JP2000042362A - Waste gas treating device and method - Google Patents
Waste gas treating device and methodInfo
- Publication number
- JP2000042362A JP2000042362A JP10213795A JP21379598A JP2000042362A JP 2000042362 A JP2000042362 A JP 2000042362A JP 10213795 A JP10213795 A JP 10213795A JP 21379598 A JP21379598 A JP 21379598A JP 2000042362 A JP2000042362 A JP 2000042362A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- activated carbon
- dioxin
- dust remover
- alkali
- 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
Landscapes
- Treating Waste Gases (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、排ガス処理装置
及び方法に係り、特にダイオキシンや塩化水素、硫黄酸
化物等の酸性ガスが発生するキルンからの排ガスを活性
炭や消石灰等のアルカリを用いて処理する装置及び方法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for treating exhaust gas, and more particularly to treating an exhaust gas from a kiln which generates an acidic gas such as dioxin, hydrogen chloride and sulfur oxide using an alkali such as activated carbon or slaked lime. Apparatus and method.
【0002】[0002]
【従来の技術】近年、都市ごみ等の廃棄物は著しく増加
し、これら廃棄物の有効利用、再資源化を図る目的で、
都市ごみ焼却灰等を原料の一部に用いる環境調和型セメ
ント(以下、エコセメントと称す)の製造が試みられて
いる。焼却灰に石灰石、粘土類等の天然原料を混合して
セメント調合原料とし、これをロータリーキルン等で焼
成することにより、エコセメントが製造される。2. Description of the Related Art In recent years, the amount of waste such as municipal solid waste has increased remarkably, and for the purpose of effective use and recycling of such waste,
Attempts have been made to produce environmentally friendly cement (hereinafter referred to as ecocement) using incinerated ash from municipal solid waste as part of the raw material. Eco-cement is produced by mixing incinerated ash with natural raw materials such as limestone and clays to prepare a cement-mixed raw material and firing it in a rotary kiln or the like.
【0003】原料の一部に都市ごみ焼却灰等を用いるこ
とから、ロータリーキルンで発生する排ガスにはダイオ
キシンや塩化水素、硫黄酸化物等の酸性ガスが含まれる
惧れがあり、従来は、図4に示されるような排ガス処理
装置で処理していた。すなわち、キルン1から排出され
た排ガスは排ガス冷却塔2で冷却された後、この排ガス
に活性炭と消石灰等のアルカリが添加される。これによ
り、排ガス中に含まれているダイオキシンは活性炭に吸
着され、塩化水素や硫黄酸化物等の酸性ガスはアルカリ
と反応して除去される。次に、除塵機3によって除塵が
なされるが、このとき排ガスから焼却飛灰と共にダイオ
キシンが吸着された活性炭や、塩化水素や硫黄酸化物等
の酸性ガスの除去に用いられたアルカリがまとめて捕集
されることとなる。除塵機3を出た排ガスは煙突4から
大気中へ放出される。[0003] Since municipal solid waste incineration ash and the like are used as a part of the raw material, the exhaust gas generated from the rotary kiln may contain acidic gases such as dioxin, hydrogen chloride and sulfur oxide. In the exhaust gas treatment device shown in FIG. That is, after the exhaust gas discharged from the kiln 1 is cooled in the exhaust gas cooling tower 2, an activated carbon and an alkali such as slaked lime are added to the exhaust gas. As a result, the dioxin contained in the exhaust gas is adsorbed on the activated carbon, and the acidic gas such as hydrogen chloride or sulfur oxide reacts with the alkali to be removed. Next, dust is removed by the dust remover 3. At this time, activated carbon to which dioxin is adsorbed together with incineration fly ash from the exhaust gas and alkali used to remove acidic gases such as hydrogen chloride and sulfur oxide are collectively collected. Will be gathered. The exhaust gas leaving the dust remover 3 is discharged from the chimney 4 into the atmosphere.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、ダイオ
キシンが吸着された活性炭や、塩化水素や硫黄酸化物等
の酸性ガスの除去に用いられたアルカリは、焼却飛灰と
一緒にまとめて捕集されるので、これらを有効利用する
ことができず、従来は焼却飛灰と共にセメント固化し、
埋め立て処理等に用いるのみであった。However, the activated carbon to which dioxin is adsorbed and the alkali used to remove acidic gases such as hydrogen chloride and sulfur oxides are collected together with the incinerated fly ash. Therefore, these materials cannot be used effectively, and in the past, cement solidified together with incineration fly ash,
It was only used for landfill treatment.
【0005】この発明はこのような問題点を解消するた
めになされたもので、排ガス中のダイオキシン除去に用
いられた活性炭の有効利用を図ることができる排ガス処
理装置及び方法を提供することを目的とする。また、排
ガス中の塩化水素や硫黄酸化物等の酸性ガスの除去に用
いられたアルカリの有効利用を図ることができる排ガス
処理装置及び方法を提供することも目的としている。The present invention has been made to solve such a problem, and an object of the present invention is to provide an exhaust gas treatment apparatus and a method capable of effectively utilizing activated carbon used for removing dioxin in exhaust gas. And It is another object of the present invention to provide an exhaust gas treatment apparatus and method capable of effectively utilizing alkali used for removing acidic gases such as hydrogen chloride and sulfur oxides in exhaust gas.
【0006】[0006]
【課題を解決するための手段】この発明に係る排ガス処
理装置は、キルンで発生した排ガスから焼却飛灰を回収
する第1の除塵機と、第1の除塵機で焼却飛灰が回収さ
れた排ガスに活性炭を添加して排ガス中のダイオキシン
を吸着させる活性炭添加装置と、活性炭が添加された排
ガスからダイオキシンを吸着した活性炭を回収する第2
の除塵機とを備えたものである。なお、第1の除塵機で
焼却飛灰が回収された排ガスにアルカリを添加して排ガ
ス中の塩化水素や硫黄酸化物等の酸性ガスを除去するア
ルカリ添加装置をさらに備え、第2の除塵機が使用した
活性炭とアルカリを同時に回収するように構成すること
ができる。An exhaust gas treatment apparatus according to the present invention has a first dust remover for collecting incineration fly ash from exhaust gas generated in a kiln, and an incineration fly ash collected by the first dust remover. Activated carbon addition device for adding activated carbon to exhaust gas to adsorb dioxin in exhaust gas, and second for collecting activated carbon adsorbing dioxin from exhaust gas to which activated carbon is added
And a dust remover. The apparatus further includes an alkali addition device for adding an alkali to the exhaust gas from which the incineration fly ash is collected by the first dust remover to remove acidic gases such as hydrogen chloride and sulfur oxides in the exhaust gas. Can be configured to simultaneously recover the activated carbon and the alkali used.
【0007】また、この発明に係る排ガス処理方法は、
キルンで発生した排ガスから焼却飛灰を回収し、焼却飛
灰が回収された排ガスに活性炭を添加して排ガス中のダ
イオキシンを吸着させ、活性炭が添加された排ガスから
ダイオキシンを吸着した活性炭を回収する方法である。
なお、活性炭と共に排ガスにアルカリを添加して排ガス
中の塩化水素や硫黄酸化物等の酸性ガスを除去し、使用
した活性炭とアルカリを同時に回収するように構成して
もよい。[0007] Further, an exhaust gas treatment method according to the present invention comprises:
Recover incineration fly ash from the flue gas generated in the kiln, add activated carbon to the recovered flue gas from the incineration fly ash to adsorb dioxin in the flue gas, and recover dioxin-adsorbed activated carbon from the flue gas containing activated carbon Is the way.
In addition, an alkali may be added to the exhaust gas together with the activated carbon to remove an acidic gas such as hydrogen chloride or sulfur oxide in the exhaust gas, and the activated carbon and the alkali used may be simultaneously recovered.
【0008】[0008]
【発明の実施の形態】以下、この発明の実施の形態を添
付図面に基づいて説明する。図1にこの発明の一実施の
形態に係る排ガス処理装置の構成を示す。セメント製造
に用いられるロータリーキルン等のキルン11に排ガス
冷却塔12が接続され、排ガス冷却塔12に第1の除塵
機13及び第2の除塵機14が直列に接続されている。
第1の除塵機13と第2の除塵機14との間には活性炭
添加装置15が接続され、第2の除塵機14の出口側に
は煙突16が接続されている。なお、第1及び第2の除
塵機13及び14としては、電気集塵機等の各種の除塵
機を用いることができる。Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows a configuration of an exhaust gas treatment apparatus according to one embodiment of the present invention. An exhaust gas cooling tower 12 is connected to a kiln 11 such as a rotary kiln used for cement production, and a first dust remover 13 and a second dust remover 14 are connected in series to the exhaust gas cooler 12.
An activated carbon adding device 15 is connected between the first dust remover 13 and the second dust remover 14, and a chimney 16 is connected to an outlet side of the second dust remover 14. As the first and second dust removers 13 and 14, various dust removers such as an electric dust collector can be used.
【0009】次に、この実施の形態に係る排ガス処理装
置の動作について説明する。まず、セメント原料の焼成
を行うキルン11から排出された排ガスは、排ガス冷却
塔12において、第1の除塵機13に流通し得る程度の
温度にまで冷却された後、第1の除塵機13に入り、こ
こで除塵されて焼却飛灰が回収される。次に、第1の除
塵機13を出た排ガスに活性炭添加装置15から活性炭
が添加され、これにより、排ガス中に含まれているダイ
オキシンが活性炭に吸着される。活性炭が添加された排
ガスは、さらに第2の除塵機14に入って、ダイオキシ
ンを吸着した活性炭が回収される。その後、排ガスは煙
突16から大気中へ放出される。Next, the operation of the exhaust gas processing apparatus according to this embodiment will be described. First, the exhaust gas discharged from the kiln 11 for firing the cement raw material is cooled in the exhaust gas cooling tower 12 to a temperature at which the exhaust gas can be circulated to the first dust remover 13, and then the exhaust gas is cooled by the first dust remover 13. Then, the dust is removed and incinerated fly ash is collected. Next, activated carbon is added to the exhaust gas that has exited the first dust remover 13 from the activated carbon adding device 15, whereby dioxin contained in the exhaust gas is adsorbed on the activated carbon. The exhaust gas to which the activated carbon has been added further enters the second dust remover 14, where the activated carbon having adsorbed dioxin is recovered. Thereafter, the exhaust gas is released from the chimney 16 into the atmosphere.
【0010】第2の除塵機14で回収された活性炭は、
キルン11の燃料として使用することができ、活性炭に
吸着されたダイオキシンがキルン11内の高温雰囲気に
より分解される。また、セメント製造設備においては、
キルン11に図示しないプレヒータが接続されたものが
多いが、第2の除塵機14で回収された活性炭をプレヒ
ータの燃料として使用することもできる。The activated carbon recovered by the second dust remover 14 is:
The dioxin, which can be used as fuel for the kiln 11 and is adsorbed on the activated carbon, is decomposed by the high-temperature atmosphere in the kiln 11. In cement production facilities,
In many cases, a preheater (not shown) is connected to the kiln 11, but activated carbon recovered by the second dust remover 14 can be used as fuel for the preheater.
【0011】第1の除塵機13で回収された焼却飛灰
は、例えば図2に示すような一連の工程により鉛や銅等
の重金属の回収を行うことができる。The incinerated fly ash collected by the first dust remover 13 can recover heavy metals such as lead and copper by a series of steps as shown in FIG. 2, for example.
【0012】なお、図3に示されるように、第1の除塵
機13と第2の除塵機14との間にさらにアルカリ添加
装置17を接続し、第1の除塵機13で焼却飛灰が回収
された排ガスにアルカリ添加装置17から消石灰等のア
ルカリを添加するように構成することもできる。アルカ
リの添加により、排ガスに含まれていた塩化水素や硫黄
酸化物等の酸性ガスはアルカリと反応して除去され、こ
の塩化水素や硫黄酸化物等の酸性ガスの除去に用いられ
たアルカリは第2の除塵機14によって回収される。回
収されたアルカリは、セメント原料の一部として使用さ
れ、キルン11内に投入されることができる。すなわ
ち、排ガス中の塩化水素や硫黄酸化物等の酸性ガスの除
去に用いられたアルカリの有効利用を図ることができ
る。アルカリ添加装置17から添加するアルカリとして
は、消石灰の他、CaO、CaCO3、NaOH、KO
H等の種々のアルカリを用いることができる。As shown in FIG. 3, an alkali addition device 17 is further connected between the first dust remover 13 and the second dust remover 14, and the incinerated fly ash is removed by the first dust remover 13. An alkali such as slaked lime may be added from the alkali addition device 17 to the collected exhaust gas. By the addition of the alkali, acidic gases such as hydrogen chloride and sulfur oxides contained in the exhaust gas are removed by reacting with the alkali, and the alkali used to remove the acidic gases such as hydrogen chloride and sulfur oxides is removed. 2 is collected by the dust remover 14. The recovered alkali is used as a part of the cement raw material, and can be introduced into the kiln 11. That is, it is possible to effectively use the alkali used for removing the acidic gas such as hydrogen chloride and sulfur oxide in the exhaust gas. The alkali added from the alkali addition device 17 includes slaked lime, CaO, CaCO 3 , NaOH, KO
Various alkalis such as H can be used.
【0013】このように、上記の実施の形態に係る排ガ
ス処理装置によれば、排ガス中の焼却飛灰とダイオキシ
ンを吸着した活性炭及び/もしくは塩化水素や硫黄酸化
物等の酸性ガスを除去するために用いられたアルカリは
別々に回収されるため、活性炭はキルン11等の燃料と
して、アルカリはセメント原料等に有効利用すると共
に、焼却飛灰から重金属の回収を行うことが可能とな
る。As described above, according to the exhaust gas treatment apparatus according to the above embodiment, the incineration fly ash and the activated carbon adsorbing dioxin and / or the acid gas such as hydrogen chloride and sulfur oxide in the exhaust gas are removed. Since the alkalis used in the process are separately recovered, the activated carbon can be effectively used as a fuel for the kiln 11 and the like, the alkali can be effectively used as a raw material for cement, and the heavy metals can be recovered from the fly ash.
【0014】[0014]
【発明の効果】以上説明したように、この発明によれ
ば、排ガス中の焼却飛灰とダイオキシンを吸着した活性
炭及び/もしくは塩化水素や硫黄酸化物等の酸性ガスを
除去するために用いられたアルカリは別々に回収される
ようにしたため、ダイオキシン除去に用いた活性炭及び
/もしくは塩化水素や硫黄酸化物等の酸性ガスを除去す
るために用いられたアルカリを有効利用することができ
る。また、焼却飛灰から重金属の回収を行うことが可能
となる。As described above, according to the present invention, the present invention is used for removing incinerated fly ash and dioxin-adsorbed activated carbon and / or acid gas such as hydrogen chloride and sulfur oxide in exhaust gas. Since the alkalis are separately collected, the alkali used for removing the activated carbon used for dioxin removal and / or the acidic gas such as hydrogen chloride or sulfur oxide can be effectively used. In addition, it becomes possible to recover heavy metals from incinerated fly ash.
【図1】この発明の一実施の形態に係る排ガス処理装置
を示すブロック図である。FIG. 1 is a block diagram showing an exhaust gas treatment apparatus according to one embodiment of the present invention.
【図2】焼却飛灰から重金属を回収する工程を示すフロ
ー図である。FIG. 2 is a flowchart showing a process of recovering heavy metals from incinerated fly ash.
【図3】他の実施の形態に係る排ガス処理装置を示すブ
ロック図である。FIG. 3 is a block diagram showing an exhaust gas treatment apparatus according to another embodiment.
【図4】従来の排ガス処理装置を示すブロック図であ
る。FIG. 4 is a block diagram showing a conventional exhaust gas treatment device.
11 キルン 12 排ガス冷却塔 13 第1の除塵機 14 第2の除塵機 15 活性炭添加装置 16 煙突 17 アルカリ添加装置 DESCRIPTION OF SYMBOLS 11 Kiln 12 Exhaust gas cooling tower 13 1st dust remover 14 2nd dust remover 15 Activated carbon addition device 16 Chimney 17 Alkali addition device
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D002 AA02 AA19 AA21 AA28 BA02 BA03 BA04 BA13 BA14 CA01 CA11 DA02 DA03 DA05 DA11 DA12 DA41 EA02 EA05 GA02 GA03 GB03 GB09 HA08 4K056 AA19 BB01 CA11 CA20 DB07 DB14 FA08 ────────────────────────────────────────────────── ─── Continued on the front page F term (reference) 4D002 AA02 AA19 AA21 AA28 BA02 BA03 BA04 BA13 BA14 CA01 CA11 DA02 DA03 DA05 DA11 DA12 DA41 EA02 EA05 GA02 GA03 GB03 GB09 HA08 4K056 AA19 BB01 CA11 CA20 DB07 DB14 FA08
Claims (4)
回収する第1の除塵機と、 前記第1の除塵機で焼却飛灰が回収された排ガスに活性
炭を添加して排ガス中のダイオキシンを吸着させる活性
炭添加装置と、 活性炭が添加された排ガスからダイオキシンを吸着した
活性炭を回収する第2の除塵機とを備えたことを特徴と
する排ガス処理装置。1. A first dust remover for collecting incineration fly ash from flue gas generated in a kiln; and activated carbon is added to the flue gas from which the incineration fly ash is collected by the first dust remover to reduce dioxin in the flue gas. An exhaust gas treatment device comprising: an activated carbon adding device for adsorbing; and a second dust remover for collecting activated carbon having adsorbed dioxin from exhaust gas to which activated carbon has been added.
た排ガスにアルカリを添加して排ガス中の塩化水素や硫
黄酸化物等の酸性ガスを除去するアルカリ添加装置をさ
らに備え、 前記第2の除塵機は排ガスから塩化水素や硫黄酸化物等
の酸性ガスの除去に用いられたアルカリも回収すること
を特徴とする請求項1に記載の排ガス処理装置。2. An apparatus for adding an alkali to an exhaust gas from which incineration fly ash is collected by the first dust remover to remove an acid gas such as hydrogen chloride or sulfur oxide in the exhaust gas, further comprising an alkali addition device. The exhaust gas treating apparatus according to claim 1, wherein the second dust remover also recovers an alkali used for removing an acid gas such as hydrogen chloride or sulfur oxide from the exhaust gas.
回収し、 焼却飛灰が回収された排ガスに活性炭を添加して排ガス
中のダイオキシンを吸着させ、 活性炭が添加された排ガスからダイオキシンを吸着した
活性炭を回収することを特徴とする排ガス処理方法。3. The incineration fly ash is recovered from the exhaust gas generated in the kiln, the activated carbon is added to the exhaust gas from which the incinerated fly ash is recovered to adsorb the dioxin in the exhaust gas, and the dioxin is absorbed from the exhaust gas to which the activated carbon is added. An exhaust gas treatment method comprising recovering activated carbon.
て排ガス中の塩化水素や硫黄酸化物等の酸性ガスを除去
し、 排ガスから塩化水素や硫黄酸化物等の酸性ガスの除去に
用いられたアルカリを回収することを特徴とする請求項
3に記載の排ガス処理方法。4. An alkali added to an exhaust gas together with activated carbon to remove an acid gas such as hydrogen chloride and sulfur oxide in the exhaust gas, and an alkali used for removing an acid gas such as hydrogen chloride and sulfur oxide from the exhaust gas. The exhaust gas treatment method according to claim 3, wherein the waste gas is recovered.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10213795A JP2000042362A (en) | 1998-07-29 | 1998-07-29 | Waste gas treating device and method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10213795A JP2000042362A (en) | 1998-07-29 | 1998-07-29 | Waste gas treating device and method |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000042362A true JP2000042362A (en) | 2000-02-15 |
Family
ID=16645184
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP10213795A Pending JP2000042362A (en) | 1998-07-29 | 1998-07-29 | Waste gas treating device and method |
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Cited By (6)
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---|---|---|---|---|
JP2002316020A (en) * | 2001-04-23 | 2002-10-29 | Kurita Water Ind Ltd | Method for removing dioxins in exhaust gas of high humidity and removing agent |
US6547758B1 (en) | 1994-05-13 | 2003-04-15 | Scimed Life Systems, Inc. | Apparatus for performing diagnostic and therapeutic modalities in the biliary tree |
JP2006298712A (en) * | 2005-04-22 | 2006-11-02 | Sumitomo Osaka Cement Co Ltd | Treatment method and apparatus of exhaust gas in cement manufacturing facility |
CN103874752A (en) * | 2011-08-12 | 2014-06-18 | 麦卡利斯特技术有限责任公司 | Liquid fuel for isolating waste material and storing energy |
JP2017060905A (en) * | 2015-09-24 | 2017-03-30 | 太平洋セメント株式会社 | Processing apparatus and method of cement kiln exhaust gas |
CN114763264A (en) * | 2021-01-11 | 2022-07-19 | 中国石油化工股份有限公司 | Process for preparing activated carbon by alkali activation method |
-
1998
- 1998-07-29 JP JP10213795A patent/JP2000042362A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6547758B1 (en) | 1994-05-13 | 2003-04-15 | Scimed Life Systems, Inc. | Apparatus for performing diagnostic and therapeutic modalities in the biliary tree |
JP2002316020A (en) * | 2001-04-23 | 2002-10-29 | Kurita Water Ind Ltd | Method for removing dioxins in exhaust gas of high humidity and removing agent |
JP2006298712A (en) * | 2005-04-22 | 2006-11-02 | Sumitomo Osaka Cement Co Ltd | Treatment method and apparatus of exhaust gas in cement manufacturing facility |
CN103874752A (en) * | 2011-08-12 | 2014-06-18 | 麦卡利斯特技术有限责任公司 | Liquid fuel for isolating waste material and storing energy |
JP2017060905A (en) * | 2015-09-24 | 2017-03-30 | 太平洋セメント株式会社 | Processing apparatus and method of cement kiln exhaust gas |
CN114763264A (en) * | 2021-01-11 | 2022-07-19 | 中国石油化工股份有限公司 | Process for preparing activated carbon by alkali activation method |
CN114763264B (en) * | 2021-01-11 | 2024-05-03 | 中国石油化工股份有限公司 | Process for preparing active carbon by alkali activation method |
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