JPS62195082A - Apparatus for recovering oil from waste resin - Google Patents

Apparatus for recovering oil from waste resin

Info

Publication number
JPS62195082A
JPS62195082A JP61036435A JP3643586A JPS62195082A JP S62195082 A JPS62195082 A JP S62195082A JP 61036435 A JP61036435 A JP 61036435A JP 3643586 A JP3643586 A JP 3643586A JP S62195082 A JPS62195082 A JP S62195082A
Authority
JP
Japan
Prior art keywords
furnace
dry distillation
gas
resin
dry
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
JP61036435A
Other languages
Japanese (ja)
Inventor
Shigeru Tada
多田 滋
Ryoichi Shiroyama
良一 白山
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.)
Hakusan Corp
Original Assignee
Hakusan Corp
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 Hakusan Corp filed Critical Hakusan Corp
Priority to JP61036435A priority Critical patent/JPS62195082A/en
Publication of JPS62195082A publication Critical patent/JPS62195082A/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 Of Solid Wastes (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (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:A waste resin is thermally decomposed in a dry distillation furnace in a state shielded from air, the generated dry distillation gas is cooled and condensed, impurities are removed from the condensed liquid to obtain a fuel oil and the noncondensed gas is washed and again used as a fuel. CONSTITUTION:Roughly crushed waste resin is charged to a dry distillation furnace 5 and heated with a burner in the furnace to effect dry distillation to generate dry distillation gas. The temperature in the furnace is raised to increase the generation of the dry distillation gas until the temperature in the furnace reaches a specific level. The furnace is continuously operated in that state to keep the generation of the dry distillation gas at a definite level. In the transient period before the generation of the dry distillation gas reaches a definite level, the gas is passed through a distillation apparatus 37 placed at a high level and composed mainly of pipes which pass necessary dry distillation gas and block other unnecessary components. The dry distillation gas passed exclusively through the dry distillation apparatus 37 is cooled with a cooler 9 and the condensed liquid is collected in a tank 7. Noncondensed gas is washed and reused as a fuel.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は樹脂系廃棄物から油を回収する装置、詳しくは
樹脂系廃棄物を、乾溜炉で空気を遮断して加熱分解し、
発生した乾溜ガスを冷却凝集させ、液化したものの不純
物を除去精製して燃料用の油とし、凝集しなかったガス
も洗浄により再び燃料として用いられる、樹脂系廃棄物
から油を回収する装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an apparatus for recovering oil from resin-based waste, and more specifically, a device for recovering oil from resin-based waste.
A device that recovers oil from resin-based waste by cooling and coagulating the generated dry distilled gas, removing impurities from the liquefied product and refining it to produce fuel oil, and cleaning the gas that does not coagulate to use it again as fuel. It is.

〔従来技術〕[Prior art]

現在合成樹脂の使用量は真人なものであるが、工場、都
市、一般家庭において生ずるこれら樹脂系廃棄物の量も
真人なものであり、この樹脂系廃葉物は地下埋蔵、焼却
等により処理されている。
Currently, the amount of synthetic resins used is a real amount, but the amount of resin waste generated in factories, cities, and ordinary households is also real. has been done.

しかしながら地下埋蔵にも地域的条件による制約があり
、また焼却処理の場合には有害ガス、黒煙の発生、高温
や発生ガスによる燃焼装置の損傷の大きいことなどのた
めに必ずしも有利な処理方法とは言えなかった。一方、
樹脂系廃棄物は150〜250°Cで熱分解して燃料油
や燃料ガスを生成することが知られているが、このよう
な樹脂系廃棄物の熱分解処理方法は資源再利用の点から
も極めて好ましいものである。樹脂系廃棄物の熱分解方
法としては従来、火床を用いた焼却炉、流動床を用いた
流動炉等があった。
However, underground reserves are also subject to restrictions due to regional conditions, and incineration is not always an advantageous disposal method because it produces harmful gases, black smoke, and can cause significant damage to combustion equipment due to high temperatures and generated gas. I couldn't say it. on the other hand,
It is known that resin-based waste is pyrolyzed at 150 to 250°C to produce fuel oil and fuel gas, but this method of pyrolysis treatment of resin-based waste is difficult from the point of view of resource reuse. is also highly preferred. Conventional methods for thermally decomposing resin waste include incinerators using a fire bed and fluidized furnaces using a fluidized bed.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし前者は樹脂系廃棄物の燃焼の際に発生する高い発
熱量のために火床の損傷が激しく、一般的に長時間の連
続稼動が困難であり、また流動炉では流動媒体の取り扱
いや長い炉長にわたる温度制御が困難であり、また加熱
を防くために炉内への空気供給量の制御に大きな注意を
払わなければならないという煩雑性があった。
However, in the former case, the fire bed is severely damaged due to the high calorific value generated during the combustion of resin-based waste, and it is generally difficult to operate continuously for a long time. It is difficult to control the temperature over the length of the furnace, and there is also the complexity of having to pay great attention to controlling the amount of air supplied into the furnace to prevent overheating.

本発明の目的は、従来の樹脂系廃棄物燃焼処理における
前記のような欠点を、排除し、樹脂系廃棄物から燃料油
を高い収率でかつ連続的に製造することのできる装置を
提供することにある。
An object of the present invention is to eliminate the above-mentioned drawbacks of conventional resin waste combustion treatment and to provide an apparatus that can continuously produce fuel oil from resin waste at a high yield. There is a particular thing.

〔問題点を解決するための手段〕[Means for solving problems]

上記目的を達成するため、本発明は次の装置を提供する
In order to achieve the above object, the present invention provides the following device.

すなわち、本発明は、樹脂系廃棄物を加熱するためのバ
ーナを内蔵し、且つ炉内の残渣を視認するための視認装
置を有する乾溜炉と、この乾溜炉に供給するための樹脂
系廃棄物を破砕する破砕機と、破砕された樹脂系廃棄物
を捕集するサイクロンと、サイクロンから供給された樹
脂系廃棄物を貯蔵するホッパと、ホッパ内の樹脂系廃棄
物を乾溜炉に連続供給する油圧シリンダと、前記乾溜炉
の加熱初期において加熱分解により発生する乾溜ガスの
みを通すため高所に設けられた蒸浄溜装置と、前記乾溜
炉から直接、又は前記蒸溜装置を経て導かれた乾溜ガス
を冷却する冷却器と、冷却により凝集した凝集液ならび
に凝集しなかったガスを集めるタンクと、タンクの凝集
液の不純物を除去精製し油として地下のオイルタンクに
供給するダストセパレータと、前記タンク内の凝集しな
かったガスをアルカリ洗浄するスクラバと、アルカリ洗
浄されたガスをさらに水洗いする洗浄器とを備え、前記
蒸溜装置は、管を主体とじコック弁とマニホールドとを
有することを特徴とする、樹脂系廃棄物から油を回収す
る装置である。
That is, the present invention provides a dry distillation furnace having a built-in burner for heating resin waste and a visual recognition device for visually checking the residue inside the furnace, and a dry distillation furnace for supplying resin waste to the dry distillation furnace. A crusher that crushes resin waste, a cyclone that collects the crushed resin waste, a hopper that stores the resin waste supplied from the cyclone, and a continuous supply of the resin waste in the hopper to the dry distillation furnace. A hydraulic cylinder, a distillation device installed at a high place to pass only the dry distillation gas generated by thermal decomposition during the initial heating stage of the dry distillation furnace, and a dry distillation device led directly from the dry distillation furnace or through the distillation device. A cooler that cools the gas, a tank that collects the flocculated liquid that has condensed by cooling and the gas that has not condensed, a dust separator that removes impurities from the flocculated liquid in the tank, refines it, and supplies it as oil to an underground oil tank, and the tank. The distillation apparatus is characterized in that it is equipped with a scrubber that cleans the unagglomerated gas in the distillation tank with an alkali, and a washer that washes the gas that has been washed with the alkali with water, and the distillation apparatus is mainly composed of a pipe and has a cock valve and a manifold. , a device for recovering oil from resin-based waste.

〔作用〕[Effect]

先ず粗砕された樹脂系廃棄物を乾溜炉内に入れ、同炉内
のバーナで加熱するので、熱交換が効率よく行われ短時
間で乾溜が始まり、乾溜ガスが発生し始める。
First, crushed resin waste is placed in a dry distillation furnace and heated by a burner inside the furnace, so heat exchange is performed efficiently and dry distillation begins in a short time, and dry distillation gas begins to be generated.

さらに、炉内温度を上げていくにつれて乾溜ガスも発生
量が増加し、炉内温度が所定の高さになった状態で本装
置は連続運転が行われ、乾溜ガスの発生も一定量が保た
れるようになる。
Furthermore, as the temperature inside the furnace increases, the amount of dry distillation gas generated also increases, and when the temperature inside the furnace reaches a predetermined level, the device is operated continuously, and the amount of dry distillation gas generated remains constant. It starts to sag.

この炉内温度が所定の高さに達するまでの過度的な段階
では、炉内の樹脂系廃棄物はまだ温度不充分なため、充
分に加熱分解されない粘性の液状いいかえればドロドロ
の状態のものが殆どで、これと少量の乾溜ガスが炉内に
併存し、炉内温度上昇につれて前記加熱分解が進み、乾
溜ガスの量が次第に増加してくる。
At this extreme stage until the temperature inside the furnace reaches a predetermined level, the resin waste inside the furnace is not sufficiently heated, so it becomes a viscous liquid that is not fully decomposed by heat. In most cases, this and a small amount of dry distillation gas coexist in the furnace, and as the temperature inside the furnace increases, the thermal decomposition proceeds and the amount of dry distillation gas gradually increases.

そこで、この乾溜の初期、すなわち乾溜ガスが一定量に
達するまでの過度期に、必要な乾溜ガスのみを通し、他
の不要なものは通さないために蒸留装置が設けられてい
る。
Therefore, at the beginning of this dry distillation, that is, during the transient period until a certain amount of dry distilled gas is reached, a distillation device is provided in order to pass only the necessary dry distilled gas and not pass any other unnecessary gas.

蒸留装置はパイプを主体とするもので高所に設けられて
いるため、乾溜ガスのみが通り得るもので、したがって
、この時点では、乾溜炉から出る乾溜ガスは、すべて蒸
留装置を経由するように、乾溜炉と冷却器を直接結ぶパ
イプはコックを閉じておく。
Since the distillation equipment is mainly made of pipes and is installed at a high place, only the dry distillation gas can pass through it. Therefore, at this point, all the dry distillation gas coming out of the dry distillation furnace has to go through the distillation equipment. , keep the cock of the pipe that directly connects the dry distillation furnace and the cooler closed.

このようにして蒸留装置のみを経た乾溜ガスは冷却器に
おいて冷却され、凝集してタンクに集められる。
The dry distilled gas that has passed through the distillation device in this manner is cooled in a cooler, coagulated, and collected in a tank.

なお、前記乾溜炉と冷却器を結ぶパイプは、乾溜炉内の
温度が一定の高さに達した後は、コックを開いて乾溜ガ
スが直接冷却器に導かれることとなり、前記藤留装置経
由のものとあわせて大量の5乾溜ガスが冷却され、凝集
してタンクに集められる。
In addition, after the temperature inside the dry distillation furnace reaches a certain level, the pipe that connects the dry distillation furnace and the cooler is opened to open the cock and the dry distillation gas is directly led to the cooler, and the dry distillation gas is directly led to the cooler via the Fujitome device. A large amount of 5 dry distillate gas is cooled, condensed and collected in a tank.

タンク内には凝集液化したものと、凝集しきれなかった
ガスとが集められる。
The flocculated and liquefied gas and the gas that could not be flocculated are collected in the tank.

このうち、凝集液はダストセパレータで不純物を除去精
製されて燃料用の油となり、地下のオイルタンクに貯蔵
される。
Among these, the flocculated liquid is purified by removing impurities in a dust separator to become fuel oil, which is stored in an underground oil tank.

また、前記タンクに凝集液とともに集められた凝集しき
れなかったガスは、タンク上部からスクラソパに導かれ
、苛性ソーダにより中和されてクリーンガスとなり、さ
らに、洗浄器で水洗いされた後、前記炉内のバーナに送
られ燃料ガスとして再利用される。
In addition, the uncoagulated gas collected in the tank together with the coagulating liquid is led from the top of the tank to the scrubber, where it is neutralized with caustic soda and becomes clean gas.Furthermore, after being washed with water in a washer, it is placed inside the furnace. The gas is sent to the burner and reused as fuel gas.

一方、破砕機は、運転中の乾溜炉に樹脂系廃棄物を連続
供給するために細かく破砕し、この破砕された樹脂系廃
棄物はサイクロンによって補集された後、ホッパに貯蔵
される。
On the other hand, the crusher crushes the resin waste into small pieces in order to continuously supply the resin waste to the operating dry distillation furnace, and after the crushed resin waste is collected by a cyclone, it is stored in a hopper.

ホッパ内の樹脂系廃棄物は油圧シリンダによって炉内へ
の空気を遮断しながら連続的に炉内に供給される。
The resin waste in the hopper is continuously fed into the furnace by a hydraulic cylinder while blocking air into the furnace.

炉内は高温に加熱され、外部よりも気圧が常に高いため
、樹脂系廃棄物が炉内に供給されるときにも外部から空
気が流入するのを防いで乾溜が合理的に行われる。
The inside of the furnace is heated to a high temperature and the pressure is always higher than the outside, so even when resin waste is fed into the furnace, air is prevented from flowing in from the outside and dry distillation is carried out rationally.

乾溜炉内の残渣を視認する内部視認装置は、カラーライ
トにより赤色系統の波長の長い光をあてて透明を良好な
状態とし、炉内の焔をとおして残渣量をテレビカメラで
視認する。これにより、炉の連続運転を中止して炉内の
残渣を排出するための適切な時期を決めることができる
The internal visual inspection device that visually checks the residue inside the dry distillation furnace uses colored lights to illuminate red light with long wavelengths to make it transparent, and then uses a television camera to visually check the amount of residue through the flame inside the furnace. This makes it possible to determine an appropriate time to stop continuous operation of the furnace and to discharge the residue in the furnace.

(実施例) 本発明の実施例について、以下、図面に従って本発明の
構成が実際上どのように具体化されるかをその作用とと
もに説明する。
(Example) Regarding an example of the present invention, how the configuration of the present invention is actually embodied will be described below with reference to the drawings, along with its operation.

第1図は本発明の一実施例の構成説明図で、1は樹脂系
廃棄物を10乃至15龍位に破砕する破砕機、2は破砕
された前記樹脂系廃棄物を捕集するサイクロン3は囲い
の中に前記サイクロン2から補給された樹脂系廃棄物を
貯蔵し、下部の開口部から少しずつ出るようにしたホッ
パ、4はホッパからの樹脂系廃棄物を、空気を遮断しな
がら乾溜炉内へ連続的に供給する油圧シリンダである。
FIG. 1 is an explanatory diagram of the configuration of an embodiment of the present invention, in which 1 is a crusher that crushes resin waste into 10 to 15 pieces, 2 is a cyclone 3 that collects the crushed resin waste. 4 is a hopper that stores the resin waste supplied from the cyclone 2 in an enclosure and allows it to come out little by little from the opening at the bottom. 4 is a dry distillation system for the resin waste from the hopper while blocking air. This is a hydraulic cylinder that continuously supplies water into the furnace.

5ば乾溜炉で、第2図の断面図で示すように炉体はひと
つの密閉容器として形成され、円筒状の周壁15の外側
は耐火レンガ16と外板17で覆われている。
5 is a dry distillation furnace, and as shown in the cross-sectional view in FIG.

また、周壁15の上部には上部蓋18、下部には下部蓋
19があり、いづれも断熱材20で保温性が保たれる。
Further, there is an upper lid 18 on the upper part of the peripheral wall 15, and a lower lid 19 on the lower part, both of which are kept warm by a heat insulating material 20.

上部M18は上部シリンダ21によりシリンダアーム2
3を介して開閉される。乾溜炉が加熱されていないとき
の、樹脂系廃棄物の初期投入は、この上部蓋18をあけ
て行われるので細かくする必要はなり、500m11位
の粗砕で充分である。
The upper M18 is connected to the cylinder arm 2 by the upper cylinder 21.
It is opened and closed via 3. When the dry distillation furnace is not heated, resin-based waste is initially charged by opening the upper lid 18, so there is no need to crush it into pieces, and coarse crushing of about 500 m1 is sufficient.

下部蓋19は、下部シリンダ22により開閉される下部
蓋19を開くことにより炉内の残渣が炉外に排出される
When the lower lid 19 is opened and closed by the lower cylinder 22, the residue inside the furnace is discharged to the outside of the furnace.

24はバーナ管で、炉の中央に水平に設けられ、一端が
周壁15から外部に現れている。
A burner tube 24 is provided horizontally in the center of the furnace, and one end thereof is exposed from the peripheral wall 15 to the outside.

バーナ管24の他端は、第3図に示すように箱部材25
.下部箱部材26.管29.前部箱部材27.管30上
部箱部材28.管31,32.33と連なり、管33の
終端部33aは炉の周壁15を貫いて外部煙道(図示せ
ず)につながる。
The other end of the burner tube 24 is connected to a box member 25 as shown in FIG.
.. Lower box member 26. Tube 29. Front box member 27. Pipe 30 upper box member 28. Continuing with the tubes 31, 32, 33, the terminal end 33a of the tube 33 passes through the peripheral wall 15 of the furnace and leads to an external flue (not shown).

ここで、箱部材は管と管を接続し、且つ、管を支持する
台としての役割を果たし、管は熱交換器の役割を果たし
ている。
Here, the box member connects the tubes and serves as a stand for supporting the tubes, and the tubes serve as a heat exchanger.

この熱交換器の主役としての、管29.30は折り返す
形状で、2本づつ並列に設け、熱交換が充分に行われる
ようしである。
The tubes 29 and 30, which play the main roles in this heat exchanger, have a folded shape and are arranged two in parallel to ensure sufficient heat exchange.

この管29.30は、断面を角形、楕円形などの非円形
として筒状の表面積を大きくし、熱交換の効率をいっそ
うアンプすることとしてもよく、最も一般的な円形とし
て、加工し易く丈夫で廉価なものとしてもよい。これら
の加熱部分はバナジュウム鋼などの耐火材でつくられて
いる。
The tubes 29 and 30 may have a non-circular cross section such as a square or ellipse to increase the cylindrical surface area and further increase the efficiency of heat exchange, and the most common round tube is easy to process and durable. It can also be a cheap one. These heating parts are made of refractory materials such as vanadium steel.

第2図の乾溜炉の上部の34はテレビカメラで、カラー
ライト35と組み合わせて炉内部を外から視る視認装置
36を構成する。
Reference numeral 34 at the top of the dry distillation furnace in FIG. 2 is a television camera, which in combination with color lights 35 constitutes a visual recognition device 36 for viewing the inside of the furnace from the outside.

本発明は長時間連続運転が可能なため、運転中に炉内の
残渣量を視認し、残渣を炉底から排出するために運転を
中止する適切な時期を決定する必要がある。残渣量は投
入される樹脂系の種類によって異なり−・定しないから
である。    □このカラーライト35は、焔をとお
して残渣量を視認できるようどこ、波長の長い赤色系統
の光を用い透明度を高め、テレビカメラ34を側面から
補佐している。“ 第1図の37は蒸溜装置で、乾溜炉の加熱初期において
加熱分解により発生する乾溜ガスのみをとおすように高
所に設けられたもので、それぞれ開閉するためのコック
弁40,41 と、分配接続用のマニホール42.’4
3と、管44.45とによって構成される。
Since the present invention is capable of continuous operation for a long period of time, it is necessary to visually check the amount of residue in the furnace during operation and determine an appropriate time to stop operation in order to discharge the residue from the bottom of the furnace. This is because the amount of residue varies depending on the type of resin system input and is not fixed. □This color light 35 uses red light with a long wavelength to increase transparency so that the amount of residue can be visually recognized through the flame, and assists the television camera 34 from the side. 1 is a distillation device, which is installed at a high place to allow only the dry distillation gas generated by thermal decomposition to pass through during the initial heating stage of the dry distillation furnace, and includes cock valves 40 and 41 for opening and closing, respectively. Manifole for distribution connection 42.'4
3 and tubes 44 and 45.

マニホールド43は、乾溜炉5から管46によって接続
され、管46にはコック弁47が備えられている。
The manifold 43 is connected to the dry distillation furnace 5 by a pipe 46, and the pipe 46 is equipped with a cock valve 47.

乾溜ガスの出はじめは、炉内温度がまだ充分に上がって
おらず、加熱分解が不充分な粘性の液状゛ 態と乾溜ガ
スが併存するので、コック弁47を閉じて粘性の液状体
が簀46からマニホールド43を経て冷却器へ流入する
のを防止する。
When the dry distillation gas starts to come out, the temperature inside the furnace has not yet risen sufficiently, and the dry distillation gas coexists with a viscous liquid state that has not been thermally decomposed sufficiently, so the cock valve 47 is closed and the viscous liquid remains. 46 through the manifold 43 and into the cooler.

このとき、蒸留装置37のコック弁40,41は開いて
おり、乾溜ガスのみが蒸留装置37を経て冷却器゛に導
かれる。
At this time, the cock valves 40 and 41 of the distillation device 37 are open, and only the dry distilled gas is guided through the distillation device 37 to the cooler.

ここで、管38.39の2木が設けであるのは、乾溜ガ
ス発生量や質を考え、乾溜ガス発生の当初には、最上部
のコック弁40のみを開は才上質少量の乾溜ガスのみを
通し、乾溜炉内の温度」1昇に拝い、コック弁41を開
いて発するガスの量の増加に対応させ、所定温度゛に達
した後はコック弁47を開いて蒸留装置を経由しない直
接のルールを開き、大量の乾溜ガスが冷却器へ送られる
ようにしたものである。なお、実施例では蒸溜装置管3
8.39の2本で示したが、必要に応じて本数を増減し
てもよい。
The reason why the two pipes 38 and 39 are provided here is to consider the quantity and quality of the dry distilled gas generated.At the beginning of generating dry distilled gas, it is not possible to open only the cock valve 40 at the top. Once the temperature inside the dry distillation furnace has increased by 1, the cock valve 41 is opened to accommodate the increase in the amount of gas being emitted.After reaching a predetermined temperature, the cock valve 47 is opened to allow the gas to pass through the distillation equipment. The direct rule that does not occur is opened, and a large amount of dry distilled gas is sent to the cooler. In addition, in the embodiment, the distillation apparatus pipe 3
8.39 is shown as two, but the number may be increased or decreased as necessary.

第1図の6は冷却器で、前記乾溜炉5で乾溜されてなる
乾溜ガスを蒸留装置を経て、または直接に導いて冷却す
る水冷装置である。
Reference numeral 6 in FIG. 1 denotes a cooler, which is a water cooling device that cools the dry distilled gas that has been dry distilled in the dry distillation furnace 5 by introducing it through the distillation apparatus or directly.

乾溜ガスは冷却により凝集し、凝集液となってタンク7
に集められる。
The dry distilled gas coagulates as it cools, becomes a coagulated liquid, and enters tank 7.
are collected in.

タン多7には凝集しきれずに乾溜ガスのままの気′体も
上部に集められている。
In the tank 7, gases that have not completely condensed and remain as dry distilled gas are also collected in the upper part.

タンク7に集′められた前記凝集液は、タンク下部から
ダストセパレータ10に導かれて不純物を除去精製され
、燃料用の油となって、地下のオイルタンク11に導か
れ、貯蔵され、出荷を待つこととなる。
The flocculated liquid collected in the tank 7 is led from the bottom of the tank to the dust separator 10, where it is purified to remove impurities and becomes fuel oil, which is led to the underground oil tank 11, where it is stored and shipped. will have to wait.

一方、タ′ンク7内上部に集められた凝集しきれなかっ
たガスは、スクラバー8に導かれ、アルカリ洗浄され中
和される。スクラバー8では、10%の苛性ソーダ溶液
のシャワーで洗浄がおこなわれる。         
  □−・ ここでアルカリ洗浄されたガスは、さらに滉浄器9に導
かれ、今度は水洗いされる。
On the other hand, the uncoagulated gas collected in the upper part of the tank 7 is led to a scrubber 8, where it is washed with alkali and neutralized. In the scrubber 8, cleaning is performed with a shower of 10% caustic soda solution.
□-- The gas that has been washed with alkali here is further led to the purifier 9, where it is washed with water.

゛前記アルカリ洗浄の際、□苛性ソニダの付着した  
Q 部分も、この水洗いによって一層きれいな無公害なガス
となり、前記乾溜炉のバーナ12に供給され重油に代っ
て燃料を自給することができる。  ′なお、ガスが少
量のときは煙突(図示せず)から外気中に排出されるが
、前述のように充分に洗浄されており公害のおそれはな
い。
゛During the above alkaline cleaning, □ Caustic sonida adhering
By washing with water, the Q portion also becomes a cleaner, non-polluting gas, which is supplied to the burner 12 of the dry distillation furnace and can be self-sufficient as a fuel in place of heavy oil. 'In addition, when the gas is small, it is discharged into the outside air from the chimney (not shown), but as mentioned above, it is thoroughly cleaned and there is no risk of pollution.

本発明はこのように構成されているので、この装置を運
転するには、先ず最初に、乾溜炉5の下部蓋19を下部
シリンダ22で油圧により開き、炉内   ′の残渣を
排出した後、下部蓋18を上部シリンダ21で油圧によ
り開き、粗砕された樹脂系廃棄物をここから炉内に初期
投入する。
Since the present invention is configured in this way, in order to operate this device, first, the lower lid 19 of the dry distillation furnace 5 is opened by hydraulic pressure using the lower cylinder 22, and after the residue inside the furnace is discharged, The lower lid 18 is hydraulically opened by the upper cylinder 21, and the crushed resin waste is initially introduced into the furnace from there.

バーナ12はコンプレッサ14からの圧縮空気の介在で
重油タンク13から重油が供給され、炉内を加熱し始め
る。
The burner 12 is supplied with heavy oil from the heavy oil tank 13 through the intervention of compressed air from the compressor 14, and begins to heat the inside of the furnace.

加熱後約30分で乾溜が始まるので、そのガスを前記バ
ーナ12に導いて重油の代わりに燃料を自給する。
Dry distillation begins approximately 30 minutes after heating, so the gas is guided to the burner 12 to provide self-sufficient fuel in place of heavy oil.

約1時間で炉内温度は150°Cに達し、このときから
、供給する樹脂系廃棄物は、前記粗砕でなく、破砕機1
により10〜15鰭の細かいものとし、破砕機1〜サイ
クロン2〜ホツパ3〜油圧シリンダ4〜乾溜炉5という
経路で自動的に炉内に供給され、本装置は連続運転稼動
される。
The temperature inside the furnace reaches 150°C in about 1 hour, and from this point on, the resin waste to be supplied is not coarsely crushed, but is crushed by the crusher 1.
The particles are finely divided into 10 to 15 fins, and are automatically fed into the furnace through the route of crusher 1 - cyclone 2 - hopper 3 - hydraulic cylinder 4 - dry distillation furnace 5, and this apparatus is operated continuously.

炉内は高温加熱され、常に微圧を有し、外部がら空気が
入りにくい状態にあるので炉が爆発するおそれはなく、
廃棄物とバーナは双方とも炉内にあって熱効率が極めて
よい。
The inside of the furnace is heated to a high temperature and always has a slight pressure, making it difficult for air to enter from the outside, so there is no risk of the furnace exploding.
Both the waste and the burner are inside the furnace, which provides extremely high thermal efficiency.

炉内の残渣は連続運転中においても、内部視認装置36
によって視認することができ、残渣量が多くなって炉外
へ排出すべき適切な時期がわかるので装置の安全かつ効
率的な運転が可能である。
Even during continuous operation, the residue inside the furnace can be checked by the internal visual inspection device 36.
This allows for safe and efficient operation of the equipment, since the amount of residue can be visually confirmed and the appropriate time to discharge it from the furnace can be determined when the amount of residue has increased.

乾溜炉5で乾溜されたガスは、炉内が所定の温度に達す
るまでの間は蒸留装置37のコック弁40゜41のうち
高い位置の方のコック弁40を開き、ガスの量が次第に
増加するのを待って次のコック弁41を開くので、ガス
の品質を保ちつつ、量の増加に対応できる。
The gas that has been dry distilled in the dry distillation furnace 5 is kept open until the inside of the furnace reaches a predetermined temperature by opening the higher cock valve 40 of the distillation device 37 and gradually increasing the amount of gas. Since the next cock valve 41 is opened after waiting for this, it is possible to respond to an increase in the amount of gas while maintaining the quality of the gas.

そして、炉内温度が所定の高さに達した後は、炉から直
接冷却器6に通ずるコック弁47を開き、乾溜ガスを大
量に冷却器6に導く。
After the temperature inside the furnace reaches a predetermined level, the cock valve 47 that directly connects the furnace to the cooler 6 is opened, and a large amount of dry distilled gas is guided to the cooler 6.

冷却器6で冷却されたガスはタンク7に導かれて凝集液
として集められ、そこからダストセパレータ10に導か
れて不純物が除去され、燃料用のオイルとなって地下の
オイルタンク11に貯蔵されて出荷を待つ。
The gas cooled by the cooler 6 is led to a tank 7 where it is collected as a coagulated liquid, and from there, it is led to a dust separator 10 to remove impurities, and is converted into fuel oil and stored in an underground oil tank 11. and wait for shipment.

一方、前記タンク7には、冷却によっても凝集しきれな
かったガスが上部に集められており、このガスはスクラ
バー8でアルカリ洗浄され、さらに洗浄器9で水洗いさ
れた後、本装置運転用の燃料として前記バーナ12に導
かれる。なお、このガスが少量の場合は煙突(図示せず
)から排出される。
On the other hand, in the tank 7, gas that could not be coagulated even after cooling is collected in the upper part, and this gas is washed with alkali in a scrubber 8 and further washed with water in a washer 9, and then used for operation of the device. It is led to the burner 12 as fuel. Note that if this gas is small, it will be exhausted from a chimney (not shown).

〔発明の効果〕〔Effect of the invention〕

本発明は、乾溜炉内にバーナを設けて炉内の樹脂系の廃
棄物を直接加熱するので熱交換が極めて効率よく行われ
る。
In the present invention, a burner is provided in the dry distillation furnace to directly heat the resin-based waste in the furnace, so that heat exchange is performed extremely efficiently.

また、装置運転中は、破砕機、サイクロン、ホッパ、油
圧シリンダにより、廃棄物が自動的に速続投入できるこ
とから、乾溜が連続的に行われ、炉の使用効率は、時間
的にも熱利用の面においてもすぐれている。
In addition, while the equipment is operating, waste can be automatically and rapidly fed into the crusher, cyclone, hopper, and hydraulic cylinder, so dry distillation is performed continuously, and the efficiency of furnace usage is reduced both in terms of time and heat utilization. It is also excellent in terms of

さらに炉内には、高温加熱による微圧が常に存在するの
で廃棄物連続供給の際、空気が流入しないから炉が爆発
するなどのおそれがない。
Furthermore, since there is always a slight pressure inside the furnace due to high-temperature heating, there is no risk of the furnace exploding because air does not flow in when waste is continuously fed.

加えて炉の上部には、テレビカメラとカラーライトを組
合わせた視認装置が設けられているので運転中の炉内の
残渣量が視認でき、残渣排出の適切な時期が決定でき、
安全かつ効率的な連続運転稼動による燃料用油の増産が
可能である。
In addition, a viewing device that combines a television camera and color light is installed at the top of the furnace, so the amount of residue inside the furnace can be visually checked during operation, and the appropriate time to discharge the residue can be determined.
It is possible to increase production of fuel oil through safe and efficient continuous operation.

その上乾溜炉と冷却との間の高所に蒸留装置を設けたの
で、乾溜初期の炉内温度が所定の温度に達する前から上
質の乾溜ガスのみを冷却器に導くことができ、製品の品
質が向上する。
In addition, since the distillation equipment is installed at a high place between the dry distillation furnace and the cooling unit, only high-quality dry distillation gas can be led to the cooler even before the temperature inside the furnace reaches a predetermined temperature during the initial stage of dry distillation. Quality improves.

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

第1図は本発明の一実施例の構成説明図、第2図は第1
図の乾溜炉の断面説明図、第3図は炉内の要部説明図、
第4図は第1図の蒸留装置の説明図である。 1・・・・・・破砕機、 2・・・・・・サイクロン、 3・・・・・・ホッパ、 4・・・・・・油圧シリンダ、 5・・・・・・乾溜炉、 6・・・・・・冷却器、 7・・・・・・タンク、 8・・・・・・スクラバー、 9・・・・・・洗浄器、  。 10・・・・・・ダストセパレータ、 11・・・・・・オイルタンク、 34・・・・・・テレビカメラ、 35・・・・・・カラーライト、 36・・・・・・視認装置、 37・・・・・・蒸留装置。 出 願 人  白山工業株式会社 代理人弁理士  鈴 木 淳 也 第3図 114 ji!1
FIG. 1 is an explanatory diagram of the configuration of one embodiment of the present invention, and FIG.
Figure 3 is an explanatory cross-sectional diagram of the dry distillation furnace, and Figure 3 is an explanatory diagram of the main parts inside the furnace.
FIG. 4 is an explanatory diagram of the distillation apparatus shown in FIG. 1. 1... Crusher, 2... Cyclone, 3... Hopper, 4... Hydraulic cylinder, 5... Dry distillation furnace, 6. ...Cooler, 7..Tank, 8..Scrubber, 9..Cleaning device. 10...Dust separator, 11...Oil tank, 34...TV camera, 35...Color light, 36...Visibility device, 37... Distillation equipment. Applicant: Hakusan Kogyo Co., Ltd. Representative Patent Attorney Junya Suzuki Figure 3 114 ji! 1

Claims (1)

【特許請求の範囲】[Claims] 樹脂系廃棄物を加熱するためのバーナを内蔵し、且つ炉
内の残渣を視認するための視認装置を有する乾溜炉と、
この乾溜炉に樹脂系廃棄物を供給するために破砕する破
砕機と、破砕された樹脂系廃棄物を捕集するサイクロン
と、サイクロンから供給された樹脂系廃棄物を貯蔵する
ホッパと、このホッパ内の樹脂系廃棄物を乾溜炉に連続
供給する油圧シリンダと、前記乾溜炉の加熱初期におい
て加熱分解により発生する乾溜ガスのみを通すため高所
に設けられた蒸溜装置と、前記乾溜炉から直接、又は前
記蒸溜装置を経て導かれた乾溜ガスを冷却する冷却器と
、冷却により凝集した凝集液ならびに凝集しなかったガ
スを集めるタンクと、タンクの凝集液の不純物を除去精
製し油として地下のオイルタンクに供給するダストセパ
レータと、前記タンク内の凝集しなかったガスをアルカ
リ洗浄するスクラバと、アルカリ洗浄されたガスをさら
に水洗いする洗浄器とを備え、前記蒸溜装置は、管を主
体としコック弁とマニホールドを有することを特徴とす
る、樹脂系廃棄物から油を回収する装置。
A dry distillation furnace that has a built-in burner for heating resin-based waste and a visual recognition device for visually checking the residue inside the furnace;
A crusher that crushes resin waste to supply it to the dry distillation furnace, a cyclone that collects the crushed resin waste, a hopper that stores the resin waste supplied from the cyclone, and a hopper that stores the resin waste supplied from the cyclone. A hydraulic cylinder that continuously supplies the resin-based waste in the dry distillation furnace to the dry distillation furnace, a distillation device installed at a high place to pass only the dry distillation gas generated by thermal decomposition during the initial heating stage of the dry distillation furnace, and a distillation device that directly supplies the resin waste from the dry distillation furnace , or a cooler for cooling the dry distilled gas led through the distillation equipment, a tank for collecting the flocculated liquid that has coagulated by cooling and the gas that has not coagulated, and a condensed liquid in the tank that is purified by removing impurities and then stored underground as oil. The distillation device is equipped with a dust separator that supplies the oil tank, a scrubber that cleans the unagglomerated gas in the tank with alkali, and a washer that washes the alkali-cleaned gas with water. A device for recovering oil from resin-based waste, characterized by having a valve and a manifold.
JP61036435A 1986-02-20 1986-02-20 Apparatus for recovering oil from waste resin Pending JPS62195082A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61036435A JPS62195082A (en) 1986-02-20 1986-02-20 Apparatus for recovering oil from waste resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61036435A JPS62195082A (en) 1986-02-20 1986-02-20 Apparatus for recovering oil from waste resin

Publications (1)

Publication Number Publication Date
JPS62195082A true JPS62195082A (en) 1987-08-27

Family

ID=12469733

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61036435A Pending JPS62195082A (en) 1986-02-20 1986-02-20 Apparatus for recovering oil from waste resin

Country Status (1)

Country Link
JP (1) JPS62195082A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100765330B1 (en) 2006-06-07 2007-10-09 (주)대명엔지니어링 Apparatus and method for reprocessing of waste materials using pyrolysis processwastes

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4929271A (en) * 1972-07-15 1974-03-15
JPS5121437A (en) * 1974-08-15 1976-02-20 Sharp Kk
JPS5237510A (en) * 1975-09-19 1977-03-23 Nippon Steel Corp Dephosphorization method of molten cast iron
JPS5345302A (en) * 1976-10-05 1978-04-24 Fujikura Ltd Preparation of hydrocarbon oils from crosslinked polyethylene wastes
JPS5357393A (en) * 1976-11-02 1978-05-24 Fuji Electric Co Ltd Reactor observation system of nuclear reactor
JPS5379712A (en) * 1976-12-24 1978-07-14 Kawasaki Steel Co Method of operating blast furnace by quantitive detection of fluidized zone in furnace
JPS5550084A (en) * 1978-10-07 1980-04-11 Konosuke Hara Treatment of hydrocarbon waste with thermal decomposition and its device
JPS59102984A (en) * 1982-12-02 1984-06-14 Akira Kameda Method for dry distillation treatment of organic waste

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4929271A (en) * 1972-07-15 1974-03-15
JPS5121437A (en) * 1974-08-15 1976-02-20 Sharp Kk
JPS5237510A (en) * 1975-09-19 1977-03-23 Nippon Steel Corp Dephosphorization method of molten cast iron
JPS5345302A (en) * 1976-10-05 1978-04-24 Fujikura Ltd Preparation of hydrocarbon oils from crosslinked polyethylene wastes
JPS5357393A (en) * 1976-11-02 1978-05-24 Fuji Electric Co Ltd Reactor observation system of nuclear reactor
JPS5379712A (en) * 1976-12-24 1978-07-14 Kawasaki Steel Co Method of operating blast furnace by quantitive detection of fluidized zone in furnace
JPS5550084A (en) * 1978-10-07 1980-04-11 Konosuke Hara Treatment of hydrocarbon waste with thermal decomposition and its device
JPS59102984A (en) * 1982-12-02 1984-06-14 Akira Kameda Method for dry distillation treatment of organic waste

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100765330B1 (en) 2006-06-07 2007-10-09 (주)대명엔지니어링 Apparatus and method for reprocessing of waste materials using pyrolysis processwastes

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