JPS6063285A - Disposal unit for plastic waste - Google Patents

Disposal unit for plastic waste

Info

Publication number
JPS6063285A
JPS6063285A JP58169212A JP16921283A JPS6063285A JP S6063285 A JPS6063285 A JP S6063285A JP 58169212 A JP58169212 A JP 58169212A JP 16921283 A JP16921283 A JP 16921283A JP S6063285 A JPS6063285 A JP S6063285A
Authority
JP
Japan
Prior art keywords
plastic waste
pyrolysis furnace
gas
waste
melted
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
JP58169212A
Other languages
Japanese (ja)
Inventor
Tomoyuki Okada
知行 岡田
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 MEKA KK
Original Assignee
NIPPON MEKA KK
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 NIPPON MEKA KK filed Critical NIPPON MEKA KK
Priority to JP58169212A priority Critical patent/JPS6063285A/en
Publication of JPS6063285A publication Critical patent/JPS6063285A/en
Pending legal-status Critical Current

Links

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
    • 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

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

PURPOSE:The plastic waste which is melted with heat in the pyrolysis furnace is increased in its surface area contacting with the gas phase to promote its gasification whereby high-efficiency pyrolysis of the waste is realized in a short time to recover the condensed oil. CONSTITUTION:Plastic waste is fed into the pyrolysis furnace 1 and the furnace is heated. The kettle containing the melt 3 is equipped with a stirrer composed of a rotary shaft 21 installed through the bottom of the kettle and spiral blades 22 and melted plastic waste is allowed to fall from the upper end of the blades 22, as the shaft is rotating. The melted waste is lifted up higher than its surface to increase its surface area contacting with the gas phase and promote its gasification. The resultant gas is cooled to collect condensed oil.

Description

【発明の詳細な説明】 得られるガスを冷却することにより、油を凝縮液化させ
て回収するプラスチック廃棄物の処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a plastic waste processing apparatus that condenses and liquefies oil and recovers it by cooling the resulting gas.

近年、廃棄物の適正処理および資源の再生利用の見地か
ら、プラスチック廃棄物を加熱分解し油として回収する
システムが研究開発されており、現在知られているシス
テムによれば、プラスチック廃棄物は熱分解炉によって
加熱分解し、炉内に生成された熱分解カスを冷却するこ
とにより油分を凝縮液化して取り出し、残りのガスは燃
焼させてその熱を回収するようにしている。
In recent years, from the perspective of proper waste treatment and resource recycling, research and development has been conducted on systems that thermally decompose plastic waste and recover it as oil.According to currently known systems, plastic waste is The oil is thermally decomposed in a decomposition furnace, and the thermal decomposition residue generated in the furnace is cooled to condense and liquefy the oil and removed, and the remaining gas is combusted to recover its heat.

ところで、このようなシステムにおいてプラスチック廃
棄物を熱分解する方法としては、熱分解炉内でプラスチ
ック廃棄物を燃焼させる方法と、熱分解炉を外部から加
熱する方法とがある。しかしながら、廃棄物を燃焼させ
る場合には、熱分解ガスの収率が減少し、しかも高い熱
カロリーが発生するため炉の損耗が大きいという問題が
あり、他方、熱分解炉を外部から加熱する場合には、炉
内で生成した可燃性ガスが爆発する危険がある。
By the way, methods for pyrolyzing plastic waste in such a system include a method of burning the plastic waste in a pyrolysis furnace and a method of heating the pyrolysis furnace from the outside. However, when burning waste, there are problems in that the yield of pyrolysis gas decreases and high heat calories are generated, resulting in large wear and tear on the furnace.On the other hand, when heating the pyrolysis furnace from the outside, There is a danger that the flammable gas generated in the furnace could explode.

そこで、熱分解炉内に空気を遮断した状態でプラスチッ
ク廃棄物を導入して加熱することとし、その空気遮断方
法として、粒状ないし粉状に破砕したプラスチック廃棄
物を不活性ガス(例えば窒素)が充満した通路中に通し
てから熱分解炉内に供給することが考えられている。
Therefore, we decided to heat the plastic waste by introducing it into the pyrolysis furnace with the air shut off.As a way to shut off the air, the plastic waste crushed into granules or powder was heated using an inert gas (e.g. nitrogen). It has been considered to pass it through a filled channel before feeding it into a pyrolysis furnace.

このような熱分解炉において、加熱溶融せしめられたプ
ラスチック廃棄物は、その表面から蒸発。
In such a pyrolysis furnace, plastic waste is heated and melted and evaporated from its surface.

気化するが、そのための表面積は熱分解炉のプラスチッ
ク収納釜の内部断面積に限られているため、プラスチッ
ク廃棄物の量が多くなればそれだけ蒸発、気化に時間が
かかり、加熱溶融に要する燃料費も多くなるという問題
があった。
However, the surface area for this purpose is limited to the internal cross-sectional area of the plastic storage pot of the pyrolysis furnace, so the larger the amount of plastic waste, the longer it will take to evaporate and vaporize, and the fuel cost required for heating and melting. The problem was that there were too many.

本発明は上記の事情に鑑みてなされたものであり、その
目的は、上記のような熱分解炉において加熱溶融したプ
ラスチック廃棄物の気化を促進することにある。
The present invention has been made in view of the above circumstances, and its purpose is to promote the vaporization of plastic waste heated and melted in a pyrolysis furnace as described above.

以下、添付図面を参照して本発明の具体例について説明
する。
Hereinafter, specific examples of the present invention will be described with reference to the accompanying drawings.

第1図は、プラスチック廃棄物の処理装置全体の構成を
示す。この処理装置は、粒状もしくは粉状に粉砕された
プラスチック廃棄物Pを、適宜の供給装置によって熱分
解炉1内に供給し、ここで加熱分解することにより熱分
解ガスを生成し、このカスを導管2によって冷却槽3に
送り、ここでカスから凝縮液化した油を導管4によって
貯油槽5に貯え、貯油槽5の下部から導管6および切換
弁7を通して油を適宜取り出す一方、貯油槽5の−L部
に充満したガスは導管8により中和槽9に送って中和し
た後、導管10およびこれから分岐した導管11により
熱分解炉lの加熱に利用するように構成したものである
。なお、導管11が分岐した導管10の下流部分には、
この処理装置内のガス圧が限度以上に上昇した場合に大
気中にガスを放出するための切換弁12が設けられてい
る。
FIG. 1 shows the overall configuration of a plastic waste processing apparatus. This processing device supplies plastic waste P that has been crushed into granules or powder into a pyrolysis furnace 1 using an appropriate feeding device, where it is thermally decomposed to generate pyrolysis gas, and this waste is The oil condensed from the waste is sent to a cooling tank 3 through a conduit 2, and the oil is stored in an oil storage tank 5 through a conduit 4. The oil is taken out from the lower part of the oil storage tank 5 through a conduit 6 and a switching valve 7. - The gas filling the L section is sent to a neutralization tank 9 through a conduit 8 to be neutralized, and then used for heating the pyrolysis furnace 1 through a conduit 10 and a conduit 11 branched from it. In addition, in the downstream part of the conduit 10 where the conduit 11 branches,
A switching valve 12 is provided for releasing gas into the atmosphere when the gas pressure within the processing apparatus rises above a limit.

上記処理装置において、熱分解炉lは、プラスチック廃
棄物−を収容する収納釜13と、その外側に設けられた
加熱用バーナー14とを具備すると共に、分岐導管ll
から送られるガスを燃焼させるためのノズル15を備え
ている。従って、プラスチック廃棄物を熱分解するとき
は、初めに加熱用バーナー14への燃料供給路16に設
けられた切換弁17を開いて燃料を供給することにより
、収納釜13を加熱するが、プラスチックが熱分解され
るに従って貯油槽5の上部に充満したカス量が多くなり
、ノズル15によるガス燃焼のみで十分加熱できるよう
になったときは、切換弁17を閉じてバーナー14の作
動を止める。
In the above processing apparatus, the pyrolysis furnace 1 is equipped with a storage pot 13 for storing plastic waste, a heating burner 14 provided on the outside of the storage pot 13, and a branch conduit 11.
It is equipped with a nozzle 15 for burning the gas sent from. Therefore, when pyrolyzing plastic waste, first open the switching valve 17 provided in the fuel supply path 16 to the heating burner 14 and supply fuel to heat the storage pot 13. As the oil is thermally decomposed, the amount of residue filling the upper part of the oil storage tank 5 increases, and when it becomes possible to heat the oil sufficiently by burning the gas through the nozzle 15, the switching valve 17 is closed and the operation of the burner 14 is stopped.

本発明によれば、上記のような熱分解炉lの収納釜13
には、次のようなプラスチック廃棄物の気化促進手段が
取り刊けられる。
According to the present invention, the storage pot 13 of the pyrolysis furnace l as described above
The following measures to promote the vaporization of plastic waste will be published:

まず、第2図は、収納釜13の底部を回転自在に貫通し
た回転輪21に取り付けられた螺旋状の回転翼22を示
す。この回転翼の軸21は、外部に設けた適宜の回転駆
動装置23により、所定の速度で回転される。なお、回
転軸21が貫通している収納釜13の底壁には、公知の
メカニカルシール24が施されている。
First, FIG. 2 shows a spiral rotor blade 22 attached to a rotary ring 21 that rotatably passes through the bottom of the storage pot 13. As shown in FIG. The shaft 21 of this rotor blade is rotated at a predetermined speed by an appropriate rotary drive device 23 provided externally. A known mechanical seal 24 is provided on the bottom wall of the storage pot 13 through which the rotating shaft 21 passes.

この気化促進手段としての回転R22は、収納釜13の
中に収納されたプラスチック廃棄物が加熱によって溶融
液化した状態になるまでは回転しないように、回転駆動
装置23によって制御される。プラスチック廃棄物が溶
融液化したときは、所定速度で回転する螺旋状の翼22
がこれを上昇させ、回転翼22の上端から落下させる。
The rotation R22 as the vaporization promoting means is controlled by the rotation drive device 23 so as not to rotate until the plastic waste stored in the storage pot 13 is melted and liquefied by heating. When plastic waste is melted and liquefied, a spiral blade 22 rotates at a predetermined speed.
raises it and drops it from the upper end of the rotor blade 22.

このように、溶融液化したプラスチック廃棄物をその表
面より上方に引き上げることにより、気相との接触面積
が増大し、気化が促進される。
In this way, by pulling the molten and liquefied plastic waste above its surface, the contact area with the gas phase increases and vaporization is promoted.

次に、第3図は、第2図と同様にプラスチック廃棄物と
気相との接触面積を増大する手段を示しているが、ここ
では前述の回転翼の如き機械的作動部は用いられていな
い。すなわち、収納釜13の底部に導管31を接続し、
との導管を介して所定のガス源から窒素等の不活性ガス
を収納釜13内に導入するようになっている。
Next, FIG. 3 shows a means for increasing the contact area between plastic waste and the gas phase in the same way as in FIG. do not have. That is, connect the conduit 31 to the bottom of the storage pot 13,
An inert gas such as nitrogen is introduced into the container 13 from a predetermined gas source through a conduit.

かくして、収納釜に導入された不活性ガスは、溶融液化
したプラスチック廃棄物の中で泡状になって上昇し、そ
の表面から飛び出す。これにより、プラスチック廃棄物
と気相との接触面積が増大し、気化が促進される。また
、不活性ガスが収納釜の中に充満することで、熱分解ガ
スによる爆発の危険が避けられるという効果もある。
In this way, the inert gas introduced into the storage container rises in the form of bubbles within the molten and liquefied plastic waste and escapes from its surface. This increases the contact area between the plastic waste and the gas phase, promoting vaporization. Also, by filling the storage pot with inert gas, there is an effect that the risk of explosion due to pyrolysis gas is avoided.

上記の通り、本発明によれば、熱分解炉内で加熱溶融し
たプラスチック廃棄物と気相との接触面積を増大するこ
とによりプラスチック廃棄物の気化を促進することがで
き、故にプラスチック廃棄物の気化に要する時間を短縮
し、加熱に要する燃料費を節減することができる。
As described above, according to the present invention, by increasing the contact area between the plastic waste heated and melted in the pyrolysis furnace and the gas phase, the vaporization of the plastic waste can be promoted. The time required for vaporization can be shortened and the fuel cost required for heating can be reduced.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はプラスチック廃棄物処理装置全体の構成を示す
概略説明図、第2図はプラスチック廃棄物の気化促進手
段の説明図、第3図は気化促進手段の別の例を示す図で
ある。 l−一一一熱分解炉、 3−一一一冷却槽、5−一一一
貯油槽、 9−一一一中和槽、13−−−一収納釜、 
14−−−一加熱用バーナー、21−−−一回転軸、2
2−−−一回転質、23−−−一回転駆動装置、24−
−−−メカニカルシール、 31−−−一導管。
FIG. 1 is a schematic explanatory diagram showing the overall configuration of the plastic waste processing apparatus, FIG. 2 is an explanatory diagram of means for promoting vaporization of plastic waste, and FIG. 3 is a diagram showing another example of the means for promoting vaporization of plastic waste. l-111 pyrolysis furnace, 3-111 cooling tank, 5-111 oil storage tank, 9-111 neutralization tank, 13--1 storage pot,
14---1 heating burner, 21---1 rotating shaft, 2
2---One rotation mass, 23---One rotation drive device, 24-
--- Mechanical seal, 31 --- Conduit.

Claims (1)

【特許請求の範囲】 1、熱分解炉内にプラスチック廃棄物を供給し、該熱分
解炉を加熱することにより該プラスチック廃棄物を熱分
解してガスを生成し、このガスを冷却することにより凝
縮液化した油を分離回収するプラスチック廃棄物の処理
装置において、上記熱分解炉内で加熱溶融したプラスチ
ック廃棄物と気相との接触面積を増大することにより該
プラスチック廃棄物の気化を促進する手段を」二記熱分
解炉に取り付けたことを特徴とする処理装置。 2、」−配気化促進手段は、上記熱分解炉内で回転する
ことにより上記プラスチック廃棄物をその表面より上方
に上Hさせた後落下させる回転翼から成ることを特徴と
する特許請求の範囲第1項記載の処理装置。 3、」二記気化促進手段は、窒素等の不活性ガスを供給
するガス源と、該カス源から不活性カスを上記熱分解炉
内の溶融プラスチック廃棄物中に導入する導管とから成
ることを特徴とする特許請求の範囲第1項記載の処理装
置。
[Claims] 1. Supplying plastic waste into a pyrolysis furnace, heating the pyrolysis furnace to pyrolyze the plastic waste to generate gas, and cooling this gas. In a plastic waste processing apparatus for separating and recovering condensed and liquefied oil, means for promoting vaporization of the plastic waste by increasing the contact area between the plastic waste heated and melted in the pyrolysis furnace and the gas phase. A processing device characterized in that it is attached to a pyrolysis furnace. 2.'' - Claims characterized in that the air distribution promoting means consists of a rotary blade that rotates within the pyrolysis furnace to cause the plastic waste to rise above its surface and then fall. The processing device according to item 1. 3. The vaporization accelerator means comprises a gas source that supplies an inert gas such as nitrogen, and a conduit that introduces the inert sludge from the sludge source into the molten plastic waste in the pyrolysis furnace. A processing device according to claim 1, characterized in that:
JP58169212A 1983-09-16 1983-09-16 Disposal unit for plastic waste Pending JPS6063285A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58169212A JPS6063285A (en) 1983-09-16 1983-09-16 Disposal unit for plastic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58169212A JPS6063285A (en) 1983-09-16 1983-09-16 Disposal unit for plastic waste

Publications (1)

Publication Number Publication Date
JPS6063285A true JPS6063285A (en) 1985-04-11

Family

ID=15882278

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58169212A Pending JPS6063285A (en) 1983-09-16 1983-09-16 Disposal unit for plastic waste

Country Status (1)

Country Link
JP (1) JPS6063285A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999024530A1 (en) * 1997-11-10 1999-05-20 Takeshi Kuroki Apparatus for decomposing waste plastics

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999024530A1 (en) * 1997-11-10 1999-05-20 Takeshi Kuroki Apparatus for decomposing waste plastics
JPH11140225A (en) * 1997-11-10 1999-05-25 Takeshi Kuroki Waste plastic decomposer

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