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JP5534126B2 - Exhaust gas treatment method and exhaust gas treatment apparatus - Google Patents

Exhaust gas treatment method and exhaust gas treatment apparatus Download PDF

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JP5534126B2
JP5534126B2 JP2008067658A JP2008067658A JP5534126B2 JP 5534126 B2 JP5534126 B2 JP 5534126B2 JP 2008067658 A JP2008067658 A JP 2008067658A JP 2008067658 A JP2008067658 A JP 2008067658A JP 5534126 B2 JP5534126 B2 JP 5534126B2
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exhaust gas
dust
gas treatment
cod
aqueous solution
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JP2009220030A (en
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有夫 松本
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IHI Corp
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Description

本発明は、例えば、石炭などの化石燃料をボイラによって燃焼させる際にこのボイラから排出される排ガスを浄化するのに用いられる排ガス処理方法及び排ガス処理装置に関するものである。   The present invention relates to an exhaust gas treatment method and an exhaust gas treatment device used to purify exhaust gas discharged from a boiler when fossil fuel such as coal is burned by a boiler, for example.

上記した排ガスを浄化する排ガス処理方法としては、例えば、石炭焚きボイラから排出される石炭の燃焼排ガスを浄化する排ガス処理方法があり、この排ガス処理方法では、石炭焚きボイラから煙突に至るまでの煙道に配置された電気集塵機において、静電気によって排ガス中のばいじんの大半を除去した後、この電気集塵機の煙突側に配置された脱硫塔内において、石灰の水溶液を循環噴霧して気液接触させることにより、排ガス中のSOxを吸収するようにしている。   As the above-described exhaust gas treatment method for purifying exhaust gas, for example, there is an exhaust gas treatment method for purifying coal combustion exhaust gas discharged from a coal fired boiler. In this exhaust gas treatment method, smoke from a coal fired boiler to a chimney In the electrostatic precipitator placed on the road, after removing most of the dust in the exhaust gas by static electricity, in the desulfurization tower placed on the chimney side of this precipitator, the lime aqueous solution is circulated and brought into gas-liquid contact Thus, SOx in the exhaust gas is absorbed.

この排ガス処理方法において、脱硫塔で生成される反応物としての石膏は、スラリー状の溶液を固液分離させることで回収するようになっており、この際、分離した排水に含まれる有機性COD(石灰に含まれている有機性CODや水溶液の水分に含まれている「藻」などの有機性COD)は、活性炭吸着法を用いて処理するようになっている(例えば、特許文献1参照)。
特開平11-137958号公報
In this exhaust gas treatment method, gypsum as a reaction product generated in the desulfurization tower is recovered by solid-liquid separation of the slurry-like solution. At this time, the organic COD contained in the separated waste water is collected. (Organic COD contained in lime or organic COD such as “algae” contained in water of aqueous solution) is treated using an activated carbon adsorption method (see, for example, Patent Document 1). ).
Japanese Patent Laid-Open No. 11-137958

しかしながら、上記した排ガス処理方法では、スラリー状の溶液から反応物としての石膏を回収したあとの排水に含まれる有機性CODを活性炭吸着法により処理するようにしているが、排水に含まれる有機性CODは、活性炭に対する吸着性が極めて小さいことから、要求を満たすだけの量の有機性CODを吸着除去するためには、吸着設備を大型化する必要があり、その結果、排ガス処理コストの増大を招いてしまうという問題があり、この問題を解決することが従来の課題となっていた。   However, in the exhaust gas treatment method described above, organic COD contained in the wastewater after recovering gypsum as a reactant from the slurry solution is treated by the activated carbon adsorption method. Since COD has extremely low adsorptivity to activated carbon, it is necessary to enlarge the adsorption equipment in order to adsorb and remove organic COD in an amount sufficient to satisfy the requirements, resulting in an increase in exhaust gas treatment costs. There has been a problem of inviting, and it has been a conventional problem to solve this problem.

本発明は、上記した課題を解決するためになされたもので、排ガス処理コストの増大を伴うことなく、排ガスを処理する際に生じる排水中のCODを減らすことが可能である排ガス処理方法及び排ガス処理装置を提供することを目的としている。   The present invention has been made to solve the above-described problems, and an exhaust gas treatment method and exhaust gas that can reduce COD in wastewater generated when treating exhaust gas without increasing the exhaust gas treatment cost. An object is to provide a processing apparatus.

石炭などの化石燃料を燃焼させて生じる排ガスから、ばいじんやSOxを除去する排ガス処理装置の研究開発を行うにあたって、本発明者らは、これまでの石灰−石膏法による脱硫機能を具備した排ガス処理装置の各種データを収集して、詳細な検討を試みたところ、図3に示すデータに着目した。
この図3に示すデータは、排ガス中に含まれるSOxを除去する脱硫塔をばいじん分離式からばいじん混合式に改造した際に得たデータであり、図3のグラフの左側に示すばいじん分離式の脱硫塔の場合に、脱硫塔内における有機性CODの値が18mg/lであったものが、図3のグラフの右側に示すばいじん混合式の脱硫塔の場合には、2mg/lまで低減しており、本発明者らは、このデータから、ばいじんが有機性CODを吸着する能力を有していることを見出した。
In conducting research and development of an exhaust gas treatment device that removes dust and SOx from exhaust gas generated by burning fossil fuels such as coal, the present inventors have conducted exhaust gas treatment with a desulfurization function based on the lime-gypsum method so far. When various data of the apparatus was collected and detailed examination was attempted, the data shown in FIG. 3 was focused.
The data shown in FIG. 3 is data obtained when the desulfurization tower for removing SOx contained in the exhaust gas is remodeled from the soot separation type to the soot mixing type, and the soot separation type shown on the left side of the graph of FIG. In the case of the desulfurization tower, the organic COD value in the desulfurization tower was 18 mg / l, but in the case of the dust mixing type desulfurization tower shown on the right side of the graph of FIG. The present inventors have found from this data that the dust has the ability to adsorb organic COD.

ここで、上記有機性CODは、脱硫に用いる石灰などの吸収剤やこの吸収剤の水溶液の水分に含まれており、脱硫塔内に流入した有機性CODは、脱硫系内で分解したり、石膏などの反応物に混ざって脱硫系外に排出されたり、脱硫塔で生じる排水に含まれて脱硫系外に排出されたりする。
そこで、本発明者らは、有機性CODが排水に含まれて脱硫系外に排出されるのを阻止するべく、ばいじんが有機性CODを吸着する能力を有していることを利用して、本発明をするに至った。
Here, the organic COD is contained in an absorbent such as lime used for desulfurization and the water content of the aqueous solution of the absorbent, and the organic COD flowing into the desulfurization tower is decomposed in the desulfurization system, It is mixed with reactants such as gypsum and discharged outside the desulfurization system, or it is included in the wastewater generated in the desulfurization tower and discharged outside the desulfurization system.
Therefore, the present inventors utilize the fact that soot and dust have the ability to adsorb organic COD in order to prevent the organic COD from being contained in the waste water and discharged outside the desulfurization system, It came to make this invention.

発明の請求項に係る発明は、化石燃料を燃焼させることで生じる排ガス中に含まれるばいじんを取り除くばいじん除去工程及びアルカリ水溶液を前記排ガスに噴霧して該排ガス中に含まれるSOxを除去する脱硫工程を有する排ガス処理方法であって、前記脱硫工程において生じる排水の有機性CODの量を監視し、この有機性CODの量の監視結果を前記ばいじん除去工程に反映させて、このばいじん除去工程を経る排ガス中のばいじん濃度を制御したうえで、前記脱硫工程において、前記濃度のばいじんを含む排ガスに対してアルカリ水溶液を噴霧して、前記ばいじんによりアルカリ水溶液中の有機性CODを吸着除去する構成としたことを特徴としており、この排ガス処理方法の構成を前述した従来の課題を解決するための手段としている。 The invention according to claim 1 of the present invention removes SOx contained a dust removal step and an alkaline aqueous solution removes dust contained in the exhaust gas generated by burning fossil fuels in the exhaust gas by spraying into the exhaust gas An exhaust gas treatment method having a desulfurization step, wherein the amount of organic COD in waste water generated in the desulfurization step is monitored, and the monitoring result of the amount of organic COD is reflected in the dust removal step, and the dust removal step In the desulfurization step, the alkaline aqueous solution is sprayed on the exhaust gas containing the dust at the concentration , and the organic COD in the alkaline aqueous solution is adsorbed and removed by the dust. The configuration of this exhaust gas treatment method is characterized by the above-mentioned means for solving the above-mentioned conventional problems. To have.

た、本発明の請求項に係る排ガス処理方法は、前記脱硫工程において前記ばいじんを含んで生成される反応物の所定純度が得られない場合に、前記反応物からばいじんを分級する構成としている。 Also, an exhaust gas processing method according to claim 2 of the present invention, when a predetermined purity of the reactants that are generated contain the dust in the desulfurization step is not obtained, a configuration of classifying the dust from the reactant Yes.

一方、本発明の請求項に係る発明は、化石燃料を燃焼させることで生じる排ガス中に含まれるばいじんを取り除く集塵手段と、アルカリ水溶液を前記排ガスに噴霧して該排ガス中に含まれるSOxを除去する脱硫塔を備えた排ガス処理装置において、前記脱硫塔において生じる排水の有機性CODの量を測るCOD量測定手段を設けると共に、前記集塵手段による集塵量を制御する制御部を設け、前記制御部では、前記COD量測定手段からの測定結果に基づいて前記集塵手段を作動させて、該集塵手段を経る排ガス中のばいじん濃度を制御して、前記脱硫塔内における前記濃度のばいじんを含む排ガスに対するアルカリ水溶液の噴霧により、前記ばいじんでアルカリ水溶液中の有機性CODを吸着除去する構成としたことを特徴としており、この排ガス処理装置の構成を前述した従来の課題を解決するための手段としている。 On the other hand , the invention according to claim 3 of the present invention includes a dust collecting means for removing dust contained in the exhaust gas generated by burning fossil fuel, and SOx contained in the exhaust gas by spraying an alkaline aqueous solution onto the exhaust gas. In the exhaust gas treatment apparatus equipped with a desulfurization tower for removing water, a COD amount measuring means for measuring the amount of organic COD in the wastewater generated in the desulfurization tower is provided, and a control unit for controlling the dust collection amount by the dust collection means is provided. in the control unit, said actuates the measurement result the dust collection unit on the basis of from COD amount measuring means, to control the dust concentration in the exhaust gas passing through said dust collection means, the concentration of the desulfurization tower It is characterized in that the organic COD in the alkaline aqueous solution is adsorbed and removed by spraying the alkaline aqueous solution to the exhaust gas containing soot and dust. , And a means for solving the conventional problems described above the configuration of the exhaust gas treatment apparatus.

た、本発明の請求項に係るガス処理装置は、前記脱硫塔で前記ばいじんを含んで生成される反応物の純度を所定値に保つべく、前記反応物からばいじんを分級する分級手段を設けた構成としている。 Also, a gas processing device according to claim 4 of the present invention, in order maintain the purity of the reactants that are generated contain the dust in the desulfurization tower to a predetermined value, the classification means for classifying the dust from the reactant The configuration is provided.

発明の請求項に係る排ガス処理方法及び請求項に係る排ガス処理装置では、脱硫系内に流入した排ガスが所定量のばいじんを含んでいるので、この排ガスに対してアルカリ水溶液を噴霧すれば、ばいじんが有する有機性CODの吸着能力によりアルカリ水溶液中の有機性CODが吸着除去されることとなり、したがって、活性炭を用いていた従来と比べて、吸着設備を大型化する必要がない分だけ、排ガス処理コストの低減を実現することが可能であるという非常に優れた効果がもたらされる。 In the exhaust gas treatment apparatus according to the exhaust gas processing method and claim 3 according to claim 1 of the present invention, since the exhaust gas which has flowed into the desulfurization system contains a predetermined amount of dust, by spraying an alkaline aqueous solution with respect to the exhaust gas For example, the organic COD in the alkaline aqueous solution is adsorbed and removed by the organic COD adsorption capacity of the dust, and therefore, it is not necessary to increase the size of the adsorption facility as compared with the conventional method using activated carbon. In addition, it is possible to achieve a very excellent effect that it is possible to reduce the exhaust gas treatment cost.

また、本発明の請求項に係る排ガス処理方法及び請求項に係る排ガス処理装置では、アルカリ水溶液中の有機性CODを除去しつつ効率の良い排ガス処理を行うことができ、本発明の請求項に係る排ガス処理方法及び請求項に係る排ガス処理装置では、脱硫系においてばいじんを含んで生成される反応物の純度を所定値に維持することができる。 Further, in the air pollution control apparatus according to the exhaust gas processing method and claim 3 according to claim 1 of the present invention can perform efficient exhaust gas treatment while removing the organic COD in A alkaline aqueous solution, of the present invention in the exhaust gas treatment apparatus according to the exhaust gas processing method and claim 4 according to claim 2 can maintain the purity of the reactants that are generated contain dust in the de vulcanization system to a predetermined value.

以下、本発明の実施形態を図面に基づいて説明する。
図1は、本発明の一実施形態による排ガス処理装置を示しており、この実施形態では、本発明の排ガス処理方法及び排ガス処理装置を石炭焚きボイラから排出される排ガスの処理に適用した場合を例に挙げて説明する。
図1に示すように、この排ガス処理装置1は、石炭焚きボイラBから煙突2に至るまでの煙道Rに順次配置した熱交換器3,電気集塵機4,誘引通風機5及び脱硫塔6を備えて
おり、電気集塵機4では、静電気によって排ガス中のばいじんの大半を除去し、一方、脱硫塔6内では、石灰の水溶液を循環噴霧して気液接触させることにより、排ガス中のSOxを吸収するようになっている。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows an exhaust gas treatment apparatus according to an embodiment of the present invention. In this embodiment, the exhaust gas treatment method and the exhaust gas treatment apparatus of the present invention are applied to the treatment of exhaust gas discharged from a coal-fired boiler. An example will be described.
As shown in FIG. 1, the exhaust gas treatment apparatus 1 includes a heat exchanger 3, an electric dust collector 4, an induction ventilator 5, and a desulfurization tower 6 that are sequentially arranged in a flue R from a coal burning boiler B to a chimney 2. The electrostatic precipitator 4 removes most of the dust in the exhaust gas by static electricity, while the desulfurization tower 6 absorbs SOx in the exhaust gas by circulating and spraying an aqueous solution of lime and bringing it into gas-liquid contact. It is supposed to be.

この場合、脱硫塔6において生成される反応物としての石膏Sは、スラリー状の溶液を石膏脱水機7にかけて固液分離させることで回収するようになっており、この際、分離した排水はろ液ピット8を介して排水処理装置9側に送られるようになっている。
また、この排ガス処理装置1は、電気集塵機4による集塵量を制御する制御部10を有しており、この制御部10では、電気集塵機4を経る排ガス中に所定量のばいじんが残留するようにして電気集塵機4による集塵量を制御するようにしている。
In this case, gypsum S as a reaction product generated in the desulfurization tower 6 is recovered by subjecting the slurry-like solution to solid-liquid separation through a gypsum dehydrator 7, and the separated waste water is filtrated at this time. It is sent to the waste water treatment device 9 side through the pit 8.
Further, the exhaust gas treatment apparatus 1 has a control unit 10 that controls the amount of dust collected by the electric dust collector 4, and in this control unit 10, a predetermined amount of dust is left in the exhaust gas that passes through the electric dust collector 4. Thus, the amount of dust collected by the electric dust collector 4 is controlled.

つまり、制御部10によりコントロールした所定量のばいじんを含む排ガスを脱硫塔6内に敢えて流入させ、この脱硫塔6内において所定量のばいじんを含む排ガスに対して石灰の水溶液(アルカリ水溶液)を噴霧することで、ばいじんが有する有機性CODの吸着能力により、アルカリ水溶液に含まれる有機性CODを吸着除去するようになっている。
さらに、この実施形態では、排水に含まれる有機性CODの量を測るCOD量測定手段11をろ液ピット8に設けており、制御部10では、このCOD量測定手段11からの測定結果に基づいて、排水に含まれる有機性CODの量が多い場合には、排ガス中のばいじん濃度を高めるべく電気集塵機4を作動させ、排水に含まれる有機性CODの量が少ない場合には、排ガス中のばいじん濃度を下げるべく電気集塵機4を作動させて排ガス中のばいじん濃度を制御するようにしている。
That is, exhaust gas containing a predetermined amount of soot and dust controlled by the control unit 10 is intentionally flowed into the desulfurization tower 6, and an aqueous solution of lime (alkaline aqueous solution) is sprayed on the exhaust gas containing a predetermined amount of soot and dust in the desulfurization tower 6. Thus, the organic COD contained in the alkaline aqueous solution is adsorbed and removed by the organic COD adsorption capability of the dust.
Furthermore, in this embodiment, the COD amount measuring means 11 for measuring the amount of organic COD contained in the waste water is provided in the filtrate pit 8, and the control unit 10 is based on the measurement result from the COD amount measuring means 11. When the amount of organic COD contained in the wastewater is large, the electrostatic precipitator 4 is operated to increase the soot concentration in the exhaust gas, and when the amount of organic COD contained in the wastewater is small, In order to lower the soot concentration, the electrostatic precipitator 4 is operated to control the soot concentration in the exhaust gas.

このような構成を成す排ガス処理装置1では、脱硫塔6内に流入した排ガスが所定量のばいじんを含むように制御しているので、この排ガスに対してアルカリ水溶液を噴霧することで、ばいじんによりアルカリ水溶液中の有機性CODを吸着除去し得ることとなり、その結果、活性炭を用いていた従来と比べて、吸着設備を大型化する必要がない分だけ、排ガス処理コストの低減が図られることとなる。   In the exhaust gas treatment apparatus 1 having such a configuration, the exhaust gas flowing into the desulfurization tower 6 is controlled so as to contain a predetermined amount of soot. By spraying an alkaline aqueous solution on the exhaust gas, Organic COD in the alkaline aqueous solution can be adsorbed and removed. As a result, compared with the conventional method using activated carbon, the cost of exhaust gas treatment can be reduced by the amount not required to enlarge the adsorption equipment. Become.

また、上記した排ガス処理装置1では、排水に含まれる有機性CODの量を測るCOD量測定手段11をろ液ピット8に設けているので、アルカリ水溶液中の有機性CODを除去しつつ効率の良い排ガス処理を行い得ることとなる。
図2は、本発明の他の実施形態による排ガス処理装置を示しており、この実施形態においても、本発明の排ガス処理方法及び排ガス処理装置を石炭焚きボイラから排出される排ガスの処理に適用した場合を例に挙げて説明する。
Further, in the exhaust gas treatment apparatus 1 described above, since the COD amount measuring means 11 for measuring the amount of organic COD contained in the waste water is provided in the filtrate pit 8, it is efficient while removing the organic COD in the alkaline aqueous solution. A good exhaust gas treatment can be performed.
FIG. 2 shows an exhaust gas treatment apparatus according to another embodiment of the present invention. In this embodiment as well, the exhaust gas treatment method and the exhaust gas treatment apparatus of the present invention are applied to the treatment of exhaust gas discharged from a coal fired boiler. A case will be described as an example.

図2に示すように、この排ガス処理装置21が、先の実施形態による排ガス処理装置1と相違するところは、脱硫塔6でばいじんを含んで生成される石膏Sの純度を所定値に保つようにするために、脱硫塔6と石膏脱水機7との間に、石膏Sからばいじんを分級する分級手段22を設けた点にあり、他の構成は先の実施形態による排ガス処理装置1と同じである。   As shown in FIG. 2, this exhaust gas treatment device 21 is different from the exhaust gas treatment device 1 according to the previous embodiment in that the purity of gypsum S produced by containing debris in the desulfurization tower 6 is kept at a predetermined value. Therefore, a classifying means 22 for classifying the dust from the gypsum S is provided between the desulfurization tower 6 and the gypsum dewatering machine 7, and the other configuration is the same as that of the exhaust gas treatment apparatus 1 according to the previous embodiment. It is.

この実施形態による排ガス処理装置21では、石膏Sからばいじんを分級する分級手段22を設けているので、脱硫塔6で生成される石膏Sの純度を所定値に維持し得ることとなる。
上記した実施形態では、いずれも本発明の排ガス処理方法及び排ガス処理装置を石炭焚きボイラから排出される排ガスの処理に適用した場合を示したが、これに限定されるものではない。
In the exhaust gas treatment device 21 according to this embodiment, since the classification means 22 for classifying the dust from the gypsum S is provided, the purity of the gypsum S generated in the desulfurization tower 6 can be maintained at a predetermined value.
In each of the above-described embodiments, the exhaust gas treatment method and the exhaust gas treatment apparatus of the present invention are applied to the treatment of exhaust gas discharged from a coal fired boiler. However, the present invention is not limited to this.

本発明の一実施形態による排ガス処理装置を示す概略構成説明図である。BRIEF DESCRIPTION OF THE DRAWINGS It is schematic structure explanatory drawing which shows the waste gas processing apparatus by one Embodiment of this invention. 本発明の他の実施形態による排ガス処理装置を示す概略構成説明図である。It is schematic structure explanatory drawing which shows the exhaust gas processing apparatus by other embodiment of this invention. 排ガス中に含まれるSOxを除去する脱硫塔をばいじん分離式からばいじん混合式に改造した際に得たデータを示すグラフである。It is a graph which shows the data obtained when the desulfurization tower which removes SOx contained in exhaust gas was remodeled from the dust separation type to the dust mixing type.

符号の説明Explanation of symbols

1,21 排ガス処理装置
4 電気集塵機(集塵手段)
6 脱硫塔(洗浄塔)
10 制御部
11 COD量測定手段
22 分級手段
S 石膏(反応物)
1,21 Exhaust gas treatment equipment 4 Electric dust collector (dust collecting means)
6 Desulfurization tower (washing tower)
10 Control Unit 11 COD Measurement Unit 22 Classification Unit S Gypsum (Reactant)

Claims (4)

化石燃料を燃焼させることで生じる排ガス中に含まれるばいじんを取り除くばいじん除去工程及びアルカリ水溶液を前記排ガスに噴霧して該排ガス中に含まれるSOxを除去する脱硫工程を有する排ガス処理方法であって、
前記脱硫工程において生じる排水の有機性CODの量を監視し、この有機性CODの量の監視結果を前記ばいじん除去工程に反映させて、このばいじん除去工程を経る排ガス中のばいじん濃度を制御したうえで、前記脱硫工程において、前記濃度のばいじんを含む排ガスに対してアルカリ水溶液を噴霧して、前記ばいじんによりアルカリ水溶液中の有機性CODを吸着除去する
ことを特徴とする排ガス処理方法。
An exhaust gas treatment method comprising: a dust removal step for removing dust contained in exhaust gas generated by burning fossil fuel; and a desulfurization step for removing SOx contained in the exhaust gas by spraying an alkaline aqueous solution on the exhaust gas,
The amount of organic COD in the wastewater generated in the desulfurization process is monitored, the result of monitoring the amount of organic COD is reflected in the dust removal process, and the concentration of dust in the exhaust gas passing through the dust removal process is controlled. Then, in the desulfurization step, an alkaline aqueous solution is sprayed on the exhaust gas containing the concentration of dust, and organic COD in the alkaline solution is adsorbed and removed by the dust.
前記脱硫工程において前記ばいじんを含んで生成される反応物の所定純度が得られない場合に、前記反応物からばいじんを分級する請求項に記載の排ガス処理方法。 Wherein when a predetermined purity of the reactants that are generated contain the dust in the desulfurization step is not obtained, an exhaust gas treatment method according to claim 1 for classifying the dust from the reactant. 化石燃料を燃焼させることで生じる排ガス中に含まれるばいじんを取り除く集塵手段と、
アルカリ水溶液を前記排ガスに噴霧して該排ガス中に含まれるSOxを除去する脱硫塔を備えた排ガス処理装置において、
前記脱硫塔において生じる排水の有機性CODの量を測るCOD量測定手段を設けると共に、前記集塵手段による集塵量を制御する制御部を設け、
前記制御部では、前記COD量測定手段からの測定結果に基づいて前記集塵手段を作動させて、該集塵手段を経る排ガス中のばいじん濃度を制御して、前記脱硫塔内における前記濃度のばいじんを含む排ガスに対するアルカリ水溶液の噴霧により、前記ばいじんでアルカリ水溶液中の有機性CODを吸着除去する
ことを特徴とする排ガス処理装置。
Dust collecting means for removing dust contained in exhaust gas generated by burning fossil fuel ;
In the exhaust gas treatment apparatus provided with a desulfurization tower for spraying an alkaline aqueous solution onto the exhaust gas to remove SOx contained in the exhaust gas,
Provided with a COD amount measuring means for measuring the amount of organic COD of the wastewater generated in the desulfurization tower, and provided with a control unit for controlling the amount of dust collected by the dust collecting means,
Wherein the control unit, said on the basis of the measurement results from COD amount measuring means actuates said dust collection means controls the dust concentration in the exhaust gas passing through said dust collection means of the concentration in the desulfurization tower An exhaust gas treatment apparatus characterized in that organic COD in an alkaline aqueous solution is adsorbed and removed by spraying the alkaline aqueous solution on exhaust gas containing dust.
前記脱硫塔で前記ばいじんを含んで生成される反応物の純度を所定値に保つべく、前記反応物からばいじんを分級する分級手段を設けた請求項に記載の排ガス処理装置。 The exhaust gas treatment apparatus according to claim 3 , further comprising a classifying means for classifying the dust from the reactant so as to keep the purity of the reactant generated including the dust in the desulfurization tower at a predetermined value.
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Publication number Priority date Publication date Assignee Title
CN105345288A (en) * 2015-11-20 2016-02-24 天津二十冶建设有限公司 Power-driven chain block combination device for installing desulfurizing tower and installation method
CN113184932A (en) * 2021-04-26 2021-07-30 武汉天空蓝环保科技有限公司 Utilize flue gas evaporative concentration device and desulfurization effluent disposal system
CN113184932B (en) * 2021-04-26 2022-03-29 武汉天空蓝环保科技有限公司 Utilize flue gas evaporative concentration device and desulfurization effluent disposal system

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