詳しく説明する。
Next, embodiments of the present invention will be described with reference to the accompanying drawings to provide an understanding of the present invention. FIG. 1 is a schematic explanatory view of a method for producing a molded product in an extrusion molding machine according to an embodiment of the present invention, and FIG. 2 is a configuration of a waste extrusion equipment to which the method for producing the molded product in the extrusion molding machine is applied. FIG. 3 and FIG. 3 are detailed sectional views of the extrusion portion of the extrusion molding machine.
As shown in FIGS. 1 and 2, a waste extrusion molding apparatus 10 to which a manufacturing method of a molded article in an extrusion molding machine according to an embodiment of the present invention applies a crushed plastic-based waste. The coke raw material is cut by the rotary blade 37 by the rotating blade 37, the feed conveyor 11, the fixed quantity feeder 12 disposed below the conveying end of the feed conveyor 11, and having a hopper function. And an extrusion molding machine 14 for producing a molded product 38 before being formed into a massive molded product 13 that can be used. Hereinafter, it will be described in detail with reference to the drawings.

図2に示すように、別途破砕されたプラスチック主体の廃棄物は供給コンベヤ11により定量供給機12に搬送される。定量供給機12は、平断面積が下方に沿って小さく形成されたホッパー15と、ホッパー15の底部に水平に配置されたスクリューフィーダ16と、ホッパー15内の上部に取付けられたブリッジブレーカー17とを備えている。ブリッジブレーカー17は、スクリューフィーダ16の軸心と平行にホッパー15の内側の両側壁に架け渡されており、滞留した廃棄物を掻き落とすもので、例えば、モータによって所定速度で回転する回転軸に複数の掻き取りアームを取付けた構造のものを使用している。かかる構成によって、供給コンベヤ11からホッパー15へ投入された廃棄物は、ブリッジブレーカー17によりブリッジを形成することなく、スクリューフィーダ16によって安定的に移送され、定量供給機12の下方に配置された押出し成形機14に向けて一定量ずつ連続的に送り出される。 As shown in FIG. 2, the waste mainly composed of plastic that has been separately crushed is transported to a quantitative feeder 12 by a supply conveyor 11. The fixed-quantity feeder 12 includes a hopper 15 having a flat cross-sectional area that is made smaller along the lower side, a screw feeder 16 that is disposed horizontally at the bottom of the hopper 15, and a bridge breaker 17 that is attached to the top of the hopper 15. It has. The bridge breaker 17 is spanned on both side walls inside the hopper 15 in parallel with the axis of the screw feeder 16 and scrapes off the accumulated waste. For example, the bridge breaker 17 is a rotating shaft that rotates at a predetermined speed by a motor. A structure with a plurality of scraping arms attached is used. With this configuration, the waste thrown into the hopper 15 from the supply conveyor 11 is stably transferred by the screw feeder 16 without forming a bridge by the bridge breaker 17, and the extrusion disposed below the metering feeder 12. A certain amount is continuously sent out toward the molding machine 14.

図2に示すように、押出し成形機14のケーシング18の上部には、廃棄物を投入可能な開口部19が形成され、ケーシング18の内部には、スクリューフィーダ20の一対のスクリュー21が軸心を平行にしてそれぞれ水平に配置されている。また、図3にも詳細に示すように、一対のスクリュー21の軸方向のケーシング18の下流側端部には、加熱プレート22及び加熱プレート22の下流側に連接されたダイスプレート23が設けられている。ダイスプレート23の下流側には廃棄物の流れ方向に貫通した押出口24がそれぞれ形成されたノズル25が、一対のスクリュー21の軸心を中心とする周方向に多数設けられている。ノズル25は、一例として、孔径は25〜50mmである。図3に詳細に示すように、ダイスプレート23にはノズル25の押出口24に連通する孔26が形成されている。加熱プレート22及びケーシング18の下流側端部の内側には、耐摩耗性を備えた交換可能なライナー27、28が設けられている。図2に示すように、成形品温度センサーの一例である熱電対29がノズル25に、複数箇所に設けられており、成形品38の成形温度を測定することができる。 As shown in FIG. 2, an opening 19 through which waste can be thrown is formed in the upper part of the casing 18 of the extrusion molding machine 14, and a pair of screws 21 of a screw feeder 20 are axially centered inside the casing 18. Are parallel to each other. As also shown in detail in FIG. 3, the downstream end of the axial casing 18 of the pair of screws 21 is provided with a heating plate 22 and a die plate 23 connected to the downstream side of the heating plate 22. ing. On the downstream side of the die plate 23, a number of nozzles 25 each having an extrusion port 24 penetrating in the waste flow direction are formed in the circumferential direction around the axis of the pair of screws 21. As an example, the nozzle 25 has a hole diameter of 25 to 50 mm. As shown in detail in FIG. 3, a hole 26 communicating with the extrusion port 24 of the nozzle 25 is formed in the die plate 23. Inside the downstream end of the heating plate 22 and the casing 18, replaceable liners 27 and 28 having wear resistance are provided. As shown in FIG. 2, thermocouples 29 as an example of a molded product temperature sensor are provided in the nozzle 25 at a plurality of locations, and the molding temperature of the molded product 38 can be measured.

図3に詳細に示すように、ダイスプレート23にボルト等により取り外し可能に連接された加熱プレート22には、主としてダイスプレート23を加熱するヒータを構成する複数のヒータエレメント31が埋め込まれて取付けられている。また、加熱プレート22に埋め込まれた温度センサーの一例である熱電対30により加熱プレート22の温度を測定することができる。通常運転時、押出し成形機14の開口部19から投入された廃棄物中のプラスチックに含まれる熱可塑性樹脂は、一対のスクリュー21の回転、圧縮等による摩擦熱と、成形品38の成形温度を制御するために必要に応じて使用するヒータによる加熱によって溶融される。また、図1に示すように、熱電対29による成形品38の成形温度(成形品温度)の測定値tと、予め制御盤に入力されている設定値(ヒータの入・切の設定温度tb)とを比較してヒータの入切を自動制御している。即ち、t<tbでは、ヒータを「入」とし、t≧tbでは、ヒータを「切」としている。更に、加熱プレート22には、過熱防止用としても機能する熱電対30が設けられており、熱電対30によって加熱プレート22が異常温度(加熱プレート22の上限温度TH)を検出すると、ヒータの電源が自動的に切れるように制御している。 As shown in detail in FIG. 3, a plurality of heater elements 31 mainly constituting a heater for heating the die plate 23 are embedded and attached to the heating plate 22 detachably connected to the die plate 23 with bolts or the like. ing. Further, the temperature of the heating plate 22 can be measured by a thermocouple 30 which is an example of a temperature sensor embedded in the heating plate 22. During normal operation, the thermoplastic resin contained in the plastic in the waste put in from the opening 19 of the extrusion molding machine 14 generates frictional heat due to the rotation and compression of the pair of screws 21 and the molding temperature of the molded product 38. It is melted by heating with a heater that is used as needed for control. Further, as shown in FIG. 1, a measured value t of the molding temperature (molded product temperature) of the molded product 38 by the thermocouple 29, and a preset value (preset temperature t for turning on / off the heater) input to the control panel. Compared with b ), heater on / off control is automatically controlled. That is, when t <t b , the heater is “ON”, and when t ≧ t b , the heater is “OFF”. Further, the heating plate 22 is provided with a thermocouple 30 that also functions to prevent overheating. When the heating plate 22 detects an abnormal temperature (the upper limit temperature T H of the heating plate 22) by the thermocouple 30, The power is controlled to turn off automatically.

図2に示すように、押出し成形機14の上方には、開口部19に向けて所定量の注水が可能な噴出ノズル32が設けられている。噴出ノズル32からの注水量の調整を行う流量調整弁33と、ノズル25に設けられた熱電対29は、温度指示調節計(TIC)34に電気配線を介してそれぞれ接続されている。図1に示すように、温度指示調節計34は、PID制御機能を有しており、熱電対29による成形品38の成形温度の測定値tと、予め制御盤に入力されている設定値(成形温度の設定値ta)とを比較して所要の注水量を演算し、注水量調節計(FIC)35を介し流量調整弁33を開閉させ、成形品38の成形温度(処理温度)が設定値(設定温度)taとなるような注水所要量を供給するように制御している。 As shown in FIG. 2, an ejection nozzle 32 capable of pouring a predetermined amount of water toward the opening 19 is provided above the extrusion molding machine 14. A flow rate adjustment valve 33 that adjusts the amount of water injected from the ejection nozzle 32 and a thermocouple 29 provided in the nozzle 25 are connected to a temperature indicating controller (TIC) 34 via electric wiring. As shown in FIG. 1, the temperature indicating controller 34 has a PID control function, and a measured value t of the molding temperature of the molded product 38 by the thermocouple 29 and a preset value ( The required water injection amount is calculated by comparing with the molding temperature set value t a ), the flow rate adjusting valve 33 is opened and closed via the water injection amount controller (FIC) 35, and the molding temperature (processing temperature) of the molded product 38 is determined. It is controlled so as to supply the set value (set temperature) becomes t a such water injection requirements.

図2に示すように、押出し成形機14のダイスプレート23の下流側には、モータ36に接続された回転刃37が設けられ、ノズル25から押出された成形品38は所定長さごとに切断されて成形製品13となり、回転刃37の下方に落下し、集積されて次工程に搬送される。かかる構成によって、押出し成形機14のノズル25から押し出された成形品38を所定形状の成形製品13に効率よく製造することができる。 As shown in FIG. 2, a rotary blade 37 connected to a motor 36 is provided on the downstream side of the die plate 23 of the extrusion molding machine 14, and a molded product 38 extruded from the nozzle 25 is cut at predetermined lengths. As a result, the molded product 13 is dropped below the rotary blade 37, collected, and conveyed to the next process. With this configuration, the molded product 38 extruded from the nozzle 25 of the extrusion molding machine 14 can be efficiently manufactured into the molded product 13 having a predetermined shape.

次に、押出し成形機14を含む廃棄物の押出し成形設備10を適用した本発明の一実施の形態に係る押出し成形機における成形品の製造方法の手順について、図を参照して説明する。
(1)まず、図2及び図3に示すように、多数のヒータエレメント31に電流を流してヒータを入りにし、加熱プレート22及び加熱プレート22を介してダイスプレート23が加熱される。
(2)図1及び図2に示すように、加熱プレート22が所定の温度に達すると、定量供給機12のスクリューフィーダ16が所定速度で回転し、プラスチック主体の破砕物が押出し成形機14に連続的に供給される。供給された破砕物中のプラスチックに含まれる熱可塑性樹脂は、加熱プレート22及びダイスプレート23からの供給熱と、スクリュー21の回転、圧縮等による摩擦熱とによって、半溶融されながら、ダイスプレート23の孔26に押し込まれる。
Next, a procedure of a method for manufacturing a molded product in the extrusion molding machine according to the embodiment of the present invention to which the waste extrusion molding equipment 10 including the extrusion molding machine 14 is applied will be described with reference to the drawings.
(1) First, as shown in FIGS. 2 and 3, current is passed through a number of heater elements 31 to turn on the heaters, and the die plate 23 is heated via the heating plate 22 and the heating plate 22.
(2) As shown in FIGS. 1 and 2, when the heating plate 22 reaches a predetermined temperature, the screw feeder 16 of the metering feeder 12 rotates at a predetermined speed, and the plastic-based crushed material is transferred to the extrusion molding machine 14. Continuously supplied. The thermoplastic resin contained in the plastic in the supplied crushed material is semi-molten by the supply heat from the heating plate 22 and the die plate 23 and the frictional heat due to the rotation, compression, etc. of the screw 21, and the die plate 23. It is pushed into the hole 26.

(3)図1及び図2に示すように、成形品38の成形温度が予め設定した設定温度になるように、押出し成形機14のスクリューフィーダ20に投入された破砕物には、温度指示調節計34による自動制御によって噴出ノズル32からの水分添加が制御されると共に、ヒータの入切が制御される。
(4)適正な成形温度に制御されて先部のノズル25から押し出された成形品38は、回転刃37により所定長さの成形製品13に切断される。
(5)成形製品13はコークス原料として使用可能な処理を行うために次工程に送られる。
(3) As shown in FIG. 1 and FIG. 2, temperature indication adjustment is performed on the crushed material introduced into the screw feeder 20 of the extrusion molding machine 14 so that the molding temperature of the molded product 38 becomes a preset temperature. The automatic addition by the meter 34 controls the addition of moisture from the ejection nozzle 32 and the heater on / off.
(4) The molded product 38 that is controlled to an appropriate molding temperature and is extruded from the nozzle 25 at the tip is cut into a molded product 13 having a predetermined length by the rotary blade 37.
(5) The molded product 13 is sent to the next step in order to perform a process that can be used as a coke raw material.

前記(3)の工程における温度指示調節計34による自動制御及びヒータの入切制御による成形品38の処理温度の制御について、図1及び図2を参照して、詳しく説明する。制御盤には、以下の温度、即ち、目標とする成形品の成形温度ta、ヒータ入切の設定温度tb、及び加熱プレート22の上限温度THを予め入力しておく。ここで、説明を簡略にするため、ta=tbとして説明する。 The control of the processing temperature of the molded product 38 by the automatic control by the temperature indicating controller 34 and the heater on / off control in the step (3) will be described in detail with reference to FIGS. The control panel, below the temperature, that is, keep the input molding temperature of the molded article as a target t a, the set temperature t b of the heater on-off, and the maximum temperature T H of the heating plate 22 in advance. Here, in order to simplify the description, it is assumed that t a = t b .

温度指示調節計34は、熱電対29を介して測定された成形品38の温度の測定値tと、予め入力されている設定温度ta(目標とする成形品の成形温度)とを比較して所要の注水量を演算し、注水量調節計35を介してPID制御により流量調整弁33を開閉させ、これによって、成形品38の成形温度が設定温度taとなるように制御している。これと同時に、成形品38の測定値tをヒータ入切の設定温度tbと比較してヒータの入・切(ON/OFF)制御を行う。即ち、測定値tが設定温度tb未満では、ヒータは常に入とし、一方、測定値tが設定温度tb以上では、ヒータは常に切とする。このように成形過程においてヒータによって熱を与えることにより、これまで成形温度を高くしないと成形できないような組成の破砕物や、水分量の多い破砕物に対しても所定の品質の成形品を自動で製造することが可能となる。また、モータ及び減速機を介して回転するスクリュー21とダイスプレート23の摩擦熱により破砕物に熱を与えるだけではなく、電気エネルギーをヒータの電熱線により直接破砕物に与えることにより、より経済性の高い自動運転が可能となる。ヒータの入の状態が継続しており、しかも加熱プレート22に取付けた温度センサーである熱電対30を介して測定した加熱プレート22の測定値Tが加熱プレート22の上限温度THを超えれば、ヒータを切とする。また、ヒータは、成形品38の温度が設定温度taに達しない場合でも、上限温度THを超えれば、自動的に切となる。これにより、加熱プレート22やダイスプレート23が異常な高温になることを防ぎ、安全な運転が可能となる。 The temperature indicating controller 34 compares the measured value t of the temperature of the molded product 38 measured through the thermocouple 29 with a preset temperature t a (target molding temperature of the molded product). Te calculates the required injection amount, via the water injection amount adjusting meter 35 is opened and closed the flow control valve 33 by PID control, thereby, it is controlled so that the molding temperature of the molded product 38 becomes the set temperature t a . At the same time, the measured value t of the molded product 38 is compared with the heater on / off set temperature t b to perform heater on / off (ON / OFF) control. That is, it is less than the measured value t is set temperature t b, the heater is always ON cities, whereas, in the measurement value t set temperature t b or more, the heater is always a switching. In this way, by applying heat with a heater during the molding process, it is possible to automatically produce molded products of a predetermined quality even for crushed materials with a composition that cannot be molded unless the molding temperature is raised, and crushed materials with a high water content. Can be manufactured. Further, not only heat is applied to the crushed material by the frictional heat of the screw 21 and the die plate 23 rotating via the motor and the speed reducer, but also electric energy is directly applied to the crushed material by the heating wire of the heater. High automatic operation is possible. And continuing the ON state of the heater, moreover if the measured value T of the heating plate 22 was measured via a thermocouple 30 is a temperature sensor attached to the heating plate 22 exceeds the upper limit temperature T H of the heating plate 22, Turn off the heater. The heater, even if the temperature of the molded product 38 does not reach the set temperature t a, if it exceeds the upper limit temperature T H, the automatic switching. As a result, the heating plate 22 and the die plate 23 are prevented from becoming abnormally high temperature, and safe operation is possible.

上述のtb=taの条件においては、ヒータは成形温度taを境として入・切を繰り返すことになるが、tb>taとした場合には、ヒータは成形温度taよりやや高い温度で入・切を繰り返すことになる。例えば、ta=120℃、tb=122℃とすると、測定値tが122℃になるまでヒータは「入」状態であり、ヒータの使用割合が大きくなる。一方、tb<taとした場合には、ヒータは成形温度taより低い温度で入・切を繰り返すことになり、ヒータの使用割合が小さくなる。このような制御を行うことで、水分が多い傾向の破砕物の場合は、ヒータの使用率を上げて(ヒータによる加熱を重視した運転)成形品の品質を確保し、水分が少ない傾向の破砕物の場合は、ヒータの使用率を下げた(注水による冷却を重視した運転)経済的な運転となり、破砕物の組成に応じて適切な運転が可能となる。 In terms of the above t b = t a, but the heater will be repeated ON-OFF as a boundary the molding temperature t a, when a t b> t a, the heater is slightly than the molding temperature t a Repeated turning on and off at high temperatures. For example, if t a = 120 ° C. and t b = 122 ° C., the heater is in the “on” state until the measured value t reaches 122 ° C., and the usage rate of the heater increases. On the other hand, when a t b <t a, the heater will be repeated input and off at a temperature lower than the molding temperature t a, the proportion of the heater is reduced. By performing such control, in the case of crushed materials that tend to have a high amount of moisture, the heater usage rate is increased (operation that emphasizes heating by the heater) to ensure the quality of the molded product and crushing tends to be low in moisture. In the case of a thing, it becomes an economical driving | operation which reduced the usage rate of the heater (operation which emphasized cooling by water injection), and an appropriate driving | operation is attained according to the composition of a crushed material.

本実施の形態において、成形品温度センサーである熱電対29を成形品38と直接接触するようにノズル25に設けたが、これに限定されず、熱電対を成形品38に直接接触しないで、間接的にノズル25に設け、その分、温度の補正を行って、成形品38の処理温度を推定することができる。さらに、成形品38の成形温度は、120℃として説明したが、これに限定されず、破砕物の種類(性状、水分や発熱量等)や破砕物の配合割合等を考慮して、100〜140℃の範囲とすることもできる。 In the present embodiment, the thermocouple 29, which is a molded product temperature sensor, is provided in the nozzle 25 so as to be in direct contact with the molded product 38. However, the present invention is not limited to this, and the thermocouple is not directly in contact with the molded product 38. The processing temperature of the molded product 38 can be estimated by indirectly providing the nozzle 25 and correcting the temperature accordingly. Furthermore, although the molding temperature of the molded product 38 has been described as 120 ° C., the present invention is not limited to this. It can also be made into the range of 140 degreeC.

ヒータを構成する多数のヒータエレメント31を加熱プレート22に埋め込み、更に加熱プレート22に温度センサーを設けた。また、ヒータはヒータエレメント以外の手段で構成することもできる。処理温度を適正温度に保つ注水制御の方法として、PID制御としたが、これに限定されず、他の制御方法、例えば、比例制御、PI制御等も適用できる。 A number of heater elements 31 constituting a heater were embedded in the heating plate 22, and a temperature sensor was provided on the heating plate 22. Further, the heater can be configured by means other than the heater element. Although the PID control is used as the water injection control method for maintaining the treatment temperature at an appropriate temperature, the present invention is not limited to this, and other control methods such as proportional control and PI control can also be applied.

スクリューフィーダ20に一対のスクリュー21を設けたが、これに限定されず、1本のスクリューを設けることもできる。成形品の温度を測定する過熱防止のための温度センサーとして、加熱プレート22に取付けた熱電対30の代わりに放射温度計を用いて、押出口24から出てきた成形品38の温度を非接触で測定するように構成することも可能である。また、押出し成形機の代わりに射出成形機を用いることも可能である。 Although the screw feeder 20 is provided with a pair of screws 21, the present invention is not limited to this, and a single screw may be provided. A radiation thermometer is used in place of the thermocouple 30 attached to the heating plate 22 as a temperature sensor for measuring the temperature of the molded product, and the temperature of the molded product 38 coming out from the extrusion port 24 is contactless. It is also possible to configure so as to measure with. It is also possible to use an injection molding machine instead of the extrusion molding machine.

本発明の一実施の形態に係る押出し成形機における成形品の製造方法の概略説明図である。It is a schematic explanatory drawing of the manufacturing method of the molded article in the extrusion molding machine concerning one embodiment of the present invention. 同押出し成形機における成形品の製造方法を適用する破砕物の押出し成形設備の構成図である。It is a block diagram of the extrusion molding equipment of the crushed material which applies the manufacturing method of the molded article in the extrusion molding machine. 押出し成形機の押出部の詳細断面図である。It is detail sectional drawing of the extrusion part of an extrusion molding machine.

符号の説明Explanation of symbols

10:廃棄物の押出し成形設備、11:供給コンベヤ、12:定量供給機、13:成形製品、14:押出し成形機、15:ホッパー、16:スクリューフィーダ、17:ブリッジブレーカー、18:ケーシング、19:開口部、20:スクリューフィーダ、21:スクリュー、22:加熱プレート、23:ダイスプレート、24:押出口、25:ノズル、26:孔、27、28:ライナー、29:熱電対(成形品温度センサー)、30:熱電対(温度センサー)、31:ヒータエレメント、32:噴出ノズル、33:流量調整弁、34:温度指示調節計、35:注水量調節計、36:モータ、37:回転刃、38:成形品 10: Waste extrusion equipment, 11: Feeding conveyor, 12: Metering feeder, 13: Molded product, 14: Extruder, 15: Hopper, 16: Screw feeder, 17: Bridge breaker, 18: Casing, 19 : Opening, 20: Screw feeder, 21: Screw, 22: Heating plate, 23: Die plate, 24: Extrusion port, 25: Nozzle, 26: Hole, 27, 28: Liner, 29: Thermocouple (molded product temperature Sensor), 30: thermocouple (temperature sensor), 31: heater element, 32: jet nozzle, 33: flow rate adjusting valve, 34: temperature indicating controller, 35: water injection amount controller, 36: motor, 37: rotary blade , 38: Molded product

Claims (5)

破砕されたプラスチック主体の廃棄物を押出し成形機に投入して加熱状態で先部のノズルから押し出して成形品とし、更に該成形品を切断して、コークス原料として使用可能な塊状の成形製品を製造する方法において、
前記押出し成形機には、前記成形品の成形温度を測定する成形品温度センサーと、前記廃棄物を加熱するヒータとが設けられ、前記成形品温度センサーによる測定値が設定温度になるように、投入された前記廃棄物に所定量の注水を自動的に行い、更に、前記成形品温度センサーを監視しながら前記ヒータの入切を行い、前記成形品の処理温度を維持することを特徴とする押出し成形機における成形品の製造方法。
The crushed plastic-based waste is put into an extrusion molding machine, extruded in a heated state through a nozzle at the front part to form a molded product, and then the molded product is cut to obtain a massive molded product that can be used as a coke raw material. In the manufacturing method,
The extrusion molding machine is provided with a molded product temperature sensor for measuring the molding temperature of the molded product and a heater for heating the waste, so that the measured value by the molded product temperature sensor becomes a set temperature, A predetermined amount of water is automatically injected into the waste that has been added, and the heater is turned on and off while monitoring the temperature sensor of the molded product to maintain the processing temperature of the molded product. A method for producing a molded product in an extrusion molding machine.
請求項1記載の押出し成形機における成形品の製造方法において、前記成形品温度センサーを監視しながら前記ヒータの入切を行う制御は、前記成形品の設定温度と前記ヒータの入切の温度とに差を持たせて行うことを特徴とする押出し成形機における成形品の製造方法。 The method for manufacturing a molded product in the extrusion molding machine according to claim 1, wherein the control for turning on and off the heater while monitoring the molded product temperature sensor is performed by: setting temperature of the molded product and temperature of turning on and off the heater; A method for producing a molded product in an extrusion molding machine, characterized in that the method is performed with a difference between the two. 請求項1又は2記載の押出し成形機における成形品の製造方法において、前記ノズルはダイスプレートに設けられ、前記成形品温度センサーは、前記成形品と直接又は間接的に接触するように、前記ノズル又は前記ノズルに連通する孔を備えた前記ダイスプレートに設けられ、前記成形品の処理温度は、100〜140℃の範囲にあることを特徴とする押出し成形機における成形品の製造方法。 3. The method of manufacturing a molded product in an extrusion molding machine according to claim 1 or 2, wherein the nozzle is provided on a die plate, and the molded product temperature sensor is in direct or indirect contact with the molded product. Or it is provided in the said die plate provided with the hole connected to the said nozzle, The process temperature of the said molded article exists in the range of 100-140 degreeC, The manufacturing method of the molded article in the extrusion molding machine characterized by the above-mentioned. 請求項3記載の押出し成形機における成形品の製造方法において、前記ヒータは、前記ダイスプレートに連接された加熱プレートに埋め込まれ、該加熱プレートには、温度センサーがあって、該温度センサーにより測定された前記加熱プレートの温度が異常温度になると前記ヒータの電源が切れることを特徴とする押出し成形機における成形品の製造方法。 4. The method of manufacturing a molded product in an extrusion molding machine according to claim 3, wherein the heater is embedded in a heating plate connected to the die plate, and the heating plate has a temperature sensor, and is measured by the temperature sensor. A method for producing a molded product in an extrusion molding machine, wherein the heater is turned off when the temperature of the heated plate becomes an abnormal temperature. 請求項1〜4のいずれか1項に記載の押出し成形機における成形品の製造方法において、前記ヒータの入切は、前記成形温度より高い温度で行われることを特徴とする押出し成形機における成形品の製造方法。 The method for producing a molded product in the extrusion molding machine according to any one of claims 1 to 4, wherein the heater is turned on and off at a temperature higher than the molding temperature. Product manufacturing method.
JP2006199785A 2006-07-21 2006-07-21 Extrusion molding equipment of refuse for manufacturing coke raw material and method for manufacturing molding using the same Pending JP2007015384A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006199785A JP2007015384A (en) 2006-07-21 2006-07-21 Extrusion molding equipment of refuse for manufacturing coke raw material and method for manufacturing molding using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006199785A JP2007015384A (en) 2006-07-21 2006-07-21 Extrusion molding equipment of refuse for manufacturing coke raw material and method for manufacturing molding using the same

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2001375443A Division JP2003171668A (en) 2001-12-10 2001-12-10 Method for manufacturing molded article in extrusion molding machine

Publications (1)

Publication Number Publication Date
JP2007015384A true JP2007015384A (en) 2007-01-25

Family

ID=37752928

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006199785A Pending JP2007015384A (en) 2006-07-21 2006-07-21 Extrusion molding equipment of refuse for manufacturing coke raw material and method for manufacturing molding using the same

Country Status (1)

Country Link
JP (1) JP2007015384A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111319224A (en) * 2020-04-10 2020-06-23 福州约春向科技有限公司 Extrusion device for molten state object
JP2021088120A (en) * 2019-12-04 2021-06-10 日本製鉄株式会社 Manufacturing method for waste plastic molded product and manufacturing apparatus for waste plastic molded product

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021088120A (en) * 2019-12-04 2021-06-10 日本製鉄株式会社 Manufacturing method for waste plastic molded product and manufacturing apparatus for waste plastic molded product
JP7343776B2 (en) 2019-12-04 2023-09-13 日本製鉄株式会社 Method for manufacturing waste plastic moldings and apparatus for manufacturing waste plastic moldings
CN111319224A (en) * 2020-04-10 2020-06-23 福州约春向科技有限公司 Extrusion device for molten state object

Similar Documents

Publication Publication Date Title
US11446865B2 (en) Print head for a 3D printer, with improved control
JP5409641B2 (en) Method and apparatus for processing synthetic resin materials
US20160001477A1 (en) Injection molding method and injection molding device
JP6116329B2 (en) Process plant start-up method for producing plastic material granules and process plant for producing plastic material granules
US20090057938A1 (en) Closed Loop Control for an Injection Unit
JP2007015384A (en) Extrusion molding equipment of refuse for manufacturing coke raw material and method for manufacturing molding using the same
EP2371519B1 (en) Startup control method and startup control device of resin extruder
JP6970484B2 (en) Automatic start-up control method for twin-screw extruder
JP2673491B2 (en) Amorphous molding material supply method
JP6507108B2 (en) Vent type injection molding apparatus and injection molding method
EP0831986A1 (en) Feed device and method for extruders
JP2003171668A (en) Method for manufacturing molded article in extrusion molding machine
JP2002178388A (en) Method for manufacturing extrusion by extruder
KR20150142661A (en) Body weight and the manufacturing device using the synthetic resin and the weight body
WO2006003977A1 (en) Injection member of molding machine and molding method
JP3897585B2 (en) Method for cutting molded product in extrusion molding machine
JP7421097B2 (en) Method for manufacturing waste plastic moldings and apparatus for manufacturing waste plastic moldings
CN106273341A (en) A kind of inflation film manufacturing machine screw extrusion apparatus
JP3552581B2 (en) Control method of solid molding machine
CN103624947B (en) Injection molding machine
CN211251120U (en) Injection molding raw material drying device
RU2125514C1 (en) Equipment to process waste of polyethylene film
KR102392906B1 (en) Hybrid extruder
JPH11309718A (en) Method for volume reduction and molding of waste plastic
JP6591891B2 (en) Manufacturing method of injection molded products

Legal Events

Date Code Title Description
A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060913

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20061219

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20081111

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090106

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090407

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20090804