JP3684114B2 - Volume reduction granulation method and apparatus for waste plastic containing combustible waste - Google Patents

Volume reduction granulation method and apparatus for waste plastic containing combustible waste Download PDF

Info

Publication number
JP3684114B2
JP3684114B2 JP21712899A JP21712899A JP3684114B2 JP 3684114 B2 JP3684114 B2 JP 3684114B2 JP 21712899 A JP21712899 A JP 21712899A JP 21712899 A JP21712899 A JP 21712899A JP 3684114 B2 JP3684114 B2 JP 3684114B2
Authority
JP
Japan
Prior art keywords
waste
screw
waste plastic
volume reduction
cylinder
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 - Fee Related
Application number
JP21712899A
Other languages
Japanese (ja)
Other versions
JP2001038726A (en
Inventor
憲明 橋本
昌吉 時久
英雄 大薮
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP21712899A priority Critical patent/JP3684114B2/en
Publication of JP2001038726A publication Critical patent/JP2001038726A/en
Application granted granted Critical
Publication of JP3684114B2 publication Critical patent/JP3684114B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、可燃ゴミを含む廃プラスチックを減容・造粒するスクリュ式減容造粒方法および装置に関するものである。
【0002】
【従来の技術】
使用済みの廃プラスチックには、大別して産業系と一般系の2種類がある。その形状はさまざまであり、取り扱いは難しいものが多い。廃プラスチックを燃焼させると有害なガスが発生し人体に悪影響を及ぼしたり、燃焼炉を損傷したりする。また、燃焼ガスは大気を汚染し環境問題の原因となる。そのため、埋め立て処理が行われているが、例えば、一般系の廃プラスチックは嵩だかで、そのまま埋め立てると、スペースの問題や土地の安定性の問題などが起きる。そのため、2軸スクリュ型の押出機などを用いて圧縮・熱溶融させ、減容化して嵩を小さくして埋め立てることが行われている。例えば、特開平7−256645号公報や特開平10−315237号公報には、次のような二軸押出機タイプの減容固形化装置が開示されている。すなわち、廃棄物は、例えば50mm角まで破砕された後、二軸押出機の投入口に供給される。廃棄物は二本の特殊なスクリュの回転により破砕、混練、加圧、圧縮されながら下流側に進み、スクリュの先端側に設けられた平面のダイスから吐出され、適当な長さに切断されてペレット化される。通常、供給された廃棄物中には水分が非常に多く、それが廃棄物中のプラスチック分の溶融を妨げるが、押出機シリンダからの外部加熱とスクリュによるせん断発熱によりプラスチック分を溶融させ、その溶融したプラスチック分が他の成分の中に混練され、他の成分をくっつけるバインダー的な役割を果たし、廃棄物は、流動性を与えられてダイスノズルから押し出されペレット(粒)になる。
【0003】
【発明が解決しようとする課題】
上記のように、圧縮・加熱溶融した廃プラスチックをダイスノズルから押し出してペレットを製造する装置では、廃プラスチック中の塩素系ポリマーの熱分解による塩化水素の発生防止や省エネルギーの観点から、廃プラスチックの溶融程度が低く抑えられており、未溶融樹脂が多く存在している。また、廃プラスチック中には、紙、木材、金属片などを含んでいることから、スクリュとダイス間で流動性が低下し流動しなくなったり、ダイスノズルの内壁面の抵抗が大きくなり流動しなくなったりする、いわゆるダイスノズルの目詰まりがよく発生する。目詰まりが発生すると、運転を中断し、ダイノズルの目詰まりを解除する作業を行わなければならないという問題がある。よく目詰まりをおこす廃プラスチックとして、ポリプロピレン樹脂、ポリエステル樹脂の厚肉包装テープやポリエステル樹脂、ナイロン等の高融点樹脂成形品などがある。
【0004】
さらに、原料廃プラスチックの組成変動や水分含有量変動により、廃プラスチックの溶融が変動する問題がある。低融点樹脂不足や高水分率に起因する溶融不足は減容化後のペレット(固形燃料)の成形度合いを損ない、形が崩れやすく、嵩密度の低いものとなる。これでは、埋め立てる場合には、埋め立てスペースが大きくなる。また、燃料にする場合には、ハンドリングが難しくなり、粉塵などがでやすくなり衛生面での問題が発生する。また、廃プラスチックの溶融度が進み過ぎると、廃プラスチック中のポリ塩化ビニルが部分的に熱分解を起こし、塩化水素が発生し、機械装置の腐蝕や運転員の健康を損なう恐れがでてくる。
【0005】
本発明は、上記従来の問題点を解決するためになされたものであって、ダイスノズルの目詰まりを防止することができると共に、廃プラスチックの溶融度合いや減容化度合いを調整することができる可燃ゴミを含む廃プラスチックの減容造粒方法及びその装置を提供することを課題とする。
【0007】
【課題を解決するための手段】
本発明の可燃ゴミを含む廃プラスチックの減容造粒装置は、供給部、混練部および押出部からなるスクリュの混練部の下流側に、背圧を調整して廃プラスチックの溶融度合や減容化度合い調整する廃プラ通過流路調整装置を設置し、スクリュの押出部を多重フライトとし、押出部のスクリュ溝とシリンダの内壁によって排出口を形成し、排出口に溶融廃プラスチックを切断するカッタを設けたことを特徴とする。
【0009】
本発明により、廃プラスチックを破砕、混練、圧縮し、発熱させて部分的に溶融し、廃プラスチックの嵩密度を上げてペレットなどの固形化物を得ることができる。
【0010】
【発明の実施の形態】
以下、本発明の実施の形態を実施例に基づき図面を参照して説明する。
【0011】
図1は本発明による可燃ゴミを含む廃プラスチック減容化造粒装置の概略構成図であり、(a)は平面断面図、(b)は(a)のA矢視図である。
【0012】
本発明の可燃ゴミを含む廃プラスチックの減容化造粒装置は、一端に廃プラスチックの原料供給入口1、他端に減容された廃プラスチックの排出口2が設けられているシリンダ3と、このシリンダ3内に装着され供給部4、混練部5および押出部6を有するスクリュ7と、前記シリンダ3の排出口2に配設されているカッタとしての固定刃8とから構成されている。前記スクリュ7は、減速機9を介してモータ10によって駆動される。なお、本実施例の廃プラスチックの減容化造粒装置は、異方向回転二軸スクリュ型押出機で、スクリュ7の供給部4、混練部5は大径で噛み合い形、押出部6は小径で非噛み合い形とされている。
【0013】
前記スクリュ7の押出部6は多条フライトからなり、スクリュ口径や処理能力によって変わるが通常2〜64条とされている。また、スクリュ7の先端部は、軸心に対して鉛直な平面とされている。
【0014】
前記シリンダ3の先端側には、その上流側の混練部5の圧力を調整して廃プラスチックの溶融度合や減容化度合いを調整するオリフィスを有する背圧調整ゲート11が設けられている。なお、シリンダ3は、電気、蒸気あるいは熱媒油により加熱されている。前記背圧調整ゲート11のオリフィスに代えて、スクリュ7の混練部5と押出部6の間にテーパー部を設け、シリンダ3にも同位置にテーパー部を設けて、両テーパー部でスロット部を形成し、スクリュ7またはシリンダ3を前後に移動してスロット部の隙間を変化させる構成としてもよい。
【0015】
前記シリンダ3の先端面には、固定刃8が接触して溶融廃プラスチックを切断する際、シリンダ加熱の影響でシリンダ端面とスクリュ端面が面位置にならないという問題が起きるので、シリンダ端面とスクリュ端面を調整するための間隙調整リング12が設けられている。
【0016】
前記固定刃8は、図1(a)に示すように、スクリュ7およびシリンダ3の端面方向にバネで押し付けられると共に、図1(b)に示すように、スクリュ7の回転方向とは逆方向にバネで押し付けられている。なお、カッタは回転刃でもよい。
【0017】
次に、その動作について説明する。
【0018】
原料となる廃プラスチックは、原料供給口1から供給され、スクリュ7の供給部4、混練部5により前方に送られながら、シリンダ3からの加熱、スクリュ7とシリンダ3の間で発生するせん断発熱、スクリュ7による圧縮および混練部5の前方に設けられている背圧調整ゲート11の抵抗を受け、混練部5に充満し、この混練部5で混練分散作用を受けて発熱し、溶融・減容化される。この溶融廃プラスチックは、背圧調整ゲート11を通過し、スクリュ7の押出部6の多条フライトで下流側に輸送され、スクリュ先端のスクリュ溝7aとシリンダ3の内壁で構成される排出口2からなんらの詰りもなく排出される。
【0019】
排出された溶融廃プラスチックは、スクリュ7の回転と排出口2に設けた固定刃8により適宜な長さに切断される。これにより、嵩密度が大きく、減容度が高く、かつポリ塩化ビニルが分解されていないペレット、例えば固形燃料を作ることができる。
【0020】
【発明の効果】
本発明は、以上説明したように構成されているので、次のような効果を得ることができる。
(a)廃棄プラスチックは、原料組成の地域性、季節性などによる変動や変化および水分含有量の日変動があるが、背圧調整ゲートにより、廃プラスチックの溶融度合や減容化度合いを自由に調整することができる。また、どのような組成の廃プラスチックでも、塩化ビニル樹脂の熱分解を起こさずに、減容化度の大きいペレット(固形燃料など)を製造することが可能になる。
(b)溶融廃プラスチックは、スクリュ溝から外部に排出され、従来の、いわゆるダイスがないので、高融点樹脂や異物などがきても目詰まりなく排出することができる。
【図面の簡単な説明】
【図1】本発明による廃プラスチック減容化造粒装置の概略構成図であり、(a)は平面断面図、(b)は(a)のA矢視図である。
【符号の説明】
1 原料供給口
2 排出口
3 シリンダ
4 供給部
5 混練部
6 押出部
7 スクリュ
7a スクリュ溝
8 固定刃(カッタ)
9 減速機
10 モータ
11 背圧調整ゲート(廃プラ通過流路調整装置)
12 間隙調整リング
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a screw-type volume reduction granulation method and apparatus for volume reduction and granulation of waste plastic containing combustible waste.
[0002]
[Prior art]
There are roughly two types of used waste plastic: industrial and general. Their shapes vary and are often difficult to handle. When waste plastic is burned, harmful gases are generated, which adversely affects the human body and damages the combustion furnace. Also, the combustion gas pollutes the atmosphere and causes environmental problems. For this reason, landfill processing is performed. For example, general waste plastic is bulky, and if it is landfilled as it is, problems such as space and land stability may occur. For this reason, compression and heat melting are performed using a twin screw type extruder or the like, and the volume is reduced to reduce the bulk and the land is filled. For example, JP-A-7-256645 and JP-A-10-315237 disclose the following twin-screw extruder type volume reduction solidification device. That is, the waste is crushed to, for example, a 50 mm square and then supplied to the inlet of the twin screw extruder. Waste is crushed, kneaded, pressurized and compressed by the rotation of two special screws, and then proceeds to the downstream side. It is discharged from a flat die provided at the tip of the screw and cut to an appropriate length. Pelletized. Normally, the supplied waste has a lot of moisture, which prevents the plastic in the waste from melting, but the plastic is melted by external heating from the extruder cylinder and shear heat generated by the screw. The melted plastic content is kneaded into the other components and serves as a binder to attach the other components, and the waste is given fluidity to be extruded from the die nozzle into pellets (grains).
[0003]
[Problems to be solved by the invention]
As described above, in an apparatus for producing pellets by extruding compressed plastic, heat-melted waste plastic from a die nozzle, from the viewpoint of preventing generation of hydrogen chloride due to thermal decomposition of chlorinated polymer in waste plastic and saving energy, The degree of melting is kept low, and there are many unmelted resins. In addition, because waste plastic contains paper, wood, metal pieces, etc., the fluidity between the screw and the die decreases and does not flow, or the resistance of the inner wall of the die nozzle increases and the fluid does not flow. The so-called die nozzle clogging often occurs. When clogging occurs, there is a problem that the operation must be interrupted and work to clear clogging of the die nozzle must be performed. Waste plastics that often cause clogging include polypropylene resin, polyester resin thick packaging tape, polyester resin, and high melting point resin molded products such as nylon.
[0004]
Furthermore, there is a problem that the melting of the waste plastic fluctuates due to fluctuations in the composition and water content of the raw material waste plastic. Insufficient melting due to a low melting point resin shortage or a high moisture content impairs the degree of molding of the pellets (solid fuel) after volume reduction, tends to lose its shape, and has a low bulk density. This increases the landfill space when landfilling. In addition, when using fuel, handling becomes difficult, dust and the like are easily generated, and a sanitary problem occurs. Moreover, if the melting degree of waste plastics is too high, the polyvinyl chloride in the waste plastics will be partially thermally decomposed to generate hydrogen chloride, which may damage the machinery and the health of operators. .
[0005]
The present invention has been made to solve the above-described conventional problems, and can prevent clogging of a die nozzle and adjust the degree of melting and volume reduction of waste plastic. It is an object of the present invention to provide a volume reduction granulation method and apparatus for waste plastic containing combustible waste.
[0007]
[Means for Solving the Problems]
The volume reduction granulator for waste plastic containing combustible waste according to the present invention has a back pressure adjusted downstream of the kneading part of the screw consisting of a supply part, a kneading part and an extrusion part to adjust the degree of melting and volume reduction of the waste plastic. Cutter that installs waste plastic passage flow path adjustment device that adjusts the degree of conversion, makes the screw extrusion part a multiple flight, forms a discharge port by the screw groove of the extrusion part and the inner wall of the cylinder, and cuts molten waste plastic at the discharge port Is provided .
[0009]
According to the present invention, waste plastic can be crushed, kneaded, compressed, heated and partially melted to increase the bulk density of the waste plastic to obtain a solidified product such as pellets.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described based on examples with reference to the drawings.
[0011]
FIG. 1 is a schematic configuration diagram of a waste plastic volume-reduction granulating apparatus containing combustible waste according to the present invention.
[0012]
The waste plastic volume reducing granulation apparatus containing combustible waste of the present invention includes a cylinder 3 provided with a waste plastic raw material supply inlet 1 at one end and a waste plastic discharge port 2 reduced at the other end, The screw 7 is mounted in the cylinder 3 and has a supply part 4, a kneading part 5 and an extrusion part 6, and a fixed blade 8 as a cutter disposed in the discharge port 2 of the cylinder 3. The screw 7 is driven by a motor 10 via a speed reducer 9. In addition, the volume reduction granulation apparatus of the waste plastic of a present Example is a different direction rotation biaxial screw type extruder, the supply part 4 and the kneading part 5 of the screw 7 are large-diameter meshing type, and the extrusion part 6 is a small diameter. In non-meshing form.
[0013]
The extrusion part 6 of the screw 7 is composed of a multi-strip flight, and is usually 2 to 64, although it varies depending on the screw diameter and processing capacity. The tip of the screw 7 is a plane that is perpendicular to the axis.
[0014]
A back pressure adjusting gate 11 having an orifice for adjusting the degree of melting and volume reduction of the waste plastic by adjusting the pressure of the kneading section 5 on the upstream side is provided on the tip side of the cylinder 3. The cylinder 3 is heated by electricity, steam or heat transfer oil. Instead of the orifice of the back pressure adjusting gate 11, a taper portion is provided between the kneading portion 5 and the extrusion portion 6 of the screw 7, and the cylinder 3 is also provided with a taper portion at the same position. It is good also as a structure which forms and moves the screw 7 or the cylinder 3 back and forth, and changes the clearance gap of a slot part.
[0015]
When the fixed blade 8 comes into contact with the tip surface of the cylinder 3 and cuts the molten waste plastic, there is a problem that the cylinder end surface and the screw end surface are not positioned due to the effect of the cylinder heating. A gap adjusting ring 12 is provided for adjusting.
[0016]
As shown in FIG. 1A, the fixed blade 8 is pressed by a spring toward the end faces of the screw 7 and the cylinder 3, and as shown in FIG. 1B, the fixed blade 8 is in a direction opposite to the rotational direction of the screw 7. It is pressed against the spring. The cutter may be a rotary blade.
[0017]
Next, the operation will be described.
[0018]
Waste plastic as a raw material is supplied from the raw material supply port 1 and is sent forward by the supply unit 4 and kneading unit 5 of the screw 7, while heating from the cylinder 3 and shearing heat generated between the screw 7 and the cylinder 3. , Compression by the screw 7 and resistance of the back pressure adjusting gate 11 provided in front of the kneading part 5 are filled, the kneading part 5 is filled, and the kneading part 5 is subjected to kneading and dispersing action to generate heat and melt and reduce. Tolerated. The molten waste plastic passes through the back pressure adjusting gate 11 and is transported downstream by the multi-strip flight of the extrusion portion 6 of the screw 7, and the discharge port 2 constituted by the screw groove 7 a at the screw tip and the inner wall of the cylinder 3. Is discharged without any clogging.
[0019]
The discharged molten waste plastic is cut into an appropriate length by the rotation of the screw 7 and the fixed blade 8 provided at the discharge port 2. As a result, pellets having a high bulk density, a high volume reduction, and undecomposed polyvinyl chloride, such as solid fuel, can be produced.
[0020]
【The invention's effect】
Since the present invention is configured as described above, the following effects can be obtained.
(A) Waste plastics may vary or change due to locality and seasonality of the raw material composition and daily fluctuations in water content, but the back pressure adjustment gate allows the degree of melting and volume reduction of waste plastics to be freely controlled. Can be adjusted. In addition, waste plastics of any composition can produce pellets (such as solid fuel) with a large volume reduction without causing thermal decomposition of the vinyl chloride resin.
(B) The molten waste plastic is discharged from the screw groove to the outside, and since there is no conventional so-called die, it can be discharged without clogging even when a high-melting point resin or foreign matter comes.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a schematic configuration diagram of a waste plastic volume reducing granulation apparatus according to the present invention, in which (a) is a cross-sectional plan view and (b) is a view as seen from an arrow A in (a).
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Raw material supply port 2 Discharge port 3 Cylinder 4 Supply part 5 Kneading part 6 Extrusion part 7 Screw 7a Screw groove 8 Fixed blade (cutter)
9 Reducer 10 Motor 11 Back pressure adjustment gate (Waste plastic passage flow adjustment device)
12 Gap adjustment ring

Claims (2)

可燃ゴミを含む廃プラスチックを減容・造粒するスクリュ式減容造粒装置において、供給部(4)、混練部(5)および押出部(6)からなるスクリュ(7)の混練部(5)の下流側に、背圧を調整して廃プラスチックの溶融度合や減容化度合い調整する廃プラ通過流路調整装置(11)を設置し、前記スクリュ(7)の前記押出部(6)を多重フライトとし、該押出部(6)のスクリュ溝(7a)とシリンダ(3)の内壁によって排出口(2)を形成し、該排出口(2)に溶融廃プラスチックを切断するカッタ(8)を設けたことを特徴とする可燃ゴミを含む廃プラスチックの減容造粒装置。In a screw-type volume reduction granulator for reducing and granulating waste plastic containing combustible waste, a kneading part (5) of a screw (7) comprising a supply part (4), a kneading part (5) and an extrusion part (6) ), A waste plastic passage channel adjusting device (11) for adjusting the degree of melting and volume reduction of the waste plastic by adjusting the back pressure is installed, and the pushing portion (6) of the screw (7) Is a multi-flight, a discharge port (2) is formed by the screw groove (7a) of the extrusion portion (6) and the inner wall of the cylinder (3), and a cutter (8) that cuts molten waste plastic into the discharge port (2). ), A volume reduction granulator for waste plastics containing combustible waste. 前記シリンダ(3)の先端面に、シリンダ端面とスクリュ端面を調整するための間隙調整リング(12)を設けたことを特徴とする請求項記載の可燃ゴミを含む廃プラスチックの減容造粒装置。The front end surface of the cylinder (3), the cylinder end face and the gap adjustment ring for adjusting the screw end face (12), characterized in that the provided claims 1 volume reduction granulated waste plastic containing the combustible waste according apparatus.
JP21712899A 1999-07-30 1999-07-30 Volume reduction granulation method and apparatus for waste plastic containing combustible waste Expired - Fee Related JP3684114B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21712899A JP3684114B2 (en) 1999-07-30 1999-07-30 Volume reduction granulation method and apparatus for waste plastic containing combustible waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21712899A JP3684114B2 (en) 1999-07-30 1999-07-30 Volume reduction granulation method and apparatus for waste plastic containing combustible waste

Publications (2)

Publication Number Publication Date
JP2001038726A JP2001038726A (en) 2001-02-13
JP3684114B2 true JP3684114B2 (en) 2005-08-17

Family

ID=16699302

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21712899A Expired - Fee Related JP3684114B2 (en) 1999-07-30 1999-07-30 Volume reduction granulation method and apparatus for waste plastic containing combustible waste

Country Status (1)

Country Link
JP (1) JP3684114B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009280632A (en) * 2008-05-19 2009-12-03 Kinki:Kk Solid fuel molding apparatus

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003048211A (en) * 2001-08-08 2003-02-18 Hokuei:Kk Volume reduction and solidification apparatus for waste such as foamed polystyrene or the like
JP2003053311A (en) * 2001-08-09 2003-02-25 Sumitomo Heavy Ind Ltd Waste disposal system
JP4559391B2 (en) * 2006-08-08 2010-10-06 ヤマハリビングテック株式会社 Compound manufacturing apparatus, mold for extruder and method for manufacturing compound
JP2015135194A (en) * 2014-01-16 2015-07-27 ▲慧▼鈴 ▲黄▼ Crumpling and drier machine
JP6120393B1 (en) * 2016-07-14 2017-04-26 日本シーム株式会社 Granulator
JP7058542B2 (en) * 2018-04-20 2022-04-22 株式会社日本製鋼所 Extruder and kneading extrusion method
CN114211716A (en) * 2021-12-10 2022-03-22 浙江海利环保科技股份有限公司 Low-temperature friction melting regeneration polyester granulation device and granulation method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009280632A (en) * 2008-05-19 2009-12-03 Kinki:Kk Solid fuel molding apparatus
JP4538061B2 (en) * 2008-05-19 2010-09-08 株式会社キンキ Solid fuel molding equipment

Also Published As

Publication number Publication date
JP2001038726A (en) 2001-02-13

Similar Documents

Publication Publication Date Title
JP7144513B2 (en) Apparatus and method for extruding thermomechanically deformable materials in bulk form, and compact screw extruder
US3867079A (en) Apparatus for extruding polymeric material
EP1832407B1 (en) Kneading extruder
JPH02202403A (en) Solidifying apparatus for continuously regranulating thermoplastic resin waste, film, thread etc, in particular
JP3684114B2 (en) Volume reduction granulation method and apparatus for waste plastic containing combustible waste
JP2546880B2 (en) Screw extruder
JP2008302555A (en) Treatment method for waste plastic and its device
TR199801717T2 (en) A method and device for the manufacture of molded plastic products and plastic products.
JP2012025153A (en) Multi-stage thermoplastic resin extrusion apparatus, and method of extruding thermoplastic resin using the same
JP2008155582A (en) Processor of waste plastic
JP3917576B2 (en) Volume reduction granulation method and apparatus for waste plastic
JP5048638B2 (en) Compression extrusion molding equipment
WO1996040483A1 (en) Feed device and method for extruders
KR20090114643A (en) Exhaust screw of plastic extrusion molding machine
JP2009084517A (en) Compression solidification method and compression solidification apparatus of waste plastic
CN215203386U (en) Special extrusion screw for efficient granulation of flat-double polyvinyl chloride powder
JP2520518B2 (en) Method for producing polyvinyl alcohol type molded article
KR0175915B1 (en) Waste styrofoam recycling apparatus
JP3154953B2 (en) Method for producing compound pellets containing wood flour
JPH09141726A (en) Method and apparatus for extrusion molding of vinyl chloride molded product
JPH0289608A (en) Recycling device of thermoplastic resin scrap material and molding line, in which the same device is equipped, of thermoplastic resin sheet of the like
CN215750647U (en) Forced feeding device for extruder and extruder
CN211917376U (en) Grain device is cut to extruder
JPH09117954A (en) Twin-screw extruder
JP4059817B2 (en) Recycled fuel made from waste plastic, production method and production apparatus

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040531

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050126

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050316

RD03 Notification of appointment of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7423

Effective date: 20050316

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050518

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050527

R150 Certificate of patent (=grant) or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080603

Year of fee payment: 3

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090603

Year of fee payment: 4

LAPS Cancellation because of no payment of annual fees