JPH06328441A - Separating equipment for pyrolysis oil and carbon residue - Google Patents
Separating equipment for pyrolysis oil and carbon residueInfo
- Publication number
- JPH06328441A JPH06328441A JP13888793A JP13888793A JPH06328441A JP H06328441 A JPH06328441 A JP H06328441A JP 13888793 A JP13888793 A JP 13888793A JP 13888793 A JP13888793 A JP 13888793A JP H06328441 A JPH06328441 A JP H06328441A
- Authority
- JP
- Japan
- Prior art keywords
- carbon residue
- oil
- pyrolysis oil
- pyrolysis
- separating equipment
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Centrifugal Separators (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)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は廃プラスチックの油化処
理設備に関し、特に熱分解した後の熱分解油からカーボ
ン残渣を分離する設備に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to equipment for oil treatment of waste plastics, and more particularly to equipment for separating carbon residue from pyrolyzed oil after pyrolysis.
【０００２】[0002]
【従来の技術】オイルショック以来、プラスチック廃棄
物を再資源化する試みとして、熱分解を基本にした油化
処理技術の研究が盛んに行われてきた。プラスチックは
炭素や水素原子が数千〜数万の単位で鎖状につながった
構造をしているが、加熱により熱分解油とカーボン残渣
に分解される。カーボン残渣は配管内壁に付着成長して
コーキング（管の閉塞）の原因となり、連続運転ができ
なかった。2. Description of the Related Art Since the oil shock, as an attempt to recycle plastic waste, oil-based processing technology based on thermal decomposition has been actively researched. Plastic has a structure in which carbon and hydrogen atoms are connected in a unit of thousands to tens of thousands, but it is decomposed into pyrolytic oil and carbon residue by heating. The carbon residue adhered and grew on the inner wall of the pipe, causing caulking (clogging of the pipe), which made continuous operation impossible.
【０００３】この問題を解決するため、特開昭５１−１
１５５７８号公報には、横型の熱分解槽を流動層炉で囲
繞し、熱分解槽にて発生するカーボン残渣を熱媒体に付
着させた状態で流動層へ循環流入させ、その後、該流動
層炉で熱媒体に付着したカーボン残渣を燃焼させて無害
化すると共に熱媒体を再生することが記載されている。To solve this problem, JP-A-51-1
In Japanese Patent No. 15578, a horizontal pyrolysis tank is surrounded by a fluidized bed furnace, and carbon residues generated in the pyrolysis tank are circulated and flowed into the fluidized bed while being attached to a heating medium, and then the fluidized bed furnace It is described that the carbon residue attached to the heat medium is burned to make it harmless and the heat medium is regenerated.
【０００４】[0004]
【発明が解決しようとする課題】しかし、特開昭５１−
１１５５７８号公報記載の技術は、熱分解槽中の液状炭
化水素までも燃焼させてしまうものであるため、流動層
炉での燃焼によりカーボン残渣のみでなくカーボン残渣
に含まれる油も同時に燃焼してしまい、油の収率が低下
する問題があった。However, JP-A-51-
Since the technique described in Japanese Patent No. 115578 burns even liquid hydrocarbons in the thermal decomposition tank, not only the carbon residue but also the oil contained in the carbon residue is simultaneously burned by the combustion in the fluidized bed furnace. Therefore, there is a problem that the yield of oil decreases.
【０００５】この他に重力沈降式の分離機が考えられる
が、これによるとカーボン残渣の分離効率が低く、管の
閉塞を完全に防止することができない。また、連続的に
抜出しができず、バッチ式となっている。さらに、抜出
し後のカーボン残渣は高温のため、空気に触れると発火
する危険がある。In addition to this, a gravity sedimentation type separator can be considered. However, according to this, the separation efficiency of carbon residue is low and it is not possible to completely prevent clogging of the pipe. Moreover, it is a batch type because it cannot be continuously withdrawn. Furthermore, since the carbon residue after extraction is hot, there is a risk of ignition if exposed to air.
【０００６】本発明はカーボン残渣の分離を効率良く行
い、その抜出しを連続的かつ安全に行う設備を提供する
ものである。The present invention provides equipment for efficiently separating carbon residue and continuously and safely removing the carbon residue.
【０００７】[0007]
【課題を解決するための手段】本発明の要旨は、廃プラ
スチックの熱分解によって発生する熱分解油とカーボン
残渣との分離設備において、遠心分離機の一方に熱分解
油とカーボン残渣の供給口を設け、該遠心分離機の他方
に分離後の熱分解油の排出口を設けると共に、前記遠心
分離機の下部に分離されたカーボン残渣の水冷式排出手
段を設けたことを特徴とする熱分解油とカーボン残渣と
の分離設備である。SUMMARY OF THE INVENTION The gist of the present invention is, in a facility for separating pyrolysis oil and carbon residue generated by the pyrolysis of waste plastic, one of the centrifuges to supply the pyrolysis oil and carbon residue. And a discharge port for the pyrolysis oil after separation is provided on the other side of the centrifuge, and a water-cooled discharge means for the separated carbon residue is provided at the bottom of the centrifuge. Separation equipment for oil and carbon residue.
【０００８】[0008]
【作用】熱分解した後の熱分解油とカーボン残渣は供給
口から遠心分離機に入り、遠心力により分離される。比
重の大きいカーボン残渣は遠心分離機の下部に落ち、水
冷式排出手段で連続的に切り出され系外に排出される。
また、水冷式排出手段に付けた水冷装置により冷却され
たカーボン残渣は発火する危険性もない。一方、熱分解
油は上部の排出口より排出されるが、カーボン残渣が取
り除かれているのでコーキングの発生頻度が低減する。The pyrolyzed oil and carbon residue after pyrolysis enter the centrifugal separator through the supply port and are separated by centrifugal force. The carbon residue having a large specific gravity falls to the lower part of the centrifuge, is continuously cut out by a water-cooled discharging means, and is discharged to the outside of the system.
Further, there is no risk of ignition of the carbon residue cooled by the water cooling device attached to the water cooling type discharging means. On the other hand, the pyrolysis oil is discharged from the upper discharge port, but since the carbon residue is removed, the frequency of occurrence of coking is reduced.
【０００９】[0009]
【実施例】図１は本発明の分離設備の一実施例を示す図
である。熱分解油とカーボン残渣の混合液を遠心分離機
１の底部の供給口４よりボウル５内に導入する。導入さ
れた液はボウル５内で遠心力を受けて、カーボン残渣が
ボウル５内壁に沈降する。カーボン残渣が分離された熱
分解油は排出口６から排出される。カーボン残渣はスク
リューコンベア８によってかきとられ、ボウル５の固形
物排出口７から排出され、遠心分離機１の下部の水冷式
排出手段であるスクリューコンベア２により排出され
る。発火防止のため、カーボン残渣は排出過程で水冷装
置３によって冷却される。この水冷装置としては、図１
に示した水冷ジャケット方式等がある。DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a diagram showing an embodiment of the separation equipment of the present invention. A mixed solution of pyrolyzed oil and carbon residue is introduced into the bowl 5 through the supply port 4 at the bottom of the centrifuge 1. The introduced liquid receives a centrifugal force in the bowl 5, and the carbon residue settles on the inner wall of the bowl 5. The pyrolysis oil from which the carbon residue has been separated is discharged from the discharge port 6. The carbon residue is scraped off by a screw conveyor 8, discharged from a solid matter discharge port 7 of the bowl 5, and discharged by a screw conveyor 2 which is a water-cooled discharge means in the lower part of the centrifuge 1. In order to prevent ignition, the carbon residue is cooled by the water cooling device 3 during the discharging process. This water cooling device is shown in FIG.
There is a water cooling jacket method as shown in.
【００１０】なお、水冷式排出手段はスクリューコンベ
アに限るものではなく、例えばベルトコンベア、スクレ
ーパコンベア等でも同一の効果を奏する。The water-cooling type discharging means is not limited to the screw conveyor, and the same effect can be obtained with a belt conveyor, a scraper conveyor or the like.
【００１１】[0011]
【発明の効果】本発明により、熱分解油からのカーボン
残渣の分離が効率良く行え、その抜出しが連続的に行え
る。また、その操作は安全かつ簡単である。これにより
廃プラスチック油化処理設備の最大の課題であったコー
キングの発生頻度を低減でき、長時間運転を可能にす
る。According to the present invention, the carbon residue can be efficiently separated from the pyrolyzed oil, and the carbon residue can be continuously extracted. Moreover, the operation is safe and easy. As a result, the frequency of coking, which was the biggest problem of waste plastic oil treatment equipment, can be reduced, and long-term operation is possible.
【図１】本発明の一実施例を示す概略図である。FIG. 1 is a schematic view showing an embodiment of the present invention.
１ 遠心分離機 ２ スクリューコンベア ３ 水冷装置 ４ 供給口 ５ ボウル ６ 排出口 ７ 固形物排出口 ８ スクリューコンベア 1 Centrifuge 2 Screw Conveyor 3 Water Cooling Device 4 Supply Port 5 Bowl 6 Discharge Port 7 Solids Discharge Port 8 Screw Conveyor
───────────────────────────────────────────────────── フロントページの続き (72)発明者 武内 隆春 北九州市戸畑区大字中原46−59 新日本製 鐵株式会社機械・プラント事業部内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Takaharu Takeuchi 46-59, Nakahara, Tobata-ku, Kitakyushu City Nippon Steel Corporation Machinery & Plant Division
Claims (1)
る熱分解油とカーボン残渣との分離設備において、遠心
分離機の一方に熱分解油とカーボン残渣の供給口を設
け、該遠心分離機の他方に分離後の熱分解油の排出口を
設けると共に、前記遠心分離機の下部に分離されたカー
ボン残渣の水冷式排出手段を設けたことを特徴とする熱
分解油とカーボン残渣との分離設備。1. In a facility for separating pyrolysis oil and carbon residue generated by pyrolysis of waste plastic, a supply port for pyrolysis oil and carbon residue is provided in one of the centrifuges, and the other of the centrifuges is provided. A separation facility for pyrolyzed oil and carbon residue, characterized in that a discharge port for pyrolyzed oil after separation is provided, and a water-cooled discharge means for the separated carbon residue is provided at the bottom of the centrifuge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13888793A JPH06328441A (en) | 1993-05-18 | 1993-05-18 | Separating equipment for pyrolysis oil and carbon residue |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13888793A JPH06328441A (en) | 1993-05-18 | 1993-05-18 | Separating equipment for pyrolysis oil and carbon residue |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06328441A true JPH06328441A (en) | 1994-11-29 |
Family
ID=15232446
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13888793A Pending JPH06328441A (en) | 1993-05-18 | 1993-05-18 | Separating equipment for pyrolysis oil and carbon residue |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06328441A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100714455B1 (en) * | 2004-06-16 | 2007-05-07 | 정임순 | Agitating hydrocyclic thermal decomposition reactor of wasted synthetic resin |
| JP2008519878A (en) * | 2004-11-15 | 2008-06-12 | ソルヴェイ（ソシエテ アノニム） | Method for purifying a solution containing a plastic material |
| CN104646399A (en) * | 2015-02-13 | 2015-05-27 | 王龙添 | Oil-dreg separator |
| CN110152360A (en) * | 2019-07-04 | 2019-08-23 | 青岛伊克斯达智能装备有限公司 | The cracked oil and carbon black separator and its separation method of waste tire thermal cracking |
-
1993
- 1993-05-18 JP JP13888793A patent/JPH06328441A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100714455B1 (en) * | 2004-06-16 | 2007-05-07 | 정임순 | Agitating hydrocyclic thermal decomposition reactor of wasted synthetic resin |
| JP2008519878A (en) * | 2004-11-15 | 2008-06-12 | ソルヴェイ（ソシエテ アノニム） | Method for purifying a solution containing a plastic material |
| JP4785860B2 (en) * | 2004-11-15 | 2011-10-05 | ソルヴェイ（ソシエテ アノニム） | Method for purifying a solution containing a plastic material |
| CN104646399A (en) * | 2015-02-13 | 2015-05-27 | 王龙添 | Oil-dreg separator |
| CN110152360A (en) * | 2019-07-04 | 2019-08-23 | 青岛伊克斯达智能装备有限公司 | The cracked oil and carbon black separator and its separation method of waste tire thermal cracking |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2581108A1 (en) | Method and apparatus for remediating drill cuttings | |
| CN114127234A (en) | Pyrolysis oil production system of discarded object | |
| HUP0302916A2 (en) | Apparatus and method for recovering marketable products from scrap rubber | |
| JPH07268354A (en) | Method for thermally decomposing waste plastic and device therefor | |
| RU96124094A (en) | DEVICE FOR DEPOLYMERIZATION OF SECONDARY PLASTICS AND PLASTIC WASTES | |
| JP3836112B2 (en) | Waste plastic oil production facility | |
| JPH06328441A (en) | Separating equipment for pyrolysis oil and carbon residue | |
| JP2002212571A (en) | Method for thermal cracking of waste plastic | |
| JP3096448B2 (en) | Waste plastic decomposition equipment | |
| JP3529502B2 (en) | Decomposition tank for waste plastic oil liquefaction equipment | |
| JPH04122791A (en) | Method for reclaiming waste ship oil | |
| FI103582B (en) | A method for treating a material comprising a metal and an organic material, including separation of the metal | |
| JP3611306B2 (en) | Oil recovery method from waste plastic | |
| JP2923909B2 (en) | Pyrolysis furnace for polymer waste | |
| JP2008163254A (en) | Continuous apparatus for liquefying waste plastic into oil | |
| JP4485621B2 (en) | Thermal decomposition of waste plastic | |
| JP2000157958A (en) | Recovering method of organic matter and inorganic matter from waste | |
| JP2002180068A (en) | Apparatus for forming waste plastic into oil | |
| JP3667836B2 (en) | Treatment method of plastic pyrolysis residue | |
| KR100817738B1 (en) | Method and apparatus for producing oil from waste plastic | |
| JP2005305275A (en) | Sludge removal method | |
| JPH1190387A (en) | Method and apparatus for dechloriantion of waste plastic | |
| JPH10237461A (en) | Process for converting waste plastic into oil | |
| JP3826532B2 (en) | Pyrolysis residue extraction equipment for plastic pyrolysis equipment | |
| JP2955551B1 (en) | Waste plastic continuous treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 19990217 |