JPS621431A - Oil recovery device for high-molecular solid waste carbonized gas - Google Patents

Oil recovery device for high-molecular solid waste carbonized gas

Info

Publication number
JPS621431A
JPS621431A JP13705085A JP13705085A JPS621431A JP S621431 A JPS621431 A JP S621431A JP 13705085 A JP13705085 A JP 13705085A JP 13705085 A JP13705085 A JP 13705085A JP S621431 A JPS621431 A JP S621431A
Authority
JP
Japan
Prior art keywords
oil recovery
recovery device
cooling pipe
dust
oil
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.)
Granted
Application number
JP13705085A
Other languages
Japanese (ja)
Other versions
JPH0148801B2 (en
Inventor
清治 道前
秋本 浩志
天宮 明
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.)
BURUTSUKU KURABU Inc
Doumae Chikuro Kogyo Kk
Original Assignee
BURUTSUKU KURABU Inc
Doumae Chikuro Kogyo 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 BURUTSUKU KURABU Inc, Doumae Chikuro Kogyo Kk filed Critical BURUTSUKU KURABU Inc
Priority to JP13705085A priority Critical patent/JPS621431A/en
Priority to US06/877,325 priority patent/US4726819A/en
Publication of JPS621431A publication Critical patent/JPS621431A/en
Publication of JPH0148801B2 publication Critical patent/JPH0148801B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Separating Particles In Gases By Inertia (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、高分子固体廃棄物の熱分解炉において生成
されるダストを含む乾留ガスからの油分の回収装置に関
し、特に、廃タイヤや廃プレスチック等の高分子固体廃
棄物の熱分解炉(又は乾留炉)において生成される可燃
ガス、油分、水分およびダストからなる乾留ガス流体か
ら、油分を連続的に回収する高分子固体廃棄物乾留ガス
の油分回収装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to an apparatus for recovering oil from carbonized gas containing dust generated in a pyrolysis furnace for solid polymer waste, and in particular, it relates to an apparatus for recovering oil from carbonized gas containing dust generated in a pyrolysis furnace for solid polymer waste, and in particular, for recovery of oil from waste tires and waste plastics. A carbonization process for polymer solid waste gas that continuously recovers oil from a carbonization gas fluid consisting of combustible gas, oil, moisture, and dust generated in a polymer solid waste pyrolysis furnace (or carbonization furnace) such as Regarding oil recovery equipment.

産業の発展による廃プラスチックや廃タイヤの発生量の
著しい増大に伴い、省資源、省エネルギーおよび環境保
全の観点から、それら廃棄物の再資源化や適正処理の問
題が最近社会的にますます大きな課題となっている。
With the significant increase in the amount of waste plastics and tires generated due to industrial development, the issue of recycling and proper disposal of these wastes has recently become an increasingly important social issue from the perspectives of resource conservation, energy conservation, and environmental protection. It becomes.

固体廃棄物1例えば廃タイヤ用熱分解炉の乾留過程にお
いて発生する乾留ガスには主としてカーボンからなる比
較的多量のダストが含有されておシ、このダストが乾留
によって生成される油分と一緒になって高粘性体となシ
、装置の比較的温度の低いガス通路や曲折した複雑な個
所、或いは装置底部1等に付着して、乾留ガスからの油
分の分離回収効率を著しく低下させたシ、付着堆積した
ダス、トによって装置内の通路を閉塞し、場合によって
は装置の運転を停止して分解掃除をしなければならない
等、種々の問題が生じていた。
Solid waste 1 For example, carbonization gas generated in the carbonization process of a pyrolysis furnace for waste tires contains a relatively large amount of dust mainly consisting of carbon, and this dust is mixed with oil produced by carbonization. It is a highly viscous substance, and it adheres to relatively low-temperature gas passages and complicated curved parts of the equipment, or the bottom 1 of the equipment, significantly reducing the efficiency of separating and recovering oil from carbonized gas. Various problems have arisen, such as the accumulated dust and dirt clogging the passages within the device, and in some cases requiring the device to be shut down and disassembled for cleaning.

従来の技術 廃タイヤの乾留ガスを冷却して油分等を分離回収する従
来の装置としては、例えば特開昭58−179799号
に開示されている熱交換機(本願発明の油分回収装置に
対応する)がある。この発明は、可燃物の乾留において
発生する乾留ガスを冷却して可燃物を回収する熱交換機
に関するものであって、(al熱交換機本体の内壁面に
沿って上下摺動させる内壁面クリーナー装置を設けたこ
と、(bl熱交換機の抜出口上部に乾留ガスから凝縮し
た油と蓄積されたダストを均一にするためのかくはん機
を設けたこと、(CJ熱交換機の底部に沈降堆積するダ
スト分の多い重質油を排出口付近に集約するための掻き
集め装置を設けたことを特徴としている。この発明は、
従来の装置と比較して、熱交換機内に付着堆積したダス
トの除去手段において優れているものと考えられる。
Conventional technology As a conventional device for cooling carbonized gas from waste tires to separate and recover oil, etc., there is, for example, a heat exchanger disclosed in Japanese Patent Application Laid-open No. 179799/1984 (corresponding to the oil recovery device of the present invention). There is. The present invention relates to a heat exchanger for recovering combustible materials by cooling carbonized gas generated during carbonization of combustible materials, and includes an inner wall surface cleaner device that slides up and down along the inner wall surface of the Al heat exchanger main body. (A stirrer was installed above the outlet of the BL heat exchanger to homogenize the oil condensed from the carbonized gas and the accumulated dust.) This invention is characterized by the provision of a scraping device for collecting heavy oil in the vicinity of the discharge port.
Compared to conventional devices, this device is considered to be superior in terms of removing dust deposited inside the heat exchanger.

しかしながら、後で詳細に説明するように、この発明は
乾留ガスからの油分およびダストの分離回収効率、付着
ダスト除去作業の容易さ、構造の簡潔さ、等の点におい
て不十分なものと考えられる。
However, as will be explained in detail later, this invention is considered to be insufficient in terms of separation and recovery efficiency of oil and dust from carbonized gas, ease of removing adhering dust, simplicity of structure, etc. .

発明が解決しようとする問題点 従来の油分回収装置5例えば前記特開昭5111−17
9799号に開示されている装置においては、邪魔板お
よび冷却パイプ群が適切に温度制御されていないため、
乾留ガスからの油分およびダストの分離回収効率が低く
、かつ邪魔板や冷却パイプの表面にダストが強固に付着
し、従ってその除去がむつかしい。まだ、熱交換機本体
と底部とが一体構造であるため、底部内表面に付着およ
び堆積したダストからなるスラッジの除去作業が困難で
あシ、場合によっては装置の運転を停止して分解掃除を
しなければならない等の欠点がある。さらに、冷却パイ
プクリーナー装置が剛体であるため。
Problems to be solved by the invention Conventional oil recovery device 5
In the device disclosed in No. 9799, the temperature of the baffle plate and cooling pipe group is not properly controlled;
The separation and recovery efficiency of oil and dust from carbonized gas is low, and the dust firmly adheres to the surfaces of baffles and cooling pipes, making it difficult to remove. However, since the heat exchanger body and the bottom are of an integrated structure, it is difficult to remove sludge consisting of dust that has adhered to and accumulated on the inner surface of the bottom, and in some cases, the equipment must be stopped and disassembled for cleaning. There are drawbacks such as having to do so. Additionally, since the cooling pipe cleaner device is a rigid body.

冷却パイプの表面に付着した高粘質、固着化ダストの摺
動除去が不完全であシ、従って油分の回収効率が低く、
場合によっては装置の運転を停止して分解掃除をしなけ
ればならない等の欠点がある。
The sliding removal of highly viscous and fixed dust adhering to the surface of the cooling pipe is incomplete, resulting in low oil recovery efficiency.
In some cases, there are drawbacks such as the need to stop the operation of the device and disassemble it for cleaning.

問題点を解決するだめの手段 本発明は、上記に鑑みてなされたものであシ、装置内部
に付着及び堆積したダストの除去を確実かつ容易にして
、長期連続操業を計るため、底部を本体から隔離し、液
封構造にした高分子固体廃棄物乾留ガスの油分回収装置
を提供することを主目的とする。
Means for Solving the Problems The present invention has been made in view of the above, and in order to ensure and easily remove the dust that has adhered and accumulated inside the device, and to ensure long-term continuous operation, the bottom part of the main body is The main purpose of the present invention is to provide an oil recovery device for carbonized polymer solid waste gas, which is isolated from the gas and has a liquid-sealed structure.

本発明のもう1つの目的は、前記乾留ガスからのダスト
の分離回収効率を高め、邪魔板や冷却パイプの表面への
油分の凝縮を制御して付着ダストの除去を容易にするた
め、邪魔板及び冷却パイプの表面を所定の温度に維持す
る温度制御手段を備えた高分子固体廃棄物乾留ガスの油
分回収装置を提供することである。
Another object of the present invention is to improve the separation and recovery efficiency of dust from the carbonized gas, to control the condensation of oil on the surfaces of the baffle plates and cooling pipes, and to facilitate the removal of adhering dust. Another object of the present invention is to provide an oil recovery device for carbonized polymer solid waste gas, which is equipped with a temperature control means for maintaining the surface of a cooling pipe at a predetermined temperature.

さらに、本発明の別の目的は上下方向に配置された冷却
パイプ群の表面に付着したダストの除去を確実かつ容易
にするため、冷却パイプ表面の周囲を上下に摺動する可
撓性の冷却パイプ・りIJ −ナー装置を備えた高分子
固体廃棄物乾留ガスの油分回収装置に関する。
Furthermore, another object of the present invention is to provide a flexible cooling device that slides up and down around the cooling pipe surface in order to ensure and facilitate the removal of dust attached to the surface of the cooling pipe group arranged in the vertical direction. The present invention relates to an oil recovery device for carbonized polymer solid waste gas equipped with a pipe rinner device.

一実施態様における本発明は1本体ハウジングと、該本
体ハウジングから分離されだ液封構造の底部ハウジング
からなる。
In one embodiment, the invention comprises a single body housing and a bottom housing that is separated from the body housing and is of a leak-tight construction.

さらに別の実施態様における本発明は、本体ハウジング
と、該本体ハウジングから隔離された底部ハウジングと
1表面を所望の温度に維持する温度制御手段を備えた邪
魔板と、表面を所望の温度に維持された油分凝縮用冷却
パイプ群と、該冷却パイプの各々の表面上を上下方向に
摺動して付着したダストを除去する可撓性の冷却パイプ
クリーナーと、冷却パイプ群の底部に設けられた乾留ガ
ス短絡防止手段からなる。
In yet another embodiment, the invention provides a body housing, a bottom housing isolated from the body housing, and a baffle with temperature control means for maintaining a surface at a desired temperature; a group of cooling pipes for oil condensation, a flexible cooling pipe cleaner that slides vertically on the surface of each cooling pipe to remove attached dust, and a flexible cooling pipe cleaner provided at the bottom of the cooling pipe group. Consists of carbonization gas short circuit prevention means.

作用 本発明による高分子固体廃棄物乾留ガスの油分回収装置
においては、底部ハウジングを本体ハウジングから隔離
して、液封構造にしたため、装置内部に付着および堆積
したダストおよびスラッジの除去が極めて容易になυ、
乾留ガス通路のダストによる閉塞等のトラブルは解消さ
れる。
Function: In the oil recovery apparatus for carbonized polymer solid waste gas according to the present invention, the bottom housing is isolated from the main housing and has a liquid-sealed structure, making it extremely easy to remove dust and sludge that have adhered and accumulated inside the apparatus. Naυ,
Problems such as clogging of carbonization gas passages with dust are eliminated.

本発明の油分回収装置においては、邪魔板および冷却パ
イプの表面を所望の温度に制御する温度制御手段を備え
ているため、乾留ガスからの油分およびダストの分離回
収効率が著しく高くなり。
Since the oil recovery apparatus of the present invention is equipped with a temperature control means for controlling the surfaces of the baffle plate and the cooling pipe to a desired temperature, the efficiency of separating and recovering oil and dust from carbonized gas is significantly increased.

邪魔板や冷却パイプの表面へのダストの付着を低減する
と共に付着ダストの除去を容易にする。
To reduce the adhesion of dust to the surfaces of baffle plates and cooling pipes, and to facilitate the removal of adhering dust.

本発明によれば、冷却パイプ表面の周囲を上下に摺動す
る可撓性の冷却パイプクリーナー装置を備えたため、冷
却パイプ群の表面に付着したダストの除去が確実かつ容
易となシ、パイプ相互間の乾留ガス通路のダストによる
閉塞は解消される。
According to the present invention, since the flexible cooling pipe cleaner device is provided which slides up and down around the surface of the cooling pipes, it is possible to reliably and easily remove dust attached to the surfaces of the cooling pipes, and the pipes can be mutually removed. The clogging of the carbonization gas passage between the two by dust is eliminated.

実施例 第1図には1本発明による高分子廃棄物乾留ガスの油分
回収装置の略側面図である。
Embodiment FIG. 1 is a schematic side view of an oil recovery apparatus for carbonized polymer waste gas according to the present invention.

1は油分回収装置の本体ハウジングであり、2は本体ハ
ウジング1から隔離されて配置された底部ハウジングで
ある。装置始動時には、底部ハウジング2と本体ハウジ
ングとの空間に液封用の水、゛廃油等を充てんするが、
時間の経過に伴い、これは乾留ガスから凝縮された油1
2と置換される。
Reference numeral 1 is a main body housing of the oil recovery device, and 2 is a bottom housing arranged to be separated from the main body housing 1. When starting the device, the space between the bottom housing 2 and the main housing is filled with water for liquid sealing, waste oil, etc.
Over time, this condensed oil from the carbonized gas 1
Replaced with 2.

一実施態様における本装置内を大気圧より少し高い圧力
に維持した場合には1図示のように装置内部の曲面は外
部の曲面より低くなっている。
In one embodiment, when the inside of the apparatus is maintained at a pressure slightly higher than atmospheric pressure, the curved surface inside the apparatus is lower than the curved surface outside, as shown in FIG.

5は高分子廃棄物の熱分解炉(図示せず)へ。5 to a polymer waste pyrolysis furnace (not shown).

一般にはサイクロン等を介して接続される乾留ガスの入
口であυ、4は油分およびダストが除去された乾留ガス
の出口である。
In general, 4 is an inlet for carbonized gas connected via a cyclone or the like, and 4 is an outlet for carbonized gas from which oil and dust have been removed.

5は乾留ガスを衝突させてダストを下方に落下させる邪
魔板である。この邪魔板5は、その内部に所定温度の流
体、例えば水を流通さすことによってその表面温度は所
望の温度に維持される。邪魔板5の表面は、例えばガス
人口うから流入する乾留ガスの温度が100〜500℃
、流速が1〜50m/秒の場合に、回収する油の種類に
よって5〜50℃、または50〜80℃に調節した液体
を内部に流通さすことによって適温に維持される。
Reference numeral 5 denotes a baffle plate that causes the carbonized gas to collide with each other to cause the dust to fall downward. The surface temperature of the baffle plate 5 is maintained at a desired temperature by flowing a fluid at a predetermined temperature, such as water, into the baffle plate 5. For example, the surface of the baffle plate 5 has a temperature of 100 to 500° C. of the carbonized gas flowing from the gas tank.
When the flow rate is 1 to 50 m/sec, the temperature is maintained at an appropriate temperature by flowing a liquid adjusted to 5 to 50°C or 50 to 80°C depending on the type of oil to be recovered.

一般に、軽質油は高い温度、そして重質油の場合には低
い温度範囲に選定する。
Generally, a higher temperature range is selected for light oils and a lower temperature range for heavy oils.

7は二重管の冷児パイプを数群(第1図においてはう群
)に分けて設置した冷却パイプ群であり。
7 is a cooling pipe group in which double-walled refrigerated pipes are divided into several groups (creeping groups in Fig. 1).

各パイプは宙吊に配置され、底部ハウジング2との間に
は適当な空間を設ける。各パイプ群の下部左方には板状
の乾留ガス流短絡防止板(又はパイプ液シール板)6が
取り付けられている。これらの冷却パイプ群7に流す液
体の温度は乾留ガスに −含まれる油の性状によって適
当な温度、例えば0〜100℃に制御する。そして邪魔
板5とは逆に、軽質油は比較的低い温度に、重質油は比
較的高い温度を選ぶことが望ましい。このように、冷却
パイプ群の表面温度を適当に選択することによって。
Each pipe is suspended in the air, and an appropriate space is provided between it and the bottom housing 2. A plate-shaped carbonized gas flow short-circuit prevention plate (or pipe liquid sealing plate) 6 is attached to the lower left side of each pipe group. The temperature of the liquid flowing through the cooling pipe group 7 is controlled to an appropriate temperature, for example, 0 to 100°C, depending on the properties of the oil contained in the carbonized gas. Contrary to the baffle plate 5, it is desirable to select a relatively low temperature for light oil and a relatively high temperature for heavy oil. Thus, by appropriately selecting the surface temperature of the cooling pipe group.

油の凝縮速度を最適に調節することができ、パイプ間の
閉塞の防止、ダストの回収効率を高めることができる。
The oil condensation rate can be optimally adjusted, preventing blockages between pipes and increasing dust collection efficiency.

8は液層の底部に堆積したダスト、スラッジ等を排出口
11に掻き集めるための掻き集め装置である。9は底部
内壁部に付着したダストや前記スラッジ等を目で見なが
ら自由な操作の下に掻き出す掻き出し装置である。10
は内部液のオーバーフローパイプ(又は油出口)である
。もちろん、このオーバーフローパイプ(又は油の出口
)は高さの異なるものを複数個設けることができる。1
1はスラッジの排出口である。
8 is a scraping device for scraping up dust, sludge, etc. accumulated at the bottom of the liquid layer to the discharge port 11. Reference numeral 9 denotes a scraping device that scrapes out dust, sludge, etc. adhering to the bottom inner wall portion while visually observing and freely operating the device. 10
is the internal liquid overflow pipe (or oil outlet). Of course, a plurality of overflow pipes (or oil outlets) with different heights can be provided. 1
1 is a sludge discharge port.

第2図は冷却パイプ群に取り付けた冷却パイプクリーナ
ー装置の部分拡大図であって、第2A図は平面図、そし
て第2B図は側面図である。この冷却パイプクリーナー
装置15は各冷却パイプ表面の周囲に上下に摺動自在に
配置されたワイヤ13と該ワイヤを上下に移動さす手段
111からなる。
FIG. 2 is a partially enlarged view of the cooling pipe cleaner device attached to the cooling pipe group, FIG. 2A is a plan view, and FIG. 2B is a side view. This cooling pipe cleaner device 15 consists of a wire 13 arranged vertically slidably around the surface of each cooling pipe and means 111 for vertically moving the wire.

発明の効果 以上本発明による高分子固体廃棄物乾留ガスの油分回収
装置は、本体ハウジングと底部ハウジングとを隔離し、
操・作自在のダスト除去手段を設け。
Effects of the Invention The oil recovery apparatus for carbonized polymer solid waste gas according to the present invention has a main body housing and a bottom housing separated from each other.
Equipped with an easily operable dust removal means.

邪魔板および冷却パイプ群の表面を所定の温度に維持す
る手段を設け、各冷却パイプ表面の周囲を上下方向に摺
動する冷却パイプクリーナーを設けたので、乾留ガスか
らの油分およびダストの分離回収効率が著しく改善され
、ダストの除去作業性が改善されると共に、乾留ガス通
路の閉塞が防止され、装置の長期連続操業が可能となる
等、極めて優れた効果を有する。
A means for maintaining the baffle plate and the surface of the cooling pipe group at a predetermined temperature is provided, and a cooling pipe cleaner that slides vertically around the surface of each cooling pipe is installed, making it possible to separate and recover oil and dust from carbonized gas. This method has extremely excellent effects such as significantly improved efficiency, improved dust removal workability, prevention of clogging of the carbonization gas passage, and enabling long-term continuous operation of the device.

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

第1図は本発明による高分子固体廃棄物乾留ガスの油分
回収装置の略側面図でるる。第2図は冷却パイプ群に取
り付けた冷却パイプクリーナーの部分拡大図であって、
第2A図はその平面図そして第2B図はその側面図であ
る。
FIG. 1 is a schematic side view of an oil recovery apparatus for carbonized polymer solid waste gas according to the present invention. FIG. 2 is a partially enlarged view of the cooling pipe cleaner attached to the cooling pipe group,
FIG. 2A is a plan view thereof, and FIG. 2B is a side view thereof.

Claims (1)

【特許請求の範囲】 1、本体と、邪魔板と、冷却パイプ群と、ダストクリー
ナー装置からなり、高分子固体廃棄物の熱分解炉におい
て生成されるダストを含む乾留ガスから、油分を分離回
収する油分回収装置において、底部ハウジングを本体ハ
ウジングから隔離し、液封構造にしたことを特徴とする
高分子固体廃棄物乾留ガスの油分回収装置。 2、前記邪魔板が、該邪魔板の表面を所定の温度に維持
するための温度制御手段を備えることを特徴とする特許
請求の範囲第1項に記載の油分回収装置。 3、前記邪魔板の表面温度が温度制御手段によつて5〜
50℃、または30〜80℃に維持されることを特徴と
する特許請求の範囲第2項に記載の油分回収装置。 4、前記冷却パイプ群がそれぞれ該冷却パイプの表面温
度を所定の温度に維持する湿度制御手段を備えることを
特徴とする特許請求の範囲第1項に記載の油分回収装置
。 5、前記冷却パイプ群が、該冷却パイプ群の底部に乾留
ガスの短絡を防止するガス短絡防止手段を備えることを
特徴とする特許請求の範囲第1項に記載の油分回収装置
。 6、前記冷却パイプ群の各々が各パイプ表面の周囲を上
下に摺動して付着した粘着性ダストを除去する可撓性の
冷却パイプクリーナー手段を備えることを特徴とする特
許請求の範囲第1項に記載の油分回収装置。
[Claims] 1. Consists of a main body, a baffle plate, a group of cooling pipes, and a dust cleaner device, which separates and recovers oil from carbonized gas containing dust generated in a pyrolysis furnace for solid polymer waste. An oil recovery device for carbonized polymer solid waste gas, characterized in that the bottom housing is isolated from the main housing and has a liquid-sealed structure. 2. The oil recovery device according to claim 1, wherein the baffle plate includes temperature control means for maintaining the surface of the baffle plate at a predetermined temperature. 3. The surface temperature of the baffle plate is controlled by the temperature control means to
The oil recovery device according to claim 2, wherein the oil recovery device is maintained at 50°C or 30 to 80°C. 4. The oil recovery device according to claim 1, wherein each of the cooling pipe groups is provided with humidity control means for maintaining the surface temperature of the cooling pipe at a predetermined temperature. 5. The oil recovery device according to claim 1, wherein the cooling pipe group is provided with a gas short circuit prevention means for preventing a short circuit of the carbonized gas at the bottom of the cooling pipe group. 6. Claim 1, wherein each of the cooling pipe groups is provided with a flexible cooling pipe cleaner means that slides up and down around the surface of each pipe to remove attached sticky dust. The oil recovery device described in section.
JP13705085A 1985-06-25 1985-06-25 Oil recovery device for high-molecular solid waste carbonized gas Granted JPS621431A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP13705085A JPS621431A (en) 1985-06-25 1985-06-25 Oil recovery device for high-molecular solid waste carbonized gas
US06/877,325 US4726819A (en) 1985-06-25 1986-06-23 Process and apparatus for recovering oil component from dry-distilled gas flow or solid polymer wastes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13705085A JPS621431A (en) 1985-06-25 1985-06-25 Oil recovery device for high-molecular solid waste carbonized gas

Publications (2)

Publication Number Publication Date
JPS621431A true JPS621431A (en) 1987-01-07
JPH0148801B2 JPH0148801B2 (en) 1989-10-20

Family

ID=15189701

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13705085A Granted JPS621431A (en) 1985-06-25 1985-06-25 Oil recovery device for high-molecular solid waste carbonized gas

Country Status (1)

Country Link
JP (1) JPS621431A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018173714A1 (en) * 2017-03-23 2018-09-27 京史 寺本 Exhaust separation device
JP2023078815A (en) * 2021-11-26 2023-06-07 テギョン エスコ カンパニー リミテッド Condenser with scraper

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018173714A1 (en) * 2017-03-23 2018-09-27 京史 寺本 Exhaust separation device
JP2023078815A (en) * 2021-11-26 2023-06-07 テギョン エスコ カンパニー リミテッド Condenser with scraper

Also Published As

Publication number Publication date
JPH0148801B2 (en) 1989-10-20

Similar Documents

Publication Publication Date Title
CN102908841A (en) Method and device for dedusting and purifying low-temperature dry-distilled gas
CN1966730A (en) Method for treating converter flue gas
CN216409843U (en) Boiler flue gas waste heat utilization equipment
CN111018193A (en) Sewage treatment system based on swirler
JPS621431A (en) Oil recovery device for high-molecular solid waste carbonized gas
CN205874041U (en) A sewage pretreatment device for park landscape pond
US4726819A (en) Process and apparatus for recovering oil component from dry-distilled gas flow or solid polymer wastes
CN110586635B (en) Energy-conserving high-efficient type soil remediation is with thermal desorption system
JPH0157602B2 (en)
CN215909704U (en) Flue gas particle trapping device
CN113318558B (en) Tail gas recovery system for oil mist separation transfer test bed
CA1292964C (en) Process and apparatus for recovering oil components from a flow of dry-distilled gas of solid polymer waste
CN102319523B (en) Mini-hydrocyclone solid removing method and device for medium oil in fractionating tower of ethylene unit
JP2023078815A (en) Condenser with scraper
CN110812980B (en) Purification and resource comprehensive utilization device for high-temperature flue gas of furnace
US2539992A (en) Washer and settler for gases
CN201848114U (en) Waste plastic pyrolysis gas separation device
CN214715426U (en) Double-layer filler dust remover for dust removal of gas inlet of gas-liquid counter-flow heat exchanger
CN103789045B (en) Dry-method purifying and recycling process for dry distillation gas and mixed type gas condensation device
KR19990051989A (en) Sludge Removal System of Landscape Oil Manufacturing Equipment
CN216498332U (en) Recovery unit is used in coal coking production
EP0870529A1 (en) Method and device for removing condensible components from warm industrial waste gas
CN221191717U (en) Oil-water separation equipment
CN217155044U (en) Cooling tower convenient to clearance
CN219050809U (en) Anti-adhesion tar and paint mist collecting device