JPH02211218A - Denitration of nox in waste gas and waste gas treatment apparatus - Google Patents

Denitration of nox in waste gas and waste gas treatment apparatus

Info

Publication number
JPH02211218A
JPH02211218A JP1030236A JP3023689A JPH02211218A JP H02211218 A JPH02211218 A JP H02211218A JP 1030236 A JP1030236 A JP 1030236A JP 3023689 A JP3023689 A JP 3023689A JP H02211218 A JPH02211218 A JP H02211218A
Authority
JP
Japan
Prior art keywords
nox
plasma
spraying
gas
waste gas
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
JP1030236A
Other languages
Japanese (ja)
Other versions
JP2692237B2 (en
Inventor
Fukuji Shoji
東海林 福治
Yuji Ishizaka
石坂 雄二
Hoki Haba
方紀 羽場
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing Co 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 Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP1030236A priority Critical patent/JP2692237B2/en
Publication of JPH02211218A publication Critical patent/JPH02211218A/en
Application granted granted Critical
Publication of JP2692237B2 publication Critical patent/JP2692237B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To perform safe treatment by spraying an aqueous solution having sodium azide dissolved therein from a spray device and charging electric energy in this spray to form plasma. CONSTITUTION:An aqueous azide solution is sent into a spray device 2 by a pump while NOx-containing waste gas is introduced into said spray device for the sake of spray. The flow rate of the aqueous azide solution and that of the NOx-containing waste gas are controlled so as to obtain such a state that the aqueous azide solution is sprayed uniformly and the high frequency power of plasma generating coils 3, 4 is charged to apply electric energy to the wet gas sprayed in a reaction chamber 5 to generate plasma. By this method, a byproduct can be inexpensively removed and the waste gas can be treated efficiently.

Description

【発明の詳細な説明】 A、産業上の利用分野 本発明は、排ガス中のNOxを処理して無害なガスとし
て排ガス中のNOxの脱硝方法及び排ガス処理装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to a denitrification method and an exhaust gas treatment apparatus for treating NOx in exhaust gas to convert it into a harmless gas.

B0発明の概要 本発明の排ガス中のNOxの脱硝方法は、NOx含有排
ガスを噴霧用ガスとしてナトリウムアザイドを溶解した
水溶液を噴霧装置から噴霧し、この噴霧中に電気エネル
ギーを投入してプラズマを生成させ、噴霧中に含まれる
物質を活性化し、NOxをアザイドにより還元してN!
とH,0に変え、NOx含有排ガスを無害なガスにする
ものである。
B0 Summary of the Invention The method of denitrating NOx in exhaust gas of the present invention involves spraying an aqueous solution in which sodium azide is dissolved using NOx-containing exhaust gas as a spraying gas, and injecting electrical energy into the spraying to generate plasma. It generates NOx, activates the substances contained in the spray, and reduces NOx with azide to N!
and H,0 to turn the NOx-containing exhaust gas into a harmless gas.

また、本発明の排ガス処理装置は、プラズマ発生用コイ
ルが施されたプラズマ反応筒と、このプラズマ反応筒内
にNOx含有ガスを噴霧用ガスとしてアザイド水溶液を
噴霧する噴霧装置と、前記プラズマ反応筒内に発生する
熱を回収する熱交換装置とを備えて゛なるものである。
Further, the exhaust gas treatment apparatus of the present invention includes a plasma reaction tube provided with a plasma generation coil, a spraying device for spraying an azide aqueous solution using NOx-containing gas as a spraying gas, and a spraying device for spraying an azide aqueous solution into the plasma reaction tube using a NOx-containing gas as a spraying gas. It is equipped with a heat exchange device that recovers the heat generated within the tank.

C1従来の技術 化石燃料の燃焼により生成する排煙又は排ガス中のSO
x、NOx、Go等は大気汚染を促進する有害物質であ
り、NOxの除去は、従来アンモニア還元接触法が主流
となっている。
C1 Conventional technology SO in exhaust smoke or exhaust gas generated by combustion of fossil fuels
BACKGROUND ART x, NOx, Go, etc. are harmful substances that promote air pollution, and the ammonia reduction contact method has conventionally been the mainstream method for removing NOx.

また、省エネルギー装置として注目を集めている熱電併
給設備は、都市部のビル等に非常電源を兼用して設置さ
れている。
Additionally, combined heat and power generation equipment, which is attracting attention as an energy-saving device, is installed in buildings in urban areas and serves as an emergency power source.

D0発明が解決しようとする課題 しかし、アンモニア還元接触法によるNOx除去装置は
、大型で高価であるばかりでなく、使用するアンモニア
ガスは照限度25 p pm、爆発範囲15.5〜27
%で、腐食性、刺激臭が強く、危険で毒性の強いガスで
あり、多量に使用する場合、漏れ等及び操作する人がガ
スハンドリングの技術を身に付けた人が望ましい等制約
が多く、とても都市、住宅地近傍に設置することは困難
である。
D0 Problems to be Solved by the Invention However, the NOx removal equipment using the ammonia reduction contact method is not only large and expensive, but also the ammonia gas used has an illumination limit of 25 ppm and an explosive range of 15.5 to 27.
%, it is a dangerous and highly toxic gas with a strong corrosive and pungent odor, and when used in large quantities, there are many restrictions such as leakage and it is desirable for the operator to have gas handling skills. It is very difficult to install in urban areas or near residential areas.

また、熱電併給設備はかなりのNOxが発生するが、N
Oxの処理は上述のように困難であるので、熱電併給設
備のNOx処理の適当な処理方法がなかった。
Additionally, combined heat and power generation equipment generates a considerable amount of NOx;
Since treatment of Ox is difficult as described above, there has been no suitable treatment method for treatment of NOx in combined heat and power generation equipment.

本発明は、従来技術の有するこのような問題点に鑑みて
なされたものであり、その目的とするところは、アンモ
ニアのような危険なガスを使うことなく安全でクリーン
な状態でNOxを処理できる排ガス中のNOxの脱硝方
法と、熱電併給装置と組合せた排ガス処理装置を提供す
ることにある。
The present invention was made in view of the problems of the prior art, and its purpose is to treat NOx in a safe and clean manner without using dangerous gases such as ammonia. It is an object of the present invention to provide a method for denitrifying NOx in exhaust gas and an exhaust gas treatment device combined with a combined heat and power supply device.

81課題を解決するための手段 上記目的を達成するために、本発明における排ガス中の
NOxの脱硝方法は、NOx含有排ガスを噴霧用ガスと
してナトリウムアザイドを溶解した水溶液を噴霧装置か
ら噴霧し、この噴霧中に電気エネルギーを投入してプラ
ズマを生成させ、噴霧中に含まれる物質を活性化し、N
Oxをアザイドにより還元してN、とH,0に変えるも
のである。
81 Means for Solving the Problems In order to achieve the above object, the method for denitrifying NOx in exhaust gas in the present invention includes spraying an aqueous solution in which sodium azide is dissolved using NOx-containing exhaust gas as a spraying gas from a spraying device, Electrical energy is input into this spray to generate plasma, activate the substances contained in the spray, and N
Ox is reduced by azide and converted into N, H, and 0.

また、本発明における排ガス処理装置は、プラズマ発生
用コイルが施されたプラズマ反応筒と、このプラズマ反
応筒内にNOx含有ガスを噴霧用ガスとしてアザイド水
溶液を噴霧する噴霧装置と、前記プラズマ反応筒内に発
生する熱を回収する熱交換装置とを備えてなるものであ
る。
Further, the exhaust gas treatment apparatus of the present invention includes a plasma reaction tube provided with a plasma generation coil, a spraying device for spraying an azide aqueous solution using NOx-containing gas as a spraying gas, and a spraying device for spraying an azide aqueous solution into the plasma reaction tube using a NOx-containing gas as a spraying gas. It is equipped with a heat exchange device that recovers the heat generated inside.

F9作用 NOx含有排ガスを噴霧用ガスとしてナトリウムアザイ
ドを溶解した水溶を噴霧してた噴霧中に、高周波等の電
気エネルギーを投入すると、プラズマが生成する。
F9 action Plasma is generated when electric energy such as high frequency is input into the atomization process in which an aqueous solution of sodium azide is atomized using NOx-containing exhaust gas as the atomization gas.

プラズマは噴霧中に含まれる物質を活性化する。The plasma activates the substances contained in the spray.

これによりNOxをアザイド還元してN、とH,0に変
えることができる。
This allows NOx to be reduced to azide and converted to N, H, and 0.

排ガス処理装置は、上記反応をプラズマ発生用コイルが
施されたプラズマ反応筒内で行い、プラズマ反応簡に熱
交換器を設けて、プラズマ反応で発生する熱を回収する
The exhaust gas treatment device performs the above reaction in a plasma reaction cylinder equipped with a plasma generation coil, and is equipped with a heat exchanger to recover the heat generated by the plasma reaction.

G、実施例 実施例1 先ず、排ガス中のNOxの脱硝方法の原理を説明する。G. Example Example 1 First, the principle of the NOx removal method in exhaust gas will be explained.

本方法は、NOxをpJ 1 + Ht Oに化学的に
変えるもので、主反応式として次の3つの式を使用する
This method chemically changes NOx to pJ 1 + Ht 2 O, and uses the following three equations as main reaction equations.

N O+ N O、+ Hto→2HNO*   ・・
・・・・(1)6 NaN5+ 6 Hc&−”6 N
sH+ 6 Nac12− (2)2HNO,+ 6N
sH→1ONt+4HtO・・・(3)通常ガスを液体
に吸収させるのは非常に効率が悪い。上記(1)式は、
No、 Notを水に吸収させてHNOtにする反応で
ある。この段階の反応が効率よく行うことができれば、
上記(3)式の反応はスムーズに進行する。上記(2)
の反応は予め行って置く。
N O+ N O, + Hto→2HNO* ・・
...(1) 6 NaN5+ 6 Hc&-"6 N
sH+ 6 Nac12- (2)2HNO, + 6N
sH→1ONt+4HtO...(3) Normally, it is very inefficient to absorb gas into liquid. The above formula (1) is
This is a reaction in which No and Not are absorbed into water to form HNOt. If this step of the reaction can be carried out efficiently,
The reaction of formula (3) above proceeds smoothly. Above (2)
Perform the reaction in advance.

上記(1)式の反応、特にその気体を液体に効率よく吸
収し、かつよく反応させる方法として、2流体噴霧装置
によりNOxを含む排ガスでナトリウムアザイドを溶解
した水溶液((2)式)をスプレーして、ウェットガス
(Wet gas)化する。
For the reaction of formula (1) above, especially as a method for efficiently absorbing the gas into a liquid and making it react well, an aqueous solution (formula (2)) in which sodium azide is dissolved in exhaust gas containing NOx is prepared using a two-fluid spray device. Spray to turn it into wet gas.

同時にこのウェットガスに対して外部から放電し易く、
かつ放電が持続する周波数の電力を投入し、ウェットガ
スをプラズマ化して、上記(1)式と(3)式の反応を
促進させNOxをN、とH,0にプラズマ化学的に変化
させることで、NOxを除去するものである。
At the same time, this wet gas is easily discharged from the outside,
In addition, power at a frequency that sustains the discharge is applied to turn the wet gas into plasma, promoting the reactions of equations (1) and (3) above, and plasma-chemically changing NOx into N, H, and 0. This removes NOx.

実施例を図面を参照して説明する。Examples will be described with reference to the drawings.

第1図において、lはプラズマ反応筒、2はプラズマ反
応筒内に噴霧する噴霧装置、3,4はプラズマ反応筒外
側に巻かれたプラズマ発生用コイル、5は反応室である
。予め上記(2)式に基づいて作製したアザイド水溶液
をポンプ等で噴霧装置2に送り込む一方、噴霧のためN
Ox含有排ガスを導入し、アザイド水溶液を均一に噴霧
した状態となるようにアザイド水溶液及びNOx含有排
ガス流量を調整し、プラズマ発生用コイル3,4に高周
波電力を投入し反応室5内に噴霧されたウェットガスに
電気エネルギーを与えてプラズマを生成させる。この場
合、高周波電力の周波数を13.56MHzを使用した
が、商用周波の電気エネルギーでもプラズマは生成する
ので、電力の周波数を高周波に限るものではない。
In FIG. 1, 1 is a plasma reaction tube, 2 is a spray device for spraying into the plasma reaction tube, 3 and 4 are plasma generation coils wound around the outside of the plasma reaction tube, and 5 is a reaction chamber. An azide aqueous solution prepared in advance based on the above formula (2) is sent to the spraying device 2 using a pump, etc., while N is used for spraying.
Ox-containing exhaust gas is introduced, the flow rates of the azide aqueous solution and NOx-containing exhaust gas are adjusted so that the azide aqueous solution is uniformly sprayed, and high-frequency power is applied to the plasma generation coils 3 and 4, so that the azide aqueous solution is sprayed into the reaction chamber 5. Electrical energy is applied to wet gas to generate plasma. In this case, the frequency of the high frequency power was 13.56 MHz, but since plasma can be generated even with commercial frequency electrical energy, the frequency of the power is not limited to high frequencies.

このようにして反応室5内で生成したプラズマは、噴霧
によりウェット化したNOx含有排ガスを励起し、瞬時
のうちに、上記(1)、(3)式の反応が促進させる。
The plasma generated in the reaction chamber 5 in this manner excites the NOx-containing exhaust gas that has been wetted by spraying, and instantly promotes the reactions of equations (1) and (3) above.

上記実施例によれば、NOxを11000pp含有した
排ガスを用いたところ、1100pp以下にNOxを低
減することができた。
According to the above example, when exhaust gas containing 11,000 pp of NOx was used, NOx could be reduced to 1,100 pp or less.

実施例2 第2図において、1はプラズマ反応筒、2は噴霧装置、
6はプラズマ発生用電源、7はプラズマ発生用コイル、
8はアザイド溶液タンク、9はアザイド溶液送給ポンプ
、lOは管をコイル状に巻回した熱回収用配管、11は
プラズマ発生用電源6への人力電線、12はプラズマ発
生用電源6を冷却する冷却水管、13はNOx含有ガス
取入口、14は処理した排ガスの出口である。
Example 2 In FIG. 2, 1 is a plasma reactor, 2 is a spray device,
6 is a power supply for plasma generation, 7 is a coil for plasma generation,
8 is an azide solution tank, 9 is an azide solution supply pump, IO is a heat recovery pipe made of a coiled tube, 11 is a human-powered electric wire to the plasma generation power source 6, and 12 is a cooling power source for the plasma generation power source 6. 13 is a NOx-containing gas intake port, and 14 is an outlet for treated exhaust gas.

しかして、取入口!3よりのエンジン等からの排ガス及
びポンプ9で送られるタンク8内のアザイド溶液は噴霧
装置2によりプラズマ反応筒内にウェットガスとして噴
霧される。プラズマ発生用コイル7には電源6より高周
波電力が供給されているので、プラズマ反応筒1内にプ
ラズマが生成され、瞬時のうちに上記(1)、(3)式
の反応が促進されてN、Oxは分解される。
However, the intake! The exhaust gas from the engine 3 and the azide solution in the tank 8 sent by the pump 9 are sprayed as wet gas into the plasma reaction cylinder by the spraying device 2. Since high-frequency power is supplied to the plasma generation coil 7 from the power supply 6, plasma is generated in the plasma reaction tube 1, and the reactions of equations (1) and (3) above are instantly promoted, resulting in N , Ox is decomposed.

プラズマ反応筒1内に発生する熱は熱回収用配管10内
に流れる水を熱湯又は蒸気として外部に取り出し利用す
る。またプラズマ発生コイル内に冷却用水を流すことに
よりプラズマ発生コイルの熱を取り出すことができる。
The heat generated in the plasma reaction tube 1 is utilized by extracting the water flowing in the heat recovery piping 10 to the outside as hot water or steam. Moreover, the heat of the plasma generation coil can be taken out by flowing cooling water into the plasma generation coil.

処理された排ガスはプラズマ反応筒lの出口14より排
出される。実施例はプラズマ発生用コイルを反応筒1の
外部に巻回しているが、内部に設けてもよい。
The treated exhaust gas is discharged from the outlet 14 of the plasma reactor l. In the embodiment, the plasma generation coil is wound around the outside of the reaction tube 1, but it may be provided inside.

実施例3 第3図において、プラズマ反応筒lの胴部15は二重に
構成され、その間を熱回収用通路16とする熱交換器が
構成されており、その他の構成は第2図のものと同様に
なっており、同一部分には同一符号を付しである。
Embodiment 3 In FIG. 3, the body 15 of the plasma reaction cylinder 1 is constructed in double layers, and a heat exchanger is constructed between which a heat recovery passage 16 is formed, and the other structure is the same as that in FIG. 2. The same parts are given the same reference numerals.

しかして、この実施例によれば、実施例2の配管!0を
熱交換器としたものに比し、プラズマ反応筒を小さく構
成することができる。
According to this example, the piping of Example 2! The plasma reactor can be configured smaller than that in which the heat exchanger is used as a heat exchanger.

H,発明の効果 本発明は、上述のとおり構成されているので、次に記載
する効果を奏する。
H. Effects of the Invention Since the present invention is configured as described above, it produces the following effects.

■アンモニアのような危険なガスを使うことなく安全で
クリーンな状態でNOxを処理できる。
■NOx can be treated safely and cleanly without using dangerous gases such as ammonia.

■処理により副生成物を伴うことなく、N、とHt O
に分解するため、副生酸物除去手段等が不用となり、安
価にできる。
■N, and HtO without producing by-products during processing.
Since it decomposes into , there is no need for a means for removing by-product oxides, and the cost can be reduced.

■プラズマ発生用電源と水及び小量の薬品があればよく
、また、臭気、爆発等の恐れがないので、都市部等に設
置するに都合がよい。
- All you need is a power source for plasma generation, water, and a small amount of chemicals, and there is no risk of odor or explosion, so it is convenient for installation in urban areas.

■アザイド水溶液でウェット化したNOx含有ガスをプ
ラズマにより活性化して化学反応を促進させているので
、効率が良い。
■Efficiency is high because the NOx-containing gas wetted with azide aqueous solution is activated by plasma to promote chemical reactions.

■排ガス処理装置は、エンジン等のN”Oxを処理し、
無害なガスとして空中に放出できる。
■Exhaust gas treatment equipment processes N”Ox from engines, etc.
It can be released into the air as a harmless gas.

■排ガス処理装置に要した熱(残存熱)を熱交換にて回
収できるので、効率が上昇する。
■The heat required by the exhaust gas treatment equipment (residual heat) can be recovered through heat exchange, increasing efficiency.

■熱交換器はプラズマ発生と一体に構成されているので
、設置に大きなスペースを要しない。
■Since the heat exchanger is integrated with the plasma generator, it does not require a large space for installation.

■装置全体が安価にできる。■The entire device can be made at low cost.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の方法の動作説明図、第2図は本発明
装置の一例を示す概略構成図、第3図は他の例を示す概
略構成図である。 l・・・プラズマ反応筒、2・・・噴霧装置、3.4゜
7・・・プラズマ発生用コイル、5・・・反応室、9・
・・ポンプ、lO・・・熱回収用配管、16・・・熱回
収用通路。 外2名 第1 図 アザイドS液 第3図 合
FIG. 1 is an explanatory diagram of the operation of the method of the present invention, FIG. 2 is a schematic diagram showing an example of the apparatus of the present invention, and FIG. 3 is a schematic diagram showing another example. 1... Plasma reaction tube, 2... Spraying device, 3.4° 7... Plasma generation coil, 5... Reaction chamber, 9...
... Pump, lO... Piping for heat recovery, 16... Passage for heat recovery. Two other people Figure 1 Azide S liquid Figure 3

Claims (2)

【特許請求の範囲】[Claims] (1)NOx含有排ガスを噴霧用ガスとしてナトリウム
アザイドを溶解した水溶液を噴霧装置から噴霧し、この
噴霧中に電気エネルギーを投入してプラズマを生成させ
、噴霧中に含まれる物質を活性化し、NOxをアザイド
により還元してN_2とH_2Oに変えることを特徴と
する排ガス中のNOxの脱硝方法。
(1) Spraying an aqueous solution in which sodium azide is dissolved using NOx-containing exhaust gas as a spraying gas from a spraying device, inputting electrical energy into this spraying to generate plasma, and activating substances contained in the spraying, A method for denitrifying NOx in exhaust gas, characterized by reducing NOx with azide and converting it into N_2 and H_2O.
(2)プラズマ発生用コイルが施されたプラズマ反応筒
と、このプラズマ反応筒内にNOx含有ガスを噴霧用ガ
スとしてアザイド水溶液を噴霧する噴霧装置と、前記プ
ラズマ反応筒内に発生する熱を回収する熱交換装置とを
備えてなることを特徴とする排ガス処理装置。
(2) A plasma reaction tube equipped with a plasma generation coil, a spraying device that sprays an azide aqueous solution into the plasma reaction tube using NOx-containing gas as the atomizing gas, and recovery of the heat generated in the plasma reaction tube. An exhaust gas treatment device characterized by comprising a heat exchange device.
JP1030236A 1989-02-09 1989-02-09 NOx denitration method in exhaust gas and exhaust gas treatment device Expired - Lifetime JP2692237B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1030236A JP2692237B2 (en) 1989-02-09 1989-02-09 NOx denitration method in exhaust gas and exhaust gas treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1030236A JP2692237B2 (en) 1989-02-09 1989-02-09 NOx denitration method in exhaust gas and exhaust gas treatment device

Publications (2)

Publication Number Publication Date
JPH02211218A true JPH02211218A (en) 1990-08-22
JP2692237B2 JP2692237B2 (en) 1997-12-17

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US6451252B1 (en) 2000-01-20 2002-09-17 Regents Of The University Of Minnesota Odor removal system and method having ozone and non-thermal plasma treatment
US6562386B2 (en) 2001-05-07 2003-05-13 Regents Of The University Of Minnesota Method and apparatus for non-thermal pasteurization
US6911225B2 (en) 2001-05-07 2005-06-28 Regents Of The University Of Minnesota Method and apparatus for non-thermal pasteurization of living-mammal-instillable liquids
US7011790B2 (en) 2001-05-07 2006-03-14 Regents Of The University Of Minnesota Non-thermal disinfection of biological fluids using non-thermal plasma
US7931811B2 (en) 2006-10-27 2011-04-26 Regents Of The University Of Minnesota Dielectric barrier reactor having concentrated electric field
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1088390C (en) * 1997-03-08 2002-07-31 韩国重工业株式会社 Process for desulfurization and denitrification by use of low-temperature plasma reactor equipped with condenser
US6146599A (en) * 1999-02-24 2000-11-14 Seagate Technology Llc Dielectric barrier discharge system and method for decomposing hazardous compounds in fluids
US6451252B1 (en) 2000-01-20 2002-09-17 Regents Of The University Of Minnesota Odor removal system and method having ozone and non-thermal plasma treatment
US6562386B2 (en) 2001-05-07 2003-05-13 Regents Of The University Of Minnesota Method and apparatus for non-thermal pasteurization
US6911225B2 (en) 2001-05-07 2005-06-28 Regents Of The University Of Minnesota Method and apparatus for non-thermal pasteurization of living-mammal-instillable liquids
US7011790B2 (en) 2001-05-07 2006-03-14 Regents Of The University Of Minnesota Non-thermal disinfection of biological fluids using non-thermal plasma
US7931811B2 (en) 2006-10-27 2011-04-26 Regents Of The University Of Minnesota Dielectric barrier reactor having concentrated electric field
CN106731545A (en) * 2017-01-13 2017-05-31 重庆大学 A kind of cooker hood and system based on lower temperature plasma technology

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