JPH06277442A - Treatment of exhaust gas - Google Patents

Treatment of exhaust gas

Info

Publication number
JPH06277442A
JPH06277442A JP5069515A JP6951593A JPH06277442A JP H06277442 A JPH06277442 A JP H06277442A JP 5069515 A JP5069515 A JP 5069515A JP 6951593 A JP6951593 A JP 6951593A JP H06277442 A JPH06277442 A JP H06277442A
Authority
JP
Japan
Prior art keywords
exhaust gas
slurry
neutralizing agent
slaked lime
particle size
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.)
Granted
Application number
JP5069515A
Other languages
Japanese (ja)
Other versions
JP2718875B2 (en
Inventor
Katsuhiro Tokukura
勝浩 徳倉
Hideaki Muramatsu
英明 村松
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP5069515A priority Critical patent/JP2718875B2/en
Publication of JPH06277442A publication Critical patent/JPH06277442A/en
Application granted granted Critical
Publication of JP2718875B2 publication Critical patent/JP2718875B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To provide an exhaust gas treatment method capable of certainly treating exhaust gas with a small amt. of a neutralizing agent such as slaked lime, facilitating the maintenance of an apparatus and low in running cost. CONSTITUTION:In an exhaust gas treatment method wherein the exhaust gas discharged from a furnace is brought into contact with a slurry of a neutralizing agent such as slaked lime in a reactor, a grinding treatment part by ultrasonic irradiation is arranged to the passage of the slurry of the neutralizing agent from a neutralizing agent slurry tank to the reactor to finely grind the neutralizing agent.

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、ごみ焼却炉等から出た
酸性成分等を含有する排ガスを効率良く処理することが
できる排ガス処理方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas treatment method capable of efficiently treating exhaust gas containing an acidic component discharged from a refuse incinerator or the like.

【0002】[0002]

【従来の技術】ごみ焼却炉等の排ガス中には、硫黄酸化
物、塩化水素等の酸性成分が多量に含有されているた
め、反応器において消石灰等の中和剤スラリーと接触さ
せて硫酸塩や塩化物の粉体とし、これをバグフィルター
で分離したうえで大気中に放出するようにした排ガス処
理方法が知られている。ところが中和剤として例えば通
常市販されている工業用消石灰等を用いる場合、中和剤
の平均粒径が15〜30μm 程度と大きいために中和剤と排
ガス中の酸性成分との反応が粒子の表面付近でしか起こ
らず、中和剤の大部分は未反応のままダストとして排出
されてしまう。このためにモル比で酸性成分の2〜3倍
量の中和剤を投入する必要があった。また粒径が大きい
ために噴霧ノズルが詰まることが多く、管中輸送の際に
沈殿、閉塞を起こすことがあった。
Exhaust gas from refuse incinerators, etc. contains a large amount of acidic components such as sulfur oxides and hydrogen chloride. Therefore, it is necessary to bring the sulfates into contact with a neutralizing agent slurry such as slaked lime in the reactor. An exhaust gas treatment method is known in which powders of chlorides and chlorides are separated by a bag filter and then released into the atmosphere. However, when a commercially available industrial slaked lime or the like, which is usually commercially available, is used as the neutralizing agent, the reaction between the neutralizing agent and the acidic component in the exhaust gas is a particle because the average particle diameter of the neutralizing agent is as large as 15 to 30 μm. It occurs only near the surface, and most of the neutralizing agent is discharged as unreacted dust. For this reason, it was necessary to add a neutralizing agent in a molar ratio of 2 to 3 times that of the acidic component. Further, since the particle size is large, the spray nozzle is often clogged, which may cause precipitation and blockage during transportation in the pipe.

【0003】そこで本発明者等は、市販されている工業
用消石灰等の中和剤を何らかの方法を用いて微粒子化
し、比表面積を増大させることによって中和剤消費量の
減少、噴霧ノズルの詰まり防止や管中輸送の改善を図る
ことを試みた。しかし通常よく用いられるボールミルや
すりばち式等の機械式粉砕器を用いて消石灰等の中和剤
を粉砕し、これをスラリーにして噴霧する方法の場合に
は、次のような幾つかの問題点がある。 〔1〕粉砕時の消費エネルギーのうち実際に粉砕に使わ
れるのは5%以下であり、そのほとんどが摩擦熱となっ
てしまうためにエネルギー効率が悪く、従って粉砕のた
めに多くの動力費を要する。 〔2〕粉砕器の粉砕部の中和剤との摩擦による摩耗が激
しく、頻繁に粉砕部の交換等が必要になるなどメンテナ
ンスの手数がかかる。 〔3〕粉砕時に主に摩擦によって生ずる熱によるオーバ
ーヒート防止のため、粉砕器専用の冷却装置等が必要と
なる。 これらの諸問題から、機械式粉砕器の導入の場合、その
ランニングコストや初期設備投資が高くなるため、実用
化が困難であった。
Therefore, the present inventors reduced the consumption of the neutralizing agent and clogging of the spray nozzle by atomizing the commercially available neutralizing agent such as industrial slaked lime by using some method to increase the specific surface area. We tried to prevent and improve transportation in pipes. However, in the case of a method in which a neutralizing agent such as slaked lime is pulverized using a mechanical pulverizer such as a ball mill or a sandblast type that is usually used, and this is made into a slurry and sprayed, there are some problems as described below. There is. [1] Of the energy consumed during crushing, less than 5% is actually used for crushing, and most of it consumes frictional heat, resulting in poor energy efficiency. Therefore, much power is consumed for crushing. It costs. [2] The crushing part of the crusher is heavily worn due to friction with the neutralizing agent, which requires frequent replacement of the crushing part and other maintenance work. [3] A cooling device dedicated to the crusher is required to prevent overheating due to heat generated mainly by friction during crushing. Due to these various problems, in the case of introducing a mechanical crusher, its running cost and initial equipment investment are high, so that it is difficult to put it into practical use.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、少量の消石灰等の中和剤により排ガ
スを確実に処理することができ、しかも装置のメンテナ
ンスが容易でランニングコストも安価な排ガス処理方法
を提供するために完成されたものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems, and can reliably treat exhaust gas with a small amount of a neutralizing agent such as slaked lime, and the maintenance of the device is easy and the running cost is low. Was completed in order to provide an inexpensive exhaust gas treatment method.

【0005】[0005]

【課題を解決するための手段】上記の課題を解決するた
めになされた本発明は、炉から出た排ガスを消石灰等の
中和剤スラリーと接触させて排ガス中の酸性成分等を除
去する排ガス処理方法において、消石灰等の中和剤スラ
リーの流路に細管部を設け、該細管中に超音波発振子よ
り超音波を照射してスラリー中の中和剤粒子を平均粒径
5μm 以下に粉砕し、該スラリーを噴霧させて排ガス中
の酸性成分等を除去することを特徴とするものである。
The present invention made to solve the above problems is an exhaust gas for removing an acidic component in exhaust gas by contacting the exhaust gas from a furnace with a neutralizing agent slurry such as slaked lime. In the treatment method, a thin tube portion is provided in the flow path of the neutralizing agent slurry such as slaked lime, and the thin tube is irradiated with ultrasonic waves from an ultrasonic oscillator to pulverize the neutralizing agent particles in the slurry to an average particle size of 5 μm or less. Then, the slurry is sprayed to remove acidic components and the like in the exhaust gas.

【0006】[0006]

【作用】本発明によれば、消石灰等の中和剤スラリーの
流路に前段に示した方法を用いて超音波を照射すること
により中和剤を効率よく微粒化し、その比表面積を従来
の数倍に増加させることができる。これは中和剤スラリ
ーに10kHz 以上の超音波を照射するとスラリー中の中和
剤粒子が激しく振動されるため、粒子自身が自己崩壊を
起こし、粒子が微細粒化することを利用したものであ
る。このため、有効な超音波が効果的に中和剤粒子に照
射されることが重要である。従って超音波は10kHz 以上
が好ましい。これは10kHz 以下では効果的に中和剤粒子
を振動させることができず、有効な粉砕が困難であるか
らである。スラリー流路に設けた細管部はその内径が5
〜100mm であることが好ましく、特に5〜50mmであるこ
とが好ましい。これは5mm以下では中和剤粒子によって
細管部が目詰まりを起こすこと、超音波発振子と中和剤
粒子との距離が大きくなるとスラリー中において超音波
の減衰等が著しくなることなどによるものである。
According to the present invention, the neutralizing agent is efficiently atomized by irradiating the flow path of the neutralizing agent slurry such as slaked lime with ultrasonic waves by using the method shown in the preceding stage, and its specific surface area is It can be increased several times. This is because when neutralizer slurry is irradiated with ultrasonic waves of 10 kHz or more, the neutralizer particles in the slurry violently vibrate, causing the particles themselves to self-disintegrate, resulting in the atomization of the particles. . Therefore, it is important that effective ultrasonic waves are effectively applied to the neutralizer particles. Therefore, the ultrasonic wave is preferably 10 kHz or more. This is because the neutralizer particles cannot be effectively vibrated below 10 kHz, and effective pulverization is difficult. The inner diameter of the thin tube provided in the slurry channel is 5
It is preferably -100 mm, particularly preferably 5-50 mm. This is because when the thickness is 5 mm or less, the narrow tube portion is clogged with the neutralizing agent particles, and when the distance between the ultrasonic oscillator and the neutralizing agent particles becomes large, the attenuation of ultrasonic waves in the slurry becomes remarkable. is there.

【0007】本発明の手法を用いて平均粒径5μm以下
に微細粒化された中和剤のスラリーを炉から出た排ガス
と接触させれば酸性成分との反応性がよくなり、中和剤
の消費量を減少させながら酸性成分の除去率を向上でき
る。しかも微細粒化された中和剤スラリーは沈殿を生じ
にくいため管中輸送が容易になり、消石灰等の中和剤粒
子による配管の摩耗や噴霧ノズルの詰まりなども防止で
きるので、装置の運転に関しての信頼性は大幅に向上す
る。しかもボールミルやすりばち式等の機械式粉砕器を
用いる場合のように、予め粉砕した後にスラリーにして
噴霧しなくてはいけないといった複雑なプロセスを採る
必要がない。粉砕に必要なエネルギーの効率は8割以上
と高く、また発生する熱はスラリーを通じているために
常に自然冷却され、特別な冷却装置等は不要である。ま
た粉砕時に磨耗する部分がないため、特に交換を要する
ような部品がほとんど存在しない。これらの理由から本
発明は多くの利点を有し、本発明の導入によりメンテナ
ンスが容易になるうえ、ランニングコストや初期設備投
資も安価になるなどその効果は計り知れないものとな
る。
When the slurry of the neutralizing agent finely divided into particles having an average particle diameter of 5 μm or less by using the method of the present invention is brought into contact with the exhaust gas discharged from the furnace, the reactivity with the acidic component is improved and the neutralizing agent is improved. It is possible to improve the removal rate of acidic components while reducing the consumption amount of. Moreover, since the finely-divided neutralizing agent slurry is unlikely to precipitate, it can be easily transported in the pipe, and it is possible to prevent abrasion of the pipe and clogging of the spray nozzle due to neutralizing agent particles such as slaked lime. Reliability is greatly improved. Moreover, unlike the case of using a mechanical crusher such as a ball mill or a sandblast type, it is not necessary to employ a complicated process such as crushing in advance and then making a slurry. The efficiency of energy required for pulverization is as high as 80% or more, and the heat generated is always naturally cooled because it is through the slurry, and no special cooling device or the like is required. Moreover, since there are no parts to be worn during crushing, there are almost no parts that require replacement. For these reasons, the present invention has many advantages, and the introduction of the present invention makes maintenance easy, and the effects thereof are immeasurable such as running cost and initial capital investment being low.

【0008】[0008]

【実施例】以下に本発明を図示の実施例によって更に詳
細に説明する。図1は本発明の排ガス処理方法のフロー
シートであり、1はごみ焼却炉のような酸性成分を含有
する排ガスを排出する炉、2はこの炉1の排ガスを消石
灰等の中和剤スラリーと接触させるための反応器、3は
排ガス中の酸性成分が消石灰等の中和剤と反応して生じ
た硫酸塩や塩化物等の粉体を分離するためのバグフィル
ター、4は煙突である。また5は消石灰等の中和剤スラ
リータンク、6は消石灰等の中和剤スラリーの流路の途
中に設置された超音波による粉砕処理部である。本実施
例では超音波による粉砕処理部6に超音波粉砕器を用
い、中和剤として通常の排ガス処理で最もよく用いられ
る1〜10%の消石灰スラリーを用いた。
The present invention will be described below in more detail with reference to the illustrated embodiments. FIG. 1 is a flow sheet of the exhaust gas treatment method of the present invention, in which 1 is a furnace for discharging exhaust gas containing an acidic component such as a refuse incinerator, and 2 is exhaust gas of this furnace 1 with a neutralizing agent slurry such as slaked lime. A reactor 3 for contacting the bag, a bag filter 4 for separating powders such as sulfates and chlorides produced by reaction of an acidic component in exhaust gas with a neutralizing agent such as slaked lime, and 4 a chimney. Further, 5 is a tank for neutralizing agent slurry such as slaked lime, and 6 is a pulverization section by ultrasonic waves installed in the flow path of the slurry for neutralizing agent such as slaked lime. In this example, an ultrasonic pulverizer was used for the ultrasonic pulverization processing unit 6, and 1 to 10% of slaked lime slurry most often used in ordinary exhaust gas treatment was used as a neutralizing agent.

【0009】図2は本実施例で使用した超音波粉砕器の
粉砕部の構造図である。図2で示す通り、粉砕器はスラ
リー流路を10mmに絞った細管中に4mmの径の棒状超音波
発振子を取付け、その周囲を消石灰スラリーが流れる際
にスラリー中の消石灰粒子に20kHz の超音波を照射して
消石灰粒子を粉砕する方式であることなどを特徴とす
る。またボールミルやすりばち式等の機械式粉砕機を用
いる場合のように予め粉砕した後にスラリーにして噴霧
しなくてはいけないといった煩雑なプロセスを採る必要
がないこと、粉砕に必要なエネルギーの効率が非常に高
く、発生する熱はスラリーを通じているために常に自然
冷却されるので特別な冷却装置等は不要であることから
ランニングコストも安価になること、粉砕時に磨耗する
部分がないため特に交換を要するような部分があまり存
在しないことからメンテナンスが容易になることなど多
くの利点を有することを特徴とするものである。消石灰
は工業用第1号を用いた。
FIG. 2 is a structural diagram of the crushing section of the ultrasonic crusher used in this embodiment. As shown in Fig. 2, the pulverizer was equipped with a rod-shaped ultrasonic oscillator with a diameter of 4 mm in a thin tube with the slurry channel narrowed to 10 mm. It is characterized by a method of irradiating sound waves to crush slaked lime particles. In addition, it is not necessary to use a complicated process such as crushing in advance and then making it into a slurry, as in the case of using a mechanical crusher such as a ball mill or a drumstick type, and the efficiency of energy required for crushing is extremely high. Since the generated heat is always naturally cooled because it is through the slurry, no special cooling device etc. is required, so the running cost is low, and there is no part to be worn during crushing, so it seems that replacement is especially required. It is characterized in that it has many advantages such as easy maintenance because there are not many parts. As the slaked lime, the first industrial grade was used.

【0010】図3は市販の工業用消石灰の粒度分布を示
すもので、その平均粒径は約18μm、比表面積は6000cm2
/cm3 である。これに対して、図4は超音波粉砕器6を
通過した後の消石灰スラリー中の消石灰粒子の粒度分布
を示すもので、平均粒径は3μm 、比表面積は30000cm2
/cm3である。このように超音波を照射することによって
平均粒径が約1/6 に微細粒化され、また比表面積も粉砕
前の約6倍に増加している。
FIG. 3 shows the particle size distribution of commercial industrial slaked lime, the average particle size of which is about 18 μm and the specific surface area is 6000 cm 2.
/ cm 3 . On the other hand, FIG. 4 shows the particle size distribution of the slaked lime particles in the slaked lime slurry after passing through the ultrasonic crusher 6, having an average particle size of 3 μm and a specific surface area of 30,000 cm 2.
/ cm 3 . By irradiating with ultrasonic waves in this way, the average particle size was reduced to about 1/6 and the specific surface area was increased to about 6 times that before pulverization.

【0011】図5は横軸にスラリー中の消石灰粒子の粒
径を取り、縦軸に塩化水素及び硫黄酸化物の除去率を取
ったグラフである。初期平均粒径18μm の市販品をその
ままスラリーとして使用した場合、その除去率がそれぞ
れ80%、70%であるのに対し、本発明により平均粒径を
3μm にまで微細粒化したスラリーを用いた場合、それ
らの除去率をそれぞれ90%と、約10〜20%程度向上させ
ることが可能なことがわかる。
FIG. 5 is a graph in which the horizontal axis represents the particle size of slaked lime particles in the slurry and the vertical axis represents the removal rate of hydrogen chloride and sulfur oxides. When a commercially available product having an initial average particle size of 18 μm is used as it is as a slurry, the removal rates are 80% and 70%, respectively, while the slurry according to the present invention, which has been made into fine particles with an average particle size of 3 μm, was used. In this case, it can be seen that their removal rates can be improved to 90% and about 10 to 20%, respectively.

【0012】また図6は一定の除去率(対HCl 80%、対
SOX 70%) を達成するために必要とされる消石灰のモル
比を縦軸に取って示したグラフである。初期平均粒径18
μmの市販品をそのままスラリーとして使用した場合、
約3モル比を要するのに対し、本発明により平均粒径3
μm にまで微細粒化したスラリーを用いた場合、必要な
モル比は1.5 と従来の半分にまで減少できることがわか
る。このように超音波粉砕器6によって5μm 以下に微
粉化された消石灰スラリーは反応器2において排ガス中
の酸性成分と接触するが、その比表面積が増大されてい
るために反応性が高く、消費量が少量でありながら酸性
成分の除去率を向上させることができる。
Further, FIG. 6 shows a constant removal rate (vs. HCl 80%, v
2 is a graph showing the molar ratio of slaked lime required to achieve SO X 70%) on the vertical axis. Initial average particle size 18
When using a commercially available product of μm as it is,
According to the invention, an average particle size of 3
It can be seen that the required molar ratio can be reduced to 1.5, which is half that of the conventional case, when using a slurry with fine particles down to μm. Thus, the slaked lime slurry finely pulverized to 5 μm or less by the ultrasonic pulverizer 6 comes into contact with the acidic component in the exhaust gas in the reactor 2, but the specific surface area of the slaked lime slurry is increased, so that the reactivity is high and the consumption amount is high. Although the amount is small, the removal rate of acidic components can be improved.

【0013】[0013]

【発明の効果】以上に説明したように、本発明の排ガス
処理方法は消石灰等の中和剤スラリーの流路に超音波を
照射して中和剤粒子の粉砕を行い、微粉化された中和剤
スラリーを排ガスと接触させるようにしたので、従来よ
りも少量の中和剤により従来よりも高い酸性成分の除去
率を達成することができる。また本発明の排ガス処理方
法はメンテナンスが容易でランニングコストも安価であ
るという利点もある。よって本発明は従来の問題点を解
決した排ガス処理方法として、産業の発展に寄与すると
ころはきわめて大きいものである。
As described above, in the exhaust gas treatment method of the present invention, the flow path of the neutralizing agent slurry such as slaked lime is irradiated with ultrasonic waves to pulverize the neutralizing agent particles to obtain a fine powder. Since the additive slurry is brought into contact with the exhaust gas, it is possible to achieve a higher removal rate of acidic components than before with a smaller amount of neutralizing agent than before. Further, the exhaust gas treatment method of the present invention has the advantages that maintenance is easy and the running cost is low. Therefore, the present invention contributes greatly to industrial development as an exhaust gas treatment method that solves the conventional problems.

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

【図1】本発明の実施例のフローシートである。FIG. 1 is a flow sheet of an example of the present invention.

【図2】本発明の実施例で用いた超音波粉砕器の構造を
示す断面図である。
FIG. 2 is a cross-sectional view showing the structure of an ultrasonic crusher used in an example of the present invention.

【図3】市販の工業用消石灰をスラリーにした場合の消
石灰粒子の粒度分布を示すグラフである。
FIG. 3 is a graph showing a particle size distribution of slaked lime particles when a commercially available industrial slaked lime is made into a slurry.

【図4】市販の工業用消石灰をスラリーにして、これに
超音波を照射した後の消石灰粒子の粒度分布を示すグラ
フである。
FIG. 4 is a graph showing a particle size distribution of slaked lime particles obtained by making commercially available slaked lime into slurry and irradiating it with ultrasonic waves.

【図5】スラリー中の消石灰平均粒度と排ガス中の塩化
水素及び硫黄酸化物の除去率との関係を示すグラフであ
る。
FIG. 5 is a graph showing the relationship between the average particle size of slaked lime in the slurry and the removal rates of hydrogen chloride and sulfur oxides in the exhaust gas.

【図6】スラリー中の消石灰平均粒度と達成除去率に対
する必要モル比との関係を示すグラフである。
FIG. 6 is a graph showing the relationship between the average particle size of slaked lime in the slurry and the required molar ratio for the achieved removal rate.

【符号の説明】[Explanation of symbols]

1 ごみ焼却炉のような酸性成分を含有する排ガスを排
出する炉 2 炉の排ガスを消石灰等の中和剤スラリーと接触させ
るための反応器 3 排ガス中の酸性成分が消石灰等の中和剤と反応して
生じた硫酸塩や塩化物等の粉体を分離するためのバグフ
ィルター 4 煙突 5 消石灰等のスラリータンク 6 消石灰等の中和剤スラリーの流路の途中に設置され
た超音波による粉砕処理部
1 Reactor for discharging exhaust gas containing acidic components such as refuse incinerators 2 Reactor for contacting exhaust gas of furnace with neutralizing agent slurry such as slaked lime 3 Neutralizer such as slaked lime for acidic components in exhaust gas Bag filter for separating powders such as sulfates and chlorides generated by reaction 4 Chimney 5 Slurry tank of slaked lime etc. 6 Neutralizing agent such as slaked lime Smashing by ultrasonic wave installed in the flow path Processing unit

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 炉から出た排ガスを消石灰等の中和剤ス
ラリーと接触させて排ガス中の酸性成分等を除去する排
ガス処理方法において、消石灰等の中和剤スラリーの流
路に細管部を設け、該細管中に超音波発振子より超音波
を照射してスラリー中の中和剤粒子を平均粒径5μm 以
下に粉砕し、該スラリーを噴霧させて排ガス中の酸性成
分等を除去することを特徴とする排ガス処理方法。
1. A method for treating an exhaust gas in which an exhaust gas discharged from a furnace is brought into contact with a neutralizing agent slurry such as slaked lime to remove acidic components and the like in the exhaust gas, a thin tube portion is provided in a channel of the neutralizing agent slurry such as slaked lime. To irradiate ultrasonic waves from an ultrasonic oscillator into the narrow tube to pulverize the neutralizing agent particles in the slurry to an average particle size of 5 μm or less, and spray the slurry to remove acidic components in exhaust gas. An exhaust gas treatment method characterized by:
【請求項2】 炉から出た排ガスを消石灰等の中和剤ス
ラリーと接触させて排ガス中の酸性成分等を除去する排
ガス処理方法において、消石灰等の中和剤スラリーの流
路に5〜100mm の細管部を設け、該細管中に設けた超音
波発振子より10kHz 以上の超音波を照射してスラリー中
の中和剤粒子を平均粒径5μm 以下に粉砕し、該スラリ
ーを噴霧させて排ガス中の酸性成分等を除去することを
特徴とする排ガス処理方法。
2. A method for treating an exhaust gas, wherein an exhaust gas discharged from a furnace is brought into contact with a neutralizing agent slurry such as slaked lime to remove acidic components and the like in the exhaust gas. The ultrasonic wave oscillator provided in the thin tube irradiates ultrasonic waves of 10 kHz or more to pulverize the neutralizing agent particles in the slurry to an average particle size of 5 μm or less, and atomize the slurry to produce exhaust gas. An exhaust gas treatment method characterized by removing acidic components and the like therein.
JP5069515A 1993-03-29 1993-03-29 Exhaust gas treatment method Expired - Lifetime JP2718875B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5069515A JP2718875B2 (en) 1993-03-29 1993-03-29 Exhaust gas treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5069515A JP2718875B2 (en) 1993-03-29 1993-03-29 Exhaust gas treatment method

Publications (2)

Publication Number Publication Date
JPH06277442A true JPH06277442A (en) 1994-10-04
JP2718875B2 JP2718875B2 (en) 1998-02-25

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6616815B2 (en) 1998-06-22 2003-09-09 Canon Kabushiki Kaisha Method of decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds and apparatus to be used for the same as well as method of clarifying exhaust gas and apparatus to be used for the same
KR101478968B1 (en) * 2013-05-01 2015-01-05 주식회사 휴비스 Method of Preparing Meta-Aramid Fibers with Improved Whiteness and m-aramid Fibers thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4859446A (en) * 1971-11-29 1973-08-21
JPS4959446A (en) * 1972-10-11 1974-06-10
JPS54103776A (en) * 1978-02-02 1979-08-15 Hitachi Plant Eng & Constr Co Ltd Urban trash incinerator waste gas treatment

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4859446A (en) * 1971-11-29 1973-08-21
JPS4959446A (en) * 1972-10-11 1974-06-10
JPS54103776A (en) * 1978-02-02 1979-08-15 Hitachi Plant Eng & Constr Co Ltd Urban trash incinerator waste gas treatment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6616815B2 (en) 1998-06-22 2003-09-09 Canon Kabushiki Kaisha Method of decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds and apparatus to be used for the same as well as method of clarifying exhaust gas and apparatus to be used for the same
KR101478968B1 (en) * 2013-05-01 2015-01-05 주식회사 휴비스 Method of Preparing Meta-Aramid Fibers with Improved Whiteness and m-aramid Fibers thereof

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