JP2008212923A - Exhaust gas treatment agent, and exhaust gas treating method and treatment system - Google Patents

Exhaust gas treatment agent, and exhaust gas treating method and treatment system Download PDF

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JP2008212923A
JP2008212923A JP2008025905A JP2008025905A JP2008212923A JP 2008212923 A JP2008212923 A JP 2008212923A JP 2008025905 A JP2008025905 A JP 2008025905A JP 2008025905 A JP2008025905 A JP 2008025905A JP 2008212923 A JP2008212923 A JP 2008212923A
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exhaust gas
powder
treatment
dust
slaked lime
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Shigeru Fukushima
繁 福島
Michito Sumimori
道人 角森
Atsushi Kidera
淳 木寺
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Ryoko Lime Industry Co Ltd
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Ryoko Lime Industry Co Ltd
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<P>PROBLEM TO BE SOLVED: To provide an exhaust gas treatment agent capable of surely cleaning exhaust gas by using a small amount and stabilizing heavy metals, and to provide an exhaust gas treatment system. <P>SOLUTION: The exhaust gas treatment agent comprises a powder mixture of a slaked lime powder and a dawsonite powder, and can neutralize an acid component and stabilize a heavy metal contained in the exhaust gas. Preferably, the powder mixture contains 20-45% of the dawsonite powder and the specific surface area of the dawsonite powder and the slake lime powder is 30 m<SP>2</SP>/g or larger. The exhaust gas treatment method comprises the steps of adding the exhaust gas treatment agent to the exhaust gas to neutralize the acid component contained in the exhaust gas and adsorb the heavy metals, passing the exhaust gas to which the agent is added through a dust collector to precipitate dust, and adding water to the collected dust and kneading the dust with water to turn the dust into clay. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、排ガスの中和処理と重金属類の安定化処理を同時に行うことができ、少ない使用量によって優れた処理効果を得ることができる排ガス処理剤とその処理方法および処理システムに関する。なお、本発明において、排ガス処理と煤塵処理を併せて排ガス処理と略称し、排ガス中の酸性成分や重金属類は煤塵中のものも含み、排ガスの中和処理は煤塵の中和処理を含む。   The present invention relates to an exhaust gas treatment agent that can simultaneously perform neutralization treatment of exhaust gas and stabilization treatment of heavy metals, and can obtain an excellent treatment effect with a small amount of use, and a treatment method and treatment system thereof. In the present invention, exhaust gas treatment and dust treatment are collectively abbreviated as exhaust gas treatment, and acidic components and heavy metals in exhaust gas include those in dust, and exhaust gas neutralization treatment includes soot dust neutralization treatment.

通常、ゴミ焼却施設の排ガス処理系には排ガスに含まれる酸性成分や煤塵を処理する設備が設けられている。具体的には、例えば、図2に示すように、ゴミ焼却施設20の排ガス流路21には、排ガス冷却部22、排ガス中の酸性成分を中和するアルカリ薬剤の投入部23、集塵機24、ブロワー25などが設けられている。一方、集塵機24には捕集した煤塵の処理設備が設けられている。該処理設備には、煤塵を留める貯槽27、混練装置30、混練装置30の煤塵に重金属処理剤を添加する手段31および給水手段32、処理物を外部に排出するホッパ33などが設けられている。   Usually, an exhaust gas treatment system of a garbage incineration facility is provided with equipment for treating acidic components and soot contained in the exhaust gas. Specifically, for example, as shown in FIG. 2, in the exhaust gas flow path 21 of the garbage incineration facility 20, an exhaust gas cooling unit 22, an alkaline chemical charging unit 23 for neutralizing acidic components in the exhaust gas, a dust collector 24, A blower 25 and the like are provided. On the other hand, the dust collector 24 is provided with a processing facility for collected dust. The treatment facility is provided with a storage tank 27 for retaining dust, a kneading device 30, a means 31 for adding a heavy metal treating agent to the dust in the kneading apparatus 30, a water supply means 32, a hopper 33 for discharging the treated material to the outside, and the like. .

ゴミ焼却施設20の燃焼排ガスは排ガス冷却部22において廃熱ボイラーまたは水噴霧などによって冷却される。次いで、排ガスに含まれるHClやSOxなどの酸性成分を中和するアルカリ薬剤が投入される。この中和剤としては一般に消石灰粉末が用いられている。中和剤を添加した排ガスは集塵機24に導かれて飛灰等の煤塵が捕集され、煤塵が除去された排ガスはブロワー25に吸引されて煙突26から外部に放出される。   The combustion exhaust gas from the waste incineration facility 20 is cooled in the exhaust gas cooling unit 22 by a waste heat boiler or water spray. Next, an alkaline agent that neutralizes acidic components such as HCl and SOx contained in the exhaust gas is introduced. As this neutralizer, slaked lime powder is generally used. The exhaust gas to which the neutralizing agent has been added is guided to the dust collector 24 where dust such as fly ash is collected, and the exhaust gas from which the dust has been removed is sucked into the blower 25 and discharged from the chimney 26 to the outside.

一方、集塵機24で捕集された煤塵は貯槽27に溜められ、定量フィーダ29を通じて混練装置30に導入される。混練装置30の煤塵には重金属類を不溶化処理する薬剤が水と共に一定量または流量が調整されて添加され、煤塵に含まれる重金属類を不溶化(安定化)すると共に粉状の煤塵を混練して粘土状にし、取り扱いやすくして外部に搬出している。   On the other hand, the dust collected by the dust collector 24 is stored in the storage tank 27 and introduced into the kneading apparatus 30 through the quantitative feeder 29. A chemical for insolubilizing heavy metals is added to the soot and dust of the kneading device 30 together with water so that a certain amount or flow rate is adjusted to insolubilize (stabilize) the heavy metals contained in the soot and knead the dusty dust. It is made in clay and made easy to handle.

従来、重金属類の安定化剤として各種薬剤が知られており、例えば、(1)ジチオカルバミン酸系やピペラジン系のキレート剤、(2)リン酸系薬剤、(3)シリカやアルミニウムシリケートの吸着剤、(4)水酸化アルミニウムや硫酸バンドなどのアルミニウム化合物、(5)ケイ酸ナトリウムなどの水ガラス類などが用いられている。   Conventionally, various drugs are known as stabilizers for heavy metals, such as (1) dithiocarbamic acid and piperazine chelating agents, (2) phosphoric acid drugs, and (3) silica and aluminum silicate adsorbents. (4) Aluminum compounds such as aluminum hydroxide and sulfuric acid band, and (5) water glasses such as sodium silicate are used.

従来の排ガス処理設備では、排ガス中の酸性成分を中和するために消石灰を添加し、この中和処理後に捕集した煤塵について重金属類の安定化剤を添加している。このような二段階処理のために従来の設備は構成が煩雑になり、処理操作も煩わしいと云う問題があった。   In conventional exhaust gas treatment equipment, slaked lime is added to neutralize acidic components in the exhaust gas, and heavy metal stabilizers are added to the dust collected after the neutralization treatment. Due to such a two-stage process, the conventional equipment has a problem in that the configuration is complicated and the processing operation is also troublesome.

そこで、排ガス中和剤と重金属安定化剤を混合した複合処理剤が提案されている。この複合処理剤は、排ガス中和剤として主に消石灰が用いられており、重金属の不溶化剤として各種の薬剤が用いられている。例えば、消石灰粉末とセメント類や硫酸塩等の中和剤やキレート剤や水ガラスやリン酸塩などを混合してなる処理剤(特許文献1)、消石灰と水酸化アルミニウム等のアルミニウム化合物とを混合してなる処理剤(特許文献2)、石灰粉末に石膏等の硫酸塩物質と水酸化アルミニウム等のアルミニウム化合物とを混合してなる処理剤(特許文献3および特許文献4)、消石灰粉末に水酸化アルミニウム及び又は活性アルミナ粉末を混合してなる処理剤(特許文献5)が知られている。
特開平09−99234号公報(特許第3867307号公報) 特開2000−42360号公報 特開2000−301101号公報 特開2001−327834号公報 特開2003−311122号公報
Therefore, a composite treatment agent in which an exhaust gas neutralizer and a heavy metal stabilizer are mixed has been proposed. In this composite treatment agent, slaked lime is mainly used as an exhaust gas neutralizing agent, and various chemicals are used as an insolubilizing agent for heavy metals. For example, slaked lime powder and a processing agent (patent document 1) formed by mixing a neutralizing agent such as cement or sulfate, a chelating agent, water glass or phosphate, slaked lime and an aluminum compound such as aluminum hydroxide. Treatment agent obtained by mixing (Patent Document 2), Treatment agent obtained by mixing sulfate substance such as gypsum and aluminum compound such as aluminum hydroxide in lime powder (Patent Document 3 and Patent Document 4), and slaked lime powder A treatment agent (Patent Document 5) obtained by mixing aluminum hydroxide and / or activated alumina powder is known.
JP 09-99234 A (Patent No. 3867307) JP 2000-42360 A JP 2000-301101 A JP 2001-327834 A JP 2003-311122 A

従来の複合処理剤の大部分は、排ガス中和成分として消石灰を用い、これに重金属安定化剤を混合したものであり、いわゆる分業性薬剤を混合したものであるため、処理剤の全使用量が排ガス中和剤と重金属処理剤とを個別に使用する従来の方法に比較して、さほど減少せず、複合処理剤としてのメリットが少ないものであった。   Most of the conventional composite treatment agents use slaked lime as an exhaust gas neutralizing component and are mixed with a heavy metal stabilizer, which is a mixture of so-called special labor chemicals. However, compared with the conventional method which uses an exhaust gas neutralizer and a heavy metal treating agent separately, it did not decrease so much and there were few merit as a composite treating agent.

本発明は、排ガス処理剤について、従来の上記問題を解決したものであり、より少ない使用量で確実に排ガスの中和処理および重金属類の安定化処理を行うことができる排ガス処理剤とその処理システムを提供する。   The present invention solves the above-mentioned conventional problems with exhaust gas treatment agents, and an exhaust gas treatment agent capable of reliably performing exhaust gas neutralization treatment and heavy metal stabilization treatment with a smaller amount of use and the treatment thereof Provide a system.

本発明は以下の構成を有する排ガス処理剤とその処理システムに関する。
〔1〕消石灰粉末とドーソナイト粉末との混合粉末からなり、排ガス中の酸性成分を中和すると共に排ガス中の重金属を安定化することを特徴とする排ガス処理剤。
〔2〕混合粉末中に20%〜45%のドーソナイト粉末を含有する上記[1]に記載する排ガス処理剤。
〔3〕消石灰粉末およびドーソナイト粉末の比表面積が30m2/g以上である上記[1]または上記[2]に記載する排ガス処理剤。
〔4〕上記[1]〜上記[3]の何れかに記載する排ガス処理剤を排ガスに添加して排ガスに含まれる酸性成分を中和すると共に重金属類を吸着させ、次いでこの排ガスを集塵機に通じて排ガス中の煤塵と排ガス処理剤とを集塵し、集塵した粉体を加水混練して粘土状にすることを特徴とする排ガスの処理方法。
〔5〕消石灰粉末とドーソナイト粉末との混合粉末からなる排ガス処理剤を排ガス中に添加する手段と、排ガスに含まれる煤塵と排ガス処理剤とを捕集する集塵機と、集塵した粉体を加水混練する手段とを有することを特徴とする排ガス処理システム。
The present invention relates to an exhaust gas treatment agent having the following configuration and a treatment system thereof.
[1] An exhaust gas treatment agent comprising a mixed powder of slaked lime powder and dawsonite powder, which neutralizes acidic components in exhaust gas and stabilizes heavy metals in exhaust gas.
[2] The exhaust gas treating agent according to [1], wherein the mixed powder contains 20% to 45% of dawsonite powder.
[3] The exhaust gas treating agent according to [1] or [2] above, wherein the specific surface areas of the slaked lime powder and the dosonite powder are 30 m 2 / g or more.
[4] The exhaust gas treating agent described in any one of [1] to [3] above is added to the exhaust gas to neutralize acidic components contained in the exhaust gas and adsorb heavy metals, and then the exhaust gas is passed to a dust collector. A method for treating exhaust gas, comprising collecting dust and exhaust gas treatment agent in the exhaust gas through the mixture, and hydromixing the collected powder into clay.
[5] Means for adding an exhaust gas treatment agent comprising a mixed powder of slaked lime powder and dosonite powder to the exhaust gas, a dust collector for collecting the soot and the exhaust gas treatment agent contained in the exhaust gas, and the collected powder An exhaust gas treatment system comprising means for kneading.

本発明の排ガス処理剤は、消石灰粉末とドーソナイト粉末を含有しており、ドーソナイト粉末は重金属類を吸着して安定化すると共に排ガス中の酸性成分を中和する作用を有するので、消石灰粉末とドーソナイト粉末による相乗的な中和効果を得ることができ、またドーソナイト粉末は重金属類を安定化する効果に優れるので、確実に排ガスを中和し、重金属類を安定化することができる。   The exhaust gas treatment agent of the present invention contains slaked lime powder and dawsonite powder, and the dowsonite powder has an action of adsorbing and stabilizing heavy metals and neutralizing acidic components in the exhaust gas. A synergistic neutralization effect by the powder can be obtained, and the dosonite powder has an excellent effect of stabilizing heavy metals, so that the exhaust gas can be reliably neutralized and the heavy metals can be stabilized.

本発明の排ガス処理剤に含まれるドーソナイトは、300℃以下では分解せず安定であり、アルカリ粉末と混合しても反応せず安定に存在する。従って、本発明の排ガス処理剤はゴミ焼却施設の排ガスに投入しても安定であり、排ガス煙道の吹込み剤として適する。また、ドーソナイトは、排ガス中の酸性成分と反応した後にも十分に重金属類を不溶化する効果を有しているので、消石灰粉末と混合してその中和作用を補助しつつ、重金属安定化剤として使用することができる。このため、従来の処理剤よりも格段に少い使用量によって排ガスに含まれる酸性成分を中和し、重金属類を不溶溶化(安定化)することができる。   The dosonite contained in the exhaust gas treating agent of the present invention is stable without being decomposed at 300 ° C. or less, and is stable without reacting even when mixed with alkali powder. Therefore, the exhaust gas treating agent of the present invention is stable even if it is put into the exhaust gas of a garbage incineration facility, and is suitable as a blowing agent for exhaust gas flue. In addition, since dosonite has the effect of sufficiently insolubilizing heavy metals even after reacting with acidic components in the exhaust gas, it is mixed with slaked lime powder to assist its neutralizing action, and as a heavy metal stabilizer Can be used. For this reason, it is possible to neutralize the acidic components contained in the exhaust gas and to insolubilize (stabilize) heavy metals by using a much smaller amount than the conventional treating agent.

本発明の排ガス処理剤は、排ガスに含まれる酸性成分に対する中和作用と重金属類に対する不溶化作用とを同時に有するので、排ガスへの投入が一度で済み、処理操作および処理設備を簡略化することができる。また、本発明の排ガス処理剤を用いたものは、重金属類が不溶化しており、埋立溶出基準値を下回っているので、そのまま埋立処分することができる。   Since the exhaust gas treating agent of the present invention has both a neutralizing action on acidic components contained in the exhaust gas and an insolubilizing action on heavy metals, it can be introduced into the exhaust gas only once, simplifying the processing operation and processing equipment. it can. Moreover, the thing using the exhaust gas treating agent of the present invention is insolubilized with heavy metals and is lower than the landfill elution reference value, so it can be disposed as landfill.

以下、本発明を具体的に説明する。なお、%は単位固有の場合を除き質量%であり、比表面積はBET比表面積である。   Hereinafter, the present invention will be specifically described. In addition,% is mass% except the case intrinsic | native to a unit, and a specific surface area is a BET specific surface area.

本発明の排ガス処理剤は、消石灰粉末とドーソナイト粉末との混合粉末からなり、排ガスに含まれる酸性成分を中和すると共に重金属を安定化することを特徴とする排ガス処理剤である。   The exhaust gas treatment agent of the present invention is an exhaust gas treatment agent comprising a mixed powder of slaked lime powder and dawsonite powder, which neutralizes acidic components contained in the exhaust gas and stabilizes heavy metals.

本発明の排ガス処理剤に含まれる消石灰粉末は、排ガスに含まれる酸性成分(HCl、SO2やSO3等の硫黄酸化物)と反応し、これを中和する作用を有する。 The slaked lime powder contained in the exhaust gas treating agent of the present invention has an action of reacting with and neutralizing acidic components (sulfur oxides such as HCl, SO 2 and SO 3 ) contained in the exhaust gas.

本発明の排ガス処理剤に含まれるドーソナイト[NaAlCO3(OH)2]は、排ガスに含まれる酸性成分と反応してこれを中和する作用を有し、さらに煤塵に含まれる重金属類に対してこれを炭酸化して安定し、また煤塵中に残留する未反応の消石灰分とドーソナイトが反応してCa−Al化合物を形成し、この反応生成物がイオン交換等によって重金属類を取り込んで安定化する作用を有する。 The dosonite [NaAlCO 3 (OH) 2 ] contained in the exhaust gas treating agent of the present invention has an action of reacting with and neutralizing the acidic component contained in the exhaust gas, and further against heavy metals contained in soot dust. This is carbonated and stabilized, and unreacted slaked lime remaining in the dust and dosonite react to form a Ca-Al compound, and this reaction product stabilizes by taking in heavy metals by ion exchange or the like. Has an effect.

ドーソナイトの排ガス中の酸性成分に対する中和効果は、消石灰の約半分程度であるので、中和効果を高めるにはドーソナイト単味で使用するよりも消石灰と併用するのが適当である。本発明の排ガス処理剤は消石灰粉末とドーソナイト粉末との混合粉末からなる。   Since the neutralization effect of the acid components in the exhaust gas of dosonite is about half that of slaked lime, it is appropriate to use it together with slaked lime rather than just using dosonite. The exhaust gas treating agent of the present invention comprises a mixed powder of slaked lime powder and dosonite powder.

本発明の排ガス処理剤に含まれるドーソナイト粉末の含有量は20%〜45%が好ましく、消石灰粉末の含有量は55%〜80%が好ましい。ドーソナイト含有量が20%より少ないとドーソナイトの効果が不十分になる。一方、ドーソナイト含有量が45%よりも多いと相対的に消石灰の含有量が少なくなるので排ガスの酸性成分に対する中和効果が低下し、このため排ガス処理剤の必要量が増加し、処理剤の費用が嵩むと共に埋立処分場に廃棄する処理物量が増加するので好ましくない。   The content of the dosonite powder contained in the exhaust gas treating agent of the present invention is preferably 20% to 45%, and the content of the slaked lime powder is preferably 55% to 80%. When the dosonite content is less than 20%, the effect of dosonite becomes insufficient. On the other hand, if the dosonite content is more than 45%, the content of slaked lime is relatively reduced, so the neutralization effect on the acidic components of the exhaust gas is reduced, and therefore the required amount of the exhaust gas treatment agent increases, This is not preferable because the cost increases and the amount of processed material to be discarded in the landfill site increases.

消石灰粉末およびドーソナイト粉末の比表面積は30m2/g以上が好ましく、消石灰粉末の比表面積は30〜50m2/g程度、ドーソナイト粉末の比表面積は60〜100m2/g程度がより好ましい。消石灰粉末およびドーソナイト粉末の比表面積が好ましい上記範囲よりも小さいと、排ガスに含まれる酸性成分および重金属類との接触が不十分になる虞がある。 The specific surface area of the slaked lime powder and dawsonite powder is preferably not less than 30 m 2 / g, the specific surface area of the slaked lime powder is 30 to 50 m 2 / g approximately, a specific surface area of dawsonite powder is more preferably about 60~100m 2 / g. When the specific surface areas of the slaked lime powder and the dawsonite powder are smaller than the above range, the contact with the acidic components and heavy metals contained in the exhaust gas may be insufficient.

本発明の排ガス処理剤に含まれるドーソナイトは、排ガスに含まれている酸性ガス成分を中和すると共に重金属類を不溶化する作用を有する。一方、従来の排ガス処理剤は消石灰粉末と共に水酸化アルミニウム、塩化アルミニウム、硫酸アルミニウム等のアルミニウム化合物を含むものが知られているが、これらのアルミニウム化合物は重金属類を固定化する作用を有するものの、排ガスの酸性成分を中和する作用を有さないか、もしくは極めて小さい。一方、ドーソナイトは重金属類の固定化作用と共に酸性成分の中和作用も併せて有するので、従来の処理剤に含まれるアルミニウム化合物とは異なり、少ない使用量でも優れた処理効果を発揮することができる。   The dosonite contained in the exhaust gas treating agent of the present invention has an effect of neutralizing the acidic gas component contained in the exhaust gas and insolubilizing heavy metals. On the other hand, conventional exhaust gas treating agents are known to contain aluminum compounds such as aluminum hydroxide, aluminum chloride, and aluminum sulfate together with slaked lime powder, although these aluminum compounds have the effect of immobilizing heavy metals, It has no or very little action to neutralize the acidic components of the exhaust gas. On the other hand, since dawsonite also has the effect of fixing heavy metals and neutralizing acidic components, unlike aluminum compounds contained in conventional treatment agents, it can exhibit excellent treatment effects even with a small amount of use. .

本発明の排ガス処理剤は、これを排ガスに添加して排ガスに含まれる酸性成分を中和すると共に重金属類を吸着させ、この処理剤を添加した排ガスを集塵機に通じて排ガス中の煤塵および処理剤を集塵し、集塵した粉体を加水混練して粘土状にする排ガス処理方法として好適に用いることができる。   The exhaust gas treatment agent of the present invention is added to the exhaust gas to neutralize acidic components contained in the exhaust gas and adsorb heavy metals, and the exhaust gas to which this treatment agent is added is passed through a dust collector to remove dust and treatment in the exhaust gas. It can be suitably used as an exhaust gas treatment method that collects an agent and hydrates and kneads the collected powder to form a clay.

本発明の排ガス処理剤は、排ガスに含まれる酸性成分に対する中和作用と重金属類に対する不溶化作用とを同時に有するので、排ガスへの投入が一度で済む。一方、消石灰粉末を添加した後に煤塵を集塵し、この集塵した煤塵に重金属処理剤と水を添加して混練する従来の処理システムでは、処理剤の添加を二段階に行っているが、本発明の処理剤を用いる処理システムでは処理剤の添加は一段階でよく、煤塵を集塵した後に処理剤を添加する工程を省略することができる。   Since the exhaust gas treating agent of the present invention has both a neutralizing action on acidic components contained in the exhaust gas and an insolubilizing action on heavy metals, it can be introduced into the exhaust gas only once. On the other hand, in the conventional processing system that collects dust after adding slaked lime powder, and kneads the collected dust by adding a heavy metal treatment agent and water, the treatment agent is added in two stages. In the treatment system using the treatment agent of the present invention, the treatment agent may be added in one step, and the step of adding the treatment agent after collecting the dust can be omitted.

本発明の排ガス処理システムは、具体的は、例えば、図1に示すように、焼却施設10の排ガス冷却部11の下流に、消石灰粉末とドーソナイト粉末との混合粉末からなる排ガス処理剤を排ガス中に添加する手段12と、排ガスに含まれるダストと排ガス処理剤とを捕集する集塵機13と、集塵した粉体を貯める貯槽14と、貯槽14から定量フィーダ19を通じて排出された煤塵を加水混練する手段15、給水手段17、排ガスを吸引するブロワ18を有するものであればよく、煤塵を集塵した後に重金属類に対する処理剤を添加する手段を設ける必要はない。なお、貯槽14は省略しても良い。浄化された排ガスは煙突16を通じて外部に排出される。   Specifically, for example, as shown in FIG. 1, the exhaust gas treatment system of the present invention contains an exhaust gas treatment agent comprising a mixed powder of slaked lime powder and dawsonite powder in the exhaust gas downstream of the exhaust gas cooling unit 11 of the incineration facility 10. Means 12 for adding to the dust, a dust collector 13 for collecting dust contained in the exhaust gas and the exhaust gas treating agent, a storage tank 14 for storing the collected powder, and the soot and dust discharged from the storage tank 14 through the quantitative feeder 19 It is only necessary to have a means 15 for supplying water, a water supply means 17 and a blower 18 for sucking exhaust gas, and it is not necessary to provide means for adding a treating agent for heavy metals after collecting dust. The storage tank 14 may be omitted. The purified exhaust gas is discharged outside through the chimney 16.

以下、本発明を実施例によって具体的に示し、実施例と共に比較例、参考例を示す。これら各例において使用した排ガス処理剤の成分を表1に示した。また、排ガス処理剤を使用した焼却施設の概要を表2に示した。   EXAMPLES Hereinafter, the present invention will be specifically described by examples, and comparative examples and reference examples will be shown together with examples. Table 1 shows the components of the exhaust gas treating agent used in each of these examples. Table 2 shows an overview of incineration facilities using exhaust gas treatment agents.

Figure 2008212923
Figure 2008212923

消石灰は比表面積39.5m2/gのものを用いた。水酸化アルミニウムは非結晶性であって比表面積90m2/gのものを用いた。ドーソナイトは比表面積79m2/gのものを用いた。平均粒径は、堀場製作所製レーザー回折式粒度分布測定装置(LA-920)を用いて測定した。かさ比重はホソカワミクロン製パウダーテスターを用いて測定した。 Slaked lime having a specific surface area of 39.5 m 2 / g was used. Aluminum hydroxide having an amorphous surface area with a specific surface area of 90 m 2 / g was used. Dorsonite having a specific surface area of 79 m 2 / g was used. The average particle size was measured using a laser diffraction particle size distribution measuring device (LA-920) manufactured by Horiba. The bulk specific gravity was measured using a powder tester made by Hosokawa Micron.

Figure 2008212923
Figure 2008212923

〔排ガス中和処理〕実施例1、比較例1〜3、参考例
施設Iの排ガス流路に、表1の処理剤(No1〜5)を導入して排ガスの中和処理試験を実施した。各処理剤は、図3に示す既設の消石灰供給配管において、消石灰定量供給機Aおよび消石灰移送ブロワーBと、集塵機の上流側に位置する消石灰供給口Cの間に、排ガス処理剤タンクDおよび定量供給フィーダEを設け、実施例の処理剤はタンクDから定量供給し、比較例の消石灰は供給機Aから定量供給した。試験方法は、焼却施設Iのごみ分別が進んでおり、ゴミピット内のゴミ攪拌が十分に実施されていることから、排ガス中に存在するHCl、SO2の酸性ガス濃度が極めて安定しているので、排ガス中のHClおよびSO2の運転管理基準値(HCl<30ppm、SO2<30ppm)を1週間連続して維持することができる処理剤の固定使用量(Xkg/hr)を求めた。この結果を表3に示した。
[Exhaust gas neutralization treatment] Example 1, Comparative Examples 1 to 3, Reference Example The treatment agent (Nos. 1 to 5) shown in Table 1 was introduced into the exhaust gas passage of the facility I, and the exhaust gas neutralization treatment test was conducted. Carried out. In the existing slaked lime supply pipe shown in FIG. 3, each treatment agent is disposed between the slaked lime quantitative supply machine A and the slaked lime transfer blower B and the slaked lime supply port C located upstream of the dust collector and the exhaust gas treatment agent tank D and the fixed quantity. A supply feeder E was provided, and the treatment agent of the example was quantitatively supplied from the tank D, and the slaked lime of the comparative example was quantitatively supplied from the feeder A. In the test method, the waste separation in the incineration facility I is progressing, and the waste gas in the waste pit is sufficiently stirred, so the acid gas concentrations of HCl and SO 2 present in the exhaust gas are extremely stable. The fixed amount (X kg / hr) of the treating agent that can maintain the operation control standard values of HCl and SO 2 in the exhaust gas (HCl <30 ppm, SO 2 <30 ppm) continuously for one week was determined. The results are shown in Table 3.

表3に示すように、本発明実施例1の処理剤必要量は比較例1〜2に比べてかなり低減されている。具体的には、排ガスの中和処理に必要な消石灰の量は、比較例1〜2および参考例1では34.7kg/hr〜35kg/hrであるが、実施例1ではドーソナイトが中和作用を有するので消石灰の使用量は少なく、29.6kg/hrで足り、消石灰量を約15%程度低減することができる。   As shown in Table 3, the necessary amount of the treating agent of Example 1 of the present invention is considerably reduced as compared with Comparative Examples 1 and 2. Specifically, the amount of slaked lime required for the neutralization treatment of the exhaust gas is 34.7 kg / hr to 35 kg / hr in Comparative Examples 1 and 2 and Reference Example 1, but in Example 1, dosonite is neutralized. Therefore, the amount of slaked lime used is small, 29.6 kg / hr is sufficient, and the amount of slaked lime can be reduced by about 15%.

なお、参考例1の排ガス処理剤量は少ないが、これは全量が消石灰であり、中和処理に必要な消石灰量は比較例1〜2とほぼ同量である。また、参考例1の処理剤は重金属安定化剤を含有しないので、次の重金属処理の結果(表4)に示すように、Pbの溶出量が格段に多く、重金属類を不溶化できない。このため、例えば参考例3に示すように、重金属類を不溶化するための薬剤処理等が別途必要になる。   In addition, although the amount of the exhaust gas treating agent of Reference Example 1 is small, the total amount is slaked lime, and the amount of slaked lime necessary for the neutralization treatment is almost the same as in Comparative Examples 1 and 2. Moreover, since the processing agent of Reference Example 1 does not contain a heavy metal stabilizer, as shown in the results of the following heavy metal processing (Table 4), the amount of Pb eluted is remarkably large and heavy metals cannot be insolubilized. For this reason, for example, as shown in Reference Example 3, a chemical treatment or the like for insolubilizing heavy metals is required separately.

Figure 2008212923
Figure 2008212923

〔重金属処理〕実施例2、比較例4〜6、参考例2〜3
上記排ガス中和処理を行った後に、集塵機で捕集した煤塵に一定量の水を加えて常法処理と同じ混練装置に導入し、参考例3を除いて従来の重金属処理剤を供給せずに水混練のみの処理を行った。これらの処理物について昭和48年環境庁告示13号試験を行い、Pb溶出量とpHを測定した。この結果を表4に示した。
[Heavy metal treatment] Example 2, Comparative Examples 4-6, Reference Examples 2-3
After performing the exhaust gas neutralization treatment, a certain amount of water is added to the dust collected by the dust collector and introduced into the same kneading apparatus as the conventional treatment, and the conventional heavy metal treatment agent is not supplied except in Reference Example 3. Only water kneading was performed. These treated products were subjected to Environmental Agency Notification No. 13 test in 1973, and the amount of Pb elution and pH were measured. The results are shown in Table 4.

表4に示すように、本発明の実施例2は、比較例4および比較例6と同程度にPbの溶出量が低減されている。一方、表3に示すように、比較例4(表3の比較例1)および比較例6(表3の比較例3)は排ガスの中和処理および煤塵の重金属安定化処理に必要な処理剤の使用量が格段に多く、従って、中和処理から重金属処理に至る一連の処理行う場合、実施例2の処理剤は比較例4(表3の比較例1)および比較例6(表3の比較例3)よりも少ない使用量で同程度の処理効果を達成している。また、表3の比較例2はドーソナイトに代えてほぼ同量の水酸化アルミニウムを含有しているが、表4の比較例5(表3の比較例2)に示すように、Pbの溶出量が多く、重金属類を十分に安定化することができない。   As shown in Table 4, in Example 2 of the present invention, the elution amount of Pb was reduced to the same extent as Comparative Example 4 and Comparative Example 6. On the other hand, as shown in Table 3, Comparative Example 4 (Comparative Example 1 in Table 3) and Comparative Example 6 (Comparative Example 3 in Table 3) are treatment agents necessary for exhaust gas neutralization treatment and dust heavy metal stabilization treatment. Therefore, when a series of treatments from neutralization treatment to heavy metal treatment is performed, the treating agent of Example 2 is Comparative Example 4 (Comparative Example 1 in Table 3) and Comparative Example 6 (Table 3). The same treatment effect is achieved with a smaller amount used than in Comparative Example 3). Further, Comparative Example 2 in Table 3 contains almost the same amount of aluminum hydroxide in place of dosonite. However, as shown in Comparative Example 5 in Table 4 (Comparative Example 2 in Table 3), the elution amount of Pb In many cases, heavy metals cannot be sufficiently stabilized.

Figure 2008212923
Figure 2008212923

〔排ガス中和処理〕実施例3〜5、比較例7〜8
焼却施設(II)において、表5に示す処理剤を施設(I)と同様に供給し、排ガスの中和処理を行った。処理剤の必要量は、排ガス中のHClおよびSO2の運転管理基準値(HCl<200ppm、SO2<35ppm)を1週間連続して維持することができる処理剤の固定使用量(Xkg/hr)として求めた。この結果を表5に示した。
[Exhaust gas neutralization treatment] Examples 3 to 5 and Comparative Examples 7 to 8
In the incineration facility (II), the treatment agents shown in Table 5 were supplied in the same manner as in the facility (I), and the exhaust gas was neutralized. The required amount of treating agent is the fixed amount of treating agent (X kg / hr) that can maintain the operation control standard values of HCl and SO 2 in exhaust gas (HCl <200 ppm, SO 2 <35 ppm) continuously for one week. ). The results are shown in Table 5.

表5に示すように、何れの処理剤も排ガスに含まれるHClおよびSO2の酸性ガス成分の濃度は十分に運転管理基準を下回っており、満足できる値であった。ただし、ドーソナイトの配合割合が増すのに伴い、排ガス処理剤の必要量が増加する傾向にあり、従って、表5のNo.23とNo.24とを考慮するとドーソナイト含有量は45%未満が好ましい。 As shown in Table 5, the concentration of the acidic gas components of HCl and SO 2 contained in the exhaust gas was sufficiently below the operation management standard for all the treatment agents and was satisfactory. However, as the blending ratio of dosonite increases, the required amount of exhaust gas treating agent tends to increase. Therefore, considering No. 23 and No. 24 in Table 5, the dosonite content is preferably less than 45%. .

Figure 2008212923
Figure 2008212923

〔重金属処理〕実施例3〜5、比較例7〜8
上記実施例3〜5、および上記比較例7〜8の排ガス中和処理の後に、集塵機で捕集した煤塵に一定量の水を加えて常法処理と同じ混練装置に導入し、従来の重金属処理剤を供給せずに水混練のみの処理を行った。これらの処理物について昭和48年環境庁告示13号試験を行い、Pb溶出量とpHを測定した。この結果を表6に示した。
[Heavy metal treatment] Examples 3 to 5 and Comparative Examples 7 to 8
After the exhaust gas neutralization treatment in Examples 3 to 5 and Comparative Examples 7 to 8, a certain amount of water was added to the dust collected by the dust collector and introduced into the same kneading apparatus as the conventional treatment, and the conventional heavy metal Only water kneading was performed without supplying the treatment agent. These treated products were subjected to Environmental Agency Notification No. 13 test in 1973, and the amount of Pb elution and pH were measured. The results are shown in Table 6.

表6に示すように、ドーソナイト含有量20%以上の試料No.26〜No.29 は何れもPbの溶出量が十分に小さく、埋立溶出基準を満たしている。例えば、試料No.26のPb溶出量は0.02mg/Lであり、埋立溶出基準0.3mg/Lの約1/10以下であり、十分に埋立基準を満たしている。一方、ドーソナイト含有量10%の試料No.25はPbの溶出量が5.6mg/Lと多く、埋立溶出基準を満たしていない。従って、表6の結果からドーソナイトの含有量は20%以上が適当であり、表5の結果を併せてみれば、ドーソナイトの含有量は20%〜45%が好ましいことが分かる。   As shown in Table 6, all of the samples No. 26 to No. 29 having a dosonite content of 20% or more have sufficiently small elution amounts of Pb and satisfy the landfill elution standard. For example, the Pb elution amount of sample No. 26 is 0.02 mg / L, which is about 1/10 or less of the landfill elution standard of 0.3 mg / L, which sufficiently satisfies the landfill standard. On the other hand, Sample No. 25 having a dosonite content of 10% has a large Pb elution amount of 5.6 mg / L and does not satisfy the landfill elution standard. Accordingly, the content of dosonite is suitably 20% or more from the results in Table 6, and when the results in Table 5 are taken together, it is understood that the content of dawsonite is preferably 20% to 45%.

Figure 2008212923
Figure 2008212923

本発明の排ガス処理システムを示す概略図。Schematic which shows the exhaust gas processing system of this invention. 従来の排ガス処理システムを示す概略図。Schematic which shows the conventional waste gas processing system. 試験において使用した排ガス処理システムを示す概略図。Schematic which shows the exhaust gas processing system used in the test.

符号の説明Explanation of symbols

10−焼却施設、11−排ガス冷却部、12−排ガス処理剤の添加手段、13−集塵機、14−貯槽14、15−加水混練手段、16−煙突、17−給水手段、18−ブロワ、19−定量フィーダ、20−焼却施設、21−排ガス流路、22−排ガス冷却部、23−アルカリ薬剤の投入部、24−集塵機、25−ブロワー、26−煙突、27−貯槽、29−定量フィーダ、30−混練装置、31−重金属処理剤添加手段、32−給水手段、33−ホッパ。A−消石灰供給機、B−ブロワ、C−処理剤供給口、D−処理剤タンク、E−定量フィーダ。 10-incineration facility, 11-exhaust gas cooling section, 12-exhaust gas treatment agent addition means, 13-dust collector, 14-storage tank 14, 15-hydrokneading means, 16-chimney, 17-water supply means, 18-blower, 19- Metering feeder, 20-incineration facility, 21-exhaust gas flow path, 22-exhaust gas cooling unit, 23-alkali chemical charging unit, 24-dust collector, 25-blower, 26-chimney, 27-storage tank, 29-quantitative feeder, 30 -Kneading device, 31-Heavy metal treatment agent addition means, 32-Water supply means, 33-Hopper. A-slaked lime feeder, B-blower, C-treatment agent supply port, D-treatment agent tank, E-quantitative feeder.

Claims (5)

消石灰粉末とドーソナイト粉末との混合粉末からなり、排ガス中の酸性成分を中和すると共に排ガス中の重金属を安定化することを特徴とする排ガス処理剤。
An exhaust gas treatment agent comprising a mixed powder of slaked lime powder and dawsonite powder, which neutralizes acidic components in exhaust gas and stabilizes heavy metals in exhaust gas.
混合粉末中に20%〜45%のドーソナイト粉末を含有する請求項1に記載する排ガス処理剤。
The exhaust gas treating agent according to claim 1, wherein the mixed powder contains 20% to 45% of dawsonite powder.
消石灰粉末およびドーソナイト粉末の比表面積が30m2/g以上である請求項1または請求項2に記載する排ガス処理剤。
The exhaust gas treating agent according to claim 1 or 2 , wherein the specific surface areas of the slaked lime powder and the dosonite powder are 30 m 2 / g or more.
請求項1〜請求項3の何れかに記載する排ガス処理剤を排ガスに添加して排ガスに含まれる酸性成分を中和すると共に重金属類を吸着させ、次いでこの排ガスを集塵機に通じて排ガス中の煤塵と排ガス処理剤とを集塵し、集塵した粉体を加水混練して粘土状にすることを特徴とする排ガスの処理方法。
The exhaust gas treating agent according to any one of claims 1 to 3 is added to the exhaust gas to neutralize acidic components contained in the exhaust gas and adsorb heavy metals, and then the exhaust gas is passed through a dust collector to A method for treating exhaust gas, comprising collecting dust and an exhaust gas treating agent, and hydromixing the collected powder to form a clay.
消石灰粉末とドーソナイト粉末との混合粉末からなる排ガス処理剤を排ガス中に添加する手段と、排ガスに含まれる煤塵と排ガス処理剤とを捕集する集塵機と、集塵した粉体を加水混練する手段とを有することを特徴とする排ガス処理システム。 Means for adding an exhaust gas treatment agent composed of a mixed powder of slaked lime powder and dosonite powder to the exhaust gas, a dust collector for collecting the soot and exhaust gas treatment agent contained in the exhaust gas, and means for hydro-kneading the collected powder An exhaust gas treatment system characterized by comprising:
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JP2011056495A (en) * 2009-08-11 2011-03-24 Kurita Water Ind Ltd Method for preventing elution of heavy metal

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JPS5610329A (en) * 1979-07-09 1981-02-02 Showa Tansan Kk Adsorbent containling dawsonite as main constituent
JPH10249148A (en) * 1996-12-24 1998-09-22 Ryoko Sekkai Kogyo Kk Exhaust gas treating agent and production thereof
JPH11128876A (en) * 1997-10-30 1999-05-18 Mitsubishi Materials Corp Treatment of incineration fly ash containing used waste gas treating agent
JP2000042360A (en) * 1998-05-22 2000-02-15 Icc:Kk Blowing agent for flue and its use method

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Publication number Priority date Publication date Assignee Title
JPS5610329A (en) * 1979-07-09 1981-02-02 Showa Tansan Kk Adsorbent containling dawsonite as main constituent
JPH10249148A (en) * 1996-12-24 1998-09-22 Ryoko Sekkai Kogyo Kk Exhaust gas treating agent and production thereof
JPH11128876A (en) * 1997-10-30 1999-05-18 Mitsubishi Materials Corp Treatment of incineration fly ash containing used waste gas treating agent
JP2000042360A (en) * 1998-05-22 2000-02-15 Icc:Kk Blowing agent for flue and its use method

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011056495A (en) * 2009-08-11 2011-03-24 Kurita Water Ind Ltd Method for preventing elution of heavy metal

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