JP2010227747A - Exhaust gas treatment apparatus and exhaust gas treatment method - Google Patents

Exhaust gas treatment apparatus and exhaust gas treatment method Download PDF

Info

Publication number
JP2010227747A
JP2010227747A JP2009075567A JP2009075567A JP2010227747A JP 2010227747 A JP2010227747 A JP 2010227747A JP 2009075567 A JP2009075567 A JP 2009075567A JP 2009075567 A JP2009075567 A JP 2009075567A JP 2010227747 A JP2010227747 A JP 2010227747A
Authority
JP
Japan
Prior art keywords
exhaust gas
adsorbent
heavy metals
particle size
size distribution
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
JP2009075567A
Other languages
Japanese (ja)
Inventor
Takuya Shinagawa
拓也 品川
Toru Shiomitsu
徹 塩満
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
JFE Engineering 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 JFE Engineering Corp filed Critical JFE Engineering Corp
Priority to JP2009075567A priority Critical patent/JP2010227747A/en
Publication of JP2010227747A publication Critical patent/JP2010227747A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an exhaust gas treatment apparatus and an exhaust gas treatment method following variation in the existence condition of heavy metals in an exhaust gas in a short period of time and supplying the appropriate amount of an adsorbent without making a supply amount excessive. <P>SOLUTION: The exhaust gas treatment apparatus 1 includes: an adsorbent supply device 10 for supplying the adsorbent for adsorbing the heavy metals included in the exhaust gas to the exhaust gas; a dust collector 20 for receiving the exhaust gas supplied with the adsorbent and removing the adsorbent which has adsorbed the heavy metals included in the exhaust gas and dust; a particle size distribution measuring device 40 for measuring the particle size distribution of fine particles of the heavy metals in the exhaust gas discharged from the dust collector 20; and a controller 50 for deriving the concentration of the heavy metals indicating the existence condition of the heavy metals in the exhaust gas on the basis of the particle size distribution of the fine particles measured by the particle size distribution measuring device 40 and controlling the supply amount of the adsorbent to be supplied to the exhaust gas on the basis of the derived concentration of the heavy metals. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、重金属類を含む排ガスの処理装置及び排ガス処理方法に関する。   TECHNICAL FIELD The present invention relates to an exhaust gas treatment apparatus and an exhaust gas treatment method containing heavy metals.

廃棄物焼却施設や製鋼精錬施設などにおける、燃焼炉装置、溶融装置、加熱装置等の熱処理プロセスから排出される排ガス中に含まれる重金属類を除去して排ガスを無害化することが検討されている。重金属類は、生成し得る化合物形態によって蒸気圧が異なるため、排ガス処理プロセスにおける温度および雰囲気条件によってはガス状になっている。ガス状の重金属類は集塵装置を通過してしまうので、該集塵装置では捕捉することができない。集塵装置を通過したガス状の重金属類は煙道内や大気放散後に凝縮して極めて粒径の小さい微粒子状物質となり、人体有害性を有することとなる。また、集塵装置の上流側でガス状の重金属類が凝縮する場合にも、重金属類は極めて粒径の小さい微粒子状物質となる。該微粒子状物質も、通常用いられている集塵装置では十分に捕捉できず、大気中に流出することとなる。   Removal of heavy metals contained in exhaust gas discharged from heat treatment processes such as combustion furnace equipment, melting equipment, and heating equipment in waste incineration facilities and steel refining facilities is being considered to make the exhaust gas harmless. . Since heavy metals have different vapor pressures depending on the form of the compound that can be produced, they are in a gaseous state depending on the temperature and atmospheric conditions in the exhaust gas treatment process. Since gaseous heavy metals pass through the dust collector, they cannot be captured by the dust collector. Gaseous heavy metals that have passed through the dust collector are condensed in the flue and after being released into the atmosphere to form particulate matter with a very small particle size, which is harmful to the human body. Further, even when gaseous heavy metals condense on the upstream side of the dust collector, the heavy metals become a particulate material having a very small particle diameter. The particulate matter cannot be sufficiently captured by a commonly used dust collector and flows out into the atmosphere.

排ガスを大気に放出する前に重金属類を排ガスから除去する対策として、特許文献1では、排ガスを集塵装置に導入してダストを除去するとともに、該集塵装置の前段において排ガス中に吸着剤を供給してガス状や微粒子状の重金属類を吸着した吸着剤を該集塵装置で捕集することにより重金属類を除去する排ガス処理方法が開示されている。   As a measure for removing heavy metals from exhaust gas before releasing the exhaust gas to the atmosphere, Patent Document 1 introduces exhaust gas into a dust collector to remove dust, and adsorbent in the exhaust gas before the dust collector. An exhaust gas treatment method is disclosed in which heavy metals are removed by collecting an adsorbent that has adsorbed gaseous and particulate heavy metals with the dust collector.

特開2001−212427JP2001-212427

廃棄物焼却施設では、処理する廃棄物の種類、処理数量の変動にともない、焼却炉等からの排ガス中の重金属類濃度が変動する。排ガス中の微粒子状態のものを含む重金属類濃度の分析は、化学的な吸収によるサンプル採取とオフサイトでの湿式分析による定量分析により行われているため、オンサイトで短時間のうちに排ガス中の重金属類濃度を得ることができなかった。   In the waste incineration facility, the concentration of heavy metals in the exhaust gas from the incinerator and the like varies with changes in the type and quantity of waste to be treated. The analysis of heavy metal concentrations including fine particles in exhaust gas is performed by sampling by chemical absorption and quantitative analysis by wet analysis off-site. Concentration of heavy metals could not be obtained.

そのため、特許文献1の排ガス処理方法によっては、排ガス中の重金属類濃度を監視しながら吸着剤の供給を制御することができない。したがって、廃棄物焼却施設におけるような変動する排ガス中の重金属類濃度に対して、安定的に高い除去率で重金属類を除去しようとすると、過剰な量の吸着剤を供給する必要がある。   Therefore, according to the exhaust gas treatment method of Patent Document 1, it is not possible to control the supply of the adsorbent while monitoring the heavy metal concentration in the exhaust gas. Therefore, in order to remove heavy metals stably at a high removal rate with respect to the concentration of heavy metals in fluctuating exhaust gas as in a waste incineration facility, it is necessary to supply an excessive amount of adsorbent.

過剰な量の吸着剤を供給する結果、吸着剤使用量が過大となり排ガス処理費用が増大し、また、集塵装置で捕集されダストとともに回収される吸着剤量が過大となるので、ダスト処理費用も増大する。また、集塵装置で捕集する吸着剤の量が過大になるので、ダストと吸着剤が付着したフィルタの圧力損失が高くなり送気装置の負荷が増加する。さらには、煙道内で吸着剤が堆積することにより、排ガス流れに異常が発生したり、煙道が閉塞したりする。   As a result of supplying an excessive amount of adsorbent, the amount of adsorbent used becomes excessive, increasing the cost of exhaust gas treatment, and the amount of adsorbent collected by the dust collector and collected together with the dust becomes excessive. Costs also increase. Further, since the amount of the adsorbent collected by the dust collector becomes excessive, the pressure loss of the filter to which the dust and the adsorbent adhere is increased and the load on the air feeding device is increased. Furthermore, the adsorbent accumulates in the flue, thereby causing an abnormality in the exhaust gas flow or blocking the flue.

このように、特許文献1の排ガス処理方法では、排ガス中の重金属類濃度の変動に対して短時間で追従して適切な量の吸着剤を供給することができず、上述したような種々の問題が生じることがある。   As described above, in the exhaust gas treatment method of Patent Document 1, it is not possible to supply an appropriate amount of adsorbent by following the fluctuation of the heavy metal concentration in the exhaust gas in a short time. Problems can arise.

本発明は、このような事情に鑑みて、排ガス中の重金属類の存在状況の変動に対して、短時間で追従でき、供給量が過大とならず適切な量の吸着剤を供給することができる排ガス処理装置及び排ガス処理方法を提供することを課題とする。   In view of such circumstances, the present invention can follow fluctuations in the presence of heavy metals in exhaust gas in a short time, and can supply an appropriate amount of adsorbent without excessive supply. It is an object to provide an exhaust gas treatment apparatus and an exhaust gas treatment method that can be performed.

<第一発明>
本発明に係る排ガス処理装置は、重金属類を含む排ガスを処理するための装置である。
<First invention>
The exhaust gas treatment apparatus according to the present invention is an apparatus for treating exhaust gas containing heavy metals.

かかる排ガス処理装置において、本発明は、該重金属類を吸着する吸着剤を排ガスに供給する吸着剤供給装置と、該吸着剤を供給された排ガスを受けて、該排ガスに含まれている重金属類を吸着した吸着剤およびダストを除去する集塵装置と、該集塵装置から排出される排ガス中の重金属類の微粒子の粒度分布を計測する粒度分布計測装置と、該粒度分布計測装置により計測された上記微粒子の粒度分布に基づき排ガス中の重金属類の存在状況を示す量を求め、求めた重金属類の存在状況に基づき、排ガスに供給する吸着剤の供給量を制御する吸着剤供給量制御装置とを有することを特徴としている。   In such an exhaust gas treatment device, the present invention includes an adsorbent supply device that supplies the exhaust gas with an adsorbent that adsorbs the heavy metals, and a heavy metal that is contained in the exhaust gas after receiving the exhaust gas supplied with the adsorbent. A dust collector that removes the adsorbent and dust adsorbed, a particle size distribution measuring device that measures the particle size distribution of heavy metal fine particles in the exhaust gas discharged from the dust collector, and the particle size distribution measuring device. Further, an adsorbent supply amount control device that obtains an amount indicating the presence state of heavy metals in the exhaust gas based on the particle size distribution of the fine particles and controls the supply amount of the adsorbent supplied to the exhaust gas based on the obtained presence state of heavy metals. It is characterized by having.

本発明では、吸着剤供給量制御装置が、粒度分布計測装置によって計測された上記粒度分布に基づいて排ガス中の重金属類の存在状況を示す量を求め、求めた重金属類の存在状況を示す量に基づいて、排ガスに供給する吸着剤供給量を制御するので、該吸着剤供給量が重金属類の存在状況に応じて増減する。したがって、重金属類の存在状況が変動しても、その変動に応じて常に適正量の吸着剤が排ガスに供給される。   In the present invention, the adsorbent supply amount control device obtains an amount indicating the presence of heavy metals in the exhaust gas based on the particle size distribution measured by the particle size distribution measuring device, and indicates the obtained presence of heavy metals. Therefore, the amount of adsorbent supplied to the exhaust gas is controlled, so that the amount of adsorbent supplied increases or decreases depending on the presence of heavy metals. Therefore, even if the presence state of heavy metals varies, an appropriate amount of adsorbent is always supplied to the exhaust gas in accordance with the variation.

吸着剤の供給量の制御は、例えば、実際に計測された微粒子の粒度分布と吸着剤供給量制御装置が予め保持している微粒子の粒度分布と重金属類の存在状況を示す量との相関関係を示すデータに基づいて重金属類の存在状況を示す量を導出し、該存在状況を示す量と所定の目標濃度との比較結果に応じて吸着剤の供給量を増減させることにより実現できる。   Control of the amount of adsorbent supplied is, for example, the correlation between the particle size distribution of the actually measured fine particles, the particle size distribution of the fine particles held in advance by the adsorbent supply amount control device, and the amount indicating the presence of heavy metals. This is realized by deriving an amount indicating the presence state of heavy metals based on the data indicating the amount of adsorbent, and increasing or decreasing the supply amount of the adsorbent according to the comparison result between the amount indicating the presence state and a predetermined target concentration.

排ガス中の重金属類の存在状況を示す量は、該重金属類の濃度であり、吸着剤供給量制御装置は、微粒子の粒度分布と重金属類の濃度との相関関係を示すデータを予め保持しており、該データに基づいて上記計測された微粒子の粒度分布と対応する重金属類濃度を導出し、導出した重金属類の濃度が所定の目標濃度よりも大きいときに、吸着剤の供給量を増加させるように吸着剤供給装置の制御を行い、導出した重金属類の濃度が所定の目標濃度よりも小さいときに、吸着剤の供給量を減少させるように吸着剤供給装置の制御を行うように設定されていることが好ましい。   The amount indicating the presence of heavy metals in the exhaust gas is the concentration of the heavy metals, and the adsorbent supply amount control device holds in advance data indicating the correlation between the particle size distribution of the fine particles and the concentration of heavy metals. Based on the data, the measured particle size distribution of the fine particles and the corresponding heavy metal concentration are derived, and when the derived heavy metal concentration is higher than a predetermined target concentration, the supply amount of the adsorbent is increased. The adsorbent supply device is controlled so that the adsorbent supply device is controlled to reduce the supply amount of the adsorbent when the derived heavy metal concentration is lower than a predetermined target concentration. It is preferable.

このように、実際に計測された微粒子の粒度分布と吸着剤供給量制御装置が予め保持している微粒子の粒度分布と重金属類の濃度との相関関係を示すデータに基づいて重金属類の濃度を導出してもよい。これによって、排ガス処理装置の運転中に重金属類の濃度が変動しても、その変動に応じて常に適正量の吸着剤を排ガスに供給することができる。   As described above, the concentration of heavy metals is determined based on the data indicating the correlation between the particle size distribution of the actually measured fine particles and the particle size distribution of the fine particles and the concentration of heavy metals previously held by the adsorbent supply amount control device. It may be derived. Thereby, even if the concentration of heavy metals fluctuates during operation of the exhaust gas treatment device, an appropriate amount of adsorbent can always be supplied to the exhaust gas according to the fluctuation.

粒度分布計測装置に導入する排ガスを希釈冷却する希釈冷却装置をさらに有することが好ましい。該希釈冷却装置によって排ガスを希釈冷却することにより、排ガス中に含まれるガス状の重金属類が凝縮されて微粒子となって粒度分布を計測できる状態となる。この結果、該微粒子の粒度分布に基づいて重金属類濃度を導出することによって、正確な重金属類の濃度を得ることができ、吸着剤の供給量もより適正な量とすることができる。   It is preferable to further have a dilution cooling device for diluting and cooling the exhaust gas to be introduced into the particle size distribution measuring device. By diluting and cooling the exhaust gas with the dilution cooling device, gaseous heavy metals contained in the exhaust gas are condensed into fine particles, and the particle size distribution can be measured. As a result, by deriving the heavy metal concentration based on the particle size distribution of the fine particles, an accurate heavy metal concentration can be obtained, and the amount of adsorbent supplied can be more appropriate.

吸着剤供給装置は、活性炭、カオリンおよび粘土鉱物のうち少なくとも一つを吸着剤として排ガス中に供給することが好ましい。   The adsorbent supply device preferably supplies at least one of activated carbon, kaolin and clay mineral as an adsorbent into the exhaust gas.

<第二発明>
本発明に係る排ガス処理方法は、重金属類を含む排ガスを処理するための方法である。
<Second invention>
The exhaust gas treatment method according to the present invention is a method for treating exhaust gas containing heavy metals.

かかる排ガス処理方法において、本発明は、該重金属類を吸着する吸着剤を排ガスに供給する吸着剤供給工程と、該吸着剤を供給された排ガスを受けて該排ガスに含まれている重金属類を吸着した吸着剤およびダストを除去する集塵工程と、該集塵工程で排出される排ガス中の重金属類の微粒子の粒度分布を計測する粒度分布計測工程と、該粒度分布計測工程で計測された上記微粒子の粒度分布に基づき排ガス中の重金属類の存在状況を示す量を求め、求めた重金属類の存在状況に基づき、排ガスに供給する吸着剤供給量を制御する吸着剤供給量制御工程とを有することを特徴としている。   In the exhaust gas treatment method, the present invention includes an adsorbent supply step of supplying an adsorbent that adsorbs the heavy metals to the exhaust gas, and a heavy metal contained in the exhaust gas that receives the exhaust gas supplied with the adsorbent. It was measured in the dust collection process for removing the adsorbent and dust adsorbed, the particle size distribution measurement process for measuring the particle size distribution of heavy metal fine particles in the exhaust gas discharged in the dust collection process, and the particle size distribution measurement process. An adsorbent supply amount control step for obtaining an amount indicating the presence of heavy metals in the exhaust gas based on the particle size distribution of the fine particles, and controlling the amount of adsorbent supplied to the exhaust gas based on the obtained presence of heavy metals. It is characterized by having.

本発明では、吸着剤供給量制御工程にて、粒度分布計測工程で計測された上記粒度分布に基づいて排ガス中の重金属類の存在状況を示す量を求め、求めた重金属類の存在状況に基づいて、排ガスに供給する吸着剤供給量を制御するので、該吸着剤供給量が重金属類の存在状況に応じて増減する。したがって、重金属類の存在状況が変動しても、その変動に応じて常に適正量の吸着剤が排ガスに供給される。   In the present invention, in the adsorbent supply amount control step, an amount indicating the presence status of heavy metals in the exhaust gas is obtained based on the particle size distribution measured in the particle size distribution measurement step, and based on the obtained presence status of heavy metals. Thus, since the amount of adsorbent supplied to the exhaust gas is controlled, the amount of adsorbent supplied increases or decreases depending on the presence of heavy metals. Therefore, even if the presence state of heavy metals varies, an appropriate amount of adsorbent is always supplied to the exhaust gas in accordance with the variation.

本発明によれば、オンサイトで計測した粒度分布に基づいて求めた重金属類の存在状況を示す量を求め、この量に応じて吸着剤の供給量を増減するので、排ガス中の重金属類の存在状況の変動に対して上記供給量を短時間で追従させることができ、適切な量の吸着剤を排ガス中に供給することができる。   According to the present invention, the amount indicating the presence of heavy metals determined based on the particle size distribution measured on-site is obtained, and the amount of adsorbent supplied is increased or decreased according to this amount. The supply amount can be followed in a short time with respect to the fluctuation of the existing state, and an appropriate amount of adsorbent can be supplied into the exhaust gas.

実施形態に係る排ガス処理装置の構成を示すブロック図である。It is a block diagram which shows the structure of the exhaust gas processing apparatus which concerns on embodiment. 図1の排ガス処理装置における吸着剤の供給量の制御を示すフローチャートである。It is a flowchart which shows control of the supply amount of the adsorption agent in the exhaust gas processing apparatus of FIG.

以下、添付図面に基づいて本発明に係る排ガス処理装置の実施形態を説明する。   Hereinafter, an embodiment of an exhaust gas treatment apparatus according to the present invention will be described based on the accompanying drawings.

図1は、本実施形態に係る排ガス処理装置1の構成を示すブロック図である。同図では、排ガスおよび吸着剤の経路が実線で示され、電気信号の経路が破線で示されている。該排ガス処理装置1は、ガス状の重金属類を含む排ガスを排出する熱処理炉2と該排ガスを大気中に放出する煙突3との間に設けられている。上記熱処理炉2は、例えば、廃棄物焼却施設や製鋼精錬施設などにおける燃焼炉、溶融炉、加熱装置等である。   FIG. 1 is a block diagram showing a configuration of an exhaust gas treatment apparatus 1 according to the present embodiment. In the figure, the paths of the exhaust gas and the adsorbent are indicated by solid lines, and the paths of the electric signals are indicated by broken lines. The exhaust gas treatment apparatus 1 is provided between a heat treatment furnace 2 that exhausts exhaust gas containing gaseous heavy metals and a chimney 3 that releases the exhaust gas into the atmosphere. The heat treatment furnace 2 is, for example, a combustion furnace, a melting furnace, a heating device or the like in a waste incineration facility or a steel refining facility.

上記排ガス処理装置1は、上記熱処理炉2からの排ガス中に含まれる重金属類を吸着する吸着剤を該排ガス中に供給する吸着剤供給装置10と、該吸着剤を供給された排ガスを受けて該排ガス中の重金属類を吸着した吸着剤およびダストを除去する集塵装置20と、該集塵装置20から排出される排ガスの一部に冷却用ガスを加えて該排ガスを希釈して冷却することによりガス状の重金属類を凝縮させて微粒子とする希釈冷却装置30と、該希釈冷却装置30から排出された排ガス中に存在する重金属類の微粒子の粒度分布を計測する粒度分布計測装置40と、該粒度分布計測装置により計測された上記微粒子の粒度分布に基づき吸着剤供給量を制御する制御装置50とを備えている。   The exhaust gas treatment device 1 receives an adsorbent supply device 10 for supplying an adsorbent for adsorbing heavy metals contained in the exhaust gas from the heat treatment furnace 2 into the exhaust gas, and an exhaust gas supplied with the adsorbent. A dust collector 20 that removes the adsorbent and dust adsorbing heavy metals in the exhaust gas, and a cooling gas is added to a part of the exhaust gas discharged from the dust collector 20 to dilute and cool the exhaust gas. A dilution cooling device 30 for condensing gaseous heavy metals to form fine particles, and a particle size distribution measuring device 40 for measuring the particle size distribution of heavy metal fine particles present in the exhaust gas discharged from the dilution cooling device 30; And a control device 50 for controlling the amount of adsorbent supplied based on the particle size distribution of the fine particles measured by the particle size distribution measuring device.

吸着剤供給装置10は、熱処理炉2から該集塵装置20へ排ガスを流通させる煙道内に粉粒状の上記吸着剤を吹きこむ。該吸着剤供給装置10は、該吸着剤を貯留しておくための吸着剤貯槽(図示せず)と、スクリューフィーダやロータリーフィーダ等で構成され吸着剤貯槽に貯留された吸着剤を切り出す切出装置(図示せず)と、該切出装置によって切り出された吸着剤を煙道内へ向けて吹き込む吹込ノズル(図示せず)とを有している。上記吸着剤は、粉粒状であって、活性炭、カオリンあるいは粘土鉱物であることが好ましい。該粘土鉱物としては、例えば、カオリナイト、モンモリロナイト、ハロイサイト、ベントナイト、ディッカイト、イライト等が挙げられる。   The adsorbent supply device 10 blows the powdery adsorbent into the flue through which the exhaust gas flows from the heat treatment furnace 2 to the dust collector 20. The adsorbent supply device 10 includes an adsorbent storage tank (not shown) for storing the adsorbent, and a cutout that cuts out the adsorbent stored in the adsorbent storage tank, which includes a screw feeder, a rotary feeder, and the like. It has a device (not shown) and a blowing nozzle (not shown) for blowing the adsorbent cut out by the cutting device into the flue. The adsorbent is powdery and is preferably activated carbon, kaolin or clay mineral. Examples of the clay mineral include kaolinite, montmorillonite, halloysite, bentonite, dickite, illite and the like.

上記吸着剤供給装置10は、上記活性炭、カオリンあるいは粘土鉱物のうちの複数種を吸着剤として供給することとしてもよい。この場合、上記吸着剤貯槽および上記切出装置は、各種類の吸着剤に対応させて複数設ける。また、本実施形態では、吸着剤供給装置10は熱処理炉2と集塵装置20との間にて煙道内に吸着剤を吹きこむこととしたが、これに代えて、吹込ノズルを集塵装置20の入口部に設けて、集塵装置20のフィルタの上流側に吸着剤が吹き込まれるようにしてもよい。   The adsorbent supply apparatus 10 may supply a plurality of types of the activated carbon, kaolin, or clay mineral as an adsorbent. In this case, a plurality of adsorbent storage tanks and cutting devices are provided corresponding to each type of adsorbent. In the present embodiment, the adsorbent supply device 10 blows the adsorbent into the flue between the heat treatment furnace 2 and the dust collector 20, but instead, the blowing nozzle is used as the dust collector. The adsorbent may be blown into the upstream side of the filter of the dust collector 20.

集塵装置20は、例えば、バグフィルタ、セラミックフィルタ等によって構成されており、上記吸着剤供給装置10によって吸着剤が供給された排ガスを受けて該排ガス中の重金属類を吸着した吸着剤およびダストを捕集して除去する。熱処理炉2からの排ガスに含まれる重金属類はガス状であり、そのままでは集塵装置20のフィルタを通過してしまう。本実施形態では、該吸着剤によって上記ガス状の重金属類を吸着させて該吸着剤を集塵装置20で捕集することにより該ガス状の重金属類は容易に捕集される。吸着剤に吸着されなかった重金属類は集塵装置20を通過して該集塵装置20から排出される。以下、集塵装置20から排出される排ガスに含まれる重金属類、すなわち集塵装置20に捕集されない重金属類を「残留重金属類」という。   The dust collector 20 is constituted by, for example, a bag filter, a ceramic filter, and the like. The dust collector 20 receives the exhaust gas supplied with the adsorbent by the adsorbent supply device 10 and adsorbs the heavy metal in the exhaust gas and dust. Is collected and removed. The heavy metals contained in the exhaust gas from the heat treatment furnace 2 are in the form of gas and pass through the filter of the dust collector 20 as they are. In this embodiment, the gaseous heavy metals are easily collected by adsorbing the gaseous heavy metals with the adsorbent and collecting the adsorbent with the dust collector 20. Heavy metals that have not been adsorbed by the adsorbent pass through the dust collector 20 and are discharged from the dust collector 20. Hereinafter, heavy metals contained in the exhaust gas discharged from the dust collector 20, that is, heavy metals not collected by the dust collector 20, are referred to as “residual heavy metals”.

希釈冷却装置30は、集塵装置20から煙突3へ排ガスを流通させる煙道にて計測用として採取された一部の排ガスに冷却用ガスを加えて該排ガスを希釈して冷却する。この結果、採取された該排ガスに含まれているガス状の残留重金属類が凝縮して微粒子となる。また、希釈冷却装置30によって採取されなかった排ガスの残部は、煙突3から大気中へ放出される。本実施形態では、後述するように、吸着剤の供給量が制御されることにより、大気中へ放出される排ガスに含まれる残留金属類の濃度は適切な値まで減少される。上記希釈冷却装置30は必須ではなく、集塵装置20からの排ガスに含まれる重金属類が微粒子状であるような場合には該希釈冷却装置30を設ける必要はない。この場合、上記煙道から採取された一部の排ガスは後述の粒度分布計測装置40に直接導入されることとなる。   The dilution cooling device 30 dilutes and cools the exhaust gas by adding a cooling gas to a part of the exhaust gas collected for measurement in the flue through which the exhaust gas flows from the dust collector 20 to the chimney 3. As a result, gaseous residual heavy metals contained in the collected exhaust gas are condensed into fine particles. Further, the remaining part of the exhaust gas not collected by the dilution cooling device 30 is released from the chimney 3 into the atmosphere. In the present embodiment, as will be described later, by controlling the supply amount of the adsorbent, the concentration of residual metals contained in the exhaust gas released into the atmosphere is reduced to an appropriate value. The dilution cooling device 30 is not essential, and it is not necessary to provide the dilution cooling device 30 when the heavy metals contained in the exhaust gas from the dust collector 20 are in the form of fine particles. In this case, a part of the exhaust gas collected from the flue is directly introduced into the particle size distribution measuring device 40 described later.

粒度分布計測装置40は、上記希釈冷却装置30で冷却された排ガス中に含まれる残留重金属類の微粒子の粒度分布を計測する。該粒度分布計測装置40は、例えば、電子式低圧インパクター、走査式モビリティーパーティクルサイザー(SMPS)、レーザー回折・散乱式粒度分布測定器等により構成される。   The particle size distribution measuring device 40 measures the particle size distribution of fine particles of residual heavy metals contained in the exhaust gas cooled by the dilution cooling device 30. The particle size distribution measuring device 40 includes, for example, an electronic low-pressure impactor, a scanning mobility particle sizer (SMPS), a laser diffraction / scattering particle size distribution measuring device, and the like.

上記電子式低圧インパクターは、慣性衝突の原理を応用したインパクターと呼ばれる分級装置に電気的な処理を適用し、オンラインで粒度分布を計測できるようにした装置である。走査式モビリティーパーティクルサイザーは、帯電した微粒子の粒径と電気移動度との対応が一対一の関係となることを利用して粒度分布を計測できるようにした装置である。レーザー回折・散乱式式粒度分布測定器は、レーザー光を微粒子に照射した時に粒子径により散乱される散乱光量と散乱パターンが異なることを利用して粒度分布を計測できるようにした装置である。   The electronic low-pressure impactor is a device that applies an electrical process to a classifier called an impactor that applies the principle of inertial collision so that the particle size distribution can be measured online. The scanning mobility particle sizer is a device that can measure the particle size distribution by utilizing the one-to-one relationship between the particle size of charged fine particles and the electric mobility. The laser diffraction / scattering type particle size distribution measuring device is an apparatus that can measure the particle size distribution by utilizing the fact that the amount of scattered light and the scattering pattern differ depending on the particle diameter when the fine particles are irradiated with laser light.

上記粒度分布計測装置40は、上記計測した粒度分布を計測データ信号として制御装置50へ発信する。   The particle size distribution measuring device 40 transmits the measured particle size distribution to the control device 50 as a measurement data signal.

制御装置50は、上記粒度分布計測装置40によって計測された残留重金属類の微粒子の粒度分布に基づいて排ガス中における残留重金属類の濃度(以下、「残留重金属類濃度」という)を導出する濃度導出部51と、該濃度導出部51によって導出された残留重金属類濃度に基づいて吸着剤の供給量を決定する供給量決定部52と、上記濃度導出部51による残留重金属類濃度の導出および上記供給量決定部52による吸着剤の供給量の決定のために用いられるデータを保持しているデータ保持部53とを有している。   The control device 50 derives the concentration for deriving the concentration of residual heavy metals in the exhaust gas (hereinafter referred to as “residual heavy metal concentration”) based on the particle size distribution of the fine particles of residual heavy metals measured by the particle size distribution measuring device 40. 51, a supply amount determination unit 52 for determining the supply amount of the adsorbent based on the residual heavy metal concentration derived by the concentration deriving unit 51, derivation of the residual heavy metal concentration by the concentration deriving unit 51 and the supply And a data holding unit 53 that holds data used for determining the supply amount of the adsorbent by the amount determining unit 52.

上記データ保持部53は、複数パターンの微粒子粒度分布と該微粒子粒度分布のそれぞれと対応する化学分析法によって求めた重金属類濃度との相関関係を示すデータベースを予め保持している。また、該データ保持部53は、残留重金属類の濃度の目標値(以下、「目標濃度」という)のデータをも予め保持している。該目標濃度は、例えば排ガス排出規制等に基づいて決定されている。   The data holding unit 53 holds in advance a database showing a correlation between a plurality of fine particle size distributions and a heavy metal concentration obtained by a chemical analysis method corresponding to each of the fine particle size distributions. The data holding unit 53 also holds in advance data of a target value (hereinafter referred to as “target concentration”) of the residual heavy metal concentration. The target concentration is determined based on, for example, exhaust gas emission regulations.

上記濃度導出部51は、上記粒度分布計測装置40からの計測データ信号を受信して、計測された粒度分布を上記データ保持部53が保持するデータベースに照合することにより残留金属類の濃度を導出する。   The concentration deriving unit 51 receives a measurement data signal from the particle size distribution measuring device 40 and compares the measured particle size distribution with a database held by the data holding unit 53 to derive the concentration of residual metals. To do.

上記供給量決定部52は、上記濃度導出部51で導出された残留金属類の残留重金属類濃度のデータを上記データ保持部53が予め保持している目標濃度のデータと比較する。そして、残留重金属類濃度が目標濃度よりも大きいときに、吸着剤の供給量を増加させるように吸着剤供給装置10の制御を行い、微粒子濃度が目標濃度よりも小さいときに、吸着剤の供給量を減少させるように吸着剤供給装置10の制御を行うように設定されている。   The supply amount determination unit 52 compares the data of the residual heavy metal concentration of the residual metal derived by the concentration deriving unit 51 with the data of the target concentration held in advance by the data holding unit 53. When the residual heavy metal concentration is higher than the target concentration, the adsorbent supply device 10 is controlled so as to increase the supply amount of the adsorbent, and when the fine particle concentration is lower than the target concentration, the supply of the adsorbent is performed. It is set to control the adsorbent supply device 10 so as to reduce the amount.

以下、本実施形態に係る排ガス処理装置1の排ガス処理動作について説明する。   Hereinafter, the exhaust gas treatment operation of the exhaust gas treatment device 1 according to the present embodiment will be described.

図2は、排ガス処理装置1における吸着剤の供給量の制御を示すフローチャートである。まず、吸着剤供給装置10が熱処理炉2からの排ガスに吸着剤を供給する(S1)。次に、集塵装置20が、排ガス中の重金属類を吸着した吸着剤およびダストを捕集する(S2)。次に、希釈冷却装置30が、集塵装置20から排出された排ガスの一部を採取して該排ガスを希釈冷却する(S3)。この結果、該排ガスに含まれているガス状の残留重金属類が凝縮して微粒子となる。そして、粒度分布計測装置40が残留重金属類の微粒子の粒度分布を計測する(S4)。   FIG. 2 is a flowchart showing control of the amount of adsorbent supplied in the exhaust gas treatment apparatus 1. First, the adsorbent supply device 10 supplies the adsorbent to the exhaust gas from the heat treatment furnace 2 (S1). Next, the dust collector 20 collects the adsorbent and dust that have adsorbed heavy metals in the exhaust gas (S2). Next, the dilution cooling device 30 collects a part of the exhaust gas discharged from the dust collector 20 and dilutes and cools the exhaust gas (S3). As a result, gaseous residual heavy metals contained in the exhaust gas are condensed into fine particles. Then, the particle size distribution measuring device 40 measures the particle size distribution of the residual heavy metal fine particles (S4).

次に、濃度導出部51が、計測された粒度分布をデータ保持部53が保持するデータベースに照合して残留金属類濃度を導出する(S5)。そして、供給量決定部52が、上記残留重金属類濃度に基づいて吸着剤の供給量を決定し、吸着剤供給装置10を制御する。具体的には、残留重金属類濃度が目標濃度より大きいとき(S6のY)、供給量決定部52は吸着剤の供給量を増加させるように吸着剤供給装置10を制御する。そして、微粒子濃度が目標濃度より小さいとき(S6のN)、供給量決定部52は吸着剤の供給量を減少させるように吸着剤供給装置10を制御する。具体的には、例えば吸着剤供給装置の切り出し装置の出力を適正値に制御する。この結果、残留金属類濃度は目標濃度へ近づく。   Next, the concentration deriving unit 51 compares the measured particle size distribution with a database held by the data holding unit 53 to derive a residual metal concentration (S5). Then, the supply amount determination unit 52 determines the supply amount of the adsorbent based on the residual heavy metal concentration, and controls the adsorbent supply device 10. Specifically, when the residual heavy metal concentration is higher than the target concentration (Y in S6), the supply amount determination unit 52 controls the adsorbent supply device 10 to increase the supply amount of the adsorbent. When the fine particle concentration is smaller than the target concentration (N in S6), the supply amount determination unit 52 controls the adsorbent supply device 10 so as to decrease the supply amount of the adsorbent. Specifically, for example, the output of the cutting device of the adsorbent supply device is controlled to an appropriate value. As a result, the residual metal concentration approaches the target concentration.

本実施形態では、排ガス処理装置1の運転中において、集塵装置20からの排ガスに含まれる重金属類濃度を導出し、導出した残留重金属類濃度に基づいて吸着剤の供給量を制御することとした。したがって、排ガス中の重金属類濃度が変動しても、その変動に応じて上記吸着剤の供給量を増減させることにより、該供給量を短時間で追従させることができ、常に適切な量の吸着剤を供給できる。この結果、最終的に大気中へ放出される排ガスに含まれる残留重金属類の濃度を適切な値まで減少させることができる。   In the present embodiment, during operation of the exhaust gas treatment device 1, the concentration of heavy metals contained in the exhaust gas from the dust collector 20 is derived, and the amount of adsorbent supplied is controlled based on the derived concentration of residual heavy metals. did. Therefore, even if the concentration of heavy metals in the exhaust gas fluctuates, the amount of adsorbent supplied can be increased or decreased in accordance with the fluctuation, so that the amount supplied can be followed in a short time, and an appropriate amount of adsorption can always be achieved. The agent can be supplied. As a result, the concentration of residual heavy metals contained in the exhaust gas finally released into the atmosphere can be reduced to an appropriate value.

また、過大な量の吸着剤が供給されることがないので、排ガス処理費用やダスト処理費用の増大を抑制できる。さらには、集塵装置のフィルタが過大な量の吸着剤を捕集することに起因してフィルタの圧力損失の増大することがなく、この結果、送気装置の負荷増加を防止できる。また、煙道内に過大な量の吸着剤が堆積することに起因する排ガスの流れの異常発生や煙道の閉塞を防止できる。   Moreover, since an excessive amount of adsorbent is not supplied, it is possible to suppress an increase in exhaust gas treatment costs and dust treatment costs. In addition, the filter pressure loss of the filter does not increase due to the filter of the dust collector collecting an excessive amount of adsorbent, and as a result, an increase in the load of the air supply device can be prevented. In addition, it is possible to prevent an abnormal flow of the exhaust gas and blockage of the flue caused by an excessive amount of adsorbent being deposited in the flue.

本発明は、ガス中のガス状または微粒子状の重金属類を除去する産業分野で利用可能である。   INDUSTRIAL APPLICABILITY The present invention can be used in the industrial field for removing gaseous or particulate heavy metals in a gas.

1 排ガス処理装置
10 吸着剤供給装置
20 集塵装置
30 希釈冷却装置
40 粒度分布計測装置
50 制御装置(吸着剤供給量制御装置)
DESCRIPTION OF SYMBOLS 1 Exhaust gas processing apparatus 10 Adsorbent supply apparatus 20 Dust collector 30 Dilution cooling apparatus 40 Particle size distribution measuring apparatus 50 Control apparatus (adsorbent supply amount control apparatus)

Claims (5)

重金属類を含む排ガスの処理装置において、
該重金属類を吸着する吸着剤を排ガスに供給する吸着剤供給装置と、
該吸着剤を供給された排ガスを受けて、該排ガスに含まれている重金属類を吸着した吸着剤およびダストを除去する集塵装置と、
該集塵装置から排出される排ガス中の重金属類の微粒子の粒度分布を計測する粒度分布計測装置と、
該粒度分布計測装置により計測された上記微粒子の粒度分布に基づき排ガス中の重金属類の存在状況を示す量を求め、求めた重金属類の存在状況に基づき、排ガスに供給する吸着剤の供給量を制御する吸着剤供給量制御装置と、
を有することを特徴とする排ガス処理装置。
In exhaust gas treatment equipment containing heavy metals,
An adsorbent supply device that supplies the exhaust gas with an adsorbent that adsorbs the heavy metals;
A dust collector that receives the exhaust gas supplied with the adsorbent and removes the adsorbent and dust adsorbing heavy metals contained in the exhaust gas;
A particle size distribution measuring device for measuring the particle size distribution of fine particles of heavy metals in the exhaust gas discharged from the dust collector;
Based on the particle size distribution of the fine particles measured by the particle size distribution measuring device, an amount indicating the presence of heavy metals in the exhaust gas is obtained, and the amount of adsorbent supplied to the exhaust gas is determined based on the obtained presence of heavy metals. An adsorbent supply amount control device to control,
An exhaust gas treatment apparatus comprising:
排ガス中の重金属類の存在状況を示す量は、該重金属類の濃度であり、
吸着剤供給量制御装置は、微粒子の粒度分布と重金属類の濃度との相関関係を示すデータを予め保持しており、該データに基づいて上記計測された微粒子の粒度分布と対応する重金属類濃度を導出し、
導出した重金属類の濃度が所定の目標濃度よりも大きいときに、吸着剤の供給量を増加させるように吸着剤供給装置の制御を行い、
導出した重金属類の濃度が所定の目標濃度よりも小さいときに、吸着剤の供給量を減少させるように吸着剤供給装置の制御を行うように設定されている
こととする請求項1に記載の排ガス処理装置。
The amount indicating the presence of heavy metals in the exhaust gas is the concentration of the heavy metals,
The adsorbent supply amount control device holds in advance data indicating the correlation between the particle size distribution of fine particles and the concentration of heavy metals, and the heavy metal concentration corresponding to the particle size distribution measured above based on the data Is derived,
When the derived heavy metal concentration is higher than a predetermined target concentration, the adsorbent supply device is controlled to increase the adsorbent supply amount,
2. The adsorbent supply device is set to perform control so as to reduce the supply amount of the adsorbent when the derived heavy metal concentration is smaller than a predetermined target concentration. Exhaust gas treatment equipment.
粒度分布計測装置に導入する排ガスを希釈冷却する希釈冷却装置をさらに有することとする請求項1または請求項2に記載の排ガス処理装置。   The exhaust gas treatment device according to claim 1 or 2, further comprising a dilution cooling device for diluting and cooling the exhaust gas introduced into the particle size distribution measuring device. 吸着剤供給装置は、活性炭、カオリンおよび粘土鉱物のうち少なくとも一つを吸着剤として排ガス中に供給することとする請求項1ないし請求項3のいずれか一つに記載の排ガス処理装置。   The exhaust gas treatment device according to any one of claims 1 to 3, wherein the adsorbent supply device supplies at least one of activated carbon, kaolin, and clay mineral as an adsorbent into the exhaust gas. 重金属類を含む排ガスの処理方法において、
該重金属類を吸着する吸着剤を排ガスに供給する吸着剤供給工程と、
該吸着剤を供給された排ガスを受けて、該排ガスに含まれている重金属類を吸着した吸着剤およびダストを除去する集塵工程と、
該集塵工程で排出される排ガス中の重金属類の微粒子の粒度分布を計測する粒度分布計測工程と、
該粒度分布計測工程で計測された上記微粒子の粒度分布に基づき排ガス中の重金属類の存在状況を示す量を求め、求めた重金属類の存在状況に基づき、排ガスに供給する吸着剤供給量を制御する吸着剤供給量制御工程と、
を有することを特徴とする排ガス処理方法。
In a method for treating exhaust gas containing heavy metals,
An adsorbent supply step of supplying an adsorbent that adsorbs the heavy metals to the exhaust gas;
A dust collection step of receiving the exhaust gas supplied with the adsorbent and removing the adsorbent and dust adsorbing heavy metals contained in the exhaust gas;
A particle size distribution measuring step for measuring a particle size distribution of fine particles of heavy metals in the exhaust gas discharged in the dust collecting step;
Based on the particle size distribution of the fine particles measured in the particle size distribution measurement step, the amount indicating the presence of heavy metals in the exhaust gas is obtained, and the amount of adsorbent supplied to the exhaust gas is controlled based on the obtained presence of heavy metals. Adsorbent supply amount control step to perform,
An exhaust gas treatment method characterized by comprising:
JP2009075567A 2009-03-26 2009-03-26 Exhaust gas treatment apparatus and exhaust gas treatment method Pending JP2010227747A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009075567A JP2010227747A (en) 2009-03-26 2009-03-26 Exhaust gas treatment apparatus and exhaust gas treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009075567A JP2010227747A (en) 2009-03-26 2009-03-26 Exhaust gas treatment apparatus and exhaust gas treatment method

Publications (1)

Publication Number Publication Date
JP2010227747A true JP2010227747A (en) 2010-10-14

Family

ID=43044144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009075567A Pending JP2010227747A (en) 2009-03-26 2009-03-26 Exhaust gas treatment apparatus and exhaust gas treatment method

Country Status (1)

Country Link
JP (1) JP2010227747A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103446830A (en) * 2013-07-02 2013-12-18 香港诺曼泰壹环保科技有限公司 Flue gas purifying system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103446830A (en) * 2013-07-02 2013-12-18 香港诺曼泰壹环保科技有限公司 Flue gas purifying system
CN103446830B (en) * 2013-07-02 2015-07-01 香港诺曼泰壹环保科技有限公司 Flue gas purifying system

Similar Documents

Publication Publication Date Title
JP6124097B1 (en) Exhaust gas treatment apparatus and exhaust gas treatment method
KR100375198B1 (en) Method of treating exhaust gas
CN112997182A (en) Exhaust gas purification device, and method and data processing system for monitoring at least one exhaust gas purification device
KR101699641B1 (en) Method and apparatus for treating exhaust gas
JP5973647B2 (en) Activated carbon and coal combustion residue treatment system and method
JP6315275B2 (en) Exhaust gas treatment apparatus and exhaust gas treatment method
WO1998029692A1 (en) Combustion equipment for flue gas exhausting plants
JP2009298677A (en) System and method for treating cement kiln extraction gas
JP2014195790A (en) Exhaust gas treatment method
JP2010227747A (en) Exhaust gas treatment apparatus and exhaust gas treatment method
Schallert et al. Do we underestimate the impact of particles in coal-derived flue gas on amine-based CO2 capture processes?
JP7047488B2 (en) Exhaust gas treatment equipment and exhaust gas treatment method
JP2015213889A (en) Treatment device and method of cement kiln exhaust gas
JP2009247998A (en) Exhaust gas treatment method
JP6221870B2 (en) Exhaust gas treatment system
JP6872169B2 (en) Exhaust gas treatment equipment and exhaust gas treatment method
JP3235513B2 (en) Exhaust gas treatment method
JP7264372B2 (en) Waste incineration system
JPH10296046A (en) Removing process for acidic component in exhaust gas
JP2014172000A (en) System and method for recovering selenium in exhaust gas
JP2010076973A (en) Apparatus and method for processing exhaust gas of cement kiln
JPH10230120A (en) Measuring device for dust collection efficiency of dust collector
JP7299721B2 (en) Exhaust gas treatment system and exhaust gas treatment method
JP2010221085A (en) Exhaust gas treatment system
JP2004000866A (en) Method and apparatus for treating waste gas