JPH0647065B2 - Desulfurization and denitration equipment using corona discharge - Google Patents

Desulfurization and denitration equipment using corona discharge

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Publication number
JPH0647065B2
JPH0647065B2 JP2314660A JP31466090A JPH0647065B2 JP H0647065 B2 JPH0647065 B2 JP H0647065B2 JP 2314660 A JP2314660 A JP 2314660A JP 31466090 A JP31466090 A JP 31466090A JP H0647065 B2 JPH0647065 B2 JP H0647065B2
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JP
Japan
Prior art keywords
electrode
needle
desulfurization
denitration
discharge
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.)
Expired - Lifetime
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JP2314660A
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Japanese (ja)
Other versions
JPH04187214A (en
Inventor
康弘 春日
健 加藤
和夫 恩田
Original Assignee
工業技術院長
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Priority to JP2314660A priority Critical patent/JPH0647065B2/en
Publication of JPH04187214A publication Critical patent/JPH04187214A/en
Publication of JPH0647065B2 publication Critical patent/JPH0647065B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) この発明は、針状のコロナ高圧放電電極を用いた脱硫・
脱硝装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention is directed to desulfurization using a needle-shaped corona high-voltage discharge electrode.
Denitration equipment

(従来の技術) 近年、地球規模での環境保護が大きな問題となってお
り、したがってその汚染原因物質である窒素酸化物、硫
黄酸化物を効率的、且つ経済的に除去する脱硫・脱硝技
術の開発は益々国際的な重要な課題となっている。
(Prior Art) In recent years, environmental protection on a global scale has become a big problem, and therefore, a desulfurization / denitration technology that efficiently and economically removes nitrogen oxides and sulfur oxides that are the pollutants thereof Development is becoming an increasingly important international issue.

従来脱硫については、湿式の石灰石−石膏法が実用化さ
れ、燃料中から直接硫黄分を除去する直接脱硫法も開発
されている。
For desulfurization, a wet limestone-gypsum method has been put into practical use, and a direct desulfurization method for directly removing sulfur from fuel has also been developed.

また脱硝法としてはアンモニアによる選択接触還元法が
実用化されている。しかし、上記方法は何れも脱硫、脱
硝の装置を独立して設置する必要があり、脱硫・脱硝を
同時に効率よく、経済的に行なうことはできない。
As the denitration method, a selective catalytic reduction method using ammonia has been put into practical use. However, in any of the above methods, it is necessary to install a desulfurization and denitration device independently, and desulfurization and denitration cannot be performed efficiently and economically at the same time.

これに対して、脱硫・脱硝を同時に行なう方式として電
子ビーム照射や、パルスコロナ放電による同時脱硫・脱
硝の研究が100℃程度の排ガスを対象として進められて
いる。これらの方式は何れも電子ビームやコロナ放電に
よる励起電子によって燃焼排ガスからO,OH,HO2等の活性
度の高い酸化ラジカルを発生させ、その酸化ラジカルに
よってNOxやSOxを硝酸や硫酸に酸化させ、更にアルカリ
物質[NH3やCa(OH)2等]で中和し、硫酸アンモニムや硝
酸アンモニウム等の有用な粉体肥料として回収するもの
である。
On the other hand, research on simultaneous electron beam irradiation and simultaneous desulfurization / denitration by pulse corona discharge as a method of simultaneously performing desulfurization / denitration is under way for exhaust gas at about 100 ° C. All of these methods generate highly active oxidizing radicals such as O, OH, and HO 2 from flue gas by excited electrons by electron beam or corona discharge, and NO x and SO x are converted to nitric acid and sulfuric acid by the oxidizing radicals. It is oxidized and further neutralized with alkaline substances [NH 3 and Ca (OH) 2 etc.] and recovered as useful powdered fertilizers such as ammonium sulfate and ammonium nitrate.

(発明が解決しようとする問題点) しかし、上述の電子ビーム照射や、パルスコロナ放電に
よる同時脱硫・脱硝法では、直流コロナ放電による電力
の増加に伴って窒素酸化物と硫黄酸化物は減少するので
あるが、従来この方法で電極として使用されてきた棒状
電極を用いて大気圧下で印加電圧を増大させると、ある
点でコロナ放電はアーク放電に転移し、コロナ放電はこ
れ以上増大せず、反対に転移したアーク放電が燃焼ガス
を局所的に加熱し、窒素酸化物を却って激増させる結果
となる。そのため、脱硫・脱硝性能を高めるためには、
アーク放電に至ることなくコロナ放電入力を増大させる
必要がある。
(Problems to be solved by the invention) However, in the above-mentioned electron beam irradiation and the simultaneous desulfurization / denitration method by pulsed corona discharge, the amount of nitrogen oxides and sulfur oxides decreases with the increase in power due to DC corona discharge. However, when the applied voltage is increased under atmospheric pressure using a rod-shaped electrode that has been conventionally used as an electrode in this method, at some point the corona discharge transitions to arc discharge, and corona discharge does not increase any further. On the contrary, the transferred arc discharge locally heats the combustion gas, resulting in a drastic increase of nitrogen oxides. Therefore, in order to improve desulfurization / denitration performance,
It is necessary to increase the corona discharge input without reaching the arc discharge.

本願発明者らは以上の問題を解決するため、使用する電
極の形状について鋭意研究の結果、針状電極を使用する
と、同一電圧で棒状電極より多い電流、即ち電力が得ら
れ、脱硫・脱硝にとって有益なコロナ放電入力が高く取
れることを見出した。
In order to solve the above problems, the inventors of the present invention have earnestly studied the shape of the electrode to be used, and as a result, when a needle-shaped electrode is used, more current, that is, electric power, can be obtained at the same voltage than that of a rod-shaped electrode. It was found that the useful corona discharge input can be high.

(問題点を解決するための手段) この発明は、上記知見に基づいて脱硫・脱硝しようとす
る排ガスの、導入ダクトを兼ねた外周接地電極と、該外
周接地電極内に設置された針状電極とから構成された脱
硫・脱硝装置を提案するものである。
(Means for Solving Problems) The present invention is based on the above findings, and an outer peripheral ground electrode also serving as an introduction duct of exhaust gas to be desulfurized and denitrated, and a needle electrode installed in the outer peripheral ground electrode. It proposes a desulfurization / denitration device composed of and.

なお、針状電極としては構造電極の側面から複数の針電
極を所定の方向に延設して構成されるものを使用するこ
とができる。
As the needle-shaped electrode, an electrode configured by extending a plurality of needle electrodes in a predetermined direction from the side surface of the structural electrode can be used.

(作用) 以上のように、この発明に係る脱硫・脱硝装置は排ガス
の、導入ダクトを兼ねた外周接地電極内に針状電極を設
置して構成されるのであるが、このように針状電極を使
用することにより従来使用されていた針状電極よりも脱
硫・脱硝にとって有益なコロナ放電電力を高く取ること
ができる。
(Operation) As described above, the desulfurization / denitration apparatus according to the present invention is configured by installing the needle electrode in the outer peripheral ground electrode of the exhaust gas, which also serves as the introduction duct. By using, the corona discharge power useful for desulfurization and denitration can be higher than that of the conventionally used needle electrode.

また、外周接地電極の形状に応じて針状電極の形状を自
由に選択することができる。
Further, the shape of the needle-shaped electrode can be freely selected according to the shape of the outer peripheral ground electrode.

更に、針状電極は構造電極の側面から複数の針電極を所
定の方向に延設して簡単な構造のものを使用することが
でき、このため容易に製造でき、また可動部分を持たな
いため、操作上不都合を生ずることがない。
Further, the needle-shaped electrode can be of a simple structure in which a plurality of needle electrodes are extended in a predetermined direction from the side surface of the structural electrode, and therefore can be easily manufactured and has no moving parts. There is no inconvenience in operation.

(実施例) 以下、この発明を図示の実施例に基づいて詳細に説明す
る。
(Example) Hereinafter, the present invention will be described in detail based on an illustrated example.

1は、この発明に使用する針状電極を示す。針状電極1
はこの実施例ではその先端に電流導入端子穴2を有する
4角柱の構造電極3の側面から適当な太さと長さの複数
の針電極4を二方向乃至四方向に延設して構成される。
Reference numeral 1 shows a needle-shaped electrode used in the present invention. Needle electrode 1
In this embodiment, a plurality of needle electrodes 4 each having an appropriate thickness and length are arranged in two or four directions from the side surface of a quadrangular prismatic structure electrode 3 having a current introduction terminal hole 2 at its tip. .

ここで、構造電極3は適当な分布で複数の針電極4を支
持し、且つこれら針電極4に電流を導入する役割を果た
すものであり、また針電極4を構成する針は、この実施
例ではその太さが直径1mmφで、長さが対向接地電極と
の距離などとの兼ね合いから放電入力が最大になるよう
に電極間距離が20mmとし、更に針電極4の間隔を30mm程
度としてあるが、勿論これに限定されるものではなく針
電極4の長さ及び形状、太さ、針電極4の間隔等につい
ては処理ガスの種類等に応じて自由に選択することがで
き、例えば針状電極1としては曲線、折線形状のものを
使用することができ、また強度上問題がなければより細
い針電極を使用することができる。
Here, the structure electrode 3 plays a role of supporting the plurality of needle electrodes 4 in an appropriate distribution and introducing a current into these needle electrodes 4, and the needles forming the needle electrodes 4 are The diameter is 1 mmφ, and the length is 20 mm so that the discharge input is maximized in consideration of the distance from the opposing ground electrode, and the distance between the needle electrodes 4 is about 30 mm. Needless to say, the present invention is not limited to this, and the length and shape of the needle electrode 4, the thickness, the interval between the needle electrodes 4 and the like can be freely selected according to the type of processing gas. A curved line or a polygonal line can be used as 1, and a finer needle electrode can be used if there is no problem in strength.

なお、構造電極3の側面には針状電極1を対向接地電極
に絶縁物の支持具6を挿入する電極支持用穴5が設けら
れているが、電流導入端子穴2を電極支持用穴5に併用
する場合には電極支持用穴5は特別に必要ない。
It should be noted that an electrode supporting hole 5 for inserting the needle-shaped electrode 1 into the opposing ground electrode and the supporting member 6 for the insulator is provided on the side surface of the structural electrode 3, but the current introducing terminal hole 2 is provided in the electrode supporting hole 5. When used in combination, the electrode supporting hole 5 is not particularly required.

第2図は、上述の針状電極1を、外部にコロナ放電用の
高圧電源7を備えた両端を開放した四角柱形状のダクト
兼用対向接地電極8内に設置して構成されたこの発明に
係る脱硫・脱硝装置の一例を示すものであるが、これよ
り明らかなように針状電極1のリード線は絶縁物の支持
具6を介して針状電極1のリード線を対向接地電極8外
に取り出し、高圧電源7と接続され、また燃焼排ガスは
矢印方向9から対向接地電極8内に導入される。
FIG. 2 shows the present invention constructed by installing the above-mentioned needle-shaped electrode 1 in a square pole-shaped duct / opposite grounding electrode 8 which is provided with a high voltage power source 7 for corona discharge outside and which has both ends open. An example of such a desulfurization / denitration apparatus is shown. As is clear from this, the lead wire of the needle-shaped electrode 1 is connected to the opposite ground electrode 8 via the support 6 of the insulator. Is connected to the high-voltage power supply 7, and the combustion exhaust gas is introduced into the counter ground electrode 8 from the direction of arrow 9.

なお、対向接地電極8はこの実施例では両端を開放した
四角柱形状であるが、これに限定されるものでなく例え
ば第3図に示すように両端を開放した円筒形状のダクト
兼用対向接地電極8内に針状電極1を設置するようにし
てもよい。
In this embodiment, the counter ground electrode 8 is in the shape of a quadrangular prism whose both ends are open. However, the present invention is not limited to this. For example, as shown in FIG. You may make it arrange | position the needle-shaped electrode 1 in 8.

第4図は、バーナ10、ボイラー11からなる燃焼装置の冷
却部にこの発明に係る脱硫・脱硝装置12を設置した例を
示すものであるが、この実施例ではボイラー11の低温部
に脱硫・脱硝装置12を配置し、脱硫・脱硝装置12で生成
された粉体肥料を電気集塵器13で取り除いた後、煙突14
より排出するようにしてある。
FIG. 4 shows an example in which the desulfurization / denitration device 12 according to the present invention is installed in the cooling part of the combustion device including the burner 10 and the boiler 11. In this embodiment, desulfurization / denitration is performed in the low temperature part of the boiler 11. After the denitration device 12 is installed and the powder fertilizer produced by the desulfurization / denitration device 12 is removed by the electrostatic precipitator 13, the stack 14
I try to discharge more.

なお、第2、第3図の実施例において針電極4の先端と
対向接地電極8の間隙(Gap:放電距離)は放電入力が
大きくとれ、電圧がそれほど高くならない2cmとした条
件下で、当量比φ=1,燃焼ガス量GG=2.06g/sに約1
00ppmのNOを添加し、入口温度150℃、出口温度70℃とな
るようにして脱硫・脱硝装置12内を流した場合の放電入
力に対する出口でのNOx,NO濃度との関係を第5図に示
す。
In the embodiment of FIGS. 2 and 3, the gap (Gap: discharge distance) between the tip of the needle electrode 4 and the opposing ground electrode 8 is 2 cm at which the discharge input is large and the voltage does not become so high. Ratio φ = 1, combustion gas amount GG = 2.06g / s approx. 1
Fig. 5 shows the relationship between the discharge input and the NO x and NO concentrations at the outlet when discharge is carried out in the desulfurization / denitrification device 12 by adding 00 ppm of NO so that the inlet temperature is 150 ° C and the outlet temperature is 70 ° C. Shown in.

同図からも明らかなように、この発明に係る脱硫・脱硝
装置を使用した場合にはコロナ放電入力量が増大するに
したがって脱硝性能の著しい向上が認められた。
As is clear from the figure, when the desulfurization / denitration device according to the present invention is used, the denitration performance is remarkably improved as the corona discharge input amount increases.

また、第6図は第5図と同じ条件下で従来の棒状電極を
放電距離3cm,2cm,1cmに設定し、またこの発明に使
用する針状電極を放電距離3cm,2cm,1cmに設定した
場合の放電電圧と放電電流の関係を示すものである。
Further, in FIG. 6, the conventional rod-shaped electrodes were set to discharge distances of 3 cm, 2 cm and 1 cm under the same conditions as in FIG. 5, and the needle electrodes used in the present invention were set to discharge distances of 3 cm, 2 cm and 1 cm. It shows the relationship between the discharge voltage and the discharge current in the case.

同図からも明らかなように、この発明に係る針状電極で
はコロナ電力投入の際、同一電圧で棒状電極より多い電
流、即ち電力が得られる。このため、脱硫・脱硝にとっ
て有益なコロナ放電入力が高く取れる。このように棒状
電極より放電電力が高く取れるのは、針状電極により電
界が局所的に集中し、棒状の場合より電流が増大するた
めであると推定される。
As is clear from the figure, when the corona power is applied to the needle-shaped electrode according to the present invention, a larger current, that is, power, can be obtained at the same voltage than the rod-shaped electrode. Therefore, a high corona discharge input, which is useful for desulfurization and denitration, can be obtained. It is estimated that the reason why the discharge power can be higher than that of the rod-shaped electrode is that the electric field is locally concentrated by the needle-shaped electrode and the current increases as compared with the rod-shaped electrode.

更に、第7図は針状電極を+極性にした場合の電圧電流
波形に示すものであるが、これからも直流成分に加え、
パルス状放電も多く、放電入力が増大していることが明
らかである。
Furthermore, FIG. 7 shows the voltage-current waveform when the needle electrode is of positive polarity, and from now on, in addition to the DC component,
There are many pulsed discharges, and it is clear that the discharge input is increasing.

(発明の効果) 以上要するに、この発明によればアーク放電に転移する
前のコロナ放電入力の増大を計ることができ、したがっ
て脱硫・脱硝性能を向上させることができる。
(Effects of the Invention) In summary, according to the present invention, it is possible to increase the input of corona discharge before the transition to arc discharge, and thus improve the desulfurization / denitration performance.

また、この発明によれば排気ダクトを兼ねた外周接地電
極の寸法形状との兼ね合いで針状電極形状を自由に選べ
ることができる。
Further, according to the present invention, the needle electrode shape can be freely selected in consideration of the size and shape of the outer peripheral ground electrode which also serves as the exhaust duct.

更に、この発明の実施に当たり設備の追加などを必要と
しないなどの利点がある。
Further, there is an advantage that no additional equipment is required for implementing the present invention.

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

第1図は、この発明で使用する針状電極の斜視図、第2
図は、この発明に係る脱硫・脱硝装置の一例を示す概略
構成図、第3図は、この発明に係る脱硫・脱硝装置の他
の一例を示す概略構成図、第4図は、この発明に係る装
置を用いた脱硫・脱硝方法の一例を示す図、第5図は当
量比φ=1,燃焼ガス量G=2.06g/sの燃焼排ガスに約1
00ppmのNOを添加し、入口温度150℃、出口温度70℃とな
るようにして脱硫・脱硝装置12内を流した場合の放電入
力に対する出口でのNOx,NO濃度との関係を示す図、第6
図はは第5図と同じ条件下で従来の棒状電極を放電距離
3cm[曲線:a],2cm[曲線:b],1cm[曲線:
c],に設定し、またこの発明に使用する針状電極を放
電距離3cm[曲線:d],,2cmm[曲線:e],1cm
[曲線:f],に設定した場合の放電電圧と放電電流の
関係を示す図、第7図は針状電極を+極性にした場合の
電圧電流波形を示す図である。 図中、1は針状電極、3は構造電極、4は針電極、7は
高圧電源、8はダクト兼用対向接地電極。
FIG. 1 is a perspective view of a needle-shaped electrode used in the present invention, and FIG.
FIG. 3 is a schematic configuration diagram showing an example of a desulfurization / denitration device according to the present invention, FIG. 3 is a schematic configuration diagram showing another example of a desulfurization / denitration device according to the present invention, and FIG. A diagram showing an example of a desulfurization / denitration method using such a device, FIG.
A figure showing the relationship between the NO x and NO concentrations at the outlet with respect to the discharge input when 00 ppm NO is added and the temperature in the inlet is 150 ° C. and the outlet temperature is 70 ° C. when flowing through the desulfurization / denitration device 12. Sixth
The figure shows the discharge distance of 3 cm [curve: a], 2 cm [curve: b], 1 cm [curve:
c], and the needle electrode used in the present invention has a discharge distance of 3 cm [curve: d], 2 cmm [curve: e], 1 cm.
FIG. 7 is a diagram showing the relationship between discharge voltage and discharge current when [curve: f] is set, and FIG. 7 is a diagram showing voltage-current waveforms when the needle electrode has a positive polarity. In the figure, 1 is a needle electrode, 3 is a structural electrode, 4 is a needle electrode, 7 is a high-voltage power supply, and 8 is a counter ground electrode that also serves as a duct.

フロントページの続き (56)参考文献 特開 昭61−15750(JP,A) 特開 昭51−56773(JP,A) 特開 昭51−56774(JP,A) 特開 昭61−71825(JP,A)Continuation of the front page (56) Reference JP-A-61-15750 (JP, A) JP-A-51-56773 (JP, A) JP-A-51-56774 (JP, A) JP-A-61-71825 (JP , A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】脱硫・脱硝しようとする排ガスの、導入ダ
クトを兼ねた外周接地電極と、構造電極の側面から複数
の針電極を所定の間隔を置いて二方向乃至四方向に延設
して構成された針状電極からなり、該針状電極は上記針
電極の先端を上記外周接地電極の内周面方向に向け、且
つ該先端と外周接地電極の内周面との間に所定間隔が保
たれるようにして外周接地電極内に設置されることを特
徴とするコロナ放電を用いた脱硫・脱硝装置。
1. An outer peripheral ground electrode also serving as an introduction duct for exhaust gas to be desulfurized and denitrated, and a plurality of needle electrodes extending from two sides to four directions at predetermined intervals from the side surface of the structural electrode. The needle-shaped electrode is configured such that the tip of the needle electrode is directed toward the inner peripheral surface of the outer peripheral ground electrode, and a predetermined distance is provided between the tip and the inner peripheral surface of the outer peripheral ground electrode. A desulfurization / denitration device using corona discharge, which is installed in the outer circumference ground electrode so as to be maintained.
JP2314660A 1990-11-20 1990-11-20 Desulfurization and denitration equipment using corona discharge Expired - Lifetime JPH0647065B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2314660A JPH0647065B2 (en) 1990-11-20 1990-11-20 Desulfurization and denitration equipment using corona discharge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2314660A JPH0647065B2 (en) 1990-11-20 1990-11-20 Desulfurization and denitration equipment using corona discharge

Publications (2)

Publication Number Publication Date
JPH04187214A JPH04187214A (en) 1992-07-03
JPH0647065B2 true JPH0647065B2 (en) 1994-06-22

Family

ID=18056006

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JP2314660A Expired - Lifetime JPH0647065B2 (en) 1990-11-20 1990-11-20 Desulfurization and denitration equipment using corona discharge

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Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5156773A (en) * 1974-11-14 1976-05-18 Fujikura Ltd HAIKIGASU JOKASOCHI
JPS5156774A (en) * 1974-11-14 1976-05-18 Fujikura Ltd HAIKIGASU JOKASOCHI
JPS6115750A (en) * 1984-06-30 1986-01-23 Corona Giken Kogyo Kk Apparatus for purifying exhaust gas
JPS6171825A (en) * 1984-09-13 1986-04-12 Matsushita Electric Ind Co Ltd Degassing cylinder

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JPH04187214A (en) 1992-07-03

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