JP2003112012A - Method and apparatus for removing dioxins in exhaust gas from waste treatment furnace - Google Patents
Method and apparatus for removing dioxins in exhaust gas from waste treatment furnaceInfo
- Publication number
- JP2003112012A JP2003112012A JP2001305692A JP2001305692A JP2003112012A JP 2003112012 A JP2003112012 A JP 2003112012A JP 2001305692 A JP2001305692 A JP 2001305692A JP 2001305692 A JP2001305692 A JP 2001305692A JP 2003112012 A JP2003112012 A JP 2003112012A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- dioxins
- waste treatment
- treatment furnace
- catalytic reaction
- 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.)
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Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treating Waste Gases (AREA)
Abstract
(57)【要約】
【課題】 ダイオキシン類の排出濃度をより低いレベル
とする廃棄物処理炉の排ガス中ダイオキシン類除去方法
及びその装置の提供。
【解決手段】 廃棄物処理炉から排出された排ガスを冷
却した後、バグフィルタ1で集じんし、集じん後の排ガ
ス中のダイオキシン類を触媒層3aで触媒反応により酸
化分解し、さらにミスト状のダイオキシン類を後流で吸
着層4aにより吸着して廃棄物処理炉の排ガス中のダイ
オキシン類を除去する。
PROBLEM TO BE SOLVED: To provide a method and an apparatus for removing dioxins in exhaust gas of a waste treatment furnace in which the emission concentration of dioxins is reduced to a lower level. SOLUTION: After exhaust gas discharged from a waste treatment furnace is cooled, dust is collected by a bag filter 1, and dioxins in the exhaust gas after dust are oxidatively decomposed by a catalytic reaction in a catalyst layer 3a, and further mist-like. The dioxins are adsorbed in the downstream by the adsorption layer 4a to remove dioxins in the exhaust gas from the waste treatment furnace.
Description
【0001】[0001]
【発明の属する技術分野】廃棄物処理設備の廃棄物処理
炉から排出される排ガスからダイオキシン類を除去する
廃棄物処理炉の排ガス中ダイオキシン類除去方法および
その装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for removing dioxins from exhaust gas of a waste treatment furnace for removing dioxins from exhaust gas discharged from the waste treatment furnace of a waste treatment facility.
【0002】[0002]
【従来の技術】廃棄物処理設備の廃棄物処理炉から排出
される排ガスからダイオキシン類を除去する除去装置と
して触媒反応塔が用いられる。例えば、特許第2633
316号公報には、図3の従来の排ガス処理のフロー図
に示すように、焼却炉11で発生した燃焼排ガスをガス
冷却塔12および空気予熱器13により冷却し、集じん
器14で集じんした後、酸化チタン担体に五酸化バナジ
ウムと三酸化タングステンを担持させた触媒が充填され
た触媒反応器15に導入して毒性の芳香族系塩素化合物
(ダイオキシン類)を酸化分解して無害化し、ブロワー
16により煙突17から放出する廃棄物焼却炉の排ガス
処理方法が記載されている。2. Description of the Related Art A catalytic reaction tower is used as a removal device for removing dioxins from exhaust gas discharged from a waste treatment furnace of a waste treatment facility. For example, Japanese Patent No. 2633
In Japanese Patent No. 316, as shown in the flow chart of the conventional exhaust gas treatment of FIG. 3, the combustion exhaust gas generated in the incinerator 11 is cooled by the gas cooling tower 12 and the air preheater 13 and collected by the dust collector 14. After that, the titanium oxide carrier is introduced into a catalytic reactor 15 in which a catalyst supporting vanadium pentoxide and tungsten trioxide is packed, and toxic aromatic chlorine compounds (dioxins) are oxidatively decomposed to be harmless, A method for treating exhaust gas of a waste incinerator that is discharged from a chimney 17 by a blower 16 is described.
【0003】[0003]
【発明が解決しようとする課題】触媒反応塔の触媒反応
では、ガス状のダイオキシン類は酸化分解されるが、油
などに捕捉されたミスト状(粒子状)のダイオキシン類
は分解することができない。ダイオキシン類は0.01
ngTEQ/m3N以下の濃度レベルではミスト状のダ
イオキシン類の占める割合が比較的大きく、触媒反応で
のダイオキシン類排出濃度には到達限界があった。In the catalytic reaction of the catalytic reaction tower, gaseous dioxins are oxidatively decomposed, but mist-like (particulate) dioxins trapped in oil or the like cannot be decomposed. . 0.01 for dioxins
At a concentration level of ngTEQ / m 3 N or less, the proportion of mist-like dioxins was relatively large, and there was a limit to the emission concentration of dioxins in the catalytic reaction.
【0004】ミスト状のダイオキシン類を除去するには
吸着除去が有効であるが、吸着除去の場合はダイオキシ
ン類を分解せず吸着剤にため込むのみであるので定常的
に吸着剤の入れ替えを行う移動層とする必要があった。Adsorption and removal are effective for removing mist-like dioxins, but in the case of adsorption and removal, dioxins are not decomposed but only accumulated in the adsorbent, so that the adsorbent is constantly replaced. Had to make layers.
【0005】また、排ガスをバグフィルタへ導入する前
に活性炭などの吸着剤を添加しダイオキシンを吸着除去
するプロセスもあるが、ダイオキシンを吸着した活性炭
は灰とともにバグフィルタで捕捉され、無害化のために
加熱処理が必要となる。There is also a process of adding an adsorbent such as activated carbon to adsorb and remove dioxin before introducing the exhaust gas into the bag filter. Requires heat treatment.
【0006】そこで、本発明は、ダイオキシン類の排出
濃度をより低いレベルとする廃棄物処理炉の排ガス中ダ
イオキシン類除去方法及びその装置を提供するものであ
る。Therefore, the present invention provides a method and an apparatus for removing dioxins in exhaust gas of a waste treatment furnace, which makes the emission concentration of dioxins lower.
【0007】[0007]
【課題を解決するための手段】本発明の廃棄物処理炉の
排ガス中ダイオキシン類除去方法は、廃棄物処理炉から
排出された排ガスを冷却した後、バグフィルタで集じん
し、集じん後の排ガス中のダイオキシン類を触媒反応に
より酸化分解し、さらに後流でミスト状のダイオキシン
類を吸着剤により吸着除去することを特徴とする。The method for removing dioxins in exhaust gas of a waste treatment furnace according to the present invention is a method for cooling exhaust gas discharged from a waste treatment furnace, then collecting it with a bag filter, and collecting dust with a bag filter. It is characterized in that dioxins in exhaust gas are oxidatively decomposed by a catalytic reaction, and mist-like dioxins are adsorbed and removed by an adsorbent in a downstream flow.
【0008】また、本発明の廃棄物処理炉の排ガス中ダ
イオキシン類除去装置は、廃棄物処理炉から排出された
排ガスを冷却した後、バグフィルタで集じんし、集じん
後の排ガス中のダイオキシン類を除去するダイオキシン
類除去装置において、
(1)集じん器の後流に排ガス中のダイオキシン類を酸
化分解する触媒層が形成された触媒反応装置を配設し、
さらに触媒反応装置の後流に排ガス中のミスト状のダイ
オキシン類を吸着する吸着層が形成された吸着装置を接
続したこと
(2)集じん器の後流に排ガス中のダイオキシン類を酸
化分解する触媒層が形成されるとともに、触媒層の後流
にミスト状のダイオキシン類を吸着する吸着層が一つの
缶体に形成された触媒反応・吸着装置を配設したことを
特徴とする。Further, the apparatus for removing dioxins in exhaust gas of a waste treatment furnace of the present invention cools the exhaust gas discharged from the waste treatment furnace, collects it with a bag filter, and dioxins in the exhaust gas after collection. In a dioxin removing device for removing gases, (1) a catalytic reaction device having a catalyst layer for oxidizing and decomposing dioxin in exhaust gas is provided downstream of a dust collector,
Further, an adsorber having an adsorption layer for adsorbing mist-like dioxins in exhaust gas is connected to the downstream of the catalytic reactor (2) Dioxins in exhaust gas are oxidatively decomposed to the downstream of the dust collector A catalyst reaction / adsorption device is provided in which a catalyst layer is formed and an adsorption layer for adsorbing mist-like dioxins is formed in one can body in the downstream of the catalyst layer.
【0009】[0009]
【発明の実施の形態】ミスト状のダイオキシン類は、個
体または液体あるいは油などに捕捉されたもので、ダイ
オキシン濃度の測定の際にろ紙に残ったものである。BEST MODE FOR CARRYING OUT THE INVENTION The mist-like dioxins are those trapped in solids, liquids, oils, etc., and remain on the filter paper when the dioxin concentration is measured.
【0010】本発明において、触媒は、従来の排ガス装
置の触媒反応装置に使用されているもので、例えば前記
の酸化チタン担体に五酸化バナジウムと三酸化タングス
テンを担持させた触媒を使用する。吸着装置あるいは触
媒反応・吸着装置の吸着層には吸着剤として活性炭また
は活性コークスを使用する。In the present invention, the catalyst is used in a conventional catalytic reaction apparatus of an exhaust gas apparatus, and for example, the catalyst in which vanadium pentoxide and tungsten trioxide are supported on the titanium oxide carrier is used. Activated carbon or activated coke is used as an adsorbent in the adsorption layer of the adsorption device or the catalytic reaction / adsorption device.
【0011】触媒は高温の方が、吸着は低温の方が、そ
れぞれダイオキシン類除去に有利であるが、本発明によ
る運転温度は150〜230℃が適当であり、望ましく
は170〜200℃でそれぞれの特性を十分に発揮する
ことができる。排ガスを蝕媒反応装置へ導入する前にN
H3を吹き込み、脱硝を同時に行ってもよい。The catalyst having a higher temperature and the catalyst having a lower temperature are advantageous in removing dioxins, respectively, but the operating temperature according to the present invention is preferably 150 to 230 ° C, and preferably 170 to 200 ° C. The characteristics of can be fully exhibited. Before introducing the exhaust gas into the corrosion medium reactor, N
Denitration may be performed simultaneously by blowing H 3 .
【0012】[0012]
【実施例】実施例1
図1は本発明の排ガス中ダイオキシン類除去方法の実施
例を示すフロー図である。EXAMPLE 1 FIG. 1 is a flow chart showing an example of a method for removing dioxins in exhaust gas according to the present invention.
【0013】廃棄物焼却炉や廃棄物溶融炉等の廃棄物処
理炉から排出される高温の排ガスは冷却されてバグフィ
ルタ1の使用温度(170℃)まで温度が下げられ、反
応助剤(消石灰)を加えて中和し、バグフィルタ1に導
入されて集じんされる。The high-temperature exhaust gas discharged from a waste treatment furnace such as a waste incinerator or a waste melting furnace is cooled to a working temperature (170 ° C.) of the bag filter 1 and a reaction aid (slaked lime). ) Is added to neutralize and is introduced into the bag filter 1 to collect dust.
【0014】バグフィルタ1から排出された排ガスは、
ブロワー2で触媒層3aが形成された触媒反応装置3に
導入され、触媒反応により排ガス中のガス状のダイオキ
シン類を酸化分解する。The exhaust gas discharged from the bag filter 1 is
The blower 2 introduces the catalyst layer 3a into the catalytic reaction device 3 and oxidatively decomposes gaseous dioxins in the exhaust gas by catalytic reaction.
【0015】触媒反応装置3から排出された排ガスは、
吸着剤からなる吸着層4aが形成された吸着装置4に導
入されて、触媒反応装置3で酸化分解できなかったミス
ト状のダイオキシン類を吸着除去する。吸着装置4から
排出された排ガスは煙突から放出する。The exhaust gas discharged from the catalytic reaction device 3 is
It is introduced into the adsorption device 4 in which the adsorption layer 4a made of an adsorbent is formed, and the mist-like dioxins that cannot be oxidized and decomposed in the catalytic reaction device 3 are adsorbed and removed. The exhaust gas discharged from the adsorption device 4 is discharged from the chimney.
【0016】実施例2
図2は本発明の排ガス中ダイオキシン類除去方法の別実
施例を示すフロー図である。Example 2 FIG. 2 is a flow chart showing another example of the method for removing dioxins in exhaust gas according to the present invention.
【0017】実施例1と同様に、バグフィルタ1から排
出された排ガスはブロワー2で触媒反応・吸着装置5に
導入される。なお、本実施例では、排ガスを触媒反応・
吸着装置5に導入する前に触媒反応を促進させる温度に
加熱するために、加熱装置6がバグフィルタ1と触媒反
応・吸着装置5との間に設置されている。As in Example 1, the exhaust gas discharged from the bag filter 1 is introduced into the catalytic reaction / adsorption device 5 by the blower 2. In this example, the exhaust gas was subjected to catalytic reaction.
A heating device 6 is installed between the bag filter 1 and the catalytic reaction / adsorption device 5 in order to heat it to a temperature that accelerates the catalytic reaction before introducing it into the adsorption device 5.
【0018】触媒反応・吸着装置5は、一つの缶体に排
ガス中のダイオキシン類を酸化分解する触媒層5aが形
成されるとともに、触媒層5aの後流に吸着層5bが組
み込まれている。触媒反応・吸着装置5では、触媒層5
aにおいて触媒反応により排ガス中のガス状のダイオキ
シン類を酸化分解し、次いで後流の吸着層5bで触媒層
5aで酸化分解しなかったミスト状のダイオキシン類を
吸着除去する。In the catalytic reaction / adsorption device 5, a catalyst layer 5a for oxidatively decomposing dioxins in exhaust gas is formed in one can body, and an adsorption layer 5b is incorporated in the downstream of the catalyst layer 5a. In the catalytic reaction / adsorption device 5, the catalyst layer 5
In a, the gaseous dioxins in the exhaust gas are oxidatively decomposed by the catalytic reaction, and then the mist-like dioxins which have not been oxidatively decomposed in the catalyst layer 5a are adsorbed and removed in the downstream adsorption layer 5b.
【0019】表1は各実施例のダイオキシン濃度を示す
もので、比較例はバグフィルタの後流に触媒反応装置の
みを設置した例である。Table 1 shows the dioxin concentration of each example, and the comparative example is an example in which only the catalytic reaction device is installed downstream of the bag filter.
【0020】いずれの例も廃棄物溶融炉で溶融処理する
例であり、廃棄物溶融炉から排出される高温の排ガス
は、燃焼室で燃焼され、温水発生器で熱回収され、排ガ
ス温度調節器で170℃に冷却してバグフィルタの使用
温度まで温度を下げ、消石灰で中和され、バグフィルタ
で集じんされ、触媒反応塔に導入される。Each of the examples is an example of melting treatment in a waste melting furnace. High-temperature exhaust gas discharged from the waste melting furnace is burned in a combustion chamber and recovered in heat by a hot water generator, and an exhaust gas temperature controller is provided. The temperature is lowered to 170 ° C. at a temperature of 70 ° C., the temperature is lowered to the operating temperature of the bag filter, the bag filter is neutralized with slaked lime, collected with the bag filter, and introduced into the catalytic reaction tower.
【0021】[0021]
【表1】
表1から明らかなとおり、触媒反応で酸化分解できない
ミスト状のダイオキシン類を吸着層で吸着除去でき、排
ガス中のダイオキシン類の排出濃度を極低濃度にするこ
とができる。[Table 1] As is clear from Table 1, mist-like dioxins that cannot be oxidatively decomposed by catalytic reaction can be adsorbed and removed by the adsorption layer, and the emission concentration of dioxins in the exhaust gas can be made extremely low.
【0022】[0022]
【発明の効果】本発明は、集じん器の後流に触媒反応装
置と吸着装置を直列に設置あるいは既設触媒反応装置の
最後流部を吸着層に置き換えて触媒反応・吸着装置とす
ることにより、触媒で分解できないミスト状のダイオキ
シン類を吸着層で吸着除去することができるので、排ガ
ス中ダイオキシン類の排出濃度を極低濃度にすることが
できる。According to the present invention, the catalytic reaction device and the adsorption device are installed in series in the downstream of the dust collector, or the last flow part of the existing catalytic reaction device is replaced with an adsorption layer to form a catalytic reaction / adsorption device. Since the mist-like dioxins that cannot be decomposed by the catalyst can be adsorbed and removed by the adsorption layer, the emission concentration of dioxins in the exhaust gas can be made extremely low.
【0023】また、本発明は、触媒でダイオキシン類を
二酸化炭素、塩化水素まで分解した後に吸着層を設置す
ることで、吸着剤の使用量削減および破過までの時間を
延長することができ、吸着塔設備をコンパクトにするこ
とができる。Further, according to the present invention, the amount of adsorbent used can be reduced and the time to breakthrough can be extended by disposing the adsorption layer after decomposing dioxins into carbon dioxide and hydrogen chloride with a catalyst. The adsorption tower equipment can be made compact.
【0024】また、缶体に触媒層と吸着層とを一体化し
て触媒反応・吸着装置とすることで簡易な設備とするこ
とができる上に、ダクト長さを短くできることでダイオ
キシン類の極低濃度レベルでの合成を防止することがで
きる。Further, the catalyst layer and the adsorption layer are integrated with the can to form a catalytic reaction / adsorption device, which can be used as a simple facility, and the duct length can be shortened to reduce the dioxins extremely low. It is possible to prevent synthesis at the concentration level.
【図1】本発明の排ガス中ダイオキシン類除去方法のフ
ロー図である。FIG. 1 is a flow chart of a method for removing dioxins in exhaust gas according to the present invention.
【図2】本発明の排ガス中ダイオキシン類除去方法の別
実施例のフロー図である。FIG. 2 is a flow chart of another embodiment of the method for removing dioxins in exhaust gas according to the present invention.
【図3】従来の排ガス処理のフロー図である。FIG. 3 is a flow chart of conventional exhaust gas treatment.
1:バグフィルタ 2:ブロワー 3:触媒反応装置 4:吸着装置 5:触媒反応・吸着装置 5a:触媒層 5b:吸着層 11:焼却炉 12:ガス冷却塔 13:空気予熱器 14:集じん器 15:触媒反応器 16:ブロワー 17:煙突 1: Bug filter 2: Blower 3: Catalytic reaction device 4: Adsorption device 5: Catalytic reaction / adsorption device 5a: catalyst layer 5b: Adsorption layer 11: Incinerator 12: Gas cooling tower 13: Air preheater 14: Dust collector 15: catalytic reactor 16: Blower 17: Chimney
───────────────────────────────────────────────────── フロントページの続き (72)発明者 小林 淳志 北九州市戸畑区大字中原46−59 新日本製 鐵株式会社エンジニアリング事業本部内 (72)発明者 樋口 雅一 北九州市戸畑区大字中原46−59 日鐵プラ ント設計株式会社内 Fターム(参考) 4D002 AA21 AC04 BA04 BA05 BA13 BA14 BA16 CA07 DA41 DA70 EA01 EA02 EA03 GA01 GB03 4D048 AA11 AB01 AB03 CD01 CD03 CD04 CD08 DA03 DA06 4G066 AA04 AA05 BA09 CA33 DA02 ─────────────────────────────────────────────────── ─── Continued front page (72) Inventor Atsushi Kobayashi 46-59 Nakahara, Tobata-ku, Kitakyushu City Made in Japan Engineering Co., Ltd. (72) Inventor Masakazu Higuchi 46-59 Nakahara, Tobata-ku, Kitakyushu Into Design Co., Ltd. F-term (reference) 4D002 AA21 AC04 BA04 BA05 BA13 BA14 BA16 CA07 DA41 DA70 EA01 EA02 EA03 GA01 GB03 4D048 AA11 AB01 AB03 CD01 CD03 CD04 CD08 DA03 DA06 4G066 AA04 AA05 BA09 CA33 DA02
Claims (5)
却した後、集じん器で集じんし、集じん後の排ガス中の
ダイオキシン類を触媒反応により酸化分解し、さらに後
流でミスト状のダイオキシン類を吸着剤により吸着除去
することを特徴とする廃棄物処理炉の排ガス中ダイオキ
シン類除去方法。1. After cooling the exhaust gas discharged from the waste treatment furnace, it is collected by a dust collector, and the dioxins in the exhaust gas after dust collection are oxidatively decomposed by a catalytic reaction, and further in a mist form in the downstream. A method for removing dioxins in exhaust gas from a waste treatment furnace, which comprises adsorbing and removing the dioxins of the above with an adsorbent.
とを特徴とする請求項1記載の廃棄物処理炉の排ガス中
ダイオキシン類除去方法。2. The method for removing dioxins from exhaust gas in a waste treatment furnace according to claim 1, wherein the exhaust gas temperature is 150 to 230 ° C.
却した後、バグフィルタで集じんし、集じん後の排ガス
中のダイオキシン類を除去するダイオキシン類除去装置
において、 集じん器の後流に排ガス中のダイオキシン類を酸化分解
する触媒層が形成された触媒反応装置を配設し、さらに
触媒反応装置の後流に排ガス中のミスト状のダイオキシ
ン類を吸着する吸着層が形成された吸着装置を接続した
ことを特徴とする廃棄物処理炉の排ガス中ダイオキシン
類除去装置。3. A dioxin-removing device that cools exhaust gas discharged from a waste treatment furnace, collects it with a bag filter, and removes dioxins from the exhaust gas after collecting dust, in a downstream flow of the dust collector. A catalytic reaction device with a catalyst layer that oxidatively decomposes dioxins in exhaust gas is formed in the adsorption reactor, and an adsorption layer that adsorbs mist-like dioxins in exhaust gas is formed in the downstream of the catalytic reaction device. A device for removing dioxins from exhaust gas of a waste treatment furnace, which is characterized by connecting the device.
却した後、集じん器で集じんし、集じん後の排ガス中の
ダイオキシン類を除去するダイオキシン類除去装置にお
いて、 集じん器の後流に排ガス中のダイオキシン類を酸化分解
する触媒層が形成されるとともに、触媒層の後流にミス
ト状のダイオキシン類を吸着する吸着層が一つの缶体に
形成された触媒反応・吸着装置を配設したことを特徴と
する廃棄物処理炉の排ガス中ダイオキシン類除去装置。4. A dioxin-removing device that cools exhaust gas discharged from a waste treatment furnace, collects it with a dust collector, and removes dioxins in the exhaust gas after dust collection. A catalytic reaction / adsorption device in which a catalyst layer that oxidatively decomposes dioxins in exhaust gas is formed in the flow and an adsorption layer that adsorbs mist-like dioxins is formed in one can body in the downstream of the catalyst layer. A device for removing dioxins from exhaust gas in a waste treatment furnace, which is characterized by being provided.
性コークスであることを特徴とする請求項3または4記
載の廃棄物処理炉の排ガス中ダイオキシン類除去装置。5. The apparatus for removing dioxins in exhaust gas of a waste treatment furnace according to claim 3 or 4, wherein the adsorbent used in the adsorption layer is activated carbon or activated coke.
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JP2006334451A (en) * | 2005-05-31 | 2006-12-14 | Jfe Steel Kk | Coke oven exhaust gas treatment method and treatment equipment, and coke production method |
JP2007296513A (en) * | 2006-04-07 | 2007-11-15 | Nippon Steel Corp | Gasification gas purification method and purification device |
JP2008068192A (en) * | 2006-09-13 | 2008-03-27 | Nippon Steel Engineering Co Ltd | Asbestos waste treatment apparatus and method |
JP2013111549A (en) * | 2011-11-30 | 2013-06-10 | Taiheiyo Cement Corp | Adsorbent for adsorbing organic chlorine compound in exhaust gas, and method for producing the same and method for using the same |
JP2018065089A (en) * | 2016-10-19 | 2018-04-26 | 株式会社プランテック | Exhaust gas treatment apparatus |
CN109799314A (en) * | 2019-03-27 | 2019-05-24 | 盛守祥 | A kind of catalyst activity evaluating apparatus and method |
US11202990B2 (en) * | 2015-09-04 | 2021-12-21 | Hidrosym S.A. | Decontamination procedure using a biofilter to retain and recycle particulate matter from combustion fumes |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006334451A (en) * | 2005-05-31 | 2006-12-14 | Jfe Steel Kk | Coke oven exhaust gas treatment method and treatment equipment, and coke production method |
JP2007296513A (en) * | 2006-04-07 | 2007-11-15 | Nippon Steel Corp | Gasification gas purification method and purification device |
JP2008068192A (en) * | 2006-09-13 | 2008-03-27 | Nippon Steel Engineering Co Ltd | Asbestos waste treatment apparatus and method |
JP2013111549A (en) * | 2011-11-30 | 2013-06-10 | Taiheiyo Cement Corp | Adsorbent for adsorbing organic chlorine compound in exhaust gas, and method for producing the same and method for using the same |
US11202990B2 (en) * | 2015-09-04 | 2021-12-21 | Hidrosym S.A. | Decontamination procedure using a biofilter to retain and recycle particulate matter from combustion fumes |
JP2018065089A (en) * | 2016-10-19 | 2018-04-26 | 株式会社プランテック | Exhaust gas treatment apparatus |
CN109799314A (en) * | 2019-03-27 | 2019-05-24 | 盛守祥 | A kind of catalyst activity evaluating apparatus and method |
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