[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JPH0531323A - Method for exhaust gas treatment - Google Patents

Method for exhaust gas treatment

Info

Publication number
JPH0531323A
JPH0531323A JP3194282A JP19428291A JPH0531323A JP H0531323 A JPH0531323 A JP H0531323A JP 3194282 A JP3194282 A JP 3194282A JP 19428291 A JP19428291 A JP 19428291A JP H0531323 A JPH0531323 A JP H0531323A
Authority
JP
Japan
Prior art keywords
exhaust gas
activated carbon
spraying
harmful substances
absorbent
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
Application number
JP3194282A
Other languages
Japanese (ja)
Inventor
Katsumi Yoshikubo
克己 吉窪
Eiichi Shibuya
榮一 澁谷
Atsushi Morishige
敦 森重
Tsuyoshi Nakao
強 仲尾
Kentaro Ito
健太郎 伊藤
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP3194282A priority Critical patent/JPH0531323A/en
Publication of JPH0531323A publication Critical patent/JPH0531323A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To provide a method for exhaust gas treatment requiring no large scale equipment and removing harmful substances in the exhaust gas with a high efficiency. CONSTITUTION:In a combustion exhaust gas line at the outlet of a boiler, a sprayer 1 for powdery activated carbon and, downstream of it, a sprayer 2 for a basic absorbent to remove acid components are installed. The substances captured by the activated carbon and the absorbent are collected in a dust catcher 3 with the activated carbon and the absorbent and removed. The combustion exhaust gas eliminated of harmful substances is discharged from a stack 4.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、焼却炉設備から排出さ
れる燃焼排ガス中の有害物質を除去する排ガス処理方法
に関する。上記有害物質には、水銀等の重金属、ダイオ
キシン等の有機塩素化合物が含まれる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas treatment method for removing harmful substances in combustion exhaust gas discharged from an incinerator facility. The harmful substances include heavy metals such as mercury and organic chlorine compounds such as dioxins.

【0002】[0002]

【従来の技術】燃焼排ガスから水銀を除去し、または回
収するため、多くの方法が示されている。また、煙道ガ
ス中のダイオキシン等の有害塩素系化合物を減少させる
方法としても種々示されている。PCT出願WO85/
03455号明細書によれば、固定ベッド上において活
性炭またはコークスを用いている。この方法では、上記
活性炭等の粒径が比較的粗くなり、粒子状活性炭の製造
に費用が掛かり、且つまた上記活性炭等の活性が低くな
るという欠点がある。
BACKGROUND OF THE INVENTION Many methods have been shown to remove or recover mercury from flue gas. In addition, various methods have been shown as a method for reducing harmful chlorine compounds such as dioxins in flue gas. PCT application WO85 /
According to the 03455 specification, activated carbon or coke is used on a fixed bed. This method has the disadvantages that the particle size of the activated carbon or the like becomes relatively coarse, the production of the particulate activated carbon is expensive, and the activity of the activated carbon or the like becomes low.

【0003】[0003]

【発明が解決しようとする課題】従来の方法では、大型
装置を必要としたり、除去効率が良好でない等の改善余
地がある。従って、煙道ガスから水銀蒸気及び/または
有害な有機化合物を除去する改良された方法が求められ
ている。本発明はかかる観点に基づいてなされたもので
あり、上述の従来技術の欠点を解消し得る排ガス処理方
法を提供することを目的とする。
In the conventional method, there is room for improvement in that a large-scale device is required and the removal efficiency is not good. Accordingly, there is a need for improved methods of removing mercury vapor and / or harmful organic compounds from flue gases. The present invention has been made based on this point of view, and an object thereof is to provide an exhaust gas treatment method capable of solving the above-mentioned drawbacks of the prior art.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するた
め、本発明方法にあっては、焼却炉設備からの排ガス処
理設備として、大型の装置を設置することなく、吸着性
の高い粉末状活性炭を排ガス中に噴霧することにより、
排ガス中の有害物質を効率よく吸着し、下流に設置され
る集塵機にて捕集除去することを特徴とする。上記粉末
状活性炭の噴霧は、塩基性吸収剤を乾式の状態で排ガス
中に噴霧することにより酸性成分を吸収する工程の上流
及び/または下流で行うことが可能となる。
In order to achieve the above object, in the method of the present invention, a powdered activated carbon having a high adsorptivity is installed as an exhaust gas treatment facility from an incinerator facility without installing a large apparatus. By spraying in the exhaust gas,
It is characterized by efficiently adsorbing harmful substances in exhaust gas and collecting and removing them with a dust collector installed downstream. The powdered activated carbon can be sprayed upstream and / or downstream of the step of absorbing the acidic component by spraying the basic absorbent in the exhaust gas in a dry state.

【0005】[0005]

【作用】本発明に係る方法は、一般のごみ焼却プラント
からの燃焼排ガス中に粉末状の活性炭を噴霧し、同活性
炭に、排ガス中の水銀等の重金属を吸着させると共に、
ダイオキシン等の有害な有機塩素化合物も合わせて吸着
させる。これらの有害物質が吸着した活性炭は、下流に
設けたバグフィルター等の集塵機によって捕集し、排ガ
ス中から除外する。
The method according to the present invention sprays powdered activated carbon into the combustion exhaust gas from a general refuse incineration plant, adsorbs heavy metals such as mercury in the exhaust gas to the activated carbon,
It also adsorbs harmful organic chlorine compounds such as dioxins. Activated carbon on which these harmful substances are adsorbed is collected by a dust collector such as a bag filter provided downstream and excluded from the exhaust gas.

【0006】また、一般に燃焼排ガス中には塩化水素な
ど酸性成分が含まれているが、この酸性成分を除去する
ため、塩基性吸収剤を排ガス中に噴霧する。塩基性吸収
剤は、排ガスをガスクーラ等のガス冷却装置により12
0℃〜200℃に冷却した後に供給される。また塩基性
吸収剤は、乾式反応塔をボイラー出口で排ガスラインに
設置し、この内部で噴霧するか、或いは、排ガスライン
中に直接噴霧する。
Generally, the combustion exhaust gas contains an acidic component such as hydrogen chloride. To remove the acidic component, a basic absorbent is sprayed into the exhaust gas. The basic absorbent absorbs exhaust gas with a gas cooling device such as a gas cooler.
It is supplied after cooling to 0 ° C to 200 ° C. Further, the basic absorbent is sprayed inside the exhaust gas line after installing the dry reaction tower at the boiler outlet in the exhaust gas line or directly in the exhaust gas line.

【0007】従って、本発明方法は、排ガスラインの塩
基性吸収剤の噴霧位置(上記乾式反応塔設置位置或いは
直接噴霧位置)と同位置、或いは当該位置の上流及び/
または下流の位置において粉末状活性炭の噴霧位置を配
置するものである。
Therefore, the method of the present invention is the same position as the spraying position of the basic absorbent in the exhaust gas line (the above-mentioned dry reaction tower installation position or direct spraying position), or upstream and / or above that position.
Alternatively, the spray position of the powdered activated carbon is arranged at the downstream position.

【0008】上記粉末状活性炭は、吸着活性を高めるた
め、粒径44μm以下が30wt%の粒度を持つ粉末を
試用し、煙道ガスNm3 当り1〜600mgの量を噴霧
するものである。
In order to enhance the adsorption activity of the powdered activated carbon, a powder having a particle size of less than 44 μm and a particle size of 30 wt% was used as a trial, and the flue gas Nm 3 The amount is 1 to 600 mg per spray.

【0009】[0009]

【実施例】図1乃至図3は、本発明に係る方法を応用し
た焼却炉設備内の異なるフローを夫々示す図である。図
中対応する部位には同一の符号を付してある。
1 to 3 are views showing different flows in an incinerator facility to which the method according to the present invention is applied. Corresponding parts in the drawings are designated by the same reference numerals.

【0010】図1図示の第1実施例において、ボイラー
出口の燃焼排ガスラインには、粉末状活性炭の噴霧部1
と、その下流に、酸性成分除去用の塩基性吸収剤の噴霧
部2とが配置される。上記活性炭及び吸収剤に吸着され
た物質は、これらと共に集塵機3で捕集除去され、有害
物質が除去された燃焼排ガスはスタック4から系外へ放
出される。
In the first embodiment shown in FIG. 1, in the combustion exhaust gas line at the outlet of the boiler, a spraying section 1 for powdered activated carbon is provided.
And the spraying section 2 of the basic absorbent for removing the acidic component is disposed downstream thereof. The substances adsorbed on the activated carbon and the absorbent are collected and removed together with them by the dust collector 3, and the combustion exhaust gas from which the harmful substances are removed is discharged from the stack 4 to the outside of the system.

【0011】図2図示の実施例において、粉末状活性炭
の噴霧部1と、塩基性吸収剤の噴霧部2とが、第1実施
例とは上下流関係が逆に配置される。集塵機3及びスタ
ック4については第1実施例と同一である。
In the embodiment shown in FIG. 2, the spraying part 1 of powdered activated carbon and the spraying part 2 of the basic absorbent are arranged in an upstream / downstream relationship opposite to that of the first embodiment. The dust collector 3 and the stack 4 are the same as in the first embodiment.

【0012】図3図示の実施例において、粉末状活性炭
の噴霧部1と、塩基性吸収剤の噴霧部2とが同じ位置に
配置される。集塵機3及びスタック4については第1実
施例と同一である。
In the embodiment shown in FIG. 3, the spraying section 1 of powdered activated carbon and the spraying section 2 of the basic absorbent are arranged at the same position. The dust collector 3 and the stack 4 are the same as in the first embodiment.

【0013】粉末状活性炭は、サイロからスクリューフ
ィーダ等により定量コントロールしながら供給し、圧縮
空気により排ガス中に噴霧することができる。またこれ
に代え、粉末状活性炭は、他の好適な手段を用いて噴霧
することも可能である。
The powdered activated carbon can be supplied from a silo while being quantitatively controlled by a screw feeder or the like, and can be sprayed into the exhaust gas by compressed air. Alternatively, the powdered activated carbon can be sprayed using any other suitable means.

【0014】表1は、第1実施例における排ガス中の有
害物質の分析結果である。この結果に示されるように、
本発明方法を応用した焼却炉設備によれば、燃焼排ガス
中のHg、ダイオキシンが高い効率で除去されることが
分かる。
Table 1 shows the analysis results of harmful substances in the exhaust gas in the first embodiment. As shown in this result,
According to the incinerator equipment to which the method of the present invention is applied, Hg and dioxin in the combustion exhaust gas are removed with high efficiency.

【0015】[0015]

【表1】 [Table 1]

【0016】[0016]

【発明の効果】本発明方法によれば、大型装置を必要と
せず、高い効率で排ガス中の水銀、ダイオキシン等の有
害物質を除去することが可能となる。
According to the method of the present invention, it is possible to remove harmful substances such as mercury and dioxins in exhaust gas with high efficiency without requiring a large-scale device.

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

【図1】本発明に係る排ガス処理方法を応用した焼却炉
設備の第1実施例を示す図。
FIG. 1 is a diagram showing a first embodiment of an incinerator facility to which an exhaust gas treatment method according to the present invention is applied.

【図2】本発明に係る排ガス処理方法を応用した焼却炉
設備の第2実施例を示す図。
FIG. 2 is a diagram showing a second embodiment of incinerator equipment to which the exhaust gas treatment method according to the present invention is applied.

【図3】本発明に係る排ガス処理方法を応用した焼却炉
設備の第3実施例を示す図。
FIG. 3 is a diagram showing a third embodiment of incinerator equipment to which the exhaust gas treatment method according to the present invention is applied.

【符号の説明】[Explanation of symbols]

1…粉末状活性炭噴霧部、2…塩基性吸収剤噴霧部、3
…集塵機、4…スタック。
1 ... Powdery activated carbon spraying part, 2 ... Basic absorbent spraying part, 3
… Dust collector, 4… Stack.

フロントページの続き (72)発明者 仲尾 強 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 伊藤 健太郎 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内Front Page Continuation (72) Inventor Tsuyoshi Nakao 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Nihon Kokan Co., Ltd. (72) Inventor Kentaro Ito 1-2-1, Marunouchi, Chiyoda-ku, Tokyo In the company

Claims (1)

【特許請求の範囲】 【請求項1】 焼却炉設備から排出される燃焼排ガス中
の有害物質を除去する方法であって、上記排ガスを12
0℃〜200℃に冷却した後、該排ガスのライン中に酸
性成分を吸収するための塩基性吸収剤を乾式の状態で噴
霧する工程と、上記排ガスライン中に粒径44μm以下
を30wt%含む粉末状活性炭を上記排ガスのNm3
り1〜600mg噴霧する工程と、上記塩基性吸収剤の
噴霧位置及び粉末状活性炭の噴霧位置よりも下流で上記
排ガスラインに設けた集塵機で有害物質を吸着した上記
粉末活性炭を捕集する工程と、を具備する排ガスの処理
方法。
Claim: What is claimed is: 1. A method for removing harmful substances in a combustion exhaust gas discharged from an incinerator facility, comprising:
After cooling to 0 ° C. to 200 ° C., a step of spraying a basic absorbent for absorbing an acidic component into the exhaust gas line in a dry state, and including 30 wt% of a particle size of 44 μm or less in the exhaust gas line Powdered activated carbon was added to the above exhaust gas Nm 3 Spraying 1 to 600 mg per step, and collecting the powdered activated carbon adsorbing harmful substances with a dust collector provided in the exhaust gas line downstream of the spraying position of the basic absorbent and the spraying position of powdered activated carbon A method for treating exhaust gas, comprising:
JP3194282A 1991-08-02 1991-08-02 Method for exhaust gas treatment Pending JPH0531323A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3194282A JPH0531323A (en) 1991-08-02 1991-08-02 Method for exhaust gas treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3194282A JPH0531323A (en) 1991-08-02 1991-08-02 Method for exhaust gas treatment

Publications (1)

Publication Number Publication Date
JPH0531323A true JPH0531323A (en) 1993-02-09

Family

ID=16322014

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3194282A Pending JPH0531323A (en) 1991-08-02 1991-08-02 Method for exhaust gas treatment

Country Status (1)

Country Link
JP (1) JPH0531323A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998048924A1 (en) * 1997-04-25 1998-11-05 Nkk Corporation Method of treating exhaust gas
US6597315B2 (en) 2000-08-04 2003-07-22 Mitsubishi Materials Corporation Antenna
US6600459B2 (en) 2000-10-27 2003-07-29 Mitsubishi Materials Corporation Antenna
US6642904B2 (en) 2000-10-31 2003-11-04 Mitsubishi Materials Corporation Antenna
US6680713B2 (en) 2000-10-31 2004-01-20 Mitsubishi Materials Corporation Antenna and radio wave receiving/transmitting apparatus therewith and method of manufacturing the antenna
US7264784B2 (en) 2003-10-22 2007-09-04 Nippon Shokubai Co., Ltd. Method for treating exhaust gas
GB2448033A (en) * 2007-03-27 2008-10-01 Gen Electric Removing mercury from combustion flue gas by injecting coolant and sorbent into a convective pass
JP2011251250A (en) * 2010-06-02 2011-12-15 Ryuki Engineering:Kk Deodorizing apparatus and deodorizing method
KR101227687B1 (en) * 2011-01-19 2013-01-29 에이치투더블유티이 주식회사 Carbonized-marerials recycling system of sludge and epr waste

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998048924A1 (en) * 1997-04-25 1998-11-05 Nkk Corporation Method of treating exhaust gas
US6597315B2 (en) 2000-08-04 2003-07-22 Mitsubishi Materials Corporation Antenna
US6600459B2 (en) 2000-10-27 2003-07-29 Mitsubishi Materials Corporation Antenna
US6642904B2 (en) 2000-10-31 2003-11-04 Mitsubishi Materials Corporation Antenna
US6680713B2 (en) 2000-10-31 2004-01-20 Mitsubishi Materials Corporation Antenna and radio wave receiving/transmitting apparatus therewith and method of manufacturing the antenna
US7264784B2 (en) 2003-10-22 2007-09-04 Nippon Shokubai Co., Ltd. Method for treating exhaust gas
GB2448033A (en) * 2007-03-27 2008-10-01 Gen Electric Removing mercury from combustion flue gas by injecting coolant and sorbent into a convective pass
US7531153B2 (en) 2007-03-27 2009-05-12 General Electric Company Methods and apparatus for removing mercury from combustion flue gas
GB2448033B (en) * 2007-03-27 2012-10-03 Gen Electric Removing mercury from combustion flue gas
JP2011251250A (en) * 2010-06-02 2011-12-15 Ryuki Engineering:Kk Deodorizing apparatus and deodorizing method
KR101227687B1 (en) * 2011-01-19 2013-01-29 에이치투더블유티이 주식회사 Carbonized-marerials recycling system of sludge and epr waste

Similar Documents

Publication Publication Date Title
JPH07204432A (en) Exhaust gas treatment method
JP2003523281A (en) Adsorbed powder for removing mercury from hot and humid gas streams
CN104353325A (en) Device and method for removing mercury from boiler flue gas of power station
JPH07299328A (en) Method of purifying exhaust gas
JPH0531323A (en) Method for exhaust gas treatment
WO2005030641A1 (en) Highly activated coke powder and process for producing the same
US5439508A (en) Process of separating halogenated dioxins and furans from exhaust gases from combustion plants
US7048779B1 (en) Method of removing mercury from exhaust gases of coal fired power plants and associated apparatus
JP2003286020A (en) Highly activated active coke powder and manufacturing method thereof
JPH05220338A (en) Treating equipment for exhaust gas of refuse incinerator
JP3411484B2 (en) Desorption gas treatment method in exhaust gas treatment equipment of garbage incinerator
CA2173288A1 (en) Method to remove organic halogenated molecules from gaseous currents and relative plant
JPH10180038A (en) Waste gas simultaneous treating device and method thereof
JP3411482B2 (en) Operating method of exhaust gas treatment device in garbage incinerator
JPH08243341A (en) Treatment of waste gas
JP3332204B2 (en) Method and apparatus for removing harmful substances from exhaust gas
JP3086156B2 (en) RDF incineration / exhaust gas treatment equipment
CN88103260A (en) The method of radiation treatment waste gas and device thereof
JPH0975667A (en) Treatment of exhaust gas
JP3491124B2 (en) Filtration type dust collector
JP3858137B2 (en) Apparatus and method for decomposing and treating harmful substances in exhaust gas
JP2560931B2 (en) Method of removing harmful substances in exhaust gas
JP2654545B2 (en) How to remove mercury from exhaust gas from refuse incinerator
JP2004081990A (en) Agent and equipment for removing toxic substance in combustion exhaust gas
JPH10216469A (en) Spraying method and device of slaked lime and adsorbent