JP2000233112A - Waste gas treatment apparatus - Google Patents

Waste gas treatment apparatus

Info

Publication number
JP2000233112A
JP2000233112A JP11035421A JP3542199A JP2000233112A JP 2000233112 A JP2000233112 A JP 2000233112A JP 11035421 A JP11035421 A JP 11035421A JP 3542199 A JP3542199 A JP 3542199A JP 2000233112 A JP2000233112 A JP 2000233112A
Authority
JP
Japan
Prior art keywords
adsorbent
powdered
exhaust gas
gas treatment
dust
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.)
Withdrawn
Application number
JP11035421A
Other languages
Japanese (ja)
Inventor
Hisatsugu Kitaguchi
久継 北口
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP11035421A priority Critical patent/JP2000233112A/en
Publication of JP2000233112A publication Critical patent/JP2000233112A/en
Withdrawn legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To remove harmful components such as dioxins to the full extent by efficiently utilizing an adsorbent employed for a packed-layer adsorption- regeneration method at the time of adsorptive removal of harmful components such as dioxins of a waste gas. SOLUTION: This waste gas treatment apparatus comprises a dust collecting apparatus 2, a packed-layer 4 filled with a carbon-based adsorbent in the downstream side of the apparatus 2, a regeneration apparatus 6 for regenerating the adsorbent whose adsorption capability is deteriorated, and a separation apparatus 7 for separating a regenerated adsorbent, a powdered adsorbent, and dust. A blowing apparatus 9 to blow the powdered adsorbent containing dust to the inlet side of a duct of the dust collecting apparatus 2 is installed in the waste gas treatment apparatus.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、例えば都市ゴミや
産業廃棄物の焼却設備、鉄鋼電気炉、鉄鋼焼結機から排
出されるダイオキシン等の有害物質の除去に有効な排ガ
スの処理装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating exhaust gas which is effective for removing harmful substances such as dioxin discharged from incineration equipment of municipal garbage and industrial waste, steel electric furnaces and steel sintering machines. It is.

【0002】[0002]

【従来の技術】ダイオキシン等の有害物質を含む排ガス
の吸着処理方法として、充填層による吸着技術と粉末の
吸着剤の吹き込み技術が存在する。充填層による吸着技
術としては、特開平7−763号公報に示されるよう
な、ダイオキシン類を含む90〜120℃の排ガスを活
性炭または活性コ−クスを充填した十字流移動層吸着装
置に送り、ダイオキシン類を除去し、使用した活性炭ま
たは活性コ−クスを加熱再生し、循環使用する方法があ
る。また、吸着剤吹き込み技術としては、特開平10−
19237号公報に示されるような、吸着剤を集塵装置
の上流側の排ガスに供給し、吸着剤とダストを捕集し、
それを燃焼器に供給する方法や、特開平8−24333
41号公報に示されるような、焼却排ガスを減温し除塵
した後に、吸着剤を添加してバグフィルタにより吸着材
を回収することを特徴とする排ガス処理方法がある。
2. Description of the Related Art As a method of adsorbing exhaust gas containing harmful substances such as dioxin, there are an adsorbing technique using a packed bed and a blowing technique of a powder adsorbent. As an adsorption technique using a packed bed, as disclosed in Japanese Patent Application Laid-Open No. 7-763, an exhaust gas at 90 to 120 ° C. containing dioxins is sent to a cross-flow moving bed adsorption apparatus filled with activated carbon or activated coke. There is a method in which dioxins are removed, the activated carbon or activated coke used is heated and regenerated, and recycled. In addition, as an adsorbent injection technique, Japanese Patent Application Laid-Open
No. 19237, an adsorbent is supplied to the exhaust gas on the upstream side of the dust collector, and the adsorbent and dust are collected.
A method for supplying it to a combustor,
There is an exhaust gas treatment method as disclosed in Japanese Patent Publication No. 41, wherein the temperature of incinerated exhaust gas is reduced and dust is removed, and then an adsorbent is added and the adsorbent is collected by a bag filter.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
特開平7−763号公報の移動層吸着、使用後再生再循
環の方法では、吸着剤の一部が粉化し、粉化した吸着剤
は細粒のため移動層で再利用できず、粉化吸着剤は再生
後、ふるい分けられ、焼却炉などの排ガス発生設備に戻
され、焼却廃棄される。
However, in the method of moving bed adsorption and recycling after use described in JP-A-7-763, a part of the adsorbent is powdered, and the powdered adsorbent is finely divided. The powdered adsorbent cannot be reused in the moving bed due to the particles, and the powdered adsorbent is sieved after regeneration, returned to an exhaust gas generation facility such as an incinerator, and incinerated.

【0004】また、特開平10−19237号公報の吸
着剤の吹き込みでは、ダストとともに吸着剤は回収され
るため、再生が困難となり、吸着剤の再使用ができな
い。さらに、特開平8−2433341号公報の場合
は、上記問題を回避するために、除塵後に吸着剤を回収
し、再生、再使用するものである。しかし、この方法で
は通常の除塵機の後に、吸着剤回収用のバグフィルター
が余分に必要となる。
In addition, in the blowing of the adsorbent disclosed in Japanese Patent Application Laid-Open No. 10-19237, the adsorbent is collected together with the dust, so that it is difficult to regenerate the adsorbent and the adsorbent cannot be reused. Further, in the case of Japanese Patent Application Laid-Open No. 8-2433331, in order to avoid the above-described problem, the adsorbent is collected after dust removal, regenerated, and reused. However, this method requires an extra bag filter for collecting the adsorbent after the ordinary dust remover.

【0005】したがって、いずれの従来方法も高価な吸
着剤を有効に利用しているといえない。そこで本発明
は、上記従来技術の問題点を解消し、充填層吸着−再生
方式で使用される吸着剤を効率的に利用し、ダイオキシ
ンなどの有害成分を高度に除去できる排ガスの処理装置
を提供することを目的とする。
[0005] Therefore, it cannot be said that any conventional method effectively utilizes an expensive adsorbent. Therefore, the present invention solves the above-mentioned problems of the prior art, and provides an exhaust gas treatment apparatus capable of efficiently using a sorbent used in a packed bed adsorption-regeneration method and highly removing harmful components such as dioxin. The purpose is to do.

【0006】[0006]

【課題を解決するための手段】炭素系吸着剤を用いた充
填層吸着−再生方式の排ガス処理方法において、加熱再
生後、ふるい分けられた粉化吸着剤に、充填層に使用さ
れている粒状の吸着剤よりも高い吸着力があることを見
出し、本発明を完成するに至った。
SUMMARY OF THE INVENTION In an exhaust gas treatment method using a packed bed adsorption-regeneration system using a carbon-based adsorbent, after heating and regeneration, the sieved powdered adsorbent is added to the granular material used in the packed bed. The inventors have found that they have a higher adsorptive power than the adsorbent, and have completed the present invention.

【0007】すなわち本発明は、集塵機とその下流に炭
素系吸着剤を充填した充填層と吸着性能が低下した吸着
剤を再生する再生装置、及び再生吸着剤と粉化吸着剤を
分離する分離装置を有する排ガス処理装置において、粉
化吸着剤を集塵機の入側煙道に吹き込むための吹き込み
装置を設けたことを特徴とする排ガスの処理装置であ
る。さらに、吹き込んだ粉化吸着剤を集塵機で回収し、
回収された吸着剤を排ガス発生設備に装入するか、また
は、ダストにシリカやアルミナなどの灰分が多い場合は
灰溶融炉に装入する。また、本発明の炭素系吸着剤とし
ては、活性炭または活性コークスが好ましい。排ガス発
生設備は、例えばゴミ焼却炉や鉄鉱石の焼結設備のよう
にダイオキシンなどの有害物質を含有する排ガスを発生
する設備をさす。
That is, the present invention provides a dust collector, a packed bed filled with a carbon-based adsorbent downstream thereof, and a regenerating apparatus for regenerating an adsorbent having reduced adsorption performance, and a separating apparatus for separating a regenerated adsorbent from a powdered adsorbent. The exhaust gas treatment device according to claim 1, further comprising a blowing device for blowing the powdered adsorbent into an inlet flue of the dust collector. Furthermore, the blown powdered adsorbent is collected by a dust collector,
The recovered adsorbent is charged into an exhaust gas generation facility, or charged into an ash melting furnace when the dust contains a large amount of ash such as silica or alumina. Activated carbon or activated coke is preferred as the carbon-based adsorbent of the present invention. The exhaust gas generation equipment refers to equipment that generates exhaust gas containing harmful substances such as dioxin, such as a garbage incinerator or a sintering equipment for iron ore.

【0008】本発明は、充填層吸着技術における粉化活
性炭の有効利用と、吸着剤吹き込み排ガス処理技術にお
ける高価な吸着剤の使用回避とともに、吸着剤吹き込み
技術と充填層吸着技術を組み合わせることにより、高度
な排ガス処理技術を可能にする。
[0008] The present invention combines the effective use of powdered activated carbon in the packed bed adsorption technology, the avoidance of the use of expensive adsorbent in the adsorbent injection exhaust gas treatment technology, and the combination of the adsorbent injection technology and the packed bed adsorption technology. Enables advanced exhaust gas treatment technology.

【0009】[0009]

【発明の実施の形態】(実施の形態1)以下、本発明の
実施形態を図1に示す焼結設備の排ガス処理を例にとり
説明する。焼結機1、電気集塵機2、誘引通風機3、活
性炭または活性コークス吸着剤充填層4、煙突5、およ
び吸着剤再生装置6、再生吸着剤と粉化吸着剤の分離装
置7からなる排ガス処理設備において、焼結機1から排
出された排ガスは電気集塵機2で除塵後、吸着剤充填層
4に導入され、ダイオキシンやその他の有害物質が吸着
除去される。また、充填層内では一部の吸着剤は粉化す
る。吸着性能が低下した吸着剤aは、充填層4より引き
出され再生装置6により不活性ガス雰囲気で加熱再生処
理され、吸着されたダイオキシンは加熱により分解除去
され、吸着剤aの吸着性能が再生される。再生装置6に
より再生された吸着剤a′は粉化吸着剤bを混在してい
るため、分離装置7にて再生吸着剤a′と粉化吸着剤b
が分離され、再生吸着剤a′は充填層4に戻され循環使
用される。従来、粉化吸着剤bは、充填層4に戻すと、
ガス流通阻害を引き起こすため、充填層4に戻すことが
できず、大部分が炭素であるため製鉄所の燃料として利
用されていた。
(Embodiment 1) Hereinafter, an embodiment of the present invention will be described with reference to an example of exhaust gas treatment of a sintering facility shown in FIG. Exhaust gas treatment comprising a sintering machine 1, an electric dust collector 2, an induction ventilator 3, an activated carbon or activated coke adsorbent packed bed 4, a chimney 5, and an adsorbent regenerating device 6, a separating device 7 for regenerated adsorbent and powdered adsorbent. In the equipment, exhaust gas discharged from the sintering machine 1 is dust-removed by the electric dust collector 2, and then introduced into the adsorbent packed layer 4, where dioxin and other harmful substances are adsorbed and removed. Some adsorbents are powdered in the packed bed. The adsorbent a having reduced adsorption performance is drawn out of the packed bed 4 and subjected to heat regeneration treatment in an inert gas atmosphere by the regenerating device 6, and the adsorbed dioxin is decomposed and removed by heating to regenerate the adsorption performance of the adsorbent a. You. Since the adsorbent a 'regenerated by the regenerating device 6 contains the powdered adsorbent b, the regenerated adsorbent a' and the powdered adsorbent b
Is separated, and the regenerated adsorbent a 'is returned to the packed bed 4 and recycled. Conventionally, when the powdered adsorbent b is returned to the packed bed 4,
Since the gas flow was hindered, it could not be returned to the packed bed 4 and was mostly used as fuel for steelworks because it was mostly carbon.

【0010】これに対して本発明では、粉化吸着剤貯留
ホッパー8および焼結機1と電気集塵機2の間の煙道に
粉化吸着剤吹き込み装置9を設け、粉化吸着剤bを吹き
込み、ダイオキシンやその他の有害物質を吸着除去し、
粉化吸着剤bを電気集塵機2で回収する。回収された粉
化吸着剤b′は製鉄所の燃料として利用される。例え
ば、焼結機1に戻され、焼結機の燃料である粉コークス
の代替として利用され、吸着ダイオキシンは燃焼分解さ
れる。ここで粉化吸着剤は、発生量の全量を吹き込みに
使用することが可能であるが、発生量や電気集塵機の能
力に応じて吹き込み量を調整する。余剰の粉化吸着剤は
直接燃焼利用とするか、または、他の排ガス処理装置の
吹き込み剤として利用することができる。
On the other hand, in the present invention, the powdered adsorbent b is supplied to the powdered adsorbent storage hopper 8 and the flue between the sintering machine 1 and the electrostatic precipitator 2 to blow the powdered adsorbent b. Adsorbs and removes dioxins and other harmful substances,
The powdered adsorbent b is collected by the electric dust collector 2. The recovered powdered adsorbent b 'is used as fuel for steelworks. For example, the adsorbed dioxin is returned to the sintering machine 1 and used as a substitute for coke breeze which is the fuel of the sintering machine, and the adsorbed dioxin is decomposed by combustion. Here, the entire amount of the powdered adsorbent can be used for blowing, but the blowing amount is adjusted according to the generated amount and the capacity of the electric dust collector. The excess powdered adsorbent can be used for direct combustion or as a blowing agent for other exhaust gas treatment devices.

【0011】粉化吸着剤は、循環使用を繰り返し行った
ため強度が低下し粉化したものであり、このため、加熱
再生処理も何度も受けている。炭素系の吸着剤は加熱再
生処理により、比表面積が増大し、活性が向上する。し
たがって、再生後の粉化吸着剤は、通常の吸着剤よりも
比表面積が大きいため、吸着性能が高く、市販の吹き込
み剤よりも高吸着性能を有する。さらに、カリウムや鉄
などの酸化活性を有する微細なダストを担持しているた
め、焼結機に戻した場合、一般の粉コークスよりも燃焼
性が良く、吸着ダイオキシンは効率よく分解される。
[0011] The powdered adsorbent has been reduced in strength and powdered due to repeated use, and thus has been subjected to heat regeneration treatment many times. The specific surface area and the activity of the carbon-based adsorbent are increased by the heat regeneration treatment. Therefore, since the powdered adsorbent after regeneration has a larger specific surface area than a normal adsorbent, it has high adsorption performance, and has higher adsorption performance than a commercially available blowing agent. Furthermore, since it carries fine dust having an oxidizing activity such as potassium or iron, when returned to a sintering machine, it has better flammability than general coke breeze and adsorbed dioxin is decomposed efficiently.

【0012】(実施の形態2)以下、本発明の別の実施
形態をゴミ焼却設備の排ガス処理を例にとり図2ととも
に説明する。焼却炉10、ガス冷却塔11、バグフィル
ター12、誘引通風機3、活性炭または活性コークス吸
着剤充填層4、煙突5、および吸着剤再生装置6、再生
吸着剤と粉化吸着剤の分離装置7からなる排ガス処理設
備において、焼却炉10から排出された排ガスはガス冷
却塔11で冷却、バグフィルター12で除塵後、吸着剤
充填層4に導入され、ダイオキシンやその他の有害物質
が吸着除去される。また、充填層内では一部の吸着剤は
粉化する。吸着性能が低下した吸着剤aは、充填層4よ
り引き出され、再生装置6により不活性ガス雰囲気で加
熱再生処理され、吸着されたダイオキシンは加熱により
分解除去され、吸着剤aの吸着性能が再生される。再生
装置により再生された吸着剤a′は粉化吸着剤bを混在
しているため分離装置7にて再生吸着剤a′と粉化吸着
剤bが分離され、再生吸着剤a′は充填層4に戻され循
環使用される。従来、粉化吸着剤bは、吸着塔に戻す
と、ガスの流通阻害を引き起こすため、充填層に戻すこ
とができず、大部分が炭素であるため焼却炉10で燃焼
廃棄される。
(Embodiment 2) Hereinafter, another embodiment of the present invention will be described with reference to FIG. Incinerator 10, gas cooling tower 11, bag filter 12, induction ventilator 3, activated carbon or activated coke adsorbent packed bed 4, chimney 5, adsorbent regenerating device 6, separation device 7 for regenerated adsorbent and powdered adsorbent The exhaust gas discharged from the incinerator 10 is cooled in the gas cooling tower 11, dust is removed by the bag filter 12, introduced into the adsorbent packed bed 4, and dioxin and other harmful substances are adsorbed and removed. . Some adsorbents are powdered in the packed bed. The adsorbent a having reduced adsorption performance is withdrawn from the packed bed 4 and heated and regenerated in an inert gas atmosphere by the regenerating device 6, and the adsorbed dioxin is decomposed and removed by heating to regenerate the adsorption performance of the adsorbent a. Is done. Since the adsorbent a 'regenerated by the regenerating device contains the powdered adsorbent b, the regenerated adsorbent a' and the powdered adsorbent b are separated by the separating device 7, and the regenerated adsorbent a 'is filled with the packed bed. It is returned to 4 and used cyclically. Conventionally, when the powdered adsorbent b is returned to the adsorption tower, the flow of gas is hindered. Therefore, the powder adsorbent b cannot be returned to the packed bed.

【0013】これに対して本発明では、粉化吸着剤貯留
ホッパー8および冷却塔11とバグフィルター12の間
の煙道に粉化吸着剤吹き込み装置9を設け、粉化吸着剤
bを吹き込み、ダイオキシンやその他の有害物質を吸着
除去し、粉化吸着剤bをバグフィルター12で回収す
る。回収された粉化吸着剤b′はシリカやアルミナなど
の灰分を含有するダストの一部として回収されるため、
灰溶融炉13に装入され溶融処理する。通常の灰溶融処
理されるダストに対して、本発明で捕集されたダスト
は、粉化吸着剤が炭素系であり、ダストと均一に混合さ
れているため、粉化吸着剤が溶融炉の燃料として利用で
き効率的な溶融処理が可能となる。
On the other hand, in the present invention, a powdered adsorbent blowing device 9 is provided in the powdered adsorbent storage hopper 8 and the flue between the cooling tower 11 and the bag filter 12 to blow the powdered adsorbent b. Dioxin and other harmful substances are adsorbed and removed, and the powdered adsorbent b is collected by the bag filter 12. Since the recovered powdered adsorbent b 'is recovered as part of dust containing ash such as silica and alumina,
It is charged into the ash melting furnace 13 and subjected to melting processing. The dust collected in the present invention, compared to the dust that is subjected to normal ash melting treatment, has a powdered adsorbent that is carbon-based and is uniformly mixed with the dust. It can be used as fuel and efficient melting process is possible.

【0014】[0014]

【発明の効果】以上の本発明によれば、充填層吸着技術
における粉化吸着剤の有効利用と、吸着剤吹き込み排ガ
ス処理技術における高価吸着剤の使用回避とともに、吸
着剤吹き込み技術と充填層吸着技術を組み合わせること
により、高度で効率的な排ガス処理技術を可能にする。
According to the present invention described above, the effective use of the powdered adsorbent in the packed bed adsorption technology, the avoidance of the use of the expensive adsorbent in the adsorbent injection exhaust gas treatment technology, and the adsorbent injection technology and the packed bed adsorption are achieved. Combining technologies enables advanced and efficient exhaust gas treatment technology.

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

【図1】焼結機排ガス処理装置の全体構成の一例を示す
図である。
FIG. 1 is a diagram showing an example of the overall configuration of a sintering apparatus for treating exhaust gas.

【図2】焼却炉排ガス処理装置の全体構成の一例を示す
図である。
FIG. 2 is a diagram showing an example of the overall configuration of an incinerator exhaust gas treatment device.

【符号の説明】[Explanation of symbols]

1 焼結機 2 電気集塵機 3 誘引通風機 4 吸着剤充填層 5 煙突 6 吸着剤再生装置 7 吸着剤分離装置 8 貯留ホッパー 9 吹き込み装置 10 焼却炉 11 ガス冷却塔 12 バグフィルタ
ー 13 灰溶融炉 a,a′ 吸着剤 b,b′ 粉化吸着剤
DESCRIPTION OF SYMBOLS 1 Sintering machine 2 Electric precipitator 3 Induction ventilator 4 Adsorbent filling layer 5 Chimney 6 Adsorbent regeneration device 7 Adsorbent separation device 8 Storage hopper 9 Blowing device 10 Incinerator 11 Gas cooling tower 12 Bag filter 13 Ash melting furnace a, a 'adsorbent b, b' powdered adsorbent

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 集塵機とその下流に炭素系吸着剤を充填
した充填層と吸着性能が低下した吸着剤を再生する再生
装置、及び再生吸着剤と粉化吸着剤を分離する分離装置
を有する排ガス処理装置において、粉化吸着剤を集塵機
の入側煙道に吹き込むための吹き込み装置を設けたこと
を特徴とする排ガスの処理装置。
An exhaust gas having a dust collector, a packed bed filled with a carbon-based adsorbent downstream thereof, a regenerating device for regenerating an adsorbent having reduced adsorption performance, and a separating device for separating the regenerated adsorbent from the powdered adsorbent. An exhaust gas treatment device, characterized in that a treatment device is provided with a blowing device for blowing a powdered adsorbent into an inlet flue of a dust collector.
【請求項2】 炭素系吸着剤が活性炭または活性コーク
スであることを特徴とする請求項1記載の排ガスの処理
装置。
2. The exhaust gas treatment apparatus according to claim 1, wherein the carbon-based adsorbent is activated carbon or activated coke.
【請求項3】 集塵機で回収されたダストを含む粉化吸
着剤を排ガス発生設備に装入するようにしたことを特徴
とする請求項1または2記載の排ガスの処理装置。
3. The exhaust gas treatment apparatus according to claim 1, wherein the powdered adsorbent containing dust collected by the dust collector is charged into an exhaust gas generation facility.
【請求項4】 集塵機で回収されたダストを含む粉化吸
着剤を灰溶融装置に装入するようにしたことを特徴とす
る請求項1または2記載の排ガスの処理装置。
4. The exhaust gas treatment device according to claim 1, wherein the powdered adsorbent containing dust collected by the dust collector is charged into the ash melting device.
JP11035421A 1999-02-15 1999-02-15 Waste gas treatment apparatus Withdrawn JP2000233112A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11035421A JP2000233112A (en) 1999-02-15 1999-02-15 Waste gas treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11035421A JP2000233112A (en) 1999-02-15 1999-02-15 Waste gas treatment apparatus

Publications (1)

Publication Number Publication Date
JP2000233112A true JP2000233112A (en) 2000-08-29

Family

ID=12441419

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11035421A Withdrawn JP2000233112A (en) 1999-02-15 1999-02-15 Waste gas treatment apparatus

Country Status (1)

Country Link
JP (1) JP2000233112A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006286645A (en) * 2005-04-04 2006-10-19 Lg Chem Ltd Lithium secondary battery containing silicon-based or tin-based anode active material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006286645A (en) * 2005-04-04 2006-10-19 Lg Chem Ltd Lithium secondary battery containing silicon-based or tin-based anode active material
JP4541315B2 (en) * 2005-04-04 2010-09-08 エルジー・ケム・リミテッド Lithium secondary battery containing silicon-based or tin-based anode active material

Similar Documents

Publication Publication Date Title
JP3207019B2 (en) How to remove harmful substances in exhaust gas
US5405812A (en) Method and arrangement for purifying a carbon-containing adsorption medium
JP5496734B2 (en) Cement kiln exhaust gas treatment apparatus and treatment method
JP2000157832A (en) Treatment of waste activated carbon and treatment of activated coke
JP2000140627A (en) Dioxin removing material, dioxin removing method and regenerating method of dioxin removing material
JPH05220338A (en) Treating equipment for exhaust gas of refuse incinerator
JP2010116283A (en) Apparatus and method for processing exhaust gas of cement kiln
JP4735353B2 (en) Exhaust gas treatment method
JP3411484B2 (en) Desorption gas treatment method in exhaust gas treatment equipment of garbage incinerator
JP2007083221A (en) Exhaust gas treatment method
JP2000233112A (en) Waste gas treatment apparatus
JP2009203117A (en) Treatment device and method of cement kiln exhaust gas
JP2010261033A (en) Use of oxygen concentrator for separating n2 from blast furnace gas
JP4084533B2 (en) Dioxins adsorption removal method and decomposition method
JPH08243341A (en) Treatment of waste gas
JP2001017833A (en) Method and device for dry treatment of exhaust gas
JPH11104456A (en) Operation of waste gas treatment apparatus in waste incinerator
JPH09248425A (en) Dioxine removing material, dioxine removing method, exhaust gas treatment equipment and dioxine removing material-regenerating method
JP3459994B2 (en) Method and apparatus for regenerating adsorbent for removing harmful substances in exhaust gas
JP2678534B2 (en) Exhaust gas treatment method after incineration of garbage
JP4241693B2 (en) Combustion exhaust gas treatment method
JP3040357B2 (en) Exhaust gas purification method in sintering machine
JP3469153B2 (en) Exhaust gas treatment equipment
JP3401485B2 (en) Method and apparatus for recycling activated carbon
JP3596424B2 (en) Exhaust gas treatment method and treatment device

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20060509