JPS5837851B2 - Pyrolysis gas cleaning method and device - Google Patents
Pyrolysis gas cleaning method and deviceInfo
- Publication number
- JPS5837851B2 JPS5837851B2 JP55114066A JP11406680A JPS5837851B2 JP S5837851 B2 JPS5837851 B2 JP S5837851B2 JP 55114066 A JP55114066 A JP 55114066A JP 11406680 A JP11406680 A JP 11406680A JP S5837851 B2 JPS5837851 B2 JP S5837851B2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized
- pyrolysis
- bed
- fluidized medium
- furnace
- 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
Links
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- Gasification And Melting Of Waste (AREA)
Description
【発明の詳細な説明】
本発明は、都市とみ、パルプスラツジ、パイオマス、石
炭などの有機物を熱分解して得られた熱分解ガスから、
チャーなどの固体粒子や油、夕一ルなどの凝縮分を除去
し、清浄な熱分解ガスを得る清浄化万法及びその装置に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention utilizes pyrolysis gas obtained by thermally decomposing organic matter such as urban waste, pulp sludge, pyomas, and coal.
The present invention relates to a cleaning method and apparatus for removing solid particles such as char, oil, condensed matter such as alcohol, and obtaining clean pyrolysis gas.
従来、熱分解炉を出るガス中の炭素粒子などを捕集除去
するために、サイクロンを単段又は多段に設けて大部分
の粒子を除去し、その後湿式のガス冷却洗浄装置に導い
て油、タールなどの凝縮分を捕集して除している。Conventionally, in order to collect and remove carbon particles in the gas exiting the pyrolysis furnace, a cyclone was installed in a single stage or in multiple stages to remove most of the particles, and then the gas was led to a wet gas cooling cleaning device to remove oil, oil, etc. It collects and removes condensate such as tar.
しかしながら、サイクロ/の捕集効率ぼ圧力損失との関
係もあって90%前後にとど1る。However, the collection efficiency of cyclo/ remains around 90% due to the relationship with pressure loss.
従って残部の10多程度の未捕集粒子は湿式ガス冷却洗
浄装置で捕集されることになる。Therefore, the remaining 10 or so uncollected particles will be collected by the wet gas cooling cleaning device.
一万湿式ガス冷却洗浄装置にかいては、ガス中に含まれ
る油やタールが凝縮して洗浄水に移行して除去されるが
、その時に未捕集炭素粒子も洗浄水に捕捉されて混合す
る。In the 10,000 wet gas cooling cleaning equipment, oil and tar contained in the gas condense and are transferred to the cleaning water and removed, but at the same time, uncollected carbon particles are also captured and mixed in the cleaning water. do.
この混合液は粘着性が強く、洗浄水から油を分離する装
置やその他の機器や管路に付着して支障を来たし、又、
これを避けるために油分離装置などの機器は複雑となり
、分離された油や炭素粒子を流動媒体再生用の加熱用流
動層に熱源として供給する場合など、移送装置にもlを
来たし、装置も複雑になる。This mixed liquid is highly sticky and adheres to devices that separate oil from cleaning water, other equipment, and pipes, causing problems.
To avoid this, equipment such as oil separation equipment has become complicated, and when supplying separated oil and carbon particles as a heat source to a heating fluidized bed for regenerating fluidized media, it has also become difficult to transport equipment and equipment. It gets complicated.
本発明は、流動媒体による移動層を形威し、サイクロン
を出たガスをこの移動層を通過せしめた後、湿式ガス冷
却洗浄塔に導くようにしたことにより、従来の方式の上
記の欠点を除き、サイクロンにて捕集されなかった未捕
集粒子及び凝縮した油分を流動媒体に付着ぜしめて捕集
し、扱い易い性状となし、湿式の油分離装置を簡略化又
は省略せしめ、輸送機器、管路などにおける支障を除き
構造を簡単となし、信頼性の高い熱分解ガス清浄化万法
及びその装置を提供することを目的とするものである。The present invention eliminates the above-mentioned drawbacks of the conventional system by forming a moving bed using a fluidized medium and making the gas exiting the cyclone pass through the moving bed before being guided to a wet gas cooling and cleaning tower. In addition, uncollected particles and condensed oil that are not collected by a cyclone are collected by adhering to a fluid medium, making them easy to handle, simplifying or omitting wet oil separation equipment, and transport equipment, The object of the present invention is to provide a highly reliable pyrolysis gas purification method and device that has a simple structure by eliminating obstacles in pipes and the like.
本発明は、有機物を流動層熱分解炉と流動層焼却炉とを
備えた熱分解装置にて熱分解して生或された熱分解ガス
の清浄化方法にかいて、熱分解ガスをサイクロンに導き
大部分の固体粒子を除去した後、流動媒体の移動層を通
過せしめて残部の固体粒子を除去しその後湿式冷却洗浄
塔にて油、タール分を凝縮、除去すると共に、前記移動
層から抜出される流動媒体を前記流動層焼却炉へ供給す
ることを特徴とする熱分解ガス清浄化方法、及びその装
置である。The present invention relates to a method for cleaning pyrolysis gas produced by pyrolysis of organic matter in a pyrolysis apparatus equipped with a fluidized bed pyrolysis furnace and a fluidized bed incinerator, in which the pyrolysis gas is passed through a cyclone. After removing most of the solid particles, the fluidized medium is passed through a moving bed to remove the remaining solid particles, and then oil and tar are condensed and removed in a wet cooling washing tower, and the fluid is extracted from the moving bed. A method for purifying pyrolysis gas, and an apparatus therefor, characterized in that the discharged fluidized medium is supplied to the fluidized bed incinerator.
本発明を、都市ごみの、二塔循環式熱分解装置の例につ
き説明すれば、都市とみぱ破砕機などにより粒径を減少
せしめられ、熱分解原料11として、流動層熱分解炉1
に供給される。To explain the present invention using an example of a two-column circulation type pyrolysis apparatus for municipal waste, the particle size is reduced by a pulverizer or the like,
supplied to
″流動層熱分解炉1、サイクロン2、移動層17、湿式
洗浄塔7及びそれらを接続する管路により熱分解ガス経
路が形或される。A pyrolysis gas path is formed by the fluidized bed pyrolysis furnace 1, the cyclone 2, the moving bed 17, the wet cleaning tower 7, and the pipes connecting them.
熱分解により生或されたガスはチャーなどの固形粒子を
含むが、サイクロン2により大部分のチャーぱ捕集され
、戻り経路15を経て流動層燃焼炉3に送られ燃焼され
て熱源となる。The gas produced by thermal decomposition contains solid particles such as char, but most of the char is collected by the cyclone 2, sent to the fluidized bed combustion furnace 3 via the return path 15, and combusted to become a heat source.
サイクロン2を出たガスは乾式除しん器4に送られる。The gas leaving the cyclone 2 is sent to a dry desaturator 4.
乾式除じん器4にかいては流動媒体による移動層17が
形或されている。The dry dust remover 4 is provided with a moving bed 17 made of a fluidized medium.
この流動媒体は、熱分解炉1の底部より、異物と共に抜
き出された流動媒体を異物・砂分別機5により分別して
流導媒体移送経路としてのコンベア6Kより送られたも
のを用いる。This fluidized medium is a fluidized medium extracted from the bottom of the pyrolysis furnace 1 together with foreign matter, separated by a foreign matter/sand separator 5, and sent from a conveyor 6K serving as a fluidized medium transfer path.
14ぱ分別された異物である。供給されたガスが移動層
17を通過する間に、未捕集チャーなどの固形粒子は流
動媒体(砂など)に付着して取り除かれる。This is a foreign substance that has been separated into 14 parts. While the supplied gas passes through the moving bed 17, solid particles such as uncollected char adhere to the fluidizing medium (such as sand) and are removed.
移動層11の温度は熱分解炉1の内部温度よりも低くな
っているので、ガスに含まれる油分の一部は凝縮して流
動媒体に付着して取り除かれる。Since the temperature of the moving bed 11 is lower than the internal temperature of the pyrolysis furnace 1, part of the oil contained in the gas condenses and adheres to the fluidized medium and is removed.
チャー油分などを付着せしめた流動媒体は、移動層11
を下降した後排出されて移動媒体供給経路としてのスク
リューコンベヤ16により、燃焼炉3の流動層内に供給
される。The fluid medium to which char oil and the like are attached is transferred to the moving bed 11.
After descending, it is discharged and supplied into the fluidized bed of the combustion furnace 3 by a screw conveyor 16 serving as a moving medium supply path.
またスクリューコンベヤ16は、戻り経路と併用しても
よい。The screw conveyor 16 may also be used in conjunction with the return path.
燃焼炉3は流動媒体の再生加熱用のものであり、スクリ
ューコンベヤ16にテ送られる流動媒体に付着している
チャーや油分は熱分解の熱源を作るために燃焼せしめて
利用される。The combustion furnace 3 is for regenerating and heating the fluidized medium, and the char and oil adhering to the fluidized medium sent to the screw conveyor 16 are combusted and used to create a heat source for pyrolysis.
乾式余じん器4から出たガスは熱交換器10により一定
の熱回収を行なった後、湿式洗浄塔7において冷却と洗
浄を行ない、凝縮した油分、夕一ル分を洗浄水にて洗浄
し除去し、清浄熱分解ガス12として次の工程に送られ
る。After a certain amount of heat is recovered from the gas discharged from the dry dust collector 4 by a heat exchanger 10, it is cooled and washed in a wet washing tower 7, and condensed oil and residue are washed away with washing water. It is removed and sent to the next process as a clean pyrolysis gas 12.
洗浄水ぱポンプ9により循環使用されるが、部抜き出さ
れて、油水分離器8にて油分を分離除去した後廃水13
として廃水処理装置に送られる。It is circulated and used by the cleaning water pump 9, but it is partially extracted and the oil is separated and removed by the oil-water separator 8, and then the waste water 13 is used.
The wastewater is sent to the wastewater treatment facility as a wastewater treatment facility.
本実施例は上記の如く構或され作用するので、乾式除じ
ん器4の流動媒体の移動層17によって、ガスの中に残
留ぜるチャーの殆んどを除去し、これにより、下流にあ
る熱交換器10や湿式焼浄塔7に釦ける、チャーが存在
するために起こる障害を除くことができる。Since this embodiment is constructed and operates as described above, most of the char remaining in the gas is removed by the moving bed 17 of the fluidized medium of the dry dust remover 4, and thereby the downstream Disturbances caused by the presence of char in the heat exchanger 10 and wet sintering tower 7 can be eliminated.
また、二塔式流動層熱分解装置の異物排出時に同伴する
流動媒体を移動層1T用の粒子としたことにより、流動
媒体が移動層11にかいて熱分解ガスと接触して予熱さ
れて燃焼炉3に送り込まれるので、燃焼炉3の流動層の
温度の低下を防ぐことができる。In addition, by using particles for the moving bed 1T as the fluidized medium that accompanies the discharge of foreign matter from the two-column fluidized bed pyrolysis device, the fluidized medium is passed through the moving bed 11 and comes into contact with the pyrolysis gas to be preheated and combusted. Since it is fed into the furnace 3, the temperature of the fluidized bed in the combustion furnace 3 can be prevented from decreasing.
また、移動層17では油分も一部捕集されるが、チャー
と度に、固形粒子である流動媒体に付着して運ばれるの
で、各機器や管路への付着などの支障がない。In addition, although a portion of the oil is also collected in the moving bed 17, since the oil is transported along with the char while adhering to the fluidized medium, which is a solid particle, there is no problem such as adhesion to each device or pipe line.
本発明により、湿式洗浄塔に至る前にチャー全部及び大
部分の油分は除かれているので、チャーと油分が混存す
ることによる粘着性物質の発生のための支障を除〈こと
ができると共に、流動媒体の予熱が行なわれ、かつ流動
媒体に付着したチャー、油分が熱源燃料となって燃焼炉
の流動層の温度低下を防いで安定した運転が確保され、
各機器、管路の保守が容易となりかつ、各機器の構造が
簡単となり、信頼性の高い熱分解ガス清浄化方法及びそ
の装置を提供することができ、実用上極めて大なる効果
を有するものである。According to the present invention, all of the char and most of the oil are removed before reaching the wet cleaning tower, so it is possible to eliminate the hindrance to the generation of sticky substances due to the coexistence of char and oil, and The fluidized medium is preheated, and the char and oil adhering to the fluidized medium serve as a heat source fuel to prevent the temperature of the fluidized bed of the combustion furnace from decreasing and ensure stable operation.
The maintenance of each device and pipeline is easy, the structure of each device is simple, and a highly reliable pyrolysis gas cleaning method and device can be provided, which has extremely great practical effects. be.
図面は本発明の実施例のフロー図である。
1・・・熱分解炉、2・・・サイクロン、3・・・燃焼
炉、4・・・乾式除じん器、5・・・異物・砂分別機、
6・・・コンベヤ、7・・・湿式洗浄塔、8・・・油水
分離器、9・・・ポンプ、10・・・熱交換器、11・
・・熱分解原料、12・・・清浄熱分解ガス、13・・
・廃水、14・・・異物、15・・・戻り経路、16・
・・スクリューコンベヤ、17・・・移動層。The drawing is a flow diagram of an embodiment of the invention. 1... Pyrolysis furnace, 2... Cyclone, 3... Combustion furnace, 4... Dry dust remover, 5... Foreign matter/sand separator,
6... Conveyor, 7... Wet cleaning tower, 8... Oil/water separator, 9... Pump, 10... Heat exchanger, 11...
...Pyrolysis raw material, 12...Clean pyrolysis gas, 13...
・Wastewater, 14... Foreign matter, 15... Return route, 16.
...screw conveyor, 17...moving layer.
Claims (1)
熱分解装置にて熱分解して生成された熱分解ガスの清浄
化方法にかいて、熱分解ガスをサイクロンに導き大部分
の固体粒子を除去した後、流動媒体の移動層を通過せし
めて残部の固体粒子を除去し、その後湿式冷却洗浄塔に
て油、タール分を凝縮、除去すると共に、前記移動層か
ら抜出される流動媒体を前記流動層焼却炉へ供給するこ
とを特徴とする熱分解ガス清浄化方法。 2 前記移動層の流動媒体が、前記流動層熱分解炉の中
から、異物排出と共に排出された流動媒体を用いる特許
請求の範囲第1項記載の方法。 3 有機物を熱分解して熱分解ガスを生成し、かつ異物
を排出するようにした流動層熱分解炉と、該熱分解炉の
流動媒体を受け人へ加熱再生せしめて再び前記熱分解炉
に戻して循fM−wしめる流動層焼焼炉と、流動媒体に
よる移動層が形或される乾式除しん器と、湿式冷却洗浄
塔とを備え、前記移動層部から排出された流動媒体を前
記燃焼炉に導く流動媒体供給経路と、前記熱分解炉で生
或された熱分解ガスを前記移動層を通過せしめた後前記
湿式冷却洗浄塔に導く熱分解ガス経路を備えたことを特
徴とする熱分解ガス清浄化装置。 4 前記熱分解炉から排出される異物と共に抜出さhる
流動媒体を前記移動層に導く流動媒体移送経路を有する
特許請求の範囲第3項記載の装置。[Claims] 1. A method for cleaning pyrolysis gas produced by pyrolysis of organic matter in a pyrolysis apparatus equipped with a fluidized bed pyrolysis furnace and a fluidized bed incinerator. After passing through a cyclone to remove most of the solid particles, the remaining solid particles are removed by passing through a moving bed of fluidized medium, and then oil and tar are condensed and removed in a wet cooling washing tower, and the transferred A method for purifying pyrolysis gas, characterized in that the fluidized medium extracted from the bed is supplied to the fluidized bed incinerator. 2. The method according to claim 1, wherein the fluidized medium of the moving bed is a fluidized medium discharged from the fluidized bed pyrolysis furnace together with foreign matter discharge. 3. A fluidized bed pyrolysis furnace that pyrolyzes organic matter to generate pyrolysis gas and discharges foreign substances, and a fluidized bed pyrolysis furnace that heats and regenerates the fluidized medium of the pyrolysis furnace to a receiver and returns to the pyrolysis furnace. The fluidized bed incinerator is equipped with a fluidized bed incinerator that circulates fM-w again, a dry desaturator in which a moving bed is formed by the fluidized medium, and a wet cooling and washing tower, and the fluidized medium discharged from the moving bed section is It is characterized by comprising a fluidized medium supply path leading to the combustion furnace, and a pyrolysis gas path leading the pyrolysis gas produced in the pyrolysis furnace to the wet cooling and cleaning tower after passing through the moving bed. Pyrolysis gas purification equipment. 4. The apparatus according to claim 3, further comprising a fluidized medium transfer path that guides the fluidized medium extracted together with the foreign matter discharged from the pyrolysis furnace to the moving bed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55114066A JPS5837851B2 (en) | 1980-08-21 | 1980-08-21 | Pyrolysis gas cleaning method and device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55114066A JPS5837851B2 (en) | 1980-08-21 | 1980-08-21 | Pyrolysis gas cleaning method and device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5738923A JPS5738923A (en) | 1982-03-03 |
| JPS5837851B2 true JPS5837851B2 (en) | 1983-08-19 |
Family
ID=14628171
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55114066A Expired JPS5837851B2 (en) | 1980-08-21 | 1980-08-21 | Pyrolysis gas cleaning method and device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5837851B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60230408A (en) * | 1984-04-27 | 1985-11-15 | 日工株式会社 | Method for preventing adhesion of sticky dust generated at time of regeneration of asphalt pavement waste material |
| KR100488904B1 (en) * | 2002-05-10 | 2005-05-10 | 박수길 | Method and Apparatus for Remove a Bad Smell |
| CN109589737A (en) * | 2019-01-23 | 2019-04-09 | 广州研华环境科技有限公司 | A kind of cracking gas purification system and method |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54157101A (en) * | 1978-06-01 | 1979-12-11 | Nippon Steel Corp | Dust-collecting method in coal preheater |
-
1980
- 1980-08-21 JP JP55114066A patent/JPS5837851B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5738923A (en) | 1982-03-03 |
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